Zinc-Modified ZSM-5 Nanozeolites Synthesized by the Seed-Induced Method: Interrelation of Their Textural, Acidic, and Catalytic Properties in DME Conversion to Hydrocarbons
- Authors: Zhang K.1, Kurumov S.A.2, Su X.1, Snatenkova Y.M.2, Bukina Z.M.2, Kolesnichenko N.V.2, Wu W.1, Khadzhiev S.N.2
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Affiliations:
- National Center for International Research on Catalytic Technology, School of Chemistry and Material Sciences
- Topchiev Institute of Petrochemical Synthesis
- Issue: Vol 57, No 12 (2017)
- Pages: 1036-1042
- Section: Article
- URL: https://journals.rcsi.science/0965-5441/article/view/179739
- DOI: https://doi.org/10.1134/S0965544117120179
- ID: 179739
Cite item
Abstract
The effect of the method of introduction of zinc cations and the zinc content in a nanocrystalline zeolite of the ZSM-5 type on the physicochemical and catalytic properties of the material in DME conversion to a mixture of liquid synthetic hydrocarbons has been studied. Zinc is introduced into the catalysts both during the zeolite synthesis and the ion exchange (ZnnAlmNZ5 and ZnNZ5, respectively). The use of nanocrystalline ZnnAlmNZ5 zeolites provides the formation of a mixture of liquid hydrocarbons with a high selectivity of no less than 90%; the liquid hydrocarbons contain more than 70% of isoparaffins and a small amount of aromatic compounds. An increase in the zinc loading of the ZnnAlmNZ5 zeolite from 0.9 to ~3% leads to an increase in the methanol content in the aqueous phase of the liquid product, an increase in the selectivity for liquid hydrocarbons, and a slight increase in the concentration of aromatic and unsaturated hydrocarbons in the mixture. In the presence of the ZnNZ5/Al2O3 catalyst with Zn introduced by ion exchange, the methanol content in the aqueous phase and the aromatics content in the liquid hydrocarbon mixture are significantly higher. The ZnnAlmNZ5 nanozeolites are characterized by a more developed external surface, a higher concentration of mesopores, and higher acidity.
Keywords
About the authors
Ke Zhang
National Center for International Research on Catalytic Technology, School of Chemistry and Material Sciences
Email: nvk@ips.ac.ru
China, Harbin, Heilongjiang, 150080
S. A. Kurumov
Topchiev Institute of Petrochemical Synthesis
Email: nvk@ips.ac.ru
Russian Federation, Moscow
Xiaofang Su
National Center for International Research on Catalytic Technology, School of Chemistry and Material Sciences
Email: nvk@ips.ac.ru
China, Harbin, Heilongjiang, 150080
Yu. M. Snatenkova
Topchiev Institute of Petrochemical Synthesis
Email: nvk@ips.ac.ru
Russian Federation, Moscow
Z. M. Bukina
Topchiev Institute of Petrochemical Synthesis
Email: nvk@ips.ac.ru
Russian Federation, Moscow
N. V. Kolesnichenko
Topchiev Institute of Petrochemical Synthesis
Email: nvk@ips.ac.ru
Russian Federation, Moscow
Wei Wu
National Center for International Research on Catalytic Technology, School of Chemistry and Material Sciences
Author for correspondence.
Email: nvk@ips.ac.ru
China, Harbin, Heilongjiang, 150080
S. N. Khadzhiev
Topchiev Institute of Petrochemical Synthesis
Author for correspondence.
Email: nvk@ips.ac.ru
Russian Federation, Moscow
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