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diff --git a/docs/correct_HTML_1520_newHPModels/naming_violations.txt b/docs/correct_HTML_1520_newHPModels/naming_violations.txt
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+AixLib/Controls/HeatPump/BaseClasses/PartialTSetToNSet.mo
+1: Name 'T_heaLim' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_hea. Affected line: parameter Modelica.Units.SI.Temperature T_heaLim=293.15 "Heating limit temperature. If the filtered outdoor air temperature surpasses this threshold, the device will be shut down" annotation(Dialog(group= "Heating limit temperature", enable=use_heaLim));
+
+2: Name 'swiNullHP' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Null. Affected line: Modelica.Blocks.Logical.Switch swiNullHP "If HP is off, zero is passed" annotation (Placement(transformation(extent={{60,-20},{80,0}})));
+
+3: Missing documentation. Affected line: AixLib.Fluid.HeatPumps.ModularReversible.BaseClasses.RefrigerantMachineControlBus sigBusHP annotation (Placement(transformation(extent={{-124,-46},{-90,-16}})));
+
+4: Name 'swiNullsecHeaGen' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Nullsec. Affected line: AixLib.Utilities.Logical.SmoothSwitch swiNullsecHeaGen if use_secHeaGen "If second heater is off, zero is passed" annotation (Placement( transformation( extent={{10,-10},{-10,10}}, rotation=90, origin={0,-70})));
+
+5: Missing documentation, Name 'lessThreshold' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: less, Threshold. Affected line: Modelica.Blocks.Logical.LessThreshold lessThreshold(final threshold= T_heaLim) if use_heaLim annotation (Placement(transformation(extent={{-60,-40},{-40,-20}})));
+
+6: Missing documentation, Name 'booleanConstant' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: boolean, Constant. Affected line: Modelica.Blocks.Sources.BooleanConstant booleanConstant(final k=true) if not use_heaLim annotation (Placement(transformation(extent={{-60,-80},{-40,-60}})));
+
+
+AixLib/Fluid/Examples/GeothermalHeatPump/BaseClasses/GeothermalHeatPumpBase.mo
+1: Name 'm_flow_nominal_layer' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: m_flow_nominal_layer. Affected line: parameter Modelica.Units.SI.MassFlowRate m_flow_nominal_layer=0.5 "Nominal mass flow rate in layers of storages";
+
+2: Name 'm_flow_nominal_HE' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: m_flow_nominal_. Affected line: parameter Modelica.Units.SI.MassFlowRate m_flow_nominal_HE=0.5 "Nominal mass flow rate of heat exchanger layers of storages";
+
+3: Name 'T_start_cold' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_start_cold. Affected line: parameter Modelica.Units.SI.Temperature T_start_cold=300 "Initial temperature of cold components";
+
+4: Name 'T_start_hot' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_start_hot. Affected line: parameter Modelica.Units.SI.Temperature T_start_hot=300 "Initial temperature of warm components";
+
+5: Missing documentation, Name 'PeakLoadDeviceModel' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Peak, Load, Device, Model. Affected line: replaceable model PeakLoadDeviceModel = AixLib.Fluid.Interfaces.PartialTwoPortTransport constrainedby AixLib.Fluid.Interfaces.PartialTwoPortTransport(redeclare package Medium=Medium) annotation(choicesAllMatching=true);
+
+6: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: PeakLoadDeviceModel peaLoaDev annotation (Placement(transformation(extent={{108,-56},{120,-44}})));Storage.StorageDetailed coldStorage( redeclare package Medium = Medium, energyDynamics=energyDynamics, redeclare package MediumHC1 = Medium, redeclare package MediumHC2 = Medium, m1_flow_nominal=m_flow_nominal_layer, m2_flow_nominal=m_flow_nominal_layer, mHC1_flow_nominal=m_flow_nominal_HE, useHeatingCoil2=false, useHeatingRod=false, redeclare DataBase.Storage.Generic_New_2000l data( hTank=1.5, hUpperPortDemand=1.45, hUpperPortSupply=1.45, hHC1Up=1.45, dTank=1, sIns=0.2, lambdaIns=0.075, hTS2=1.45), n=5, hConIn=100, hConOut=10, hConHC1=500, upToDownHC1=false) "Storage tank for buffering cold demand" annotation (Placement(transformation(extent={{24,-14}, {52,20}})));FixedResistances.PressureDrop resistanceColdStorage( redeclare package Medium = Medium, m_flow_nominal=0.5, dp_nominal=15000) "Resistance in evaporator circuit" annotation (Placement(transformation( extent={{-6,-7},{6,7}}, rotation=180, origin={-34,38})));
+
+7: Name 'geothFieldSource' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: geoth, Field, Source. Affected line: AixLib.Fluid.Sources.Boundary_pT geothFieldSource( redeclare package Medium = Medium, nPorts=1, T=284.15) "Source representing geothermal field" annotation (Placement(transformation(extent={{-158,-60},{-146,-48}})));
+
+8: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: FixedResistances.PressureDrop resistanceGeothermalSource( redeclare package Medium = Medium, m_flow_nominal=0.5, dp_nominal=15000) "Resistance in geothermal field circuit" annotation (Placement(transformation( extent={{-6,-7},{6,7}}, rotation=0, origin={-70,-54})));FixedResistances.PressureDrop resistanceColdConsumerFlow( redeclare package Medium = Medium, m_flow_nominal=0.2, dp_nominal=10000) "Resistance in cold consumer flow line" annotation (Placement(transformation( extent={{-7,-7},{7,7}}, rotation=0, origin={87,-20})));Actuators.Valves.TwoWayQuickOpening valveHeatSink( redeclare package Medium = Medium, m_flow_nominal=0.5, dpValve_nominal=5000) "Valve connecting geothermal field to the condenser of the heat pump" annotation (Placement(transformation(extent={{-36,-61},{-24,-47}})));Actuators.Valves.TwoWayQuickOpening valveHeatSource(redeclare package Medium = Medium, m_flow_nominal=0.5, dpValve_nominal=5000) "Valve connecting geothermal field to the evaporator of the heat pump" annotation (Placement( transformation( extent={{-6,-7},{6,7}}, rotation=90, origin={-60,1})));
+
+9: Name 'heatStorage' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heat, Storage. Affected line: AixLib.Fluid.Storage.StorageDetailed heatStorage( redeclare package Medium = Medium, energyDynamics=energyDynamics, redeclare package MediumHC1 = Medium, redeclare package MediumHC2 = Medium, m1_flow_nominal=m_flow_nominal_layer, m2_flow_nominal=m_flow_nominal_layer, mHC1_flow_nominal=m_flow_nominal_HE, useHeatingCoil2=false, useHeatingRod=false, redeclare DataBase.Storage.Generic_New_2000l data( hTank=1.5, hUpperPortDemand=1.45, hUpperPortSupply=1.45, hHC1Up=1.45, dTank=1, sIns=0.2, lambdaIns=0.075, hTS2=1.45), n=5, hConIn=100, hConOut=10, hConHC1=500) "Storage tank for buffering heat demand" annotation (Placement(transformation(extent={{24,-96},{52,-62}})));
+
+10: Name 'resistanceHeatStorage' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: resistance, Heat, Storage. Affected line: AixLib.Fluid.FixedResistances.PressureDrop resistanceHeatStorage( redeclare package Medium = Medium, m_flow_nominal=0.5, dp_nominal=15000) "Resistance in condenser circuit" annotation (Placement(transformation( extent={{-6,-7},{6,7}}, rotation=90, origin={-18,-78})));
+
+11: Name 'geothField_sink1' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: geoth, Field_sink. Affected line: AixLib.Fluid.Sources.Boundary_pT geothField_sink1(redeclare package Medium = Medium, nPorts=2) "One of two sinks representing geothermal field" annotation (Placement(transformation(extent={{-158,20},{-146,32}})));
+
+12: Name 'resistanceHeatConsumerFlow' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: resistance, Heat, Consumer. Affected line: AixLib.Fluid.FixedResistances.PressureDrop resistanceHeatConsumerFlow( redeclare package Medium = Medium, m_flow_nominal=0.2, dp_nominal=10000) "Resistance in heat consumer flow line" annotation (Placement(transformation( extent={{-7,-7},{7,7}}, rotation=0, origin={87,-50})));
+
+13: Name 'valveColdStorage' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: valve, Cold, Storage. Affected line: AixLib.Fluid.Actuators.Valves.TwoWayQuickOpening valveColdStorage( redeclare package Medium = Medium, m_flow_nominal=0.5, dpValve_nominal=5000) "Valve connecting cold storage to the evaporator of the heat pump" annotation (Placement( transformation( extent={{-6,7},{6,-7}}, rotation=180, origin={-52,38})));
+
+14: Name 'valveHeatStorage' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: valve, Heat, Storage. Affected line: AixLib.Fluid.Actuators.Valves.TwoWayQuickOpening valveHeatStorage( redeclare package Medium = Medium, m_flow_nominal=0.5, dpValve_nominal=5000) "Valve connecting heat storage to the condenser of the heat pump" annotation (Placement( transformation( extent={{-6,-7},{6,7}}, rotation=90, origin={-18,-63})));
+
+15: Name 'pumpColdConsumer' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: pump, Cold, Consumer. Affected line: AixLib.Fluid.Movers.FlowControlled_dp pumpColdConsumer( energyDynamics=energyDynamics, m_flow_nominal=0.05, redeclare package Medium = Medium, addPowerToMedium=false, T_start=T_start_cold) "Pump moving fluid from storage tank to cold consumers" annotation (Placement(transformation(extent={{58,-27},{72,-13}})));
+
+16: Name 'pumpHeatConsumer' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: pump, Heat, Consumer. Affected line: AixLib.Fluid.Movers.FlowControlled_dp pumpHeatConsumer( energyDynamics=energyDynamics, m_flow_nominal=0.05, redeclare package Medium = Medium, addPowerToMedium=false, T_start=T_start_hot) "Pump moving fluid from storage tank to heat consumers" annotation (Placement(transformation(extent={{58,-57},{72,-43}})));
+
+17: Name 'resistanceColdConsumerReturn' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: resistance, Cold, Consumer, Return. Affected line: AixLib.Fluid.FixedResistances.PressureDrop resistanceColdConsumerReturn( redeclare package Medium = Medium, m_flow_nominal=0.2, dp_nominal=10000) "Resistance in cold consumer return line" annotation (Placement(transformation( extent={{-7,-7},{7,7}}, rotation=180, origin={87,32})));
+
+18: Name 'resistanceHeatConsumerReturn' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: resistance, Heat, Consumer, Return. Affected line: AixLib.Fluid.FixedResistances.PressureDrop resistanceHeatConsumerReturn( redeclare package Medium = Medium, m_flow_nominal=0.2, dp_nominal=10000) "Resistance in heat consumer return line" annotation (Placement(transformation( extent={{-7,-7},{7,7}}, rotation=180, origin={87,-106})));
+
+19: Name 'pumpCondenser' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: pump, Condenser. Affected line: AixLib.Fluid.Movers.FlowControlled_dp pumpCondenser( energyDynamics=energyDynamics, m_flow_nominal=0.05, redeclare package Medium = Medium, addPowerToMedium=false, T_start=T_start_cold) "Pump moving fluid from storage tank to condenser of heat pump" annotation (Placement(transformation( extent={{-7,7},{7,-7}}, rotation=180, origin={-1,-98})));
+
+20: Name 'pumpEvaporator' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: pump, Evaporator. Affected line: AixLib.Fluid.Movers.FlowControlled_dp pumpEvaporator( energyDynamics=energyDynamics, m_flow_nominal=0.05, redeclare package Medium = Medium, addPowerToMedium=false, T_start=T_start_cold) "Pump moving fluid from storage tank to evaporator of heat pump" annotation (Placement(transformation( extent={{-7,7},{7,-7}}, rotation=180, origin={7,36})));
+
+21: Name 'pumpGeothermalSource' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: pump, Geothermal, Source. Affected line: AixLib.Fluid.Movers.FlowControlled_dp pumpGeothermalSource( energyDynamics=energyDynamics, m_flow_nominal=0.05, redeclare package Medium = Medium, addPowerToMedium=false, T_start=T_start_cold) "Pump moving fluid from geothermal source into system" annotation ( Placement(transformation( extent={{-7,-7},{7,7}}, rotation=0, origin={-89,-54})));
+
+22: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: HeatPumps.ModularReversible.BaseClasses.RefrigerantMachineControlBus heatPumpControlBus annotation (Placement(transformation(extent={{-21,60},{20,98}})));
+
+23: Missing documentation, Name 'heatPump' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heat, Pump. Affected line: AixLib.Fluid.HeatPumps.ModularReversible.Modular heatPump( redeclare package MediumCon = Medium, redeclare package MediumEva = Medium, use_rev=false, tauCon=0.005*heatPump.rhoCon/heatPump.mCon_flow_nominal, dTCon_nominal=0, tauEva=0.005*heatPump.rhoEva/heatPump.mEva_flow_nominal, dpCon_nominal=0, use_conCap=false, CCon=0, GConOut=0, GConIns=0, dTEva_nominal=0, dpEva_nominal=0, use_evaCap=false, CEva=0, GEvaOut=0, GEvaIns=0, use_intSafCtr=false, energyDynamics=energyDynamics, QHea_flow_nominal=12740, redeclare model RefrigerantCycleHeatPumpHeating = AixLib.Fluid.HeatPumps.ModularReversible.RefrigerantCycle.TableData2D ( redeclare AixLib.Fluid.HeatPumps.ModularReversible.Data.TableData2D.EN255.Vitocal350BWH110 datTab), redeclare model RefrigerantCycleHeatPumpCooling = AixLib.Fluid.Chillers.ModularReversible.RefrigerantCycle.BaseClasses.NoCooling, mCon_flow_nominal=0.5, mEva_flow_nominal=0.5, TConHea_nominal=318.15, TEvaHea_nominal=273.15, TConCoo_nominal=273.15, TEvaCoo_nominal=273.15, use_busConOnl=true) annotation ( Placement(transformation( extent={{-10,10},{10,-10}}, rotation=90, origin={-30,10})));
+
+
+AixLib/Controls/HeatPump/TwoPointControlledHP.mo
+1: Name 'bandwidth' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: bandwidth. Affected line: parameter Real bandwidth "Bandwith of hysteresis of controller";
+
+2: Name 'onOffController' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Controller. Affected line: Modelica.Blocks.Logical.OnOffController onOffController(final bandwidth=bandwidth, final pre_y_start=false) "Hysteresis controller for set temperature" annotation (Placement(transformation(extent={{-60,20},{-40,40}})));
+
+
+AixLib/Obsolete/Year2019/Fluid/HeatPumps/HeatPumpDetailed.mo
+1: Missing documentation. Affected line: import Modelica.Units.SI;
+
+2: Name 'HPctrlType' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Pctrl, Type. Affected line: parameter Boolean HPctrlType=true "Capacity control type" annotation (Dialog( group="Heat Pump cycle", compact=true, descriptionLabel=true), choices( choice=true "On/off heat pump", choice=false "Speed controlled heat pump", radioButtons=true));
+
+3: Name 'capCalcType' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Calc, Type. Affected line: parameter Integer capCalcType=1 "Type of capacity calculation" annotation ( Dialog( group="Heat Pump cycle", compact=true, descriptionLabel=true, enable=HPctrlType), choices( choice=1 "Polynomial", choice=2 "Table (only on/off heat pump)", radioButtons=true));
+
+4: Name 'Medium_con' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Medium_con. Affected line: replaceable package Medium_con = Modelica.Media.Interfaces.PartialMedium "Medium outside the refrigerant cycle (Condenser)" annotation ( Evaluate=true, Dialog(tab="Evaporator, Condenser", group="Condenser"), choicesAllMatching=true);
+
+5: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: parameter SI.PressureDifference dp_conNominal=0 "Pressure loss at nominal mass flow in condenser" annotation (Dialog(tab="Evaporator, Condenser", group="Condenser"));
+
+6: Name 'Medium_eva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Medium_eva. Affected line: replaceable package Medium_eva = Modelica.Media.Interfaces.PartialMedium "Medium outside the refrigerant cycle (Evaporator)" annotation ( Evaluate=true, Dialog(tab="Evaporator, Condenser", group="Evaporator"), choicesAllMatching=true);
+
+7: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: parameter SI.PressureDifference dp_evaNominal=0 "Pressure loss at nominal mass flow in evaporator" annotation (Dialog(tab="Evaporator, Condenser", group="Evaporator"));parameter SI.Volume volume_eva=0.004 "External medium volume in heat exchanger" annotation (Dialog(tab="Evaporator, Condenser", group="Evaporator"));parameter SI.Volume volume_con=0.004 "External medium volume in heat exchanger" annotation (Dialog(tab="Evaporator, Condenser", group="Condenser"));
+
+8: Name 'dataTable' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: data, Table. Affected line: parameter AixLib.Obsolete.Year2024.DataBase.HeatPump.HeatPumpBaseDataDefinition dataTable=AixLib.Obsolete.Year2024.DataBase.HeatPump.EN255.Vitocal350BWH113() "Look-up table data for on/off heat pump according to EN255 or EN14511" annotation (choicesAllMatching=true, Dialog(enable=HPctrlType and ( capCalcType == 2), group="Capacity data"));
+
+9: Name 'data_poly' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: data_poly. Affected line: replaceable function data_poly = AixLib.Obsolete.Year2024.DataBase.HeatPump.Functions.Characteristics.ConstantQualityGrade constrainedby AixLib.Obsolete.Year2024.DataBase.HeatPump.Functions.Characteristics.PartialBaseFct "Polynomial heat pump characteristics for inverter heat pump" annotation ( choicesAllMatching=true, Dialog(enable=(capCalcType == 1), group="Capacity data"));
+
+10: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: parameter SI.Temperature T_startEva=273.15 "Initial evaporator temperature" annotation (Evaluate=true, Dialog( tab="Evaporator, Condenser", group="Initialization", enable=initEvaporatorVol));parameter SI.Temperature T_startCon=308.15 "Initial condenser temperature" annotation (Evaluate=true, Dialog( tab="Evaporator, Condenser", group="Initialization", enable=initCondenserVol));
+
+11: Name 'Corr_icing' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Corr_icing. Affected line: replaceable function Corr_icing = AixLib.Obsolete.Year2024.DataBase.HeatPump.Functions.DefrostCorrection.NoModel constrainedby AixLib.Obsolete.Year2024.DataBase.HeatPump.Functions.DefrostCorrection.PartialBaseFct "Frost/Defrost model (only air-to-water heat pumps)" annotation ( choicesAllMatching=true, Dialog( enable=(capCalcType == 1), group="Defrosting/Icing correction", tab="Advanced"));
+
+12: Name 'N_max' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: N. Affected line: parameter Real N_max=4200 "Maximum speed of compressor in 1/min (only used if used in polynom)" annotation (Dialog(enable=not (HPctrlType), group="Capacity data"));
+
+13: Name 'N_min' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: N. Affected line: parameter Real N_min=1500 "Minimum speed of compressor in 1/min (only used if used in polynom)" annotation (Dialog(enable=not (HPctrlType), group="Capacity data"));
+
+14: Name 'N_nom' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: N_nom. Affected line: parameter Real N_nom=3600 "Nominal speed of compressor in 1/min (only used if used in polynom)" annotation (Dialog(enable=HPctrlType and (capCalcType == 1), group="Capacity data"));
+
+15: Name 'P_eleOutput' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: P_ele, Output. Affected line: parameter Boolean P_eleOutput=false "Electric power consumption" annotation ( Dialog( group="Optional outputs", tab="Advanced", descriptionLabel=true), choices(checkBox=true));
+
+16: Documentation too short, Name 'CoP_output' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Co, P_output. Affected line: parameter Boolean CoP_output=false "CoP" annotation (Dialog( group="Optional outputs", tab="Advanced", descriptionLabel=true), choices(checkBox=true));
+
+17: Name 'PT1_cycle' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T1_cycle. Affected line: parameter Boolean PT1_cycle=false "First Order model for capacity" annotation (Dialog(group="Start/stop behavior", tab="Advanced"), choices( checkBox=true));
+
+18: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: parameter SI.Time timeConstantCycle=1 "Time constant for first order model" annotation (Dialog( group="Start/stop behavior", tab="Advanced", enable=PT1_cycle));
+
+19: Name 'eta_ele' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: eta_ele. Affected line: parameter Real eta_ele=1 "Assumption of P_tech/P_el (for calculation of Evaporator load)" annotation (Dialog(group="Assumptions", tab="Advanced"));
+
+20: Name 'factorScale' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: factor, Scale. Affected line: parameter Real factorScale=1 "Scaling factor (Attention: not physically correct)" annotation (Dialog(group="Assumptions", tab="Advanced"));
+
+21: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: parameter SI.Power P_eleAdd=0 "Additional electric power when heat pump is on (not influenced through scaling factor)" annotation (Dialog(group="Assumptions", tab="Advanced"));
+
+22: Name 'CorrFlowCo' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Corr, Co. Affected line: parameter Boolean CorrFlowCo=false "Correction of mass flow different from nominal flow in condenser (polynomials: make sure mass flow rate is not corrected in polynomials)" annotation (Dialog(group="Mass flow correction", tab="Advanced"), choices( checkBox=true));
+
+23: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: parameter SI.MassFlowRate mFlow_conNominal=0.5 "Nominal mass flow rate in condenser (only with polynomials, as already given in data tables)" annotation (Dialog( group="Mass flow correction", tab="Advanced", enable=(CorrFlowCo and capCalcType == 1)));
+
+24: Name 'CorrFlowEv' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Corr, Ev. Affected line: parameter Boolean CorrFlowEv=false "Correction of mass flow different from nominal flow in evaporator (polynomials: make sure mass flow rate is not corrected in polynomials)" annotation (Dialog(group="Mass flow correction", tab="Advanced"), choices( checkBox=true));
+
+25: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: parameter SI.MassFlowRate mFlow_evaNominal=0.5 "Nominal mass flow rate in evaporator (only for polynomials, as already given in data tables)" annotation (Dialog( group="Mass flow correction", tab="Advanced", enable=(CorrFlowEv and capCalcType == 1)));
+
+26: Name 'T_evaIn' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_eva. Affected line: AixLib.Fluid.Sensors.TemperatureTwoPort T_evaIn( redeclare package Medium = Medium_eva, m_flow_nominal=mFlow_evaNominal, T_start=T_startEva) "Temperature sensor at inlet of the evaporator" annotation (Placement(transformation( origin={-130,26}, extent={{-10,-10},{10,10}}, rotation=270)));
+
+27: Name 'T_conIn' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_con. Affected line: AixLib.Fluid.Sensors.TemperatureTwoPort T_conIn( redeclare package Medium = Medium_con, m_flow_nominal=mFlow_conNominal, T_start=T_startCon) "Temperature sensor at inlet of the condenser" annotation (Placement(transformation( origin={130,-26}, extent={{-10,-10},{10,10}}, rotation=90)));
+
+28: Name 'T_conOut' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_con. Affected line: AixLib.Fluid.Sensors.TemperatureTwoPort T_conOut( redeclare package Medium = Medium_con, m_flow_nominal=mFlow_conNominal, T_start=T_startCon) "Temperature sensor at outlet of the condenser" annotation (Placement(transformation( origin={130,48}, extent={{-10,-10},{10,10}}, rotation=90)));
+
+29: Name 'T_evaOut' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_eva. Affected line: AixLib.Fluid.Sensors.TemperatureTwoPort T_evaOut( redeclare package Medium = Medium_eva, m_flow_nominal=mFlow_evaNominal, T_start=T_startEva) "Temperature sensor at outlet of the evaporator" annotation (Placement(transformation( origin={-130,-46}, extent={{-10,-10},{10,10}}, rotation=270)));
+
+30: Name 'mFlow_con' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Flow_con. Affected line: AixLib.Fluid.Sensors.MassFlowRate mFlow_con(redeclare package Medium = Medium_con) "Mass flow sensor at the condenser" annotation (Placement( transformation( origin={130,-50}, extent={{-10,-10},{10,10}}, rotation=90)));
+
+31: Name 'P_eleOut' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: P_ele. Affected line: Modelica.Blocks.Interfaces.RealOutput P_eleOut(unit="W") if P_eleOutput "Electical power consumption" annotation (Placement(transformation( extent={{-10,-10},{10,10}}, rotation=270, origin={-50,-90})));
+
+32: Name 'CoP_out' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Co. Affected line: Modelica.Blocks.Interfaces.RealOutput CoP_out if CoP_output "Coefficient of Performance" annotation (Placement(transformation( extent={{-10,-10},{10,10}}, rotation=270, origin={-10,-90})));
+
+33: Name 'heatFlowRate_con' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heat, Rate_con. Affected line: Modelica.Thermal.HeatTransfer.Sources.PrescribedHeatFlow heatFlowRate_con "Heat flow rate of the condenser" annotation (Placement(transformation( origin={95,1}, extent={{9,-9},{-9,9}}, rotation=180)));
+
+34: Name 'heatFlowRate_eva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heat, Rate_eva. Affected line: public Modelica.Thermal.HeatTransfer.Sources.PrescribedHeatFlow heatFlowRate_eva "Heat flow rate of the evaporator" annotation (Placement(transformation( extent={{-10,-10},{10,10}}, rotation=180, origin={-96,2})));
+
+35: Name 'mFlow_eva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Flow_eva. Affected line: AixLib.Fluid.Sensors.MassFlowRate mFlow_eva(redeclare package Medium = Medium_eva) "Mass flow sensor at the evaporator" annotation (Placement( transformation( origin={-130,52}, extent={{-10,-10},{10,10}}, rotation=270)));
+
+36: Name 'cycle' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: cycle. Affected line: AixLib.Fluid.HeatPumps.BaseClasses.CycleHP cycle( HPctrlType=HPctrlType, capCalcType=capCalcType, dataTable=dataTable, redeclare function data_poly = data_poly, N_max=N_max, N_min=N_min, N_nom=N_nom, Corr_icing=Corr_icing, eta_ele=eta_ele, factorScale=factorScale, P_eleAdd=P_eleAdd, CorrFlowCo=CorrFlowCo, CorrFlowEv=CorrFlowEv, timeConstantCycle=timeConstantCycle, smoothness=smoothness, PT1_cycle=PT1_cycle, mFlow_conNominal=mFlow_conNominal, mFlow_evaNominal=mFlow_evaNominal, T_conMax=T_conMax) "Heat pump refrigerant circuit black box model" annotation (Placement(transformation(extent={{-50,-20},{40,40}})));
+
+37: Name 'N_in' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: N. Affected line: Modelica.Blocks.Interfaces.RealInput N_in if not HPctrlType "Rotational speed of compressor" annotation (Placement(transformation( extent={{-10,-10},{10,10}}, rotation=270, origin={-10,90})));
+
+38: Name 'heatLosses_con' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heat, Losses_con. Affected line: parameter Boolean heatLosses_con=false "Consider heat losses of condenser to ambient" annotation (Dialog(group="Heat losses of condenser", tab="Advanced"), choices(checkBox=true));
+
+39: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: parameter SI.ThermalConductance R_loss=1 "Thermal conductance of heat loss to ambient" annotation (Dialog( group="Heat losses of condenser", tab="Advanced", enable=heatLosses_con));
+
+40: Name 'N_inInternal' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: N, Internal. Affected line: protected Modelica.Blocks.Interfaces.RealInput N_inInternal "Needed to connect to conditional connector";
+
+41: Name 'T_ambInternal' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_amb, Internal. Affected line: Modelica.Blocks.Interfaces.RealInput T_ambInternal "Needed to connect to conditional connector";
+
+42: Name 'dummyZero' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: dummy, Zero. Affected line: public Modelica.Blocks.Sources.RealExpression dummyZero(y=0) "Dummy value used for rotational speed" annotation (Placement(transformation(extent={{0,60},{20,80}}, rotation=0)));
+
+43: Name 'heatConv' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heat, Conv. Affected line: Modelica.Thermal.HeatTransfer.Components.ThermalConductor heatConv(G=R_loss) "Heat flow through condenser casing with a given conductance" annotation (Placement(transformation(extent={{80,52},{100,72}})));
+
+44: Name 'T_amb' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_amb. Affected line: Modelica.Blocks.Interfaces.RealInput T_amb if heatLosses_con "Ambient temperatur input signal" annotation (Placement(transformation( extent={{-10,-10},{10,10}}, rotation=270, origin={50,90})));
+
+45: Name 'varTemp' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Temp. Affected line: Modelica.Thermal.HeatTransfer.Sources.PrescribedTemperature varTemp "Foreces heat losses according to ambient temperature" annotation (Placement(transformation(extent={{80,76},{100,96}})));
+
+46: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: parameter SI.Temperature T_conMax=338.15 "Maximum condenser outlet temperature" annotation (Dialog(group="Capacity data"));
+
+47: Name 'gainMinusOne' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Minus. Affected line: Modelica.Blocks.Math.Gain gainMinusOne(k=-1) "Calculated heat flow in evaporator has to be withdrawn" annotation ( Placement(transformation( extent={{-5,-5},{5,5}}, rotation=180, origin={-73,5})));
+
+48: Name 'evaporator' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: evaporator. Affected line: AixLib.Fluid.MixingVolumes.MixingVolume evaporator( nPorts=2, T_start(displayUnit="K") = T_startEva, m_flow_nominal=mFlow_evaNominal, redeclare package Medium = Medium_eva, V=volume_eva) "Volume of evaporator" annotation (Placement(transformation( extent={{-7,-6.75},{7,6.75}}, rotation=-90, origin={-120.75,1})));
+
+49: Name 'hydRes_eva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Res_eva. Affected line: AixLib.Fluid.FixedResistances.PressureDrop hydRes_eva( redeclare package Medium = Medium_eva, m_flow_nominal=mFlow_evaNominal, m_flow(start=mFlow_evaNominal), dp_nominal=dp_evaNominal) "The pressure drop caused by flow resistance in the evaporator" annotation ( Placement(transformation( extent={{8,-8},{-8,8}}, rotation=90, origin={-130,-22})));
+
+50: Name 'condenser' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: condenser. Affected line: AixLib.Fluid.MixingVolumes.MixingVolume condenser( nPorts=2, redeclare package Medium = Medium_con, T_start(displayUnit="K") = T_startCon, m_flow_nominal=mFlow_conNominal, V=volume_con) "Volume of condenser" annotation (Placement(transformation( extent={{7,6.75},{-7,-6.75}}, rotation=-90, origin={121.25,-1})));
+
+51: Name 'hydRes_con' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Res_con. Affected line: AixLib.Fluid.FixedResistances.PressureDrop hydRes_con( redeclare package Medium = Medium_con, m_flow_nominal=mFlow_conNominal, m_flow(start=mFlow_conNominal), dp_nominal=dp_conNominal) "The pressure drop caused by flow resistance in the condenser" annotation ( Placement(transformation( extent={{-8,-8},{8,8}}, rotation=90, origin={130,22})));
+
+
+AixLib/Controls/HeatPump/Examples/PartialHeatPumpController.mo
+1: Name 'T_meas' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_meas. Affected line: Modelica.Blocks.Sources.Sine T_meas( f=1/3600, amplitude=6, offset=310) "Generates the measured temperature" annotation (Placement(transformation(extent={{-100,20},{-80,40}})));
+
+2: Name 'T_set' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_set. Affected line: Modelica.Blocks.Sources.Constant T_set(k=310) "Provides the temperature set point" annotation (Placement(transformation(extent={{-100,-40},{-80,-20}})));
+
+3: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: replaceable BaseClasses.PartialTSetToNSet hPController constrainedby BaseClasses.PartialTSetToNSet( final use_secHeaGen=false, use_heaLim=false, T_heaLim=293.15, movAveTime=300) annotation (Placement(transformation(extent={{-20,-20}, {20,20}})), __Dymola_choicesAllMatching=true);
+
+4: Name 'T_oda' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_oda. Affected line: Modelica.Blocks.Sources.Constant T_oda(k=273.15) "Provides the temperature set point" annotation (Placement(transformation(extent={{-100,-80},{-80,-60}})));
+
+
+AixLib/Obsolete/Year2019/Fluid/HeatPumps/Examples/HeatPumpDetailed.mo
+1: Missing documentation, Name 'Medium_sin' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Medium_sin. Affected line: replaceable package Medium_sin = AixLib.Media.Water constrainedby Modelica.Media.Interfaces.PartialMedium annotation (choicesAllMatching=true);
+
+2: Missing documentation, Name 'Medium_sou' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Medium_sou. Affected line: replaceable package Medium_sou = AixLib.Media.Air constrainedby Modelica.Media.Interfaces.PartialMedium annotation (choicesAllMatching=true);
+
+3: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: .AixLib.Obsolete.Year2019.Fluid.HeatPumps.HeatPumpDetailed heatPump( P_eleOutput=true, capCalcType=2, CorrFlowCo=false, CorrFlowEv=false, dataTable=DataBase.HeatPump.EN255.Vitocal350BWH113(), PT1_cycle=true, timeConstantCycle=1, mFlow_conNominal=1, mFlow_evaNominal=1, T_evaIn(transferHeat=true, TAmb=291.15), T_evaOut(transferHeat=true, TAmb=291.15), T_conIn(transferHeat=true, TAmb=273.15), T_conOut(transferHeat=true, TAmb=273.15), redeclare package Medium_con = Medium_sin, redeclare package Medium_eva = Medium_sou) "Detailed heat pump mainly based on manufacturing data" annotation (Placement(transformation(extent={{-16,14},{14,-6}})));
+
+4: Name 'sourceSideMassFlowSource' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: source, Side, Mass, Source. Affected line: AixLib.Fluid.Sources.MassFlowSource_T sourceSideMassFlowSource( use_T_in=true, m_flow=1, redeclare package Medium = Medium_sou, nPorts=1, T=275.15) "Ideal mass flow source at the inlet of the source side" annotation (Placement(transformation(extent={{-54,-80},{-34,-60}})));
+
+5: Name 'sourceSideFixedBoundary' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: source, Side, Fixed, Boundary. Affected line: AixLib.Fluid.Sources.Boundary_pT sourceSideFixedBoundary(redeclare package Medium = Medium_sou, nPorts=1) "Fixed boundary at the outlet of the source side" annotation (Placement( transformation( extent={{-10,10},{10,-10}}, rotation=0, origin={-80,36})));
+
+6: Name 'TsuSourceRamp' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Source, Ramp. Affected line: Modelica.Blocks.Sources.Ramp TsuSourceRamp( duration=1000, startTime=1000, height=25, offset=278) "Ramp signal for the temperature input of the source side's ideal mass flow source" annotation (Placement(transformation(extent={{-94,-84},{-74,-64}})));
+
+7: Missing documentation. Affected line: Modelica.Blocks.Logical.Hysteresis hys( pre_y_start=true, uLow=273.15 + 30, uHigh=273.15 + 40) annotation (Placement(transformation(extent={{64,50},{44,70}})));
+
+8: Missing documentation, Name 'sine' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sine. Affected line: Modelica.Blocks.Sources.Sine sine( f=1/3600, amplitude=3000, offset=3000) annotation (Placement(transformation(extent={{76,26},{84,34}})));
+
+9: Missing documentation. Affected line: Modelica.Blocks.Sources.Constant nIn(k=100) annotation (Placement( transformation( extent={{4,-4},{-4,4}}, rotation=90, origin={50,34})));
+
+10: Name 'heatFlowRateCon' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heat, Rate. Affected line: Modelica.Thermal.HeatTransfer.Sources.PrescribedHeatFlow heatFlowRateCon "Heat flow rate of the condenser" annotation (Placement(transformation( extent={{-6,6},{6,-6}}, rotation=270, origin={94,6})));
+
+11: Missing documentation. Affected line: Modelica.Blocks.Math.Gain gain(k=-1) annotation (Placement(transformation( extent={{-4,-4},{4,4}}, rotation=270, origin={96,22})));
+
+12: Name 'sinkSideFixedBoundary' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sink, Side, Fixed, Boundary. Affected line: AixLib.Fluid.Sources.Boundary_pT sinkSideFixedBoundary(redeclare package Medium = Medium_sin, nPorts=1) "Fixed boundary at the outlet of the sink side" annotation (Placement( transformation( extent={{10,-10},{-10,10}}, rotation=0, origin={88,-64})));
+
+
+AixLib/Obsolete/Year2019/Fluid/HeatPumps/BaseClasses/CycleHP.mo
+1: Missing documentation. Affected line: import Modelica.Units.SI;
+
+2: Name 'HPctrlType' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Pctrl, Type. Affected line: parameter Boolean HPctrlType = true "Capacity control type" annotation(Dialog(group = "Heat Pump cycle", compact = true, descriptionLabel = true), choices(choice=true "On/off heat pump",choice = false "Speed controlled heat pump", radioButtons = true));
+
+3: Name 'capCalcType' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Calc, Type. Affected line: parameter Integer capCalcType = 1 "Type of capacity calculation" annotation(Dialog(group = "Heat Pump cycle", compact = true, descriptionLabel = true, enable=HPctrlType), choices(choice=1 "Polynomial", choice = 2 "Table (only on/off heat pump)", radioButtons = true));
+
+4: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: parameter DataBase.HeatPump.HeatPumpBaseDataDefinition dataTable=AixLib.Obsolete.Year2024.DataBase.HeatPump.EN255.Vitocal350BWH113() "Look-up table data for on/off heat pump according to EN255/EN14511" annotation (choicesAllMatching=true, Dialog(enable=HPctrlType and ( capCalcType == 2), group="Capacity data"));
+
+5: Missing documentation, Name 'tableQdot_con' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: table, Qdot_con. Affected line: protected final parameter Real tableQdot_con[:,:]=dataTable.tableQdot_con;
+
+6: Missing documentation, Name 'tableP_ele' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: table, P_ele. Affected line: final parameter Real tableP_ele[:,:]= dataTable.tableP_ele;
+
+7: Name 'data_poly' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: data_poly. Affected line: public replaceable function data_poly = AixLib.Obsolete.Year2024.DataBase.HeatPump.Functions.Characteristics.ConstantQualityGrade constrainedby AixLib.Obsolete.Year2024.DataBase.HeatPump.Functions.Characteristics.PartialBaseFct "Polynomial heat pump characteristics" annotation(choicesAllMatching = true,Dialog(enable=(capCalcType==1),group="Capacity data"));
+
+8: Name 'Corr_icing' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Corr_icing. Affected line: replaceable function Corr_icing = AixLib.Obsolete.Year2024.DataBase.HeatPump.Functions.DefrostCorrection.NoModel constrainedby AixLib.Obsolete.Year2024.DataBase.HeatPump.Functions.DefrostCorrection.PartialBaseFct "Frost/Defrost model (only air-to-water heat pumps)" annotation(choicesAllMatching = true,Dialog(enable=(capCalcType==1),group="Defrosting/Icing correction",tab="Advanced"));
+
+9: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: parameter SI.Temperature T_conMax=338.15 "Maximum condenser outlet temperature" annotation(Dialog(group="Heat Pump cycle"));
+
+10: Name 'N_max' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: N. Affected line: parameter Real N_max=4200 "Maximum speed of compressor in 1/min (only used if used in polynom)" annotation(Dialog(enable=not (HPctrlType),group="Capacity data"));
+
+11: Name 'N_min' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: N. Affected line: parameter Real N_min=1500 "Minimum speed of compressor in 1/min (only used if used in polynom)" annotation(Dialog(enable=not (HPctrlType),group="Capacity data"));
+
+12: Name 'N_nom' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: N_nom. Affected line: parameter Real N_nom=3600 "Nominal speed of compressor in 1/min (only used if used in polynom)" annotation(Dialog(enable=HPctrlType and (capCalcType == 1),group="Capacity data"));
+
+13: Name 'PT1_cycle' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T1_cycle. Affected line: parameter Boolean PT1_cycle=false "First Order model for capacity" annotation(Dialog(group = "Start/stop behavior",tab="Advanced"), choices(checkBox=true));
+
+14: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: parameter SI.Time timeConstantCycle=1 "Time constant for first order model" annotation(Dialog(group = "Start/stop behavior",tab="Advanced", enable=PT1_cycle));
+
+15: Name 'eta_ele' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: eta_ele. Affected line: parameter Real eta_ele=1 "Assumption of P_tech/P_el (for calculation of Evaporator load)" annotation(Dialog(group="Assumptions",tab="Advanced"));
+
+16: Name 'factorScale' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: factor, Scale. Affected line: parameter Real factorScale=1 "Scaling factor (Attention: not physically correct)" annotation(Dialog(group="Assumptions",tab="Advanced"));
+
+17: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: parameter SI.Power P_eleAdd=0 "Additional electric power when heat pump is on (not influenced through scaling factor)" annotation(Dialog(group="Assumptions",tab="Advanced"));
+
+18: Name 'CorrFlowCo' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Corr, Co. Affected line: parameter Boolean CorrFlowCo=false "Correction of mass flow different from nominal flow in condenser (use only if not included in polynom)" annotation(Dialog(group="Mass flow correction",tab="Advanced"), choices(checkBox=true));
+
+19: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: parameter SI.MassFlowRate mFlow_conNominal=0.5 "Nominal mass flow rate in condenser" annotation(Dialog(group="Mass flow correction",tab="Advanced", enable=(CorrFlowCo and capCalcType==1)));
+
+20: Name 'CorrFlowEv' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Corr, Ev. Affected line: parameter Boolean CorrFlowEv=false "Correction of mass flow different from nominal flow in evaporator (use only if not included in polynom)" annotation(Dialog(group="Mass flow correction",tab="Advanced"), choices(checkBox=true));
+
+21: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: parameter SI.MassFlowRate mFlow_evaNominal=0.5 "Nominal mass flow rate in evaporator" annotation(Dialog(group="Mass flow correction",tab="Advanced",enable=(CorrFlowEv and capCalcType==1)));SI.Power P_ele;SI.Power P_eleChar;SI.HeatFlowRate Qdot_eva;SI.HeatFlowRate Qdot_con;SI.HeatFlowRate Qdot_conChar;
+
+22: Missing documentation, Name 'CoP;' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Co. Affected line: Real CoP;
+
+23: Missing documentation, Name 'CoP_corr;' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Co, P_corr. Affected line: Real CoP_corr;
+
+24: Missing documentation, Name 'CoP_char;' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Co, P_char. Affected line: Real CoP_char;
+
+25: Missing documentation, Name 'N;' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: N. Affected line: Real N;
+
+26: Missing documentation, Name 'factorCoP_icing;' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: factor, Co, P_icing. Affected line: Real factorCoP_icing;
+
+27: Missing documentation, Name 'Char' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Char. Affected line: Real Char[2];
+
+28: Missing documentation, Name 'T_conOutCorr;' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_con, Corr. Affected line: Real T_conOutCorr;
+
+29: Missing documentation, Name 'T_evaInCorr;' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_eva, Corr. Affected line: Real T_evaInCorr;
+
+30: Missing documentation, Name 'P_eleOut' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: P_ele. Affected line: Modelica.Blocks.Interfaces.RealOutput P_eleOut annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=270, origin={-50,-90})));
+
+31: Missing documentation. Affected line: Modelica.Blocks.Interfaces.BooleanInput onOff_in annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=270, origin={-50,90})));
+
