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A reactive distillation column with double reactive sections for the separations of two-stage consecutive reversible reactions

机译:具有双反应段的反应蒸馏塔,用于分离两阶段连续的可逆反应

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摘要

In this paper, a novel reactive distillation column with double reactive sections (RDC-DRS) is proposed for the separations of two-stage consecutive reversible reactions. The arrangement of two reactive sections not only allows the careful coordination of the two reaction operations involved, but also provides additional degrees of freedom for the reinforcement of internal mass integration and/or internal energy integration between the reaction operations and the separation operation involved, which could facilitate the RDC-DRS to be more advantageous than the conventional reactive distillation column with a single reactive section (RDC-SRS) in operating cost and capital investment. A representative hypothetical and real two-stage consecutive reversible reactions are chosen to evaluate the steady-state performance of the RDC-DRS. With the constraints of the same total number of stages and the same total number of reactive stages, the RDC-DRS is demonstrated to require less utility consumption than the RDC-SRS and this outcome indicates that the former could be a competitive alternative to the latter in the separations of the two-stage consecutive reversible reactions. The number of reactive sections should therefore be viewed as an important decision variable for the synthesis and design of reactive distillation columns especially in the separations of complicated reacting mixtures involving multiple reversible reactions.
机译:本文提出了一种新型的具有双反应区的反应蒸馏塔(RDC-DRS),用于两步连续可逆反应的分离。两个反应区的布置不仅允许仔细协调所涉及的两个反应操作,而且还提供了额外的自由度,以增强反应操作和所涉及的分离操作之间的内部质量积分和/或内部能量积分。可以使RDC-DRS在运行成本和资本投资方面比具有单个反应段的常规反应蒸馏塔(RDC-SRS)更具优势。选择具有代表性的假设和真实的两阶段连续可逆反应来评估RDC-DRS的稳态性能。在相同的阶段总数和相同的反应阶段总数的约束下,RDC-DRS被证明比RDC-SRS需要更少的公用事业消耗,并且这一结果表明,前者可以替代后者在两阶段连续可逆反应的分离中。因此,反应段的数量应被视为反应蒸馏塔的合成和设计的重要决策变量,尤其是在涉及多个可逆反应的复杂反应混合物的分离中。

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