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An ideal internally heat integrated batch distillation with a jacketed still with application to a reactive system

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  • Jana, Amiya K.
  • Maiti, Debadrita

Abstract

Batch distillation is an irreversible process and consumes many times the theoretical minimum energy requirement. The present work focuses on the development of an internally heat integrated batch distillation with a jacketed still (IHIBDJS) aiming to reduce the degree of irreversibility towards zero. The IHIBDJS scheme consists of a rectifying tower equipped with an overhead condenser and a still pot or reboiler that surrounds the tower concentrically. For improving the energy efficiency by the reduction of external energy input, the rectifier is operated at an elevated pressure so that a thermal driving force should exist between the rectifying tower and the concentric still. For this purpose, an isentropic compression system is mounted in the reboiled vapor line. Aiming to reduce further the degree of process irreversibility, we propose an additional thermal arrangement into the IHIBDJS configuration that couples the overhead vapor with the reboiler liquid, thereby reducing further the external heat consumption. It is investigated for a reactive batch distillation column that the effective use of internal heat sources would make the heat integrated column an independent scheme of external heat source.

Suggested Citation

  • Jana, Amiya K. & Maiti, Debadrita, 2013. "An ideal internally heat integrated batch distillation with a jacketed still with application to a reactive system," Energy, Elsevier, vol. 57(C), pages 527-534.
    • Handle: RePEc:eee:energy:v:57:y:2013:i:c:p:527-534
    DOI: 10.1016/j.energy.2013.05.014
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    References listed on IDEAS

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    1. Maiti, Debadrita & Jana, Amiya K. & Samanta, Amar Nath, 2011. "A novel heat integrated batch distillation scheme," Applied Energy, Elsevier, vol. 88(12), pages 5221-5225.
    2. Jana, Amiya K., 2010. "Heat integrated distillation operation," Applied Energy, Elsevier, vol. 87(5), pages 1477-1494, May.
    3. 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.
    4. Suphanit, B., 2010. "Design of internally heat-integrated distillation column (HIDiC): Uniform heat transfer area versus uniform heat distribution," Energy, Elsevier, vol. 35(3), pages 1505-1514.
    5. Babu, G. Uday Bhaskar & Aditya, R. & Jana, Amiya K., 2012. "Economic feasibility of a novel energy efficient middle vessel batch distillation to reduce energy use," Energy, Elsevier, vol. 45(1), pages 626-633.
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    Cited by:

    1. Kim, Young Han, 2014. "Application of partially diabatic divided wall column to floating liquefied natural gas plant," Energy, Elsevier, vol. 70(C), pages 435-443.

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