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A novel intensified heat integration in multicomponent distillation

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  • Kiran, Bandaru
  • Jana, Amiya K.
  • Samanta, Amar Nath

Abstract

In this contribution, a novel intensified heat integrated ternary distillation column (int-HITDiC) is introduced. The objective is to show the superiority of the int-HITDiC over its general form, namely the HITDiC and the conventional standalone column on the basis of two criteria: energy consumption and economics. The concept of pinch technology has been applied to identify the feasibility region for internal thermal coupling between two diabatic sections, namely the rectifying section and stripping section. In this study, the influence of system parameters on the behavior of HITDiC is examined. The optimum compression ratio is arrived at by taking into account the energetic and economic aspects. Performing a detailed analysis, it is observed that the general HITDiC scheme shows lower energy consumption and better economic figure compared to its conventional counterpart. Aiming to improve the overall efficiency further, the int-HITDiC scheme has been explored. The proposed intensified strategy gets the advantage of both HIDiC and direct vapor recompression column (VRC).

Suggested Citation

  • Kiran, Bandaru & Jana, Amiya K. & Samanta, Amar Nath, 2012. "A novel intensified heat integration in multicomponent distillation," Energy, Elsevier, vol. 41(1), pages 443-453.
    • Handle: RePEc:eee:energy:v:41:y:2012:i:1:p:443-453
    DOI: 10.1016/j.energy.2012.02.055
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    References listed on IDEAS

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    2. Kiss, Anton A. & Flores Landaeta, Servando J. & Infante Ferreira, Carlos A., 2012. "Towards energy efficient distillation technologies – Making the right choice," Energy, Elsevier, vol. 47(1), pages 531-542.
    3. Jana, Amiya K., 2016. "A new divided-wall heat integrated distillation column (HIDiC) for batch processing: Feasibility and analysis," Applied Energy, Elsevier, vol. 172(C), pages 199-206.
    4. 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.
    5. Bessa, Larissa C.B.A. & Ferreira, M.C. & Batista, Eduardo A.C. & Meirelles, Antonio J.A., 2013. "Performance and cost evaluation of a new double-effect integration of multicomponent bioethanol distillation," Energy, Elsevier, vol. 63(C), pages 1-9.
    6. Modla, G. & Lang, P., 2013. "Heat pump systems with mechanical compression for batch distillation," Energy, Elsevier, vol. 62(C), pages 403-417.
    7. Jana, Amiya K., 2016. "An internal thermal integration arrangement for multicomponent batch rectifier: 1. Feasibility and analysis," Energy, Elsevier, vol. 115(P1), pages 230-237.
    8. Haragovics, Máté & Mizsey, Péter, 2014. "A novel application of exergy analysis: Lean manufacturing tool to improve energy efficiency and flexibility of hydrocarbon processing," Energy, Elsevier, vol. 77(C), pages 382-390.
    9. Tgarguifa, Ahmed & Abderafi, Souad & Bounahmidi, Tijani, 2018. "Energy efficiency improvement of a bioethanol distillery, by replacing a rectifying column with a pervaporation unit," Renewable Energy, Elsevier, vol. 122(C), pages 239-250.
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