Dear all,
I am working on my graduation Project and i am asked to make a complete simulation for a simple binary distillation coloumn control using LabView software.
So far I have studied the control strategies and the different control schemes so please correct me if wrong.
The control variables are:
Top and bottom Compositions
Condenser drum level
Bottom level
Compositions are controled by controlling bottom and top trays temperatures.
Bottom temperature is varied by varying the steam flow rate in the reboiler
Levels are controlled by the bottoms and distillates flow
I assumed that Pressure is perfectly controlled.
so
The coloumn control is a MIMO and i want to break it first into SISOs
how can i get a model or transfer function for these variables or should i develop a mathematical model from the mass, material and energy balances???
also i have a question..
Is the reflux ratio kept constant for the coloumn??? i.e when controlling top temperaure using reflux flow, does the distillate flow change as well to keep L/D constant.
Thanks in advance
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Distillation Column Control Questions
Started by omarax, Apr 28 2009 05:19 AM
4 replies to this topic
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#1
Posted 28 April 2009 - 05:19 AM
#2
Posted 28 April 2009 - 07:13 PM
Omarax,
a) It is very important that you should control the pressure at the top of the tower. In real world you will never get the exact same feed all the time and separation is influenced strongly by the pressure of the tower.
You say that you control the top and bottom product composition by varying the heat input to the tower. You control the distillate and bottom flow based on level, to me it seems that this could create problem in maintaining the material balance ie. feed in = product out.
c) The reflux ratio varies to get the required distillate purity. It depends on the quality of feed.
Hope this helps,
Abhishek
a) It is very important that you should control the pressure at the top of the tower. In real world you will never get the exact same feed all the time and separation is influenced strongly by the pressure of the tower.

c) The reflux ratio varies to get the required distillate purity. It depends on the quality of feed.
Hope this helps,
Abhishek
#3
Posted 29 April 2009 - 02:39 PM
Thanks for your concern
How is Column pressure controlled? Which Manipulated variable is used?
i read that the cooling water flow in the condenser is used to control the coloumn pressure but i dont understand how pressure is affected by cooling water flow??
Is there a mathematical model or transfer function for pressure control??
Thanks
How is Column pressure controlled? Which Manipulated variable is used?
i read that the cooling water flow in the condenser is used to control the coloumn pressure but i dont understand how pressure is affected by cooling water flow??
Is there a mathematical model or transfer function for pressure control??
Thanks
#4
Posted 30 April 2009 - 11:17 AM
QUOTE (omarax @ Apr 29 2009, 11:39 AM) <{POST_SNAPBACK}>
Thanks for your concern
How is Column pressure controlled? Which Manipulated variable is used?
i read that the cooling water flow in the condenser is used to control the coloumn pressure but i dont understand how pressure is affected by cooling water flow??
Is there a mathematical model or transfer function for pressure control??
Thanks
How is Column pressure controlled? Which Manipulated variable is used?
i read that the cooling water flow in the condenser is used to control the coloumn pressure but i dont understand how pressure is affected by cooling water flow??
Is there a mathematical model or transfer function for pressure control??
Thanks
Column pressure is most often controlled by controlling the overhead flowrate out of the column. Under some circumstances, you might control the top pressure using the heat removed (i.e. condenser duty). To some extent this is done by controlling the reflux flow. You imply that that is done in a different way when you talk about manipulating cooling water flow to the condenser. Though I don't see anything inherently wrong with the concept of manipulating condenser duty, it would not be wise to throttle the cooling water flowrate. this is best kept constant to minimize fouling.
#5
Posted 30 April 2009 - 06:23 PM
Oramax,
The most effective scheme to control the column pressure depends on the type of condenser. Go though the article : A Soley, Effectively Control Column Pressure, CEP January 2001.
If you can upload a sketch of your configuration we will be in a better position to advise you.
abhishek
The most effective scheme to control the column pressure depends on the type of condenser. Go though the article : A Soley, Effectively Control Column Pressure, CEP January 2001.
If you can upload a sketch of your configuration we will be in a better position to advise you.
abhishek
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