Hello everybody,
I'm trying to get an estimate of how much would be the total drop of temperature right after a pressure reduction valve using Invenys PRO/II 9.0.
I have the stream composition, the strem temperature before passing through the valve and I have the total pressure drop caused by the valve; how can I use PRO/II to predict the total temperature drop due to Joule-Thomson effect?
Thanks a lot!



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