jamesbanda
Chemical
- Sep 21, 2004
- 223
I'd like some perspective on setting of design p's for tall columns which are linked..as i approach a re-engineering exercise on a proces design..
col 1: RV P 100 Psig top
Col 1 bottom Design P = Pressure from (Tray liquid loading at flood) + Pmax liquid level in sump + P margin.
Col 2,
Ptop = vapour loss to P1+ Relief P atP1
Option 1: P base = P sump col2 + P liquid col 2+ P liquid col 1(assumping all liquid is transferred) + margin
or
Option 2: P base = P sump col 2+ pliquid col 2 + P back pressure through col 1 to relief + margin.
i think option 2 is viable becuase it is reasonable to assume in a fire pumps will be stopped due to burning of fire safe valves..
i've been told we dont allow for Pbase = PRV at top + col full of liquid becuase we hydrotest in verticle and all our relief cases are only fire.. no other crediable case..
But i'd like to see what is convention for other firms with tall columns..
col 1: RV P 100 Psig top
Col 1 bottom Design P = Pressure from (Tray liquid loading at flood) + Pmax liquid level in sump + P margin.
Col 2,
Ptop = vapour loss to P1+ Relief P atP1
Option 1: P base = P sump col2 + P liquid col 2+ P liquid col 1(assumping all liquid is transferred) + margin
or
Option 2: P base = P sump col 2+ pliquid col 2 + P back pressure through col 1 to relief + margin.
i think option 2 is viable becuase it is reasonable to assume in a fire pumps will be stopped due to burning of fire safe valves..
i've been told we dont allow for Pbase = PRV at top + col full of liquid becuase we hydrotest in verticle and all our relief cases are only fire.. no other crediable case..
But i'd like to see what is convention for other firms with tall columns..