nasser358
Mechanical
- Jun 3, 2009
- 2
A company in California holding an R1 certificates will repair an epoxy lined pressure vessel with a 2-inch diameter hole on the shell. Aside from the hole, there are corrosion damage (pittings)around the bottom of the distributor. Question:
1. The hole would be repaired by flush patch and inspected by means DPT on root and final passes in lieu of hydrotest. Is it OK to DPT the patch as long as the AI is informed?
2. The pittings around the bottom of the tank might have gone to some extent that the wall thickness has reduced considerably low. What is the remaining plate wall thickness that should be considered for replacement?
Design pressure: 75 psi
Design Temperature: 150 Deg F
Corrosion Allowance: None
Thanks in advance
1. The hole would be repaired by flush patch and inspected by means DPT on root and final passes in lieu of hydrotest. Is it OK to DPT the patch as long as the AI is informed?
2. The pittings around the bottom of the tank might have gone to some extent that the wall thickness has reduced considerably low. What is the remaining plate wall thickness that should be considered for replacement?
Design pressure: 75 psi
Design Temperature: 150 Deg F
Corrosion Allowance: None
Thanks in advance