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Abstract.
The Petlyuk or dividing-wall or fully thermally coupled distillation
column is an interesting alternative to the conventional cascaded
binary columns for separation of multi-component mixtures. However,
the industrial use has been limited, and difficulties in operation
have been reported as one reason. With three product compositions
controlled, the system has two degrees of freedom left for online
optimization. We show that the steady-state optimal solution surface
is quite narrow, and depends strongly on disturbances and design
parameters. Thus it seems difficult to achieve the potential energy
savings compared to conventional approaches without a good control
strategy. We discuss candidate variables which may be used as feedback
variables in order to keep the column operation close to optimal in a
self-optimizing control scheme.
Note: This version may be slightly different from the finally published journal paper.