Di Felice Drag Model for Spouted/Fluidised Beds
Hi everyone!
I have a question about implementing Di Felice as a UDF drag model (in TFM) in FLUENT.
Would I be giving FLUENT the expression for gas-solid coefficient, K_gs or do I give it the expression for calculating the drag force?
/* compute reynolds no */
re = rho_g*abs_v*diam*vof_g/mu_g;
/* cd and voidage function */
cd = pow(0.63+4.8*sqrt(1/res),2); /* dallavalle */
beta = 4.8-0.65*exp(-0.5*pow(1.5-log10(re),2)); /* which one? */
ge = pow(vof_g,-beta);
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