+32: Missing documentation, Name 'CoP_out' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Co. Affected line: Modelica.Blocks.Interfaces.RealOutput CoP_out annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=270, origin={-10,-90})));
+
+33: Missing documentation, Name 'N_in' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: N. Affected line: Modelica.Blocks.Interfaces.RealInput N_in annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=270, origin={-10,90})));
+
+34: Name 'firstOrder_outInternal' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: first, Order, Internal. Affected line: protected Modelica.Blocks.Interfaces.RealInput firstOrder_outInternal "Needed to connect to conditional model";
+
+35: Name 'firstOrder_inInternal' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: first, Order, Internal. Affected line: Modelica.Blocks.Interfaces.RealOutput firstOrder_inInternal "Needed to connect to conditional model";
+
+36: Name 'Qdot_conTableInternal' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Qdot_con, Table, Internal. Affected line: Modelica.Blocks.Interfaces.RealInput Qdot_conTableInternal "Needed to connect to conditional model";
+
+37: Name 'P_eleTableInternal' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: P_ele, Table, Internal. Affected line: Modelica.Blocks.Interfaces.RealInput P_eleTableInternal "Needed to connect to conditional model";
+
+38: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: SI.MassFlowRate mFlow_conNom;SI.MassFlowRate mFlow_evaNom;
+
+39: Missing documentation, Name 'realQdot_con' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: real, Qdot_con. Affected line: public Modelica.Blocks.Sources.RealExpression realQdot_con(y=Qdot_con) annotation (Placement(transformation(extent={{40,24},{60,44}}, rotation=0)));
+
+40: Missing documentation, Name 'realQdot_eva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: real, Qdot_eva. Affected line: public Modelica.Blocks.Sources.RealExpression realQdot_eva(y=Qdot_eva) annotation (Placement(transformation(extent={{-10,-10},{10,10}}, rotation=180, origin={-110,-10})));
+
+41: Missing documentation, Name 'realPel' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: real. Affected line: public Modelica.Blocks.Sources.RealExpression realPel(y=P_ele) annotation (Placement( transformation(extent={{-92,-40},{-72,-20}}, rotation=0)));
+
+42: Missing documentation, Name 'realCoP' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: real, Co. Affected line: public Modelica.Blocks.Sources.RealExpression realCoP(y=CoP) annotation (Placement( transformation(extent={{-32,-66},{-12,-46}}, rotation=0)));
+
+43: Name 'Qdot_ConTable' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Qdot_, Table. Affected line: Modelica.Blocks.Tables.CombiTable2Ds Qdot_ConTable( tableName="NoName", fileName="NoName", table=tableQdot_con, smoothness=smoothness) if not (capCalcType == 1) annotation (extent=[-60,40;-40,60], Placement(transformation(extent={{-40,20},{-20,40}})));
+
+44: Name 'P_eleTable' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: P_ele, Table. Affected line: Modelica.Blocks.Tables.CombiTable2Ds P_eleTable( tableName="NoName", fileName="NoName", table=tableP_ele, smoothness=smoothness) if not (capCalcType == 1) "Electrical power table" annotation (extent=[-60,-20; -40,0], Placement(transformation(extent={{-40, -10},{-20,10}})));
+
+45: Missing documentation, Name 'realT_evaIn' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: real, T_eva. Affected line: public Modelica.Blocks.Sources.RealExpression realT_evaIn(y=T_evaInCorr) annotation (Placement(transformation(extent={{-94,26},{-74,46}}, rotation=0)));
+
+46: Missing documentation, Name 'realT_conOut' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: real, T_con. Affected line: public Modelica.Blocks.Sources.RealExpression realT_conOut(y=T_conOutCorr) annotation (Placement(transformation(extent={{-94,6},{-74,26}}, rotation=0)));
+
+47: Missing documentation, Name 'firstOrder' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: first, Order. Affected line: Modelica.Blocks.Continuous.FirstOrder firstOrder(T=timeConstantCycle) if PT1_cycle annotation (Placement(transformation(extent={{42,-6},{62,14}})));
+
+48: Missing documentation, Name 'productPelCoP1' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: product, Co. Affected line: public Modelica.Blocks.Math.Product productPelCoP1 annotation (Placement( transformation(extent={{8,-46},{28,-26}}, rotation=0)));
+
+49: Missing documentation, Name 't_Ev_in' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: t_, Ev. Affected line: Modelica.Blocks.Math.UnitConversions.To_degC t_Ev_in annotation (extent=[-88,38; -76,50], Placement(transformation(extent={{-68,30}, {-56,42}})));
+
+50: Missing documentation, Name 't_Co_out' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: t_, Co. Affected line: Modelica.Blocks.Math.UnitConversions.To_degC t_Co_out annotation (extent=[-88,38; -76,50], Placement(transformation(extent={{-68,10}, {-56,22}})));
+
+51: Missing documentation, Name 'dummyZero' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: dummy, Zero. Affected line: public Modelica.Blocks.Sources.RealExpression dummyZero(y=0) annotation (Placement( transformation(extent={{40,-86},{60,-66}}, rotation=0)));
+
+52: Missing documentation, Name 'realCoP_corr' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: real, Co, P_corr. Affected line: public Modelica.Blocks.Sources.RealExpression realCoP_corr(y=CoP_corr) annotation ( Placement(transformation(extent={{-32,-50},{-12,-30}}, rotation=0)));
+
+53: Missing documentation, Name 'realP_eleAdd' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: real, P_ele. Affected line: public Modelica.Blocks.Logical.TriggeredTrapezoid realP_eleAdd(amplitude=P_eleAdd) annotation (Placement(transformation(extent={{-72,-54},{-64,-46}}, rotation=0)));
+
+54: Missing documentation, Name 'greaterZero' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: greater, Zero. Affected line: public Modelica.Blocks.Logical.GreaterThreshold greaterZero annotation (Placement( transformation(extent={{-88,-54},{-80,-46}}, rotation=0)));
+
+55: Missing documentation. Affected line: Modelica.Blocks.Math.Add add annotation (Placement(transformation(extent={{-56,-52},{-46,-42}})));
+
+56: Missing documentation, Name 'dummyOne' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: dummy. Affected line: public Modelica.Blocks.Sources.RealExpression dummyOne(y=1) annotation (Placement( transformation(extent={{40,-70},{60,-50}}, rotation=0)));
+
+57: Name 'Qdot_conOut' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Qdot_con. Affected line: public Modelica.Blocks.Interfaces.RealOutput Qdot_conOut "Value of Real output" annotation (Placement(transformation(extent={{120,0},{140,20}})));
+
+58: Missing documentation, Name 't_conIn' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: t_con. Affected line: Modelica.Blocks.Math.UnitConversions.To_degC t_conIn annotation (extent=[-88,38; -76,50], Placement(transformation(extent={{116,-36}, {104,-24}})));
+
+59: Name 'T_conIn' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_con. Affected line: Modelica.Blocks.Interfaces.RealInput T_conIn "Connector of Real input signal to be converted" annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=180, origin={130,-30})));
+
+60: Name 'T_evaIn' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_eva. Affected line: Modelica.Blocks.Interfaces.RealInput T_evaIn "Connector of Real input signal to be converted" annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=0, origin={-130,-30})));
+
+61: Name 'Qdot_evaOut' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Qdot_eva. Affected line: Modelica.Blocks.Interfaces.RealOutput Qdot_evaOut "Value of Real output" annotation (Placement(transformation( extent={{-10,-10},{10,10}}, rotation=180, origin={-130,10})));
+
+62: Name 'T_conOut' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_con. Affected line: Modelica.Blocks.Interfaces.RealInput T_conOut "Connector of Real input signal to be converted" annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=180, origin={130,50})));
+
+63: Name 'T_evaOut' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_eva. Affected line: Modelica.Blocks.Interfaces.RealInput T_evaOut "Connector of Real input signal to be converted" annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=0, origin={-130,50})));
+
+64: Name 'mFlow_eva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Flow_eva. Affected line: Modelica.Blocks.Interfaces.RealInput mFlow_eva "Connector of Real input signal to be converted" annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=0, origin={-130,30})));
+
+65: Name 'mFlow_con' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Flow_con. Affected line: Modelica.Blocks.Interfaces.RealInput mFlow_con "Connector of Real input signal to be converted" annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=180, origin={130,-10})));
+
+66: Missing documentation, Name 'maxTempCon' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Temp. Affected line: public Modelica.Blocks.Sources.RealExpression maxTempCon(y=T_conMax) annotation ( Placement(transformation(extent={{14,52},{34,72}}, rotation=0)));
+
+67: Missing documentation, Name 'productPelCoP2' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: product, Co. Affected line: public Modelica.Blocks.Math.Product productPelCoP2 annotation (Placement( transformation(extent={{80,30},{100,50}}, rotation=0)));
+
+68: Missing documentation, Name 'PIDmaxHeatFlowCon' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Heat. Affected line: Modelica.Blocks.Continuous.LimPID PIDmaxHeatFlowCon( controllerType=Modelica.Blocks.Types.SimpleController.PI, Ti=1, yMax=1, yMin=0, y_start=1) annotation (Placement(transformation(extent={{46,52},{66,72}})));
+
+
+AixLib/Fluid/Examples/GeothermalHeatPump/GeothermalHeatPump.mo
+1: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Sources.Boundary_pT coldConsumerFlow(redeclare package Medium = Medium, nPorts=1) annotation (Placement(transformation( extent={{-6,-6},{6,6}}, rotation=180, origin={154,-20})));Sources.Boundary_pT heatConsumerFlow(redeclare package Medium = Medium, nPorts=1) "Sink representing heat consumer" annotation (Placement(transformation( extent={{-6,-6},{6,6}}, rotation=180, origin={154,-50})));Sources.Boundary_pT heatConsumerReturn(redeclare package Medium = Medium, nPorts=1, T=303.15) "Source representing heat consumer" annotation (Placement(transformation( extent={{-6,-6},{6,6}}, rotation=180, origin={154,-106})));Sources.Boundary_pT coldConsumerReturn(redeclare package Medium = Medium, nPorts=1, T=287.15) "Source representing cold consumer" annotation (Placement(transformation( extent={{-6,-6},{6,6}}, rotation=180, origin={154,32})));
+
+2: Name 'pressureDifference' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: pressure, Difference. Affected line: Modelica.Blocks.Sources.Constant pressureDifference(k=60000) "Pressure difference used for all pumps" annotation ( Placement(transformation( extent={{-6,-6},{6,6}}, rotation=180, origin={154,6})));
+
+3: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Controls.HeatPump.TwoPointControlledHP twoPointControlledHP( use_secHeaGen=false, use_heaLim=false, T_heaLim=293.15, movAveTime=300, bandwidth=2) "Controls the temperature in the heat storage by switching the heat pump on or off" annotation (Placement(transformation(extent={{-80,60},{-60,80}})));
+
+4: Name 'TStorageSet' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Storage. Affected line: Modelica.Blocks.Sources.Constant TStorageSet(k=273.15 + 45) "Set point of upper heat storage temperature" annotation (Placement(transformation(extent={{-120,70},{-110,80}})));
+
+5: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Control.geothermalFieldController geothermalFieldControllerCold( temperature_low=273.15 + 8, temperature_high=273.15 + 10) "Controls the heat exchange with the geothermal field and the heat storage" annotation (Placement(transformation(extent={{-102,28},{-86,44}})));Control.geothermalFieldController geothermalFieldControllerHeat( temperature_low=308.15, temperature_high=313.15) "Controls the heat exchange with the geothermal field and the heat storage" annotation (Placement(transformation(extent={{-100,-34},{-84,-18}})));
+
+6: Name 'mode' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: mode. Affected line: Modelica.Blocks.Sources.BooleanConstant mode "Dummy signal for unit mode, true: heat pump, false: chiller" annotation (Placement(transformation(extent={{-56,56},{-44,68}})));
+
+
+AixLib/Obsolete/YearIndependent/FastHVAC/Examples/HeatGenerators/HeatPump/HeatPump.mo
+1: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: FastHVAC.Components.Sensors.TemperatureSensor temperatureSensor annotation (Placement(transformation(extent={{48,-70},{66,-52}})));FastHVAC.Components.Pumps.FluidSource fluidSource(medium= FastHVAC.Media.WaterSimple()) "Fluidsource for source" annotation (Placement(transformation(extent={{-50,-44},{-30,-24}})));
+
+2: Documentation too short, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Components.HeatGenerators.HeatPump.HeatPump heatPump( refIneFre_constant=1, Medium_con=Media.WaterSimple(), Medium_eva=Media.WaterSimple(), mFlow_conNominal=0.5, VCon=0.4, deltaM_con=0.1, use_ConCap=false, CCon=100, GCon=5, mFlow_evaNominal=0.5, VEva=0.04, deltaM_eva=0.1, use_EvaCap=false, CEva=100, GEva=5, allowFlowReversalEva=true, use_revHP=true, TCon_start(displayUnit="K"), TEva_start(displayUnit="K"), redeclare model PerDataHea = AixLib.Obsolete.Year2024.DataBase.HeatPump.PerformanceData.LookUpTable2D ( dataTable=AixLib.Obsolete.Year2024.DataBase.HeatPump.EN14511.Vitocal200AWO201()), redeclare model PerDataChi = AixLib.Obsolete.Year2024.DataBase.Chiller.PerformanceData.LookUpTable2D ( dataTable=AixLib.Obsolete.Year2024.DataBase.Chiller.EN14511.Vitocal200AWO201()), Q_useNominal=0, use_autoCalc=false, TAmbCon_nominal=288.15) annotation (Placement(transformation( extent={{-13,-16},{13,16}}, rotation=-90, origin={3,-2})));
+
+3: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: FastHVAC.Components.Sinks.Vessel vessel_ev "vessel for open evaporator circuit" annotation (Placement( transformation( extent={{-11,-9},{11,9}}, rotation=180, origin={-35,57})));
+
+4: Name 'dotm_source' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: dotm_source. Affected line: Modelica.Blocks.Sources.Constant dotm_source(k=1) "Source mass flow signal" annotation (Placement(transformation(extent={{-98,-82},{-78,-62}})));
+
+5: Name 'dotm_sink' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: dotm_sink. Affected line: Modelica.Blocks.Sources.Constant dotm_sink(k=0.106) "sink mass flow signal" annotation (Placement( transformation( extent={{-4,-4},{4,4}}, rotation=270, origin={36,38})));
+
+6: Name 'T_amb_internal' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_amb. Affected line: Modelica.Blocks.Sources.Constant T_amb_internal(k=291.15) "Constant internal ambient temeprature" annotation (Placement(transformation(extent={{7,-7},{-7,7}}, rotation=-90, origin={3,-35})));
+
+7: Name 'booleanToReal' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: boolean, Real. Affected line: Modelica.Blocks.Math.BooleanToReal booleanToReal "on off control " annotation (Placement(transformation(extent={{4,4},{-4,-4}}, rotation=90, origin={6,40})));
+
+8: Name 'TsuSourceRamp' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Source, Ramp. Affected line: Modelica.Blocks.Sources.Ramp TsuSourceRamp( duration=1000, startTime=1000, height=25, offset=278) "Ramp signal for the temperature input of the source side's ideal mass flow source" annotation (Placement(transformation(extent={{-96,-34},{-76,-14}})));
+
+9: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: BaseClasses.WorkingFluid Room(m_fluid=5*1000, T0=293.15) "Volume" annotation ( Placement(transformation( extent={{-10,-10},{10,10}}, rotation=90, origin={90,-26})));
+
+10: Name 'heatFlowRateCon' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heat, Rate. Affected line: Modelica.Thermal.HeatTransfer.Sources.PrescribedHeatFlow heatFlowRateCon "Heat flow rate of the condenser" annotation (Placement(transformation( extent={{-6,6},{6,-6}}, rotation=270, origin={52,-18})));
+
+11: Name 'sine' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sine. Affected line: Modelica.Blocks.Sources.Sine sine( f=1/3600, amplitude=3000, offset=3000) "hourly sine " annotation (Placement(transformation(extent={{66,8},{58,16}})));
+
+12: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Components.Pumps.Pump pump "sink pump" annotation (Placement(transformation( extent={{10,-10},{-10,10}}, rotation=0, origin={36,20})));
+
+13: Missing documentation, Name 'booleanStep' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: boolean, Step. Affected line: Modelica.Blocks.Sources.BooleanStep booleanStep(startTime=10000, startValue=true) annotation (Placement(transformation(extent={{-6,-6},{6,6}}, rotation=270, origin={0,78})));
+
+14: Missing documentation, Name 'hysHeating' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Heating. Affected line: Modelica.Blocks.Logical.Hysteresis hysHeating( pre_y_start=true, uLow=273.15 + 30, uHigh=273.15 + 35) annotation (Placement(transformation(extent={{66,58},{56,68}})));
+
+15: Missing documentation, Name 'logicalSwitch' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: logical, Switch. Affected line: Modelica.Blocks.Logical.LogicalSwitch logicalSwitch annotation (Placement(transformation(extent={{26,50},{16,60}})));
+
+16: Missing documentation, Name 'hysCooling' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Cooling. Affected line: Modelica.Blocks.Logical.Hysteresis hysCooling( pre_y_start=false, uLow=273.15 + 15, uHigh=273.15 + 19) annotation (Placement(transformation(extent={{58,42},{48,52}})));
+
+
+AixLib/Controls/HeatPump/HPControl.mo
+1: Missing documentation, Name 'HeatingCurveFunction' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Heating, Curve, Function. Affected line: replaceable function HeatingCurveFunction = SetPoints.Functions.HeatingCurveFunction constrainedby SetPoints.Functions.PartialBaseFct annotation (Dialog(group="Heating Curve - Data", enable = not use_tableData),choicesAllMatching=true);
+
+2: Name 'heatingCurveRecord' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heating, Curve, Record. Affected line: parameter AixLib.DataBase.Boiler.DayNightMode.HeatingCurvesDayNightBaseDataDefinition heatingCurveRecord= AixLib.DataBase.Boiler.DayNightMode.HeatingCurves_Vitotronic_Day25_Night10() "Record with information about heating curve data" annotation (Dialog(group="Heating Curve - Data", enable = use_tableData),choicesAllMatching=true);
+
+3: Name 'declination' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: declination. Affected line: parameter Real declination=2 "Declination of curve" annotation (Dialog(group="Heating Curve - Data", enable = use_tableData));
+
+4: Name 'day_hour' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: day_hour. Affected line: parameter Real day_hour=6 "Hour of day at which day mode is enabled" annotation (Dialog(group="Heating Curve - Night mode"));
+
+5: Name 'night_hour' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: night_hour. Affected line: parameter Real night_hour=22 "Hour of day at which night mode is enabled" annotation (Dialog(group="Heating Curve - Night mode"));
+
+6: Name 'weekly' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: weekly. Affected line: parameter Boolean weekly=true "Switch between a daily or weekly trigger approach" annotation(Dialog(tab="Anti Legionella",descriptionLabel=true), choices(choice=true "Weekly", choice=false "Daily", radioButtons=true));
+
+7: Name 'trigWeekDay' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: trig, Week. Affected line: parameter Integer trigWeekDay "Day of the week at which control is triggered" annotation (Dialog(tab="Anti Legionella", enable=use_antLeg and weekly));
+
+8: Name 'trigHour' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: trig, Hour. Affected line: parameter Integer trigHour=3 "Hour of the day at which control is triggered" annotation (Dialog(tab="Anti Legionella", enable=use_antLeg));
+
+9: Missing documentation, Name 'antiLegionella' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: anti, Legionella. Affected line: AixLib.Controls.HeatPump.AntiLegionella antiLegionella( final TLegMin=TLegMin, minTimeAntLeg=minTimeAntLeg, trigWeekDay=trigWeekDay, trigHour=trigHour, yearRef=2017, final zerTim=zerTim) if use_antLeg annotation (Placement(transformation(extent={{-26,-14},{14,26}})));
+
+10: Missing documentation. Affected line: AixLib.Fluid.HeatPumps.ModularReversible.BaseClasses.RefrigerantMachineControlBus sigBusHP annotation (Placement(transformation(extent={{-116,-72},{-88,-44}})));
+
+11: Name 'T_oda' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_oda. Affected line: Modelica.Blocks.Interfaces.RealInput T_oda "Outdoor air temperature" annotation (Placement(transformation(extent={{-128,-14},{-100,14}}), iconTransformation(extent={{-140,-26},{-100,14}})));
+
+12: Missing documentation, Name 'y_sou' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: y_sou. Affected line: Modelica.Blocks.Interfaces.RealOutput y_sou annotation (Placement(transformation(extent={{14,-14},{-14,14}}, rotation=90, origin={-60,-114})));
+
+13: Missing documentation, Name 'y_sin' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: y_sin. Affected line: Modelica.Blocks.Interfaces.RealOutput y_sin annotation (Placement(transformation( extent={{14,-14},{-14,14}}, rotation=90, origin={60,-114})));
+
+14: Name 'constHeating1' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Heating. Affected line: Modelica.Blocks.Sources.Constant constHeating1(final k=1) "If you want to include chilling, please insert control blocks first" annotation (Placement(transformation(extent={{10,-10},{-10,10}}, rotation=90, origin={-12,-72})));
+
+15: Missing documentation, Name 'heatCurve' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heat, Curve. Affected line: AixLib.Controls.SetPoints.HeatingCurve heatCurve( final TOffset=0, final use_dynTRoom=false, final zerTim=zerTim, final day_hour=day_hour, final night_hour=night_hour, final heatingCurveRecord=heatingCurveRecord, final declination=declination, redeclare function HeatingCurveFunction = HeatingCurveFunction, use_tableData=use_tableData, final TRoom_nominal=293.15) annotation (Placement(transformation(extent={{-74,10},{-54,30}})));
+
+16: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: TSetToNSet ConvTSetToNSet annotation (Placement(transformation(extent={{44,-8},{76,26}})));
+
+17: Name 'realPasThrAntLeg' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: real. Affected line: Modelica.Blocks.Routing.RealPassThrough realPasThrAntLeg if not use_antLeg "No Anti Legionella" annotation ( choicesAllMatching=true, Placement( transformation(extent={{-10,38},{6,54}})));
+
+18: Name 'constHeating' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Heating. Affected line: Modelica.Blocks.Sources.BooleanConstant constHeating(final k=true) "If you want to include chilling, please insert control blocks first" annotation (Placement(transformation(extent={{82,-26},{94,-14}})));
+
+
+AixLib/Obsolete/YearIndependent/FastHVAC/Examples/Chiller/Chiller.mo
+1: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: FastHVAC.Components.Sensors.TemperatureSensor temperatureSensor annotation (Placement(transformation(extent={{52,-38},{66,-52}})));FastHVAC.Components.Pumps.FluidSource fluidSource(medium= FastHVAC.Media.WaterSimple()) "Fluidsource for sink" annotation (Placement(transformation(extent={{-50,-44},{-30,-24}})));
+
+2: Documentation too short, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Components.Chiller.Chiller chiller( use_revChi=true, redeclare model PerDataMainChi = AixLib.Obsolete.Year2024.DataBase.Chiller.PerformanceData.LookUpTable2D ( dataTable=AixLib.Obsolete.Year2024.DataBase.Chiller.EN14511.Vitocal200AWO201()), redeclare model PerDataRevChi = AixLib.Obsolete.Year2024.DataBase.HeatPump.PerformanceData.LookUpTable2D ( smoothness=Modelica.Blocks.Types.Smoothness.LinearSegments, dataTable= AixLib.Obsolete.Year2024.DataBase.HeatPump.EN14511.Vitocal200AWO201()), Q_useNominal=0, use_autoCalc=false, refIneFre_constant=1, Medium_con=Media.WaterSimple(), Medium_eva=Media.WaterSimple(), mFlow_conNominal=0.5, VCon=0.04, deltaM_con=0.1, use_ConCap=false, CCon=100, GCon=5, mFlow_evaNominal=0.5, VEva=0.4, deltaM_eva=0.1, use_EvaCap=false, CEva=100, GEva=5, allowFlowReversalEva=true, TCon_start(displayUnit="K"), TEva_start(displayUnit="K"), TAmbCon_nominal=273.15, TAmbEva_nominal=288.15) annotation (Placement(transformation( extent={{-13,-16},{13,16}}, rotation=90, origin={3,-2})));
+
+3: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: FastHVAC.Components.Sinks.Vessel vessel_ev "vessel for open evaporator circuit" annotation (Placement( transformation( extent={{-11,-9},{11,9}}, rotation=180, origin={-35,57})));
+
+4: Name 'dotm_sink' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: dotm_sink. Affected line: Modelica.Blocks.Sources.Constant dotm_sink(k=1) "Sink mass flow signal" annotation (Placement(transformation(extent={{-98,-82},{-78,-62}})));
+
+5: Name 'dotm_source' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: dotm_source. Affected line: Modelica.Blocks.Sources.Constant dotm_source(k=0.106) "source mass flow signal" annotation (Placement(transformation( extent={{-5,5},{5,-5}}, rotation=180, origin={73,77})));
+
+6: Name 'T_amb_internal' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_amb. Affected line: Modelica.Blocks.Sources.Constant T_amb_internal(k=291.15) "Constant internal ambient temeprature" annotation (Placement(transformation(extent={{-7,-7},{7,7}}, rotation=-90, origin={3,33})));
+
+7: Name 'TsuSinkRamp' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Sink, Ramp. Affected line: Modelica.Blocks.Sources.Ramp TsuSinkRamp( duration=1000, startTime=1000, height=25, offset=278) "Ramp signal for the temperature input of the sink side's ideal mass flow source" annotation (Placement(transformation(extent={{-96,-34},{-76,-14}})));
+
+8: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: BaseClasses.WorkingFluid Room(m_fluid=5*1000, T0=293.15) "Volume" annotation ( Placement(transformation( extent={{-10,-10},{10,10}}, rotation=90, origin={90,-26})));
+
+9: Name 'heatFlowRateCon' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heat, Rate. Affected line: Modelica.Thermal.HeatTransfer.Sources.PrescribedHeatFlow heatFlowRateCon "Heat flow rate of the condenser" annotation (Placement(transformation( extent={{-6,6},{6,-6}}, rotation=270, origin={52,-18})));
+
+10: Name 'sine' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sine. Affected line: Modelica.Blocks.Sources.Sine sine( f=1/3600, amplitude=500, phase=3.1415926535898, offset=500) "hourly sine " annotation (Placement(transformation(extent={{66,8},{58,16}})));
+
+11: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Components.Pumps.Pump pump "source pump" annotation (Placement(transformation( extent={{10,-10},{-10,10}}, rotation=0, origin={36,20})));
+
+12: Missing documentation, Name 'booleanToReal' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: boolean, Real. Affected line: Modelica.Blocks.Math.BooleanToReal booleanToReal annotation (Placement(transformation(extent={{7,-7},{-7,7}}, rotation=270, origin={-3,-53})));
+
+13: Missing documentation, Name 'hysCooling' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Cooling. Affected line: Modelica.Blocks.Logical.Hysteresis hysCooling( pre_y_start=false, uHigh=273.15 + 17, uLow=273.15 + 14) annotation (Placement(transformation(extent={{46,-98},{34,-86}})));
+
+14: Missing documentation, Name 'booleanStep' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: boolean, Step. Affected line: Modelica.Blocks.Sources.BooleanStep booleanStep( startValue=true, startTime=15000) annotation (Placement(transformation(extent={{8,-8},{-8,8}}, rotation=0, origin={32,-54})));
+
+15: Missing documentation, Name 'hysHeating' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Heating. Affected line: Modelica.Blocks.Logical.Hysteresis hysHeating( pre_y_start=true, uLow=273.15 + 25, uHigh=273.15 + 30) annotation (Placement(transformation(extent={{46,-82},{34,-70}})));
+
+16: Missing documentation, Name 'logicalSwitch' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: logical, Switch. Affected line: Modelica.Blocks.Logical.LogicalSwitch logicalSwitch annotation (Placement(transformation(extent={{10,-78},{0,-88}})));
+
+
+AixLib/Fluid/HeatPumps/ModularReversible/BaseClasses/PartialReversibleRefrigerantMachine.mo
+1: Name 'MediumEva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Medium. Affected line: replaceable package MediumEva = Modelica.Media.Interfaces.PartialMedium "Medium on evaporator side" annotation (choicesAllMatching=true);
+
+2: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: replaceable PartialModularRefrigerantCycle refCyc constrainedby PartialModularRefrigerantCycle(final use_rev=use_rev) "Model of the refrigerant cycle" annotation (Placement(transformation( extent={{-18,-18},{18,18}}, rotation=90)));
+
+3: Name 'RefrigerantCycleInertia' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Refrigerant, Cycle, Inertia. Affected line: replaceable model RefrigerantCycleInertia = AixLib.Fluid.HeatPumps.ModularReversible.RefrigerantCycle.Inertias.NoInertia constrainedby AixLib.Fluid.HeatPumps.ModularReversible.RefrigerantCycle.Inertias.BaseClasses.PartialInertia "Inertia between the refrigerant cycle outputs and the heat exchangers." annotation (choicesAllMatching=true, Dialog(group="Inertia"));
+
+4: Name 'allowDifferentDeviceIdentifiers' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: allow, Different, Device, Identifiers. Affected line: parameter Boolean allowDifferentDeviceIdentifiers=false "if use_rev=true, device data for cooling and heating need to entered. Set allowDifferentDeviceIdentifiers=true to allow different device identifiers devIde" annotation(Dialog(tab="Advanced", enable=use_rev));
+
+5: Name 'GConOut' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: G. Affected line: parameter Modelica.Units.SI.ThermalConductance GConOut=0 "Outer thermal conductance for condenser heat loss calculations" annotation (Dialog( group="Heat Losses", tab="Condenser", enable=use_conCap));
+
+6: Name 'GConIns' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: G. Affected line: parameter Modelica.Units.SI.ThermalConductance GConIns=0 "Inner thermal conductance for condenser heat loss calculations" annotation (Dialog( group="Heat Losses", tab="Condenser", enable=use_conCap));
+
+7: Name 'GEvaOut' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: G. Affected line: parameter Modelica.Units.SI.ThermalConductance GEvaOut=0 "Outer thermal conductance for evaporator heat loss calculations" annotation ( Dialog( group="Heat Losses", tab="Evaporator", enable=use_evaCap));
+
+8: Name 'GEvaIns' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: G. Affected line: parameter Modelica.Units.SI.ThermalConductance GEvaIns=0 "Inner thermal conductance for evaporator heat loss calculations" annotation ( Dialog( group="Heat Losses", tab="Evaporator", enable=use_evaCap));
+
+9: Name 'allowFlowReversalCon' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: allow, Reversal. Affected line: parameter Boolean allowFlowReversalCon=true "= false to simplify equations, assuming, but not enforcing, no flow reversal" annotation (Dialog(group="Condenser", tab="Assumptions"));
+
+10: Name 'Q1_flow' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Q1. Affected line: Modelica.Units.SI.HeatFlowRate Q1_flow = QCon_flow "Heat transferred into the medium 1";
+
+11: Name 'Q2_flow' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Q2. Affected line: Modelica.Units.SI.HeatFlowRate Q2_flow = QEva_flow "Heat transferred into the medium 2";
+
+12: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: RefrigerantCycleInertia refCycIneCon "Inertia model for condenser side" annotation(Placement(transformation( extent={{-10,-10},{10,10}}, rotation=90, origin={0,50})));RefrigerantCycleInertia refCycIneEva "Inertia model for evaporator side" annotation (Placement(transformation( extent={{-10,-10},{10,10}}, rotation=270, origin={0,-50})));
+
+
+AixLib/Fluid/Examples/GeothermalHeatPump/BaseClasses/GeothermalHeatPumpControlledBase.mo
+1: Name 'getTStorageUpper' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Storage, Upper. Affected line: Modelica.Blocks.Sources.RealExpression getTStorageUpper(y=heatStorage.layer[ heatStorage.n].T) "Gets the temperature of upper heat storage layer" annotation (Placement(transformation(extent={{-160,58},{-140,78}})));
+
+2: Name 'getTStorageLower' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Storage, Lower. Affected line: Modelica.Blocks.Sources.RealExpression getTStorageLower(y=coldStorage.layer[1].T) "Gets the temperature of lower cold storage layer" annotation (Placement(transformation(extent={{-160,42},{-140,62}})));
+
+3: Name 'coldStorageTemperature' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: cold, Storage, Temperature. Affected line: Modelica.Blocks.Interfaces.RealOutput coldStorageTemperature( final quantity="ThermodynamicTemperature", final unit="K", displayUnit="degC", min=0, start=T_start_cold) "Temperature in the cold storage" annotation ( Placement(transformation( origin={-134,-120}, extent={{10,-10},{-10,10}}, rotation=90), iconTransformation( extent={{10,-10},{-10,10}}, rotation=90, origin={-100,-110})));
+
+4: Name 'heatStorageTemperature' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heat, Storage, Temperature. Affected line: Modelica.Blocks.Interfaces.RealOutput heatStorageTemperature( final quantity="ThermodynamicTemperature", final unit="K", displayUnit="degC", min=0, start=T_start_hot) "Temperature in the heat storage" annotation (Placement( transformation( origin={-100,-120}, extent={{10,-10},{-10,10}}, rotation=90), iconTransformation( extent={{10,-10},{-10,10}}, rotation=90, origin={-140,-110})));
+
+5: Name 'chemicalEnergyFlowRate' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: chemical, Energy, Rate. Affected line: Modelica.Blocks.Interfaces.RealOutput chemicalEnergyFlowRate(final unit="W") "Flow of primary (chemical) energy into boiler " annotation (Placement( transformation( extent={{-10,10},{10,-10}}, rotation=270, origin={-71.5,-119.5}), iconTransformation(extent={{10,-10},{-10,10}}, rotation=90, origin={-20.5,-109})));
+
+6: Name 'heatPumpPower' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heat, Pump, Power. Affected line: Modelica.Blocks.Interfaces.RealOutput heatPumpPower(final unit="W") "Electrical power of the heat pump" annotation (Placement(transformation( extent={{-10,10},{10,-10}}, rotation=270, origin={-45.5,-119.5}), iconTransformation(extent={{10,-10},{-10,10}}, rotation=90, origin={-60.5,-109})));
+
+7: Missing documentation, Name 'system' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: system. Affected line: inner Modelica.Fluid.System system annotation (Placement(transformation(extent={{140,60},{160,80}})));
+
+
+AixLib/Obsolete/YearIndependent/FastHVAC/Components/HeatGenerators/HeatPump/HeatPump.mo
+1: Name 'Medium_eva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Medium_eva. Affected line: parameter AixLib.Obsolete.YearIndependent.FastHVAC.Media.BaseClasses.MediumSimple Medium_eva= AixLib.Obsolete.YearIndependent.FastHVAC.Media.WaterSimple() "Medium at source side" annotation (Dialog(tab="Evaporator"), choicesAllMatching=true);
+
+2: Name 'use_autoCalc' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: use_auto, Calc. Affected line: parameter Boolean use_autoCalc=false "Enable automatic estimation of volumes and mass flows?" annotation(choices(checkBox=true), Dialog(descriptionLabel=true));
+
+3: Name 'Q_useNominal' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Q_use, Nominal. Affected line: parameter Modelica.Units.SI.Power Q_useNominal(start=0) "Nominal usable heat flow of the vapour compression machine (HP: Heating; Chiller: Cooling)" annotation (Dialog(enable=use_autoCalc));
+
+4: Name 'PerDataHea' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Data. Affected line: replaceable model PerDataHea = AixLib.Obsolete.Year2024.DataBase.HeatPump.PerformanceData.BaseClasses.PartialPerformanceData "Performance data of HP in heating mode" annotation (choicesAllMatching=true);
+
+5: Name 'PerDataChi' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Data. Affected line: replaceable model PerDataChi = AixLib.Obsolete.Year2024.DataBase.Chiller.PerformanceData.BaseClasses.PartialPerformanceData "Performance data of HP in chilling mode" annotation (Dialog(enable=use_revHP),choicesAllMatching=true);
+
+6: Name 'scalingFactor' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: scaling, Factor. Affected line: parameter Real scalingFactor=1 "Scaling-factor of HP";
+
+7: Name 'refIneFre_constant' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Fre_constant. Affected line: parameter Modelica.Units.SI.Frequency refIneFre_constant "Cut off frequency for inertia of refrigerant cycle" annotation (Dialog( enable=use_refIne, group="Refrigerant inertia"), Evaluate=true);
+
+8: Name 'nthOrder' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Order. Affected line: parameter Integer nthOrder=3 "Order of refrigerant cycle interia" annotation (Dialog(enable= use_refIne, group="Refrigerant inertia"));
+
+9: Name 'useBusConnectorOnly' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Connector, Only. Affected line: parameter Boolean useBusConnectorOnly = false "Set true to use bus connector for modeSet, nSet and iceFac input" annotation(choices(checkBox=true), Dialog(group="Input Connectors"));
+
+10: Name 'm_fluidCon' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: m_fluid. Affected line: parameter Modelica.Units.SI.Mass m_fluidCon=VCon_final*con.medium.rho "Mass of working fluid";
+
+11: Name 'deltaM_con' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: _con. Affected line: parameter Real deltaM_con=0.1 "Fraction of nominal mass flow rate where transition to turbulent occurs" annotation (Dialog(tab="Condenser", group="Flow resistance"));
+
+12: Name 'GCon' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: G. Affected line: parameter Modelica.Units.SI.ThermalConductance GCon "Constant thermal conductance of condenser material" annotation (Evaluate= true, Dialog( group="Heat Losses", tab="Condenser", enable=use_ConCap));
+
+13: Name 'GConIns' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: G. Affected line: parameter Modelica.Units.SI.ThermalConductance GConIns=0 "Constant thermal conductance of condenser material" annotation (Evaluate= true, Dialog( group="Heat Losses", tab="Condenser", enable=use_ConCap));
+
+14: Name 'm_fluidEva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: m_fluid. Affected line: parameter Modelica.Units.SI.Mass m_fluidEva=VEva_final*eva.medium.rho "Mass of working fluid";
+
+15: Name 'deltaM_eva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: _eva. Affected line: parameter Real deltaM_eva=0.1 "Fraction of nominal mass flow rate where transition to turbulent occurs" annotation (Dialog(tab="Evaporator", group="Flow resistance"));
+
+16: Name 'GEva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: G. Affected line: parameter Modelica.Units.SI.ThermalConductance GEva "Constant thermal conductance of Evaporator material" annotation (Evaluate= true, Dialog( group="Heat Losses", tab="Evaporator", enable=use_EvaCap));
+
+17: Name 'GEvaIns' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: G. Affected line: parameter Modelica.Units.SI.ThermalConductance GEvaIns=0 "Constant thermal conductance of Evaporator material" annotation (Evaluate= true, Dialog( group="Heat Losses", tab="Evaporator", enable=use_EvaCap));
+
+18: Name 'allowFlowReversalCon' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: allow, Reversal. Affected line: parameter Boolean allowFlowReversalCon=true "= false to simplify equations, assuming, but not enforcing, no flow reversal" annotation (Dialog(group="Condenser", tab="Assumptions"));
+
+19: Name 'transferHeat' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: transfer, Heat. Affected line: parameter Boolean transferHeat=true "If true, temperature T converges towards TAmb when no flow" annotation (Dialog(tab="Assumptions", group="Temperature sensors"),choices(checkBox=true));
+
+20: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Interfaces.EnthalpyPort_a enthalpyPort_a( m_flow(min=if allowFlowReversalCon then -Modelica.Constants.inf else 0)) "Fluid connector a1 (positive design flow direction is from port_a1 to port_b1)" annotation (Placement(transformation(extent={{-104,56},{-96,64}})));Interfaces.EnthalpyPort_b enthalpyPort_b( m_flow(max=if allowFlowReversalCon then +Modelica.Constants.inf else 0)) "Fluid connector b1 (positive design flow direction is from port_a1 to port_b1)" annotation (Placement(transformation(extent={{104,56},{96,64}})));Interfaces.EnthalpyPort_a enthalpyPort_a1( m_flow(min=if allowFlowReversalEva then -Modelica.Constants.inf else 0)) "Fluid connector a2 (positive design flow direction is from port_a2 to port_b2)" annotation (Placement(transformation(extent={{96,-64},{104,-56}})));Interfaces.EnthalpyPort_b enthalpyPort_b1( m_flow(max=if allowFlowReversalEva then +Modelica.Constants.inf else 0)) "Fluid connector b2 (positive design flow direction is from port_a2 to port_b2)" annotation (Placement(transformation(extent={{-96,-64},{-104,-56}})));BaseClasses.EvaporatorCondenserWithCapacity con( final kAOut_nominal=GCon, final m_fluid=m_fluidCon, final T_start=TCon_start, final use_cap=use_ConCap, final is_con=true, final V=VCon_final*scalingFactor, final C=CCon*scalingFactor, final kAInn=GCon + GConIns*abs(mFlow_con.dotm/mFlow_conNominal_final)^0.88, final medium=Medium_con, final m_flow_small=1E-4*abs(mFlow_conNominal_final), final m_flow_nominal=mFlow_conNominal_final) "Heat exchanger model for the condenser" annotation (Placement(transformation(extent={{-16,76},{16,108}})));BaseClasses.EvaporatorCondenserWithCapacity eva( final medium=Medium_eva, final use_cap=use_EvaCap, final kAOut_nominal=GEva, final m_fluid=m_fluidEva, final T_start=TEva_start, final m_flow_small=1E-4*abs(mFlow_evaNominal_final), final is_con=false, final V=VEva_final*scalingFactor, final C=CEva*scalingFactor, final m_flow_nominal=mFlow_evaNominal_final, final kAInn=GEva + GEvaIns*abs(mFlow_eva.dotm/mFlow_evaNominal_final)^0.88) "Heat exchanger model for the evaporator" annotation (Placement(transformation(extent={{16,-70},{-16,-102}})));
+
+21: Name 'heatFlowIneEva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heat. Affected line: Modelica.Blocks.Continuous.CriticalDamping heatFlowIneEva( final initType=initType, final normalized=true, final n=nthOrder, final f=refIneFre_constant, final y_start=yRefIne_start) if use_refIne "This n-th order block represents the inertia of the refrigerant cycle and delays the heat flow" annotation (Placement(transformation( extent={{6,6},{-6,-6}}, rotation=90, origin={-14,-52})));
+
