Journal
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION
Volume 110, Issue -, Pages 172-187Publisher
ELSEVIER SCIENCE SA
DOI: 10.1016/j.cep.2016.10.009
Keywords
Extractive dividing wall column; Pressure-swing distillation; Dynamic control; Acetonitrile/n-propanol system
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This paper addresses the design and the control analysis of the extractive dividing wall column and the pressure-swing distillation for separating acetonitrile (MeCN)/n-propanol system using Aspen Plus and Aspen Dynamics. The steady state design of the two processes was optimized by minimizing the total annual cost (TAC) via a sequential iterative optimization procedure. On the basis of the steady-state results, the dynamic control of the two processes and the comparison between them were presented. The results show that the pressure-swing distillation has the advantages for the economic savings and the control stability compared with the extractive dividing wall column process. (C) 2016 Elsevier B.V. All rights reserved.
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