Iradah
Chemical
- May 31, 2011
- 66
Hello all,
I have a question regarding lube oil heat exchanger designed for us by one of the companies.
we noticed after commissioning the system that the hot oil is not getting cooled. we think that there is no enough cooling water flow into the heat exchanger and working on increasing it. however, it was observed that the change in water temperature is very small, we think that if there is a small flow of cooling water into the heat exchanger, then the outlet temperature of water should be much higher than the inlet which is not the case. Does this suggest that there is a blockage inside the exchangers and there is no water flow inside the exchangers and that is why a very small temperature difference is observed between the inlet and outlet?
Another big concern I have is the configuration of the exchanger, it is shell and tube with the inlet and outlet of the shell on the top of the shell, inlet on right side and outlet on left side. the tubes are two passes with inlet and outlet nozzles above each other at the left side of the exchanger, the inlet is the top nozzle and the outlet is the bottom nozzle.
Please advise if you think that this configuration can lead to temperature cross or diminish the temperature driving force.
Thank you.
I have a question regarding lube oil heat exchanger designed for us by one of the companies.
we noticed after commissioning the system that the hot oil is not getting cooled. we think that there is no enough cooling water flow into the heat exchanger and working on increasing it. however, it was observed that the change in water temperature is very small, we think that if there is a small flow of cooling water into the heat exchanger, then the outlet temperature of water should be much higher than the inlet which is not the case. Does this suggest that there is a blockage inside the exchangers and there is no water flow inside the exchangers and that is why a very small temperature difference is observed between the inlet and outlet?
Another big concern I have is the configuration of the exchanger, it is shell and tube with the inlet and outlet of the shell on the top of the shell, inlet on right side and outlet on left side. the tubes are two passes with inlet and outlet nozzles above each other at the left side of the exchanger, the inlet is the top nozzle and the outlet is the bottom nozzle.
Please advise if you think that this configuration can lead to temperature cross or diminish the temperature driving force.
Thank you.