carol2005
Chemical
- May 24, 2005
- 21
Some PSV sizing programs provide a feature to calculate PSV inlet and outlet piping pressure loss by using the process required relief rate instead of PSV actual relief capacity. I know ASME VIII Div I appendix M gives recommendation of 3% and 10% limitation for compressible fluid inlet/outlet piping pressure loss with conventional PSV. But I couldn't find clear guidiline about imcompressible fluid. Can I assume:
For compressible fluid, i.e. vapor or gas or two-phase relief, actual PSV capacity should be applied for piping delta P calculation.
For imcompressible fluid, i.e. pure liquid relief without flashing at tailpipe, the process required relief rate can be used for piping calculation, provide the PSV is ASME compliant, UV stamped, liquid trim PSV. By saying this, I assume the PSV will open proportional to process relief rate.
Please advise me if this is not correct.
For compressible fluid, i.e. vapor or gas or two-phase relief, actual PSV capacity should be applied for piping delta P calculation.
For imcompressible fluid, i.e. pure liquid relief without flashing at tailpipe, the process required relief rate can be used for piping calculation, provide the PSV is ASME compliant, UV stamped, liquid trim PSV. By saying this, I assume the PSV will open proportional to process relief rate.
Please advise me if this is not correct.