Steady State Simulation of Reactive Distillation for TAME Synthesis

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  • Matsuda Keigo
    Department of Chemistry and Chemical Engineering, Yamagata University
  • Ikoshi Tatsuro
    Department of Chemistry and Chemical Engineering, Yamagata University
  • Yamaki Takehiro
    Department of Chemistry and Chemical Engineering, Yamagata University
  • Shishido Masahiro
    Department of Chemistry and Chemical Engineering, Yamagata University
  • Iwakabe Koichi
    Polypropylene Division, Prime Polymer Co., Ltd.
  • Ohmori Takao
    Research Institute for Innovation in Sustainable Chemistry, National Institute of Advanced Industrial Science and Technology (AIST)
  • Nakaiwa Masaru
    Research Institute for Innovation in Sustainable Chemistry, National Institute of Advanced Industrial Science and Technology (AIST)

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Other Title
  • ＴＡＭＥ合成反応蒸留システムの定常シミュレーション
  • TAME ゴウセイ ハンノウ ジョウリュウ システム ノ テイジョウ シミュレーション

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Abstract

The present work proposes a method for process intensification of the reaction-separation process. A model of the reactive distillation (RD) system involving a prereactor was developed by use of an equilibrium stage model, and the reaction-separation of a multicomponent mixture was simulated by use of a simulator that was capable of predicting steady-state conditions. The developed model was applied to an RD system with multi-feed, and the reaction-separation and operation performance were examined. As a result, the RD system was found to be usable for reaction-separation interaction phenomena. This process improved the function and performance of conventional reaction-separation process and could be miniaturized.

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