Be careful to select the right material in the Settings window for External Film Resistance. Many times this should be another material than the Domain material which is the internal fluid.
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The natural convection correlations (see External Film Resistance under The Heat Transfer Equation in the section Theory for the Heat Transfer in Pipes Interface) require a temperature dependent density, or else the coefficient of thermal expansion β evaluates to 0 (Equation 3-26), which might generate unexpected results or even unstable models. Also, make sure that the density correlation ρ(T) is smooth throughout the temperature interval used, or else β is discontinuous and can cause numerical instability.
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Enter the Nusselt number (dimensionless). The default is 3.66.
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The Thermal conductivity k (SI unit: W/(m·K)) takes its value From material. For User defined enter a different value or expression. The default is 0 W/(m·K).
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