I am in process of calculating depressurization rate for condensate dehydrator. LPG condensate composition as follows: Component Mole. Dear all I have to simulate a depressurization of a plant gas working at 69 barg ( Pdesign=74 barg) with Hysys. I know that I have to do 2. HYSYS Depressurisation Example – Free download as PDF File .pdf), Text File . txt) or read online for free. Depressurization Hysys.
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Depressurization By Hysys – Chemical Process Simulation – Community
I am in process of calculating depressurization rate for condensate dehydrator. LPG condensate composition as follows: Total System Volume Depressurization within a vessel results in adiabatic cooling. Lowered temperature even negative is expected. At the outlet of a valve, the gas could either warm or cool, depending on the Joule-Thompson coefficient.
These are both described in most textbooks about thermodynamics. As a practical consideration, in real world applications the cooling could be so great that specialized metallurgy low temperature carbon steel or stainless steel would be required because of the possibility of metal embrittlement.
Chemical & Process Technology: How to apply valve equation in HYSYS Depressuring ?
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