MrSpike
Chemical
- May 13, 2007
- 7
I'm on a petrochemical project which happens to produce steam as part of the process as well. This steam will be even sold to battery limit but is still not the main application of the plant. There is a steam drum and superheaters in the plant and is point of argument whether should be designed as ASME I or ASME VIII; consequently the piping would get split partially in B31.1 and B31.3 if ASME I was selected.
Does this have to be considered as ASME I while is part of the typical B31.3 plant and therefore we should split them for before and after first shut-off valve for B31.1 and B31.3 spec break, stress analysis, etc.?
(By the way client has no obligation for either way)
I myself think that the criteria of B31.3 dominates this case and we should go for ASME VIII.
Any thoughts?
Does this have to be considered as ASME I while is part of the typical B31.3 plant and therefore we should split them for before and after first shut-off valve for B31.1 and B31.3 spec break, stress analysis, etc.?
(By the way client has no obligation for either way)
I myself think that the criteria of B31.3 dominates this case and we should go for ASME VIII.
Any thoughts?