2 replies to this topic

[Mahmoud84]

I have a case where there is a quantity of natural gas of 50 MMSCFD having the following composition :
N2 0.0988
CO2 0.65
C1 91.2626
C2 6.3481
C3 1.375
IC4 0.1703
NC4 0.0835
NEO C5 0.0005
IC5 0.0068
NC5 0.0022
C6+ 0.0024
Preesure is 55 barg and temperature is -10°C upstream the turbo expander
The question is what is the roughly estimated quantity of LPG and condesate that can be extracted from this mixture?
Taking into consideration that pressure downstream the turbo expander is 25 barg and temperature is -42°C.

[FRBChemE]

I have run you question through the DWSIM process simulator.  I find that there is no liquid at the conditions of 25 barg & -42°C.  I am attaching the print out etc.

[breizh]

Hi,

Consider the result from canary software to support your work .

100% gas @ 2600 Kpa Absolute  & -33.15 C 

 

Hope this is helping you.

 

Breizh

Edited by breizh, 07 March 2021 - 01:44 AM.