david6245
Chemical
- Sep 10, 2009
- 28
Hello,
I have a PSV set at vessel MAWP of 20 psig. API recommends the inlet pipe to the PSV not have a pressure loss greater than 3% of set pressure at valve capacity. However, this is only 0.6 psi. ASME allows an overpressure of 10% for vessels with MAWP greater than or equal to 30 psig and 3 psig over pressure for vessels with MAWP less than 30 psig.
If my total overpressure at the vessel at PSV capacity is less than 3 psig, can my inlet pressure drop exceed 3% or 0.6 psi?
My pressure profile would look like the following for example:
vessel P ->PSV inlet->PSV outlet -> Atmosphere
23 psig ->22 psig ->2 psig -> 0 psig
Acceptable?
I have a PSV set at vessel MAWP of 20 psig. API recommends the inlet pipe to the PSV not have a pressure loss greater than 3% of set pressure at valve capacity. However, this is only 0.6 psi. ASME allows an overpressure of 10% for vessels with MAWP greater than or equal to 30 psig and 3 psig over pressure for vessels with MAWP less than 30 psig.
If my total overpressure at the vessel at PSV capacity is less than 3 psig, can my inlet pressure drop exceed 3% or 0.6 psi?
My pressure profile would look like the following for example:
vessel P ->PSV inlet->PSV outlet -> Atmosphere
23 psig ->22 psig ->2 psig -> 0 psig
Acceptable?