FDS Verification: Add check of INTERNAL_HEAT_SOURCE

Manuals/FDS_User_Guide/FDS_User_Guide.tex

@@ -2434,23 +2434,32 @@ \subsection{Walls with Different Materials Front and Back}
 \subsection{Specified Internal Heat Source}
 
 \label{info:INTERNAL_HEAT_SOURCE}
+\label{internal_heating}
 
 The condensed phase heat conduction equation has a source term that describes the internal sources and sinks of energy.
 There are three types of sources that contribute to this term:
 heats of reaction for the pyrolysis (see Sec.~\ref{info:solid_pyrolysis}),
 internal absorption and emission of radiation (see Sec.~\ref{info:liquid_fuels}), and the source specified by the user.
 An example of the case where specified heat source could be needed is the heating of electrical cables due to internal current.
 
-The internal source term for each layer of the surface is specified using \ct{INTERNAL_HEAT_SOURCE} on the \ct{SURF} line. Its units are \unit{kW/m^3} and the default value is zero. An optional time ramp can be specified for each layer's heat source using \ct{RAMP_IHS}. In the example below, the cylindrical surface describing a cable consists of an outer plastic layer and inner core of metal. The metal core is heated with a power of 300~\unit{kW/m^3}.
+The internal source term for each layer of the surface is specified using \ct{INTERNAL_HEAT_SOURCE} on the \ct{SURF} line. Its units are \unit{kW/m^3} and the default value is zero. An optional time ramp can be specified for each layer's heat source using \ct{RAMP_IHS}. In the example below, the cylindrical surface describing a 10~cm long cable segment consists of an outer plastic layer and inner core of metal. The metal core is heated with a power of 300~\unit{kW/m^3}.
 \begin{lstlisting}
-    &SURF ID               = 'Cable'
-    THICKNESS              = 0.002,0.008
-    MATL_ID(1,1)           = 'PLASTIC'
-    MATL_ID(2,1)           = 'METAL'
-    GEOMETRY               = 'CYLINDRICAL'
-    LENGTH                 = 0.1
-    INTERNAL_HEAT_SOURCE   = 0.,300. /
+&SURF ID                   = 'Cable'
+      THICKNESS            = 0.002,0.008
+      MATL_ID(1,1)         = 'PLASTIC'
+      MATL_ID(2,1)         = 'METAL'
+      GEOMETRY             = 'CYLINDRICAL'
+      LENGTH               = 0.1
+      INTERNAL_HEAT_SOURCE = 0.,300. /
 \end{lstlisting}
+Figure~\ref{fig:internal_heating} displays the heat generated by 10 of these cable segments. The exact value is 300~\unit{kW/m^3} multiplied by the volume of the metal within the cable segment, $2 \times 10^{-5}$~\unit{m^3}, multiplied by the number of segments, 10, which equals approximately 0.06~kW.
+\begin{figure}[!ht]
+    \centering
+    \includegraphics[height=2.35in]{SCRIPT_FIGURES/internal_heating}
+    \caption[Results of the \ct{internal_heating} test case]{Heating rate of a set of 10 cable segments. The dashed line represents the heat generated by the cable and the dotted line the heat flowing out of the computational domain.}
+    \label{fig:internal_heating}
+\end{figure}
+
 
 \subsection{Non-Planar Walls and Targets}
 
@@ -13531,7 +13540,7 @@ \section{\texorpdfstring{{\tt SURF}}{SURF} (Surface Properties)}
 \ct{INIT_IDS}                                         & Char.~Array     & Section~\ref{info:trees}                  &                     &                         \\ \hline
 \ct{INIT_PER_AREA}                                    & Real            & Section~\ref{info:trees}                  & m$^{-2}$            &                         \\ \hline
 \ct{INNER_RADIUS}                                     & Real            & Section~\ref{info:PART_GEOMETRY}          & m                   &                         \\ \hline
-\ct{INTERNAL_HEAT_SOURCE}                             & Real Array      & Section~\ref{info:INTERNAL_HEAT_SOURCE}   & \unit{kW/m^3}       &                         \\ \hline
+\ct{INTERNAL_HEAT_SOURCE}                             & Real Array      & Section~\ref{info:INTERNAL_HEAT_SOURCE}   & \unit{kW/m^3}       & 0                       \\ \hline
 \ct{LAYER_DIVIDE}                                     & Real            & Section~\ref{info:LAYER_DIVIDE}           &                     & \ct{N_LAYERS}/2         \\ \hline
 \ct{LEAK_PATH}                                        & Int.~Pair       & Section~\ref{info:Leaks}                  &                     &                         \\ \hline
 \ct{LEAK_PATH_ID}                                     & Character~Pair  & Section~\ref{info:Leaks}                  &                     &                         \\ \hline