+22: Name 'realPassThroughnSetCon' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: real, Pass, Throughn. Affected line: Modelica.Blocks.Routing.RealPassThrough realPassThroughnSetCon if not use_refIne "Use default nSet value" annotation (Placement(transformation( extent={{-6,-6},{6,6}}, rotation=90, origin={16,58})));
+
+23: Name 'heatFlowIneCon' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heat. Affected line: Modelica.Blocks.Continuous.CriticalDamping heatFlowIneCon( final initType=initType, final normalized=true, final n=nthOrder, final f=refIneFre_constant, final y_start=yRefIne_start) if use_refIne "This n-th order block represents the inertia of the refrigerant cycle and delays the heat flow" annotation (Placement(transformation( extent={{-6,-6},{6,6}}, rotation=90, origin={-16,58})));
+
+24: Name 'realPassThroughnSetEva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: real, Pass, Throughn. Affected line: Modelica.Blocks.Routing.RealPassThrough realPassThroughnSetEva if not use_refIne "Use default nSet value" annotation (Placement(transformation( extent={{6,-6},{-6,6}}, rotation=90, origin={16,-52})));
+
+25: Name 'varTempOutEva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Temp. Affected line: Modelica.Thermal.HeatTransfer.Sources.PrescribedTemperature varTempOutEva if use_EvaCap "Forces heat losses according to ambient temperature" annotation (Placement(transformation( extent={{-8,-8},{8,8}}, rotation=180, origin={68,-108})));
+
+26: Name 'varTempOutCon' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Temp. Affected line: Modelica.Thermal.HeatTransfer.Sources.PrescribedTemperature varTempOutCon if use_ConCap "Forces heat losses according to ambient temperature" annotation (Placement(transformation( extent={{-8,-8},{8,8}}, rotation=180, origin={68,110})));
+
+27: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Year2024.Controls.Interfaces.VapourCompressionMachineControlBus sigBusHP annotation (Placement(transformation(extent={{-120,-60},{-90,-26}}), iconTransformation(extent={{-108,-52},{-90,-26}})));
+
+28: Missing documentation, Name 'innerCycle' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: inner, Cycle. Affected line: AixLib.Obsolete.Year2024.Fluid.HeatPumps.BaseClasses.InnerCycle_HeatPump innerCycle( redeclare final model PerDataMainHP =PerDataHea, redeclare final model PerDataRevHP = PerDataChi, final use_rev=use_revHP, final scalingFactor=scalingFactor) annotation ( Placement(transformation( extent={{-27,-26},{27,26}}, rotation=90, origin={0,-1})));
+
+29: Name 'T_amb_eva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_amb_eva. Affected line: Modelica.Blocks.Interfaces.RealInput T_amb_eva(final unit="K", final displayUnit="degC") if use_EvaCap "Ambient temperature on the evaporator side" annotation (Placement(transformation(extent={{10,-10},{-10,10}}, rotation=0, origin={110,-100})));
+
+30: Name 'T_amb_con' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_amb_con. Affected line: Modelica.Blocks.Interfaces.RealInput T_amb_con(final unit="K", final displayUnit="degC") if use_ConCap "Ambient temperature on the condenser side" annotation (Placement(transformation(extent={{-10,10},{10,-10}}, rotation=180, origin={110,100})));
+
+31: Name 'modeSet' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: mode. Affected line: Modelica.Blocks.Interfaces.BooleanInput modeSet if not useBusConnectorOnly and use_revHP "Set value of HP mode" annotation (Placement(transformation(extent={{-132,-34},{-100,-2}})));
+
+32: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Sensors.TemperatureSensor senT_a2 "Temperature at sink inlet" annotation (Placement( transformation( extent={{10,-10},{-10,10}}, rotation=0, origin={40,-86})));Sensors.TemperatureSensor senT_b2 "Temperature at sink outlet" annotation (Placement( transformation( extent={{10,-10},{-10,10}}, rotation=0, origin={-52,-86})));Sensors.MassFlowSensor mFlow_eva "Mass flow sensor at the evaporator" annotation (Placement(transformation( origin={70,-60}, extent={{10,-10},{-10,10}}, rotation=0)));Sensors.TemperatureSensor senT_b1 "Temperature at sink outlet" annotation (Placement( transformation( extent={{-10,10},{10,-10}}, rotation=0, origin={38,92})));Sensors.TemperatureSensor senT_a1 "Temperature at sink inlet" annotation (Placement( transformation( extent={{-10,10},{10,-10}}, rotation=0, origin={-34,92})));Sensors.MassFlowSensor mFlow_con "Mass flow sensor at the evaporator" annotation (Placement(transformation( origin={-80,60}, extent={{-10,10},{10,-10}}, rotation=0)));
+
+33: Name 'autoCalc_mFlow_min' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: auto, Calc_m. Affected line: parameter Modelica.Units.SI.MassFlowRate autoCalc_mFlow_min=0.3 "Realistic mass flow minimum for simulation plausibility";
+
+34: Name 'autoCalc_Vmin' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: auto, Calc_, Vmin. Affected line: parameter Modelica.Units.SI.Volume autoCalc_Vmin=0.003 "Realistic volume minimum for simulation plausibility";
+
+35: Missing documentation, Name 'autoCalc_mFlow_eva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: auto, Calc_m, Flow_eva. Affected line: parameter Modelica.Units.SI.MassFlowRate autoCalc_mFlow_eva=if machineType then max(0.00004*Q_useNominal - 0.3177, autoCalc_mFlow_min) else max( 0.00005*Q_useNominal - 0.5662, autoCalc_mFlow_min);
+
+36: Missing documentation, Name 'autoCalc_mFlow_con' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: auto, Calc_m, Flow_con. Affected line: parameter Modelica.Units.SI.MassFlowRate autoCalc_mFlow_con=if machineType then max(0.00004*Q_useNominal - 0.6162, autoCalc_mFlow_min) else max( 0.00005*Q_useNominal + 0.3161, autoCalc_mFlow_min);
+
+37: Missing documentation, Name 'mFlow_evaNominal_final' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Flow_eva, Nominal_final. Affected line: parameter Modelica.Units.SI.MassFlowRate mFlow_evaNominal_final=if use_autoCalc then autoCalc_mFlow_eva else mFlow_evaNominal;
+
+38: Missing documentation, Name 'mFlow_conNominal_final' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Flow_con, Nominal_final. Affected line: parameter Modelica.Units.SI.MassFlowRate mFlow_conNominal_final=if use_autoCalc then autoCalc_mFlow_con else mFlow_conNominal;
+
+39: Missing documentation, Name 'autoCalc_VEva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: auto, Calc_. Affected line: parameter Modelica.Units.SI.Volume autoCalc_VEva=if machineType then max( 0.0000001*Q_useNominal - 0.0075, autoCalc_Vmin) else max(0.0000001* Q_useNominal - 0.0066, autoCalc_Vmin);
+
+40: Missing documentation, Name 'autoCalc_VCon' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: auto, Calc_. Affected line: parameter Modelica.Units.SI.Volume autoCalc_VCon=if machineType then max( 0.0000001*Q_useNominal - 0.0094, autoCalc_Vmin) else max(0.0000002* Q_useNominal - 0.0084, autoCalc_Vmin);
+
+41: Missing documentation, Name 'VEva_final' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Eva_final. Affected line: parameter Modelica.Units.SI.Volume VEva_final=if use_autoCalc then autoCalc_VEva else VEva;
+
+42: Missing documentation, Name 'VCon_final' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Con_final. Affected line: parameter Modelica.Units.SI.Volume VCon_final=if use_autoCalc then autoCalc_VCon else VCon;
+
+
+AixLib/Obsolete/Year2019/Fluid/HeatPumps/HeatPumpSimple.mo
+1: Missing documentation, Name 'Medium' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Medium. Affected line: replaceable package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater constrainedby Modelica.Media.Interfaces.PartialMedium;
+
+2: Name 'port_a_source' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: port_a_source. Affected line: Modelica.Fluid.Interfaces.FluidPort_a port_a_source(redeclare package Medium = Medium) "Heat pump inlet on the source side" annotation(Placement(transformation(extent = {{-100, 60}, {-80, 80}})));
+
+3: Name 'port_b_source' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: port_b_source. Affected line: Modelica.Fluid.Interfaces.FluidPort_b port_b_source(redeclare package Medium = Medium) "Heat pump outlet on the source side" annotation(Placement(transformation(extent = {{-100, -80}, {-80, -60}})));
+
+4: Name 'port_a_sink' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: port_a_sink. Affected line: Modelica.Fluid.Interfaces.FluidPort_a port_a_sink(redeclare package Medium = Medium) "Heat pump inlet on the sink side" annotation(Placement(transformation(extent = {{80, -80}, {100, -60}})));
+
+5: Name 'port_b_sink' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: port_b_sink. Affected line: Modelica.Fluid.Interfaces.FluidPort_b port_b_sink(redeclare package Medium = Medium) "Heat pump outlet on the sink side" annotation(Placement(transformation(extent = {{80, 60}, {100, 80}})));
+
+6: Name 'volumeEvaporator' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: volume, Evaporator. Affected line: AixLib.Fluid.MixingVolumes.MixingVolume volumeEvaporator( V=VolumeEvaporator, nPorts=2, redeclare package Medium = Medium, m_flow_nominal=0.01) "Water volume of the evaporator on the source side" annotation (Placement(transformation( extent={{-10,-10},{10,10}}, rotation=270, origin={-70,-60})));
+
+7: Name 'volumeCondenser' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: volume, Condenser. Affected line: AixLib.Fluid.MixingVolumes.MixingVolume volumeCondenser( V=VolumeCondenser, nPorts=2, redeclare package Medium = Medium, m_flow_nominal=0.01) "Water volume of the condenser on the sink side" annotation (Placement(transformation( extent={{-10,-10},{10,10}}, rotation=90, origin={70,-30})));
+
+8: Name 'temperatureSinkOut' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: temperature, Sink. Affected line: AixLib.Fluid.Sensors.TemperatureTwoPort temperatureSinkOut(redeclare package Medium = Medium, m_flow_nominal=0.01) "Temperature sensor at outlet on the sink side" annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=90, origin={80,50})));
+
+9: Name 'temperatureSourceIn' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: temperature, Source. Affected line: AixLib.Fluid.Sensors.TemperatureTwoPort temperatureSourceIn(redeclare package Medium = Medium, m_flow_nominal=0.01) "Temperature sensor at inlet on the source side" annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=270, origin={-80,36})));
+
+10: Name 'HeatFlowCondenser' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Heat, Condenser. Affected line: Modelica.Thermal.HeatTransfer.Sources.PrescribedHeatFlow HeatFlowCondenser "Heat flow on the sink side" annotation(Placement(transformation(extent={{-4,-4}, {4,4}}, origin={48,-40})));
+
+11: Name 'HeatFlowEvaporator' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Heat, Evaporator. Affected line: Modelica.Thermal.HeatTransfer.Sources.PrescribedHeatFlow HeatFlowEvaporator "Heat flow on the source side" annotation(Placement(transformation(extent={{4,-4},{ -4,4}}, origin={-46,-50})));
+
+12: Name 'PowerTable' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Power, Table. Affected line: Modelica.Blocks.Tables.CombiTable2Ds PowerTable(table=tablePower) "Calculates electric power based on temperature in source and sink" annotation (Placement(transformation(extent={{-52,20},{-32,40}})));
+
+13: Name 'HeatFlowCondenserTable' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Heat, Condenser, Table. Affected line: Modelica.Blocks.Tables.CombiTable2Ds HeatFlowCondenserTable(table= tableHeatFlowCondenser) "Calculates heat flow based on temperature in source and sink" annotation (Placement(transformation(extent={{-52,-12},{-32,8}})));
+
+14: Name 'SwitchHeatFlowCondenser' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Switch, Heat, Condenser. Affected line: Modelica.Blocks.Logical.Switch SwitchHeatFlowCondenser "Switch to deactivate heat flow when off" annotation(Placement(transformation(extent = {{14, -20}, {34, 0}})));
+
+15: Name 'constZero2' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Zero. Affected line: Modelica.Blocks.Sources.Constant constZero2(k = 0) "Zero heat flow, when heat pump off" annotation(Placement(transformation(extent = {{-26, -28}, {-6, -8}})));
+
+16: Name 'SwitchPower' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Switch, Power. Affected line: Modelica.Blocks.Logical.Switch SwitchPower "Switch to deactivate Power when off" annotation(Placement(transformation(extent = {{14, 12}, {34, 32}})));
+
+17: Name 'constZero1' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Zero. Affected line: Modelica.Blocks.Sources.Constant constZero1(k = 0) "Zero power, when heat pump off" annotation(Placement(transformation(extent = {{-26, 4}, {-6, 24}})));
+
+18: Name 'feedbackHeatFlowEvaporator' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: feedback, Heat, Evaporator. Affected line: Modelica.Blocks.Math.Feedback feedbackHeatFlowEvaporator "Calculates evaporator heat flow with total energy balance" annotation(Placement(transformation(extent = {{10, -60}, {-10, -40}})));
+
+19: Name 'Power' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Power. Affected line: Modelica.Blocks.Interfaces.RealOutput Power "Connector of Real output signal" annotation(Placement(transformation(extent = {{-10, -10}, {10, 10}}, rotation = 270, origin = {0, -90})));
+
+20: Name 'VolumeEvaporator' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Volume, Evaporator. Affected line: parameter Modelica.Units.SI.Volume VolumeEvaporator=0.01 "Volume im m3";
+
+21: Name 'VolumeCondenser' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Volume, Condenser. Affected line: parameter Modelica.Units.SI.Volume VolumeCondenser=0.01 "Volume im m3";
+
+22: Name 'tablePower' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: table, Power. Affected line: parameter Real tablePower[:, :] = fill(0.0, 0, 2) "Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1])";
+
+23: Name 'tableHeatFlowCondenser' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: table, Heat, Condenser. Affected line: parameter Real tableHeatFlowCondenser[:, :] = fill(0.0, 0, 2) "Table matrix (grid u1 = first column, grid u2 = first row; e.g., table=[0,0;0,1])";
+
+24: Missing documentation. Affected line: Modelica.Blocks.Math.Gain gain(k=-1) annotation(Placement(transformation(extent = {{-18, -60}, {-38, -40}})));
+
+
+AixLib/Obsolete/YearIndependent/FastHVAC/Components/Chiller/Chiller.mo
+1: Name 'Medium_eva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Medium_eva. Affected line: parameter AixLib.Obsolete.YearIndependent.FastHVAC.Media.BaseClasses.MediumSimple Medium_eva=AixLib.Obsolete.YearIndependent.FastHVAC.Media.WaterSimple() "Medium at source side" annotation (Dialog(tab="Evaporator"), choicesAllMatching=true);
+
+2: Name 'use_autoCalc' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: use_auto, Calc. Affected line: parameter Boolean use_autoCalc=false "Enable automatic estimation of volumes and mass flows?" annotation(choices(checkBox=true), Dialog(descriptionLabel=true));
+
+3: Name 'Q_useNominal' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Q_use, Nominal. Affected line: parameter Modelica.Units.SI.Power Q_useNominal(start=0) "Nominal usable heat flow of the vapour compression machine (HP: Heating; Chiller: Cooling)" annotation (Dialog(enable=use_autoCalc));
+
+4: Name 'PerDataMainChi' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Data, Main. Affected line: replaceable model PerDataMainChi = AixLib.Obsolete.Year2024.DataBase.Chiller.PerformanceData.BaseClasses.PartialPerformanceData "Performance data of chiller in cooling mode" annotation (Diagram(obsolete = "Obsolete model - FastHVAC is not maintained anymore but can still be used."),choicesAllMatching=true);
+
+5: Name 'PerDataRevChi' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Data. Affected line: replaceable model PerDataRevChi = AixLib.Obsolete.Year2024.DataBase.Chiller.PerformanceData.BaseClasses.PartialPerformanceData "Performance data of chiller in heating mode" annotation (Dialog(enable=use_revHP),choicesAllMatching=true);
+
+6: Name 'scalingFactor' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: scaling, Factor. Affected line: parameter Real scalingFactor=1 "Scaling-factor of chiller";
+
+7: Name 'refIneFre_constant' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Fre_constant. Affected line: parameter Modelica.Units.SI.Frequency refIneFre_constant "Cut off frequency for inertia of refrigerant cycle" annotation (Dialog( enable=use_refIne, group="Refrigerant inertia"), Evaluate=true);
+
+8: Name 'nthOrder' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Order. Affected line: parameter Integer nthOrder=3 "Order of refrigerant cycle interia" annotation (Dialog(enable= use_refIne, group="Refrigerant inertia"));
+
+9: Name 'useBusConnectorOnly' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Connector, Only. Affected line: parameter Boolean useBusConnectorOnly = false "Set true to use bus connector for modeSet, nSet and iceFac input" annotation(choices(checkBox=true), Dialog(group="Input Connectors"));
+
+10: Name 'm_fluidCon' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: m_fluid. Affected line: parameter Modelica.Units.SI.Mass m_fluidCon=VCon_final*con.medium.rho "Mass of working fluid";
+
+11: Name 'deltaM_con' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: _con. Affected line: parameter Real deltaM_con=0.1 "Fraction of nominal mass flow rate where transition to turbulent occurs" annotation (Dialog(tab="Condenser", group="Flow resistance"));
+
+12: Name 'GCon' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: G. Affected line: parameter Modelica.Units.SI.ThermalConductance GCon "Constant thermal conductance of condenser material" annotation (Evaluate= true, Dialog( group="Heat Losses", tab="Condenser", enable=use_ConCap));
+
+13: Name 'GConIns' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: G. Affected line: parameter Modelica.Units.SI.ThermalConductance GConIns=0 "Constant thermal conductance of condenser material" annotation (Evaluate= true, Dialog( group="Heat Losses", tab="Condenser", enable=use_ConCap));
+
+14: Name 'm_fluidEva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: m_fluid. Affected line: parameter Modelica.Units.SI.Mass m_fluidEva=VEva_final*eva.medium.rho "Mass of working fluid";
+
+15: Name 'deltaM_eva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: _eva. Affected line: parameter Real deltaM_eva=0.1 "Fraction of nominal mass flow rate where transition to turbulent occurs" annotation (Dialog(tab="Evaporator", group="Flow resistance"));
+
+16: Name 'GEva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: G. Affected line: parameter Modelica.Units.SI.ThermalConductance GEva "Constant thermal conductance of Evaporator material" annotation (Evaluate= true, Dialog( group="Heat Losses", tab="Evaporator", enable=use_EvaCap));
+
+17: Name 'GEvaIns' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: G. Affected line: parameter Modelica.Units.SI.ThermalConductance GEvaIns=0 "Constant thermal conductance of Evaporator material" annotation (Evaluate= true, Dialog( group="Heat Losses", tab="Evaporator", enable=use_EvaCap));
+
+18: Name 'allowFlowReversalCon' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: allow, Reversal. Affected line: parameter Boolean allowFlowReversalCon=true "= false to simplify equations, assuming, but not enforcing, no flow reversal" annotation (Dialog(group="Condenser", tab="Assumptions"));
+
+19: Name 'transferHeat' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: transfer, Heat. Affected line: parameter Boolean transferHeat=true "If true, temperature T converges towards TAmb when no flow" annotation (Dialog(tab="Assumptions", group="Temperature sensors"),choices(checkBox=true));
+
+20: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Interfaces.EnthalpyPort_a enthalpyPort_a( m_flow(min=if allowFlowReversalCon then -Modelica.Constants.inf else 0)) "Fluid connector a1 (positive design flow direction is from port_a1 to port_b1)" annotation (Placement(transformation(extent={{-104,56},{-96,64}})));Interfaces.EnthalpyPort_b enthalpyPort_b( m_flow(max=if allowFlowReversalCon then +Modelica.Constants.inf else 0)) "Fluid connector b1 (positive design flow direction is from port_a1 to port_b1)" annotation (Placement(transformation(extent={{104,56},{96,64}})));Interfaces.EnthalpyPort_a enthalpyPort_a1( m_flow(min=if allowFlowReversalEva then -Modelica.Constants.inf else 0)) "Fluid connector a2 (positive design flow direction is from port_a2 to port_b2)" annotation (Placement(transformation(extent={{96,-64},{104,-56}})));Interfaces.EnthalpyPort_b enthalpyPort_b1( m_flow(max=if allowFlowReversalEva then +Modelica.Constants.inf else 0)) "Fluid connector b2 (positive design flow direction is from port_a2 to port_b2)" annotation (Placement(transformation(extent={{-96,-64},{-104,-56}})));
+
+21: Name 'heatFlowIneEva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heat. Affected line: Modelica.Blocks.Continuous.CriticalDamping heatFlowIneEva( final initType=initType, final normalized=true, final n=nthOrder, final f=refIneFre_constant, final y_start=yRefIne_start) if use_refIne "This n-th order block represents the inertia of the refrigerant cycle and delays the heat flow" annotation (Placement(transformation( extent={{6,6},{-6,-6}}, rotation=90, origin={-14,-52})));
+
+22: Name 'realPassThroughnSetCon' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: real, Pass, Throughn. Affected line: Modelica.Blocks.Routing.RealPassThrough realPassThroughnSetCon if not use_refIne "Use default nSet value" annotation (Placement(transformation( extent={{-6,-6},{6,6}}, rotation=90, origin={16,58})));
+
+23: Name 'heatFlowIneCon' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heat. Affected line: Modelica.Blocks.Continuous.CriticalDamping heatFlowIneCon( final initType=initType, final normalized=true, final n=nthOrder, final f=refIneFre_constant, final y_start=yRefIne_start) if use_refIne "This n-th order block represents the inertia of the refrigerant cycle and delays the heat flow" annotation (Placement(transformation( extent={{-6,-6},{6,6}}, rotation=90, origin={-16,58})));
+
+24: Name 'realPassThroughnSetEva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: real, Pass, Throughn. Affected line: Modelica.Blocks.Routing.RealPassThrough realPassThroughnSetEva if not use_refIne "Use default nSet value" annotation (Placement(transformation( extent={{6,-6},{-6,6}}, rotation=90, origin={16,-52})));
+
+25: Name 'varTempOutEva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Temp. Affected line: Modelica.Thermal.HeatTransfer.Sources.PrescribedTemperature varTempOutEva if use_EvaCap "Forces heat losses according to ambient temperature" annotation (Placement(transformation( extent={{-8,-8},{8,8}}, rotation=180, origin={68,-108})));
+
+26: Name 'varTempOutCon' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Temp. Affected line: Modelica.Thermal.HeatTransfer.Sources.PrescribedTemperature varTempOutCon if use_ConCap "Forces heat losses according to ambient temperature" annotation (Placement(transformation( extent={{-8,-8},{8,8}}, rotation=180, origin={68,110})));
+
+27: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Year2024.Controls.Interfaces.VapourCompressionMachineControlBus sigBus annotation (Placement( transformation(extent={{-120,-60},{-90,-26}}), iconTransformation( extent={{-108,-52},{-90,-26}})));
+
+28: Missing documentation, Name 'innerCycle' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: inner, Cycle. Affected line: AixLib.Obsolete.Year2024.Fluid.Chillers.BaseClasses.InnerCycle_Chiller innerCycle( redeclare final model PerDataMainChi = PerDataMainChi, redeclare final model PerDataRevChi = PerDataRevChi, final use_rev=use_revChi, final scalingFactor=scalingFactor) annotation (Placement(transformation( extent={{-27,-26},{27,26}}, rotation=90, origin={0,-1})));
+
+29: Name 'T_amb_eva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_amb_eva. Affected line: Modelica.Blocks.Interfaces.RealInput T_amb_eva(final unit="K", final displayUnit="degC") if use_EvaCap "Ambient temperature on the evaporator side" annotation (Placement(transformation(extent={{10,-10},{-10,10}}, rotation=0, origin={110,-100})));
+
+30: Name 'T_amb_con' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_amb_con. Affected line: Modelica.Blocks.Interfaces.RealInput T_amb_con(final unit="K", final displayUnit="degC") if use_ConCap "Ambient temperature on the condenser side" annotation (Placement(transformation(extent={{-10,10},{10,-10}}, rotation=180, origin={110,100})));
+
+31: Name 'modeSet' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: mode. Affected line: Modelica.Blocks.Interfaces.BooleanInput modeSet if not useBusConnectorOnly "Set value of HP mode" annotation (Placement(transformation(extent={{-132,-34},{-100,-2}})));
+
+32: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Sensors.TemperatureSensor senT_a2 "Temperature at sink inlet" annotation (Placement( transformation( extent={{10,-10},{-10,10}}, rotation=0, origin={40,-86})));Sensors.TemperatureSensor senT_b2 "Temperature at sink outlet" annotation (Placement( transformation( extent={{10,-10},{-10,10}}, rotation=0, origin={-52,-86})));Sensors.MassFlowSensor mFlow_eva "Mass flow sensor at the evaporator" annotation (Placement(transformation( origin={70,-60}, extent={{10,-10},{-10,10}}, rotation=0)));Sensors.TemperatureSensor senT_b1 "Temperature at sink outlet" annotation (Placement( transformation( extent={{-10,10},{10,-10}}, rotation=0, origin={38,92})));Sensors.TemperatureSensor senT_a1 "Temperature at sink inlet" annotation (Placement( transformation( extent={{-10,10},{10,-10}}, rotation=0, origin={-34,92})));Sensors.MassFlowSensor mFlow_con "Mass flow sensor at the evaporator" annotation (Placement(transformation( origin={-80,60}, extent={{-10,10},{10,-10}}, rotation=0)));
+
+33: Name 'autoCalc_mFlow_min' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: auto, Calc_m. Affected line: parameter Modelica.Units.SI.MassFlowRate autoCalc_mFlow_min=0.3 "Realistic mass flow minimum for simulation plausibility";
+
+34: Name 'autoCalc_Vmin' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: auto, Calc_, Vmin. Affected line: parameter Modelica.Units.SI.Volume autoCalc_Vmin=0.003 "Realistic volume minimum for simulation plausibility";
+
+35: Missing documentation, Name 'autoCalc_mFlow_eva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: auto, Calc_m, Flow_eva. Affected line: parameter Modelica.Units.SI.MassFlowRate autoCalc_mFlow_eva=if machineType then max(0.00004*Q_useNominal - 0.3177, autoCalc_mFlow_min) else max( 0.00005*Q_useNominal - 0.5662, autoCalc_mFlow_min);
+
+36: Missing documentation, Name 'autoCalc_mFlow_con' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: auto, Calc_m, Flow_con. Affected line: parameter Modelica.Units.SI.MassFlowRate autoCalc_mFlow_con=if machineType then max(0.00004*Q_useNominal - 0.6162, autoCalc_mFlow_min) else max( 0.00005*Q_useNominal + 0.3161, autoCalc_mFlow_min);
+
+37: Missing documentation, Name 'mFlow_evaNominal_final' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Flow_eva, Nominal_final. Affected line: parameter Modelica.Units.SI.MassFlowRate mFlow_evaNominal_final=if use_autoCalc then autoCalc_mFlow_eva else mFlow_evaNominal;
+
+38: Missing documentation, Name 'mFlow_conNominal_final' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Flow_con, Nominal_final. Affected line: parameter Modelica.Units.SI.MassFlowRate mFlow_conNominal_final=if use_autoCalc then autoCalc_mFlow_con else mFlow_conNominal;
+
+39: Missing documentation, Name 'autoCalc_VEva' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: auto, Calc_. Affected line: parameter Modelica.Units.SI.Volume autoCalc_VEva=if machineType then max( 0.0000001*Q_useNominal - 0.0075, autoCalc_Vmin) else max(0.0000001* Q_useNominal - 0.0066, autoCalc_Vmin);
+
+40: Missing documentation, Name 'autoCalc_VCon' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: auto, Calc_. Affected line: parameter Modelica.Units.SI.Volume autoCalc_VCon=if machineType then max( 0.0000001*Q_useNominal - 0.0094, autoCalc_Vmin) else max(0.0000002* Q_useNominal - 0.0084, autoCalc_Vmin);
+
+41: Missing documentation, Name 'VEva_final' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Eva_final. Affected line: parameter Modelica.Units.SI.Volume VEva_final=if use_autoCalc then autoCalc_VEva else VEva;
+
+42: Missing documentation, Name 'VCon_final' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Con_final. Affected line: parameter Modelica.Units.SI.Volume VCon_final=if use_autoCalc then autoCalc_VCon else VCon;
\ No newline at end of file
diff --git a/docs/correct_HTML_1520_newHPModels/regression/Airflow/comparison-dymola.log b/docs/correct_HTML_1520_newHPModels/regression/Airflow/comparison-dymola.log
new file mode 100644
index 0000000000..d3b17117dd
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Airflow/comparison-dymola.log
@@ -0,0 +1,608 @@
+[
+ {
+ "comparison": {
+ "file_name": "AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSimpleOpening.mat",
+ "funnel_dirs": [
+ "funnel_comp/AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSimpleOpening.mat_TRoomSet.y",
+ "funnel_comp/AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSimpleOpening.mat_TAmbSet.y",
+ "funnel_comp/AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSimpleOpening.mat_winSpe10Set.y",
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Airflow/funnel_comp/AixLib.Airflow.AirHandlingUnit.Examples.AHU.mat_ahu.T_oda/upperBound.csv b/docs/correct_HTML_1520_newHPModels/regression/Airflow/funnel_comp/AixLib.Airflow.AirHandlingUnit.Examples.AHU.mat_ahu.T_oda/upperBound.csv
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+64.799000,9.609594
+66.599000,13.213203
+68.399000,16.816796
+70.199000,19.619594
+70.201000,19.619594
+73.801000,12.412406
+75.601000,8.808797
+77.401000,5.205203
+79.201000,1.601594
+81.001000,0.001000
+98.999000,0.001000
+100.799000,1.601594
+102.599000,5.205203
+104.399000,8.808797
+106.199000,12.412406
+109.799000,19.619594
+109.801000,19.619594
+111.601000,16.816796
+113.401000,13.213203
+115.201000,9.609594
+117.001000,6.006000
+118.801000,2.402406
+120.600000,0.602002
+122.399000,2.402399
+124.199000,4.204203
+129.599000,9.609594
+129.601000,9.609594
+131.401000,8.608594
+135.001000,5.005000
+136.801000,3.203203
+138.601000,1.401406
+140.400143,0.201575
+142.199000,1.101102
+143.999000,2.002000
+145.799000,2.902899
+147.599000,3.803797
+149.399000,4.704703
+149.401000,4.704703
+151.201000,4.404399
+154.801000,2.602601
+156.601000,1.701703
+158.401000,0.800997
+160.201000,0.001000
+180.001000,0.001000
diff --git a/docs/correct_HTML_1520_newHPModels/regression/Airflow/simulator-dymola.log b/docs/correct_HTML_1520_newHPModels/regression/Airflow/simulator-dymola.log
new file mode 100644
index 0000000000..45cf8be1de
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Airflow/simulator-dymola.log
@@ -0,0 +1,241 @@
+ = true
+
+
+rCheck = checkModel("AixLib.Airflow.WindowVentilation.Examples.OpeningArea");
+Check of AixLib.Airflow.WindowVentilation.Examples.OpeningArea:
+The model has the same number of unknowns and equations: 282
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 282
+scalar unknowns and
+ 281+(if not opnSasSdHunInGeo.use_opnWidth_in then 1 else 0)+(if not opnSasSdHunInPrj.use_opnWidth_in then 1 else 0)+(if not opnSasSdHunInEqv.use_opnWidth_in then 1 else 0)+(if not opnSasSdHunInEff.use_opnWidth_in then 1 else 0)+(if not opnSasSdHunOutGeo.use_opnWidth_in then 1 else 0)+(if not opnSasBtmHunInGeo.use_opnWidth_in then 1 else 0)+(if not opnSasBtmHunInPrj.use_opnWidth_in then 1 else 0)+(if not opnSasBtmHunInEqv.use_opnWidth_in then 1 else 0)+(if not opnSasBtmHunInEff.use_opnWidth_in then 1 else 0)+(if not opnSasTopHunOutPrj.use_opnWidth_in then 1 else 0)+(if not opnSasPivVerGeo.use_opnWidth_in then 1 else 0)+(if not opnSasPivVerPrj.use_opnWidth_in then 1 else 0)+(if not opnSasPivVerEqv.use_opnWidth_in then 1 else 0)+(if not opnSasPivVerEff.use_opnWidth_in then 1 else 0)+(if not opnSasPivHorGeo.use_opnWidth_in then 1 else 0)+(if not opnSasPivHorPrj.use_opnWidth_in then 1 else 0)+(if not opnSasPivHorEqv.use_opnWidth_in then 1 else 0)+(if not opnSasPivHorEff.use_opnWidth_in then 1 else 0)+(if not opnSasPivHorEffPre.use_opnWidth_in then 1 else 0)+(if not opnSasSldVerGeo.use_opnWidth_in then 1 else 0)+(if not opnSasSldHorGeo.use_opnWidth_in then 1 else 0)+(if not opnSasBtmHunInDIN16798.use_opnWidth_in then 1 else 0) +(if not opnSasSdHunInDIN4108.use_opnWidth_in then 1 else 0)+(if not opnSasBtmHunInDIN4108.use_opnWidth_in then 1 else 0)+(if not opnSasPivHorDIN4108.use_opnWidth_in then 1 else 0)+(if not opnSasBtmHunInHall.use_opnWidth_in then 1 else 0)+( if not opnSasBtmHunInVDI2078.use_opnWidth_in then 1 else 0)+(if not opnSasAngBtmHunInGeo.use_opnWidth_in then 1 else 0)
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 282
+Check of AixLib.Airflow.WindowVentilation.Examples.OpeningArea successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Airflow/WindowVentilation/Examples/OpeningArea.mos\",", "AixLib.Airflow.WindowVentilation.Examples.OpeningArea.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Airflow.WindowVentilation.Examples.OpeningArea\",", "AixLib.Airflow.WindowVentilation.Examples.OpeningArea.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Airflow.WindowVentilation.Examples.OpeningArea.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Airflow.WindowVentilation.Examples.OpeningArea\\\");\",", "AixLib.Airflow.WindowVentilation.Examples.OpeningArea.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Airflow.WindowVentilation.Examples.OpeningArea.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Airflow.WindowVentilation.Examples.OpeningArea.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Airflow/WindowVentilation/Examples/OpeningArea.mos");
+simulateModel("AixLib.Airflow.WindowVentilation.Examples.OpeningArea", startTime=0, stopTime=60, outputInterval=1, method="dassl", tolerance=1e-6, resultFile="AixLib.Airflow.WindowVentilation.Examples.OpeningArea");
+Translation of AixLib.Airflow.WindowVentilation.Examples.OpeningArea:
+The DAE has 282 scalar unknowns and 282 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 36
+ Variables: 549
+ Parameters: 267 (267 scalars)
+ Unknowns: 282 (282 scalars)
+ Equations: 247
+ Nontrivial: 246
+Translated Model
+ Constants: 63 scalars
+ Free parameters: 66 scalars
+ Parameter depending: 213 scalars
+ Time-varying variables: 144 scalars
+ Alias variables: 63 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: { }
+ Sizes after manipulation of the linear systems: { }
+ Sizes of nonlinear systems of equations: { }
+ Sizes after manipulation of the nonlinear systems: { }
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Airflow.WindowVentilation.Examples.OpeningArea.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSimpleOpening");
+Check of AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSimpleOpening:
+The model has the same number of unknowns and equations: 177
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 177
+scalar unknowns and
+ 175+(if not vdi2078_1.use_cofSunSha_in then 1 else 0)+(if not vdi2078_2.use_cofSunSha_in then 1 else 0)+(if not vdi2078_3.use_cofSunSha_in then 1 else 0)
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 177
+Check of AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSimpleOpening successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Airflow/WindowVentilation/Examples/VentilationFlowRateSimpleOpening.mos\",", "AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSimpleOpening.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSimpleOpening\",", "AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSimpleOpening.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSimpleOpening.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSimpleOpening\\\");\",", "AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSimpleOpening.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSimpleOpening.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSimpleOpening.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Airflow/WindowVentilation/Examples/VentilationFlowRateSimpleOpening.mos");
+simulateModel("AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSimpleOpening", startTime=0, stopTime=180, outputInterval=0.1, method="dassl", tolerance=1e-6, resultFile="AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSimpleOpening");
+Translation of AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSimpleOpening:
+The DAE has 177 scalar unknowns and 177 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 31
+ Variables: 323
+ Parameters: 146 (177 scalars)
+ Unknowns: 177 (177 scalars)
+ Equations: 209
+ Nontrivial: 186
+Translated Model
+ Constants: 74 scalars
+ Free parameters: 65 scalars
+ Parameter depending: 72 scalars
+ Time-varying variables: 98 scalars
+ Alias variables: 45 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: {2}
+ Sizes after manipulation of the linear systems: {0}
+ Sizes of nonlinear systems of equations: { }
+ Sizes after manipulation of the nonlinear systems: { }
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSimpleOpening.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSashOpening");
+Check of AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSashOpening:
+The model has the same number of unknowns and equations: 319
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 319
+scalar unknowns and
+ 315+(if not warrenParkins.openingArea.use_opnWidth_in then 1 else 0)+(if not gidsPhaff.openingArea.use_opnWidth_in then 1 else 0)+(if not larsenHeiselberg.openingArea.use_opnWidth_in then 1 else 0)+(if not caciolo.openingArea.use_opnWidth_in then 1 else 0)+( if not tang.openingArea.use_opnWidth_in then 1 else 0)+(if not vdi2078_1.openingArea.use_opnWidth_in then 1 else 0)+(if not vdi2078_1.use_cofSunSha_in then 1 else 0)+(if not vdi2078_2.openingArea.use_opnWidth_in then 1 else 0)+ (if not vdi2078_2.use_cofSunSha_in then 1 else 0)+(if not vdi2078_3.openingArea.use_opnWidth_in then 1 else 0)+(if not vdi2078_3.use_cofSunSha_in then 1 else 0)+(if not din16798_1.openingArea.use_opnWidth_in then 1 else 0)+(if not din4108_1.openingArea.use_opnWidth_in then 1 else 0)+(if not ashrae.openingArea.use_opnWidth_in then 1 else 0)+(if not maas.openingArea.use_opnWidth_in then 1 else 0)+(if not hall.openingArea.use_opnWidth_in then 1 else 0)+(if not jiang.openingArea.use_opnWidth_in then 1 else 0)
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 319
+Check of AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSashOpening successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Airflow/WindowVentilation/Examples/VentilationFlowRateSashOpening.mos\",", "AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSashOpening.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSashOpening\",", "AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSashOpening.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSashOpening.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSashOpening\\\");\",", "AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSashOpening.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSashOpening.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSashOpening.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Airflow/WindowVentilation/Examples/VentilationFlowRateSashOpening.mos");
+simulateModel("AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSashOpening", startTime=0, stopTime=180, outputInterval=0.1, method="dassl", tolerance=1e-6, resultFile="AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSashOpening");
+Translation of AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSashOpening:
+The DAE has 319 scalar unknowns and 319 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 40
+ Variables: 551
+ Parameters: 232 (263 scalars)
+ Unknowns: 319 (319 scalars)
+ Equations: 326
+ Nontrivial: 306
+Translated Model
+ Constants: 81 scalars
+ Free parameters: 107 scalars
+ Parameter depending: 134 scalars
+ Time-varying variables: 176 scalars
+ Alias variables: 84 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: {2}
+ Sizes after manipulation of the linear systems: {0}
+ Sizes of nonlinear systems of equations: { }
+ Sizes after manipulation of the nonlinear systems: { }
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Airflow.WindowVentilation.Examples.VentilationFlowRateSashOpening.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Airflow.AirHandlingUnit.Examples.AHU");
+Check of AixLib.Airflow.AirHandlingUnit.Examples.AHU:
+The model has the same number of unknowns and equations: 175
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 157+2*ahu.sample.n
+scalar unknowns and
+ 165+(if not ahu.use_Vflow_in_extractAir then 1 else 0)+ahu.sample.n
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 175
+Check of AixLib.Airflow.AirHandlingUnit.Examples.AHU successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Airflow/AirHandlingUnit/Examples/AHU.mos\",", "AixLib.Airflow.AirHandlingUnit.Examples.AHU.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Airflow.AirHandlingUnit.Examples.AHU\",", "AixLib.Airflow.AirHandlingUnit.Examples.AHU.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Airflow.AirHandlingUnit.Examples.AHU.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Airflow.AirHandlingUnit.Examples.AHU\\\");\",", "AixLib.Airflow.AirHandlingUnit.Examples.AHU.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Airflow.AirHandlingUnit.Examples.AHU.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Airflow.AirHandlingUnit.Examples.AHU.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Airflow/AirHandlingUnit/Examples/AHU.mos");
+simulateModel("AixLib.Airflow.AirHandlingUnit.Examples.AHU", stopTime=86400, outputInterval=60, method="lsodar", tolerance=1e-6, resultFile="AixLib.Airflow.AirHandlingUnit.Examples.AHU");
+Translation of AixLib.Airflow.AirHandlingUnit.Examples.AHU:
+The DAE has 175 scalar unknowns and 175 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 27
+ Variables: 206
+ Constants: 8 (8 scalars)
+ Parameters: 40 (40 scalars)
+ Unknowns: 156 (220 scalars)
+ Equations: 187
+ Nontrivial: 140
+Translated Model
+ Constants: 16 scalars
+ Free parameters: 30 scalars
+ Parameter depending: 13 scalars
+ Outputs: 3 scalars
+ Time-varying variables: 184 scalars
+ Alias variables: 25 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: { }
+ Sizes after manipulation of the linear systems: { }
+ Sizes of nonlinear systems of equations: {6, 6, 1}
+ Sizes after manipulation of the nonlinear systems: {1, 1, 0}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Finished
+ = true
+
+
+
+
+
+
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Airflow.AirHandlingUnit.Examples.AHU.translation.log");
\ No newline at end of file
diff --git a/docs/correct_HTML_1520_newHPModels/regression/Airflow/unitTests-dymola.log b/docs/correct_HTML_1520_newHPModels/regression/Airflow/unitTests-dymola.log
new file mode 100644
index 0000000000..9613672d63
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Airflow/unitTests-dymola.log
@@ -0,0 +1,10 @@
+Regression tests are only run for the following package:
+ AixLib.Airflow
+Comparison files output by funnel are stored in the directory 'funnel_comp' of size 0.6 MB.
