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Merge pull request #15082 from cxp484/FireX
FireX: Merge with firemodels/master
2 parents fc9d99d + 68dc554 commit 3dfd1f3

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.github/workflows/linux.yml

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@@ -34,9 +34,9 @@ jobs:
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- uses: rscohn2/setup-oneapi@v0
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with:
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components: |
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ifx
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impi
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mkl
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ifx@2025.2.0
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impi@2021.16.0
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mkl@2025.2.0
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prune: false
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- uses: actions/checkout@v5
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steps:
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- uses: actions/checkout@v5
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- uses: actions/setup-python@v5
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- uses: actions/setup-python@v6
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with:
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python-version: '3.9'
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cache: 'pip' # caching pip dependencies

.github/workflows/windows.yml

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@@ -26,9 +26,9 @@ permissions:
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env:
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# update urls for oneapi packages according to
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# https://github.com/oneapi-src/oneapi-ci/blob/master/.github/workflows/build_all.yml
29-
WINDOWS_BASEKIT_URL: https://registrationcenter-download.intel.com/akdlm/IRC_NAS/09a8acaf-265f-4460-866c-a3375ed5b4ff/intel-oneapi-base-toolkit-2025.2.0.591_offline.exe
29+
WINDOWS_BASEKIT_URL: https://registrationcenter-download.intel.com/akdlm/IRC_NAS/f5881e61-dcdc-40f1-9bd9-717081ac623c/intel-oneapi-base-toolkit-2025.2.1.46_offline.exe
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WINDOWS_BASEKIT_COMPONENTS: intel.oneapi.win.mkl.devel
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WINDOWS_HPCKIT_URL: https://registrationcenter-download.intel.com/akdlm/IRC_NAS/3bbdaf75-6728-492e-a18c-be654dae9ee2/intel-oneapi-hpc-toolkit-2025.2.0.576_offline.exe
31+
WINDOWS_HPCKIT_URL: https://registrationcenter-download.intel.com/akdlm/IRC_NAS/e63ac2b4-8a9a-4768-979a-399a8b6299de/intel-oneapi-hpc-toolkit-2025.2.1.46_offline.exe
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WINDOWS_HPCKIT_COMPONENTS: intel.oneapi.win.ifort-compiler:intel.oneapi.win.mpi.devel
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Build/makefile

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@@ -403,7 +403,7 @@ ompi_gnu_linux : setup $(obj_mpi)
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$(FCOMPL) $(FFLAGS) $(FOPENMPFLAGS) -o $(obj) $(obj_mpi) $(LFLAGSMKL)
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# Add ignores for vtk library
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ompi_gnu_linux_db : FFLAGS = -O0 -std=f2018 -ggdb -Wall -Wunused-parameter -Wcharacter-truncation -Wno-target-lifetime -Wno-maybe-uninitialized -Wno-uninitialized -Wno-unused-function -fcheck=all -fbacktrace -ffpe-trap=invalid,zero,overflow -frecursive -ffpe-summary=none -fall-intrinsics -fbounds-check $(GITINFOGNU) $(FFLAGSMKL) $(GFORTRAN_OPTIONS) $(FFLAGS_HYPRE) $(FFLAGS_SUNDIALS) $(FFLAGS_HDF5)
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ompi_gnu_linux_db : FFLAGS = -O0 -std=f2018 -ggdb -finit-real=snan -finit-integer=-999999 -Wall -Wunused-parameter -Wcharacter-truncation -Wno-target-lifetime -Wno-maybe-uninitialized -Wno-uninitialized -Wno-unused-function -fcheck=all -fbacktrace -ffpe-trap=invalid,zero,overflow -frecursive -ffpe-summary=none -fall-intrinsics -fbounds-check $(GITINFOGNU) $(FFLAGSMKL) $(GFORTRAN_OPTIONS) $(FFLAGS_HYPRE) $(FFLAGS_SUNDIALS) $(FFLAGS_HDF5)
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ompi_gnu_linux_db : LFLAGSMKL = $(LFLAGSMKL_GNU_OPENMP) $(LFLAGS_HYPRE) $(LFLAGS_SUNDIALS) $(LFLAGS_HDF5) $(LFLAGS_GPU)
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ompi_gnu_linux_db : FCOMPL = $(COMP_FC)
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ompi_gnu_linux_db : FOPENMPFLAGS = -fopenmp

