KernOily
Petroleum
- Jan 29, 2002
- 711
Hi guys. S&T exchanger, type BEM, in shop to repair the flange face on the shell flange (shell-to-tubesheet) for corrosion damage.
Shell: SA106B shell 24" sch 100 pipe x 324" long, 1.531" wall
Shell flange: SA105 shell flange 24" class 900.
The flange face is being repaired by weld overlay of CRA then machining back to spec. The WPS position of the weld repair to the flange face is flat, which means they will cut the flange off the shell, do the repair, then weld the flange back on to the shell.
Do I need to be concerned about the PWHT of the shell-to-flange weld pulling the flange face out of plumb? That would be Very Bad if it happened. I've seen vessel shell nozzles get pulled out of plumb, but those weren't as critical as this. The tubesheet gasket won't seat if that happens.
Thanks guys. Pete
Shell: SA106B shell 24" sch 100 pipe x 324" long, 1.531" wall
Shell flange: SA105 shell flange 24" class 900.
The flange face is being repaired by weld overlay of CRA then machining back to spec. The WPS position of the weld repair to the flange face is flat, which means they will cut the flange off the shell, do the repair, then weld the flange back on to the shell.
Do I need to be concerned about the PWHT of the shell-to-flange weld pulling the flange face out of plumb? That would be Very Bad if it happened. I've seen vessel shell nozzles get pulled out of plumb, but those weren't as critical as this. The tubesheet gasket won't seat if that happens.
Thanks guys. Pete