Utilities/Python/FDS_verification_dataplot_inputs.csv

@@ -452,6 +452,8 @@ d,init_overlap,Miscellaneous/init_overlap_git.txt,Miscellaneous/init_overlap.csv
 d,insulated_steel_pipe,Heat_Transfer/insulated_steel_pipe_git.txt,Heat_Transfer/insulated_steel_pipe.csv,1,2,Radius,Temp,Analytical (Temp),k-,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Heat_Transfer/insulated_steel_pipe_prof_1.csv,2,3,Radius,Temperature,FDS (Temperature),ko,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Temperature (insulated_steel_pipe),Radius (m),Temperature (°C),0.01,0.06,1,0,500,1,no,0.05 0.90,SouthEast,,1,linear,FDS_Verification_Guide/SCRIPT_FIGURES/insulated_steel_pipe,Relative Error,end,0.01,Heat Transfer,r^,r,TeX
 d,insulated_steel_pipe,Heat_Transfer/insulated_steel_pipe_2d_git.txt,Heat_Transfer/insulated_steel_pipe_2d.csv,1,2,Radius,Temp,Analytical (Temp),k-,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Heat_Transfer/insulated_steel_pipe_2d_prof_2.csv,2,3,Radius,T_in,FDS (Temperature),ko,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Temperature (insulated_steel_pipe_2d),Radius (m),Temperature (°C),0.01,0.06,1,0,500,1,no,0.05 0.90,SouthEast,,1,linear,FDS_Verification_Guide/SCRIPT_FIGURES/insulated_steel_pipe_2d,Relative Error,end,0.01,Heat Transfer,r^,r,TeX
 d,insulated_steel_plate,Heat_Transfer/insulated_steel_plate_git.txt,Heat_Transfer/insulated_steel_plate.csv,1,2,Depth,Temp,Analytical (Temp),k-,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Heat_Transfer/insulated_steel_plate_prof_1.csv,2,3,Depth,Temperature,FDS (Temperature),ko,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Temperature (insulated_steel_plate),Depth (m),Temperature (°C),0,0.05,1,0,500,1,no,0.05 0.90,SouthEast,,1,linear,FDS_Verification_Guide/SCRIPT_FIGURES/insulated_steel_plate,Relative Error,end,0.01,Heat Transfer,r^,r,TeX
+d,internal_heating,Heat_Transfer/internal_heating_git.txt,Heat_Transfer/internal_heating.csv,1,3,Time,HF,Analytical (HF),k-,0,100000,,400,600,-1.00E+09,1.00E+09,0,Heat_Transfer/internal_heating_devc.csv,2,3,Time,HF_1,FDS (HF_1),k--,0,100000,,400,600,-1.00E+09,1.00E+09,0,Heat Flow (internal_heating),Time (min),Heat Flow (kW),0,10.,60,0,0.08,1,no,0.05 0.90,SouthEast,,1,linear,FDS_User_Guide/SCRIPT_FIGURES/internal_heating,Relative Error,mean,0.01,Heat Transfer,r^,r,TeX
+f,internal_heating,Heat_Transfer/internal_heating_git.txt,Heat_Transfer/internal_heating.csv,1,3,Time,HF,blank,blank,0,100000,,400,600,-1.00E+09,1.00E+09,0,Heat_Transfer/internal_heating_devc.csv,2,3,Time,HF_2,FDS (HF_2),k:,0,100000,,400,600,-1.00E+09,1.00E+09,0,Heat Flow (internal_heating),Time (s),Heat Flow (kW),0,10.,60,0,0.08,1,no,0.05 0.90,SouthEast,,1,linear,FDS_User_Guide/SCRIPT_FIGURES/internal_heating,Relative Error,mean,0.01,Heat Transfer,r^,r,TeX
 d,isentropic,Pressure_Effects/isentropic_git.txt,Pressure_Effects/isentropic.csv,1,2,Time,Density_1|Density_2,Exact (Density_1)|Exact (Density_2),ko|ro,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Pressure_Effects/isentropic_devc.csv,2,3,Time,density_1|density_2,FDS (density_1)|FDS (density_2),k-|r-,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Density (isentropic),Time (s),Density (kg/m³),0,60,1,1.1,1.4,1,no,0.05 0.90,SouthEast,,1,linear,FDS_Verification_Guide/SCRIPT_FIGURES/isentropic_density,Relative Error,end,0.01,Pressure Effects,kd,k,TeX
 d,isentropic,Pressure_Effects/isentropic_git.txt,Pressure_Effects/isentropic.csv,1,2,Time,Pressure_1|Pressure_2,Exact (Pressure_1)|Exact (Pressure_2),ko|ro,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Pressure_Effects/isentropic_devc.csv,2,3,Time,pressure_1|pressure_2,FDS (pressure_1)|FDS (pressure_2),k-|r-,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Pressure (isentropic),Time (s),Pressure (Pa),0,60,1,0,25000,1,no,0.05 0.90,SouthEast,,1,linear,FDS_Verification_Guide/SCRIPT_FIGURES/isentropic_pressure,Relative Error,end,0.01,Pressure Effects,k+,k,TeX
 d,isentropic,Pressure_Effects/isentropic_git.txt,Pressure_Effects/isentropic.csv,1,2,Time,Temperature_1|Temperature_2,Exact (Temperature_1)|Exact (Temperature_2),ko|ro,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Pressure_Effects/isentropic_devc.csv,2,3,Time,temperature_1|temperature_2,FDS (temperature_1)|FDS (temperature_2),k-|r-,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Temperature (isentropic),Time (s),Temperature (°C),0,60,1,15,40,1,no,0.05 0.90,SouthEast,,1,linear,FDS_Verification_Guide/SCRIPT_FIGURES/isentropic_temperature,Relative Error,end,0.01,Pressure Effects,k+,k,TeX

