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Copy file name to clipboardExpand all lines: Manuals/FDS_User_Guide/FDS_User_Guide.tex
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@@ -2282,14 +2282,11 @@ \subsubsection{Logarithmic Law of the Wall}
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\subsubsection{Blowing Heat Transfer}
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\label{info:blowing}
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If a surface is emitting (``blowing'') or removing (``sucking'') gas, the flow normal to the surface disrupts the thermal boundary layer. Blowing tends to decrease the heat transfer coefficient while sucking tends to increase it. Adding \ct{BLOWING=T} to the \ct{SURF} line will account for this effect, except for DNS simulations where empirical heat transfer correlations are not used. When \ct{BLOWING=T}, the heat transfer coefficient is adjusted as follows~\cite{Plate_blowing}:
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If a surface is emitting (``blowing'') or removing (``sucking'') gas, the flow normal to the surface disrupts the thermal boundary layer. Blowing tends to decrease the heat transfer coefficient while sucking tends to increase it. Adding \ct{BLOWING=T} to the \ct{SURF} line will account for this effect, except for DNS simulations where empirical heat transfer correlations are not used. When \ct{BLOWING=T}, the heat transfer coefficient is adjusted as follows~\cite{Plate_blowing,Taylor&Krishna}:
h_{\rm blowing} = \underbrace{\left[\frac{\Phi_h}{{\exp}(\Phi_h)-1}\right]}_{{\mbox{\scriptsize \tt BLOWING CORRECTION}}} h
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\end{equation}
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where $h$ is the unadjusted heat transfer coefficient, $\dot{m}''$ is the mass flow rate per unit area (positive for blowing), and $c_p$ is the specific heat of the gas.
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where $h$ is the unadjusted heat transfer coefficient, $\dot{m}''$ is the mass flow rate per unit area (positive for blowing), and $c_p$ is the specific heat of the gas.,
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