In one of my project, propylene is being pumped out of bullet and fed to process units. My Objective is to find the lowest operating pressure inside the propylene bullet.
Bullet volume : 3000 m3
Initial operating pressure of bullet: 21 barg
Min / Max ambient temperature : 4 / 46 C
Pump-out flow rate : 100 m3/h
I can directly calculate saturation pressure of propylene for Min / Max ambient temperature as 5.6 / 18 barg. But when propylene is emptied out of bullet (say from HLL to LLL), liquid propylene is flashed inside bullet to occupy vapor expansion? Due to flashing, temperature inside the bullet is reduced?
How to find out the lowest temperature reached in the bullet at LLL from HLL in the bullet for which I can calculate the propylene saturation pressure?
Note: no propylene vent equalization line & assuming no heat ingress.
Thanks in advance!
Paranthaman