Formation of Epoxycyclooctane during the Co-Oxidation of Cyclooctene and Alkylbenzenes

IF 1.3 Q4 ENGINEERING, CHEMICAL Catalysis in Industry Pub Date : 2024-05-27 DOI:10.1134/S2070050424700041
N. I. Kuznetsova, V. N. Zudin
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Abstract

Cyclooctene and alkylbenzenes are subjected to co-oxidation in oxygen and a system of two catalysts. Radical catalyst Fe(acac)3/NHPI mediates the formation of alkylbenzene hydroperoxides, which are consumed in situ during the MoO3/SiO2-catalyzed epoxidation of cyclooctene. The chain oxidation rate is limited in cyclooctene and MoO3/SiO2, but radical catalyst Fe(acac)3/NHPI retains fairly high activity in the oxidation of alkylbenzene in hydroperoxide. It is found that isopropylbenzene is a better co-reducing agent than ethylbenzene because it ensures more vigorous and selective formation of epoxycyclooctane. At optimized amounts of components and a temperature of 80°C, selectivity toward epoxycyclooctane reaches 92 and 96% in ethylbenzene or isopropylbenzene, respectively, with more than 70% conversion of cyclooctene.

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环辛烯和烷基苯的共氧化作用生成环氧环辛烷
摘要环辛烯和烷基苯在氧气和两种催化剂体系中发生共氧化反应。自由基催化剂 Fe(acac)3/NHPI 介导了烷基苯氢过氧化物的形成,这些氢过氧化物在 MoO3/SiO2 催化环辛烯环氧化过程中被就地消耗。环辛烯和 MoO3/SiO2 的链氧化速率有限,但自由基催化剂 Fe(acac)3/NHPI 在过氧化氢烷基苯氧化过程中保持了相当高的活性。研究发现,异丙苯是比乙苯更好的共还原剂,因为它能确保环氧环辛烷的形成更有活力和选择性。在各组分的最佳用量和 80°C 的温度下,乙苯或异丙苯对环氧环辛烷的选择性分别达到 92% 和 96%,环辛烯的转化率超过 70%。
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来源期刊
Catalysis in Industry
Catalysis in Industry ENGINEERING, CHEMICAL-
CiteScore
1.30
自引率
14.30%
发文量
21
期刊介绍: The journal covers the following topical areas: Analysis of specific industrial catalytic processes: Production and use of catalysts in branches of industry: chemical, petrochemical, oil-refining, pharmaceutical, organic synthesis, fuel-energetic industries, environment protection, biocatalysis; technology of industrial catalytic processes (generalization of practical experience, improvements, and modernization); technology of catalysts production, raw materials and equipment; control of catalysts quality; starting, reduction, passivation, discharge, storage of catalysts; catalytic reactors.Theoretical foundations of industrial catalysis and technologies: Research, studies, and concepts : search for and development of new catalysts and new types of supports, formation of active components, and mechanochemistry in catalysis; comprehensive studies of work-out catalysts and analysis of deactivation mechanisms; studies of the catalytic process at different scale levels (laboratory, pilot plant, industrial); kinetics of industrial and newly developed catalytic processes and development of kinetic models; nonlinear dynamics and nonlinear phenomena in catalysis: multiplicity of stationary states, stepwise changes in regimes, etc. Advances in catalysis: Catalysis and gas chemistry; catalysis and new energy technologies; biocatalysis; nanocatalysis; catalysis and new construction materials.History of the development of industrial catalysis.
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