Hi,
after study state simulation of a refining column, i am tring the dynamic simulation.
the software didn't converge because i made valves between the refining column and the side stripper to controle the stripper level wich made a pressure dop of draw stream.
please, what is the solution? can any one help me with an example if it is possible.
thank you.
regards,
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Dynamic Simulation Of Refining Column
Started by mhamdi khaled, Nov 27 2016 07:14 PM
3 replies to this topic
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#1
Posted 27 November 2016 - 07:14 PM
#2
Posted 27 November 2016 - 09:47 PM
Side strippers are usually fed via pump at a pumparound stage.
Bobby
#3
Posted 28 November 2016 - 01:30 AM
Bobby,
thank you for you response.
In the reality,there are not pumps between the main column and side stripper. in fact, side strippers are not fed via pumps and in steady state simulation, products (naphtha, kerosene, L.Gasoil and H.Gasoil) enter side strippers with trays pressure.
the software is hysys.
regards,
thank you for you response.
In the reality,there are not pumps between the main column and side stripper. in fact, side strippers are not fed via pumps and in steady state simulation, products (naphtha, kerosene, L.Gasoil and H.Gasoil) enter side strippers with trays pressure.
the software is hysys.
regards,
Edited by mhamdi khaled, 28 November 2016 - 01:34 AM.
#4
Posted 28 November 2016 - 01:53 AM
hi, can you share your simulation please (in XML because i have 9.0 version). regards
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