fdomin
Chemical
- Jan 10, 2002
- 49
I have to protect the tubeside of a heat exchanger for tubeside thermal expansion scenario. Tubeside fluid is crude at 400ºF and shellside fluid is atm. tower bottoms at 590ºF.
PSV set pressure is 425 psig and at that pressure saturation temperature is 565ºF.
Do I need to calculate the PSV to handle vapor-liquid mixture? The valve will open before the crude reaches ATB temperature but if trapped crude heating continues will it vaporize and a liquid service PSV would be insufficient?
PSV set pressure is 425 psig and at that pressure saturation temperature is 565ºF.
Do I need to calculate the PSV to handle vapor-liquid mixture? The valve will open before the crude reaches ATB temperature but if trapped crude heating continues will it vaporize and a liquid service PSV would be insufficient?