Manuals/Bibliography/FDS_general.bib

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@@ -4068,6 +4068,17 @@ @ARTICLE{Mawhinney:FT2012
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year = {2012}
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}
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@ARTICLE{McCaffrey:1976,
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author = {B.J. McCaffrey and G. Heskestad},
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title = {{A Robust Bidirectional Low-Velocity Probe
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for Flame and Fire Application}},
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journal = {Combustion and Flame},
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volume = {26},
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number = {},
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pages = {125-127},
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year = {1976},
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}
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@TECHREPORT{McCaffrey:NBSIR_79-1910,
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author = {McCaffrey, B.J.},
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title = {{Purely Buoyant Diffusion Flames: Some Experimental Results}},

Manuals/FDS_User_Guide/FDS_User_Guide.tex

Lines changed: 13 additions & 2 deletions
Original file line numberDiff line numberDiff line change
@@ -10554,7 +10554,7 @@ \subsection{Thermocouples}
1055410554
\tau = \frac{D_{\rm eff} \, \rho_{\rm eff} \, c_{\rm eff} }{6 \, h} \quad ; \quad h=\frac{k \, \NU}{D_{\rm eff}} \quad ; \quad \NU = 2 + 0.6 \, \RE^{1/2} \, \PR^{1/3} \quad ; \quad
1055510555
\RE = \frac{\rho \|\bu\| D_{\rm eff}}{\mu} \label{TC_tau}
1055610556
\ee
10557-
For a given value of the time constant, $\tau$, and effective thermal properties, Eq.~(\ref{TC_tau}) can be solved implicitly for the effective diameter. The \ct{TIME_CONSTANT} is specified on a \ct{PROP} line which is identified by the \ct{DEVC} line using a \ct{PROP_ID}. If you specify the \ct{TIME_CONSTANT}, you can still specify the effective \ct{EMISSIVITY}, \ct{DENSITY}, \ct{SPECIFIC_HEAT}, and \ct{HEAT_TRANSFER_COEFFICIENT} as well, but not the \ct{DIAMETER} because this will be calculated automatically. In most cases, it is sufficient to simply specify the \ct{TIME_CONSTANT}.
10557+
For a given value of the time constant, $\tau$, and effective thermal properties, Eq.~(\ref{TC_tau}) can be solved implicitly for the effective diameter. The \ct{TIME_CONSTANT} is specified on a \ct{PROP} line which is identified by the \ct{DEVC} line using a \ct{PROP_ID}. If you specify the \ct{TIME_CONSTANT}, you can still specify the effective \ct{EMISSIVITY}, \ct{DENSITY}, \ct{SPECIFIC_HEAT} (or \ct{SPECIFIC_HEAT_RAMP}), and \ct{HEAT_TRANSFER_COEFFICIENT} as well, but not the \ct{DIAMETER} because this will be calculated automatically. In most cases, it is sufficient to simply specify the \ct{TIME_CONSTANT}.
1055810558

1055910559
Figure~\ref{fig:thermocouple_time_constant} shows the results of a simple test case called \ct{thermocouple_time_constant} whose input file is in the \ct{Heat_Transfer} samples folder. Three thermocouples with given time constants of 0.5~s, 3.0~s, and 8.0~s are suddenly subjected to a 20~m/s air stream of 30~$^\circ$C. It is expected that each TC should reach a temperature of 26.32~$^\circ$C at their given time constants.
1056010560
\begin{figure}[!ht]
@@ -10566,13 +10566,24 @@ \subsection{Thermocouples}
1056610566

1056710567
\subsection{Bi-Directional Probe}
1056810568
\label{info:bidir_probe}
10569+
\label{bi_dir}
1056910570

