MexTijuana
Chemical
- Jul 4, 2013
- 4
Hello guys,
I try to calculate the temperature drop in the vena contracta of a pressure regulation valve to get an imagine, if propane condensate occurs.
The upstream pressure is app. 13 bar and the downstream pressure is 3 bar. It is a DN25 pipe and the mass flow is 200 g/s. The fluid is propane.
To my knowledge their should be a temperture drop due to Joule Thompson effect and a temperture due to the acceleration of the propane in the vena contracta. Drops the temperature below the dew point condensate occurs.
My Problem is that I do not know how to calculate the temperature drop.
Can you please help.
Thanks in advance!
I try to calculate the temperature drop in the vena contracta of a pressure regulation valve to get an imagine, if propane condensate occurs.
The upstream pressure is app. 13 bar and the downstream pressure is 3 bar. It is a DN25 pipe and the mass flow is 200 g/s. The fluid is propane.
To my knowledge their should be a temperture drop due to Joule Thompson effect and a temperture due to the acceleration of the propane in the vena contracta. Drops the temperature below the dew point condensate occurs.
My Problem is that I do not know how to calculate the temperature drop.
Can you please help.
Thanks in advance!