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Manuals: minor edits
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Manuals/FDS_User_Guide/FDS_User_Guide.tex

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@@ -9139,7 +9139,7 @@ \section{Flux Limiters}
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Central differencing & \ct{'CENTRAL'} \\
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Godunov & \ct{'GODUNOV'} \\
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Superbee (VLES, SVLES default) & \ct{'SUPERBEE'} \\
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CHARM (DNS, LES default) & \ct{'CHARM'} \\
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CHARM (DNS, LES default) & \ct{'CHARM'} \\
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\hline
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\end{tabular}
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\end{table}
@@ -14426,8 +14426,8 @@ \chapter{Error Codes}
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610 \> \ct{HOLE ... Cannot overlap HOLEs with a DEVC or CTRL_ID.} \> Section~\ref{info:HOLE} \\
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611 \> \ct{OBST ... has a BULK_DENSITY but zero volume.} \> Section~\ref{info:BURN_AWAY} \\
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612 \> \ct{OBST ... must have a volume to be assigned HT3D.} \> Section~\ref{checkerboard} \\
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614 \> \ct{OBST_ID ... cannot have a SURF with NODE_ID} \> Section~\ref{info:hvac_geom} \\
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615 \> \ct{OBST ... cannot overlap OBST ...} \> Section~\ref{info:OVERLAY} \\
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614 \> \ct{OBST_ID ... cannot have a SURF with NODE_ID} \> Section~\ref{info:hvac_geom} \\
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615 \> \ct{OBST ... cannot overlap OBST ...} \> Section~\ref{info:OVERLAY} \\
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\> \> \\
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701 \> \ct{problem with GEOM, local SURF_ID index ... out of bounds.} \> Section~\ref{info:GEOM_Basics} \\
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702 \> \ct{problem with GEOM, SURF_IDS not defined properly.} \> Section~\ref{info:first_geom} \\

Manuals/FDS_Verification_Guide/FDS_Verification_Guide.tex

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@@ -5141,7 +5141,7 @@ \subsection{Case 8: 2-D Heat Transfer with Temperature-Dependent Conductivity}
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\FloatBarrier
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\subsection{Case 9: 2-D Heat Transfer in a Composite Section with Temperature-Dependent Conductivity}
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\subsection{Case 9: 2-D Heat Transfer in a Composite Section, Variable Conductivity}
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\label{SFPE_Case_9}
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A hollow square metal tube ($\rho=7850$~kg/m$^3$, $c=0.6$~kJ/(kg~K), $\epsilon=0.8$) is filled with an insulation material ($k=0.05$~W/(m~K), $\rho=50$~kg/m$^3$, $c=1$~kJ/(kg~K)). The thermal conductivity of the metal tube varies linearly with temperature such that its value is 54.7~W/(m~K) at 0~°C, 27.3~W/(m~K) at 800~°C, and 27.3~W/(m~K) at 1200~°C. The tube walls are 0.5~mm thick, and the exterior width of the assembly is 0.201~m. The surrounding air temperature is 1000~°C, and the initial temperature of the assembly is 0~°C. Assuming that the heating is by convection and radiation, and that the heat transfer coefficient is 10~W/(m$^2$~K), calculate the temperature at the center of the tube as a function of time (Fig.~\ref{fig:SFPE_Case_9}).

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