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Advanced energy saving in distillation process with self-heat recuperation technology

Author

Listed:
  • Matsuda, Kazuo
  • Kawazuishi, Kenichi
  • Kansha, Yasuki
  • Fushimi, Chihiro
  • Nagao, Masaki
  • Kunikiyo, Hiroshi
  • Masuda, Fusao
  • Tsutsumi, Atsushi

Abstract

In the distillation process, heat is supplied at a feed heater and a reboiler, and an overhead stream is cooled at a condenser. Almost all of the supplied heat at the reboiler in the conventional distillation process is discarded in the overhead condenser. Conventional energy savings of the distillation processes were fundamentally attained as a result of heat recovery duty in the feed heater being maximized by using the heat of the bottom stream, which enabled the utility (steam or hot oil) rate to the feed heater to be reduced. To achieve further energy saving in the distillation process, “self-heat recuperation technology” (SHRT) was adopted. In this technology, two compressors are installed in the overhead vapor line, which consists of the reflux and the overhead product streams. A compressor (compressor-1) treats the reflux stream and the other compressor (compressor-2) treats the overhead stream. The reboiler duty is supplied by the recuperated heat of the discharged stream from compressor-1 and the feed heater duty is supplied by that from compressor-2, by adiabatic compressions. It could be found that the advanced process with SHRT was able to reduce the energy consumption significantly by using the recuperated heat of the overhead vapor.

Suggested Citation

  • Matsuda, Kazuo & Kawazuishi, Kenichi & Kansha, Yasuki & Fushimi, Chihiro & Nagao, Masaki & Kunikiyo, Hiroshi & Masuda, Fusao & Tsutsumi, Atsushi, 2011. "Advanced energy saving in distillation process with self-heat recuperation technology," Energy, Elsevier, vol. 36(8), pages 4640-4645.
    • Handle: RePEc:eee:energy:v:36:y:2011:i:8:p:4640-4645
    DOI: 10.1016/j.energy.2011.03.042
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    References listed on IDEAS

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    2. Van Duc Long, Nguyen & Lee, Moonyong, 2013. "A novel NGL (natural gas liquid) recovery process based on self-heat recuperation," Energy, Elsevier, vol. 57(C), pages 663-670.
    3. Mojarab Soufiyan, Mohamad & Dadak, Ali & Hosseini, Seyed Sina & Nasiri, Farshid & Dowlati, Majid & Tahmasebi, Maryam & Aghbashlo, Mortaza, 2016. "Comprehensive exergy analysis of a commercial tomato paste plant with a double-effect evaporator," Energy, Elsevier, vol. 111(C), pages 910-922.
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    5. Cui, Chengtian & Qi, Meng & Zhang, Xiaodong & Sun, Jinsheng & Li, Qing & Kiss, Anton A. & Wong, David Shan-Hill & Masuku, Cornelius M. & Lee, Moonyong, 2024. "Electrification of distillation for decarbonization: An overview and perspective," Renewable and Sustainable Energy Reviews, Elsevier, vol. 199(C).
    6. Cui, Chengtian & Long, Nguyen Van Duc & Sun, Jinsheng & Lee, Moonyong, 2020. "Electrical-driven self-heat recuperative pressure-swing azeotropic distillation to minimize process cost and CO2 emission: Process electrification and simultaneous optimization," Energy, Elsevier, vol. 195(C).
    7. Kansha, Yasuki & Ishizuka, Masanori & Song, Chunfeng & Tsutsumi, Atsushi, 2015. "Process intensification for dimethyl ether production by self-heat recuperation," Energy, Elsevier, vol. 90(P1), pages 122-127.
    8. Xia, Hui & Ye, Qing & Feng, Shenyao & Li, Rui & Suo, Xiaomeng, 2017. "A novel energy-saving pressure swing distillation process based on self-heat recuperation technology," Energy, Elsevier, vol. 141(C), pages 770-781.
    9. Kazemi, Abolghasem & Mehrabani-Zeinabad, Arjomand & Beheshti, Masoud, 2018. "Recently developed heat pump assisted distillation configurations: A comparative study," Applied Energy, Elsevier, vol. 211(C), pages 1261-1281.
    10. Modla, G., 2013. "Energy saving methods for the separation of a minimum boiling point azeotrope using an intermediate entrainer," Energy, Elsevier, vol. 50(C), pages 103-109.
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