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FDS Source: Allow different BACKINGs for HT3d
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mcgratta committed Nov 1, 2023
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8 changes: 4 additions & 4 deletions Manuals/FDS_User_Guide/FDS_User_Guide.tex
Original file line number Diff line number Diff line change
Expand Up @@ -2443,7 +2443,7 @@ \subsection{3-D Heat Conduction (Beta)}
\subsubsection{Limitations}

\begin{enumerate}
\item {\ct HT3D} cannot be applied to an exterior boundary; it must be applied to an {\ct OBST} that is completely within the computational domain.
\item {\ct HT3D} cannot be applied to an exterior boundary; it must be applied to an {\ct OBST} for which at least one face in each coordinate direction is exposed.
\item Avoid contact between 3-D and 1-D solids. If two sides of a 3-D solid touch 1-D solids, there will be no lateral heat conduction computed in that particular direction.
\item If your 3-D obstruction extends beyond meshes that abut, add the parameter {\ct NEIGHBOR\_SEPARATION\_DISTANCE} to the {\ct MISC} line. Any mesh within this distance of another mesh will share geometry information for use in the 3-D heat conduction calculation.
\item By default, the interior nodes are clustered near the surface and stretched out deeper within the solid. If you want to maintain uniform spacing, set {\ct CELL\_SIZE} on the {\ct SURF} line to indicate the desired interior node spacing. The {\ct CELL\_SIZE} is typically the same as the gas phase cells.
Expand Down Expand Up @@ -2478,7 +2478,7 @@ \subsubsection{Example: Steel Assembly}
The quantity {\ct 'WALL ENTHALPY'} is the total energy within the volume carved out by a wall cell from front to back. This is why the {\ct IOR} is included because the integration need only be carried out for upward facing wall cells. Also, because the unit associated with this quantity is kJ rather than kJ/m$^2$, the {\ct CONVERSION\_FACTOR} is needed to cancel out the area of each wall cell (0.01~m by 0.01~m) after the summation. The parameter {\ct RELATIVE=T} means that only the change in enthalpy is desired.
.

\subsubsection{Example: Uncoated Structural Steel}
\subsubsection{Example: Unprotected Structural Steel}

Structural steel members like I-beams are difficult to model for two reasons. First, the underlying grid must be reasonably well-resolved to capture the cross-sectional shape, and second, the lateral heat transfer can be important. At best, I-beams are typically modeled as a collection of thin (i.e. zero cell thick) obstructions representing the web and flanges.
\begin{lstlisting}
Expand All @@ -2502,7 +2502,7 @@ \subsubsection{Example: Uncoated Structural Steel}
\end{figure}


\subsubsection{Example: Coated Structural Steel}
\subsubsection{Example: Insulated Structural Steel}
\label{info:normal_direction_only}

An insulated steel beam can be modeled as a hybrid of 1-D and 3-D objects. The heat conducted through the insulation varies mainly in the direction normal to the surface, while the heat conducted along the steel beam varies mainly in the lateral direction. The following lines provide an example where a steel plate is coated with insulation. The steel plate is entered as a relatively thin obstruction, and the insulation is entered as a slightly thicker obstruction with a {\ct SURF} line that indicates that heat is to be conducted in the {\ct NORMAL\_DIRECTION\_ONLY} even though it is declared to be {\ct HT3D}. This latter parameter ensures that the thin steel obstruction and the insulation obstruction are included in the calculation of solid overlap volumes. Note that all dimensions are exact to ensure that the overlap volumes are computed properly.
Expand Down Expand Up @@ -2930,7 +2930,7 @@ \subsection{The Heat of Reaction}
\subsection{Liquid Fuels}
\label{info:liquid_fuels}

The evaporation rate of a liquid fuel is analogous to the convective heating rate in that the evaporation rate is a function of a mass transfer coefficient, $h_{\rm m}$, much like thermal convection is a function of the heat transfer coefficient, $h$, discussed in Section~\ref{info:convection}\footnote{As with the convective heat transfer coefficient, there is an option to specify a fixed {\ct MASS\_TRANSFER\_COEFFICIENT} (m/s) on the {\ct SURF} line that describes a liquid pool.}. The FDS Technical Reference Guide~\cite{FDS_Tech_Guide} provides further details on how the evaporation rate is computed.
The evaporation rate of a liquid fuel is analogous to the convective heating rate in that the evaporation rate is a function of a mass transfer coefficient, $h_{\rm m}$, much like thermal convection is a function of the heat transfer coefficient, $h$, discussed in Section~\ref{info:convection}\footnote{As with the convective heat transfer coefficient, there is an option to specify a fixed {\ct MASS\_TRANSFER\_COEFFICIENT} (m/s) on the {\ct SURF} line that describes a liquid pool.}. The FDS Technical Reference Guide~\cite{FDS_Tech_Guide} provides further details on how the evaporation rate is computed.