+Run 'python -c "import buildingspy.development.regressiontest as t; t.Tester(tool=\"dymola\").report()"'
+to access a summary of the comparison results.
+
+Script that runs unit tests had 0 warnings and 0 errors.
+
+Unit tests completed successfully.
+
diff --git a/docs/correct_HTML_1520_newHPModels/regression/Controls/comparison-dymola.log b/docs/correct_HTML_1520_newHPModels/regression/Controls/comparison-dymola.log
new file mode 100644
index 0000000000..d0e9474186
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Controls/comparison-dymola.log
@@ -0,0 +1,83 @@
+[
+ {
+ "comparison": {
+ "file_name": "AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime.mat",
+ "funnel_dirs": [
+ "funnel_comp/AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime.mat_occSchDay.occupied",
+ "funnel_comp/AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime.mat_occSchDay1.occupied",
+ "funnel_comp/AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime.mat_occSchDay2.occupied",
+ "funnel_comp/AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime.mat_occSchDay.tNexNonOcc",
+ "funnel_comp/AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime.mat_occSchDay.tNexOcc",
+ "funnel_comp/AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime.mat_occSchDay1.tNexNonOcc",
+ "funnel_comp/AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime.mat_occSchDay1.tNexOcc",
+ "funnel_comp/AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime.mat_occSchDay2.tNexNonOcc",
+ "funnel_comp/AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime.mat_occSchDay2.tNexOcc"
+ ],
+ "success_rate": 1.0,
+ "t_err_max": [
+ -112320.0,
+ -112320.0,
+ -112320.0,
+ -112320.0,
+ -112320.0,
+ -112320.0,
+ -112320.0,
+ -112320.0,
+ -112320.0
+ ],
+ "test_passed": [
+ 1,
+ 1,
+ 1,
+ 1,
+ 1,
+ 1,
+ 1,
+ 1,
+ 1
+ ],
+ "var_groups": [
+ 0,
+ 1,
+ 2,
+ 3,
+ 3,
+ 4,
+ 4,
+ 5,
+ 5
+ ],
+ "variables": [
+ "occSchDay.occupied",
+ "occSchDay1.occupied",
+ "occSchDay2.occupied",
+ "occSchDay.tNexNonOcc",
+ "occSchDay.tNexOcc",
+ "occSchDay1.tNexNonOcc",
+ "occSchDay1.tNexOcc",
+ "occSchDay2.tNexNonOcc",
+ "occSchDay2.tNexOcc"
+ ],
+ "warnings": [
+ null,
+ null,
+ null,
+ null,
+ null,
+ null,
+ null,
+ null,
+ null
+ ]
+ },
+ "model": "AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime",
+ "simulation": {
+ "elapsed_time": 0.00764489,
+ "final_time": 207360,
+ "jacobians": 24,
+ "start_time": -112320,
+ "state_events": 0,
+ "success": true
+ }
+ }
+]
diff --git a/docs/correct_HTML_1520_newHPModels/regression/Controls/funnel_comp/AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime.mat_occSchDay.occupied/errors.csv b/docs/correct_HTML_1520_newHPModels/regression/Controls/funnel_comp/AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime.mat_occSchDay.occupied/errors.csv
new file mode 100644
index 0000000000..d6a61d3184
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Controls/funnel_comp/AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime.mat_occSchDay.occupied/errors.csv
@@ -0,0 +1,102 @@
+x,y
+-112320.000000,0.000000
+-109123.200000,0.000000
+-105926.400000,0.000000
+-102729.600000,0.000000
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Controls/simulator-dymola.log b/docs/correct_HTML_1520_newHPModels/regression/Controls/simulator-dymola.log
new file mode 100644
index 0000000000..004be3fac3
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Controls/simulator-dymola.log
@@ -0,0 +1,49 @@
+ = true
+
+
+rCheck = checkModel("AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime");
+Check of AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime:
+The model has the same number of unknowns and equations: 18
+Check of AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Controls/SetPoints/Validation/OccupancyScheduleNegativeStartTime.mos\",", "AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime\",", "AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime\\\");\",", "AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Controls/SetPoints/Validation/OccupancyScheduleNegativeStartTime.mos");
+simulateModel("AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime", startTime=-112320, stopTime=207360, method="Cvode", tolerance=1e-06, resultFile="AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime");
+Translation of AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime:
+The DAE has 18 scalar unknowns and 18 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 4
+ Variables: 30
+ Parameters: 12 (17 scalars)
+ Unknowns: 18 (18 scalars)
+ Equations: 9
+ Nontrivial: 9
+Translated Model
+ Constants: 3 scalars
+ Free parameters: 14 scalars
+ Time-varying variables: 18 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: { }
+ Sizes after manipulation of the linear systems: { }
+ Sizes of nonlinear systems of equations: { }
+ Sizes after manipulation of the nonlinear systems: { }
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Controls.SetPoints.Validation.OccupancyScheduleNegativeStartTime.translation.log");
\ No newline at end of file
diff --git a/docs/correct_HTML_1520_newHPModels/regression/Controls/unitTests-dymola.log b/docs/correct_HTML_1520_newHPModels/regression/Controls/unitTests-dymola.log
new file mode 100644
index 0000000000..ab71597f9f
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Controls/unitTests-dymola.log
@@ -0,0 +1,10 @@
+Regression tests are only run for the following package:
+ AixLib.Controls
+Comparison files output by funnel are stored in the directory 'funnel_comp' of size 0.1 MB.
+Run 'python -c "import buildingspy.development.regressiontest as t; t.Tester(tool=\"dymola\").report()"'
+to access a summary of the comparison results.
+
+Script that runs unit tests had 0 warnings and 0 errors.
+
+Unit tests completed successfully.
+
diff --git a/docs/correct_HTML_1520_newHPModels/regression/Electrical/comparison-dymola.log b/docs/correct_HTML_1520_newHPModels/regression/Electrical/comparison-dymola.log
new file mode 100644
index 0000000000..341638c30f
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Electrical/comparison-dymola.log
@@ -0,0 +1,74 @@
+[
+ {
+ "comparison": {
+ "file_name": "AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.mat",
+ "funnel_dirs": [
+ "funnel_comp/AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.mat_DCOutputPower",
+ "funnel_comp/AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.mat_DCOutputPower_Measured"
+ ],
+ "success_rate": 1.0,
+ "t_err_max": [
+ 28684800.0,
+ 28684800.0
+ ],
+ "test_passed": [
+ 1,
+ 1
+ ],
+ "var_groups": [
+ 0,
+ 0
+ ],
+ "variables": [
+ "DCOutputPower",
+ "DCOutputPower_Measured"
+ ],
+ "warnings": [
+ null,
+ null
+ ]
+ },
+ "model": "AixLib.Electrical.PVSystem.Validation.ValidationPVSystem",
+ "simulation": {
+ "elapsed_time": 0.0173,
+ "final_time": 28771200.0,
+ "jacobians": 940,
+ "start_time": 28684800.0,
+ "state_events": 81,
+ "success": true
+ }
+ },
+ {
+ "comparison": {
+ "file_name": "AixLib.Electrical.PVSystem.Examples.ExamplePVSystem.mat",
+ "funnel_dirs": [
+ "funnel_comp/AixLib.Electrical.PVSystem.Examples.ExamplePVSystem.mat_DCOutputPower"
+ ],
+ "success_rate": 1.0,
+ "t_err_max": [
+ 0.0
+ ],
+ "test_passed": [
+ 1
+ ],
+ "var_groups": [
+ 0
+ ],
+ "variables": [
+ "DCOutputPower"
+ ],
+ "warnings": [
+ null
+ ]
+ },
+ "model": "AixLib.Electrical.PVSystem.Examples.ExamplePVSystem",
+ "simulation": {
+ "elapsed_time": 1,
+ "final_time": 31536000.0,
+ "jacobians": 23122,
+ "start_time": 0,
+ "state_events": 4856,
+ "success": true
+ }
+ }
+]
diff --git a/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Examples.ExamplePVSystem.mat_DCOutputPower/errors.csv b/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Examples.ExamplePVSystem.mat_DCOutputPower/errors.csv
new file mode 100644
index 0000000000..6f6f206b86
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Examples.ExamplePVSystem.mat_DCOutputPower/errors.csv
@@ -0,0 +1,102 @@
+x,y
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Examples.ExamplePVSystem.mat_DCOutputPower/lowerBound.csv b/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Examples.ExamplePVSystem.mat_DCOutputPower/lowerBound.csv
new file mode 100644
index 0000000000..b390cfc090
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Examples.ExamplePVSystem.mat_DCOutputPower/lowerBound.csv
@@ -0,0 +1,120 @@
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Examples.ExamplePVSystem.mat_DCOutputPower/reference.csv b/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Examples.ExamplePVSystem.mat_DCOutputPower/reference.csv
new file mode 100644
index 0000000000..491994bf25
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Examples.ExamplePVSystem.mat_DCOutputPower/reference.csv
@@ -0,0 +1,102 @@
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Examples.ExamplePVSystem.mat_DCOutputPower/test.csv b/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Examples.ExamplePVSystem.mat_DCOutputPower/test.csv
new file mode 100644
index 0000000000..491994bf25
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Examples.ExamplePVSystem.mat_DCOutputPower/test.csv
@@ -0,0 +1,102 @@
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.mat_DCOutputPower/upperBound.csv b/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.mat_DCOutputPower/upperBound.csv
new file mode 100644
index 0000000000..90e998cdd8
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+++ b/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.mat_DCOutputPower/upperBound.csv
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.mat_DCOutputPower_Measured/errors.csv b/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.mat_DCOutputPower_Measured/errors.csv
new file mode 100644
index 0000000000..f90c451d71
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.mat_DCOutputPower_Measured/lowerBound.csv b/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.mat_DCOutputPower_Measured/lowerBound.csv
new file mode 100644
index 0000000000..64d76fdb75
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.mat_DCOutputPower_Measured/lowerBound.csv
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.mat_DCOutputPower_Measured/reference.csv b/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.mat_DCOutputPower_Measured/reference.csv
new file mode 100644
index 0000000000..7f07ab60b4
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.mat_DCOutputPower_Measured/reference.csv
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.mat_DCOutputPower_Measured/test.csv b/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.mat_DCOutputPower_Measured/test.csv
new file mode 100644
index 0000000000..7f07ab60b4
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.mat_DCOutputPower_Measured/test.csv
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.mat_DCOutputPower_Measured/upperBound.csv b/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.mat_DCOutputPower_Measured/upperBound.csv
new file mode 100644
index 0000000000..2a7937adb3
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Electrical/funnel_comp/AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.mat_DCOutputPower_Measured/upperBound.csv
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Electrical/simulator-dymola.log b/docs/correct_HTML_1520_newHPModels/regression/Electrical/simulator-dymola.log
new file mode 100644
index 0000000000..678f2c1de0
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Electrical/simulator-dymola.log
@@ -0,0 +1,139 @@
+ = true
+
+
+rCheck = checkModel("AixLib.Electrical.PVSystem.Validation.ValidationPVSystem");
+Check of AixLib.Electrical.PVSystem.Validation.ValidationPVSystem:
+Warning: The quantity of pVSystem.weaBus.TDryBul is "ThermodynamicTemperature" and the quantity of pVSystem.cellTemperature.T_a is "Temp_C".
+In connect(pVSystem.weaBus.TDryBul, pVSystem.cellTemperature.T_a);
+Found in class AixLib.Electrical.PVSystem.PVSystem, /tmp/tmp-AixLib-0-oalq7gas/AixLib/Electrical/PVSystem/PVSystem.mo at line 132, and used in component pVSystem.
+Variable pVSystem.weaBus.TDryBul was declared in class Modelica.Units.SI, /tmp/tmp-AixLib-0-oalq7gas/AixLib/BoundaryConditions/WeatherData/Bus.mo at line 5, and used in component pVSystem.weaBus.
+Variable pVSystem.cellTemperature.T_a was declared in class Modelica.Blocks.Interfaces, /tmp/tmp-AixLib-0-oalq7gas/AixLib/Electrical/PVSystem/BaseClasses/PartialCellTemperature.mo at line 21, and used in component pVSystem.cellTemperature.PartialCellTemperature.
+The model has the same number of unknowns and equations: 106
+The model has the same number of unknowns and equations:
+ 102+max([size(NISTdata.columns, 1); size(NISTdata.offset, 1)])
+Check of AixLib.Electrical.PVSystem.Validation.ValidationPVSystem successful.
+Warning: WARNINGS have been issued.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Electrical/Validation/ValidationPVSystem.mos\",", "AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Electrical.PVSystem.Validation.ValidationPVSystem\",", "AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Electrical.PVSystem.Validation.ValidationPVSystem\\\");\",", "AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Electrical/Validation/ValidationPVSystem.mos");
+simulateModel("AixLib.Electrical.PVSystem.Validation.ValidationPVSystem", startTime=28684800, stopTime=28771200, tolerance=1e-06, method="dassl", resultFile="AixLib.Electrical.PVSystem.Validation.ValidationPVSystem");
+Translation of AixLib.Electrical.PVSystem.Validation.ValidationPVSystem:
+Warning: The quantity of pVSystem.weaBus.TDryBul is "ThermodynamicTemperature" and the quantity of pVSystem.cellTemperature.T_a is "Temp_C".
+In connect(pVSystem.weaBus.TDryBul, pVSystem.cellTemperature.T_a);
+Found in class AixLib.Electrical.PVSystem.PVSystem, /tmp/tmp-AixLib-0-oalq7gas/AixLib/Electrical/PVSystem/PVSystem.mo at line 132, and used in component pVSystem.
+Variable pVSystem.weaBus.TDryBul was declared in class Modelica.Units.SI, /tmp/tmp-AixLib-0-oalq7gas/AixLib/BoundaryConditions/WeatherData/Bus.mo at line 5, and used in component pVSystem.weaBus.
+Variable pVSystem.cellTemperature.T_a was declared in class Modelica.Blocks.Interfaces, /tmp/tmp-AixLib-0-oalq7gas/AixLib/Electrical/PVSystem/BaseClasses/PartialCellTemperature.mo at line 21, and used in component pVSystem.cellTemperature.PartialCellTemperature.
+The DAE has 106 scalar unknowns and 106 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 20
+ Variables: 292
+ Constants: 6 (6 scalars)
+ Parameters: 141 (146 scalars)
+ Unknowns: 145 (106 scalars)
+ Equations: 102
+ Nontrivial: 92
+Translated Model
+ Constants: 16 scalars
+ Free parameters: 47 scalars
+ Parameter depending: 105 scalars
+ Outputs: 5 scalars
+ Time-varying variables: 55 scalars
+ Alias variables: 35 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: { }
+ Sizes after manipulation of the linear systems: { }
+ Sizes of nonlinear systems of equations: { }
+ Sizes after manipulation of the nonlinear systems: { }
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Warning: WARNINGS have been issued.
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Electrical.PVSystem.Validation.ValidationPVSystem.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Electrical.PVSystem.Examples.ExamplePVSystem");
+Check of AixLib.Electrical.PVSystem.Examples.ExamplePVSystem:
+Warning: The quantity of pVSystem.weaBus.TDryBul is "ThermodynamicTemperature" and the quantity of pVSystem.cellTemperature.T_a is "Temp_C".
+In connect(pVSystem.weaBus.TDryBul, pVSystem.cellTemperature.T_a);
+Found in class AixLib.Electrical.PVSystem.PVSystem, /tmp/tmp-AixLib-1-7r0sdxip/AixLib/Electrical/PVSystem/PVSystem.mo at line 132, and used in component pVSystem.
+Variable pVSystem.weaBus.TDryBul was declared in class Modelica.Units.SI, /tmp/tmp-AixLib-1-7r0sdxip/AixLib/BoundaryConditions/WeatherData/Bus.mo at line 5, and used in component pVSystem.weaBus.
+Variable pVSystem.cellTemperature.T_a was declared in class Modelica.Blocks.Interfaces, /tmp/tmp-AixLib-1-7r0sdxip/AixLib/Electrical/PVSystem/BaseClasses/PartialCellTemperature.mo at line 21, and used in component pVSystem.cellTemperature.PartialCellTemperature.
+The model has the same number of unknowns and equations: 294
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 294
+scalar unknowns and
+ 290+(if weaDat.pAtmSou == AixLib.BoundaryConditions.Types.DataSource.Parameter then 1 else 0)+(if weaDat.TDewPoiSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TDryBulSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TBlaSkySou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.relHumSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.opaSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.ceiHeiSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.totSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winSpeSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winDirSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HInfHorSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HDifHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HGloHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HGloHor_HDifHor then 2 else 1)
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 294
+Check of AixLib.Electrical.PVSystem.Examples.ExamplePVSystem successful.
+Warning: WARNINGS have been issued.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Electrical/Examples/ExamplePVSystem.mos\",", "AixLib.Electrical.PVSystem.Examples.ExamplePVSystem.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Electrical.PVSystem.Examples.ExamplePVSystem\",", "AixLib.Electrical.PVSystem.Examples.ExamplePVSystem.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Electrical.PVSystem.Examples.ExamplePVSystem.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Electrical.PVSystem.Examples.ExamplePVSystem\\\");\",", "AixLib.Electrical.PVSystem.Examples.ExamplePVSystem.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Electrical.PVSystem.Examples.ExamplePVSystem.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Electrical.PVSystem.Examples.ExamplePVSystem.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Electrical/Examples/ExamplePVSystem.mos");
+simulateModel("AixLib.Electrical.PVSystem.Examples.ExamplePVSystem", stopTime=31536000, method="dassl", tolerance=1e-06, resultFile="AixLib.Electrical.PVSystem.Examples.ExamplePVSystem");
+Translation of AixLib.Electrical.PVSystem.Examples.ExamplePVSystem:
+Warning: The quantity of pVSystem.weaBus.TDryBul is "ThermodynamicTemperature" and the quantity of pVSystem.cellTemperature.T_a is "Temp_C".
+In connect(pVSystem.weaBus.TDryBul, pVSystem.cellTemperature.T_a);
+Found in class AixLib.Electrical.PVSystem.PVSystem, /tmp/tmp-AixLib-1-7r0sdxip/AixLib/Electrical/PVSystem/PVSystem.mo at line 132, and used in component pVSystem.
+Variable pVSystem.weaBus.TDryBul was declared in class Modelica.Units.SI, /tmp/tmp-AixLib-1-7r0sdxip/AixLib/BoundaryConditions/WeatherData/Bus.mo at line 5, and used in component pVSystem.weaBus.
+Variable pVSystem.cellTemperature.T_a was declared in class Modelica.Blocks.Interfaces, /tmp/tmp-AixLib-1-7r0sdxip/AixLib/Electrical/PVSystem/BaseClasses/PartialCellTemperature.mo at line 21, and used in component pVSystem.cellTemperature.PartialCellTemperature.
+The DAE has 294 scalar unknowns and 294 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 67
+ Variables: 530
+ Constants: 24 (24 scalars)
+ Parameters: 239 (265 scalars)
+ Unknowns: 267 (294 scalars)
+ Equations: 288
+ Nontrivial: 262
+Translated Model
+ Constants: 132 scalars
+ Free parameters: 64 scalars
+ Parameter depending: 126 scalars
+ Outputs: 1 scalars
+ Time-varying variables: 116 scalars
+ Alias variables: 145 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: { }
+ Sizes after manipulation of the linear systems: { }
+ Sizes of nonlinear systems of equations: {3}
+ Sizes after manipulation of the nonlinear systems: {1}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Warning: WARNINGS have been issued.
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Electrical.PVSystem.Examples.ExamplePVSystem.translation.log");
\ No newline at end of file
diff --git a/docs/correct_HTML_1520_newHPModels/regression/Electrical/unitTests-dymola.log b/docs/correct_HTML_1520_newHPModels/regression/Electrical/unitTests-dymola.log
new file mode 100644
index 0000000000..ea91a32aa7
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Electrical/unitTests-dymola.log
@@ -0,0 +1,10 @@
+Regression tests are only run for the following package:
+ AixLib.Electrical
+Comparison files output by funnel are stored in the directory 'funnel_comp' of size 0.0 MB.
+Run 'python -c "import buildingspy.development.regressiontest as t; t.Tester(tool=\"dymola\").report()"'
+to access a summary of the comparison results.
+
+Script that runs unit tests had 0 warnings and 0 errors.
+
+Unit tests completed successfully.
