inammanj123
Mechanical
- Oct 11, 2013
- 103
Hi,
I have a BEU type exchanger on old asme sec div.1 edition. job is to upgrade exchanger by replace channel bonnet to new 1.25Cr material. This is done because service is hydrogen temperature is high, so chance of HTHA is there. Shell side, tubesheet and tube will remain same. Client is ARAMCO. In this regard i have following question:
1- keeping in view that process conditions will be same, calculations need to be performed as per latest asme edition, so to make sure girth flange dimensions, nozzle project mates with existing dimensions, will it be alteration job or repairing job and will channel have r-stamp or simply U-part?
2- If client ask to check tubesheet and tube in accordance with latest TEMA AND API 660, what are few major condition i need to look for to propose a change in tube sheet.
3- For new channel design, I think i will limit MAWP and hydro-test pressure?
Thx
I have a BEU type exchanger on old asme sec div.1 edition. job is to upgrade exchanger by replace channel bonnet to new 1.25Cr material. This is done because service is hydrogen temperature is high, so chance of HTHA is there. Shell side, tubesheet and tube will remain same. Client is ARAMCO. In this regard i have following question:
1- keeping in view that process conditions will be same, calculations need to be performed as per latest asme edition, so to make sure girth flange dimensions, nozzle project mates with existing dimensions, will it be alteration job or repairing job and will channel have r-stamp or simply U-part?
2- If client ask to check tubesheet and tube in accordance with latest TEMA AND API 660, what are few major condition i need to look for to propose a change in tube sheet.
3- For new channel design, I think i will limit MAWP and hydro-test pressure?
Thx