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Optimal configuration of ternary distillation columns using heat integration with external heat exchangers

机译:通过与外部热交换器进行热集成来优化三元蒸馏塔的配置

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摘要

The subject of energy saving in distillation column sequencing is of critical importance. Heat integration in a multicomponent separation can be industrialized by saving considerable energy and cost. In this work, external heat-integrated distillation column with external heat exchanger has been studied and the annual cost function has been optimized using Genetic Algorithm. Introducing the layout and binary matrices enabled the investigation of all possible locations for the heat exchanger arrangement successfully. Moreover, exchangers heat loads and compressors pressure, have also been considered as optimization variables. Benzene, toluene, xylene and n-alkanes, separations have been studied as case studies. It has been demonstrated that the proposed optimization method in the alkane separation case decreased the total annual cost by 22.6% in comparison with the proposed thermally coupled distillation sequence columns. The heat integration of external heat exchangers in an external heat-integrated distillation column configuration and the proposed dived-wall column resulted in decreasing the total annual cost by 17% and 39% respectively, in comparison with conventional distillation columns.
机译:蒸馏塔测序中的节能主题至关重要。多组分分离中的热集成可通过节省大量能源和成本实现工业化。在这项工作中,研究了带有外部热交换器的外部热集成蒸馏塔,并使用遗传算法优化了年度成本函数。通过引入布局和二进制矩阵,可以成功研究热交换器布置的所有可能位置。此外,换热器的热负荷和压缩机压力也被视为优化变量。苯,甲苯,二甲苯和正构烷烃的分离已作为案例研究。已经证明,与提出的热耦合蒸馏顺序塔相比,在烷烃分离情况下提出的优化方法使年度总成本降低了22.6%。与传统的蒸馏塔相比,采用外部热集成蒸馏塔配置的外部热交换器和拟议的浮壁塔的热集成分别使年度总成本降低了17%和39%。

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