Skip to main content
Log in

Development and introduction of a highly efficient catalyst for the butane–butylene fraction oligomerization process for the production of a high-octane automobile gasoline compound

  • Catalysis in Petroleum Refining Industry
  • Published:
Catalysis in Industry Aims and scope Submit manuscript

Abstract

The main stages in developing a technology for the production of high-silica ZSM-5 zeolite-based catalyst for the butane–butylene fraction (BBF) oligomerization process are described. The application of a new zeolite surface modification procedure allows the attainment of higher selectivity and target product yields (compared to familiar analogs) and the synthesis of more branched (and thus more high-octane) oligomers at lower pressures. The introduction of promoting metal Ga raises the target gasoline fraction yield by 0.9%, compared to the unpromoted catalyst. Comparative pilot tests of industrial (BAK-70U) and the developed (Ga-ZSM-5/Al2O3) BBF oligomerization catalysts are performed under the following conditions: pressure, 1.5 MPa; initial working temperature, 300°C; feedstock hourly space velocity (FHSV), 1.5 mL BBF/(mL cat h). It is shown that using modified ZSM-5 based catalyst results in a gasoline fraction yield 7% higher than with BAK-70U. The higher quality of the oligomerizate obtained on Ga-ZSM-5/Al2O3 is observed throughout the period of tests (191 h): MON is 2 points higher, and the concentration of gums is 50% lower. The results from these studies and tests are used for the development and industrial implementation of a technology for the production of the KOB-1 zeolite oligomerization catalyst: 2.5 t of industrial catalyst has been produced by September of 2016 at the industrial facilities of ZAO Redkino Catalyst Plant. The next important stage in the implementation of the Gazprom Netf innovative development strategy in oil refining is a pilot run of the new oligomerization catalyst in the combined industrial MTBE–oligomerizate production plant of Gazprom Neft Moscow Oil Refinery. The introduction of the KOB-1 catalyst at the Gazprom Neft Oil Refinery will be an important step in improving the efficiency of technologies for the production of high-margin products, especially compounds of commercial automobile gasoline.

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. Popov, A.G., Fedosov, D.A., Ivanova, I.I., Vedernikov, O.S., Kleimenov, A.V., Kondrashev, D.O., Miroshkina, V.D., Abrashenkov, P.A., and Kuznetsov, S.E., Pet. Chem., 2016, vol. 56, no. 3, pp. 237–243.

    Article  CAS  Google Scholar 

  2. Coelho, A., Caeiro, G., Lemos, M.A.N.D.A., Lemos, F., and Ribeirol, F.R., Fuel, 2013, vol. 111, pp. 449–460.

    Article  CAS  Google Scholar 

  3. Miller, S.J., Stud. Surf. Sci. Catal., 1988, vol. 38, pp. 187–197.

    Article  Google Scholar 

  4. Pellet, R.J., Coughlin, P.K., Shamshoum, E.S., and Rabo, J.A., ACS Symp. Ser., 1988, vol. 368, pp. 512–531.

    Article  CAS  Google Scholar 

  5. De Klerk, A., Energy Fuels, 2007, vol. 21, no. 6, pp. 3084–3089.

    Article  Google Scholar 

  6. O’Connor, C.T., in Handbook of Heterogeneous Catalysis, Ertl, G., Knözinger, H., and Weitkamp, J., Eds., Weinheim: Wiley-VHC, 1997, vol. 5, p. 2380.

    Google Scholar 

  7. WO Patent 0204575A2, 2002.

  8. Occelli, M.L., Hsu, J.T., and Galaya, L.G., J. Mol. Catal., 1985, vol. 32, no. 3, pp. 377–390.

    Article  CAS  Google Scholar 

  9. Corma, A. and Iborra, S., in Catalysts for Fine Chemical Synthesis, Microporous and Mesoporous Solid Catalysts, Derouane, E.G. and Roberts, S.M., Eds., New York: Wiley, 2006, vol. 4, p. 125.

    Book  Google Scholar 

  10. Chen, N.Y., Garwood, W.A., and Dwyer, F.G., Shape Selective Catalysis in Industrial Applications, New York: Marcel Dekker, 1996.

    Google Scholar 

  11. TR (Technical Regulations) 05766623-20-2011: Combined MTBE–Oligomerizate Production Plant, 2011.

Download references

Author information

Authors and Affiliations

Authors

Corresponding author

Correspondence to D. O. Kondrashev.

Additional information

Original Russian Text © D.O. Kondrashev, A.V. Andreeva, 2017, published in Kataliz v Promyshlennosti.

Rights and permissions

Reprints and permissions

About this article

Check for updates. Verify currency and authenticity via CrossMark

Cite this article

Kondrashev, D.O., Andreeva, A.V. Development and introduction of a highly efficient catalyst for the butane–butylene fraction oligomerization process for the production of a high-octane automobile gasoline compound. Catal. Ind. 9, 239–246 (2017). https://doi.org/10.1134/S2070050417030072

Download citation

  • Received:

  • Published:

  • Issue Date:

  • DOI: https://doi.org/10.1134/S2070050417030072

Keywords

Navigation