Abstract:Self-optimizing control of a reactor−separator−recycle process with A + B → C reaction chemistry is evaluated for mode I (minimize recycle rate or column boilup at given production) and mode II (maximize throughput with maximum recycle or boilup as the bottleneck). In both modes, one unconstrained degree of freedom (DOF) remains after accounting for the active constraints. Through an analysis of the overall plant material balance, it is shown that the reactor A to B ratio is a good self-optimizing variable for… Show more
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