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Deethanizer Column Operation

coloumn operation

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#1 Piyush Kaushal

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Posted 19 May 2015 - 12:45 AM

Respected All,

 

I am into process consulting and as a result monitor an ethlyene cracker unit. In the de-ethanizer (DC2) unit i experience a decrease in coloumn overhead C3s with increase in coloumn bottom temperature (control tray temperature). I am unable to comprhend this phenomena. Kindly help



#2 shan

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Posted 19 May 2015 - 07:32 AM

Overhead C3s mass flow increase or mole fraction increase?



#3 ColinR33

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Posted 19 May 2015 - 10:24 AM

Is the column refluxed? Has the reflux flow/temperature changed? Has the tower operating pressure changed? We need more info for something like this in order to properly understand the system and offer suggestions. A PFD with the process variable before and after the temperature increase would be a great help.

#4 Bobby Strain

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Posted 19 May 2015 - 03:28 PM

If you don't have a process simulator like HYSYS, you should get one of the free distillation programs. Then you can understand the phenomena.

 

Bobby



#5 RockDock

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Posted 20 May 2015 - 09:26 AM

It sounds like the reflux has increased, too. While a higher reboiler temperature would vaporize more C3, the condenser is what ultimately controls the C3 in the C2 product.






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