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I am trying to design a Kettle Reboler for a Demethanizer where the liquid entering will have to raise its temperature by around 15C due to the flasing of almost 3% of its mass. The liquid composition is Methane, Ethane and Propane (basically). The heat experts that I have consulted are...

I always get an error when using that option with a nine flash flowsheet. Has any one got troubles with that option?? Regards

I will apprecaite to exchange experiences on the way to best applicate the PR-SV using Margules and WS mixing rules..

I will apreciate to know how to export and HYSYS 3.01 to make it readable to PRO II. Best Regards Attilio Praderio

I am looking for a CO2 partial pressure vs. corrosion levels similar to the one thai I have found fot the H2S where there is a line that states the maximum pressure level to admisible corrosion... I have looked for the Gas Processors (GPSA) books... without sucess.. Ihave no acces to NACE...