膨润土催化体系中氧化铁含量对模型含硫原料裂化产物中硫分布的影响

IF 0.7 Q4 ENGINEERING, CHEMICAL
T. V. Bobkova, K. I. Dmitriev, O. V. Potapenko, V. P. Doronin, T. P. Sorokina
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引用次数: 0

摘要

研究了在催化裂化体系中加入不同氧化铁含量的粘土对合成产物中原料硫分布的影响,以及对含硫1万ppm的2-甲基噻吩和苯并噻吩模型含硫原料裂化后,焦化催化剂再生过程中硫氧化物生成量的影响。当使用较高分子量的含硫组分时,可以看到转化为液体产品和焦炭的原料硫的比例增加。将催化剂中氧化铁的含量从0.61 wt %提高到1.53 wt %,可以提高模型原料裂解过程中液体产物的收率,降低模型烃的转化率。催化剂上焦炭的产率由3.8%提高到5.2%,原料硫转化为二氧化硫的比例提高了四倍。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Effect of the Iron Oxide Content in Bentonite Clay Incorporated into a Catalytic System on the Sulfur Distribution in the Products of Cracking from Model Sulfur-Containing Feedstock

Effect of the Iron Oxide Content in Bentonite Clay Incorporated into a Catalytic System on the Sulfur Distribution in the Products of Cracking from Model Sulfur-Containing Feedstock

The effect of adding clay with different contents of iron oxides to a catalytic cracking system on the distribution of feedstock sulfur in synthesized products and the amount of sulfur oxides formed during the regeneration of coked catalyst after the cracking of a model sulfur-containing feedstock with a sulfur content of 10 000 ppm, derived from 2-methylthiophene or benzothiophene has been studied. The fraction of the feedstock sulfur converted into liquid products and coke can be seen to grow when a sulfur-containing component with a higher molecular weight is used. Raising the content of iron oxide in the catalyst from 0.61 to 1.53 wt % increases the yield of liquid products during the cracking of a model feedstock, reduces the conversion of a model hydrocarbon. The yield of coke on the catalyst grows from 3.8 to 5.2 wt %, and the fraction of feedstock sulfur converted into SO2 quadruples.

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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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