首页> 外文OA文献 >Conceptual design of reactive distillation for selectivity improvement in multiple reactant systems
【2h】

Conceptual design of reactive distillation for selectivity improvement in multiple reactant systems

机译:反应精馏的概念设计,可提高多种反应物系统的选择性

摘要

Reactive distillation (RD) can be effectively used to improve selectivity by manipulating the composition profiles of reactants and products inside the reactive zone of a RD column. One can obtain close to quantitative yields if the azeotropes, if any, do not limit the separation. As against the single reactant systems (i.e. condensation, dimerization), more design options are available in the case of multiple reactants (e.g. esterification, cross aldol condensation) and we propose design guidelines for such systems in this work. The parametric studies for the representative hypothetical reaction systems, involving both reversible and irreversible reactions, form the basis of these guidelines. The cases associated with non-ideality through formation of azeotropes are also discussed. The analysis is further extended to real processes involving reactions such as cross aldol condensation, esterification and transesterification.
机译:反应性蒸馏(RD)可通过控制RD柱反应区内的反应物和产物的组成分布图有效地用于提高选择性。如果共沸物(如果有的话)不限制分离,则可以获得接近定量的产率。与单一反应物系统(即缩合,二聚)相比,在多种反应物(例如酯化,醛醇缩合)的情况下可提供更多的设计选择,我们在这项工作中提出了针对此类系统的设计指南。代表性假设反应系统的参数研究涉及可逆和不可逆反应,构成了本指南的基础。还讨论了通过共沸物的形成与非理想相关的情况。该分析进一步扩展到涉及反应的实际过程,例如,交叉羟醛缩合,酯化和酯交换反应。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号