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Merge remote-tracking branch 'firemodels/master' into FireX
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Manuals/FDS_Verification_Guide/FDS_Verification_Guide.tex

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@@ -6536,7 +6536,7 @@ \subsection{Case 7}
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A gas burner lies near the bottom of a 1~m by 1~m by 5~m high vertical channel whose walls are made of a thin sheet of insulated steel. Air at 20~$^\circ$C is forced into the bottom of the channel at 1~m/s. Mono-disperse water droplets with a diameter of $2\,000~\mu$m are introduced via a nozzle in the middle of the channel at a rate of 0.5~L/min, starting at 60~s. The water temperature is 20~\si{\degree C}, and the spray is directed at the walls with an initial velocity of 5~m/s. The water completely evaporates before it drips down to the bottom of the channel. Figure~\ref{water_evaporation_7_plot} displays the energy balance for this case. The heat release rate, \ct{HRR}, of the fire is expected to be 384~kW. The rate at which the water droplets extract energy from the system, \ct{Q_PART}, is expected to be
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\be - \left( 4.189 \; \hbox{\si{kJ/(kg.K)}} \times 80 \; \hbox{K} + 2269 \; \hbox{kJ/kg} \right) \times 0.5/60 \; \hbox{kg/s} = -21.7 \; \hbox{kW} \ee
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The sum of all the terms, \ct{Q_TOTAL}, is expected to be zero. The three other quantities, \ct{Q_COND}, \ct{Q_RADI}, \ct{Q_CONV}, all have plausible values, but there is no way to determine the exact values.
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The sum of all the terms, \ct{Q_TOTAL}, is expected to be zero.
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\begin{figure}[h!]
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\centering

Utilities/Python/FDS_validation_dataplot_inputs.csv

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Utilities/Python/FDS_verification_dataplot_inputs.csv

