Deactivation of Silicoaluminophosphate SAPO-34 in Methanol Conversion to Lower Olefins in Different Types of Reactors


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Comparative analysis of deactivation of the catalyst SAPO-34 for methanol conversion to lower olefins was carried out in fixed-bed flow reactors, in fluidized-bed reactors, and slurry reactors with the catalyst dispersed in a polydimethylsiloxane (PDMS) medium. It has been found that the deactivation rate of the catalyst essentially depends on the reactor type. The uniform contact of methanol with the fluidized catalyst makes it possible to increase by one and a half the on-stream stability compared with the fixed bed catalyst. However, the reaction run in the PDMS medium in the slurry reactor leads to significant acceleration of deactivation, which is due to high solubility of olefins and methanol in PDMS and results in an increase in the contact time of the catalyst with the reactants and products. A method has been proposed for measuring the solubility of gases in liquid polymers at high temperatures using mass-spectroscopic detection of effluent gases.

作者简介

V. Pavlov

Topchiev Institute of Petrochemical Synthesis, Russian Academy of Sciences

编辑信件的主要联系方式.
Email: pavlov@ips.ac.ru
俄罗斯联邦, Moscow

S. Konnov

Topchiev Institute of Petrochemical Synthesis, Russian Academy of Sciences

Email: pavlov@ips.ac.ru
俄罗斯联邦, Moscow

P. Kots

Faculty of Chemistry, Moscow State University

Email: pavlov@ips.ac.ru
俄罗斯联邦, Moscow

I. Ivanova

Topchiev Institute of Petrochemical Synthesis, Russian Academy of Sciences; Faculty of Chemistry, Moscow State University

Email: pavlov@ips.ac.ru
俄罗斯联邦, Moscow; Moscow

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