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Abstract.
The multivessel batch column consists of a reboiler, several column
sections and intermediate vessels and a condenser vessel. This
configuration provides a generalization of previously proposed batch
distillation schemes, including the inverted column and the middle
vessel column. The total reflux operation of the multivessel batch
distillation column was presented recently, and the main contribution
of this paper is to propose a simple feedback control strategy for its
operation. We propose to adjust the vessel holdups indirectly, by
manipulating the reflux flow out of each vessel to control the
temperature at some location in the column section below. The
feasibility of this strategy is demonstrated by simulations.