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December 31, 2019 at 10:29 pm
soumitra2102
SubscriberIf there is no heat source but only heat sink in my simulation, in order to achieve condensation only, will ANSYS Fluent use only equation 16.7-40, i.e. when T>Tsat to calculate the mass transfer source term for vapor fraction/continuity equation?
In other words, for condensation only, does the highlighted term in the following mentioned continuity equation 16.5.4 is entirely equal to the term calculated by above mentioned equation 16.7.40? or is equal to the difference between two terms calculated by equations 16.7.40 and 16.7.41?
Thanks
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