Stefan2211
Chemical
- Jun 25, 2020
- 104
Anyone has quick solution:
Problem: We have a large heat exchanger with floating head. The diameter of the tubesheet is around 900 mm with 641 tubes (25.4 x 2 mm). The whole bundle is SS316L (5000kg). The bundle had to be heated in a furance to remove the internal turbulators as there was a severe coking problem. After reinstatement of the bundle (30 m high - vertical)the hydro test failed at 8 bar. There is a leak between tube sheet and floating head. Max. torque of 300 Nm has been already applied. We suspect the heating could have deformed the tube sheet (85mm thick). In the furnace only the tubes were heated - tube sheets were outside the heating zone.
Question: How can the leak be repaired in short time?
Some ideas:
1. Using bolts with higher torque allowance.
2. Using different gaskets to allow a higher compression rate. Right now it uses metal grooved gaskets (2 mm stainless steel with 1 mm graphite layers). Could we use double (sandwich)?
The heat exchanger is operated with 275 Deg C hot oil in the shell and 200 of hydrocarbons in the tube side. A leak would cause major problems.
Thanks for any suggestion.
Problem: We have a large heat exchanger with floating head. The diameter of the tubesheet is around 900 mm with 641 tubes (25.4 x 2 mm). The whole bundle is SS316L (5000kg). The bundle had to be heated in a furance to remove the internal turbulators as there was a severe coking problem. After reinstatement of the bundle (30 m high - vertical)the hydro test failed at 8 bar. There is a leak between tube sheet and floating head. Max. torque of 300 Nm has been already applied. We suspect the heating could have deformed the tube sheet (85mm thick). In the furnace only the tubes were heated - tube sheets were outside the heating zone.
Question: How can the leak be repaired in short time?
Some ideas:
1. Using bolts with higher torque allowance.
2. Using different gaskets to allow a higher compression rate. Right now it uses metal grooved gaskets (2 mm stainless steel with 1 mm graphite layers). Could we use double (sandwich)?
The heat exchanger is operated with 275 Deg C hot oil in the shell and 200 of hydrocarbons in the tube side. A leak would cause major problems.
Thanks for any suggestion.