+
diff --git a/docs/correct_HTML_1520_newHPModels/regression/Fluid/comparison-dymola.log b/docs/correct_HTML_1520_newHPModels/regression/Fluid/comparison-dymola.log
new file mode 100644
index 0000000000..ff3bf263b8
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Fluid/comparison-dymola.log
@@ -0,0 +1,1427 @@
+[
+ {
+ "comparison": {
+ "file_name": "AixLib.Fluid.FixedResistances.Examples.SimplePipe.mat",
+ "funnel_dirs": [
+ "funnel_comp/AixLib.Fluid.FixedResistances.Examples.SimplePipe.mat_senTemIn.T",
+ "funnel_comp/AixLib.Fluid.FixedResistances.Examples.SimplePipe.mat_senTemOut.T"
+ ],
+ "success_rate": 1.0,
+ "t_err_max": [
+ 0.0,
+ 0.0
+ ],
+ "test_passed": [
+ 1,
+ 1
+ ],
+ "var_groups": [
+ 0,
+ 0
+ ],
+ "variables": [
+ "senTemIn.T",
+ "senTemOut.T"
+ ],
+ "warnings": [
+ null,
+ null
+ ]
+ },
+ "model": "AixLib.Fluid.FixedResistances.Examples.SimplePipe",
+ "simulation": {
+ "elapsed_time": 0.00922,
+ "final_time": 1000,
+ "jacobians": 43,
+ "start_time": 0,
+ "state_events": 0,
+ "success": true
+ }
+ },
+ {
+ "comparison": {
+ "file_name": "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.mat",
+ "funnel_dirs": [
+ "funnel_comp/AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.mat_rampValvePosition.y",
+ "funnel_comp/AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.mat_pumpBus.rpmMea",
+ "funnel_comp/AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.mat_pumpBus.rpmSet",
+ "funnel_comp/AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.mat_pumpBus.onSet"
+ ],
+ "success_rate": 1.0,
+ "t_err_max": [
+ 0.0,
+ 0.0,
+ 0.0,
+ 0.0
+ ],
+ "test_passed": [
+ 1,
+ 1,
+ 1,
+ 1
+ ],
+ "var_groups": [
+ 0,
+ 1,
+ 1,
+ 2
+ ],
+ "variables": [
+ "rampValvePosition.y",
+ "pumpBus.rpmMea",
+ "pumpBus.rpmSet",
+ "pumpBus.onSet"
+ ],
+ "warnings": [
+ null,
+ null,
+ null,
+ null
+ ]
+ },
+ "model": "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled",
+ "simulation": {
+ "elapsed_time": 0.02,
+ "final_time": 600,
+ "jacobians": 170,
+ "start_time": 0,
+ "state_events": 3,
+ "success": true
+ }
+ },
+ {
+ "comparison": {
+ "file_name": "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.mat",
+ "funnel_dirs": [
+ "funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.mat_demand.port_a.m_flow"
+ ],
+ "success_rate": 1.0,
+ "t_err_max": [
+ 0.0
+ ],
+ "test_passed": [
+ 1
+ ],
+ "var_groups": [
+ 0
+ ],
+ "variables": [
+ "demand.port_a.m_flow"
+ ],
+ "warnings": [
+ null
+ ]
+ },
+ "model": "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass",
+ "simulation": {
+ "elapsed_time": 0.0521,
+ "final_time": 100000,
+ "jacobians": 162,
+ "start_time": 0,
+ "state_events": 0,
+ "success": true
+ }
+ },
+ {
+ "comparison": {
+ "file_name": "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.mat",
+ "funnel_dirs": [
+ "funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.mat_senTemIn.T",
+ "funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.mat_senTemOut.T"
+ ],
+ "success_rate": 1.0,
+ "t_err_max": [
+ 0.0,
+ 0.0
+ ],
+ "test_passed": [
+ 1,
+ 1
+ ],
+ "var_groups": [
+ 0,
+ 0
+ ],
+ "variables": [
+ "senTemIn.T",
+ "senTemOut.T"
+ ],
+ "warnings": [
+ null,
+ null
+ ]
+ },
+ "model": "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded",
+ "simulation": {
+ "elapsed_time": 0.0112,
+ "final_time": 1000,
+ "jacobians": 109,
+ "start_time": 0,
+ "state_events": 0,
+ "success": true
+ }
+ },
+ {
+ "comparison": {
+ "file_name": "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.mat",
+ "funnel_dirs": [
+ "funnel_comp/AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.mat_senEff.y",
+ "funnel_comp/AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.mat_latEff.y",
+ "funnel_comp/AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.mat_senTemColOut.T",
+ "funnel_comp/AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.mat_senTemHotIn.T",
+ "funnel_comp/AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.mat_senTemColIn.T",
+ "funnel_comp/AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.mat_senTemHotOut.T",
+ "funnel_comp/AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.mat_senMasFraColIn.X",
+ "funnel_comp/AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.mat_senMasFraHotIn.X",
+ "funnel_comp/AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.mat_senMasFraColOut.X",
+ "funnel_comp/AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.mat_senMasFraHotOut.X"
+ ],
+ "success_rate": 1.0,
+ "t_err_max": [
+ 0.0,
+ 0.0,
+ 0.0,
+ 0.0,
+ 0.0,
+ 0.0,
+ 0.0,
+ 0.0,
+ 0.0,
+ 0.0
+ ],
+ "test_passed": [
+ 1,
+ 1,
+ 1,
+ 1,
+ 1,
+ 1,
+ 1,
+ 1,
+ 1,
+ 1
+ ],
+ "var_groups": [
+ 0,
+ 0,
+ 1,
+ 1,
+ 1,
+ 1,
+ 2,
+ 2,
+ 2,
+ 2
+ ],
+ "variables": [
+ "senEff.y",
+ "latEff.y",
+ "senTemColOut.T",
+ "senTemHotIn.T",
+ "senTemColIn.T",
+ "senTemHotOut.T",
+ "senMasFraColIn.X",
+ "senMasFraHotIn.X",
+ "senMasFraColOut.X",
+ "senMasFraHotOut.X"
+ ],
+ "warnings": [
+ null,
+ null,
+ null,
+ null,
+ null,
+ null,
+ null,
+ null,
+ null,
+ null
+ ]
+ },
+ "model": "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger",
+ "simulation": {
+ "elapsed_time": 0.315,
+ "final_time": 7200,
+ "jacobians": 62,
+ "start_time": 0,
+ "state_events": 0,
+ "success": true
+ }
+ },
+ {
+ "comparison": {
+ "file_name": "AixLib.Fluid.Storage.Examples.StorageSolarCollector.mat",
+ "funnel_dirs": [
+ "funnel_comp/AixLib.Fluid.Storage.Examples.StorageSolarCollector.mat_bufferStorage.layer[10].T",
+ "funnel_comp/AixLib.Fluid.Storage.Examples.StorageSolarCollector.mat_bufferStorage.layer[5].T",
+ "funnel_comp/AixLib.Fluid.Storage.Examples.StorageSolarCollector.mat_bufferStorage.layer[1].T",
+ "funnel_comp/AixLib.Fluid.Storage.Examples.StorageSolarCollector.mat_temperatureSensor.T",
+ "funnel_comp/AixLib.Fluid.Storage.Examples.StorageSolarCollector.mat_solarThermal.Irradiation",
+ "funnel_comp/AixLib.Fluid.Storage.Examples.StorageSolarCollector.mat_solarThermal.heater.Q_flow"
+ ],
+ "success_rate": 1.0,
+ "t_err_max": [
+ 0.0,
+ 0.0,
+ 0.0,
+ 0.0,
+ 0.0,
+ 0.0
+ ],
+ "test_passed": [
+ 1,
+ 1,
+ 1,
+ 1,
+ 1,
+ 1
+ ],
+ "var_groups": [
+ 0,
+ 0,
+ 0,
+ 1,
+ 2,
+ 2
+ ],
+ "variables": [
+ "bufferStorage.layer[10].T",
+ "bufferStorage.layer[5].T",
+ "bufferStorage.layer[1].T",
+ "temperatureSensor.T",
+ "solarThermal.Irradiation",
+ "solarThermal.heater.Q_flow"
+ ],
+ "warnings": [
+ null,
+ null,
+ null,
+ null,
+ null,
+ null
+ ]
+ },
+ "model": "AixLib.Fluid.Storage.Examples.StorageSolarCollector",
+ "simulation": {
+ "elapsed_time": 0.62,
+ "final_time": 172800,
+ "jacobians": 1201,
+ "start_time": 0,
+ "state_events": 3,
+ "success": true
+ }
+ },
+ {
+ "comparison": {
+ "file_name": "AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.mat",
+ "funnel_dirs": [
+ "funnel_comp/AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.mat_indoorSwimming.TPool",
+ "funnel_comp/AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.mat_prescribedHeatFlow.Q_flow",
+ "funnel_comp/AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.mat_indoorSwimming.PPool",
+ "funnel_comp/AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.mat_indoorSwimming.QEva"
+ ],
+ "success_rate": 1.0,
+ "t_err_max": [
+ 0.0,
+ 0.0,
+ 0.0,
+ 0.0
+ ],
+ "test_passed": [
+ 1,
+ 1,
+ 1,
+ 1
+ ],
+ "var_groups": [
+ 0,
+ 0,
+ 0,
+ 0
+ ],
+ "variables": [
+ "indoorSwimming.TPool",
+ "prescribedHeatFlow.Q_flow",
+ "indoorSwimming.PPool",
+ "indoorSwimming.QEva"
+ ],
+ "warnings": [
+ null,
+ null,
+ null,
+ null
+ ]
+ },
+ "model": "AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem",
+ "simulation": {
+ "elapsed_time": 0.409848,
+ "final_time": 604800,
+ "jacobians": 97,
+ "start_time": 0,
+ "state_events": 9,
+ "success": true
+ }
+ },
+ {
+ "comparison": {
+ "file_name": "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.mat",
+ "funnel_dirs": [
+ "funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.mat_demand.senT_supply.T",
+ "funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.mat_demand.senT_return.T",
+ "funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.mat_demand.port_a.m_flow"
+ ],
+ "success_rate": 1.0,
+ "t_err_max": [
+ 0.0,
+ 0.0,
+ 0.0
+ ],
+ "test_passed": [
+ 1,
+ 1,
+ 1
+ ],
+ "var_groups": [
+ 0,
+ 0,
+ 1
+ ],
+ "variables": [
+ "demand.senT_supply.T",
+ "demand.senT_return.T",
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.mat_demand.senT_return.T/test.csv b/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.mat_demand.senT_return.T/test.csv
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.mat_demand.senT_return.T/upperBound.csv b/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.mat_demand.senT_return.T/upperBound.csv
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.mat_demand.senT_supply.T/errors.csv b/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.mat_demand.senT_supply.T/errors.csv
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.mat_demand.senT_supply.T/test.csv b/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.mat_demand.senT_supply.T/test.csv
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.mat_demand.senT_supply.T/upperBound.csv b/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.mat_demand.senT_supply.T/upperBound.csv
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.mat_demand.port_a.m_flow/errors.csv b/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.mat_demand.port_a.m_flow/errors.csv
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.mat_senTemIn1.T/errors.csv b/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.mat_senTemIn1.T/errors.csv
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.mat_senTemIn2.T/errors.csv b/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.mat_senTemIn2.T/errors.csv
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.mat_senTemIn3.T/errors.csv b/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.mat_senTemIn3.T/errors.csv
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.mat_senTemIn3.T/test.csv b/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.mat_senTemIn3.T/test.csv
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.mat_senTemOut.T/errors.csv b/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.mat_senTemOut.T/errors.csv
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.mat_senTemOut.T/reference.csv b/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.mat_senTemOut.T/reference.csv
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.mat_senTemOut1.T/errors.csv b/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.mat_senTemOut1.T/errors.csv
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.mat_senTemOut1.T/reference.csv b/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.mat_senTemOut1.T/reference.csv
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.mat_coldStorage.layer[1].T/reference.csv b/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.mat_coldStorage.layer[1].T/reference.csv
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.mat_FRdp.m_flow/errors.csv b/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.mat_FRdp.m_flow/errors.csv
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diff --git a/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.HeatExchangers.Examples.HeatingRod.mat_TOut.y/errors.csv b/docs/correct_HTML_1520_newHPModels/regression/Fluid/funnel_comp/AixLib.Fluid.HeatExchangers.Examples.HeatingRod.mat_TOut.y/errors.csv
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+112319.999000,346.159382
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+114048.001000,343.869160
+115776.000438,342.581742
+117503.999000,343.084960
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+120959.999000,345.142252
+122687.999000,345.818648
+124415.999000,346.592768
+126143.999000,347.730684
+127871.999000,348.563792
+129599.999000,349.560637
+131327.999000,350.103049
+133055.999000,350.683463
+134783.999000,350.789648
+136511.999000,350.891679
+136512.001000,350.891679
+138240.001000,350.561851
+139968.001000,350.214061
+141696.001000,349.499052
+143424.001000,348.760858
+145152.001000,347.900684
+146880.001000,347.412770
+148608.001000,347.013934
+150336.001000,346.802389
+152064.001000,346.640178
+153792.001000,346.512059
+155520.001000,346.438897
+157248.001000,346.279405
+158976.001000,346.221272
+160704.001000,345.983486
+162432.001000,345.923948
+164160.001000,345.605972
+165888.001000,345.555996
+167616.001000,345.178055
+169344.001000,345.136051
+171072.001000,344.737826
+172800.001000,344.691698
diff --git a/docs/correct_HTML_1520_newHPModels/regression/Fluid/simulator-dymola.log b/docs/correct_HTML_1520_newHPModels/regression/Fluid/simulator-dymola.log
new file mode 100644
index 0000000000..2e4c6855f3
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Fluid/simulator-dymola.log
@@ -0,0 +1,3683 @@
+ = true
+
+
+rCheck = checkModel("AixLib.Fluid.FixedResistances.Examples.SimplePipe");
+Check of AixLib.Fluid.FixedResistances.Examples.SimplePipe:
+The model has the same number of unknowns and equations: 368
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 360+simplePipe.vol[1].dynBal.nPorts+simplePipe.vol[2].dynBal.nPorts+ simplePipe.vol[3].dynBal.nPorts+simplePipe.vol[4].dynBal.nPorts
+scalar unknowns and
+ 334+2*Source.nPorts+(if not Source.use_m_flow_in then 1 else 0)+(if not Source.use_T_in then 1 else 0)+(if not Source.use_X_in then 1 else 0)+2* Sink.nPorts+(if not simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* simplePipe.vol[1].dynBal.nPorts+(if not simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*simplePipe.vol[2].dynBal.nPorts+(if not simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*simplePipe.vol[3].dynBal.nPorts+(if not simplePipe.vol[4].dynBal.use_mWat_flow then 1 else 0)+3*simplePipe.vol[4].dynBal.nPorts
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 368
+Check of AixLib.Fluid.FixedResistances.Examples.SimplePipe successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/FixedResistances/Examples/SimplePipe.mos\",", "AixLib.Fluid.FixedResistances.Examples.SimplePipe.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.FixedResistances.Examples.SimplePipe\",", "AixLib.Fluid.FixedResistances.Examples.SimplePipe.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.FixedResistances.Examples.SimplePipe.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.FixedResistances.Examples.SimplePipe\\\");\",", "AixLib.Fluid.FixedResistances.Examples.SimplePipe.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.FixedResistances.Examples.SimplePipe.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.FixedResistances.Examples.SimplePipe.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/FixedResistances/Examples/SimplePipe.mos");
+translateModel("AixLib.Fluid.FixedResistances.Examples.SimplePipe");
+Translation of AixLib.Fluid.FixedResistances.Examples.SimplePipe:
+The DAE has 368 scalar unknowns and 368 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 80
+ Variables: 963
+ Constants: 18 (18 scalars)
+ Parameters: 450 (428 scalars)
+ Unknowns: 495 (378 scalars)
+ Differentiated variables: 14 scalars
+ Equations: 363
+ Nontrivial: 270
+Translated Model
+ Constants: 341 scalars
+ Free parameters: 44 scalars
+ Parameter depending: 126 scalars
+ Continuous time states: 10 scalars
+ Time-varying variables: 71 scalars
+ Alias variables: 242 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: { }
+ Sizes after manipulation of the linear systems: { }
+ Sizes of nonlinear systems of equations: { }
+ Sizes after manipulation of the nonlinear systems: { }
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ senTemIn.T
+ senTemOut.T
+ simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T
+ simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T
+ simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T
+ simplePipe.PipeWall[4].CylindricLoad1.heatCapacitor.T
+ simplePipe.vol[1].dynBal.U
+ simplePipe.vol[2].dynBal.U
+ simplePipe.vol[3].dynBal.U
+ simplePipe.vol[4].dynBal.U
+
+ = true
+simulateModel("AixLib.Fluid.FixedResistances.Examples.SimplePipe", stopTime=1000, method="dassl", tolerance=1e-006, resultFile="AixLib.Fluid.FixedResistances.Examples.SimplePipe");
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.FixedResistances.Examples.SimplePipe.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger");
+Check of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger:
+The model has the same number of unknowns and equations: 5083
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 3373+32*enthalpyExchanger.n+16*enthalpyExchanger.airDuct2.heatTransfer.n+18* enthalpyExchanger.airDuct2.massTransfer.n+16*enthalpyExchanger.airDuct1.heatTransfer.n +18*enthalpyExchanger.airDuct1.massTransfer.n+5*enthalpyExchanger.membrane.heatTransfer.n +enthalpyExchanger.membrane.massTransfer.n+2*enthalpyExchanger.airDuct2.vol[1].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[2].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[3].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[4].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[5].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[6].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[7].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[8].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[9].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[10].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[11].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[12].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[13].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[14].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[15].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[1].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[2].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[3].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[4].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[5].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[6].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[7].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[8].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[9].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[10].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[11].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[12].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[13].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[14].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[15].dynBal.nPorts
+scalar unknowns and
+ 3043+17*enthalpyExchanger.airDuct2.heatTransfer.n+19*enthalpyExchanger.airDuct2.massTransfer.n +3*(if enthalpyExchanger.couFloArr then 2*enthalpyExchanger.n else 0)+17* enthalpyExchanger.airDuct1.heatTransfer.n+19*enthalpyExchanger.airDuct1.massTransfer.n +7*enthalpyExchanger.membrane.heatTransfer.n+3*enthalpyExchanger.membrane.massTransfer.n +2*(if enthalpyExchanger.useConPer then 1 else 0)+32*enthalpyExchanger.n+(if souAirHot.use_Xi_in then 2 else (if souAirHot.use_X_in then 1 else 3))+3* souAirHot.nPorts+(if not souAirHot.use_p_in then 1 else 0)+(if not souAirHot.use_T_in then 1 else 0)+(if sinAirHot.use_Xi_in then 2 else (if sinAirHot.use_X_in then 1 else 3))+3*sinAirHot.nPorts+(if not sinAirHot.use_p_in then 1 else 0)+(if not sinAirHot.use_T_in then 1 else 0)+( if souAirCol.use_Xi_in then 2 else (if souAirCol.use_X_in then 1 else 3))+3* souAirCol.nPorts+(if not souAirCol.use_p_in then 1 else 0)+(if not souAirCol.use_T_in then 1 else 0)+(if sinAirCol.use_Xi_in then 2 else (if sinAirCol.use_X_in then 1 else 3))+3*sinAirCol.nPorts+(if not sinAirCol.use_p_in then 1 else 0)+(if not sinAirCol.use_T_in then 1 else 0)+5 *enthalpyExchanger.airDuct2.vol[1].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[2].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[3].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[4].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[5].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[6].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[7].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[8].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[9].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[10].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[11].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[12].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[13].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[14].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[15].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[1].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[2].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[3].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[4].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[5].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[6].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[7].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[8].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[9].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[10].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[11].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[12].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[13].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[14].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[15].dynBal.nPorts
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 5083
+Check of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/MassExchangers/MembraneBasedEnthalpyExchangers/Examples/Test_EnthalpyExchanger.mos\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger\\\");\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/MassExchangers/MembraneBasedEnthalpyExchangers/Examples/Test_EnthalpyExchanger.mos");
+simulateModel("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger", stopTime=7200, outputInterval=10, method="dassl", tolerance=1e-6, resultFile="AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger");
+Translation of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger:
+The DAE has 5083 scalar unknowns and 5083 scalar equations.
+Redundant consistent initial conditions.
+Removed the following equations which are redundant and consistent:
+ if (enthalpyExchanger.airDuct2.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[1].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[1].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[1].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[1].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[1].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[2].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[2].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[2].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[2].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[2].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[3].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[3].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[3].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[3].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[3].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[4].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[4].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[4].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[4].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[4].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[5].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[5].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[5].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[5].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[5].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[6].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[6].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[6].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[6].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[6].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[7].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[7].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[7].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[7].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[7].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[8].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[8].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[8].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[8].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[8].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[9].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[9].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[9].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[9].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[9].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[10].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[10].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[10].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[10].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[10].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[11].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[11].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[11].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[11].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[11].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[12].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[12].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[12].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[12].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[12].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[13].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[13].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[13].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[13].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[13].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[14].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[14].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[14].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[14].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[14].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[15].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[15].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[15].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[15].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[15].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[1].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[1].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[1].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[1].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[1].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[2].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[2].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[2].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[2].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[2].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[3].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[3].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[3].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[3].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[3].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[4].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[4].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[4].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[4].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[4].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[5].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[5].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[5].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[5].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[5].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[6].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[6].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[6].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[6].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[6].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[7].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[7].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[7].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[7].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[7].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[8].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[8].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[8].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[8].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[8].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[9].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[9].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[9].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[9].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[9].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[10].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[10].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[10].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[10].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[10].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[11].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[11].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[11].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[11].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[11].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[12].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[12].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[12].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[12].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[12].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[13].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[13].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[13].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[13].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[13].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[14].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[14].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[14].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[14].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[14].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[15].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[15].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[15].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[15].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[15].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+
+This required evaluation of
+the interactive parameters
+ sinAirCol.p(start = 101325)
+ sinAirHot.p(start = 101325)
+
+The redundancies involve
+initial equations:
+ sinAirCol.p = 101325.0;
+ sinAirCol.p = 101325.0;
+ sinAirCol.p = 101325.0;
+ sinAirCol.p = 101325.0;
+ sinAirCol.p = 101325.0;
+ sinAirCol.p = 101325.0;
+ sinAirCol.p = 101325.0;
+ sinAirCol.p = 101325.0;
+ sinAirCol.p = 101325.0;
+ sinAirCol.p = 101325.0;
+ sinAirCol.p = 101325.0;
+ sinAirCol.p = 101325.0;
+ sinAirCol.p = 101325.0;
+ sinAirCol.p = 101325.0;
+ sinAirCol.p = 101325.0;
+ sinAirHot.p = 101325.0;
+ sinAirHot.p = 101325.0;
+ sinAirHot.p = 101325.0;
+ sinAirHot.p = 101325.0;
+ sinAirHot.p = 101325.0;
+ sinAirHot.p = 101325.0;
+ sinAirHot.p = 101325.0;
+ sinAirHot.p = 101325.0;
+ sinAirHot.p = 101325.0;
+ sinAirHot.p = 101325.0;
+ sinAirHot.p = 101325.0;
+ sinAirHot.p = 101325.0;
+ sinAirHot.p = 101325.0;
+ sinAirHot.p = 101325.0;
+ sinAirHot.p = 101325.0;
+
+
+Statistics
+
+Original Model
+ Number of components: 556
+ Variables: 6181
+ Constants: 154 (154 scalars)
+ Parameters: 2178 (2382 scalars)
+ Unknowns: 3849 (5219 scalars)
+ Differentiated variables: 117 scalars
+ Equations: 2512
+ Nontrivial: 1919
+Translated Model
+ Constants: 2163 scalars
+ Free parameters: 163 scalars
+ Parameter depending: 1011 scalars
+ Continuous time states: 87 scalars
+ Time-varying variables: 1614 scalars
+ Alias variables: 2804 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: {2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3}
+ Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2}
+ Sizes of nonlinear systems of equations: {1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1}
+ Sizes after manipulation of the nonlinear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ enthalpyExchanger.airDuct1.senRelHum.phi
+ enthalpyExchanger.airDuct1.senTem.T
+ enthalpyExchanger.airDuct1.vol[1].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[1].dynBal.U
+ enthalpyExchanger.airDuct1.vol[2].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[2].dynBal.U
+ enthalpyExchanger.airDuct1.vol[3].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[3].dynBal.U
+ enthalpyExchanger.airDuct1.vol[4].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[4].dynBal.U
+ enthalpyExchanger.airDuct1.vol[5].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[5].dynBal.U
+ enthalpyExchanger.airDuct1.vol[6].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[6].dynBal.U
+ enthalpyExchanger.airDuct1.vol[7].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[7].dynBal.U
+ enthalpyExchanger.airDuct1.vol[8].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[8].dynBal.U
+ enthalpyExchanger.airDuct1.vol[9].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[9].dynBal.U
+ enthalpyExchanger.airDuct1.vol[10].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[10].dynBal.U
+ enthalpyExchanger.airDuct1.vol[11].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[11].dynBal.U
+ enthalpyExchanger.airDuct1.vol[12].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[12].dynBal.U
+ enthalpyExchanger.airDuct1.vol[13].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[13].dynBal.U
+ enthalpyExchanger.airDuct1.vol[14].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[14].dynBal.U
+ enthalpyExchanger.airDuct1.vol[15].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[15].dynBal.U
+ enthalpyExchanger.airDuct2.senRelHum.phi
+ enthalpyExchanger.airDuct2.senTem.T
+ enthalpyExchanger.airDuct2.vol[1].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[1].dynBal.U
+ enthalpyExchanger.airDuct2.vol[2].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[2].dynBal.U
+ enthalpyExchanger.airDuct2.vol[3].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[3].dynBal.U
+ enthalpyExchanger.airDuct2.vol[4].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[4].dynBal.U
+ enthalpyExchanger.airDuct2.vol[5].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[5].dynBal.U
+ enthalpyExchanger.airDuct2.vol[6].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[6].dynBal.U
+ enthalpyExchanger.airDuct2.vol[7].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[7].dynBal.U
+ enthalpyExchanger.airDuct2.vol[8].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[8].dynBal.U
+ enthalpyExchanger.airDuct2.vol[9].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[9].dynBal.U
+ enthalpyExchanger.airDuct2.vol[10].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[10].dynBal.U
+ enthalpyExchanger.airDuct2.vol[11].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[11].dynBal.U
+ enthalpyExchanger.airDuct2.vol[12].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[12].dynBal.U
+ enthalpyExchanger.airDuct2.vol[13].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[13].dynBal.U
+ enthalpyExchanger.airDuct2.vol[14].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[14].dynBal.U
+ enthalpyExchanger.airDuct2.vol[15].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[15].dynBal.U
+ enthalpyExchanger.membrane.heatTransfer.Ts[1]
+ enthalpyExchanger.membrane.heatTransfer.Ts[2]
+ enthalpyExchanger.membrane.heatTransfer.Ts[3]
+ enthalpyExchanger.membrane.heatTransfer.Ts[4]
+ enthalpyExchanger.membrane.heatTransfer.Ts[5]
+ enthalpyExchanger.membrane.heatTransfer.Ts[6]
+ enthalpyExchanger.membrane.heatTransfer.Ts[7]
+ enthalpyExchanger.membrane.heatTransfer.Ts[8]
+ enthalpyExchanger.membrane.heatTransfer.Ts[9]
+ enthalpyExchanger.membrane.heatTransfer.Ts[10]
+ enthalpyExchanger.membrane.heatTransfer.Ts[11]
+ enthalpyExchanger.membrane.heatTransfer.Ts[12]
+ enthalpyExchanger.membrane.heatTransfer.Ts[13]
+ enthalpyExchanger.membrane.heatTransfer.Ts[14]
+ enthalpyExchanger.membrane.heatTransfer.Ts[15]
+ senMasFraColIn.X
+ senMasFraColOut.X
+ senMasFraHotIn.X
+ senMasFraHotOut.X
+ senTemColIn.T
+ senTemColOut.T
+ senTemHotIn.T
+ senTemHotOut.T
+
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem");
+Check of AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem:
+The model has the same number of unknowns and equations: 733
+The model has the same number of unknowns and equations
+for the given numerical settings of parameters: 733
+Check of AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Pools/Examples/IndoorSwimmingPoolExternalHeatingSystem.mos\",", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem\",", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem\\\");\",", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Pools/Examples/IndoorSwimmingPoolExternalHeatingSystem.mos");
+simulateModel("AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem", tolerance=1e-6, stopTime=604800, numberOfIntervals=0, outputInterval=900, method="CVode", resultFile="AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem");
+Translation of AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem:
+The DAE has 733 scalar unknowns and 733 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 171
+ Variables: 1742
+ Constants: 45 (45 scalars)
+ Parameters: 777 (964 scalars)
+ Unknowns: 920 (764 scalars)
+ Differentiated variables: 3 scalars
+ Equations: 763
+ Nontrivial: 619
+Translated Model
+ Constants: 629 scalars
+ Free parameters: 133 scalars
+ Parameter depending: 374 scalars
+ Continuous time states: 3 scalars
+ Time-varying variables: 191 scalars
+ Alias variables: 446 scalars
+ Number of mixed real/discrete systems of equations: 1
+ Sizes of linear systems of equations: {26}
+ Sizes after manipulation of the linear systems: {13}
+ Sizes of nonlinear systems of equations: {79, 1, 1}
+ Sizes after manipulation of the nonlinear systems: {17, 0, 1}
+ Number of numerical Jacobians: 0
+ Initialization problem
+ Sizes of nonlinear systems of equations: {1, 78, 1}
+ Sizes after manipulation of the nonlinear systems: {0, 17, 1}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ indoorSwimming.cirPump.filter.s[1]
+ indoorSwimming.cirPump.filter.s[2]
+ PI.I.y
+
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.Storage.Examples.StorageSolarCollector");
+Check of AixLib.Fluid.Storage.Examples.StorageSolarCollector:
+The model has the same number of unknowns and equations: 3387
+Check of AixLib.Fluid.Storage.Examples.StorageSolarCollector successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageSolarCollector.mos\",", "AixLib.Fluid.Storage.Examples.StorageSolarCollector.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Storage.Examples.StorageSolarCollector\",", "AixLib.Fluid.Storage.Examples.StorageSolarCollector.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Storage.Examples.StorageSolarCollector.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Storage.Examples.StorageSolarCollector\\\");\",", "AixLib.Fluid.Storage.Examples.StorageSolarCollector.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Storage.Examples.StorageSolarCollector.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Storage.Examples.StorageSolarCollector.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageSolarCollector.mos");
+simulateModel("AixLib.Fluid.Storage.Examples.StorageSolarCollector", tolerance=1e-6, stopTime=172800, method="dassl", resultFile="AixLib.Fluid.Storage.Examples.StorageSolarCollector");
+Translation of AixLib.Fluid.Storage.Examples.StorageSolarCollector:
+The DAE has 3387 scalar unknowns and 3387 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 688
+ Variables: 8995
+ Constants: 163 (163 scalars)
+ Parameters: 4276 (4349 scalars)
+ Unknowns: 4556 (3492 scalars)
+ Differentiated variables: 114 scalars
+ Equations: 3534
+ Nontrivial: 2710
+Translated Model
+ Constants: 2921 scalars
+ Free parameters: 420 scalars
+ Parameter depending: 1577 scalars
+ Continuous time states: 83 scalars
+ Time-varying variables: 870 scalars
+ Alias variables: 2216 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: {4, 3, 3, 2, 2, 2, 4, 3, 3, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2}
+ Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0}
+ Sizes of nonlinear systems of equations: {24, 1, 6, 6, 6, 6, 6, 6, 6, 6, 6, 6}
+ Sizes after manipulation of the nonlinear systems: {1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1}
+ Number of numerical Jacobians: 0
+ Initialization problem
+ Sizes of nonlinear systems of equations: {24, 1, 1}
+ Sizes after manipulation of the nonlinear systems: {1, 0, 1}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ bufferStorage.bottomCover.loadIns.T
+ bufferStorage.bottomCover.loadWall.T
+ bufferStorage.heatingCoil1.pipe[1].del.x
+ bufferStorage.heatingCoil1.pipe[1].timDel.x
+ bufferStorage.heatingCoil1.pipe[1].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[1].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[2].del.x
+ bufferStorage.heatingCoil1.pipe[2].timDel.x
+ bufferStorage.heatingCoil1.pipe[2].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[2].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[3].del.x
+ bufferStorage.heatingCoil1.pipe[3].timDel.x
+ bufferStorage.heatingCoil1.pipe[3].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[3].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[4].del.x
+ bufferStorage.heatingCoil1.pipe[4].timDel.x
+ bufferStorage.heatingCoil1.pipe[4].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[4].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[5].del.x
+ bufferStorage.heatingCoil1.pipe[5].timDel.x
+ bufferStorage.heatingCoil1.pipe[5].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[5].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[6].del.x
+ bufferStorage.heatingCoil1.pipe[6].timDel.x
+ bufferStorage.heatingCoil1.pipe[6].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[6].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[7].del.x
+ bufferStorage.heatingCoil1.pipe[7].timDel.x
+ bufferStorage.heatingCoil1.pipe[7].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[7].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[8].del.x
+ bufferStorage.heatingCoil1.pipe[8].timDel.x
+ bufferStorage.heatingCoil1.pipe[8].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[8].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[9].del.x
+ bufferStorage.heatingCoil1.pipe[9].timDel.x
+ bufferStorage.heatingCoil1.pipe[9].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[9].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[10].del.x
+ bufferStorage.heatingCoil1.pipe[10].timDel.x
+ bufferStorage.heatingCoil1.pipe[10].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[10].vol_b.dynBal.U
+ bufferStorage.layer[1].dynBal.U
+ bufferStorage.layer[2].dynBal.U
+ bufferStorage.layer[3].dynBal.U
+ bufferStorage.layer[4].dynBal.U
+ bufferStorage.layer[5].dynBal.U
+ bufferStorage.layer[6].dynBal.U
+ bufferStorage.layer[7].dynBal.U
+ bufferStorage.layer[8].dynBal.U
+ bufferStorage.layer[9].dynBal.U
+ bufferStorage.layer[10].dynBal.U
+ bufferStorage.storageMantle[1].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[1].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[2].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[2].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[3].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[3].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[4].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[4].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[5].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[5].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[6].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[6].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[7].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[7].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[8].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[8].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[9].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[9].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[10].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[10].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.topCover.loadIns.T
+ bufferStorage.topCover.loadWall.T
+ PI.I.y
+ pump.filter.s[1]
+ pump.filter.s[2]
+ solarThermal.senTCold.T
+ solarThermal.senTHot.T
+ solarThermal.vol.dynBal.U
+ temperatureSensor.T
+ valve.filter.s[1]
+ valve.filter.s[2]
+
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.Storage.Examples.StorageSolarCollector.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass");
+Check of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass:
+The model has the same number of unknowns and equations: 572
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 562+demand.vol.dynBal.nPorts+pipeSupply.vol_b.dynBal.nPorts+pipeSupply.vol_a.dynBal.nPorts +pipeReturn.vol_b.dynBal.nPorts+pipeReturn.vol_a.dynBal.nPorts
+scalar unknowns and
+ 522+(if sourceIdeal.source.use_Xi_in then 1 else (if sourceIdeal.source.use_X_in then 0 else 1))+(if not sourceIdeal.source.use_p_in then 1 else 0)+2* sourceIdeal.source.nPorts+(if not sourceIdeal.source.use_T_in then 1 else 0)+ (if sourceIdeal.sink.use_Xi_in then 1 else (if sourceIdeal.sink.use_X_in then 0 else 1))+(if not sourceIdeal.sink.use_p_in then 1 else 0)+2*sourceIdeal.sink.nPorts +(if not sourceIdeal.sink.use_T_in then 1 else 0)+(if demand.sink.use_Xi_in then 1 else (if demand.sink.use_X_in then 0 else 1))+(if not demand.sink.use_m_flow_in then 1 else 0)+2*demand.sink.nPorts+(if not demand.sink.use_T_in then 1 else 0)+(if demand.source.use_Xi_in then 1 else ( if demand.source.use_X_in then 0 else 1))+(if not demand.source.use_m_flow_in then 1 else 0)+2*demand.source.nPorts+(if not demand.source.use_T_in then 1 else 0)+(if not demand.vol.dynBal.use_mWat_flow then 1 else 0)+3* demand.vol.dynBal.nPorts+(if not pipeSupply.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*pipeSupply.vol_b.dynBal.nPorts+(if not pipeSupply.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*pipeSupply.vol_a.dynBal.nPorts+(if not pipeReturn.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*pipeReturn.vol_b.dynBal.nPorts+(if not pipeReturn.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*pipeReturn.vol_a.dynBal.nPorts
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 572
+Check of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Demands/Examples/OpenLoopVarTSupplyDpFixedTempDifferenceBypass.mos\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass\\\");\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Demands/Examples/OpenLoopVarTSupplyDpFixedTempDifferenceBypass.mos");
+translateModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass");
+Translation of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass:
+The DAE has 572 scalar unknowns and 572 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 114
+ Variables: 1506
+ Constants: 29 (29 scalars)
+ Parameters: 675 (646 scalars)
+ Unknowns: 802 (590 scalars)
+ Differentiated variables: 17 scalars
+ Equations: 680
+ Nontrivial: 543
+Translated Model
+ Constants: 509 scalars
+ Free parameters: 121 scalars
+ Parameter depending: 138 scalars
+ Continuous time states: 12 scalars
+ Time-varying variables: 132 scalars
+ Alias variables: 365 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: { }
+ Sizes after manipulation of the linear systems: { }
+ Sizes of nonlinear systems of equations: {8}
+ Sizes after manipulation of the nonlinear systems: {1}
+ Number of numerical Jacobians: 0
+ Initialization problem
+ Sizes of nonlinear systems of equations: {8}
+ Sizes after manipulation of the nonlinear systems: {1}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ demand.senT_return.T
+ demand.senT_supply.T
+ demand.vol.dynBal.U
+ pControl.I.y
+ pipeReturn.del.x
+ pipeReturn.timDel.x
+ pipeReturn.vol_a.dynBal.U
+ pipeReturn.vol_b.dynBal.U
+ pipeSupply.del.x
+ pipeSupply.timDel.x
+ pipeSupply.vol_a.dynBal.U
+ pipeSupply.vol_b.dynBal.U
+
+ = true
+simulateModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass", stopTime=100000, method="dassl", tolerance=1e-006, resultFile="AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass");
