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Exergy simulation and optimization of adiabatic and diabatic binary distillation

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  • Rivero, Ricardo

Abstract

A detailed exergy analysis of a distillation system has been conducted. This analysis is divided in four parts: (1) adiabatic rectification column; (2) adiabatic stripping column; (3) diabatic rectification column; and (4) diabatic stripping column. The results of all cases are presented in this paper. This analysis concerns the mixture water–ethanol working at 1 bar. The main objective is to determine the distribution of exergy losses inside the column and the optimal distribution of heat to be transferred inside the column in order to produce the minimum overall exergy losses.

Suggested Citation

  • Rivero, Ricardo, 2001. "Exergy simulation and optimization of adiabatic and diabatic binary distillation," Energy, Elsevier, vol. 26(6), pages 561-593.
    • Handle: RePEc:eee:energy:v:26:y:2001:i:6:p:561-593
    DOI: 10.1016/S0360-5442(01)00020-2
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    Cited by:

    1. Nguyen, Nghi & Demirel, Yaşar, 2010. "Retrofit of distillation columns in biodiesel production plants," Energy, Elsevier, vol. 35(4), pages 1625-1632.
    2. Suphanit, B. & Bischert, A. & Narataruksa, P., 2007. "Exergy loss analysis of heat transfer across the wall of the dividing-wall distillation column," Energy, Elsevier, vol. 32(11), pages 2121-2134.
    3. Cortés, E. & Rivera, W., 2010. "Exergetic and exergoeconomic optimization of a cogeneration pulp and paper mill plant including the use of a heat transformer," Energy, Elsevier, vol. 35(3), pages 1289-1299.
    4. Nguyen, Nghi & Demirel, Yaşar, 2011. "Using thermally coupled reactive distillation columns in biodiesel production," Energy, Elsevier, vol. 36(8), pages 4838-4847.
    5. Chen, Ting & Zhang, Bingjian & Chen, Qinglin, 2014. "Heat integration of fractionating systems in para-xylene plants based on column optimization," Energy, Elsevier, vol. 72(C), pages 311-321.
    6. Rizk, J. & Nemer, M. & Clodic, D., 2012. "A real column design exergy optimization of a cryogenic air separation unit," Energy, Elsevier, vol. 37(1), pages 417-429.
    7. Khalili-Garakani, Amirhossein & Ivakpour, Javad & Kasiri, Norollah, 2016. "Evolutionary synthesis of optimum light ends recovery unit with exergy analysis application," Applied Energy, Elsevier, vol. 168(C), pages 507-522.
    8. Olujić, Ž. & Sun, L. & de Rijke, A. & Jansens, P.J., 2006. "Conceptual design of an internally heat integrated propylene-propane splitter," Energy, Elsevier, vol. 31(15), pages 3083-3096.
    9. Hernández, Salvador & Gabriel Segovia-Hernández, Juan & Rico-Ramírez, Vicente, 2006. "Thermodynamically equivalent distillation schemes to the Petlyuk column for ternary mixtures," Energy, Elsevier, vol. 31(12), pages 2176-2183.
    10. Wei, Zhiqiang & Zhang, Bingjian & Wu, Shengyuan & Chen, Qinglin & Tsatsaronis, George, 2012. "Energy-use analysis and evaluation of distillation systems through avoidable exergy destruction and investment costs," Energy, Elsevier, vol. 42(1), pages 424-433.
    11. Sun, Jinsheng & Wang, Fan & Ma, Tingting & Gao, Hong & Wu, Peng & Liu, Lili, 2012. "Energy and exergy analysis of a five-column methanol distillation scheme," Energy, Elsevier, vol. 45(1), pages 696-703.
    12. de Koeijer, Gelein & Røsjorde, Audun & Kjelstrup, Signe, 2004. "Distribution of heat exchange in optimum diabatic distillation columns," Energy, Elsevier, vol. 29(12), pages 2425-2440.

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