1057010571
The output quantity \ct{BI-DIRECTIONAL PROBE} is the velocity of a modeled bi-directional probe. A bi-directional probe uses the following equation:
1057110572
\be
1057210573
C \sqrt{\frac{2 \Delta P}{\rho}}
1057310574
\label{BDP}
1057410575
\ee
10575-
where $C$ is a calibration constant (default value is 0.93), $\Delta P$ is the pressure difference across the probe, and $\rho$ is the gas density at the probe. In a typical experiment, the gas density is computed assuming standard pressure (101325 Pa), the molecular weight of air (28.8 g/mol), and the temperature as measured by a thermocouple near the probe. Bi-directional probes have biases due to both the Reynolds number (based on the probe diameter) of the flow and the angle of the flow with respect to the probe axis. This model accounts for those sensitivities and the impact of density differences from varied molecular weight at the probe. The orientation of the probe can be specified with either \ct{IOR} or \ct{ORIENTATION} on \ct{DEVC}. A probe with \ct{IOR}=-1 would have a positive velocity output when the flow is in the negative x direction. Parameters for the probe can be specified with a \ct{PROP_ID} on the \ct {DEVC}. The calibration constant and the probe diameter (default of 0.0254 m) can be set respectively with \ct{CALIBRATION_CONSTANT} and \ct{PROBE_DIAMETER} on \ct{PROP}. If the probe temperature is an aspirated thermocouple or other measurement not sensitive to the radiative environment, then set \ct{TC=F} on \ct{PROP}.
10576+
where $C$ is a calibration constant (default value is 0.93), $\Delta P$ is the pressure difference across the probe, and $\rho$ is the gas density at the probe. In a typical experiment, the gas density is computed assuming standard pressure (101325 Pa), the molecular weight of air (28.8 g/mol), and the temperature as measured by a thermocouple near the probe.
10577+
10578+
Bi-directional probes have biases due to both the Reynolds number (based on the probe diameter) of the flow and the angle of the flow with respect to the probe axis~\cite{McCaffrey:1976}. At low Reynolds number a probe will measure a higher effective velocity. As the angle of the flow vector with the axis increases, the effective velocity at first increases up to an angle of 30$^\circ$ due to a low pressure region forming downstream of the probe, and then decreases reaching no measured flow at an angle of 90$^\circ$. This model accounts for these sensitivities and the impact of density differences from varied molecular weight at the probe. The orientation of the probe can be specified with either \ct{IOR} or \ct{ORIENTATION} on \ct{DEVC}. A probe with \ct{IOR}=-1 would have a positive velocity output when the flow is in the -x direction. Parameters for the probe can be specified with a \ct{PROP_ID} on the \ct {DEVC}. The calibration constant (default of 0.93) and the probe diameter (default of 0.0254 m) can be set respectively with \ct{CALIBRATION_CONSTANT} and \ct{PROBE_DIAMETER} on \ct{PROP}. If the probe temperature is an aspirated thermocouple or other measurement not sensitive to the radiative environment, then set \ct{TC=F} on \ct{PROP}. Thermocouple specific properties for a bi-directional probe, see Section~\ref{info:THERMOCOUPLE}, should be set with the same \ct{PROP} as for the probe.
10579+
10580+
Figure~\ref{bi_dir_fig} shows the results of a bi-directional probe with varying angle to a 1~m/s flow and varying flow speed.
10581+
\begin{figure}[ht]
10582+
\includegraphics[width=3in]{SCRIPT_FIGURES/bi_dir}
10583+
\includegraphics[width=3in]{SCRIPT_FIGURES/bi_dir_2}
10584+
\caption[Results of the \ct{bi_dir} test case]{Measured velocities using a bi-directional probe. (Left) Varying angle for a 1~m/s flow. (Right) Probe axis aligned flow with varied flow speed.}
10585+
\label{bi_dir_fig}
10586+
\end{figure}
1057610587

1057710588
\subsection{Volume Flow}
1057810589
\label{info:volume_flow}

Source/wall.f90

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Original file line numberDiff line numberDiff line change
@@ -10,7 +10,7 @@ MODULE WALL_ROUTINES
1010
PRIVATE
1111

