Skip to main content
Log in

Process design of complex systems of rectification columns and the evaluation of their effectiveness with the assumption of the range of feed composition

  • Chemical Engineering Processes and Equipment
  • Published:
Theoretical Foundations of Chemical Engineering Aims and scope Submit manuscript

Abstract

Using the CHEMCAD modeling program, a procedure has been developed for designing complex systems of rectification columns with partially and fully coupled heat and mass flows for various compositions of feed flow that vary in a wide range. The developed procedure has been implemented based on the example of close-cut separation of a three-component zeotropic system. The separation efficiency has been evaluated using two criteria, i.e., the economic (reduced economic expenses) and energy (total heat load of condensers and boilers) efficiency of simple and complex rectification systems.

This is a preview of subscription content, log in via an institution to check access.

Access this article

Price excludes VAT (USA)
Tax calculation will be finalised during checkout.

Instant access to the full article PDF.

Similar content being viewed by others

References

  1. Aleksandrov, I.A., Peregonka i rektifikatsiya v neftepererabotke (Sublimation and Rectification in Oil Refining), Moscow: Khimiya, 1981.

    Google Scholar 

  2. Komissarov, Yu.A., Gordeev, L.S., and Vent, D.P., Nauchnye osnovy protsessov rektifikarsii. Uchebnoe posobie (Scientific Foundations of Rectification Processes. A Tutorial), Serafimov, L.A., Ed., Moscow: Khimiya, 2004, vol.2.

  3. Frolkova, A.K. and Khakhin, L.A., Entropy estimation of binary mixture rectification at different variants of process calculation, Mosk. Gos. Univ. Tonkikh Khim. Tekhnol. im. M.V. Lomonosova, 2008, vol. 3, no. 2, pp. 53–61.

    Google Scholar 

  4. Petlyuk, F.B. and Serafimov, L.A., Mnogokomponentnaya rektifikatsiya. Teorita i raschet (Multicomponent Rectification: Theory and Calculation), Moscow: Khimiya, 1983.

    Google Scholar 

  5. Petlyuk, F.B., Platonov, V.M., and Avet’yan, V.S., Optimal schemes of rectification of multicomponent mixtures, Khim. Prom., 1966, no. 11, pp. 65–69.

    Google Scholar 

  6. Dodge, B.F., Chemical Engineering Thermodynamics, New York: McGraw-Hill, 1944.

    Google Scholar 

  7. Alcantara-Avila, J.R., Cabrera-Ruiz, J., Segovia-Hernandez, J.G., Hernandez, S., and Rong, N.-G., Controllability analysis of thermodynamically equivalent thermally coupled arrangements for quaternary distillations, Chem. Eng. Res. Des., 2008, vol. 86, no. 1, pp. 23–37.

    Article  CAS  Google Scholar 

  8. Platonov, V.M. and Bergo, B.G., Razdelenie mnogokomponentnykh smesei (Separation of Multicomponent Mixtures), Moscow: Khimiya, 1965.

    Google Scholar 

  9. Nakaiwa, M. and Ohmori, T., Process intensification for energy savings through concept of “detuning” from ideal state, Transl. Synthesiol., 2009, vol. 2, no. 1, pp. 51–59.

    Article  Google Scholar 

  10. Nakaiwa, M., Huang, K., Endo, A., Ohmori, T., Akiya, T., and Takamatsu, T., Internally heat-integrated distillation columns: a review, Chem. Eng. Res. Des., 2003, vol. 81, no. 1, pp. 162–177.

    Article  CAS  Google Scholar 

  11. Mah, R.S.H., Nicholas, J.J., and Wodnik, R.B., Distillation with secondary reflux and vaporization: a comparative evaluation, AIChE J., 1977, vol. 23, no. 5, pp. 651–658.

    Article  CAS  Google Scholar 

  12. Timoshenko, A.V., Anokhina, E.A., Rudakov, D.G., Timofeev, V.S., Tatsievskaya, G.I., and Matyushenkova, Yu.V., Power saving in distillation using complexes with coupled flows, Mosk. Gos. Univ. Tonkikh Khim. Tekhnol. im. M.V. Lomonosova, 2011, vol. 6, no. 4, pp. 28–40.

    CAS  Google Scholar 

  13. Frolkova, A.K. and Khakhin, L.A., Entropy estimation of binary mixture rectification at different variants of process calculation, Mosk. Gos. Univ. Tonkikh Khim. Tekhnol. im. M.V. Lomonosova, 2008, vol. 3, no. 2, pp. 53–61.

    Google Scholar 

  14. Gartman, T.N. and Klushin, D.V., Osnovy kompyuternogo modelirovaniya khimiko-rekhnologicheskikh prorsessov (Fundamentals of Computer Simulation of Chemical Engineering Processes), Moscow: Akademkniga, 2006.

    Google Scholar 

  15. Wolff, E.A. and Skogestad, S., Operation of integrated three-product (Petlyuk) distillation columns, Ind. Eng. Chem. Res., 1995, vol. 34, no. 6, pp. 2094–2103.

    Article  CAS  Google Scholar 

  16. Caballero, J.A. and Grossmann, I.E., Logic based algorithms for the rigorous design of thermally coupled distillation sequences, Proc. 17th European Symp. on Computer Aided Process Engineering (ESCAPE17), Amsterdam: Elsevier, 2007.

    Google Scholar 

  17. Smith, R., Chemical Process Design, New York: McGraw-Hill, 1995.

    Google Scholar 

Download references

Author information

Authors and Affiliations

Authors

Corresponding author

Correspondence to A. V. Pankrushina.

Additional information

Original Russian Text © A.V. Pankrushina, T.N. Gartman, 2016, published in Khimicheskaya Tekhnologiya, 2016, Vol. 17, No. 8, pp. 367–376.

Rights and permissions

Reprints and permissions

About this article

Check for updates. Verify currency and authenticity via CrossMark

Cite this article

Pankrushina, A.V., Gartman, T.N. Process design of complex systems of rectification columns and the evaluation of their effectiveness with the assumption of the range of feed composition. Theor Found Chem Eng 51, 858–866 (2017). https://doi.org/10.1134/S0040579517050177

Download citation

  • Received:

  • Published:

  • Issue Date:

  • DOI: https://doi.org/10.1134/S0040579517050177

Keywords

Navigation