[Nazanin]

Hi Formers
I have managed to implement the interPhaseChangeFoam solver according to the project done by Martin Andersen,So i have a solver that Psat depend temprature.now,I want use this solver for my case,But I dont know how modified empirical coefficients in mass transfer models.foe example if I choose Kunz model ,How determine t or Cprod or Cdest ?
If in my case,dont have velocity (all of the case U=0)? whats happen?
It means,I have a case with water and vapor and I want evaporate water with Temprature (Psat depend temp)...
regards,
Nazanin

[mecman]

Hi Nazanin
for stimulation evaporate with temp,I think you should use another mass transfer model and modified the source term
you can read this page
http://www.cfd-online.com/Forums/blo...-openfoam.html

or if you use this solver I think you should variable diffusion coefficient [DT ] based on the volume fraction of both phases.I did this work,but I have problem too. you tell good point...can we use interPhasechangeFoam solver base this phasechange model without U. as I know ,this solver for cavitation and Cavitation without U....?
you can see my thread in this page:
http://www.cfd-online.com/Forums/ope...base-temp.html