sahsanb
Materials
- May 31, 2013
- 56
We have been facing repeated tube leakages issues with our ammonia condensers having carbon steel tubes. Exchanger shell side has Ammonia at 130oC and 17 kg/cm2g while tube side has cooling water at 34oC and 4.2 kg/cm2g. Tube OD is 19.05 mm and ID is 14.83 mm. We suspect due to poor cooling water quality, tubes fouling and subsequent corrosion is the cause of tube leakages. We have engaged a vendor for providing us a solution to salvage the exchanger before it gets beyond repair. They have proposed installation of SS 316L full length liners of 0.7 mm thickness on the 11.7 meter long horizontal shell & tube type heat exchanger.
Vendor has claimed in addition to salvaging the non-leaking tubes, full length liners will also reclaim the leaking tubes. Considering your experience please share:
What is the extent of leakage in terms of through & through flaw size that full length liner can bear
What is the likelihood that full length liner will fail under differential pressure of shell and tube side pressure when installed on a leaking tube.
Considering tube thickness of 2.11 CS metallurgy and liner thickness of 0.7 mm how much heat transfer capability will be reduced in terms of approx %age / tube
Any other areas we must look into prior to installing the lines on our equipment
Regards,
Vendor has claimed in addition to salvaging the non-leaking tubes, full length liners will also reclaim the leaking tubes. Considering your experience please share:
What is the extent of leakage in terms of through & through flaw size that full length liner can bear
What is the likelihood that full length liner will fail under differential pressure of shell and tube side pressure when installed on a leaking tube.
Considering tube thickness of 2.11 CS metallurgy and liner thickness of 0.7 mm how much heat transfer capability will be reduced in terms of approx %age / tube
Any other areas we must look into prior to installing the lines on our equipment
Regards,