CWIMET
Materials
- May 18, 2012
- 1
Does anyone have any experience or preference on the number of PWHT cycles that may be performed on Grade 91? We have a CC HRSG that has had multiple repairs (multiple PWHT's) performed on a P91 stop valve (repair of Small Bore by-pass line, replacement of same, removal and plugging of by-pass with manufacturer's blessing, and lastly repair of a cracked valve seat). I'm feeling the cracked valve seat is indicating we should be looking into replacement at this point.
I understand that chemistry, stress, PWHT temp and process are all significant factors when dealing with P91, but assuming everything has been done properly to this point and hardness ranges are still acceptable, is there an industry standard or general consensus that would limit the time at PWHT temperature? Is there any NDE method recommended or would a boat sample sent out give me any further insight? My refinery experience has me stuck on three repairs and replace, and we've gone that far already.
I can find no references in Code or technical literature and could not find anything in the forum. As a first time user, not sure if this thread would be better located here or somewhere else? Thanks for any assistance that may be provided.
I understand that chemistry, stress, PWHT temp and process are all significant factors when dealing with P91, but assuming everything has been done properly to this point and hardness ranges are still acceptable, is there an industry standard or general consensus that would limit the time at PWHT temperature? Is there any NDE method recommended or would a boat sample sent out give me any further insight? My refinery experience has me stuck on three repairs and replace, and we've gone that far already.
I can find no references in Code or technical literature and could not find anything in the forum. As a first time user, not sure if this thread would be better located here or somewhere else? Thanks for any assistance that may be provided.