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Comparison of heterogeneous azeotropic and pressure-swing distillations for separating the diisopropylether/isopropanol/water mixtures

机译:非均相共沸和压力 - 摆动蒸馏除去二异丙基/异丙醇/水混合物的比较

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摘要

Isopropanol and diisopropylether are the two important organic solvents in the chemical industry. The diisopropylether/isopropanol/water mixtures contain multiple homogenous and heterogeneous minimum-boiling azeotropes being sensitive to the pressure. In the present study, three separation alternatives, including a new heterogeneous azeotropic distillation (HAD) and two conventional pressure-swing distillations (PSD), are designed conceptually on the ternary diagram of this mixture. And then their optimal design parameters are obtained via the sequential iterative search procedure based on the minimum total annual cost. Furthermore, several partial or full heat integration schemes of the optimal configuration are constructed and explored by using the temperature-enthalpy diagram. The result shows that the most competitive heat-integrated PSD configuration compared to the HAD can save 19.47% and 16.14% in the energy consumption and TAC, respectively. (C) 2019 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
机译:异丙醇和二异丙基是化学工业中的两个重要的有机溶剂。二异丙基/异丙醇/水混合物含有多种均匀和非均相最小沸腾的共沸物对压力敏感。在本研究中,三种分离替代品,包括新的异构共沸蒸馏(具有)和两个常规的压力 - 摆动蒸馏(PSD)在该混合物的三元图上概念设计。然后,通过基于最短的年度成本,通过顺序迭代搜索程序获得最佳设计参数。此外,通过使用温度 - 焓图来构建和探索最佳配置的几种部分或全热集成方案。结果表明,与曾有相比的最具竞争性的热量PSD配置分别可以节省19.47%和16.14%的能耗和TAC。 (c)2019化学工程师机构。 elsevier b.v出版。保留所有权利。

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