1212
REAL(EB), POINTER, DIMENSION(:,:) :: PBAR_P
13-
REAL(EB), POINTER, DIMENSION(:,:,:) :: RHOP,HP,UU,VV,WW
13+
REAL(EB), POINTER, DIMENSION(:,:,:) :: RHOP,UU,VV,WW
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REAL(EB), POINTER, DIMENSION(:,:,:,:) :: ZZP
1515

1616
PUBLIC WALL_BC,TGA_ANALYSIS,HT3D_TEMPERATURE_EXCHANGE
@@ -57,15 +57,13 @@ SUBROUTINE WALL_BC(T,DT,NM)
5757
RHOP => RHOS
5858
ZZP => ZZS
5959
PBAR_P => PBAR_S
60-
HP => HS
6160
ELSE
6261
UU => U
6362
VV => V
6463
WW => W
6564
RHOP => RHO
6665
ZZP => ZZ
6766
PBAR_P => PBAR
68-
HP => H
6967
ENDIF
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! For thermally-thick boundary conditions, set the flag, CALL_HT_1D, to call the subroutine SOLID_HEAT_TRANSFER.
@@ -924,7 +922,7 @@ SUBROUTINE CALCULATE_ZZ_F(T,DT,WALL_INDEX,CFACE_INDEX,PARTICLE_INDEX)
924922
REAL(EB) :: T_SCALE(MAX_QDOTPP_REF),QDOTPP_REF(MAX_QDOTPP_REF),QDOTPP_T(MAX_QDOTPP_REF), &
925923
QDOTPP,QDOTPP1,QDOTPP2,DT_SPYRO(MAX_QDOTPP_REF),CP,H_G,MW_RATIO
926924
REAL(EB) :: RVC,M_DOT_PPP_SINGLE,ZZ_GET(1:N_TRACKED_SPECIES),DENOM
927-
INTEGER :: N,NS,IDX1,IDX2,NQ,ITER,IIO,JJO,KKO,OBST_INDEX,OTHER_MESH_OBST_INDEX,LL,SPECIES_BC_INDEX,IC,ICG,N_ZZ_MAX
925+
INTEGER :: N,NS,IDX1,IDX2,NQ,ITER,IIO,JJO,KKO,OBST_INDEX,OTHER_MESH_OBST_INDEX,LL,SPECIES_BC_INDEX,IC,ICG
928926
INTEGER, INTENT(IN), OPTIONAL :: WALL_INDEX,CFACE_INDEX,PARTICLE_INDEX
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TYPE(RAMPS_TYPE), POINTER :: RP,RP_E2T,RP_REF
930928
TYPE(EXTERNAL_WALL_TYPE), POINTER :: EWC
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10311029
IF (B1%U_NORMAL_S<0._EB) THEN ! If there is a non-zero velocity into the domain, assign appropriate species
10321030
! mass fractions to the face
1033-
DO N=1,N_TRACKED_SPECIES
1031+
DO N=2,N_TRACKED_SPECIES
10341032
ZZ_GET(N) = SPECIES_MIXTURE(N)%ZZ0 + EVALUATE_RAMP(TSI,SF%RAMP(N)%INDEX,TAU=SF%RAMP(N)%TAU)* &
10351033
(SF%MASS_FRACTION(N)-SPECIES_MIXTURE(N)%ZZ0)
10361034
ENDDO
1037-
N_ZZ_MAX = MAXLOC(ZZ_GET(1:N_TRACKED_SPECIES),1)
1038-
ZZ_GET(N_ZZ_MAX) = 1._EB-SUM(ZZ_GET(1:N_ZZ_MAX-1))-SUM(ZZ_GET(N_ZZ_MAX+1:N_TRACKED_SPECIES))
1035+
ZZ_GET(1) = 1._EB-SUM(ZZ_GET(2:N_TRACKED_SPECIES))
10391036
CALL GET_REALIZABLE_MF(ZZ_GET)
10401037
B1%ZZ_F = ZZ_GET
10411038
ELSE
@@ -1330,9 +1327,10 @@ SUBROUTINE CALCULATE_ZZ_F(T,DT,WALL_INDEX,CFACE_INDEX,PARTICLE_INDEX)
13301327
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13311328