+Not possible to open file "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.mat": No such file or directory
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded");
+Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded:
+The model has the same number of unknowns and equations: 256
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 254+pip.plugFlowPipeZeta.vol.dynBal.nPorts
+scalar unknowns and
+ 240+(if sin.use_Xi_in then 1 else (if sin.use_X_in then 0 else 1))+(if not sin.use_p_in then 1 else 0)+2*sin.nPorts+(if not sin.use_T_in then 1 else 0)+ (if sou.use_Xi_in then 1 else (if sou.use_X_in then 0 else 1))+(if not sou.use_m_flow_in then 1 else 0)+2*sou.nPorts+(if not sou.use_T_in then 1 else 0)+(if not pip.plugFlowPipeZeta.vol.dynBal.use_mWat_flow then 1 else 0) +3*pip.plugFlowPipeZeta.vol.dynBal.nPorts
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 256
+Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/PlugFlowPipeEmbedded.mos\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded\\\");\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/PlugFlowPipeEmbedded.mos");
+translateModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded");
+Translation of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded:
+The DAE has 256 scalar unknowns and 256 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 53
+ Variables: 739
+ Constants: 11 (11 scalars)
+ Parameters: 390 (383 scalars)
+ Unknowns: 338 (264 scalars)
+ Differentiated variables: 9 scalars
+ Equations: 267
+ Nontrivial: 229
+Translated Model
+ Constants: 224 scalars
+ Free parameters: 64 scalars
+ Parameter depending: 145 scalars
+ Continuous time states: 8 scalars
+ Time-varying variables: 57 scalars
+ Alias variables: 168 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: {2, 2}
+ Sizes after manipulation of the linear systems: {0, 0}
+ Sizes of nonlinear systems of equations: {6}
+ Sizes after manipulation of the nonlinear systems: {1}
+ Number of numerical Jacobians: 0
+ Initialization problem
+ Sizes of nonlinear systems of equations: {14}
+ Sizes after manipulation of the nonlinear systems: {6}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ pip.cylindricHeatTransfer_1.CylindricLoad1.heatCapacitor.T
+ pip.cylindricHeatTransfer_2.CylindricLoad1.heatCapacitor.T
+ pip.cylindricHeatTransfer_3.CylindricLoad1.heatCapacitor.T
+ pip.plugFlowPipeZeta.plugFlowCore.del.x
+ pip.plugFlowPipeZeta.plugFlowCore.timDel.x
+ pip.plugFlowPipeZeta.vol.dynBal.U
+ senTemIn.T
+ senTemOut.T
+
+ = true
+simulateModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded", stopTime=1000, method="dassl", tolerance=1e-6, resultFile="AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded");
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled");
+Check of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled:
+The model has the same number of unknowns and equations: 156
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 144+2*(size(pump.maxMinTable.columns, 1)+pump.deMultiplex2.n1+pump.deMultiplex2.n2) +pump.criticalDamping.n+pump.vol.dynBal.nPorts
+scalar unknowns and
+ 134+2*size(pump.maxMinTable.columns, 1)+pump.deMultiplex2.n1+pump.deMultiplex2.n2 +pump.criticalDamping.n+(if vessle.use_Xi_in then 1 else (if vessle.use_X_in then 0 else 1))+(if not vessle.use_p_in then 1 else 0)+2*vessle.nPorts+(if not vessle.use_T_in then 1 else 0)+(if not pump.vol.dynBal.use_mWat_flow then 1 else 0)+3*pump.vol.dynBal.nPorts
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 156
+Check of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Movers/PumpsPolynomialBased/Examples/PumpSpeedControlled.mos\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled\\\");\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Movers/PumpsPolynomialBased/Examples/PumpSpeedControlled.mos");
+simulateModel("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled", tolerance=1e-6, stopTime=600.0, method="dassl", resultFile="AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled");
+Translation of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled:
+The DAE has 156 scalar unknowns and 156 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 35
+ Variables: 388
+ Constants: 15 (15 scalars)
+ Parameters: 177 (374 scalars)
+ Unknowns: 196 (160 scalars)
+ Differentiated variables: 6 scalars
+ Equations: 163
+ Nontrivial: 137
+Translated Model
+ Constants: 242 scalars
+ Free parameters: 135 scalars
+ Parameter depending: 38 scalars
+ Outputs: 7 scalars
+ Continuous time states: 4 scalars
+ Time-varying variables: 37 scalars
+ Alias variables: 97 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: { }
+ Sizes after manipulation of the linear systems: { }
+ Sizes of nonlinear systems of equations: {1}
+ Sizes after manipulation of the nonlinear systems: {0}
+ Number of numerical Jacobians: 0
+ Initialization problem
+ Sizes of nonlinear systems of equations: {1}
+ Sizes after manipulation of the nonlinear systems: {1}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ pump.criticalDamping.x[1]
+ pump.criticalDamping.x[2]
+ simpleValve.filter.s[1]
+ simpleValve.filter.s[2]
+
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.HeatExchangers.Examples.HeatingRod");
+Check of AixLib.Fluid.HeatExchangers.Examples.HeatingRod:
+The model has the same number of unknowns and equations: 327
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 322+vol.dynBal.nPorts+heatingRod.vol.dynBal.nPorts
+scalar unknowns and
+ 301+(if conPI.reset <> AixLib.Types.Reset.Input then 1 else 0)+(if bou.use_Xi_in then 1 else (if bou.use_X_in then 0 else 1))+(if not bou.use_p_in then 1 else 0)+2*bou.nPorts+(if not bou.use_T_in then 1 else 0)+(if not vol.dynBal.use_mWat_flow then 1 else 0)+3*vol.dynBal.nPorts+(if not mov.vol.steBal.use_mWat_flow then 1 else 0)+(if (if conPI.reset == AixLib.Types.Reset.Disabled then conPI.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if conPI.reset == AixLib.Types.Reset.Disabled then conPI.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0)+(if not heatingRod.vol.dynBal.use_mWat_flow then 1 else 0)+3*heatingRod.vol.dynBal.nPorts
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 327
+Check of AixLib.Fluid.HeatExchangers.Examples.HeatingRod successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/HeatExchangers/Examples/HeatingRod.mos\",", "AixLib.Fluid.HeatExchangers.Examples.HeatingRod.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.HeatExchangers.Examples.HeatingRod\",", "AixLib.Fluid.HeatExchangers.Examples.HeatingRod.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.HeatExchangers.Examples.HeatingRod.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.HeatExchangers.Examples.HeatingRod\\\");\",", "AixLib.Fluid.HeatExchangers.Examples.HeatingRod.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.HeatExchangers.Examples.HeatingRod.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.HeatExchangers.Examples.HeatingRod.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/HeatExchangers/Examples/HeatingRod.mos");
+simulateModel("AixLib.Fluid.HeatExchangers.Examples.HeatingRod", stopTime=172800, method="Radau", tolerance=1e-6, resultFile="AixLib.Fluid.HeatExchangers.Examples.HeatingRod");
+Translation of AixLib.Fluid.HeatExchangers.Examples.HeatingRod:
+The DAE has 327 scalar unknowns and 327 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 93
+ Variables: 927
+ Constants: 21 (21 scalars)
+ Parameters: 472 (578 scalars)
+ Unknowns: 434 (342 scalars)
+ Differentiated variables: 8 scalars
+ Equations: 376
+ Nontrivial: 305
+Translated Model
+ Constants: 397 scalars
+ Free parameters: 66 scalars
+ Parameter depending: 209 scalars
+ Outputs: 2 scalars
+ Continuous time states: 6 scalars
+ Time-varying variables: 79 scalars
+ Alias variables: 190 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: {2}
+ Sizes after manipulation of the linear systems: {0}
+ Sizes of nonlinear systems of equations: { }
+ Sizes after manipulation of the nonlinear systems: { }
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ conPI.I.y
+ heatingRod.vol.dynBal.U
+ mov.filter.s[1]
+ mov.filter.s[2]
+ THeaOut.T
+ vol.dynBal.U
+
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.HeatExchangers.Examples.HeatingRod.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.Storage.Examples.StorageDetailedExample");
+Check of AixLib.Fluid.Storage.Examples.StorageDetailedExample:
+The model has the same number of unknowns and equations: 2714
+Check of AixLib.Fluid.Storage.Examples.StorageDetailedExample successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageDetailedExample.mos\",", "AixLib.Fluid.Storage.Examples.StorageDetailedExample.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Storage.Examples.StorageDetailedExample\",", "AixLib.Fluid.Storage.Examples.StorageDetailedExample.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Storage.Examples.StorageDetailedExample.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Storage.Examples.StorageDetailedExample\\\");\",", "AixLib.Fluid.Storage.Examples.StorageDetailedExample.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Storage.Examples.StorageDetailedExample.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Storage.Examples.StorageDetailedExample.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageDetailedExample.mos");
+simulateModel("AixLib.Fluid.Storage.Examples.StorageDetailedExample", tolerance=1e-6, stopTime=86400, method="dassl", resultFile="AixLib.Fluid.Storage.Examples.StorageDetailedExample");
+Translation of AixLib.Fluid.Storage.Examples.StorageDetailedExample:
+The DAE has 2714 scalar unknowns and 2714 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 532
+ Variables: 7113
+ Constants: 124 (124 scalars)
+ Parameters: 3345 (3234 scalars)
+ Unknowns: 3644 (2792 scalars)
+ Differentiated variables: 92 scalars
+ Equations: 2756
+ Nontrivial: 2117
+Translated Model
+ Constants: 2426 scalars
+ Free parameters: 222 scalars
+ Parameter depending: 1324 scalars
+ Continuous time states: 66 scalars
+ Time-varying variables: 623 scalars
+ Alias variables: 1555 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: {2, 2, 4, 3, 3, 2, 2, 2, 2, 2, 2, 2, 2, 2, 4, 3, 3, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2}
+ Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0}
+ Sizes of nonlinear systems of equations: {6, 6, 6, 6, 6, 6, 6, 6}
+ Sizes after manipulation of the nonlinear systems: {1, 1, 1, 1, 1, 1, 1, 1}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ bufferStorage.bottomCover.loadIns.T
+ bufferStorage.bottomCover.loadWall.T
+ bufferStorage.heatingCoil1.pipe[1].del.x
+ bufferStorage.heatingCoil1.pipe[1].timDel.x
+ bufferStorage.heatingCoil1.pipe[1].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[1].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[2].del.x
+ bufferStorage.heatingCoil1.pipe[2].timDel.x
+ bufferStorage.heatingCoil1.pipe[2].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[2].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[3].del.x
+ bufferStorage.heatingCoil1.pipe[3].timDel.x
+ bufferStorage.heatingCoil1.pipe[3].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[3].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[4].del.x
+ bufferStorage.heatingCoil1.pipe[4].timDel.x
+ bufferStorage.heatingCoil1.pipe[4].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[4].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[5].del.x
+ bufferStorage.heatingCoil1.pipe[5].timDel.x
+ bufferStorage.heatingCoil1.pipe[5].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[5].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[6].del.x
+ bufferStorage.heatingCoil1.pipe[6].timDel.x
+ bufferStorage.heatingCoil1.pipe[6].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[6].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[7].del.x
+ bufferStorage.heatingCoil1.pipe[7].timDel.x
+ bufferStorage.heatingCoil1.pipe[7].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[7].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[8].del.x
+ bufferStorage.heatingCoil1.pipe[8].timDel.x
+ bufferStorage.heatingCoil1.pipe[8].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[8].vol_b.dynBal.U
+ bufferStorage.layer[1].dynBal.U
+ bufferStorage.layer[2].dynBal.U
+ bufferStorage.layer[3].dynBal.U
+ bufferStorage.layer[4].dynBal.U
+ bufferStorage.layer[5].dynBal.U
+ bufferStorage.layer[6].dynBal.U
+ bufferStorage.layer[7].dynBal.U
+ bufferStorage.layer[8].dynBal.U
+ bufferStorage.layer[9].dynBal.U
+ bufferStorage.layer[10].dynBal.U
+ bufferStorage.storageMantle[1].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[1].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[2].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[2].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[3].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[3].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[4].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[4].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[5].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[5].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[6].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[6].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[7].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[7].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[8].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[8].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[9].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[9].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[10].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[10].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.topCover.loadIns.T
+ bufferStorage.topCover.loadWall.T
+
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.Storage.Examples.StorageDetailedExample.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV");
+Check of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV:
+The model has the same number of unknowns and equations: 220
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 208+2*(size(pump.maxMinTable.columns, 1)+pump.deMultiplex2.n1+pump.deMultiplex2.n2) +pump.criticalDamping.n+pump.vol.dynBal.nPorts
+scalar unknowns and
+ 198+2*size(pump.maxMinTable.columns, 1)+pump.deMultiplex2.n1+pump.deMultiplex2.n2 +pump.criticalDamping.n+(if vessle.use_Xi_in then 1 else (if vessle.use_X_in then 0 else 1))+(if not vessle.use_p_in then 1 else 0)+2*vessle.nPorts+(if not vessle.use_T_in then 1 else 0)+(if not pump.vol.dynBal.use_mWat_flow then 1 else 0)+3*pump.vol.dynBal.nPorts
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 220
+Check of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Movers/PumpsPolynomialBased/Examples/PumpSpeedControlledDpV.mos\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV\\\");\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Movers/PumpsPolynomialBased/Examples/PumpSpeedControlledDpV.mos");
+simulateModel("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV", tolerance=1e-6, stopTime=600.0, method="dassl", resultFile="AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV");
+Translation of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV:
+The DAE has 220 scalar unknowns and 220 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 58
+ Variables: 526
+ Constants: 16 (16 scalars)
+ Parameters: 242 (586 scalars)
+ Unknowns: 268 (224 scalars)
+ Differentiated variables: 8 scalars
+ Equations: 228
+ Nontrivial: 195
+Translated Model
+ Constants: 261 scalars
+ Free parameters: 310 scalars
+ Parameter depending: 59 scalars
+ Outputs: 4 scalars
+ Continuous time states: 6 scalars
+ Time-varying variables: 50 scalars
+ Alias variables: 146 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: { }
+ Sizes after manipulation of the linear systems: { }
+ Sizes of nonlinear systems of equations: {1}
+ Sizes after manipulation of the nonlinear systems: {0}
+ Number of numerical Jacobians: 0
+ Initialization problem
+ Sizes of nonlinear systems of equations: {1}
+ Sizes after manipulation of the nonlinear systems: {1}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ ctrlDpVarN.PID.D.x
+ ctrlDpVarN.PID.I.y
+ pump.criticalDamping.x[1]
+ pump.criticalDamping.x[2]
+ simpleValve.filter.s[1]
+ simpleValve.filter.s[2]
+
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot");
+Check of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot:
+The model has the same number of unknowns and equations: 699
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 691+pipeSupply.vol_b.dynBal.nPorts+pipeSupply.vol_a.dynBal.nPorts+ pipeReturn.vol_b.dynBal.nPorts+pipeReturn.vol_a.dynBal.nPorts
+scalar unknowns and
+ 647+(if sourceIdeal.source.use_Xi_in then 1 else (if sourceIdeal.source.use_X_in then 0 else 1))+(if not sourceIdeal.source.use_p_in then 1 else 0)+2* sourceIdeal.source.nPorts+(if not sourceIdeal.source.use_T_in then 1 else 0)+ (if sourceIdeal.sink.use_Xi_in then 1 else (if sourceIdeal.sink.use_X_in then 0 else 1))+(if not sourceIdeal.sink.use_p_in then 1 else 0)+2*sourceIdeal.sink.nPorts +(if not sourceIdeal.sink.use_T_in then 1 else 0)+(if demand.sink.use_Xi_in then 1 else (if demand.sink.use_X_in then 0 else 1))+(if not demand.sink.use_m_flow_in then 1 else 0)+2*demand.sink.nPorts+(if not demand.sink.use_T_in then 1 else 0)+(if demand.source.use_Xi_in then 1 else ( if demand.source.use_X_in then 0 else 1))+(if not demand.source.use_m_flow_in then 1 else 0)+2*demand.source.nPorts+(if not demand.source.use_T_in then 1 else 0)+(if demand.sourceHeating.use_Xi_in then 1 else (if demand.sourceHeating.use_X_in then 0 else 1))+(if not demand.sourceHeating.use_m_flow_in then 1 else 0)+2* demand.sourceHeating.nPorts+(if not demand.sourceHeating.use_T_in then 1 else 0)+(if demand.sinkHeating.use_Xi_in then 1 else (if demand.sinkHeating.use_X_in then 0 else 1))+(if not demand.sinkHeating.use_p_in then 1 else 0)+2* demand.sinkHeating.nPorts+(if not demand.sinkHeating.use_T_in then 1 else 0)+ (if not demand.heaPum.eva.vol.steBal.use_mWat_flow then 1 else 0)+(if not pipeSupply.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*pipeSupply.vol_b.dynBal.nPorts +(if not pipeSupply.vol_a.dynBal.use_mWat_flow then 1 else 0)+3* pipeSupply.vol_a.dynBal.nPorts+(if not pipeReturn.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*pipeReturn.vol_b.dynBal.nPorts+(if not pipeReturn.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*pipeReturn.vol_a.dynBal.nPorts
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 699
+Check of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Demands/Examples/OpenLoopHeatPumpCarnot.mos\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot\\\");\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Demands/Examples/OpenLoopHeatPumpCarnot.mos");
+translateModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot");
+Translation of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot:
+The DAE has 699 scalar unknowns and 699 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 145
+ Variables: 1843
+ Constants: 38 (38 scalars)
+ Parameters: 847 (817 scalars)
+ Unknowns: 958 (725 scalars)
+ Differentiated variables: 15 scalars
+ Equations: 799
+ Nontrivial: 663
+Translated Model
+ Constants: 653 scalars
+ Free parameters: 145 scalars
+ Parameter depending: 165 scalars
+ Continuous time states: 11 scalars
+ Time-varying variables: 163 scalars
+ Alias variables: 454 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: { }
+ Sizes after manipulation of the linear systems: { }
+ Sizes of nonlinear systems of equations: {13, 8}
+ Sizes after manipulation of the nonlinear systems: {1, 1}
+ Number of numerical Jacobians: 0
+ Initialization problem
+ Sizes of nonlinear systems of equations: {13, 8}
+ Sizes after manipulation of the nonlinear systems: {1, 1}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ demand.senT_return.T
+ demand.senT_supply.T
+ pControl.I.y
+ pipeReturn.del.x
+ pipeReturn.timDel.x
+ pipeReturn.vol_a.dynBal.U
+ pipeReturn.vol_b.dynBal.U
+ pipeSupply.del.x
+ pipeSupply.timDel.x
+ pipeSupply.vol_a.dynBal.U
+ pipeSupply.vol_b.dynBal.U
+
+ = true
+simulateModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot", stopTime=100000, method="dassl", tolerance=1e-006, resultFile="AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot");
+Not possible to open file "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.mat": No such file or directory
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances");
+Check of AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances:
+The model has the same number of unknowns and equations: 60
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 60
+scalar unknowns and
+ 48+(if sou1.use_Xi_in then 1 else (if sou1.use_X_in then 0 else 1))+(if not sou1.use_p_in then 1 else 0)+2*sou1.nPorts+(if not sou1.use_T_in then 1 else 0) +(if sin1.use_Xi_in then 1 else (if sin1.use_X_in then 0 else 1))+(if not sin1.use_p_in then 1 else 0)+2*sin1.nPorts+(if not sin1.use_T_in then 1 else 0)
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 60
+Check of AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/FixedResistances/Examples/CompareFixedResistances.mos\",", "AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances\",", "AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances\\\");\",", "AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/FixedResistances/Examples/CompareFixedResistances.mos");
+simulateModel("AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances", stopTime=3600, method="dassl", tolerance=1e-006, resultFile="AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances");
+Translation of AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances:
+The DAE has 60 scalar unknowns and 60 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 12
+ Variables: 181
+ Constants: 6 (6 scalars)
+ Parameters: 87 (85 scalars)
+ Unknowns: 88 (60 scalars)
+ Equations: 88
+ Nontrivial: 81
+Translated Model
+ Constants: 66 scalars
+ Free parameters: 22 scalars
+ Parameter depending: 9 scalars
+ Time-varying variables: 7 scalars
+ Alias variables: 47 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: { }
+ Sizes after manipulation of the linear systems: { }
+ Sizes of nonlinear systems of equations: { }
+ Sizes after manipulation of the nonlinear systems: { }
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl");
+Check of AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl:
+The model has the same number of unknowns and equations: 181
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 175+combinedHeatPower.vol.dynBal.nPorts+size(combinedHeatPower.combiTable1Ds.columns, 1)
+scalar unknowns and
+ 161+size(combinedHeatPower.combiTable1Ds.columns, 1)+2*source.nPorts+(if not source.use_m_flow_in then 1 else 0)+(if not source.use_T_in then 1 else 0)+( if not source.use_X_in then 1 else 0)+2*sink.nPorts+(if not sink.use_p_in then 1 else 0)+(if not sink.use_T_in then 1 else 0)+(if not sink.use_X_in then 1 else 0)+(if not combinedHeatPower.vol.dynBal.use_mWat_flow then 1 else 0)+3*combinedHeatPower.vol.dynBal.nPorts
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 181
+Check of AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/BoilerCHP/Examples/CHPSystemNoControl.mos\",", "AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl\",", "AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl\\\");\",", "AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/BoilerCHP/Examples/CHPSystemNoControl.mos");
+simulateModel("AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl", tolerance=1e-06, stopTime=300, method="dassl", resultFile="AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl");
+Translation of AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl:
+The DAE has 181 scalar unknowns and 181 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 38
+ Variables: 432
+ Constants: 5 (5 scalars)
+ Parameters: 195 (229 scalars)
+ Unknowns: 232 (185 scalars)
+ Differentiated variables: 5 scalars
+ Equations: 210
+ Nontrivial: 170
+Translated Model
+ Constants: 143 scalars
+ Free parameters: 58 scalars
+ Parameter depending: 71 scalars
+ Continuous time states: 3 scalars
+ Time-varying variables: 38 scalars
+ Alias variables: 109 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: {5}
+ Sizes after manipulation of the linear systems: {0}
+ Sizes of nonlinear systems of equations: { }
+ Sizes after manipulation of the nonlinear systems: { }
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ combinedHeatPower.internalCapacity.T
+ combinedHeatPower.senTCold.T
+ combinedHeatPower.senTHot.T
+
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe");
+Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe:
+The model has the same number of unknowns and equations: 804
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 796+pip.vol.dynBal.nPorts+pip1.vol.dynBal.nPorts+pip2.vol.dynBal.nPorts+ pip3.vol.dynBal.nPorts
+scalar unknowns and
+ 740+(if sin.use_Xi_in then 1 else (if sin.use_X_in then 0 else 1))+(if not sin.use_p_in then 1 else 0)+2*sin.nPorts+(if not sin.use_T_in then 1 else 0)+ (if sou.use_Xi_in then 1 else (if sou.use_X_in then 0 else 1))+(if not sou.use_m_flow_in then 1 else 0)+2*sou.nPorts+(if not sou.use_T_in then 1 else 0)+(if sin1.use_Xi_in then 1 else (if sin1.use_X_in then 0 else 1))+(if not sin1.use_p_in then 1 else 0)+2*sin1.nPorts+(if not sin1.use_T_in then 1 else 0)+(if sou1.use_Xi_in then 1 else (if sou1.use_X_in then 0 else 1))+(if not sou1.use_m_flow_in then 1 else 0)+2*sou1.nPorts+(if not sou1.use_T_in then 1 else 0)+(if sin2.use_Xi_in then 1 else (if sin2.use_X_in then 0 else 1)) +(if not sin2.use_p_in then 1 else 0)+2*sin2.nPorts+(if not sin2.use_T_in then 1 else 0)+(if sou2.use_Xi_in then 1 else (if sou2.use_X_in then 0 else 1)) +(if not sou2.use_m_flow_in then 1 else 0)+2*sou2.nPorts+(if not sou2.use_T_in then 1 else 0)+(if sin3.use_Xi_in then 1 else (if sin3.use_X_in then 0 else 1))+(if not sin3.use_p_in then 1 else 0)+2*sin3.nPorts+(if not sin3.use_T_in then 1 else 0)+(if sou3.use_Xi_in then 1 else (if sou3.use_X_in then 0 else 1))+(if not sou3.use_m_flow_in then 1 else 0)+2*sou3.nPorts+(if not sou3.use_T_in then 1 else 0)+(if not pip.vol.dynBal.use_mWat_flow then 1 else 0)+3*pip.vol.dynBal.nPorts+(if not pip1.vol.dynBal.use_mWat_flow then 1 else 0)+3*pip1.vol.dynBal.nPorts+(if not pip2.vol.dynBal.use_mWat_flow then 1 else 0)+3*pip2.vol.dynBal.nPorts+(if not pip3.vol.dynBal.use_mWat_flow then 1 else 0)+3*pip3.vol.dynBal.nPorts
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 804
+Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/DHCPipe.mos\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe\\\");\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/DHCPipe.mos");
+translateModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe");
+Translation of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe:
+The DAE has 804 scalar unknowns and 804 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 144
+ Variables: 2246
+ Constants: 37 (37 scalars)
+ Parameters: 1101 (1073 scalars)
+ Unknowns: 1108 (828 scalars)
+ Differentiated variables: 33 scalars
+ Equations: 923
+ Nontrivial: 790
+Translated Model
+ Constants: 721 scalars
+ Free parameters: 205 scalars
+ Parameter depending: 321 scalars
+ Continuous time states: 29 scalars
+ Time-varying variables: 177 scalars
+ Alias variables: 514 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: {2, 2}
+ Sizes after manipulation of the linear systems: {0, 0}
+ Sizes of nonlinear systems of equations: {6}
+ Sizes after manipulation of the nonlinear systems: {1}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ pip.Q_gai
+ pip.Q_los
+ pip.vol.dynBal.U
+ pip1.pipCor.del.x
+ pip1.pipCor.timDel.x
+ pip1.Q_gai
+ pip1.Q_los
+ pip1.vol.dynBal.U
+ pip2.cylHeaTra1.CylindricLoad1.heatCapacitor.T
+ pip2.cylHeaTra2.CylindricLoad1.heatCapacitor.T
+ pip2.cylHeaTra3.CylindricLoad1.heatCapacitor.T
+ pip2.pipCor.del.x
+ pip2.pipCor.timDel.x
+ pip2.Q_gai
+ pip2.Q_los
+ pip2.vol.dynBal.U
+ pip3.pipCor.del.x
+ pip3.pipCor.timDel.x
+ pip3.Q_gai
+ pip3.Q_los
+ pip3.vol.dynBal.U
+ senTemIn.T
+ senTemIn1.T
+ senTemIn2.T
+ senTemIn3.T
+ senTemOut.T
+ senTemOut1.T
+ senTemOut2.T
+ senTemOut3.T
+
+ = true
+simulateModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe", stopTime=3600, method="dassl", tolerance=1e-6, resultFile="AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe");
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe");
+Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe:
+The model has the same number of unknowns and equations: 175
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 173+pip.vol.dynBal.nPorts
+scalar unknowns and
+ 159+(if sin.use_Xi_in then 1 else (if sin.use_X_in then 0 else 1))+(if not sin.use_p_in then 1 else 0)+2*sin.nPorts+(if not sin.use_T_in then 1 else 0)+ (if sou.use_Xi_in then 1 else (if sou.use_X_in then 0 else 1))+(if not sou.use_m_flow_in then 1 else 0)+2*sou.nPorts+(if not sou.use_T_in then 1 else 0)+(if not pip.vol.dynBal.use_mWat_flow then 1 else 0)+3* pip.vol.dynBal.nPorts
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 175
+Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/StaticPipe.mos\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe\\\");\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/StaticPipe.mos");
+translateModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe");
+Translation of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe:
+The DAE has 175 scalar unknowns and 175 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 33
+ Variables: 506
+ Constants: 10 (10 scalars)
+ Parameters: 251 (244 scalars)
+ Unknowns: 245 (181 scalars)
+ Differentiated variables: 4 scalars
+ Equations: 205
+ Nontrivial: 171
+Translated Model
+ Constants: 185 scalars
+ Free parameters: 45 scalars
+ Parameter depending: 61 scalars
+ Continuous time states: 3 scalars
+ Time-varying variables: 31 scalars
+ Alias variables: 113 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: { }
+ Sizes after manipulation of the linear systems: { }
+ Sizes of nonlinear systems of equations: { }
+ Sizes after manipulation of the nonlinear systems: { }
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ pip.vol.dynBal.U
+ senTemIn.T
+ senTemOut.T
+
+ = true
+simulateModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe", stopTime=1000, method="dassl", tolerance=1e-006, resultFile="AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe");
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled");
+Check of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled:
+The model has the same number of unknowns and equations: 151
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 140+2*(size(pump.maxMinTable.columns, 1)+pump.deMultiplex3_1.n1+pump.deMultiplex3_1.n2) +pump.criticalDamping.n+pump.vol.dynBal.nPorts
+scalar unknowns and
+ 130+2*size(pump.maxMinTable.columns, 1)+pump.deMultiplex3_1.n1+pump.deMultiplex3_1.n2 +pump.criticalDamping.n+(if vessle.use_Xi_in then 1 else (if vessle.use_X_in then 0 else 1))+(if not vessle.use_p_in then 1 else 0)+2*vessle.nPorts+(if not vessle.use_T_in then 1 else 0)+(if not pump.vol.dynBal.use_mWat_flow then 1 else 0)+3*pump.vol.dynBal.nPorts
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 151
+Check of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Movers/PumpsPolynomialBased/Examples/PumpHeadControlled.mos\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled\\\");\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Movers/PumpsPolynomialBased/Examples/PumpHeadControlled.mos");
+simulateModel("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled", tolerance=1e-6, stopTime=600, method="dassl", resultFile="AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled");
+Translation of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled:
+The DAE has 151 scalar unknowns and 151 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 34
+ Variables: 378
+ Constants: 9 (9 scalars)
+ Parameters: 177 (481 scalars)
+ Unknowns: 192 (155 scalars)
+ Differentiated variables: 5 scalars
+ Equations: 158
+ Nontrivial: 131
+Translated Model
+ Constants: 136 scalars
+ Free parameters: 253 scalars
+ Parameter depending: 127 scalars
+ Outputs: 7 scalars
+ Continuous time states: 3 scalars
+ Time-varying variables: 36 scalars
+ Alias variables: 93 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: { }
+ Sizes after manipulation of the linear systems: { }
+ Sizes of nonlinear systems of equations: {1}
+ Sizes after manipulation of the nonlinear systems: {0}
+ Number of numerical Jacobians: 0
+ Initialization problem
+ Sizes of nonlinear systems of equations: {1}
+ Sizes after manipulation of the nonlinear systems: {1}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ pump.criticalDamping.x[1]
+ simpleValve.filter.s[1]
+ simpleValve.filter.s[2]
+
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp");
+Check of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp:
+The model has the same number of unknowns and equations: 522
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 514+pipeSupply.vol_b.dynBal.nPorts+pipeSupply.vol_a.dynBal.nPorts+ pipeReturn.vol_b.dynBal.nPorts+pipeReturn.vol_a.dynBal.nPorts
+scalar unknowns and
+ 479+(if sourceIdeal.source.use_Xi_in then 1 else (if sourceIdeal.source.use_X_in then 0 else 1))+(if not sourceIdeal.source.use_p_in then 1 else 0)+2* sourceIdeal.source.nPorts+(if not sourceIdeal.source.use_T_in then 1 else 0)+ (if sourceIdeal.sink.use_Xi_in then 1 else (if sourceIdeal.sink.use_X_in then 0 else 1))+(if not sourceIdeal.sink.use_p_in then 1 else 0)+2*sourceIdeal.sink.nPorts +(if not sourceIdeal.sink.use_T_in then 1 else 0)+(if demand.sink.use_Xi_in then 1 else (if demand.sink.use_X_in then 0 else 1))+(if not demand.sink.use_m_flow_in then 1 else 0)+2*demand.sink.nPorts+(if not demand.sink.use_T_in then 1 else 0)+(if demand.source.use_Xi_in then 1 else ( if demand.source.use_X_in then 0 else 1))+(if not demand.source.use_m_flow_in then 1 else 0)+2*demand.source.nPorts+(if not demand.source.use_T_in then 1 else 0)+(if not pipeSupply.vol_b.dynBal.use_mWat_flow then 1 else 0)+3* pipeSupply.vol_b.dynBal.nPorts+(if not pipeSupply.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*pipeSupply.vol_a.dynBal.nPorts+(if not pipeReturn.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*pipeReturn.vol_b.dynBal.nPorts+(if not pipeReturn.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*pipeReturn.vol_a.dynBal.nPorts
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 522
+Check of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Demands/Examples/OpenLoopVarTSupplyDp.mos\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp\\\");\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Demands/Examples/OpenLoopVarTSupplyDp.mos");
+translateModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp");
+Translation of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp:
+The DAE has 522 scalar unknowns and 522 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 105
+ Variables: 1376
+ Constants: 25 (25 scalars)
+ Parameters: 625 (601 scalars)
+ Unknowns: 726 (538 scalars)
+ Differentiated variables: 15 scalars
+ Equations: 623
+ Nontrivial: 504
+Translated Model
+ Constants: 457 scalars
+ Free parameters: 119 scalars
+ Parameter depending: 129 scalars
+ Continuous time states: 11 scalars
+ Time-varying variables: 123 scalars
+ Alias variables: 336 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: { }
+ Sizes after manipulation of the linear systems: { }
+ Sizes of nonlinear systems of equations: {8}
+ Sizes after manipulation of the nonlinear systems: {1}
+ Number of numerical Jacobians: 0
+ Initialization problem
+ Sizes of nonlinear systems of equations: {8}
+ Sizes after manipulation of the nonlinear systems: {1}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ demand.senT_return.T
+ demand.senT_supply.T
+ pControl.I.y
+ pipeReturn.del.x
+ pipeReturn.timDel.x
+ pipeReturn.vol_a.dynBal.U
+ pipeReturn.vol_b.dynBal.U
+ pipeSupply.del.x
+ pipeSupply.timDel.x
+ pipeSupply.vol_a.dynBal.U
+ pipeSupply.vol_b.dynBal.U
+
+ = true
+simulateModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp", stopTime=100000, method="dassl", tolerance=1e-006, resultFile="AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp");
+Not possible to open file "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.mat": No such file or directory
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.BoilerCHP.Examples.CHPSystem");
+Check of AixLib.Fluid.BoilerCHP.Examples.CHPSystem:
+The model has the same number of unknowns and equations: 367
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 361+combinedHeatPower.vol.dynBal.nPorts+size(combinedHeatPower.combiTable1Ds.columns, 1)
+scalar unknowns and
+ 347+size(combinedHeatPower.combiTable1Ds.columns, 1)+2*source.nPorts+(if not source.use_m_flow_in then 1 else 0)+(if not source.use_T_in then 1 else 0)+( if not source.use_X_in then 1 else 0)+2*sink.nPorts+(if not sink.use_p_in then 1 else 0)+(if not sink.use_T_in then 1 else 0)+(if not sink.use_X_in then 1 else 0)+(if not combinedHeatPower.vol.dynBal.use_mWat_flow then 1 else 0)+3*combinedHeatPower.vol.dynBal.nPorts
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 367
+Check of AixLib.Fluid.BoilerCHP.Examples.CHPSystem successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/BoilerCHP/Examples/CHPSystem.mos\",", "AixLib.Fluid.BoilerCHP.Examples.CHPSystem.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.BoilerCHP.Examples.CHPSystem\",", "AixLib.Fluid.BoilerCHP.Examples.CHPSystem.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.BoilerCHP.Examples.CHPSystem.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.BoilerCHP.Examples.CHPSystem\\\");\",", "AixLib.Fluid.BoilerCHP.Examples.CHPSystem.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.BoilerCHP.Examples.CHPSystem.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.BoilerCHP.Examples.CHPSystem.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/BoilerCHP/Examples/CHPSystem.mos");
+simulateModel("AixLib.Fluid.BoilerCHP.Examples.CHPSystem", tolerance=1e-06, stopTime=1200, method="dassl", resultFile="AixLib.Fluid.BoilerCHP.Examples.CHPSystem");
+Translation of AixLib.Fluid.BoilerCHP.Examples.CHPSystem:
+The DAE has 367 scalar unknowns and 367 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 105
+ Variables: 786
+ Constants: 8 (8 scalars)
+ Parameters: 360 (394 scalars)
+ Unknowns: 418 (371 scalars)
+ Differentiated variables: 8 scalars
+ Equations: 404
+ Nontrivial: 360
+Translated Model
+ Constants: 177 scalars
+ Free parameters: 143 scalars
+ Parameter depending: 115 scalars
+ Continuous time states: 6 scalars
+ Time-varying variables: 112 scalars
+ Alias variables: 226 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: { }
+ Sizes after manipulation of the linear systems: { }
+ Sizes of nonlinear systems of equations: {8, 9}
+ Sizes after manipulation of the nonlinear systems: {1, 1}
+ Number of numerical Jacobians: 0
+ Initialization problem
+ Sizes of linear systems of equations: {5}
+ Sizes after manipulation of the linear systems: {0}
+
+Selected continuous time states
+Statically selected continuous time states
+ combinedHeatPower.elControl.I.y
+ combinedHeatPower.senTCold.T
+ combinedHeatPower.senTHot.T
+ combinedHeatPower.thControl.PI.I.y
+ combinedHeatPower.thControl.PI1.I.y
+ combinedHeatPower.vol.dynBal.medium.T
+
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.BoilerCHP.Examples.CHPSystem.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst");
+Check of AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst:
+The model has the same number of unknowns and equations: 250
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 248+vol.dynBal.nPorts
+scalar unknowns and
+ 237+(if sou.use_Xi_in then 1 else (if sou.use_X_in then 0 else 1))+(if not sou.use_p_in then 1 else 0)+2*sou.nPorts+(if not sou.use_T_in then 1 else 0)+ (if not dpControlled_dp.mov.vol.steBal.use_mWat_flow then 1 else 0)+(if not vol.dynBal.use_mWat_flow then 1 else 0)+3*vol.dynBal.nPorts
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 250
+Check of AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Movers/DpControlledMovers/Examples/DpConst.mos\",", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst\",", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst\\\");\",", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Movers/DpControlledMovers/Examples/DpConst.mos");
+simulateModel("AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst", startTime=0, stopTime=3600, tolerance=1e-6, method="dassl", resultFile="AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst");
+Translation of AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst:
+The DAE has 250 scalar unknowns and 250 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 82
+ Variables: 814
+ Constants: 19 (19 scalars)
+ Parameters: 465 (949 scalars)
+ Unknowns: 330 (265 scalars)
+ Differentiated variables: 7 scalars
+ Equations: 284
+ Nontrivial: 236
+Translated Model
+ Constants: 686 scalars
+ Free parameters: 51 scalars
+ Parameter depending: 271 scalars
+ Outputs: 1 scalars
+ Continuous time states: 5 scalars
+ Time-varying variables: 61 scalars
+ Alias variables: 164 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: { }
+ Sizes after manipulation of the linear systems: { }
+ Sizes of nonlinear systems of equations: {3, 1}
+ Sizes after manipulation of the nonlinear systems: {1, 1}
+ Number of numerical Jacobians: 0
+ Initialization problem
+ Sizes of nonlinear systems of equations: {3, 1, 1}
+ Sizes after manipulation of the nonlinear systems: {1, 0, 1}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ dpControlled_dp.mov.filter.s[1]
+ dpControlled_dp.mov.filter.s[2]
+ integrator.y
+ val.filter.s[1]
+ val.filter.s[2]
+
+Finished
+ = true
+
+
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation");
+Check of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation:
+The model has the same number of unknowns and equations: 5514
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 3787+32*enthalpyExchanger.n+16*enthalpyExchanger.airDuct2.heatTransfer.n+18* enthalpyExchanger.airDuct2.massTransfer.n+16*enthalpyExchanger.airDuct1.heatTransfer.n +18*enthalpyExchanger.airDuct1.massTransfer.n+5*enthalpyExchanger.membrane.heatTransfer.n +enthalpyExchanger.membrane.massTransfer.n+2*enthalpyExchanger.airDuct2.vol[1].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[2].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[3].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[4].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[5].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[6].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[7].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[8].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[9].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[10].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[11].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[12].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[13].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[14].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[15].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[1].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[2].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[3].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[4].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[5].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[6].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[7].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[8].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[9].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[10].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[11].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[12].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[13].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[14].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[15].dynBal.nPorts+max([size(bondaryEta.columns, 1); size(bondaryEta.offset, 1)])+max([size(bondaryOda.columns, 1); size( bondaryOda.offset, 1)])+max([size(Results.columns, 1); size(Results.offset, 1)]) +2*fan.vol.dynBal.nPorts+2*fan1.vol.dynBal.nPorts
+scalar unknowns and
+ 3439+17*enthalpyExchanger.airDuct2.heatTransfer.n+19*enthalpyExchanger.airDuct2.massTransfer.n +3*(if enthalpyExchanger.couFloArr then 2*enthalpyExchanger.n else 0)+17* enthalpyExchanger.airDuct1.heatTransfer.n+19*enthalpyExchanger.airDuct1.massTransfer.n +7*enthalpyExchanger.membrane.heatTransfer.n+3*enthalpyExchanger.membrane.massTransfer.n +2*(if enthalpyExchanger.useConPer then 1 else 0)+32*enthalpyExchanger.n+(if souEta.use_Xi_in then 2 else (if souEta.use_X_in then 1 else 3))+3* souEta.nPorts+(if not souEta.use_p_in then 1 else 0)+(if not souEta.use_T_in then 1 else 0)+(if sinEha.use_Xi_in then 2 else (if sinEha.use_X_in then 1 else 3))+3*sinEha.nPorts+(if not sinEha.use_p_in then 1 else 0)+(if not sinEha.use_T_in then 1 else 0)+(if souOda.use_Xi_in then 2 else (if souOda.use_X_in then 1 else 3))+3*souOda.nPorts+(if not souOda.use_p_in then 1 else 0)+(if not souOda.use_T_in then 1 else 0)+(if sinSup.use_Xi_in then 2 else (if sinSup.use_X_in then 1 else 3))+3*sinSup.nPorts+(if not sinSup.use_p_in then 1 else 0)+(if not sinSup.use_T_in then 1 else 0)+max([ size(bondaryEta.columns, 1); size(bondaryEta.offset, 1)])+max([size( bondaryOda.columns, 1); size(bondaryOda.offset, 1)])+max([size(Results.columns, 1); size(Results.offset, 1)])+(if conPID.reset <> AixLib.Types.Reset.Input then 1 else 0)+(if conPID1.reset <> AixLib.Types.Reset.Input then 1 else 0)+5 *enthalpyExchanger.airDuct2.vol[1].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[2].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[3].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[4].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[5].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[6].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[7].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[8].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[9].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[10].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[11].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[12].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[13].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[14].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[15].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[1].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[2].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[3].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[4].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[5].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[6].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[7].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[8].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[9].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[10].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[11].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[12].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[13].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[14].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[15].dynBal.nPorts +(if not fan.vol.dynBal.use_mWat_flow then 1 else 0)+5*fan.vol.dynBal.nPorts+ (if (if conPID.reset == AixLib.Types.Reset.Disabled then conPID.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if conPID.reset == AixLib.Types.Reset.Disabled then conPID.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0)+(if not fan1.vol.dynBal.use_mWat_flow then 1 else 0)+5*fan1.vol.dynBal.nPorts+( if (if conPID1.reset == AixLib.Types.Reset.Disabled then conPID1.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if conPID1.reset == AixLib.Types.Reset.Disabled then conPID1.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0)
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 5514
+Check of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/MassExchangers/MembraneBasedEnthalpyExchangers/Validation/DynamicValidation.mos\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation\\\");\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/MassExchangers/MembraneBasedEnthalpyExchangers/Validation/DynamicValidation.mos");
+simulateModel("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation", stopTime=7200, numberOfIntervals=0, outputInterval=2, method="dassl",tolerance=1E-6, resultFile="AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation");
+Translation of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation:
+The DAE has 5514 scalar unknowns and 5514 scalar equations.
+Redundant consistent initial conditions.
