|December 14, 2011, 09:18||
UDF for VR Rate calculation
I am fairly new to using UDF along with Fluent. I am trying to model reduction of CO2 with coal or Carbon. The reation rate is defined using Langmuir-Henselwood formulation and I am trying to do that with the UDF because most of the Species Transport models use the Arrhenius rate equation.
My question is, how do I use concentrations of the species' as my variable in the code.
Here is the code I have so far (fairly simple and premature):
#define K 1000
#define K2 0.508
#define Mtot 84.
DEFINE_VR_RATE(lang_hens_reac_rate,c,t,r,mole_weig ht,species_mf,rate,rr_t, yi)
real s1 = species_mf;
real s2 = specief_mf;
real mw1 = mole_weight;
real mw2 = mole_weight;
if (FLUID_THREAD_P(t) && THREAD_VAR(t).fluid.porous)
*rate = K2*mw1/(1+K*(mw1+mw2));
*rate = 0.;
*rr_t = *rate;
However, all the mw variables need to be concentrations. Please help me as soon as possible as I am running out of ideas and options
I found this piece of code that people are using to obtain concentration:
ci = yi[dindex][sp_id]*C_R(c,t_reactant)/mw[dindex][sp_id];
ci = MAX(ci,SMALL_S);
But i have no idea what all those arguements and variables and syntax are. Please help
The basic equation for calculating the reaction rate is:
rate = K2*[species 2]/(1+K*([species1]+[species2]))
where K and K2 are constants given and the objects in the square brackets are obviously concentrations that I need.
Last edited by ADI; December 14, 2011 at 09:47. Reason: More info found after further research.
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