Hello
I am looking at start up of a new facility where the available medium to warm a reactor and its catalyst is H2. I know that H2 is not typically used as a heat carrier but in this hydro treating service it is available without needing extra facilities. The problem is the flow is small and...
Hi
In rating an installed SV for increased throughput the installed ASME area has been quoted by the vendor as 361mm (G). The standard API equivalent is 325mm.
I have calculated an area based on API methodology and assumed K for the valve. I get 350mm.
The question is: should I conclude...