Changes in the Physicochemical and Catalytic Properties of Iron–Potassium Catalysts under Operation in a Reactor of Ethylbenzene Dehydrogenation to Styrene at Nizhnekamskneftekhim

IF 0.7 Q4 ENGINEERING, CHEMICAL
I. R. Nabiullin, A. V. Boretskaya, M. V. Berezkina, R. R. Gil’mullin, S. R. Egorova
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Abstract

A study of original iron–potassium catalysts of ethylbenzene (EB) dehydrogenation to styrene and industrially used catalysts: Cat-1 (imported), Cat-2 and Cat-3 (domestic) is performed. Initial samples are multiphase systems consisting of potassium ferrites, hematite, and cerianite (CeO2). The phase composition of the catalysts after two years of operation consists mainly of magnetite and cerianite, while the amount of potassium (K+) in Cat-1, Cat-2, and Cat-3 samples falls by 40, 20, and 26%, respectively. At the same time, K+ for the Cat-2 sample is distributed uniformly in granules of the waste catalyst. XRD data indicate the CSR size of its CeO2 crystals does not change appreciably. The CSR size of CeO2 crystals in the Cat-3 sample falls from 302 to 110 Å, while it grows from 284 to 419 Å in the Cat-1 sample. After two years of operation, the greatest conversion of EB (72.1%) was observed for the Cat-2 sample, and it fell from 72.3 to 57.4% on the Cat-3 sample. There is a 600–1100% drop in the waste samples’ resistance to crushing, making them unsuitable for further use.

Abstract Image

铁钾催化剂在乙苯脱氢制苯乙烯反应器运行过程中理化性质和催化性能的变化
对乙苯(EB)脱氢制苯乙烯的原铁钾催化剂和工业用催化剂Cat-1(进口)、Cat-2和Cat-3(国产)进行了研究。初始样品是由钾铁氧体、赤铁矿和铈矿(CeO2)组成的多相体系。运行2年后,催化剂的物相组成主要为磁铁矿和铈矿,而Cat-1、Cat-2和Cat-3样品中的钾(K+)含量分别下降了40%、20%和26%。同时,Cat-2样品中的K+均匀分布在废催化剂的颗粒中。XRD数据表明,其CeO2晶体的CSR尺寸没有明显变化。Cat-3样品中CeO2晶体的CSR尺寸从302减小到110 Å,而Cat-1样品中CeO2晶体的CSR尺寸从284增大到419 Å。经过两年的操作,Cat-2样品的EB转化率最高(72.1%),Cat-3样品的EB转化率从72.3%下降到57.4%。废弃样品的抗破碎性下降了600-1100%,不适合进一步使用。
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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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