13321329
IF (PRESENT(WALL_INDEX)) THEN
1333-
IF (WALL_INDEX<=N_EXTERNAL_WALL_CELLS .AND. .NOT.CELL(IC)%SOLID .AND. .NOT.CELL(ICG)%SOLID) &
1334-
ZZP(BC%II,BC%JJ,BC%KK,1:N_TRACKED_SPECIES) = 2._EB*B1%ZZ_F(1:N_TRACKED_SPECIES) - B1%ZZ_G(1:N_TRACKED_SPECIES)
1335-
ZZP(BC%II2,BC%JJ2,BC%KK2,1:N_TRACKED_SPECIES) = 2._EB*B1%ZZ_F(1:N_TRACKED_SPECIES) - B1%ZZ_G(1:N_TRACKED_SPECIES)
1330+
IF (WALL_INDEX<=N_EXTERNAL_WALL_CELLS .AND. .NOT.CELL(IC)%SOLID .AND. .NOT.CELL(ICG)%SOLID) THEN
1331+
ZZP(BC%II,BC%JJ,BC%KK,1:N_TRACKED_SPECIES) = 2._EB*B1%ZZ_F(1:N_TRACKED_SPECIES) - B1%ZZ_G(1:N_TRACKED_SPECIES)
1332+
ZZP(BC%II2,BC%JJ2,BC%KK2,1:N_TRACKED_SPECIES) = 2._EB*B1%ZZ_F(1:N_TRACKED_SPECIES) - B1%ZZ_G(1:N_TRACKED_SPECIES)
1333+
ENDIF
13361334
ENDIF
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13381336
END SUBROUTINE CALCULATE_ZZ_F