+Removed the following equations which are redundant and consistent:
+ fan1.vol.p_start = fan1.p_start;
+ if (enthalpyExchanger.airDuct2.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[1].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[1].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[1].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[1].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[1].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[2].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[2].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[2].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[2].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[2].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[3].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[3].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[3].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[3].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[3].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[4].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[4].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[4].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[4].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[4].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[5].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[5].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[5].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[5].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[5].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[6].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[6].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[6].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[6].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[6].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[7].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[7].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[7].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[7].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[7].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[8].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[8].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[8].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[8].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[8].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[9].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[9].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[9].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[9].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[9].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[10].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[10].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[10].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[10].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[10].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[11].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[11].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[11].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[11].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[11].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[12].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[12].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[12].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[12].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[12].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[13].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[13].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[13].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[13].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[13].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[14].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[14].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[14].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[14].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[14].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[15].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[15].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[15].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[15].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[15].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[1].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[1].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[1].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[1].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[1].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[2].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[2].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[2].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[2].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[2].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[3].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[3].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[3].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[3].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[3].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[4].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[4].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[4].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[4].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[4].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[5].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[5].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[5].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[5].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[5].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[6].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[6].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[6].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[6].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[6].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[7].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[7].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[7].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[7].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[7].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[8].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[8].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[8].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[8].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[8].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[9].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[9].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[9].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[9].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[9].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[10].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[10].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[10].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[10].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[10].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[11].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[11].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[11].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[11].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[11].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[12].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[12].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[12].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[12].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[12].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[13].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[13].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[13].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[13].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[13].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[14].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[14].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[14].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[14].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[14].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[15].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[15].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[15].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[15].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[15].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (fan.vol.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.FixedInitial) then
+ if (fan.vol.dynBal.initialize_p) then
+ fan.vol.dynBal.medium.p = fan.vol.dynBal.p_start;
+ end if;
+ else
+ if (fan.vol.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. SteadyStateInitial) then
+ if (fan.vol.dynBal.initialize_p) then
+ der(fan.vol.dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+
+This required evaluation of
+the interactive parameters
+ fan.p_start(start = 101325)
+ fan1.p_start(start = 101325)
+ sinEha.p(start = 101325)
+ sinSup.p(start = 101325)
+ souEta.p(start = 101325)
+ souOda.p(start = 101325)
+
+The redundancies involve
+initial equations:
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ souOda.p = fan.vol.dynBal.p_start;
+ souEta.p = fan1.vol.dynBal.p_start;
+
+
+Statistics
+
+Original Model
+ Number of components: 678
+ Variables: 7286
+ Constants: 168 (168 scalars)
+ Parameters: 2808 (3271 scalars)
+ Unknowns: 4310 (5682 scalars)
+ Differentiated variables: 129 scalars
+ Equations: 2965
+ Nontrivial: 2307
+Translated Model
+ Constants: 2677 scalars
+ Free parameters: 251 scalars
+ Parameter depending: 1421 scalars
+ Continuous time states: 97 scalars
+ Time-varying variables: 1772 scalars
+ Alias variables: 3000 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: {2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3}
+ Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2}
+ Sizes of nonlinear systems of equations: {1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1}
+ Sizes after manipulation of the nonlinear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0}
+ Number of numerical Jacobians: 0
+ Initialization problem
+ Sizes of nonlinear systems of equations: {1, 1}
+ Sizes after manipulation of the nonlinear systems: {0, 0}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ conPID.I.y
+ conPID1.I.y
+ enthalpyExchanger.airDuct1.senRelHum.phi
+ enthalpyExchanger.airDuct1.senTem.T
+ enthalpyExchanger.airDuct1.vol[1].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[1].dynBal.U
+ enthalpyExchanger.airDuct1.vol[2].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[2].dynBal.U
+ enthalpyExchanger.airDuct1.vol[3].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[3].dynBal.U
+ enthalpyExchanger.airDuct1.vol[4].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[4].dynBal.U
+ enthalpyExchanger.airDuct1.vol[5].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[5].dynBal.U
+ enthalpyExchanger.airDuct1.vol[6].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[6].dynBal.U
+ enthalpyExchanger.airDuct1.vol[7].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[7].dynBal.U
+ enthalpyExchanger.airDuct1.vol[8].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[8].dynBal.U
+ enthalpyExchanger.airDuct1.vol[9].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[9].dynBal.U
+ enthalpyExchanger.airDuct1.vol[10].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[10].dynBal.U
+ enthalpyExchanger.airDuct1.vol[11].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[11].dynBal.U
+ enthalpyExchanger.airDuct1.vol[12].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[12].dynBal.U
+ enthalpyExchanger.airDuct1.vol[13].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[13].dynBal.U
+ enthalpyExchanger.airDuct1.vol[14].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[14].dynBal.U
+ enthalpyExchanger.airDuct1.vol[15].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[15].dynBal.U
+ enthalpyExchanger.airDuct2.senRelHum.phi
+ enthalpyExchanger.airDuct2.senTem.T
+ enthalpyExchanger.airDuct2.vol[1].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[1].dynBal.U
+ enthalpyExchanger.airDuct2.vol[2].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[2].dynBal.U
+ enthalpyExchanger.airDuct2.vol[3].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[3].dynBal.U
+ enthalpyExchanger.airDuct2.vol[4].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[4].dynBal.U
+ enthalpyExchanger.airDuct2.vol[5].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[5].dynBal.U
+ enthalpyExchanger.airDuct2.vol[6].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[6].dynBal.U
+ enthalpyExchanger.airDuct2.vol[7].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[7].dynBal.U
+ enthalpyExchanger.airDuct2.vol[8].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[8].dynBal.U
+ enthalpyExchanger.airDuct2.vol[9].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[9].dynBal.U
+ enthalpyExchanger.airDuct2.vol[10].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[10].dynBal.U
+ enthalpyExchanger.airDuct2.vol[11].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[11].dynBal.U
+ enthalpyExchanger.airDuct2.vol[12].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[12].dynBal.U
+ enthalpyExchanger.airDuct2.vol[13].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[13].dynBal.U
+ enthalpyExchanger.airDuct2.vol[14].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[14].dynBal.U
+ enthalpyExchanger.airDuct2.vol[15].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[15].dynBal.U
+ enthalpyExchanger.membrane.heatTransfer.Ts[1]
+ enthalpyExchanger.membrane.heatTransfer.Ts[2]
+ enthalpyExchanger.membrane.heatTransfer.Ts[3]
+ enthalpyExchanger.membrane.heatTransfer.Ts[4]
+ enthalpyExchanger.membrane.heatTransfer.Ts[5]
+ enthalpyExchanger.membrane.heatTransfer.Ts[6]
+ enthalpyExchanger.membrane.heatTransfer.Ts[7]
+ enthalpyExchanger.membrane.heatTransfer.Ts[8]
+ enthalpyExchanger.membrane.heatTransfer.Ts[9]
+ enthalpyExchanger.membrane.heatTransfer.Ts[10]
+ enthalpyExchanger.membrane.heatTransfer.Ts[11]
+ enthalpyExchanger.membrane.heatTransfer.Ts[12]
+ enthalpyExchanger.membrane.heatTransfer.Ts[13]
+ enthalpyExchanger.membrane.heatTransfer.Ts[14]
+ enthalpyExchanger.membrane.heatTransfer.Ts[15]
+ fan.filter.s[1]
+ fan.filter.s[2]
+ fan.vol.dynBal.medium.Xi[1]
+ fan.vol.dynBal.U
+ fan1.filter.s[1]
+ fan1.filter.s[2]
+ fan1.vol.dynBal.medium.Xi[1]
+ fan1.vol.dynBal.U
+ senMasFraEha.X
+ senMasFraEta.X
+ senMasFraOda.X
+ senMasFraSup.X
+ senTemEha.T
+ senTemEta.T
+ senTemOda.T
+ senTemSup.T
+
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.Storage.Examples.StorageSimpleExample");
+Check of AixLib.Fluid.Storage.Examples.StorageSimpleExample:
+The model has the same number of unknowns and equations: 964
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 938+storageSimple.layer[1].dynBal.nPorts+storageSimple.layer[2].dynBal.nPorts+ storageSimple.layer[3].dynBal.nPorts+storageSimple.layer_HE[1].dynBal.nPorts+ storageSimple.layer_HE[2].dynBal.nPorts+storageSimple.layer_HE[3].dynBal.nPorts +2*storageSimple.n+heatingRod.vol.dynBal.nPorts+simpleConsumer.volume.dynBal.nPorts +pumpGen.vol.dynBal.nPorts+pumpCon.vol.dynBal.nPorts
+scalar unknowns and
+ 869+(if storageSimple.use_TOut then 2*storageSimple.n else 0)+(if pressureBoundary.use_Xi_in then 1 else (if pressureBoundary.use_X_in then 0 else 1))+(if not pressureBoundary.use_p_in then 1 else 0)+2*pressureBoundary.nPorts +(if not pressureBoundary.use_T_in then 1 else 0)+(if pressureBoundary1.use_Xi_in then 1 else (if pressureBoundary1.use_X_in then 0 else 1))+(if not pressureBoundary1.use_p_in then 1 else 0)+2*pressureBoundary1.nPorts+(if not pressureBoundary1.use_T_in then 1 else 0)+(if PIDHR.reset <> AixLib.Types.Reset. Input then 1 else 0)+(if PIDPumpGen.reset <> AixLib.Types.Reset.Input then 1 else 0)+(if PIDPumpCon.reset <> AixLib.Types.Reset.Input then 1 else 0)+(if not storageSimple.layer[1].dynBal.use_mWat_flow then 1 else 0)+3* storageSimple.layer[1].dynBal.nPorts+(if not storageSimple.layer[2].dynBal.use_mWat_flow then 1 else 0)+3*storageSimple.layer[2].dynBal.nPorts+(if not storageSimple.layer[3].dynBal.use_mWat_flow then 1 else 0)+3*storageSimple.layer[3].dynBal.nPorts +(if not storageSimple.layer_HE[1].dynBal.use_mWat_flow then 1 else 0)+3* storageSimple.layer_HE[1].dynBal.nPorts+(if not storageSimple.layer_HE[2].dynBal.use_mWat_flow then 1 else 0)+3*storageSimple.layer_HE[2].dynBal.nPorts+(if not storageSimple.layer_HE[3].dynBal.use_mWat_flow then 1 else 0)+3* storageSimple.layer_HE[3].dynBal.nPorts+(if not heatingRod.vol.dynBal.use_mWat_flow then 1 else 0)+3*heatingRod.vol.dynBal.nPorts+(if not simpleConsumer.volume.dynBal.use_mWat_flow then 1 else 0)+3*simpleConsumer.volume.dynBal.nPorts+(if not pumpGen.vol.dynBal.use_mWat_flow then 1 else 0)+3*pumpGen.vol.dynBal.nPorts+( if not pumpCon.vol.dynBal.use_mWat_flow then 1 else 0)+3*pumpCon.vol.dynBal.nPorts +(if (if PIDHR.reset == AixLib.Types.Reset.Disabled then PIDHR.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if PIDHR.reset == AixLib.Types.Reset.Disabled then PIDHR.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0)+(if ( if PIDPumpGen.reset == AixLib.Types.Reset.Disabled then PIDPumpGen.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if PIDPumpGen.reset == AixLib.Types.Reset.Disabled then PIDPumpGen.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0)+(if ( if PIDPumpCon.reset == AixLib.Types.Reset.Disabled then PIDPumpCon.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if PIDPumpCon.reset == AixLib.Types.Reset.Disabled then PIDPumpCon.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0)
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 964
+Check of AixLib.Fluid.Storage.Examples.StorageSimpleExample successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageSimpleExample.mos\",", "AixLib.Fluid.Storage.Examples.StorageSimpleExample.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Storage.Examples.StorageSimpleExample\",", "AixLib.Fluid.Storage.Examples.StorageSimpleExample.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Storage.Examples.StorageSimpleExample.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Storage.Examples.StorageSimpleExample\\\");\",", "AixLib.Fluid.Storage.Examples.StorageSimpleExample.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Storage.Examples.StorageSimpleExample.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Storage.Examples.StorageSimpleExample.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageSimpleExample.mos");
+simulateModel("AixLib.Fluid.Storage.Examples.StorageSimpleExample", tolerance=1e-6, stopTime=38200, method="dassl", resultFile="AixLib.Fluid.Storage.Examples.StorageSimpleExample");
+Translation of AixLib.Fluid.Storage.Examples.StorageSimpleExample:
+The DAE has 964 scalar unknowns and 964 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 247
+ Variables: 2530
+ Constants: 57 (57 scalars)
+ Parameters: 1181 (1670 scalars)
+ Unknowns: 1292 (1010 scalars)
+ Differentiated variables: 28 scalars
+ Equations: 1101
+ Nontrivial: 860
+Translated Model
+ Constants: 1047 scalars
+ Free parameters: 186 scalars
+ Parameter depending: 627 scalars
+ Outputs: 1 scalars
+ Continuous time states: 17 scalars
+ Time-varying variables: 245 scalars
+ Alias variables: 632 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: {4}
+ Sizes after manipulation of the linear systems: {0}
+ Sizes of nonlinear systems of equations: {5, 7}
+ Sizes after manipulation of the nonlinear systems: {1, 1}
+ Number of numerical Jacobians: 0
+ Initialization problem
+ Sizes of nonlinear systems of equations: {5, 7}
+ Sizes after manipulation of the nonlinear systems: {1, 1}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ heatingRod.vol.dynBal.U
+ PIDHR.I.y
+ PIDPumpCon.I.y
+ PIDPumpGen.I.y
+ pumpCon.filter.s[1]
+ pumpCon.filter.s[2]
+ pumpCon.vol.dynBal.U
+ pumpGen.filter.s[1]
+ pumpGen.filter.s[2]
+ pumpGen.vol.dynBal.U
+ simpleConsumer.heatCapacitor.T
+ storageSimple.layer[1].dynBal.U
+ storageSimple.layer[2].dynBal.U
+ storageSimple.layer[3].dynBal.U
+ storageSimple.layer_HE[1].dynBal.U
+ storageSimple.layer_HE[2].dynBal.U
+ storageSimple.layer_HE[3].dynBal.U
+
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.Storage.Examples.StorageSimpleExample.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar");
+Check of AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar:
+The model has the same number of unknowns and equations: 250
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 248+vol.dynBal.nPorts
+scalar unknowns and
+ 237+(if sou.use_Xi_in then 1 else (if sou.use_X_in then 0 else 1))+(if not sou.use_p_in then 1 else 0)+2*sou.nPorts+(if not sou.use_T_in then 1 else 0)+ (if not dpControlled_dp.mov.vol.steBal.use_mWat_flow then 1 else 0)+(if not vol.dynBal.use_mWat_flow then 1 else 0)+3*vol.dynBal.nPorts
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 250
+Check of AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Movers/DpControlledMovers/Examples/DpVar.mos\",", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar\",", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar\\\");\",", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Movers/DpControlledMovers/Examples/DpVar.mos");
+simulateModel("AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar", startTime=0, stopTime=3600, tolerance=1e-6, method="dassl", resultFile="AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar");
+Translation of AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar:
+The DAE has 250 scalar unknowns and 250 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 82
+ Variables: 814
+ Constants: 19 (19 scalars)
+ Parameters: 465 (949 scalars)
+ Unknowns: 330 (265 scalars)
+ Differentiated variables: 7 scalars
+ Equations: 284
+ Nontrivial: 236
+Translated Model
+ Constants: 686 scalars
+ Free parameters: 51 scalars
+ Parameter depending: 271 scalars
+ Outputs: 1 scalars
+ Continuous time states: 5 scalars
+ Time-varying variables: 61 scalars
+ Alias variables: 164 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: { }
+ Sizes after manipulation of the linear systems: { }
+ Sizes of nonlinear systems of equations: {3, 1}
+ Sizes after manipulation of the nonlinear systems: {1, 1}
+ Number of numerical Jacobians: 0
+ Initialization problem
+ Sizes of nonlinear systems of equations: {3, 1, 1}
+ Sizes after manipulation of the nonlinear systems: {1, 0, 1}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ dpControlled_dp.mov.filter.s[1]
+ dpControlled_dp.mov.filter.s[2]
+ integrator.y
+ val.filter.s[1]
+ val.filter.s[2]
+
+Finished
+ = true
+
+
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump");
+Check of AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump:
+Warning: Redeclaration requires a subtype.
+ But missing component dp_start.
+ In redeclaration of PeakLoadDeviceModel.
+ File: /tmp/tmp-AixLib-3-xeq7e3j4/AixLib/Fluid/Examples/GeothermalHeatPump/BaseClasses/GeothermalHeatPumpBase.mo, line 20
+ Context: AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.PeakLoadDeviceModel
+The model has the same number of unknowns and equations: 4699
+Check of AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Examples/GeothermalHeatPump.mos\",", "AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump\",", "AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump\\\");\",", "AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Examples/GeothermalHeatPump.mos");
+simulateModel("AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump", startTime=0, stopTime=86400, method="dassl", tolerance=1e-06, resultFile="AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump");
+Translation of AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump:
+Warning: Redeclaration requires a subtype.
+ But missing component dp_start.
+ In redeclaration of PeakLoadDeviceModel.
+ File: /tmp/tmp-AixLib-3-xeq7e3j4/AixLib/Fluid/Examples/GeothermalHeatPump/BaseClasses/GeothermalHeatPumpBase.mo, line 20
+ Context: AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.PeakLoadDeviceModel
+The DAE has 4699 scalar unknowns and 4699 scalar equations.
+Sparse solver handling possible: false.
+Due to flag Advanced.SparseActivate=false.
+Model sparse and large enough: true.
+Sparse solvers are available for dassl, lsodar, cvode, radau, esdirk*, sdirk* (using OpenMP, set number of cores with Advanced.NumberOfCores).
+
+Statistics
+
+Original Model
+ Number of components: 1061
+ Variables: 12395
+ Constants: 219 (219 scalars)
+ Parameters: 6093 (7317 scalars)
+ Unknowns: 6083 (4872 scalars)
+ Differentiated variables: 147 scalars
+ Equations: 4946
+ Nontrivial: 3872
+Translated Model
+ Constants: 4153 scalars
+ Free parameters: 915 scalars
+ Parameter depending: 3104 scalars
+ Outputs: 17 scalars
+ Continuous time states: 109 scalars
+ Time-varying variables: 1171 scalars
+ Alias variables: 3065 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: {2, 3, 2, 2, 4, 3, 17, 2, 2, 2, 2, 2, 2, 2, 2, 3, 4, 2, 4, 3, 17, 4, 2, 2, 2, 2, 2, 2, 2, 2}
+ Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 8, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 8, 0, 0, 0, 0, 0, 0, 0, 0, 0}
+ Sizes of nonlinear systems of equations: {5, 12, 12, 5, 6, 6, 6, 3, 1, 6, 6, 6, 6, 6, 6, 6}
+ Sizes after manipulation of the nonlinear systems: {1, 1, 1, 1, 1, 1, 1, 0, 0, 1, 1, 1, 1, 1, 1, 1}
+ Number of numerical Jacobians: 0
+ Initialization problem
+ Sizes of nonlinear systems of equations: {5, 1, 12, 1, 12, 1, 5, 1, 3, 1}
+ Sizes after manipulation of the nonlinear systems: {2, 0, 1, 0, 1, 0, 1, 0, 1, 0}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ coldStorage.bottomCover.loadIns.T
+ coldStorage.bottomCover.loadWall.T
+ coldStorage.heatingCoil1.pipe[1].del.x
+ coldStorage.heatingCoil1.pipe[1].timDel.x
+ coldStorage.heatingCoil1.pipe[1].vol_a.dynBal.U
+ coldStorage.heatingCoil1.pipe[1].vol_b.dynBal.U
+ coldStorage.heatingCoil1.pipe[2].del.x
+ coldStorage.heatingCoil1.pipe[2].timDel.x
+ coldStorage.heatingCoil1.pipe[2].vol_a.dynBal.U
+ coldStorage.heatingCoil1.pipe[2].vol_b.dynBal.U
+ coldStorage.heatingCoil1.pipe[3].del.x
+ coldStorage.heatingCoil1.pipe[3].timDel.x
+ coldStorage.heatingCoil1.pipe[3].vol_a.dynBal.U
+ coldStorage.heatingCoil1.pipe[3].vol_b.dynBal.U
+ coldStorage.heatingCoil1.pipe[4].del.x
+ coldStorage.heatingCoil1.pipe[4].timDel.x
+ coldStorage.heatingCoil1.pipe[4].vol_a.dynBal.U
+ coldStorage.heatingCoil1.pipe[4].vol_b.dynBal.U
+ coldStorage.heatingCoil1.pipe[5].del.x
+ coldStorage.heatingCoil1.pipe[5].timDel.x
+ coldStorage.heatingCoil1.pipe[5].vol_a.dynBal.U
+ coldStorage.heatingCoil1.pipe[5].vol_b.dynBal.U
+ coldStorage.layer[1].dynBal.U
+ coldStorage.layer[2].dynBal.U
+ coldStorage.layer[3].dynBal.U
+ coldStorage.layer[4].dynBal.U
+ coldStorage.layer[5].dynBal.U
+ coldStorage.storageMantle[1].Insulation.CylindricLoad1.heatCapacitor.T
+ coldStorage.storageMantle[1].Wall.CylindricLoad1.heatCapacitor.T
+ coldStorage.storageMantle[2].Insulation.CylindricLoad1.heatCapacitor.T
+ coldStorage.storageMantle[2].Wall.CylindricLoad1.heatCapacitor.T
+ coldStorage.storageMantle[3].Insulation.CylindricLoad1.heatCapacitor.T
+ coldStorage.storageMantle[3].Wall.CylindricLoad1.heatCapacitor.T
+ coldStorage.storageMantle[4].Insulation.CylindricLoad1.heatCapacitor.T
+ coldStorage.storageMantle[4].Wall.CylindricLoad1.heatCapacitor.T
+ coldStorage.storageMantle[5].Insulation.CylindricLoad1.heatCapacitor.T
+ coldStorage.storageMantle[5].Wall.CylindricLoad1.heatCapacitor.T
+ coldStorage.topCover.loadIns.T
+ coldStorage.topCover.loadWall.T
+ heatPump.con.vol.dynBal.U
+ heatPump.eva.vol.dynBal.U
+ heatStorage.bottomCover.loadIns.T
+ heatStorage.bottomCover.loadWall.T
+ heatStorage.heatingCoil1.pipe[1].del.x
+ heatStorage.heatingCoil1.pipe[1].timDel.x
+ heatStorage.heatingCoil1.pipe[1].vol_a.dynBal.U
+ heatStorage.heatingCoil1.pipe[1].vol_b.dynBal.U
+ heatStorage.heatingCoil1.pipe[2].del.x
+ heatStorage.heatingCoil1.pipe[2].timDel.x
+ heatStorage.heatingCoil1.pipe[2].vol_a.dynBal.U
+ heatStorage.heatingCoil1.pipe[2].vol_b.dynBal.U
+ heatStorage.heatingCoil1.pipe[3].del.x
+ heatStorage.heatingCoil1.pipe[3].timDel.x
+ heatStorage.heatingCoil1.pipe[3].vol_a.dynBal.U
+ heatStorage.heatingCoil1.pipe[3].vol_b.dynBal.U
+ heatStorage.heatingCoil1.pipe[4].del.x
+ heatStorage.heatingCoil1.pipe[4].timDel.x
+ heatStorage.heatingCoil1.pipe[4].vol_a.dynBal.U
+ heatStorage.heatingCoil1.pipe[4].vol_b.dynBal.U
+ heatStorage.heatingCoil1.pipe[5].del.x
+ heatStorage.heatingCoil1.pipe[5].timDel.x
+ heatStorage.heatingCoil1.pipe[5].vol_a.dynBal.U
+ heatStorage.heatingCoil1.pipe[5].vol_b.dynBal.U
+ heatStorage.layer[1].dynBal.U
+ heatStorage.layer[2].dynBal.U
+ heatStorage.layer[3].dynBal.U
+ heatStorage.layer[4].dynBal.U
+ heatStorage.layer[5].dynBal.U
+ heatStorage.storageMantle[1].Insulation.CylindricLoad1.heatCapacitor.T
+ heatStorage.storageMantle[1].Wall.CylindricLoad1.heatCapacitor.T
+ heatStorage.storageMantle[2].Insulation.CylindricLoad1.heatCapacitor.T
+ heatStorage.storageMantle[2].Wall.CylindricLoad1.heatCapacitor.T
+ heatStorage.storageMantle[3].Insulation.CylindricLoad1.heatCapacitor.T
+ heatStorage.storageMantle[3].Wall.CylindricLoad1.heatCapacitor.T
+ heatStorage.storageMantle[4].Insulation.CylindricLoad1.heatCapacitor.T
+ heatStorage.storageMantle[4].Wall.CylindricLoad1.heatCapacitor.T
+ heatStorage.storageMantle[5].Insulation.CylindricLoad1.heatCapacitor.T
+ heatStorage.storageMantle[5].Wall.CylindricLoad1.heatCapacitor.T
+ heatStorage.topCover.loadIns.T
+ heatStorage.topCover.loadWall.T
+ peaLoaDev.boiler.internalControl.ControlerHeater.PI.I.y
+ peaLoaDev.boiler.internalControl.eEnergyMeter_P.q_joule
+ peaLoaDev.boiler.internalControl.eEnergyMeter_S.q_joule
+ peaLoaDev.boiler.senTCold.T
+ peaLoaDev.boiler.senTHot.T
+ peaLoaDev.boiler.vol.dynBal.U
+ pumpColdConsumer.filter.s[1]
+ pumpColdConsumer.filter.s[2]
+ pumpColdConsumer.vol.dynBal.U
+ pumpCondenser.filter.s[1]
+ pumpCondenser.filter.s[2]
+ pumpCondenser.vol.dynBal.U
+ pumpEvaporator.filter.s[1]
+ pumpEvaporator.filter.s[2]
+ pumpEvaporator.vol.dynBal.U
+ pumpGeothermalSource.filter.s[1]
+ pumpGeothermalSource.filter.s[2]
+ pumpGeothermalSource.vol.dynBal.U
+ pumpHeatConsumer.filter.s[1]
+ pumpHeatConsumer.filter.s[2]
+ pumpHeatConsumer.vol.dynBal.U
+ valveColdStorage.filter.s[1]
+ valveColdStorage.filter.s[2]
+ valveHeatSink.filter.s[1]
+ valveHeatSink.filter.s[2]
+ valveHeatSource.filter.s[1]
+ valveHeatSource.filter.s[2]
+ valveHeatStorage.filter.s[1]
+ valveHeatStorage.filter.s[2]
+
+Warning: WARNINGS have been issued.
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.Pools.Examples.IndoorSwimmingPool");
+Check of AixLib.Fluid.Pools.Examples.IndoorSwimmingPool:
+The model has the same number of unknowns and equations: 677
+The model has the same number of unknowns and equations
+for the given numerical settings of parameters: 677
+Check of AixLib.Fluid.Pools.Examples.IndoorSwimmingPool successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Pools/Examples/IndoorSwimmingPool.mos\",", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPool.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Pools.Examples.IndoorSwimmingPool\",", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPool.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPool.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Pools.Examples.IndoorSwimmingPool\\\");\",", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPool.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Pools.Examples.IndoorSwimmingPool.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPool.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Pools/Examples/IndoorSwimmingPool.mos");
+simulateModel("AixLib.Fluid.Pools.Examples.IndoorSwimmingPool", tolerance=1e-6, stopTime=604800, numberOfIntervals=0, outputInterval=900, method="CVode", resultFile="AixLib.Fluid.Pools.Examples.IndoorSwimmingPool");
+Translation of AixLib.Fluid.Pools.Examples.IndoorSwimmingPool:
+The DAE has 677 scalar unknowns and 677 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 161
+ Variables: 1600
+ Constants: 41 (41 scalars)
+ Parameters: 725 (917 scalars)
+ Unknowns: 834 (704 scalars)
+ Differentiated variables: 3 scalars
+ Equations: 700
+ Nontrivial: 575
+Translated Model
+ Constants: 579 scalars
+ Free parameters: 125 scalars
+ Parameter depending: 369 scalars
+ Continuous time states: 3 scalars
+ Time-varying variables: 180 scalars
+ Alias variables: 409 scalars
+ Number of mixed real/discrete systems of equations: 1
+ Sizes of linear systems of equations: {26}
+ Sizes after manipulation of the linear systems: {13}
+ Sizes of nonlinear systems of equations: {75, 1, 1}
+ Sizes after manipulation of the nonlinear systems: {16, 0, 1}
+ Number of numerical Jacobians: 0
+ Initialization problem
+ Sizes of nonlinear systems of equations: {1, 74, 1}
+ Sizes after manipulation of the nonlinear systems: {0, 16, 1}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ indoorSwimming.cirPump.filter.s[1]
+ indoorSwimming.cirPump.filter.s[2]
+ indoorSwimming.PI.I.y
+
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.Pools.Examples.IndoorSwimmingPool.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta");
+Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta:
+The model has the same number of unknowns and equations: 187
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 185+pip.vol.dynBal.nPorts
+scalar unknowns and
+ 171+(if sin.use_Xi_in then 1 else (if sin.use_X_in then 0 else 1))+(if not sin.use_p_in then 1 else 0)+2*sin.nPorts+(if not sin.use_T_in then 1 else 0)+ (if sou.use_Xi_in then 1 else (if sou.use_X_in then 0 else 1))+(if not sou.use_m_flow_in then 1 else 0)+2*sou.nPorts+(if not sou.use_T_in then 1 else 0)+(if not pip.vol.dynBal.use_mWat_flow then 1 else 0)+3* pip.vol.dynBal.nPorts
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 187
+Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/PlugFlowPipeZeta.mos\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta\\\");\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/PlugFlowPipeZeta.mos");
+simulateModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta", stopTime=1000, method="dassl", tolerance=1e-6, resultFile="AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta");
+Translation of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta:
+The DAE has 187 scalar unknowns and 187 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 34
+ Variables: 537
+ Constants: 10 (10 scalars)
+ Parameters: 262 (255 scalars)
+ Unknowns: 265 (193 scalars)
+ Differentiated variables: 6 scalars
+ Equations: 220
+ Nontrivial: 186
+Translated Model
+ Constants: 189 scalars
+ Free parameters: 46 scalars
+ Parameter depending: 66 scalars
+ Continuous time states: 5 scalars
+ Time-varying variables: 39 scalars
+ Alias variables: 118 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: { }
+ Sizes after manipulation of the linear systems: { }
+ Sizes of nonlinear systems of equations: { }
+ Sizes after manipulation of the nonlinear systems: { }
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ pip.plugFlowCore.del.x
+ pip.plugFlowCore.timDel.x
+ pip.vol.dynBal.U
+ senTemIn.T
+ senTemOut.T
+
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation");
+Check of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation:
+The model has the same number of unknowns and equations: 5511
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 3783+32*enthalpyExchanger.n+16*enthalpyExchanger.airDuct2.heatTransfer.n+18* enthalpyExchanger.airDuct2.massTransfer.n+16*enthalpyExchanger.airDuct1.heatTransfer.n +18*enthalpyExchanger.airDuct1.massTransfer.n+5*enthalpyExchanger.membrane.heatTransfer.n +enthalpyExchanger.membrane.massTransfer.n+2*enthalpyExchanger.airDuct2.vol[1].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[2].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[3].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[4].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[5].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[6].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[7].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[8].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[9].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[10].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[11].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[12].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[13].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[14].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[15].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[1].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[2].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[3].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[4].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[5].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[6].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[7].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[8].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[9].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[10].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[11].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[12].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[13].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[14].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[15].dynBal.nPorts+max([size(bondaryEta.columns, 1); size(bondaryEta.offset, 1)])+max([size(bondaryOda.columns, 1); size( bondaryOda.offset, 1)])+max([size(Results.columns, 1); size(Results.offset, 1)]) +2*fan.vol.dynBal.nPorts+2*fan1.vol.dynBal.nPorts
+scalar unknowns and
+ 3435+17*enthalpyExchanger.airDuct2.heatTransfer.n+19*enthalpyExchanger.airDuct2.massTransfer.n +3*(if enthalpyExchanger.couFloArr then 2*enthalpyExchanger.n else 0)+17* enthalpyExchanger.airDuct1.heatTransfer.n+19*enthalpyExchanger.airDuct1.massTransfer.n +7*enthalpyExchanger.membrane.heatTransfer.n+3*enthalpyExchanger.membrane.massTransfer.n +2*(if enthalpyExchanger.useConPer then 1 else 0)+32*enthalpyExchanger.n+(if souEta.use_Xi_in then 2 else (if souEta.use_X_in then 1 else 3))+3* souEta.nPorts+(if not souEta.use_p_in then 1 else 0)+(if not souEta.use_T_in then 1 else 0)+(if sinEha.use_Xi_in then 2 else (if sinEha.use_X_in then 1 else 3))+3*sinEha.nPorts+(if not sinEha.use_p_in then 1 else 0)+(if not sinEha.use_T_in then 1 else 0)+(if souOda.use_Xi_in then 2 else (if souOda.use_X_in then 1 else 3))+3*souOda.nPorts+(if not souOda.use_p_in then 1 else 0)+(if not souOda.use_T_in then 1 else 0)+(if sinSup.use_Xi_in then 2 else (if sinSup.use_X_in then 1 else 3))+3*sinSup.nPorts+(if not sinSup.use_p_in then 1 else 0)+(if not sinSup.use_T_in then 1 else 0)+max([ size(bondaryEta.columns, 1); size(bondaryEta.offset, 1)])+max([size( bondaryOda.columns, 1); size(bondaryOda.offset, 1)])+max([size(Results.columns, 1); size(Results.offset, 1)])+(if conPID.reset <> AixLib.Types.Reset.Input then 1 else 0)+(if conPID1.reset <> AixLib.Types.Reset.Input then 1 else 0)+5 *enthalpyExchanger.airDuct2.vol[1].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[2].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[3].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[4].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[5].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[6].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[7].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[8].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[9].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[10].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[11].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[12].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[13].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[14].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[15].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[1].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[2].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[3].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[4].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[5].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[6].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[7].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[8].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[9].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[10].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[11].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[12].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[13].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[14].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[15].dynBal.nPorts +(if not fan.vol.dynBal.use_mWat_flow then 1 else 0)+5*fan.vol.dynBal.nPorts+ (if (if conPID.reset == AixLib.Types.Reset.Disabled then conPID.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if conPID.reset == AixLib.Types.Reset.Disabled then conPID.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0)+(if not fan1.vol.dynBal.use_mWat_flow then 1 else 0)+5*fan1.vol.dynBal.nPorts+( if (if conPID1.reset == AixLib.Types.Reset.Disabled then conPID1.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if conPID1.reset == AixLib.Types.Reset.Disabled then conPID1.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0)
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 5511
+Check of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/MassExchangers/MembraneBasedEnthalpyExchangers/Validation/StaticValidation.mos\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation\\\");\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/MassExchangers/MembraneBasedEnthalpyExchangers/Validation/StaticValidation.mos");
+simulateModel("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation", stopTime=29600, numberOfIntervals=0, outputInterval=1, method="dassl",tolerance=1E-6, resultFile="AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation");
+Translation of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation:
+The DAE has 5511 scalar unknowns and 5511 scalar equations.
+Redundant consistent initial conditions.
+Removed the following equations which are redundant and consistent:
+ fan1.vol.p_start = fan1.p_start;
+ if (enthalpyExchanger.airDuct2.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[1].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[1].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[1].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[1].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[1].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[2].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[2].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[2].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[2].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[2].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[3].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[3].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[3].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[3].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[3].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[4].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[4].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[4].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[4].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[4].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[5].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[5].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[5].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[5].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[5].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[6].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[6].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[6].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[6].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[6].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[7].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[7].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[7].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[7].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[7].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[8].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[8].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[8].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[8].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[8].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[9].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[9].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[9].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[9].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[9].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[10].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[10].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[10].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[10].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[10].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[11].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[11].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[11].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[11].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[11].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[12].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[12].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[12].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[12].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[12].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[13].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[13].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[13].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[13].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[13].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[14].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[14].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[14].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[14].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[14].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct2.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct2.vol[15].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct2.vol[15].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[15].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct2.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct2.vol[15].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct2.vol[15].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[1].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[1].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[1].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[1].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[1].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[2].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[2].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[2].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[2].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[2].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[3].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[3].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[3].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[3].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[3].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[4].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[4].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[4].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[4].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[4].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[5].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[5].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[5].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[5].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[5].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[6].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[6].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[6].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[6].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[6].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[7].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[7].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[7].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[7].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[7].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[8].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[8].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[8].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[8].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[8].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[9].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[9].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[9].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[9].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[9].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[10].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[10].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[10].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[10].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[10].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[11].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[11].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[11].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[11].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[11].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[12].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[12].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[12].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[12].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[12].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[13].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[13].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[13].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[13].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[13].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[14].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[14].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[14].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[14].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[14].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (enthalpyExchanger.airDuct1.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then
+ if (enthalpyExchanger.airDuct1.vol[15].dynBal.initialize_p) then
+ enthalpyExchanger.airDuct1.vol[15].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[15].dynBal.p_start;
+ end if;
+ else
+ if (enthalpyExchanger.airDuct1.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then
+ if (enthalpyExchanger.airDuct1.vol[15].dynBal.initialize_p) then
+ der(enthalpyExchanger.airDuct1.vol[15].dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+ if (fan.vol.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.FixedInitial) then
+ if (fan.vol.dynBal.initialize_p) then
+ fan.vol.dynBal.medium.p = fan.vol.dynBal.p_start;
+ end if;
+ else
+ if (fan.vol.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. SteadyStateInitial) then
+ if (fan.vol.dynBal.initialize_p) then
+ der(fan.vol.dynBal.medium.p) = 0;
+ end if;
+ end if;
+ end if;
+
+This required evaluation of
+the interactive parameters
+ fan.p_start(start = 101325)
+ fan1.p_start(start = 101325)
+ sinEha.p(start = 101325)
+ sinSup.p(start = 101325)
+ souEta.p(start = 101325)
+ souOda.p(start = 101325)
+
+The redundancies involve
+initial equations:
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinSup.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ sinEha.p = 101325.0;
+ souOda.p = fan.vol.dynBal.p_start;
+ souEta.p = fan1.vol.dynBal.p_start;
+
+
+Statistics
+
+Original Model
+ Number of components: 676
+ Variables: 7282
+ Constants: 168 (168 scalars)
+ Parameters: 2808 (3273 scalars)
+ Unknowns: 4306 (5679 scalars)
+ Differentiated variables: 129 scalars
+ Equations: 2961
+ Nontrivial: 2303
+Translated Model
+ Constants: 2677 scalars
+ Free parameters: 252 scalars
+ Parameter depending: 1422 scalars
+ Continuous time states: 97 scalars
+ Time-varying variables: 1771 scalars
+ Alias variables: 2998 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: {2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3}
+ Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2}
+ Sizes of nonlinear systems of equations: {1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1}
+ Sizes after manipulation of the nonlinear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0}
+ Number of numerical Jacobians: 0
+ Initialization problem
+ Sizes of nonlinear systems of equations: {1, 1}
+ Sizes after manipulation of the nonlinear systems: {0, 0}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ conPID.I.y
+ conPID1.I.y
+ enthalpyExchanger.airDuct1.senRelHum.phi
+ enthalpyExchanger.airDuct1.senTem.T
+ enthalpyExchanger.airDuct1.vol[1].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[1].dynBal.U
+ enthalpyExchanger.airDuct1.vol[2].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[2].dynBal.U
+ enthalpyExchanger.airDuct1.vol[3].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[3].dynBal.U
+ enthalpyExchanger.airDuct1.vol[4].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[4].dynBal.U
+ enthalpyExchanger.airDuct1.vol[5].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[5].dynBal.U
+ enthalpyExchanger.airDuct1.vol[6].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[6].dynBal.U
+ enthalpyExchanger.airDuct1.vol[7].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[7].dynBal.U
+ enthalpyExchanger.airDuct1.vol[8].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[8].dynBal.U
+ enthalpyExchanger.airDuct1.vol[9].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[9].dynBal.U
+ enthalpyExchanger.airDuct1.vol[10].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[10].dynBal.U
+ enthalpyExchanger.airDuct1.vol[11].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[11].dynBal.U
+ enthalpyExchanger.airDuct1.vol[12].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[12].dynBal.U
+ enthalpyExchanger.airDuct1.vol[13].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[13].dynBal.U
+ enthalpyExchanger.airDuct1.vol[14].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[14].dynBal.U
+ enthalpyExchanger.airDuct1.vol[15].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct1.vol[15].dynBal.U
+ enthalpyExchanger.airDuct2.senRelHum.phi
+ enthalpyExchanger.airDuct2.senTem.T
+ enthalpyExchanger.airDuct2.vol[1].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[1].dynBal.U
+ enthalpyExchanger.airDuct2.vol[2].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[2].dynBal.U
+ enthalpyExchanger.airDuct2.vol[3].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[3].dynBal.U
+ enthalpyExchanger.airDuct2.vol[4].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[4].dynBal.U
+ enthalpyExchanger.airDuct2.vol[5].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[5].dynBal.U
+ enthalpyExchanger.airDuct2.vol[6].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[6].dynBal.U
+ enthalpyExchanger.airDuct2.vol[7].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[7].dynBal.U
+ enthalpyExchanger.airDuct2.vol[8].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[8].dynBal.U
+ enthalpyExchanger.airDuct2.vol[9].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[9].dynBal.U
+ enthalpyExchanger.airDuct2.vol[10].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[10].dynBal.U
+ enthalpyExchanger.airDuct2.vol[11].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[11].dynBal.U
+ enthalpyExchanger.airDuct2.vol[12].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[12].dynBal.U
+ enthalpyExchanger.airDuct2.vol[13].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[13].dynBal.U
+ enthalpyExchanger.airDuct2.vol[14].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[14].dynBal.U
+ enthalpyExchanger.airDuct2.vol[15].dynBal.medium.Xi[1]
+ enthalpyExchanger.airDuct2.vol[15].dynBal.U
+ enthalpyExchanger.membrane.heatTransfer.Ts[1]
+ enthalpyExchanger.membrane.heatTransfer.Ts[2]
+ enthalpyExchanger.membrane.heatTransfer.Ts[3]
+ enthalpyExchanger.membrane.heatTransfer.Ts[4]
+ enthalpyExchanger.membrane.heatTransfer.Ts[5]
+ enthalpyExchanger.membrane.heatTransfer.Ts[6]
+ enthalpyExchanger.membrane.heatTransfer.Ts[7]
+ enthalpyExchanger.membrane.heatTransfer.Ts[8]
+ enthalpyExchanger.membrane.heatTransfer.Ts[9]
+ enthalpyExchanger.membrane.heatTransfer.Ts[10]
+ enthalpyExchanger.membrane.heatTransfer.Ts[11]
+ enthalpyExchanger.membrane.heatTransfer.Ts[12]
+ enthalpyExchanger.membrane.heatTransfer.Ts[13]
+ enthalpyExchanger.membrane.heatTransfer.Ts[14]
+ enthalpyExchanger.membrane.heatTransfer.Ts[15]
+ fan.filter.s[1]
+ fan.filter.s[2]
+ fan.vol.dynBal.medium.Xi[1]
+ fan.vol.dynBal.U
+ fan1.filter.s[1]
+ fan1.filter.s[2]
+ fan1.vol.dynBal.medium.Xi[1]
+ fan1.vol.dynBal.U
+ senMasFraEha.X
+ senMasFraEta.X
+ senMasFraOda.X
+ senMasFraSup.X
+ senTemEha.T
+ senTemEta.T
+ senTemOda.T
+ senTemSup.T
+
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation.translation.log"); = true
+
+
+rCheck = checkModel("AixLib.Fluid.Storage.Examples.StorageBoiler");
+Check of AixLib.Fluid.Storage.Examples.StorageBoiler:
+The model has the same number of unknowns and equations: 3241
+Check of AixLib.Fluid.Storage.Examples.StorageBoiler successful.
