Recent content by hniaboujemaa

Thanks guys for your valuable information.

Hi guys, Given that the pipe has been tested @ 1.5xDP, what will be the impact on operating this pipe above the Design pressure.. Thanks

Thanks don1980 for your valuable information. In my case, I'm having a bloiler feed water vessel with a desaerator in the head. The vessel is 9' ID with a normal water level in 6'-9''. Thanks

Hi, what is the dirrefence of using wetted vs unwetted area calculation approch while calculating the required RV capacity for a vessel ? Thanks

Hi, What is the difference between the MAWP and DP (Design Pressure)? Thanks

Thanks don1980 for your valuable info

What is the definition of ASME capacity for a given PSV ? Thanks

Hello, "" Where liquid certified valves are specified, the sizing method for certified relief valves (refer to API Std 520 Part I) should be used. This ensures a more accurate size determination, avoids oversizing and thereby minimises the probability of chatter. If chatter is a problem, the...

I'm currently working in this issues with our current client. In my previous at the refinery, we didn't have such isolation valves and to be honnest as per my experience, these valves are important basicaly for PSV maintenance. In the past I have seen making unit shutdown for a PSV leaking or...

Interesting, moltenmetal ! Thanks for sharing this

Thanks guys for your feedbacks. Mouss

Any though ? Regards.

Thanks CJKruger for your clarif the design and actual are quite clear but the rated one is still not. regards,

Hi guys, Any thoughs about the difference between rated / actual / design rate for PSV, I have seen many definitions through API and ASME. Thanks in advance :-) Mouss

Thanks guys for your feedback, @sheiko : Here some clarif to the following: 1/ Your are dealing with existing PSV but you want the method to size them. Yes Sir, the question is to review & validate the existing one ! 2/ Later you talk about specifying the PSV while before you wanted to size...