|
[Sponsors] |
Smearing of Mass Transfer(condensation)using UDS over interface. |
|
LinkBack | Thread Tools | Search this Thread | Display Modes |
May 23, 2016, 12:19 |
Smearing of Mass Transfer(condensation)using UDS over interface.
|
#1 |
Member
Rajukiran Antham
Join Date: Dec 2012
Location: Sweden
Posts: 41
Rep Power: 13 |
Hej,
I am working on phase change problem (condensation). I wrote UDF's for calculation of source terms. I want to smear mass transfer near the interface using a Diffusion equation and then pass the smeared values as source terms to the equations. I am solving the diffusion equation using UDS and passing mass transfer as source term to UDS. Below is the diffusion equation which I am solving, D*del2(phi)= S here, D is diffusion coefficient, phi is scalar variable and S is source term, I am passing source term using Define_source UDF, DEFINE_SOURCE(UDS_src,c,t,dS,eqn) /*smearing source udf*/ { real UDS_source; UDS_source = 0.0; UDS_source = C_UDMI(c,t,1)-C_UDSI_M1(c,t,0) ; dS[eqn] = 0.0; return (UDS_source); } In the above UDF C_UDMI(c,t,1) is the mass transfer term which is calculated in a different UDF. Diffusion coefficient D is passed using below UDF. #include "udf.h" DEFINE_DIFFUSIVITY(mean_age_diff,c,t,i) { return 0.0000001; } What I was expecting was a smeared mass transfer over few cells close to the interface , since mass transfer is calculated only at the interface. but I am not getting the expected result. I am not sure where I am going wrong. I would really appreciate if someone can point out where I am going wrong. regards, Rajukiran. PS: I am also attaching pic of scalar value of phi and interface where source terms are added. |
|
May 24, 2016, 09:19 |
|
#2 |
Member
Rajukiran Antham
Join Date: Dec 2012
Location: Sweden
Posts: 41
Rep Power: 13 |
Hej,
I tried a simple case, where I tried solving a steady diffusion equation using UDS. I switched off inlet Diffusion, Flux and unsteady function in the UDS. I used Neumann boundary conditions over the domain. I gave a constant source term through UDF only at the interface. I was expecting that the given source term to smear over the interface. But I got something similar to previous case. I would really appreciate if someone can answer this. Thanks in advance Regards, Rajkiran |
|
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
DPMFoam - Serious Error --particle-laden flow in simple geometric config | benz25 | OpenFOAM Running, Solving & CFD | 27 | December 19, 2017 21:47 |
Difficulty in calculating angular velocity of Savonius turbine simulation | alfaruk | CFX | 14 | March 17, 2017 07:08 |
Modeling the fan with a mass flow interface | saisanthoshm88 | CFX | 6 | August 1, 2014 07:11 |
Modelling valves/orifices using interface models | DarrenC | CFX | 5 | June 3, 2014 07:14 |
why my momentum and mass not convergence | wwwuxing | CFX | 3 | May 18, 2012 08:49 |