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Eco-efficient vapor recompression-assisted pressure-swing distillation process for the separation of a maximum-boiling azeotrope

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  • Shi, Pengyuan
  • Zhang, Qingjun
  • Zeng, Aiwu
  • Ma, Youguang
  • Yuan, Xigang

Abstract

The feasibility and effectiveness of the intensified vapor recompression-assisted pressure-swing distillation (PSDVRC) arrangements in different separation sequences are explored with separating a maximum-boiling methanol/diethylamine azeotrope as the specific example. The energy-efficient Heat Exchanger Network Synthesis (HENs) option is used to further improve the possible energy recovery in certain arrangement. The globally optimal arrangement is the intensified self-heat recuperative vapor recompression-assisted PSDVRC-FP-HEN process in the low-pressure column (LPC)-to-high pressure column (HPC) sequence. The reductions of 39.33% (13.93%) in total annual cost, 89.12% (81.95%) in carbon footprints, and the improvement of 116.31% (44.71%) in second-law efficiency can be achieved in comparison with the conventional process, wherein, the data in these brackets represent the economically optimal heat-integrated configuration. And the exergy destruction in each component (Sankey diagram) for all eco-efficiently intensified alternatives are obtained. Result shows that the exergy increase in LPC-to-HPC sequence is higher than that of another sequence, along with the major exergy losses generated in columns, and the distribution of the irreversibility for each individual component in the system is approximately identical when the entropy production analysis and exergy analysis are employed.

Suggested Citation

  • Shi, Pengyuan & Zhang, Qingjun & Zeng, Aiwu & Ma, Youguang & Yuan, Xigang, 2020. "Eco-efficient vapor recompression-assisted pressure-swing distillation process for the separation of a maximum-boiling azeotrope," Energy, Elsevier, vol. 196(C).
    • Handle: RePEc:eee:energy:v:196:y:2020:i:c:s0360544220302024
    DOI: 10.1016/j.energy.2020.117095
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    References listed on IDEAS

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    1. Kravanja, Philipp & Modarresi, Ala & Friedl, Anton, 2013. "Heat integration of biochemical ethanol production from straw – A case study," Applied Energy, Elsevier, vol. 102(C), pages 32-43.
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    3. 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.
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    Cited by:

    1. Hegely, Laszlo & Lang, Peter, 2023. "Optimisation of the higher pressure of pressure-swing distillation of a maximum azeotropic mixture," Energy, Elsevier, vol. 271(C).
    2. Ferchichi, Mariem & Hegely, Laszlo & Lang, Peter, 2022. "Economic and environmental evaluation of heat pump-assisted pressure-swing distillation of maximum-boiling azeotropic mixture water-ethylenediamine," Energy, Elsevier, vol. 239(PE).
    3. Wang, Danfeng & Gu, Yu & Chen, Qianqian & Tang, Zhiyong, 2023. "Direct conversion of syngas to alpha olefins via Fischer–Tropsch synthesis: Process development and comparative techno-economic-environmental analysis," Energy, Elsevier, vol. 263(PE).
    4. 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).
    5. Dai, Min & Yang, Han & Yang, Fusheng & Zhang, Zaoxiao & Yu, Yunsong & Liu, Guilian & Feng, Xiao, 2022. "Multi-strategy Ensemble Non-dominated sorting genetic Algorithm-II (MENSGA-II) and application in energy-enviro-economic multi-objective optimization of separation for isopropyl alcohol/diisopropyl et," Energy, Elsevier, vol. 254(PA).

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