Benzene Column Delta T Conrol Using Reflux
Benzene Column Delta T Conrol Using Reflux
(OP)
I am involved with the operation of a Benzene Column being fed with extract from a Sulfolane Unit. Even though this unit is 40 years old, all the instrumentation is working (with some updates). The operators refuse to run the Differential Temperature controller in the automatic mode, because they are afraid the tower will flood if a temperature excursion occurs. Currently, the reboiler is being operated by controlling the steam flow to it. My question is : Would operating the reboiler on temperature control improve the column's ability to withstand changes in feed rates/composition? Any input would be greatly appreciated.





RE: Benzene Column Delta T Conrol Using Reflux
"Distillation Control" (McGraw-Hill) in particular the chapter on reboiler control.
RE: Benzene Column Delta T Conrol Using Reflux
the reason operators like flow control to the reboiler is that it is predictable and stable.
you can use temperature to modulate the steam flow setpoint but it is not a good idea to control the steam valve by the temperature controller only. The swings are too wild.
Given that you have old instrumentation, leave it alone, when you go to cascade controls you also have to build into your controls various constraints (pressure, boilup, L/V, etc.) to keep the column stable. That is easy for modern DCS type systems, though commissioning the controls is potentially difficult.
Shinskey's book is a good one to have, Page Buckley is also a good refeence-though mostly dealing with modeling.
RE: Benzene Column Delta T Conrol Using Reflux
I have seen several unstable columns that are run in "manual" or have layers of DCS constraints placed on them to make up for this problem. My opinion on this last part is that controls engineers over emphasize programming over the basics.