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Dear Users,
I am having a problem with tuning a PI controller for a dynamic reactive distillation column model. My problem is that my degrees of freedome are Reflux Ratio and Reboiler Duty which I can have to control bottom product composition. Can anyone suggest how it can be done?
I am having a problem with tuning a PI controller for a dynamic reactive distillation column model. My problem is that my degrees of freedome are Reflux Ratio and Reboiler Duty which I can have to control bottom product composition. Can anyone suggest how it can be done?