Окислительная переработка пропана в важные нефтехимические продукты на нанесенных ванадиевых катализаторах

Gulnar N. Kaumenova; Rabiga O. Sarsenova; Banu D. Kazhdenbek; Damir A. Abdyhalykov; Zauresh Zh. Zheksenbaeva; Svetlana A. Tungatarova; Tolkyn S. Baizhumanova

doi:10.15328/cb1037

Gulnar N. Kaumenova D.V. Sokolsky Institute of Fuel, Catalysis and Electrochemistry; al-Farabi Kazakh National University, Almaty, Kazakhstan https://orcid.org/0000-0002-6448-6607
Rabiga O. Sarsenova D.V. Sokolsky Institute of Fuel, Catalysis and Electrochemistry; Abay Kazakh National Pedagogical University, Almaty, Kazakhstan https://orcid.org/0000-0001-5669-8178
Banu D. Kazhdenbek al-Farabi Kazakh National University, Almaty, Kazakhstan https://orcid.org/0000-0002-9682-3313
Damir A. Abdyhalykov D.V. Sokolsky Institute of Fuel, Catalysis and Electrochemistry, Almaty, Kazakhstan https://orcid.org/0000-0001-7023-947X
Zauresh Zh. Zheksenbaeva D.V. Sokolsky Institute of Fuel, Catalysis and Electrochemistry; al-Farabi Kazakh National University, Almaty, kazakhstan
Svetlana A. Tungatarova D.V. Sokolsky Institute of Fuel, Catalysis and Electrochemistry; al-Farabi Kazakh National University, Almaty, kazakhstan https://orcid.org/0000-0001-6005-747X
Tolkyn S. Baizhumanova D.V. Sokolsky Institute of Fuel, Catalysis and Electrochemistry; al-Farabi Kazakh National University, Almaty, kazakhstan https://orcid.org/0000-0001-9851-2642

Keywords: catalytic oxidation, ethylene, hydrogen, activity of catalyst, vanadium catalyst

Abstract

The paper presents the data on activity of the deposited catalyst based on vanadium. The developed catalyst allows conducting the process of oxidative conversion of propane into ethylene and hydrogen using CO₂ as an oxidant. The study of the activity of the developed vanadium catalyst at the oxidative conversion of propane showed that the maximum ethylene yield was 24.5% at: C₃H₈:CO₂=2:1, T=700°C and W=1000 h^-1. The increase of temperature to 800°C resulted in the in formation of 27.5% hydrogen. By methods of BET and XRD the developed catalyst 5% V/Al₂O₃, is differed by increase of specific surface area and bonding of the carrier with active phase, contributing to increase of efficiency of the developed catalyst in the oxidative conversion of propane to ethylene and hydrogen.

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Oxidative processing of propane into important petrochemical products on deposited vanadium catalysts

Abstract

References

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