ReliaEng2008
Mechanical
- Mar 5, 2021
- 22
Hello there. This question is regarding the inclusion of an equipment to an inspection program per OSHA's PSM/Mechanical Integrity (29 CFR paragraph 1019.119(j)), considering the applicable RAGAGEP Codes and Standards.
I have an 2.5 gallon (volume less than 1 cubic feet) hydraulic oil accumulator that is part of the hydraulic system of a rotating equipment. It is ASME design and has a U1 form. The MAWP is 2000 psi. Material of construction is 316L SS.
As you can imagine, this pressure vessel is not a concern (assuming the rotating equipment is maintained properly). There is basically no expected damage mechanisms.
I would like to exempt this equipment from inspection requirements of API 510. I am reading the exemption section of the Standard and I cannot find any options to exempt this equipment. Even though it is part of a rotating equipment skid, I don't consider it an integral part of a rotating equipment (for example, a built-in heat exchanger inside a compressor would be an integral part of the rotating equipment). Even though the volume is less then 1.5 cuft, since the design pressure is more than 600 psi, it looks like I will have to include this equipment in my inspection program, although I don't expect inspections to be of much value.
Any thoughts?
I have an 2.5 gallon (volume less than 1 cubic feet) hydraulic oil accumulator that is part of the hydraulic system of a rotating equipment. It is ASME design and has a U1 form. The MAWP is 2000 psi. Material of construction is 316L SS.
As you can imagine, this pressure vessel is not a concern (assuming the rotating equipment is maintained properly). There is basically no expected damage mechanisms.
I would like to exempt this equipment from inspection requirements of API 510. I am reading the exemption section of the Standard and I cannot find any options to exempt this equipment. Even though it is part of a rotating equipment skid, I don't consider it an integral part of a rotating equipment (for example, a built-in heat exchanger inside a compressor would be an integral part of the rotating equipment). Even though the volume is less then 1.5 cuft, since the design pressure is more than 600 psi, it looks like I will have to include this equipment in my inspection program, although I don't expect inspections to be of much value.
Any thoughts?