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Multiphase flow and Phase change due to heat transferevaporation |
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May 29, 2010, 21:34 |
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#81 |
Senior Member
Sandy Lee
Join Date: Mar 2009
Posts: 213
Rep Power: 18 |
Hi, why you not to try to combine compressibleInterFoam solver and some heatTransfer solver? I will try it too.
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June 9, 2010, 10:54 |
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#82 |
Member
Join Date: Apr 2010
Posts: 51
Rep Power: 16 |
hi at all!
at the moment i am doing some simulations of a flow through a piston valve. right now i achieved some good results with the simpleFoam solver including k-w-SST model for low velocities or volume rate respectively. but when the effect of cavitation sets in, my results donīt follow the measured ones. therefore I try to set up a simulation with a multi-phase-solver. I decided to use rasCavitatingFoam but I achieved just unphysical results. After I read that some more people have problems with this solver and a friedly guy showed me a comparison of solvers ( http://web.student.chalmers.se/group...PosterOFW5.pdf ) I thought I rather use interPhaseChangeFoam. Would you say this is a good decision? (1) Unfortunately I wasnīt able to set up a case now because I always get errors. I downloaded the dambreak case calculated with interPhaseChangeFoam but I am not exactly sure what I need to change besides BCs and values of nu and rho. Is there somethin else? (2) at the inlet i define my velocity with fixedValue (0 0 -1.04), outlet has fixedValue with 476.2. I heard that it would be good to use solutions from a converged calculation as starting values for the more complicated. But how can I do that? (3) After simpleFoam my resulting pressures are given in m^2/s^2 because of the density. interPhaseChangeFoam is compressilble and the pressure unit is Pa. best wishes! |
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September 24, 2010, 15:02 |
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#83 |
Senior Member
Nima Samkhaniani
Join Date: Sep 2009
Location: Tehran, Iran
Posts: 1,267
Blog Entries: 1
Rep Power: 25 |
hi buddies
could you please correct me if im wrong first in phaseChangeTwoPhaseMixture::vDotAlphal() there is following expression volScalarField alphalCoeff = 1.0/rho1() - alpha1_*(1.0/rho1() - 1.0/rho2()); but the source term in gamma equation is mdot/rhoLiquid , so how the above code can be right ? second : why the following expression has been added in pEqn.H : - (vDotvP - vDotcP)*pSat + fvm::Sp(vDotvP - vDotcP, p) |
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February 24, 2012, 03:31 |
mDotAlphal() and mDotP() In interphasechange
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#84 |
Member
vahid
Join Date: Feb 2012
Location: Mashhad-Iran
Posts: 80
Rep Power: 13 |
Hello OpenFoam users ,
I'mstudying on the Kunz model.we know in this model we have two term for mass dest and prod.(m+ and m-) What mean mDotAlphal() and mDotP()In interphasechange? What is the difference between these two?? |
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April 8, 2013, 08:19 |
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#85 |
Member
ABE
Join Date: Jul 2012
Posts: 46
Rep Power: 14 |
Hi,
I am using InterPhaseChange solver to simulate cavitation in OF2.1x Although by old versions (i.e. OF1.5) I can get good results, with this new version results are not good at all. Dose anybody else get similar conflicts? ABE |
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April 8, 2013, 08:21 |
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#86 |
Member
ABE
Join Date: Jul 2012
Posts: 46
Rep Power: 14 |
Hi,
I am using InterPhaseChange solver to simulate cavitation in OF2.1x Although by old versions (i.e. OF1.5) I can get good results, with this new version results are not good at all. Dose anybody else get similar conflicts? ABE |
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April 9, 2013, 03:49 |
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#87 |
Member
ABE
Join Date: Jul 2012
Posts: 46
Rep Power: 14 |
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July 30, 2017, 10:02 |
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#88 | |
New Member
Alice
Join Date: Jun 2017
Posts: 26
Rep Power: 9 |
Quote:
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February 11, 2020, 09:00 |
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#89 |
New Member
Navid
Join Date: Nov 2015
Posts: 20
Rep Power: 11 |
can someone please answer this question?
I am also wondering about the vDot terms in phasechange solvers of OF. where do they come from? I have found the analytical explanation for gas/liquid interface. but does should it also be considered for melting/solidification? |
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