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@@ -767,7 +767,7 @@ f,water_evaporation_5,Sprinklers_and_Sprays/water_evaporation_5_git.txt,../../ex
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d,water_evaporation_6,Sprinklers_and_Sprays/water_evaporation_6_git.txt,Sprinklers_and_Sprays/water_evaporation_6.csv,1,2,Time,T_gas|T_wall,Exact (T_gas)|Exact (T_wall),ko|ro,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Sprinklers_and_Sprays/water_evaporation_6_devc.csv,2,3,Time,T_gas|T_wall,FDS (T_gas)|FDS (T_wall),k-|r-,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Temperature (water_evaporation_6),Time (s),Temperature (°C),0,200,1,90,260,1,no,0.05 0.90,SouthEast,,1,linear,FDS_Verification_Guide/SCRIPT_FIGURES/water_evaporation_6_T,Relative Error,end,0.01,Sprinklers and Sprays,bs,b,TeX
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d,water_evaporation_6,Sprinklers_and_Sprays/water_evaporation_6_git.txt,Sprinklers_and_Sprays/water_evaporation_6.csv,1,2,Time,Pressure,Exact (Pressure),ko,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Sprinklers_and_Sprays/water_evaporation_6_devc.csv,2,3,Time,pres,FDS (pres),k-,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Pressure Rise (water_evaporation_6),Time (s),Pressure (kPa),0,200,1,0,40,1000,no,0.05 0.90,SouthEast,,1,linear,FDS_Verification_Guide/SCRIPT_FIGURES/water_evaporation_6_P,Relative Error,end,0.015,Sprinklers and Sprays,bs,b,TeX
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d,water_evaporation_6,Sprinklers_and_Sprays/water_evaporation_6a_git.txt,Sprinklers_and_Sprays/water_evaporation_6a.csv,1,2,Time,sum,Exact (sum),ko,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Sprinklers_and_Sprays/water_evaporation_6a_devc.csv,2,3,Time,u_gas|h_liquid|sum,FDS (u_gas)|FDS (h_liquid)|FDS (sum),r-|b-|k-,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Change in Energy (water_evaporation_6a),Time (s),Change in Energy (kJ),0,20,1,-10,10,1,no,0.05 0.90,East,,1,linear,FDS_Verification_Guide/SCRIPT_FIGURES/water_evaporation_6a,Absolute Error,mean_1_3,0.01,Sprinklers and Sprays,bs,b,TeX
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d,water_evaporation_7,Sprinklers_and_Sprays/water_evaporation_7_git.txt,Sprinklers_and_Sprays/water_evaporation_7.csv,1,2,Time,HRR|Q_TOTAL|Q_PART,Expected (HRR)|Expected (Q_TOTAL)|Expected (Q_PART),ko|go|bo,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Sprinklers_and_Sprays/water_evaporation_7_hrr.csv,2,3,Time,HRR|Q_COND|Q_TOTAL|Q_PART|Q_RADI|Q_CONV,FDS (HRR)|FDS (Q_COND)|FDS (Q_TOTAL)|FDS (Q_PART)|FDS (Q_RADI)|FDS (Q_CONV),k-|r-|g-|b-|c-|m-,0,100000,,100,200,-1.00E+09,1.00E+09,0,Energy Budget (water_evaporation_7),Time (s),Heat Loss/Gain (kW),0,200,1,-400,600,1,no,0.05 0.90,EastOutside,,1.35,linear,FDS_Verification_Guide/SCRIPT_FIGURES/water_evaporation_7,Relative Error,mean_3_4,0.01,Sprinklers and Sprays,kd,k,TeX
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d,water_evaporation_7,Sprinklers_and_Sprays/water_evaporation_7_git.txt,Sprinklers_and_Sprays/water_evaporation_7.csv,1,2,Time,HRR|Q_TOTAL|Q_PART,Expected (HRR)|Expected (Q_TOTAL)|Expected (Q_PART),ko|go|bo,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Sprinklers_and_Sprays/water_evaporation_7_hrr.csv,2,3,Time,HRR|Q_TOTAL|Q_PART,FDS (HRR)|FDS (Q_TOTAL)|FDS (Q_PART),k-|g-|b-,0,100000,,100,200,-1.00E+09,1.00E+09,0,Energy Budget (water_evaporation_7),Time (s),Heat Loss/Gain (kW),0,200,1,-400,600,1,no,0.05 0.90,EastOutside,,1.35,linear,FDS_Verification_Guide/SCRIPT_FIGURES/water_evaporation_7,Relative Error,mean,0.01,Sprinklers and Sprays,kd,k,TeX
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d,water_evaporation_8,Sprinklers_and_Sprays/water_evaporation_8_git.txt,Sprinklers_and_Sprays/water_evaporation_8.csv,1,2,Time,z,Measured,ko,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Sprinklers_and_Sprays/water_evaporation_8_devc.csv,2,3,Time,z_thin,FDS thermally thin,k-,0,100000,,0,100000,-1.00E+09,1.00E+09,0,(water_evaporation_8),Time (s),Position (m),0,16,1,0.5,4,1,no,0.05 0.90,East,,1,linear,FDS_Verification_Guide/SCRIPT_FIGURES/water_evaporation_8_z,Absolute Error,end,0.05,Sprinklers and Sprays,kd,k,TeX
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f,water_evaporation_8,Sprinklers_and_Sprays/water_evaporation_8_git.txt,Sprinklers_and_Sprays/water_evaporation_8.csv,1,2,Time,z,blank,blank,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Sprinklers_and_Sprays/water_evaporation_8_devc.csv,2,3,Time,z_thick,FDS thermally thick,r--,0,100000,,0,100000,-1.00E+09,1.00E+09,0,(water_evaporation_8),Time (s),Position (m),0,16,1,0.5,4,1,no,0.05 0.90,East,,1,linear,FDS_Verification_Guide/SCRIPT_FIGURES/water_evaporation_8_z,Absolute Error,end,0.05,Sprinklers and Sprays,kd,k,TeX
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d,water_evaporation_8,Sprinklers_and_Sprays/water_evaporation_8_git.txt,Sprinklers_and_Sprays/water_evaporation_8.csv,1,2,Time,d,Measured,ko,0,100000,,0,100000,-1.00E+09,1.00E+09,0,Sprinklers_and_Sprays/water_evaporation_8_devc.csv,2,3,Time,D_thin,FDS thermally thin,k-,0,100000,,0,100000,-1.00E+09,1.00E+09,0,(water_evaporation_8),Time (s),Diameter (µm),0,16,1,0,120,1,no,0.05 0.90,Southwest,,1,linear,FDS_Verification_Guide/SCRIPT_FIGURES/water_evaporation_8_d,Absolute Error,end,5,Sprinklers and Sprays,kd,k,TeX

