Hydroisomerization of Benzene-Containing Gasoline Fraction on Pt/B2O3–Al2O3 and Pt/WO3–Al2O3 Catalysts


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Abstract

The effect of the hydroisomerization conditions of the benzene-containing fraction of catalytic reforming gasoline on the yield and composition of products is studied on Pt/B2O3–Al2O3 and Pt/WO3–Al2O3 catalysts. These catalysts allow benzene to be completely removed from the raw material. At the same time, the greatest yields of liquid products are obtained with minimal losses of the octane number at 2 MPa, a mass feedstock hourly space velocity (MFHSV) of 2 h−1, and 325°C: 96.3 and 95.4 wt % on Pt/B2O3–Al2O3 and Pt/WO3–Al2O3 catalysts, respectively. The activity of the catalysts is maintained for 100 h during their operation.

About the authors

E. A. Buluchevskii

Institute of Problems of Hydrocarbon Processing, Siberian Branch; Omsk State University

Author for correspondence.
Email: bulu@ihcp.ru
Russian Federation, Omsk, 644040; Omsk, 644053

E. D. Fedorova

Institute of Problems of Hydrocarbon Processing, Siberian Branch

Email: bulu@ihcp.ru
Russian Federation, Omsk, 644040

A. V. Lavrenov

Institute of Problems of Hydrocarbon Processing, Siberian Branch

Email: bulu@ihcp.ru
Russian Federation, Omsk, 644040

M. V. Zhuravleva

Institute of Problems of Hydrocarbon Processing, Siberian Branch

Email: bulu@ihcp.ru
Russian Federation, Omsk, 644040

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