2 replies to this topic

[mrbabu]

with Prode Properties which thermodynamic models should I select for vapor and liquid fugacities when modeling a separation with natural gas, water, TEG ? 

I would prefer models with BIPS already in Prode database.

 

[marchem]

according my experience for fugacity and volume CPA-PR gives good results,

for solving enthalpy (columns) you may select the Extended Peng Robinson

[mrbabu]

thanks,

comparing results from CPA model with literature agreement seems good.