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Pt/BEA–Al2O3 catalysts for the isomerization of benzene/heptane mixtures. I: Optimizing the support’s composition Full article

Journal Catalysis in Industry
ISSN: 2070-0504 , E-ISSN: 2070-0555
Output data Year: 2017, Volume: 9, Number: 1, Pages: 48-53 Pages count : 6 DOI: 10.1134/s2070050417010032
Tags BEA, benzene hydroisomerization, beta zeolite, n-heptane isomerization, platinum catalysts
Authors Belopukhov E. A. 1,2 , Kalashnikov I. M. 1,2 , Smolikov M. D. 1,2 , Kir’yanov D. I. 1 , Gulyaeva T. I. 1 , Belyi A. S. 1,2
Affiliations
1 Institute of Hydrocarbons Processing, Siberian Branch, Russian Academy of Sciences, Omsk
2 Omsk State Technical University

Funding (2)

1 Ministry of Science and Higher Education of the Russian Federation 46.2.4
2 Federal Agency for Scientific Organizations V.46.2.8

Abstract: Pt/BEA–Al2O3 catalysts for the hydroisomerization of benzene-containing gasoline fractions are studied using a model feedstock (20% benzene and 80% n-heptane). The catalysts are prepared by varying the zeolite content from 5 to 70 wt % at a constant Pt loading of 0.3 wt % in all samples, with an aqueous H2PtCl6 solution being used as the Pt precursor. The acid properties of the samples are studied by means of temperature-programmed desorption (TPD). The effect of the support’s zeolite/binder ratio on the activity of the catalysts is determined: an increase in the zeolite content raises the system’s acidity and shifts the range of the reaction toward lower temperatures. The optimum zeolite/binder ratio is found to be 30% BEA/70% Al2O3. Changing the SiO2/Al2O3 ratio of the zeolite from 25 to 40 is shown to have no noticeable effect on catalyst activity. The use of the catalysts supported on 30% BEA/70% Al2O3 in the hydroisomerization of benzenecontaining gasoline fractions can be recommended for improving environmental performance.
Cite: Belopukhov E.A. , Kalashnikov I.M. , Smolikov M.D. , Kir’yanov D.I. , Gulyaeva T.I. , Belyi A.S.
Pt/BEA–Al2O3 catalysts for the isomerization of benzene/heptane mixtures. I: Optimizing the support’s composition
Catalysis in Industry. 2017. V.9. N1. P.48-53. DOI: 10.1134/s2070050417010032 WOS Scopus РИНЦ OpenAlex
Original: Белопухов Е.А. , Калашников И.М. , Смоликов М.Д. , Кирьянов Д.И. , Гуляева Т.И. , Белый А.С.
Катализаторы Pt/BEA–Al2O3 в реакции гидроизомеризации смеси бензол – гептан: i. оптимизация состава носителя
Катализ в промышленности. 2016. Т.16. №5. С.60-65. DOI: 10.18412/1816-0387-2016-5-60-65 РИНЦ OpenAlex
Dates:
Submitted: May 8, 2016
Published print: Jan 1, 2017
Published online: Apr 7, 2017
Identifiers:
Web of science: WOS:000423241100007
Scopus: 2-s2.0-85017150979
Elibrary: 29515072
OpenAlex: W2604503593
Citing:
DB Citing
Scopus 6
Web of science 7
Elibrary 5
OpenAlex 6
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