Utilities/Python/scripts/Memorial_Tunnel.py

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x_min=0, x_max=16, y_min=0, y_max=400,
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revision_label=version_string,
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x_label='Number of Fans',
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y_label='Volume Flow (m$^3$/s)')
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y_label='Volume Flow (m³/s)')
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fdsplotlib.plot_to_fig(x_data=M.data[mod_time_index,0]/300, y_data=M.data[mod_time_index,1],
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marker_style='ko-', marker_fill_color='none', data_label='FDS', figure_handle=fig)
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Utilities/Python/scripts/NIST_NRC_Parallel_Panels.py

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fig = fdsplotlib.plot_to_fig(x_data=[-1,-1], y_data=[-1,-1],
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x_min=0, x_max=150, y_min=0, y_max=250,
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revision_label=version_string,
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x_label='Heat Flux (kW/m$^2$)',
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x_label='Heat Flux (kW/m²)',
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y_label='Height (cm)')
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qdot = {}
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fig = fdsplotlib.plot_to_fig(x_data=[-1,-1], y_data=[-1,-1],
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x_min=0, x_max=80, y_min=0, y_max=180,
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revision_label=version_string,
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x_label='Heat Flux (kW/m$^2$)',
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x_label='Heat Flux (kW/m²)',
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y_label='Height (cm)')
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# Plot experimental data

Utilities/Python/scripts/Sandia_Plumes.py

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plot_title='Sandia Methane Pool Fire, Test 17',
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plot_type='loglog',
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x_label='Frequency (Hz)',
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y_label='Autospectral Density (m$^2$/s)')
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y_label='Autospectral Density (m²/s)')
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# Find peak frequency
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k_fds = np.where(pave[k-1].real == np.max(pave[k-1].real))[0]

Utilities/Python/scripts/Sandia_Pools.py

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plot_origin=(plot_style['Scat_Plot_X'],plot_style['Scat_Plot_Y']),
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legend_location='upper left',
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revision_label=version_string,
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x_label='Measured Heat Flux (kW/m$^2$)',
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y_label='Predicted Heat Flux (kW/m$^2$)'
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x_label='Measured Heat Flux (kW/m²)',
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y_label='Predicted Heat Flux (kW/m²)'
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)
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for i in range(4):

Utilities/Python/scripts/compression_wave.py

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x_min=0, x_max=12.5, y_min=0, y_max=8,
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revision_label=version_string,
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x_label='Time (s)',
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y_label=r'Density (kg/m$^3$)',
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usetex=True)
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y_label='Density (kg/m³)')
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fdsplotlib.plot_to_fig(x_data=t_FL4_16, y_data=rho_fds_FL4_16, marker_style='c--', data_label=r'FDS $N=16$', figure_handle=fig)
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fdsplotlib.plot_to_fig(x_data=t_FL4_32, y_data=rho_fds_FL4_32, marker_style='g--', data_label=r'FDS $N=32$', figure_handle=fig)
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plot_type='loglog',
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x_label='Grid Spacing (m)',
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y_label=r'L2 Error (kg/m$^3$)',
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usetex=True)
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y_label='L2 Error (kg/m³)')
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fdsplotlib.plot_to_fig(x_data=h, y_data=0.1*h**2, marker_style='k-', data_label=r'${\cal O}(\delta x^2)$', figure_handle=fig)
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fdsplotlib.plot_to_fig(x_data=h, y_data=e_FL0, marker_style='b*-', data_label='Central', figure_handle=fig)

Utilities/Python/scripts/fan_curve.py

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fig = fdsplotlib.plot_to_fig(x_data=[vdot1,vdot1], y_data=[-1000,1000], marker_style='r-', data_label='constant volume',
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x_min=-10, x_max=20, y_min=-1000, y_max=1000,
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x_label='Volume Flow Rate (m$^3$/s)',
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x_label='Volume Flow Rate (m³/s)',
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fdsplotlib.plot_to_fig(x_data=vdot, y_data=dp, marker_style='k-', data_label='quadratic', figure_handle=fig)

Utilities/Python/scripts/plate_view_factor.py

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plot_title=r'Radiative Heat Flux (plate_view_factor)',
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x_label='Number of Radiation Angles',
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y_label='Heat Flux (kW/m²)')
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fdsplotlib.plot_to_fig(x_data=NRA, y_data=Exact_Flux_2D*np.ones(3), marker_style='r-', figure_handle=fig)
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fdsplotlib.plot_to_fig(x_data=NRA, y_data=Flux_2D , marker_style='ro', data_label='FDS 2D', figure_handle=fig)

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