Hello good people,
Would any one be kind enough to advise me on the relevant literature to consult when setting up steam mains in a Process System.
I am in a team saddled with "cogeneration of power and heat". Power, by expanding steam at different pressure levels, VHP, HP, MP & LP levels...
IFRs,
Would it be right then to accept a deisgn that has different thickness for the bottom and annular plate?
For example, are these values tenable?
Bottom plate (plus corrosion allowance)- 6mm + 4mm
Annular plate - 20mm
Regards
Would anyone assist in calculating the bottom (not annular) plate thickness of a 50 cubic metre crude oil storage tank, with regards to API 650.
The copy I have does not seem to address it.
Regards