Verification/FDS_Cases.sh

@@ -324,6 +324,7 @@ $QFDS -d Heat_Transfer ht3d_slab.fds
 $QFDS -d Heat_Transfer ht3d_sphere_24.fds
 $QFDS -p 4 -d Heat_Transfer ht3d_sphere_48.fds
 $QFDS -p 64 -d Heat_Transfer ht3d_sphere_96.fds
+$QFDS -d Heat_Transfer internal_heating.fds
 $QFDS -d Heat_Transfer back_wall.fds
 $QFDS -p 4 -d Heat_Transfer back_wall_test.fds
 $QFDS -p 3 -d Heat_Transfer back_wall_test_2.fds

Verification/Heat_Transfer/internal_heating.csv

@@ -0,0 +1,4 @@
+Time,HF
+s,kW
+400,0.0603
+600,0.0603

Verification/Heat_Transfer/internal_heating.fds

@@ -0,0 +1,54 @@
+&HEAD CHID='internal_heating', TITLE='Test INTERNAL_HEAT_SOURCE' /
+
+&MESH IJK=25,25,25, XB=-0.25, 0.25,-0.25, 0.25,0.00,0.50 /
+
+&TIME T_END=600. /
+
+&RADI RADIATION=F /
+
+&SURF ID = 'Cable'
+      THICKNESS = 0.002,0.008
+      MATL_ID(1,1) = 'PLASTIC'
+      MATL_ID(2,1) = 'METAL'
+      GEOMETRY = 'CYLINDRICAL'
+      LENGTH = 0.1
+      INTERNAL_HEAT_SOURCE = 0.,300. /
+
+&MATL ID = 'PLASTIC'
+      CONDUCTIVITY = 0.1
+      SPECIFIC_HEAT = 0.05
+      DENSITY = 100. /
+
+&MATL ID = 'METAL'
+      CONDUCTIVITY = 50.
+      SPECIFIC_HEAT = 0.1
+      DENSITY = 2000. /
+
+&PART ID='Cable Segment', SURF_ID='Cable', STATIC=.TRUE., SAMPLING_FACTOR=1, 
+      PROP_ID='Segment Image', QUANTITIES='PARTICLE TEMPERATURE' /
+
+&PROP ID='Segment Image', SMOKEVIEW_ID='tube', SMOKEVIEW_PARAMETERS='L=0.1','D=0.01','RANDXYZ=1' /
+
+&INIT N_PARTICLES=10, PART_ID='Cable Segment', XB=-0.15,0.15,-0.15,0.15,0.1,0.4 /
+
+&VENT MB='XMIN', SURF_ID='OPEN' /
+&VENT MB='XMAX', SURF_ID='OPEN' /
+&VENT MB='YMIN', SURF_ID='OPEN' /
+&VENT MB='YMAX', SURF_ID='OPEN' /
+&VENT MB='ZMIN', SURF_ID='OPEN' /
+&VENT MB='ZMAX', SURF_ID='OPEN' /
+
+&DUMP DT_HRR=10, DT_DEVC=10 /
+
+&BNDF QUANTITY='GAUGE HEAT FLUX', CELL_CENTERED=T  /
+&BNDF QUANTITY='WALL TEMPERATURE', CELL_CENTERED=T  /
+&BNDF QUANTITY='CONVECTIVE HEAT FLUX', CELL_CENTERED=T  /
+&BNDF QUANTITY='HEAT TRANSFER COEFFICIENT', CELL_CENTERED=T  /
+
+&SLCF PBZ=0.5, QUANTITY='TEMPERATURE', CELL_CENTERED=T /
+
+&DEVC ID='HF_1', QUANTITY='CONVECTIVE HEAT FLUX', SPATIAL_STATISTIC='SURFACE INTEGRAL', 
+      XB=-0.25,0.25,-0.25,0.25,0.0,0.5, CONVERSION_FACTOR=-1, PART_ID='Cable Segment' /
+&DEVC ID='HF_2', QUANTITY='ENTHALPY FLUX Z', SPATIAL_STATISTIC='AREA INTEGRAL', XB=-0.25,0.25,-0.25,0.25,0.5,0.5 /
+
+&TAIL /