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Process integration in bioprocess indystry: waste heat recovery in yeast and ethyl alcohol plant

Author

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  • Rašković, P.
  • Anastasovski, A.
  • Markovska, Lj.
  • Meško, V.

Abstract

The process integration of the bioprocess plant for production of yeast and alcohol was studied. Preliminary energy audit of the plant identified the huge amount of thermal losses, caused by waste heat in exhausted process streams, and reviled the great potential for energy efficiency improvement by heat recovery system. Research roadmap, based on process integration approach, is divided on six phases, and the primary tool used for the design of heat recovery network was Pinch Analysis. Performance of preliminary design are obtained by targeting procedure, for three process stream sets, and evaluated by the economic criteria. The results of process integration study are presented in the form of heat exchanger networks which fulfilled the utilization of waste heat and enable considerable savings of energy in short payback period.

Suggested Citation

  • Rašković, P. & Anastasovski, A. & Markovska, Lj. & Meško, V., 2010. "Process integration in bioprocess indystry: waste heat recovery in yeast and ethyl alcohol plant," Energy, Elsevier, vol. 35(2), pages 704-717.
    • Handle: RePEc:eee:energy:v:35:y:2010:i:2:p:704-717
    DOI: 10.1016/j.energy.2009.11.020
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    References listed on IDEAS

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    1. Rašković, Predrag & Stoiljković, Sreten, 2009. "Pinch design method in the case of a limited number of process streams," Energy, Elsevier, vol. 34(5), pages 593-612.
    2. Quintero, J.A. & Montoya, M.I. & Sánchez, O.J. & Giraldo, O.H. & Cardona, C.A., 2008. "Fuel ethanol production from sugarcane and corn: Comparative analysis for a Colombian case," Energy, Elsevier, vol. 33(3), pages 385-399.
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    Cited by:

    1. Luo, Xianglong & Zhang, Bingjian & Chen, Ying & Mo, Songping, 2012. "Heat integration of regenerative Rankine cycle and process surplus heat through graphical targeting and mathematical modeling technique," Energy, Elsevier, vol. 45(1), pages 556-569.
    2. Toffolo, Andrea & Lazzaretto, Andrea & von Spakovsky, Michael R., 2012. "On the nature of the heat transfer feasibility constraint in the optimal synthesis/design of complex energy systems," Energy, Elsevier, vol. 41(1), pages 236-243.
    3. Cortes-Rodríguez, Edgar Fernando & Fukushima, Nilton Asao & Palacios-Bereche, Reynaldo & Ensinas, Adriano V. & Nebra, Silvia A., 2018. "Vinasse concentration and juice evaporation system integrated to the conventional ethanol production process from sugarcane – Heat integration and impacts in cogeneration system," Renewable Energy, Elsevier, vol. 115(C), pages 474-488.
    4. Posada, J.A. & Cardona, C.A., 2010. "Design and analysis of fuel ethanol production from raw glycerol," Energy, Elsevier, vol. 35(12), pages 5286-5293.
    5. Stamp, Jane & Majozi, Thokozani, 2011. "Optimum heat storage design for heat integrated multipurpose batch plants," Energy, Elsevier, vol. 36(8), pages 5119-5131.
    6. Klemeš, Jiří Jaromír & Varbanov, Petar Sabev & Walmsley, Timothy G. & Jia, Xuexiu, 2018. "New directions in the implementation of Pinch Methodology (PM)," Renewable and Sustainable Energy Reviews, Elsevier, vol. 98(C), pages 439-468.
    7. Yun, Huimin & Wang, Meng & Feng, Wei & Tan, Tianwei, 2013. "Process simulation and energy optimization of the enzyme-catalyzed biodiesel production," Energy, Elsevier, vol. 54(C), pages 84-96.

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