Nickel Catalysts Based on LaCeY Ternary Oxide Supports for Dry Methane Reforming

IF 0.9 Q4 ENGINEERING, CHEMICAL
N. V. Dorofeeva, P. K. Putanenko, V. A. Svetlichnyi, O. V. Vodyankina
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引用次数: 0

Abstract

The structure of 10%Ni/LaCeY(n)Ox catalysts containing different amounts of yttrium (0.5–10 mol %) and their catalytic activity in dry methane reforming (DMR) have been studied. The phase composition of the support and catalyst samples has been characterized using a set of physicochemical methods; the effect of yttrium introduction method on the formation of the active surface of the catalysts has been studied. Varying the yttrium content in the support, it has been found that 1 mol % is the optimum amount of the introduced additive to provide minimum changes in the initial conversions of the reactants (methane and CO2) and the H2/CO ratio at 650°C for 6 h as compared to the respective parameters of the unmodified catalyst. An increase in the modifier content to 10 mol % leads to an increase in the deactivation rate due to more vigorous carbon deposition and the formation of encapsulating carbon species (amorphous carbon and onion-like carbon). The Ni/LaCeY(1)Ox sample exhibiting the highest stability under DMR conditions is characterized by the dominant content of multiwalled carbon nanotubes with uncapped end Ni nanoparticles.

Abstract Image

基于LaCeY三元氧化物载体的镍催化剂用于甲烷干重整
研究了不同钇含量(0.5 ~ 10 mol %)的10%Ni/LaCeY(n)Ox催化剂的结构及其在甲烷干重整(DMR)中的催化活性。采用一套物理化学方法对载体和催化剂样品的相组成进行了表征;研究了引入钇对催化剂活性表面形成的影响。通过改变载体中钇的含量,发现与未改性催化剂的相应参数相比,1mol %的添加量可以使反应物(甲烷和二氧化碳)的初始转化率和H2/CO比在650℃下持续6小时的变化最小。当改性剂的含量增加到10 mol %时,由于更剧烈的碳沉积和包封碳(无定形碳和洋葱状碳)的形成,导致失活率增加。Ni/LaCeY(1)Ox样品在DMR条件下表现出最高的稳定性,其主要特征是多壁碳纳米管的含量占主导地位,其末端是无盖的Ni纳米颗粒。
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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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