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Abstract.
The experimental verification of the operation of a multivessel batch
distillation column, operated under total reflux is presented. This
column configuration, consisting of several column sections and
intermediate vessels, provides a generalization of previously proposed
batch distillation schemes. We propose a simple feedback control
strategy which is capable to achieve a desired product composition in
all product vessels, even for widely varying feed compositions. The
idea is to use the reflux flow out of each vessel to control the
temperature at some location in the section below. The practicality of
the proposed control scheme has previously been demonstrated by
dynamic simulations, and in this paper we present experimental results
from a laboratory scale apparatus which verify these simulations.