Utilities/Matlab/FDS_verification_dataplot_inputs.csv

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d,back_wall_test_2,Heat_Transfer/back_wall_test_2_git.txt,Heat_Transfer/back_wall_test_2_devc.csv,2,3,Time,T_F_Target|T_B_Target,Exact Front|Exact Back,ko|ro,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Heat_Transfer/back_wall_test_2_devc.csv,2,3,Time,T_F3|T_B3,FDS Front|FDS Back,k-|r-,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Rotated GEOM Surface Temp. (back\_wall\_test\_2),Time (s),Temperature (°C),0,20,1,0,1000,1,no,0.05 0.90,SouthEast,,1,linear,FDS_Verification_Guide/SCRIPT_FIGURES/back_wall_test_2_temp_geom_rotated,Relative Error,end,0.02,Heat Transfer,r^,r,TeX
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d,beam_detector,Detectors/beam_detector_git.txt,Detectors/beam_detector.csv,1,2,Time,Obs|Obs|Obs,Exact|Exact|Exact,k-|k-|k-,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Detectors/beam_detector_devc.csv,2,3,Time,beam_1|beam_2|beam_3,FDS (beam\_1)|FDS (beam\_2)|FDS (beam\_3),ko|ro|go,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Path Obscuration (beam\_detector),Time (s),Path Obscuration (%),0,1,1,0,110,1,no,0.25 0.90,East,,1,linear,FDS_User_Guide/SCRIPT_FIGURES/beam_detector_obs,Relative Error,end,0.01,Aerosols,r^,r,TeX
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d,beam_detector,Detectors/beam_detector_git.txt,Detectors/beam_detector_ss_check.csv,1,2,L,value,Exact,k-,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Detectors/beam_detector_ss_smv.csv,1,2,L,value,Smokeview,ko,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Smoke Obscuration (beam\_detector),Distance (m),Pixel Value,0,10,1,0,255,1,no,0.25 0.90,East,,1,linear,FDS_User_Guide/SCRIPT_FIGURES/beam_detector,N/A,end,0.02,Aerosols,r^,r,TeX
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d,bi_dir,Controls/bi_dir_git.txt,Controls/bi_dir.csv,1,2,Time,V1_0|V1_180|V1_30|V1_55,Expected 0^\circ|Expected 180^\circ|Expected 30^\circ|Expected 55^\circ,ko|ro|bo|go,0,100000,,5,100000,-1.00E+09,1.00E+09,0,Controls/bi_dir_devc.csv,2,3,Time,V1_0|V1_180|V1_30|V1_55,FDS 0^\circ|FDS 180^\circ|FDS 30^\circ|FDS 55^\circ,k-|r-|b-|g-,0,100000,,5,100000,-1.00E+09,1.00E+09,0,Measured Velocity (bi\_dir),Time (s),Velocity (m/s),0,20,1,-1.5,1.5,1,no,0.25 0.92,East,,1,linear,FDS_User_Guide/SCRIPT_FIGURES/bi_dir,Relative Error,mean,0.02,Controls,kd,k,TeX
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d,bi_dir,Controls/bi_dir_git.txt,Controls/bi_dir.csv,1,2,Time,Vp1_0|V10_0,Expected 0.1 m/s \times 100 |Expected 10 m/s,ko|ro,0,100000,,5,100000,-1.00E+09,1.00E+09,0,Controls/bi_dir_devc.csv,2,3,Time,Vp1_0|V10_0,FDS 0.1 m/s \times 100 |FDS 10 m/s,k-|r-,0,100000,,5,100000,-1.00E+09,1.00E+09,0,Measured Velocity (bi\_dir),Time (s),Velocity (m/s),0,20,1,0,15,1,no,0.25 0.92,SouthEast,,1,linear,FDS_User_Guide/SCRIPT_FIGURES/bi_dir_2,Relative Error,mean,0.02,Controls,kd,k,TeX
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d,bound_test_1,Species/bound_test_1_git.txt,Species/bound_test_1.csv,1,2,Time,F1|A1|P1|F2|A2|P2|Sum,F1|A1|P1|F2|A2|P2|Sum,ko|ro|bo|go|mo|co|k+,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Species/bound_test_1_devc.csv,2,3,Time,XF1|XA1|XP1|XF2|XA2|XP2|SUM,FDS F1|FDS A1|FDS P1|FDS F2|FDS A2|FDS P2|FDS SUM,k-|r-|b-|g-|m-|c-|k--,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Boundedness Test (bound\_test\_1),Time (s),Volume Fraction,0,1,1,0,1.05,1,no,0.05 0.90,EastOutside,,1.3,linear,FDS_Verification_Guide/SCRIPT_FIGURES/bound_test_1,Absolute Error,end,0.001,Species,kd,k,TeX
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d,bound_test_2,Species/bound_test_2_git.txt,Species/bound_test_2.csv,1,2,Time,F1|F2|A1|A2|P1|P2|P3|Sum,F1|F2|A1|A2|P1|P2|P3|Sum,ko|ro|bo|go|mo|co|yo|k+,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Species/bound_test_2_devc.csv,2,3,Time,XF1|XF2|XA1|XA2|XP1|XP2|XP3|SUM,FDS F1|FDS F2|FDS A1|FDS A2|FDS P1|FDS P2|FDS P3|FDS SUM,k-|r-|b-|g-|m-|c-|y-|k--,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Boundedness Test (bound\_test\_2),Time (s),Volume Fraction,0,1,1,0,1.05,1,no,0.05 0.90,EastOutside,,1.3,linear,FDS_Verification_Guide/SCRIPT_FIGURES/bound_test_2,Absolute Error,end,0.001,Species,kd,k,TeX
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d,box_burn_away1,Fires/box_burn_away1_git.txt,Fires/box_burn_away.csv,1,2,Time,Mass (kg),Ideal,ko,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Fires/box_burn_away1_devc.csv,2,3,Time,Mass fuel,FDS (fuel),k-,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Pyrolyzed Mass (box\_burn\_away1),Time (s),Mass (kg),0,30,1,0,1.5,1,no,0.05 0.90,East,,1,linear,FDS_User_Guide/SCRIPT_FIGURES/box_burn_away1,Relative Error,end,0.02,Fires,r*,r,TeX

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