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Synthesis of heat exchanger network considering pressure drop and layout of equipment exchanging heat

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  • Souza, Rachitha D
  • Khanam, Shabina
  • Mohanty, Bikash

Abstract

The present work is related to development of a MINLP (Mixed integer non linear programming) model for the synthesis of HEN (heat exchanger network) considering pressure drop through connecting pipelines, heat exchangers and the layout of the equipment exchanging heat simultaneously. The pressure drop of shell and tube sides in a heat exchanger is considered in the model. Further, detailed plant layout is considered for accounting pressure drop in pipe line as well as piping cost. The objective function of the MINLP model is the TAC (total annual cost), which considers utility cost, capital investment cost of exchangers, pipe investment cost and pumping cost due to pressure drops in exchanger as well as in pipe length. The developed model is illustrated using a case study. The results show that the TAC of HEN is reduced by 27.4% than that obtained for the topology without considering pressure drop in exchanger. However, placement of exchangers in the layout contributes to 4.5% in TAC. Results found through the present model are compared with that of published models.

Suggested Citation

  • Souza, Rachitha D & Khanam, Shabina & Mohanty, Bikash, 2016. "Synthesis of heat exchanger network considering pressure drop and layout of equipment exchanging heat," Energy, Elsevier, vol. 101(C), pages 484-495.
    • Handle: RePEc:eee:energy:v:101:y:2016:i:c:p:484-495
    DOI: 10.1016/j.energy.2016.02.040
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    References listed on IDEAS

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    1. Soltani, Hadi & Shafiei, Sirous, 2011. "Heat exchanger networks retrofit with considering pressure drop by coupling genetic algorithm with LP (linear programming) and ILP (integer linear programming) methods," Energy, Elsevier, vol. 36(5), pages 2381-2391.
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    Cited by:

    1. Li, Nianqi & Klemeš, Jiří Jaromír & Sunden, Bengt & Wu, Zan & Wang, Qiuwang & Zeng, Min, 2022. "Heat exchanger network synthesis considering detailed thermal-hydraulic performance: Methods and perspectives," Renewable and Sustainable Energy Reviews, Elsevier, vol. 168(C).
    2. Chang, Chenglin & Wang, Yufei & Ma, Jiaze & Chen, Xiaolu & Feng, Xiao, 2018. "An energy hub approach for direct interplant heat integration," Energy, Elsevier, vol. 159(C), pages 878-890.
    3. Xiao, Wu & Wang, Kaifeng & Jiang, Xiaobin & Li, Xiangcun & Wu, Xuemei & Hao, Ze & He, Gaohong, 2019. "Simultaneous optimization strategies for heat exchanger network synthesis and detailed shell-and-tube heat-exchanger design involving phase changes using GA/SA," Energy, Elsevier, vol. 183(C), pages 1166-1177.
    4. Li, Nianqi & Klemeš, Jiří Jaromír & Sunden, Bengt & Wang, Qiuwang & Zeng, Min, 2022. "Heat exchanger network optimisation considering different shell-side flow arrangements," Energy, Elsevier, vol. 261(PA).
    5. Matthias Rathjens & Georg Fieg, 2019. "Cost-Optimal Heat Exchanger Network Synthesis Based on a Flexible Cost Functions Framework," Energies, MDPI, vol. 12(5), pages 1-18, February.
    6. Wang, Bohong & Klemeš, Jiří Jaromír & Li, Nianqi & Zeng, Min & Varbanov, Petar Sabev & Liang, Yongtu, 2021. "Heat exchanger network retrofit with heat exchanger and material type selection: A review and a novel method," Renewable and Sustainable Energy Reviews, Elsevier, vol. 138(C).

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