Hi all,
With a colleague I'm having a discussion on how to interpretarte the API 520 Part II recommendation of not having more than 3% pressure loss at the inlet piping to the PSV. I'm already aware of the following: “The calculation should contain only NON-RECOVERABLE losses. For gases, you DO...
Hi everybody,
I've been doing some searching in various threads of the forum, but I still remain with some doubts on this topic: I've seen various plants that use the typical NPT stainless steel ball valves in Carbon Steel piping, for example for vents and drains on cooling water piping...