Skip to main content
Log in

Optimal Operation and Control of Four-Product Dividing-Wall (Kaibel) Distillation Column

  • Research Article - Chemical Engineering
  • Published:
Arabian Journal for Science and Engineering Aims and scope Submit manuscript

Abstract

Due to globalization and increased market competition, the process industry is seeking to maximize productivity at minimal operational cost. Distillation operation alone accounts for a significant amount of the world’s energy consumption. This consumption can be greatly reduced by using a complex distillation column configuration, such as a fully thermally coupled distillation column or divided-wall distillation column, over conventional arrangements. The divided-wall column offers potential energy and capital investment savings. In this study, it was shown that energy savings of up to 25% can be achieved by using a four-product divided-wall distillation column (Kaibel) compared with conventional column arrangements. The reported capital investment associated with a four-product divided-wall column is approximately 30%. However, design and operation remain a challenge due to the large number of design and operational degrees of freedom. Divided-wall columns can be used for multicomponent separation as well. This research demonstrated the steady-state and dynamic behavior of a Kaibel distillation column using commercial simulation software, i.e., Aspen HYSYS. A self-optimizing control scheme was implemented to reject disturbances during operation and to meet the required product specifications for a Kaibel distillation column.

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. Humphrey, J.; Siebert, A.: Separation technologies: an opportunity for energy savings. Chem. Eng. Prog. 88, 32–41 (1992)

    Google Scholar 

  2. Schaller, M.: Numerically optimized diabatic distillation columns. PHD thesis, Technische Universitat Chemnitz, Fakultat fur Naturwissenschaften, Germany (2007)

  3. Brugma, A.: Dutch Patent No. 41,850 (1937)

  4. Wright, R.: Fractionation apparatus, US Patent 2,471,134 (1949)

  5. Petlyuk, F.: Thermodynamically optimal method for separating multicomponent mixtures. Int. Chem. Eng. 5, 555–561 (1965)

    Google Scholar 

  6. Kolbe, B.; Wenzel, S.: Novel distillation concepts using one-shell columns. Chem. Eng. Process. Process Intensif. 43(3), 339–346 (2004)

    Article  Google Scholar 

  7. Kaibel, G.: Distillation columns with vertical partitions. Chem. Eng. Technol. 10, 92–98 (1987)

    Article  Google Scholar 

  8. Agrawal, R.: More operable fully thermally coupled distillation column configurations for multicomponent distillation. Chem. Eng. Res. Des. 77(6), 543–553 (1999)

    Article  Google Scholar 

  9. Kvernland, M.: Model predictive control of a Kaibel distillation column. IFAC Proc. 43, 553–558 (2009)

    Article  Google Scholar 

  10. Pan, H.; Yu, H.; Yuan, M.: Optimal operation mode switching of dividing wall distillation based on model-predictive control. In: Control and Decision Conference (2015)

  11. Kiss, A.; Rewagad, R.: Energy efficient control of a BTX dividing-wall column. Comput. Chem. Eng. 35(12), 2896–2904 (2011)

    Article  Google Scholar 

  12. Dwivedi, D.; Strandberg, J.: Steady state and dynamic operation of four-product dividing-wall (Kaibel) columns: experimental verification. Ind. Eng. Chem. Res. 51(48), 15696–15709 (2012)

    Article  Google Scholar 

  13. Strandberg, J.; Skogestad, S.: Stabilizing operation of a 4-product integrated Kaibel column. In: Institution of Chemical Engineers Symposium, pp. 638–647 (2006)

  14. Strandberg, J., Skogestad, S., Halvorsen, I.: Practical control of dividing wall columns. Proceedings of distillation and Absorption, pp. 527–532 (2010)

  15. Ghadrdan, M.; Skogestad, S.; Halvorsen, I.: Economically optimal control of Kaibel distillation column: fixed boilup rate. In: 8th IFAC Symposium, pp. 744–749 (2012)

    Article  Google Scholar 

  16. Skogestad, S.: Plantwide control: the search for the self-optimizing control structure. J. Process Control 10(5), 487–507 (2000)

    Article  Google Scholar 

  17. Ghadrdan, M.; Halvorsen, I.J.; Skogestad, S.: Optimal operation of Kaibel distillation columns. Chem. Eng. Res. Des. 89(8), 1382–1391 (2011)

    Article  Google Scholar 

  18. Halvorsen, I.; Skogestad, S.: Minimum energy consumption in multicomponent distillation. 3. More than three products and generalized Petlyuk arrangements. Ind. Eng. Chem. 42(3), 605–615 (2003)

    Article  Google Scholar 

  19. Ashrafian, R.: Using Dividing Wall Columns (DWC) in LNG Production: deviding wall column, double dividing wall column, prefractionator arrangement, Petlyuk column, NGL recovery, distillation. Master’s Thesis, NTNU, Trondheim (2014)

  20. Dejanović, I.; Matijašević, L.; Halvorsen, I.J.; Skogestad, S.; Jansen, H.; Kaibel, B.; Olujić, Ž.: Designing four-product dividing wall columns for separation of a multicomponent aromatics mixture. Chem. Eng. Res. Des. 89(8), 1155–1167 (2011)

    Article  Google Scholar 

Download references

Author information

Authors and Affiliations

Authors

Corresponding author

Correspondence to Abdallah Alshammari.

Ethics declarations

Conflict of interest

The authors declare that they have no conflict of interest.

Rights and permissions

Reprints and permissions

About this article

Check for updates. Verify currency and authenticity via CrossMark

Cite this article

Abid, F., Shamsuzzoha, M., Binous, H. et al. Optimal Operation and Control of Four-Product Dividing-Wall (Kaibel) Distillation Column. Arab J Sci Eng 43, 6067–6085 (2018). https://doi.org/10.1007/s13369-018-3259-2

Download citation

  • Received:

  • Accepted:

  • Published:

  • Issue Date:

  • DOI: https://doi.org/10.1007/s13369-018-3259-2

Keywords

Navigation