The properties of a liquid fuel are given on the {\ct MATL} line:
\begin{lstlisting}
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5 changes: 3 additions & 2 deletions Manuals/FDS_Verification_Guide/FDS_Verification_Guide.tex
Original file line number Diff line number Diff line change
Expand Up @@ -4458,9 +4458,10 @@ \subsection{Energy Conservation in a 3-D Solid (\texorpdfstring{\textct{ht3d\_en
\begin{tabular*}{\textwidth}{l@{\extracolsep{\fill}}r}
\includegraphics[height=2.2in]{SCRIPT_FIGURES/ht3d_energy_conservation_4} &
\includegraphics[height=2.2in]{SCRIPT_FIGURES/ht3d_energy_conservation_5} \\
\multicolumn{2}{c}{\includegraphics[height=2.2in]{SCRIPT_FIGURES/ht3d_energy_conservation_6}}
\includegraphics[height=2.2in]{SCRIPT_FIGURES/ht3d_energy_conservation_6} &
\includegraphics[height=2.2in]{SCRIPT_FIGURES/ht3d_energy_conservation_7}
\end{tabular*}
\caption[Additional \textct{ht3d\_energy\_conservation} test cases, 4, 5, and 6]{Comparison of the integrated net heat flux versus the internal enthalpy for a homogenous solid block of insulation material (upper left), a block of steel with a single layer of insulation (upper right), and a block with multiple layers of multi-component insulation (bottom).}
\caption[Additional \textct{ht3d\_energy\_conservation} test cases, 4, 5, 6, and 7]{Comparison of the integrated net heat flux versus the internal enthalpy for a homogenous solid block of insulation material (upper left), a block of steel with a single layer of insulation (upper right), a block with multiple layers of multi-component insulation (bottom left), a block of steel that abuts an open boundary (bottom right).}
\label{fig:ht3d_energy_conservation_4}
\end{figure}

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3 changes: 2 additions & 1 deletion Source/init.f90
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Expand Up @@ -3620,7 +3620,7 @@ SUBROUTINE FIND_WALL_BACK_INDEX(NM,IW)

WC => M%WALL(IW)
SF => SURFACE(WC%SURF_INDEX)
IF (SF%THERMAL_BC_INDEX/=THERMALLY_THICK .OR. SF%BACKING/=EXPOSED) RETURN
IF (SF%THERMAL_BC_INDEX/=THERMALLY_THICK) RETURN
BC => M%BOUNDARY_COORD(WC%BC_INDEX)
ICG = M%CELL_INDEX(BC%IIG,BC%JJG,BC%KKG)
IF (M%CELL(ICG)%SOLID) RETURN
Expand Down Expand Up @@ -3718,6 +3718,7 @@ SUBROUTINE FIND_WALL_BACK_INDEX(NM,IW)
! Determine if the back face is found

