Hello,
I’m reviewing a calculation sheet for a liquid ammonia storage tank designed to API 620 App "R". One of the scenarios listed is heat gain from pump (8,256 kg/hr), which turns out to be the largest and governing case for PSV sizing (picture attached below).
My question is: what could be the cause of such a high relief requirement from pump heat gain? According to API 2000, the common scenarios are normal/thermal outbreathing, fire exposure, and some specific cases related to refrigerant tanks (Section 4).
Has anyone encountered a similar situation, or can explain why pump heat input would dominate the PSV sizing?