I did recombine the condensate and the dry gas to find out the recombination of fluid at reservoir condition. However, my phase envelope did not show the critical point. Is that a resonable result? And if the fluid has not a critical point, could you guys explain for me?
I just learn to study Pipeline simulation. Could you explain the terms "Slugvoid" & "Bubblevoid" ? and give me some addresses in the Internet about these ?
I have a case folowing:
A field with reserves are 65 Bcf, Developping facilities are include: 01 monotower, 01 gas producer with peak flowrate is 30 MMscfd, produced gas wil be transported to another platform for processing by a 10"x10.5 km sub-sea pipeline. We have to set up a gas metering...
