Angsi
Mechanical
- Feb 17, 2003
- 83
Equipment: TEMA S&T Heat Exchanger, BEU type.
Design: ASME Div 1/TEMA
Service: Crude Oil Cooler
Location: Offshore Platform
Tubeside, 316L, Shell side CS (Cooling water)
=============================================
We plan to rerate an existing S&T Hex which has already been operating for a period of close to 3 years. The idea is to increase the design temperature of the exchanger from 115 deg to 145 deg C.
Steps:
=====
1. Take measurement to acertain remaning thickness (UT, etc).
2. Review calc to determine if the increase in temperature can be accomodated by the present design
3. If required and depending upon the magnitude of this mod, removal of it to the fab shop might be necessary. Then the complete mods, design calcs and rehydrotest will be required I guess.
4. If the current mech design can accomodate the change, the design calcs needs to certification and the nameplate rating has to be cahnged and the equipment rehydrotested again.
The question is, can anyone here tell me based on past their experience, how the change in temperature will affect the mechanical design of the following comp:
1. Tube (SS) - Guess the tube thickness will not be affected.
2. Shell - Un affected
3. Tubesheet - ??
4. Bolts - ???
5. Other comps - ??
Thanks in advance.
2.
Design: ASME Div 1/TEMA
Service: Crude Oil Cooler
Location: Offshore Platform
Tubeside, 316L, Shell side CS (Cooling water)
=============================================
We plan to rerate an existing S&T Hex which has already been operating for a period of close to 3 years. The idea is to increase the design temperature of the exchanger from 115 deg to 145 deg C.
Steps:
=====
1. Take measurement to acertain remaning thickness (UT, etc).
2. Review calc to determine if the increase in temperature can be accomodated by the present design
3. If required and depending upon the magnitude of this mod, removal of it to the fab shop might be necessary. Then the complete mods, design calcs and rehydrotest will be required I guess.
4. If the current mech design can accomodate the change, the design calcs needs to certification and the nameplate rating has to be cahnged and the equipment rehydrotested again.
The question is, can anyone here tell me based on past their experience, how the change in temperature will affect the mechanical design of the following comp:
1. Tube (SS) - Guess the tube thickness will not be affected.
2. Shell - Un affected
3. Tubesheet - ??
4. Bolts - ???
5. Other comps - ??
Thanks in advance.
2.