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Dehydrogenation of Cumene to α-Methylstyrene on [Re,W]/γ-Al2O3(K,Ce)/α-Al2O3 and [Fe,Cr]/γ-Al2O3(K,Ce)/α-Al2O3 Porous Ceramic Catalytic Converters

А. С. Федотов, В. И. Уваров, М. В. Цодиков, Sébastien Paul, Pardis Simon, Maya Marinova, Franck Dumeignil

2020Petroleum Chemistry12 citationsDOI

Abstract

Abstract The features of cumene dehydrogenation to α-methylstyrene on unique porous ceramic catalytic converters having the composition [Re,W]/γ-Al2O3(K,Ce)/α-Al2O3 and [Fe,Cr]/γ-Al2O3(K,Ce)/α-Al2O3, obtained using self-propagating high-temperature synthesis and the sol–gel method, have been studied. It has been established that at an optimum temperature of 625°C, the rhenium–tungsten-containing system has approximately 1.5 times higher catalytic activity than the iron–chromium system. On the Re–W-containing catalytic converter at the optimum temperature, the cumene conversion is ~71 mol %, the α-methylstyrene yield is ~77 mol % of theoretical, and the α-methylstyrene content in the products is ~35 mol %, with productivity for the desired product being ~7.4 g/(h gact.comp.). The degree of catalyst coking for 6 h of the experiment did not exceed 5 wt %.

Topics & Concepts

CumeneDehydrogenationCatalysisMaterials scienceYield (engineering)ChromiumSinteringPorosityTungstenCeramicCokeInorganic chemistryRheniumNuclear chemistryChemistryChemical engineeringMetallurgyOrganic chemistryComposite materialEngineeringCatalysis and Oxidation ReactionsCatalytic Processes in Materials ScienceCatalysts for Methane Reforming
Dehydrogenation of Cumene to α-Methylstyrene on [Re,W]/γ-Al2O3(K,Ce)/α-Al2O3 and [Fe,Cr]/γ-Al2O3(K,Ce)/α-Al2O3 Porous Ceramic Catalytic Converters | Litcius