hello ahyong
sad to hear yet another young engineer has been set a task with insufficient guidance from senior engineers on what to do .
Lets see if I can assist you
1) you must model the blocked outlet ( BO) in AFSA , you cannot take account of the BDV being opened by the operator. What if he fell over on the way to open the BDV ? the PSV must provide protection to the vessel.
Model the PSV to flare with the load set at the BO required rate, at the set pressure of the PSV of course and not 92%
2)_ the PCV will normally control the pressure in the tank by venting gas to flare . If it fails open then you will have a flow of gas to flare, amount will be determined by the capacity of the PCV based on the pressure in the tank.
If the PCV failed closed or became stuck in the closed position then the PRV , i assume this is a PSV, would open if the pressure rose above the tank design P and vent to flare.
3) you cannot model anything in AFSA without the pipe lengths and diameters , you are wasting your time here. The FEED Co must have this information as you say you are to verify their calculations. do you not have any information at all ? if No then you must get some otherwise you cannot do anything.
I am also surprised that you have warm wet and cold dry reliefs going into the same KO drum, you could have major problems with liquid knoc out, hydrates or thermal shock mixing these.
4) they most likely did a different AFSA model for this , if at all .
5) AFSA will work in MW only but if you have a HMB then you should get the detailed composition.
having read through your problems here i cannot believe that you have been asked to verify the FEED co workings without being given their AFSA model or sufficient other data. You do not have enough information to do anything ahyong. I could not do this for you given what you have been told , and i have 30 yrs experience in this field ..
go back to your boss and say you need more information or better still the AFSA model .
flarenuf