First a little bit of background (and sorry for the long post)
We have a process waste heat boiler. It produces steam above 80 bar pressure. The manufacturer (we contacted them over the phone) do the mechanical designs to ASME VIII and depending on the jurisdiction and customer request they provide relief to ASME I (considering it an unfired boiler) or they stamp to ASME VIII per UG-1-(g)(2)(a and b ) and let the customer take the responsibility for the relief. The last one is our case.
ASME VIII has legal status in our province.
There are multiple valves in the steam drum. The valves calculations show that any of of the valves can be blocked /removed and still have enough relief capacity.
They do not have block valves and on occasions, leaking valves have caused an unplanned shutdown. So, a couple of years back, the Maintenance department, having a budget surplus, decided to buy gate valves (Class 1500) to install under the PSV's . And then asked the Process Engineering group to "do the papers" and also specify the trapped key system to avoid more than one being isolated at a time.
Problem is: the valves are conventional port, not full port. So for some time we, the process engineers, have refused to "do the papers" stating that the ASME code UG135 b 1 states that "the opening of all pipe,fittings....shall have at least the area of the pressure relief valve inlet", in Appendix M calls for "full area stop valves" and the guidance on API 520 part II further clarify that "The opening through all pipe and fittings (including stop valves) between a pressure vessel and its PRV shall have at least the area of the PRV inlet connection"
Up to here is the plain letter of the code.
However, the PSV has a small oriffice for the body size. This is because, being high pressure steam what is vented, the limitation is on the discharge nozzle and / or piping. So, we've got 6X8 valves with an oriffice that would normally fit in 4x6 valves. A 4" inlet connection would ensure less than 3% unrecoverable pressure drop. If a 4x8 PSV were available that would be good solution
So, if I follow the plain letter of the code, I should stick to my guns and recommend that those valves are not used. However, all the calculations show that there should not be any problems with the PSV operation with a conventional port, since a 4" inlet line would be adequate.
Yes... I know... cannot buy anything without specification and then ask others to circumvent the code.
Yes...there are no consequences for me for saying no. I am not under pressure.
I just want to be sure that I am doing the right thing by recommending that those 20kUSD a piece valves are scrapped. And honestly, while I know that the code is written for a reason, and that many problems have arisen from people believing that exceptions were reasonable, it is also clear that the code cannot cover any imaginable case and that I should use my engineering judgment on each specific case. And that is telling me that these conventional port valves should work.
So, what I am asking is your point of view on this.
Thank you very much.
Edited by Saml, 06 April 2017 - 09:42 PM.