Rate-based Modeling for Internally Heat-integrated Distillation Column (HIDiC) in Binary System

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  • Matsuda Keigo
    Energy-Efficient Chemical Systems Gr., Research Institute for Innovation in Sustainable Chemistry, National Institute of Advanced Industrial Science and Technology
  • Iwakabe Koichi
    Energy-Efficient Chemical Systems Gr., Research Institute for Innovation in Sustainable Chemistry, National Institute of Advanced Industrial Science and Technology
  • Kubo Kazuya
    Production Technology Lab., Mitsubishi Chemical Group Science and Technology Research Center, Inc.
  • Horiguchi Akio
    Production Technology Lab., Mitsubishi Chemical Group Science and Technology Research Center, Inc.
  • Weifang Yu
    Energy-Efficient Chemical Systems Gr., Research Institute for Innovation in Sustainable Chemistry, National Institute of Advanced Industrial Science and Technology
  • Kosuge Hitoshi
    Dept. of Chemical Engineering, Graduate School of Science and Engineering, Tokyo Institute of Technology
  • Kataoka Sho
    Energy-Efficient Chemical Systems Gr., Research Institute for Innovation in Sustainable Chemistry, National Institute of Advanced Industrial Science and Technology
  • Yamamoto Takuji
    Energy-Efficient Chemical Systems Gr., Research Institute for Innovation in Sustainable Chemistry, National Institute of Advanced Industrial Science and Technology
  • Ohmori Takao
    Energy-Efficient Chemical Systems Gr., Research Institute for Innovation in Sustainable Chemistry, National Institute of Advanced Industrial Science and Technology
  • Nakaiwa Masaru
    Energy-Efficient Chemical Systems Gr., Research Institute for Innovation in Sustainable Chemistry, National Institute of Advanced Industrial Science and Technology

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Other Title
  • 速度論モデルを用いた内部熱交換型蒸留塔（HIDiC）の2成分系分離シミュレーション
  • ソクドロン モデル オ モチイタ ナイブ ネツ コウカンガタ ジョウリュウトウ HIDiC ノ 2 セイブンケイ ブンリ シミュレーション

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Abstract

The model for the bench plant of internally heat-integrated distillation column (HIDiC) with structured packings was developed by a rate-based model and the separation of benzene-toluene binary mixture was simulated. The developed model has been applied as bench-plant for HIDiC, and their separation and operation performance was discussed. The validity of the simulation results was confirmed with the experimental data of the HIDiC bench plant. In addition, the simulation results were also compared with those obtained with the conventional equilibrium model. It was found that the present model can predict the behavior of the bench plant more precisely than the conventional equilibrium model. Moreover, the energy-saving ratio in the HIDiC system has also investigated using this simulator with rate-based model.<br>

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