Control of a triple-column pressure-swing distillation process
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文摘

A control system is developed for a non-ideal azeotropic distillation process.

Four control structures are evaluated for a triple-column pressure-swing process.

Single-end temperature control is used in each column.

Pressure-compensation improves performance in the low-pressure column.

Disturbances in throughput and feed composition are adequately handled.

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