dimeivan
Chemical
- Jun 25, 2009
- 11
I need to specify a water cooled exchanger.
The problem is that I have an elevated temperature difference between tubeside and shellside, and temperature cross.
The conditions of service are as follow:
Tubeside - high pressure N2/H2 mixture (gas, no condensation) 6868 kg/h, Tin/out= 168/40ºC
Shellside - cooling water, 44900 kg/h, Tin/out= 32/48.2ºC
As shown, temperature cross put multipass exchangers out of the question. I do not want to use F shells either because of thermal expansion issues. Expansion joints in E shells are not allowed by client´s design practices too.
Increasing water flow is not feasible either because of supply limits.
The only solution I forsee are multitube hairpins, but my client strongly prefers TEMA hxs.
Has anyone a practical TEMA solution to this? Have in mind that multiple one-pass shells do not solve the thermal expansion issue.
Many Thanks
The problem is that I have an elevated temperature difference between tubeside and shellside, and temperature cross.
The conditions of service are as follow:
Tubeside - high pressure N2/H2 mixture (gas, no condensation) 6868 kg/h, Tin/out= 168/40ºC
Shellside - cooling water, 44900 kg/h, Tin/out= 32/48.2ºC
As shown, temperature cross put multipass exchangers out of the question. I do not want to use F shells either because of thermal expansion issues. Expansion joints in E shells are not allowed by client´s design practices too.
Increasing water flow is not feasible either because of supply limits.
The only solution I forsee are multitube hairpins, but my client strongly prefers TEMA hxs.
Has anyone a practical TEMA solution to this? Have in mind that multiple one-pass shells do not solve the thermal expansion issue.
Many Thanks