Jack Nicholson
Chemical
- Oct 20, 2016
- 119
Hi everyone. I have a question. Would you please help me?
On the attached PFD, we have a circulation drum (310-V-4) which transfer and get refrigerant ethane to/from coldbox heat exchanger.
In the case of accidentally closing of PV and LV, all liquid ethane in circulation drum could vaporize due to heat transfer with atmosphere, so that at 35 C, the vessel pressure would be 45 barg (design pressure: 13 barg).
What would be the PSV sizing scenario? We have thermal expansion scenario, but it is applicable to line with full of liquid. Also we have blocked outlet scenario, but it is applicable to pump discharge or wellhead pipelines.
Thanks in advance
On the attached PFD, we have a circulation drum (310-V-4) which transfer and get refrigerant ethane to/from coldbox heat exchanger.
In the case of accidentally closing of PV and LV, all liquid ethane in circulation drum could vaporize due to heat transfer with atmosphere, so that at 35 C, the vessel pressure would be 45 barg (design pressure: 13 barg).
What would be the PSV sizing scenario? We have thermal expansion scenario, but it is applicable to line with full of liquid. Also we have blocked outlet scenario, but it is applicable to pump discharge or wellhead pipelines.
Thanks in advance