IF ((.NOT.OM%CELL(IC)%SOLID .AND. OM%CELL(IC)%WALL_INDEX(IOR)>0) .OR. NOM==0) THEN ! the back wall face is found
IF (NOM>0 .AND. SF%BACKING/=EXPOSED) RETURN ! No need to assign back cell information for anything but exposed backing
ONE_D%BACK_INDEX = OM%CELL(IC)%WALL_INDEX(IOR)
ONE_D%BACK_MESH = NOM
ONE_D%BACK_SURF = OM%CELL(IC)%SURF_INDEX(IOR)
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17 changes: 9 additions & 8 deletions Utilities/Matlab/FDS_verification_dataplot_inputs.csv
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Expand Up @@ -259,14 +259,15 @@ d,ht1d_pile,Heat_Transfer/ht1d_pile_git.txt,Heat_Transfer/ht1d_pile.csv,2,3,Dept
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d,ht3d_energy_conservation,Heat_Transfer/ht3d_energy_conservation_git.txt,Heat_Transfer/ht3d_energy_conservation_devc.csv,2,3,Time,E3D,Enthalpy,k-,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Heat_Transfer/ht3d_energy_conservation_devc.csv,2,3,Time,Q_net,Integrated Heat Flux,r-,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Energy Balance (ht3d\_energy\_conservation),Time (s),Enthalpy (kJ),0,10,1,0,100,1,no,0.05 0.90,SouthEast,,1,linear,FDS_Verification_Guide/SCRIPT_FIGURES/ht3d_energy_conservation,Relative Error,end,1.00E-02,Heat Transfer,r^,r,TeX
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d,ht3d_energy_conservation,Heat_Transfer/ht3d_energy_conservation_5_git.txt,Heat_Transfer/ht3d_energy_conservation_5_devc.csv,2,3,Time,H1,Enthalpy,k-,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Heat_Transfer/ht3d_energy_conservation_5_devc.csv,2,3,Time,Q_net,Integrated Heat Flux,ko,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Energy Balance (ht3d\_energy\_conservation\_5),Time (s),Enthalpy (kJ),0,100,1,0,4,1,no,0.05 0.90,SouthEast,,1,linear,FDS_Verification_Guide/SCRIPT_FIGURES/ht3d_energy_conservation_5,Relative Error,end,1.00E-02,Heat Transfer,r^,r,TeX
d,ht3d_energy_conservation,Heat_Transfer/ht3d_energy_conservation_6_git.txt,Heat_Transfer/ht3d_energy_conservation_6_devc.csv,2,3,Time,H1,Enthalpy,k-,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Heat_Transfer/ht3d_energy_conservation_6_devc.csv,2,3,Time,Q_net,Integrated Heat Flux,ko,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Energy Balance (ht3d\_energy\_conservation\_6),Time (s),Enthalpy (kJ),0,100,1,0,4,1,no,0.05 0.90,SouthEast,,1,linear,FDS_Verification_Guide/SCRIPT_FIGURES/ht3d_energy_conservation_6,Relative Error,end,1.00E-02,Heat Transfer,r^,r,TeX
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d,ht3d_ibeam,Heat_Transfer/ht3d_ibeam_git.txt,Heat_Transfer/ht3d_ibeam_FEM_results.csv,2,3,Time,Ts_x195_40|Ts_x145_30|Ts_x095_20|Ts_x025_40|Ts_x195_1|Ts_x025_1,FEM 1|FEM 2|FEM 3|FEM 4|FEM 5|FEM 6,ro|k^|bd|gsq|mv|c>,0,100000,,0,100000,-1.00E+09,1.00E+09,20,Heat_Transfer/ht3d_ibeam_devc.csv,2,3,Time,TS_x195-40|TS_x145-30|TS_x095-20|TS_x025-40|TS_x195-01|TS_x025-01,FDS 1|FDS 2|FDS 3|FDS 4|FDS 5|FDS 6,r-|k-|b-|g-|m-|c-,0,100000,,0,100000,-1.00E+09,1.00E+09,20,HT3D I-beam Surface Temperature (ht3d\_ibeam),Time (s),Temperature (°C),0,3600,1,0,1000,1,no,0.05 0.90,EastOutside,,1.2,linear,FDS_Verification_Guide/SCRIPT_FIGURES/ht3d_ibeam_TS,Relative Error,end,8.00E-02,Heat Transfer,r^,r,TeX
d,ht3d_mass_conservation,Heat_Transfer/ht3d_mass_conservation_git.txt,Heat_Transfer/ht3d_mass_conservation.csv,1,2,Time,Mass,Exact (Mass),ko,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Heat_Transfer/ht3d_mass_conservation_mass.csv,2,3,Time,WOOD MOISTURE,FDS (WOOD MOISTURE),k-,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Mass Balance (ht3d\_mass\_conservation),Time (s),Mass (kg),0,180,1,0,0.3,1,no,0.05 0.90,SouthEast,,1,linear,FDS_Verification_Guide/SCRIPT_FIGURES/ht3d_mass_conservation,Relative Error,end,1.00E-02,Heat Transfer,r^,r,TeX
d,ht3d_mass_conservation,Heat_Transfer/ht3d_mass_conservation_2_git.txt,Heat_Transfer/ht3d_mass_conservation.csv,1,2,Time,Mass,Exact (Mass),ko,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Heat_Transfer/ht3d_mass_conservation_2_mass.csv,2,3,Time,WOOD MOISTURE,FDS (WOOD MOISTURE),k-,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Mass Balance (ht3d\_mass\_conservation\_2),Time (s),Mass (kg),0,180,1,0,0.3,1,no,0.05 0.90,SouthEast,,1,linear,FDS_Verification_Guide/SCRIPT_FIGURES/ht3d_mass_conservation_2,Relative Error,end,1.00E-02,Heat Transfer,r^,r,TeX
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1 change: 1 addition & 0 deletions Verification/FDS_Cases.sh
Original file line number Diff line number Diff line change
Expand Up @@ -254,6 +254,7 @@ $QFDS -d Heat_Transfer ht3d_energy_conservation_3.fds
$QFDS -p 8 -d Heat_Transfer ht3d_energy_conservation_4.fds
$QFDS -p 8 -d Heat_Transfer ht3d_energy_conservation_5.fds
$QFDS -p 8 -d Heat_Transfer ht3d_energy_conservation_6.fds
$QFDS -p 8 -d Heat_Transfer ht3d_energy_conservation_7.fds
$QFDS -d Heat_Transfer ht3d_ibeam.fds
$QFDS -d Heat_Transfer ht3d_mass_conservation.fds
$QFDS -d Heat_Transfer ht3d_mass_conservation_2.fds
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