+Declaring variable: Boolean rCheck ;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageBoiler.mos\",", "AixLib.Fluid.Storage.Examples.StorageBoiler.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Storage.Examples.StorageBoiler\",", "AixLib.Fluid.Storage.Examples.StorageBoiler.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Storage.Examples.StorageBoiler.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Storage.Examples.StorageBoiler\\\");\",", "AixLib.Fluid.Storage.Examples.StorageBoiler.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Storage.Examples.StorageBoiler.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Storage.Examples.StorageBoiler.statistics.log");
+
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageBoiler.mos");
+simulateModel("AixLib.Fluid.Storage.Examples.StorageBoiler", tolerance=1e-6, stopTime=86400, method="dassl", resultFile="AixLib.Fluid.Storage.Examples.StorageBoiler");
+Translation of AixLib.Fluid.Storage.Examples.StorageBoiler:
+The DAE has 3241 scalar unknowns and 3241 scalar equations.
+
+Statistics
+
+Original Model
+ Number of components: 651
+ Variables: 8627
+ Constants: 159 (159 scalars)
+ Parameters: 4092 (4095 scalars)
+ Unknowns: 4376 (3344 scalars)
+ Differentiated variables: 106 scalars
+ Equations: 3314
+ Nontrivial: 2545
+Translated Model
+ Constants: 2850 scalars
+ Free parameters: 287 scalars
+ Parameter depending: 1523 scalars
+ Continuous time states: 76 scalars
+ Time-varying variables: 843 scalars
+ Alias variables: 2095 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: {4, 3, 3, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 4, 3, 3, 2, 2, 2, 2, 2, 2, 2, 2, 2}
+ Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0}
+ Sizes of nonlinear systems of equations: {22, 1, 6, 6, 6, 6, 6, 6, 6, 6, 6, 6, 1}
+ Sizes after manipulation of the nonlinear systems: {1, 0, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1}
+ Number of numerical Jacobians: 0
+ Initialization problem
+ Sizes of nonlinear systems of equations: {22, 1, 1}
+ Sizes after manipulation of the nonlinear systems: {1, 0, 1}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ bufferStorage.bottomCover.loadIns.T
+ bufferStorage.bottomCover.loadWall.T
+ bufferStorage.heatingCoil1.pipe[1].del.x
+ bufferStorage.heatingCoil1.pipe[1].timDel.x
+ bufferStorage.heatingCoil1.pipe[1].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[1].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[2].del.x
+ bufferStorage.heatingCoil1.pipe[2].timDel.x
+ bufferStorage.heatingCoil1.pipe[2].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[2].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[3].del.x
+ bufferStorage.heatingCoil1.pipe[3].timDel.x
+ bufferStorage.heatingCoil1.pipe[3].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[3].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[4].del.x
+ bufferStorage.heatingCoil1.pipe[4].timDel.x
+ bufferStorage.heatingCoil1.pipe[4].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[4].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[5].del.x
+ bufferStorage.heatingCoil1.pipe[5].timDel.x
+ bufferStorage.heatingCoil1.pipe[5].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[5].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[6].del.x
+ bufferStorage.heatingCoil1.pipe[6].timDel.x
+ bufferStorage.heatingCoil1.pipe[6].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[6].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[7].del.x
+ bufferStorage.heatingCoil1.pipe[7].timDel.x
+ bufferStorage.heatingCoil1.pipe[7].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[7].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[8].del.x
+ bufferStorage.heatingCoil1.pipe[8].timDel.x
+ bufferStorage.heatingCoil1.pipe[8].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[8].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[9].del.x
+ bufferStorage.heatingCoil1.pipe[9].timDel.x
+ bufferStorage.heatingCoil1.pipe[9].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[9].vol_b.dynBal.U
+ bufferStorage.heatingCoil1.pipe[10].del.x
+ bufferStorage.heatingCoil1.pipe[10].timDel.x
+ bufferStorage.heatingCoil1.pipe[10].vol_a.dynBal.U
+ bufferStorage.heatingCoil1.pipe[10].vol_b.dynBal.U
+ bufferStorage.layer[1].dynBal.U
+ bufferStorage.layer[2].dynBal.U
+ bufferStorage.layer[3].dynBal.U
+ bufferStorage.layer[4].dynBal.U
+ bufferStorage.layer[5].dynBal.U
+ bufferStorage.layer[6].dynBal.U
+ bufferStorage.layer[7].dynBal.U
+ bufferStorage.layer[8].dynBal.U
+ bufferStorage.layer[9].dynBal.U
+ bufferStorage.layer[10].dynBal.U
+ bufferStorage.storageMantle[1].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[1].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[2].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[2].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[3].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[3].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[4].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[4].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[5].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[5].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[6].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[6].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[7].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[7].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[8].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[8].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[9].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[9].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[10].Insulation.CylindricLoad1.heatCapacitor.T
+ bufferStorage.storageMantle[10].Wall.CylindricLoad1.heatCapacitor.T
+ bufferStorage.topCover.loadIns.T
+ bufferStorage.topCover.loadWall.T
+ pump.filter.s[1]
+ pump.filter.s[2]
+
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+
+savelog("AixLib.Fluid.Storage.Examples.StorageBoiler.translation.log");
\ No newline at end of file
diff --git a/docs/correct_HTML_1520_newHPModels/regression/Fluid/unitTests-dymola.log b/docs/correct_HTML_1520_newHPModels/regression/Fluid/unitTests-dymola.log
new file mode 100644
index 0000000000..65c1e78f75
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Fluid/unitTests-dymola.log
@@ -0,0 +1,13 @@
+Regression tests are only run for the following package:
+ AixLib.Fluid
+*** Error: AixLib_Fluid_Examples_GeothermalHeatPump.txt: Errors during result verification.
+ Absolute error = 2.247e+02 at t = 52704.0 for heatPumpPower
+*** Warning: AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump: Translation statistics for simulation and results changed for number of continuous time states.
+ Old = 113
+ New = 109
+Comparison files output by funnel are stored in the directory 'funnel_comp' of size 1.1 MB.
+Run 'python -c "import buildingspy.development.regressiontest as t; t.Tester(tool=\"dymola\").report()"'
+to access a summary of the comparison results.
+
+Script that runs unit tests had 1 warnings and 1 errors.
+
diff --git a/docs/correct_HTML_1520_newHPModels/regression/Obsolete/comparison-dymola.log b/docs/correct_HTML_1520_newHPModels/regression/Obsolete/comparison-dymola.log
new file mode 100644
index 0000000000..c49fac8592
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Obsolete/comparison-dymola.log
@@ -0,0 +1,203 @@
+[
+ {
+ "comparison": {
+ "file_name": "AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller.mat",
+ "funnel_dirs": [
+ "funnel_comp/AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller.mat_chiller.sigBus.TConInMea",
+ "funnel_comp/AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller.mat_chiller.sigBus.TEvaInMea",
+ "funnel_comp/AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller.mat_chiller.sigBus.TConOutMea",
+ "funnel_comp/AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller.mat_chiller.sigBus.TEvaOutMea",
+ "funnel_comp/AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller.mat_chiller.innerCycle.QEva",
+ "funnel_comp/AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller.mat_chiller.innerCycle.QCon",
+ "funnel_comp/AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller.mat_chiller.innerCycle.Pel"
+ ],
+ "success_rate": 1.0,
+ "t_err_max": [
+ 0.0,
+ 0.0,
+ 0.0,
+ 0.0,
+ 0.0,
+ 0.0,
+ 0.0
+ ],
+ "test_passed": [
+ 1,
+ 1,
+ 1,
+ 1,
+ 1,
+ 1,
+ 1
+ ],
+ "var_groups": [
+ 0,
+ 0,
+ 0,
+ 0,
+ 1,
+ 1,
+ 1
+ ],
+ "variables": [
+ "chiller.sigBus.TConInMea",
+ "chiller.sigBus.TEvaInMea",
+ "chiller.sigBus.TConOutMea",
+ "chiller.sigBus.TEvaOutMea",
+ "chiller.innerCycle.QEva",
+ "chiller.innerCycle.QCon",
+ "chiller.innerCycle.Pel"
+ ],
+ "warnings": [
+ null,
+ null,
+ null,
+ null,
+ null,
+ null,
+ null
+ ]
+ },
+ "model": "AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller",
+ "simulation": {
+ "elapsed_time": 0.016,
+ "final_time": 3600,
+ "jacobians": 79,
+ "start_time": 0,
+ "state_events": 1,
+ "success": true
+ }
+ },
+ {
+ "comparison": {
+ "file_name": "AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump.mat",
+ "funnel_dirs": [
+ "funnel_comp/AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump.mat_heatPump.sigBus.TConInMea",
+ "funnel_comp/AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump.mat_heatPump.sigBus.TEvaInMea",
+ "funnel_comp/AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump.mat_heatPump.sigBus.TConOutMea",
+ "funnel_comp/AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump.mat_heatPump.sigBus.TEvaOutMea",
+ "funnel_comp/AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump.mat_heatPump.innerCycle.QEva",
+ "funnel_comp/AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump.mat_heatPump.innerCycle.QCon",
+ "funnel_comp/AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump.mat_heatPump.innerCycle.Pel"
+ ],
+ "success_rate": 1.0,
+ "t_err_max": [
+ 0.0,
+ 0.0,
+ 0.0,
+ 0.0,
+ 0.0,
+ 0.0,
+ 0.0
+ ],
+ "test_passed": [
+ 1,
+ 1,
+ 1,
+ 1,
+ 1,
+ 1,
+ 1
+ ],
+ "var_groups": [
+ 0,
+ 0,
+ 0,
+ 0,
+ 1,
+ 1,
+ 1
+ ],
+ "variables": [
+ "heatPump.sigBus.TConInMea",
+ "heatPump.sigBus.TEvaInMea",
+ "heatPump.sigBus.TConOutMea",
+ "heatPump.sigBus.TEvaOutMea",
+ "heatPump.innerCycle.QEva",
+ "heatPump.innerCycle.QCon",
+ "heatPump.innerCycle.Pel"
+ ],
+ "warnings": [
+ null,
+ null,
+ null,
+ null,
+ null,
+ null,
+ null
+ ]
+ },
+ "model": "AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump",
+ "simulation": {
+ "elapsed_time": 0.0276,
+ "final_time": 3600,
+ "jacobians": 72,
+ "start_time": 0,
+ "state_events": 1,
+ "success": true
+ }
+ },
+ {
+ "comparison": {
+ "file_name": "AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem.mat",
+ "funnel_dirs": [
+ null,
+ null,
+ null,
+ null,
+ null,
+ null
+ ],
+ "success_rate": 0.0,
+ "t_err_max": [
+ 0,
+ 0,
+ 0,
+ 0,
+ 0,
+ 0
+ ],
+ "test_passed": [
+ 0,
+ 0,
+ 0,
+ 0,
+ 0,
+ 0
+ ],
+ "var_groups": [
+ 0,
+ 0,
+ 0,
+ 1,
+ 1,
+ 2
+ ],
+ "variables": [
+ "heatPumpSystem.heatPump.sigBus.TConInMea",
+ "heatPumpSystem.heatPump.sigBus.TConOutMea",
+ "heatPumpSystem.hPSystemController.hPControls.heatCurve.TSet",
+ "heatPumpSystem.heatPump.innerCycle.QCon",
+ "heatPumpSystem.heatPump.innerCycle.Pel",
+ "vol.T"
+ ],
+ "warnings": [
+ "Translation, simulation or extracting simulation results failed. IOError while reading /tmp/tmp-AixLib-0-cwcgxl59/AixLib/AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem.mat generated by Obsolete/Year2024/Systems/HeatPumpSystems/Examples/HeatPumpSystem.mos.\nFile /tmp/tmp-AixLib-0-cwcgxl59/AixLib/AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem.mat does not exist.\n",
+ "",
+ "",
+ "",
+ "",
+ ""
+ ]
+ },
+ "model": "AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem",
+ "simulation": {
+ "elapsed_time": 0,
+ "final_time": 86400,
+ "jacobians": 0,
+ "start_time": 0,
+ "state_events": 0,
+ "success": false
+ }
+ }
+]
diff --git a/docs/correct_HTML_1520_newHPModels/regression/Obsolete/funnel_comp/AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller.mat_chiller.innerCycle.Pel/errors.csv b/docs/correct_HTML_1520_newHPModels/regression/Obsolete/funnel_comp/AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller.mat_chiller.innerCycle.Pel/errors.csv
new file mode 100644
index 0000000000..0bf904e264
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Obsolete/funnel_comp/AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller.mat_chiller.innerCycle.Pel/errors.csv
@@ -0,0 +1,102 @@
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+2988.000000,305.084808
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+3312.000000,305.084778
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+3492.000000,305.085022
+3528.000000,305.085083
+3564.000000,305.085175
+3600.000000,305.085266
diff --git a/docs/correct_HTML_1520_newHPModels/regression/Obsolete/funnel_comp/AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump.mat_heatPump.sigBus.TEvaOutMea/upperBound.csv b/docs/correct_HTML_1520_newHPModels/regression/Obsolete/funnel_comp/AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump.mat_heatPump.sigBus.TEvaOutMea/upperBound.csv
new file mode 100644
index 0000000000..d191d32262
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Obsolete/funnel_comp/AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump.mat_heatPump.sigBus.TEvaOutMea/upperBound.csv
@@ -0,0 +1,86 @@
+x,y
+-0.001000,293.443144
+0.001000,293.443144
+36.001000,284.102025
+72.001000,280.240868
+108.001000,278.677172
+144.001000,278.043818
+180.001000,277.787245
+216.001000,277.683198
+252.001000,277.640950
+288.001000,277.623751
+324.001000,277.616664
+360.001000,277.613671
+396.001000,277.612357
+432.001000,277.611715
+467.999099,277.611349
+503.999000,277.618375
+539.999000,278.296604
+575.999000,279.594531
+611.999000,281.152606
+647.999000,282.825787
+683.999000,284.548730
+719.999000,286.291865
+755.999000,288.043249
+791.999000,289.797962
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+935.999000,296.791154
+971.999000,298.535756
+1007.999000,300.247946
+1043.999000,301.199092
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+1295.999000,301.849124
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+1403.999000,301.852057
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+1763.999000,301.857739
+1799.999000,301.858289
+1835.999000,303.863160
+1871.999000,304.738272
+1907.999000,305.112364
+1943.999000,305.272252
+1979.999000,305.340619
+2015.999000,305.369793
+2051.999000,305.382226
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+2123.999000,305.389710
+2159.999000,305.390626
+2195.999000,305.390962
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+2268.001000,305.391085
+2304.001000,305.391023
+2340.001000,305.390993
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+2412.001000,305.390840
+2484.001000,305.390718
+2520.001000,305.390626
+2592.001000,305.390504
+2628.001000,305.390412
+2808.001000,305.390107
+2844.001000,305.390076
+2880.001000,305.390015
+2952.001000,305.389954
+2988.001000,305.389893
+3024.001000,305.389893
+3096.001000,305.389832
+3239.999000,305.389832
+3275.999000,305.389863
+3311.999000,305.389863
+3347.999000,305.389893
+3383.999000,305.389954
+3419.999000,305.389985
+3527.999000,305.390168
+3599.999000,305.390351
+3600.001000,305.390351
diff --git a/docs/correct_HTML_1520_newHPModels/regression/Obsolete/simulator-dymola.log b/docs/correct_HTML_1520_newHPModels/regression/Obsolete/simulator-dymola.log
new file mode 100644
index 0000000000..8f2e29b93d
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Obsolete/simulator-dymola.log
@@ -0,0 +1,264 @@
+ = true
+
+Advanced.PedanticModelica = false;
+
+rCheck = checkModel("AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem");
+Check of AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem:
+Warning: Top class AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem specified an obsolete type: Obsolete model - This model is obsolete and not maintained anymore.
+Warning: Failed to find class Controls.HeatPump.BaseClasses.PartialTSetToNSet
+ In redeclaration of TSetToNSet.
+ File: /tmp/tmp-AixLib-0-cwcgxl59/AixLib/Obsolete/Year2024/Systems/HeatPumpSystems/BaseClasses/PartialHeatPumpSystem.mo, line 67
+ Component context: AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem.TSetToNSet
+ Component declared as HeatPumpSystem heatPumpSystem in AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem
+Warning: Failed to find class Controls.HeatPump.BaseClasses.PartialTSetToNSet
+ In declaration of TSetToNSet.
+ File: /tmp/tmp-AixLib-0-cwcgxl59/AixLib/Obsolete/Year2024/Systems/HeatPumpSystems/BaseClasses/PartialHeatPumpSystem.mo, line 67
+ Context: AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.BaseClasses.PartialHeatPumpSystem.TSetToNSet
+Warning: WARNINGS have been issued.
+Declaring variable: Boolean rCheck ;
+Advanced.PedanticModelica = true;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Obsolete/Year2024/Systems/HeatPumpSystems/Examples/HeatPumpSystem.mos\",", "AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem\",", "AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem\\\");\",", "AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem.statistics.log");
+
+Advanced.PedanticModelica = false;
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Obsolete/Year2024/Systems/HeatPumpSystems/Examples/HeatPumpSystem.mos");
+simulateModel("AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem", stopTime=86400, method="dassl", tolerance=1e-06, resultFile="AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem");
+Translation of AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem:
+Warning: Top class AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem specified an obsolete type: Obsolete model - This model is obsolete and not maintained anymore.
+Warning: Failed to find class Controls.HeatPump.BaseClasses.PartialTSetToNSet
+ In redeclaration of TSetToNSet.
+ File: /tmp/tmp-AixLib-0-cwcgxl59/AixLib/Obsolete/Year2024/Systems/HeatPumpSystems/BaseClasses/PartialHeatPumpSystem.mo, line 67
+ Component context: AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem.TSetToNSet
+ Component declared as HeatPumpSystem heatPumpSystem in AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem
+Warning: Failed to find class Controls.HeatPump.BaseClasses.PartialTSetToNSet
+ In declaration of TSetToNSet.
+ File: /tmp/tmp-AixLib-0-cwcgxl59/AixLib/Obsolete/Year2024/Systems/HeatPumpSystems/BaseClasses/PartialHeatPumpSystem.mo, line 67
+ Context: AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.BaseClasses.PartialHeatPumpSystem.TSetToNSet
+Warning: WARNINGS have been issued.
+ = false
+
+Declaring variable: Boolean rScript ;
+Advanced.PedanticModelica = true;
+
+savelog("AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem.translation.log"); = true
+
+Advanced.PedanticModelica = false;
+
+rCheck = checkModel("AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump");
+Check of AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump:
+Warning: Top class AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump specified an obsolete type: Obsolete model - This model is obsolete and not maintained anymore.
+Warning: Component type specifier Vitocal200AWO201 specified an obsolete type: Obsolete model - This model is obsolete and not maintained anymore.
+ Near file: /tmp/tmp-AixLib-0-cwcgxl59/AixLib/Obsolete/Year2024/DataBase/HeatPump/EN14511/Vitocal200AWO201.mo, line 2
+ Component context: _out
+ Component declared as Vitocal200AWO201 _out in AixLib.Obsolete.Year2024.DataBase.HeatPump.EN14511
+Warning: Component type specifier Vitocal200AWO201 specified an obsolete type: Obsolete model - This model is obsolete and not maintained anymore.
+ Near file: /tmp/tmp-AixLib-0-cwcgxl59/AixLib/Obsolete/Year2024/DataBase/Chiller/EN14511/Vitocal200AWO201.mo, line 2
+ Component context: _out
+ Component declared as Vitocal200AWO201 _out in AixLib.Obsolete.Year2024.DataBase.Chiller.EN14511
+The model has the same number of unknowns and equations: 634
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 626+heatPump.con.vol.dynBal.nPorts+heatPump.eva.vol.dynBal.nPorts+ pumSou.vol.dynBal.nPorts+Room.dynBal.nPorts
+scalar unknowns and
+ 592+(if sourceSideMassFlowSource.use_Xi_in then 1 else (if sourceSideMassFlowSource.use_X_in then 0 else 1))+(if not sourceSideMassFlowSource.use_m_flow_in then 1 else 0) +2*sourceSideMassFlowSource.nPorts+(if not sourceSideMassFlowSource.use_T_in then 1 else 0)+(if sourceSideFixedBoundary.use_Xi_in then 1 else (if sourceSideFixedBoundary.use_X_in then 0 else 1))+(if not sourceSideFixedBoundary.use_p_in then 1 else 0)+2*sourceSideFixedBoundary.nPorts+(if not sourceSideFixedBoundary.use_T_in then 1 else 0)+(if sinkSideFixedBoundary.use_Xi_in then 1 else (if sinkSideFixedBoundary.use_X_in then 0 else 1))+(if not sinkSideFixedBoundary.use_p_in then 1 else 0)+2*sinkSideFixedBoundary.nPorts+(if not sinkSideFixedBoundary.use_T_in then 1 else 0)+(if not heatPump.con.vol.dynBal.use_mWat_flow then 1 else 0)+3 *heatPump.con.vol.dynBal.nPorts+(if not heatPump.eva.vol.dynBal.use_mWat_flow then 1 else 0)+3*heatPump.eva.vol.dynBal.nPorts+(if not pumSou.vol.dynBal.use_mWat_flow then 1 else 0)+3*pumSou.vol.dynBal.nPorts+(if not Room.dynBal.use_mWat_flow then 1 else 0)+3*Room.dynBal.nPorts
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 634
+Check of AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump successful.
+Warning: WARNINGS have been issued.
+Declaring variable: Boolean rCheck ;
+Advanced.PedanticModelica = true;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Obsolete/Year2024/Fluid/HeatPumps/Examples/HeatPump.mos\",", "AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump\",", "AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump\\\");\",", "AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump.statistics.log");
+
+Advanced.PedanticModelica = false;
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Obsolete/Year2024/Fluid/HeatPumps/Examples/HeatPump.mos");
+simulateModel("AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump", tolerance=1e-6, stopTime=3600, method="dassl", resultFile="AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump");
+Translation of AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump:
+Warning: Top class AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump specified an obsolete type: Obsolete model - This model is obsolete and not maintained anymore.
+Warning: Component type specifier Vitocal200AWO201 specified an obsolete type: Obsolete model - This model is obsolete and not maintained anymore.
+ Near file: /tmp/tmp-AixLib-0-cwcgxl59/AixLib/Obsolete/Year2024/DataBase/HeatPump/EN14511/Vitocal200AWO201.mo, line 2
+ Component context: _out
+ Component declared as Vitocal200AWO201 _out in AixLib.Obsolete.Year2024.DataBase.HeatPump.EN14511
+Warning: Component type specifier Vitocal200AWO201 specified an obsolete type: Obsolete model - This model is obsolete and not maintained anymore.
+ Near file: /tmp/tmp-AixLib-0-cwcgxl59/AixLib/Obsolete/Year2024/DataBase/Chiller/EN14511/Vitocal200AWO201.mo, line 2
+ Component context: _out
+ Component declared as Vitocal200AWO201 _out in AixLib.Obsolete.Year2024.DataBase.Chiller.EN14511
+The DAE has 634 scalar unknowns and 634 scalar equations.
+Warning: The conditions of the following assert statements are always false:
+Warning: assert(heatPump.con.preDro.homotopyInitialization, "In HeatPump.heatPump.con.preDro: The constant homotopyInitialization has been modified from its default value. This constant will be removed in future releases.", AssertionLevel.warning);
+ The variable heatPump.con.preDro.homotopyInitialization = false, was declared in class AixLib.Fluid.BaseClasses.PartialResistance, /tmp/tmp-AixLib-0-cwcgxl59/AixLib/Fluid/BaseClasses/PartialResistance.mo at line 12, and used in component heatPump.con.preDro.PartialResistance.
+Warning: assert(heatPump.eva.preDro.homotopyInitialization, "In HeatPump.heatPump.eva.preDro: The constant homotopyInitialization has been modified from its default value. This constant will be removed in future releases.", AssertionLevel.warning);
+ The variable heatPump.eva.preDro.homotopyInitialization = false, was declared in class AixLib.Fluid.BaseClasses.PartialResistance, /tmp/tmp-AixLib-0-cwcgxl59/AixLib/Fluid/BaseClasses/PartialResistance.mo at line 12, and used in component heatPump.eva.preDro.PartialResistance.
+
+Statistics
+
+Original Model
+ Number of components: 164
+ Variables: 1624
+ Constants: 27 (27 scalars)
+ Parameters: 761 (1295 scalars)
+ Unknowns: 836 (659 scalars)
+ Differentiated variables: 15 scalars
+ Equations: 724
+ Nontrivial: 604
+Translated Model
+ Constants: 697 scalars
+ Free parameters: 238 scalars
+ Parameter depending: 497 scalars
+ Outputs: 11 scalars
+ Continuous time states: 11 scalars
+ Time-varying variables: 127 scalars
+ Alias variables: 422 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: { }
+ Sizes after manipulation of the linear systems: { }
+ Sizes of nonlinear systems of equations: {1}
+ Sizes after manipulation of the nonlinear systems: {1}
+ Number of numerical Jacobians: 0
+ Initialization problem
+ Sizes of nonlinear systems of equations: {1}
+ Sizes after manipulation of the nonlinear systems: {1}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ heatPump.con.vol.dynBal.U
+ heatPump.eva.vol.dynBal.U
+ heatPump.senT_a1.T
+ heatPump.senT_a2.T
+ heatPump.senT_b1.T
+ heatPump.senT_b2.T
+ pumSou.filter.s[1]
+ pumSou.filter.s[2]
+ pumSou.vol.dynBal.U
+ Room.dynBal.U
+ senTAct.T
+
+Warning: WARNINGS have been issued.
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+Advanced.PedanticModelica = true;
+
+savelog("AixLib.Obsolete.Year2024.Fluid.HeatPumps.Examples.HeatPump.translation.log"); = true
+
+Advanced.PedanticModelica = false;
+
+rCheck = checkModel("AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller");
+Check of AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller:
+Warning: Top class AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller specified an obsolete type: Obsolete model - This model is obsolete and not maintained anymore.
+Warning: Component type specifier Vitocal200AWO201 specified an obsolete type: Obsolete model - This model is obsolete and not maintained anymore.
+ Near file: /tmp/tmp-AixLib-0-cwcgxl59/AixLib/Obsolete/Year2024/DataBase/Chiller/EN14511/Vitocal200AWO201.mo, line 2
+ Component context: _out
+ Component declared as Vitocal200AWO201 _out in AixLib.Obsolete.Year2024.DataBase.Chiller.EN14511
+Warning: Component type specifier Vitocal200AWO201 specified an obsolete type: Obsolete model - This model is obsolete and not maintained anymore.
+ Near file: /tmp/tmp-AixLib-0-cwcgxl59/AixLib/Obsolete/Year2024/DataBase/HeatPump/EN14511/Vitocal200AWO201.mo, line 2
+ Component context: _out
+ Component declared as Vitocal200AWO201 _out in AixLib.Obsolete.Year2024.DataBase.HeatPump.EN14511
+The model has the same number of unknowns and equations: 625
+The model could not be deduced to be symbolically well-posed.
+The model has
+ 617+chiller.con.vol.dynBal.nPorts+chiller.eva.vol.dynBal.nPorts+pumSou.vol.dynBal.nPorts +Room.dynBal.nPorts
+scalar unknowns and
+ 583+(if sinkSideMassFlowSource.use_Xi_in then 1 else (if sinkSideMassFlowSource.use_X_in then 0 else 1))+(if not sinkSideMassFlowSource.use_m_flow_in then 1 else 0)+2 *sinkSideMassFlowSource.nPorts+(if not sinkSideMassFlowSource.use_T_in then 1 else 0)+(if sinkSideFixedBoundary.use_Xi_in then 1 else (if sinkSideFixedBoundary.use_X_in then 0 else 1))+(if not sinkSideFixedBoundary.use_p_in then 1 else 0)+2* sinkSideFixedBoundary.nPorts+(if not sinkSideFixedBoundary.use_T_in then 1 else 0)+(if sourceSideFixedBoundary.use_Xi_in then 1 else (if sourceSideFixedBoundary.use_X_in then 0 else 1))+(if not sourceSideFixedBoundary.use_p_in then 1 else 0)+2*sourceSideFixedBoundary.nPorts+(if not sourceSideFixedBoundary.use_T_in then 1 else 0)+(if not chiller.con.vol.dynBal.use_mWat_flow then 1 else 0)+3 *chiller.con.vol.dynBal.nPorts+(if not chiller.eva.vol.dynBal.use_mWat_flow then 1 else 0)+3*chiller.eva.vol.dynBal.nPorts+(if not pumSou.vol.dynBal.use_mWat_flow then 1 else 0)+3*pumSou.vol.dynBal.nPorts+(if not Room.dynBal.use_mWat_flow then 1 else 0)+3*Room.dynBal.nPorts
+scalar equations.
+However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations:
+ 625
+Check of AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller successful.
+Warning: WARNINGS have been issued.
+Declaring variable: Boolean rCheck ;
+Advanced.PedanticModelica = true;
+
+Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Obsolete/Year2024/Fluid/Chillers/Examples/Chiller.mos\",", "AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller.statistics.log");
+Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller\",", "AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller.statistics.log");
+Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller.statistics.log");
+Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller\\\");\",", "AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller.statistics.log");
+Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller.statistics.log");
+Modelica.Utilities.Streams.print(" },", "AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller.statistics.log");
+
+Advanced.PedanticModelica = false;
+
+rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Obsolete/Year2024/Fluid/Chillers/Examples/Chiller.mos");
+simulateModel("AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller", tolerance=1e-6, stopTime=3600, method="dassl", resultFile="AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller");
+Translation of AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller:
+Warning: Top class AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller specified an obsolete type: Obsolete model - This model is obsolete and not maintained anymore.
+Warning: Component type specifier Vitocal200AWO201 specified an obsolete type: Obsolete model - This model is obsolete and not maintained anymore.
+ Near file: /tmp/tmp-AixLib-0-cwcgxl59/AixLib/Obsolete/Year2024/DataBase/Chiller/EN14511/Vitocal200AWO201.mo, line 2
+ Component context: _out
+ Component declared as Vitocal200AWO201 _out in AixLib.Obsolete.Year2024.DataBase.Chiller.EN14511
+Warning: Component type specifier Vitocal200AWO201 specified an obsolete type: Obsolete model - This model is obsolete and not maintained anymore.
+ Near file: /tmp/tmp-AixLib-0-cwcgxl59/AixLib/Obsolete/Year2024/DataBase/HeatPump/EN14511/Vitocal200AWO201.mo, line 2
+ Component context: _out
+ Component declared as Vitocal200AWO201 _out in AixLib.Obsolete.Year2024.DataBase.HeatPump.EN14511
+The DAE has 625 scalar unknowns and 625 scalar equations.
+Warning: The conditions of the following assert statements are always false:
+Warning: assert(chiller.con.preDro.homotopyInitialization, "In Chiller.chiller.con.preDro: The constant homotopyInitialization has been modified from its default value. This constant will be removed in future releases.", AssertionLevel.warning);
+ The variable chiller.con.preDro.homotopyInitialization = false, was declared in class AixLib.Fluid.BaseClasses.PartialResistance, /tmp/tmp-AixLib-0-cwcgxl59/AixLib/Fluid/BaseClasses/PartialResistance.mo at line 12, and used in component chiller.con.preDro.PartialResistance.
+Warning: assert(chiller.eva.preDro.homotopyInitialization, "In Chiller.chiller.eva.preDro: The constant homotopyInitialization has been modified from its default value. This constant will be removed in future releases.", AssertionLevel.warning);
+ The variable chiller.eva.preDro.homotopyInitialization = false, was declared in class AixLib.Fluid.BaseClasses.PartialResistance, /tmp/tmp-AixLib-0-cwcgxl59/AixLib/Fluid/BaseClasses/PartialResistance.mo at line 12, and used in component chiller.eva.preDro.PartialResistance.
+
+Statistics
+
+Original Model
+ Number of components: 163
+ Variables: 1610
+ Constants: 27 (27 scalars)
+ Parameters: 760 (1294 scalars)
+ Unknowns: 823 (650 scalars)
+ Differentiated variables: 15 scalars
+ Equations: 722
+ Nontrivial: 603
+Translated Model
+ Constants: 696 scalars
+ Free parameters: 238 scalars
+ Parameter depending: 496 scalars
+ Continuous time states: 11 scalars
+ Time-varying variables: 123 scalars
+ Alias variables: 418 scalars
+ Number of mixed real/discrete systems of equations: 0
+ Sizes of linear systems of equations: { }
+ Sizes after manipulation of the linear systems: { }
+ Sizes of nonlinear systems of equations: {1}
+ Sizes after manipulation of the nonlinear systems: {1}
+ Number of numerical Jacobians: 0
+ Initialization problem
+ Sizes of nonlinear systems of equations: {1}
+ Sizes after manipulation of the nonlinear systems: {1}
+ Number of numerical Jacobians: 0
+
+Selected continuous time states
+Statically selected continuous time states
+ chiller.con.vol.dynBal.U
+ chiller.eva.vol.dynBal.U
+ chiller.senT_a1.T
+ chiller.senT_a2.T
+ chiller.senT_b1.T
+ chiller.senT_b2.T
+ pumSou.filter.s[1]
+ pumSou.filter.s[2]
+ pumSou.vol.dynBal.U
+ Room.dynBal.U
+ senTAct.T
+
+Warning: WARNINGS have been issued.
+Finished
+ = true
+
+Declaring variable: Boolean rScript ;
+Advanced.PedanticModelica = true;
+
+savelog("AixLib.Obsolete.Year2024.Fluid.Chillers.Examples.Chiller.translation.log");
\ No newline at end of file
diff --git a/docs/correct_HTML_1520_newHPModels/regression/Obsolete/unitTests-dymola.log b/docs/correct_HTML_1520_newHPModels/regression/Obsolete/unitTests-dymola.log
new file mode 100644
index 0000000000..ce1d93f3f2
--- /dev/null
+++ b/docs/correct_HTML_1520_newHPModels/regression/Obsolete/unitTests-dymola.log
@@ -0,0 +1,13 @@
+Regression tests are only run for the following package:
+ AixLib.Obsolete
+*** Error: Model check failed for 'AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem'.
+*** Error: Simulation failed for 'RunScript("modelica://AixLib/Resources/Scripts/Dymola/Obsolete/Year2024/Systems/HeatPumpSystems/Examples/HeatPumpSystem.mos");'.
+*** Error: IOError while reading /tmp/tmp-AixLib-0-cwcgxl59/AixLib/AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem.mat generated by Obsolete/Year2024/Systems/HeatPumpSystems/Examples/HeatPumpSystem.mos.
+File /tmp/tmp-AixLib-0-cwcgxl59/AixLib/AixLib.Obsolete.Year2024.Systems.HeatPumpSystems.Examples.HeatPumpSystem.mat does not exist.
+
+Comparison files output by funnel are stored in the directory 'funnel_comp' of size 0.2 MB.
+Run 'python -c "import buildingspy.development.regressiontest as t; t.Tester(tool=\"dymola\").report()"'
+to access a summary of the comparison results.
+
+Script that runs unit tests had 0 warnings and 3 errors.
+