
[Sponsors] 
January 31, 2018, 13:12 
Adding Source Terms to K epsilon equation

#1 
New Member
ashi
Join Date: Jan 2017
Posts: 6
Rep Power: 8 
hello,
I am having some troubles in using UDF to add a source term to k equation in turbulent model. here is my udf which is for a multiphase flow. It is a bubble column filled with water with a simple inlet of air at the bottom. #include "udf.h" DEFINE_SOURCE(k_BIT, cell, pri_th, dS, eqn) { Thread *mix_th, *sec_th; mix_th = THREAD_SUPER_THREAD(pri_th); sec_th = THREAD_SUB_THREAD (mix_th, 1); real diam; real CD, Re, abs_v; real x_vel_a, x_vel_w, y_vel_a, y_vel_w, slip_x, slip_y,slip_z, z_vel_a, z_vel_w, rho_a, rho_w, mu_w, sigma, betastar, Liquidtef, K1, K; real void_a, Eo, uC, SrcK; x_vel_w = C_U(cell, pri_th); y_vel_w = C_V(cell, pri_th); z_vel_w = C_W(cell, pri_th); x_vel_a = C_U(cell, sec_th); y_vel_a = C_V(cell, sec_th); z_vel_a = C_W(cell, sec_th); void_a = C_VOF(cell, sec_th); slip_x = x_vel_a  x_vel_w; slip_y = y_vel_a  y_vel_w; slip_z = z_vel_a  z_vel_w; sigma=0.072; /*surface tension*/ rho_w = 997; rho_a = 1.185; mu_w = 0.00089; diam = 0.003; abs_v = MAX(sqrt(slip_x*slip_x + slip_y*slip_y+slip_z*slip_z),0.00000001); Re=rho_w*abs_v*diam/mu_w; Eo = 9.81*(rho_wrho_a)*diam*diam/sigma; CD = 1; uC = MIN(0.184*pow(Re,0.229),1); SrcK = uC*0.75*(CD/diam)*void_a*rho_w*pow(abs_v,3); dS[eqn] = 0 return SrcK; } I will have a divergence after few iteration at first time step. I could not solve the problem so far. That would be great if you could guide me through this. Many thanks in advance Ashkan 

February 1, 2018, 02:51 

#2 
Senior Member
Join Date: Nov 2013
Posts: 1,965
Rep Power: 25 
If you are getting divergence with the UDF, and no problems without the UDF (you tested this, right?), then it must be that your UDF is returning problematic values.
Test this by printing the values. So directly above your return statement, set Code:
Message("SrcK = %f\n",SrcK); If the values are unexpectedly high or low (as in a factor 1000 too high or too low, not just 10%), print intermediate values to see where the problem comes from. If the returned value is correct, I can't help you. 

February 1, 2018, 06:25 

#3 
New Member
ashi
Join Date: Jan 2017
Posts: 6
Rep Power: 8 
Hello pakk
Thanks a lot for the reply. Exactly ... I get a huge number. I have tried the same expression in CFX and I got results without problem. I tried to compute the values even manually ... logically it should not get that high. Do you think I have defined thread variables wrong? My case is a multiphase case and I add these source in cell zone condition tap and to the liquid phase. is the source term that I have defined applicable to multiphase case? I have been using this type of UDF for single phase without problems so far but for mutiphase I am not sure if I am missing some thing. I appreciate it if you could guide me a little bit more. Thanks 

February 1, 2018, 06:48 

#4 
New Member
ashi
Join Date: Jan 2017
Posts: 6
Rep Power: 8 
I checked again and the issue is with the velocity of the water phase. they are getting too large all of a sudden.


Tags 
multiphase flow, source terms, turbulence kinetic energy, udf code 
Thread Tools  Search this Thread 
Display Modes  


Similar Threads  
Thread  Thread Starter  Forum  Replies  Last Post 
[Other] How to use finite area method in official OpenFOAM 2.2.0?  Detian Liu  OpenFOAM Meshing & Mesh Conversion  4  November 3, 2015 03:04 
[swak4Foam] Error bulding swak4Foam  sfigato  OpenFOAM Community Contributions  18  August 22, 2013 12:41 
[swak4Foam] build problem swak4Foam OF 2.2.0  mcathela  OpenFOAM Community Contributions  14  April 23, 2013 13:59 
Adding source terms to turbulent models  makaveli_lcf  OpenFOAM Running, Solving & CFD  0  June 8, 2009 09:34 
OpenFOAM on MinGW crosscompiler hosted on Linux  allenzhao  OpenFOAM Installation  127  January 30, 2009 19:08 