mlazard
Petroleum
- Feb 9, 2013
- 9
I have water solubility measurements in vapor for methane-water, ethane-water, propane-water etc. for each measurement I know
Temperature Pressure Water content in vapor phase (Y)
282 K 10 Bar.a 0.0012
I wish to calculate the BIPs for different models (such as Peng Robinson, Soave Redlick Kowng etc.) and compare results (vapor-liquid equilibria),
my free copy of Prode Properties includes the procedure however I do not know how to enter X1 and Y1 (as I know only Y1),
is that possible with the free copy of Prode ?
Temperature Pressure Water content in vapor phase (Y)
282 K 10 Bar.a 0.0012
I wish to calculate the BIPs for different models (such as Peng Robinson, Soave Redlick Kowng etc.) and compare results (vapor-liquid equilibria),
my free copy of Prode Properties includes the procedure however I do not know how to enter X1 and Y1 (as I know only Y1),
is that possible with the free copy of Prode ?