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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

Probably the best but not the most economic solution is trying some simulation tool like PIPESYS, PROFES, HYSYS 3.0.1 that calculate transient pressures/flow. I really admire your effort in dealing yourself with a spreadsheet. Good Luck and best regards

fdomin, I am engaged in the same problem about predicting a slug catcher after running HYSYS / PIPESYS software. Then I will appreciate very much if you can send me the GPSA article you have mentiones above. MY EMAIL IS: attiliopraderio@cantv.net Also if TD2K could remember a more exact...

Morten, Thanks a lot for the info. It is very useful. Regards. Attilio

Morten I tried the address but it moved I can no get there can you help me please??

zdas04 could you provide a little more detail in the "dry gas" term..please.... I deal with a retrogade gas condensation fluid in a 200 km 16 inches pipeline and I will like to use your 36 ft/sec term...

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...