I want to fit the NRTL activity model to match some plant data that I have been given (i.e. I want to do a regression). The data that I have is from 3 different plants whose operating conditions are at different temperatures and pressures. Oh, and there are 31 components in the system (which means there are lots of different binary interactions that could occur ;-) ). This is for a 3-phase system (ie VLL) at the cold separator of a refrigeration plant using Ethylene Glycol as a hydrate inhibitor. So hydrocarbon vapor off the top, HC Liquid phase and a EG-Water phase. I will be using the Peng-Robinson EOS to model the vapor phase. I have done a regression for a 2-component system during my undergrad studies however, this seems quite different as I have no VLLE data and the 3 plants are at different conditons.
Thanks very much in advance!
P.S. I am sure there will be questions, and if I am not making, sense I apologize. I am new at this....
Edited by KeJoSa2010, 24 September 2012 - 09:49 AM.