Estimating the Efficiency of Commercial Domestic Catalysts in the Reaction of Ammonia Decomposition

IF 0.7 Q4 ENGINEERING, CHEMICAL
R. E. Yakovenko, T. V. Krasnyakova, A. V. Dul’nev, A. N. Saliev, M. A. Shilov, A. V. Volik, A. P. Savost’yanov, S. A. Mitchenko
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Abstract

Adapting domestic commercial catalysts for use in such important technological processes as the environmentally friendly production of hydrogen accompanied by СОх and NОх emissions is in demand under import substitution conditions. Ammonia seems to be the most promising Н2 accumulator, due to its high hydrogen density and simple storage and transportation. This work considers the possibility of using the domestic NIAP-03-01, NIAP-07-01, NIAP-06-06 catalysts and Со-Al2O3/SiO2 developed by the authors in the ammonia dissociation reaction. The conversion and hydrogen production capacity grow in the order NIAP-06-06<NIAP-03-01<NIAP-07-01<Со-Al2O3/SiO2. The conversion of ammonia on Со-Al2O3/SiO2 is close to 100% at 550°C and a gas hourly space velocity (GHSV) of 3000 h−1. The effective activation energies of all the catalysts are comparable to the available literature data for the ammonia decomposition reaction to potentially enable their application at moderate temperatures.

Abstract Image

Abstract Image

估算商用家用催化剂在氨分解反应中的效率
摘要在进口替代的条件下,需要将国内商用催化剂应用于重要的技术工艺中,如以环保方式生产氢气,同时减少СОх和НОх的排放。由于氨的氢密度高、储存和运输简单,它似乎是最有前途的Н2蓄电池。本研究考虑了在氨解离反应中使用作者开发的国产 NIAP-03-01、NIAP-07-01、NIAP-06-06 催化剂和 Со-Al2O3/SiO2 的可能性。转化率和制氢能力按照 NIAP-06-06<NIAP-03-01<NIAP-07-01<Со-Al2O3/SiO2 的顺序增长。在 550°C 和气体时空速度 (GHSV) 为 3000 h-1 时,Со-Al2O3/SiO2 上的氨转化率接近 100%。所有催化剂的有效活化能都与氨分解反应的现有文献数据相当,因此可以在中等温度下应用。
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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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