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FDS Tech Guide: fix instance of \ct{}
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Manuals/FDS_Technical_Reference_Guide/Appendices.tex

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@@ -352,7 +352,7 @@ \section{Simplifications for Constant Specific Heat}
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\begin{align}
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\rho h_s = \rho c_p T = \rho T \sum_\alpha Y_\alpha c_{p,\alpha} = \rho R T \left(\frac{\gamma}{\gamma-1}\right)\sum_\alpha \frac{Y_\alpha}{W_\alpha} = \rho \frac{R T}{\overline{W}} \left(\frac{\gamma}{\gamma-1}\right) = \bar{p}\left(\frac{\gamma}{\gamma-1}\right)
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\end{align}
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Therefore, if $\bar{p}$ is constant and uniform then $\rho h_s$ is constant and uniform. Consequently, $\partial (\rho h_s)/\partial t = 0$ and $\nabla (\rho h_s) = 0$, so we require no corrections to the divergence expression. This improves the speed of the code since these divergence corrections are rather expensive. To employ this simplification, the user enters \emph{both} {\ct CONSTANT\_SPECIFIC\_HEAT\_RATIO=.TRUE.} and {\ct STRATIFICATION=.FALSE.} on the {\ct MISC} line of the input file.
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Therefore, if $\bar{p}$ is constant and uniform then $\rho h_s$ is constant and uniform. Consequently, $\partial (\rho h_s)/\partial t = 0$ and $\nabla (\rho h_s) = 0$, so we require no corrections to the divergence expression. This improves the speed of the code since these divergence corrections are rather expensive. To employ this simplification, the user enters \emph{both} \ct{CONSTANT\_SPECIFIC\_HEAT\_RATIO=.TRUE.} and \ct{STRATIFICATION=.FALSE.} on the \ct{MISC} line of the input file.
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%\chapter{Multi-environment Extension of Reactor Model}

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