用于庚烷异构化的多孔氧化铝支撑钨酸氧化锆催化剂

IF 0.7 Q4 ENGINEERING, CHEMICAL
M. D. Smolikov, V. A. Shkurenok, S. S. Yablokova, K. V. Kazantsev, T. I. Gulyaeva, I. V. Muromtsev, A. V. Lavrenov
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引用次数: 0

摘要

摘要在不同相组成的多孔氧化铝载体上合成了以钯为活性金属的新型 WO3-ZrO2 (WZ) 催化剂。以萨索尔公司生产的挤压成型氧化铝(E)和球形氧化铝(S)为载体,其中氧化铝的相组成为θ-Al2O3、δ-Al2O3 和 α-Al2O3。研究表明,载体的相组成对基于载体的 Pd/WZ 催化剂的活性有显著影响。从一组 θ- 和 δ-Al2O3 相过渡到 θ- 和 α-Al2O3 相组成后,催化剂的活性提高了,这表现在庚烷转化的温度依赖性向低温转变了 10-30°C 。随着 α-Al2O3 相的出现,催化剂的比表面积也随之减小,这导致了酸性位点密度的增加,从而改变了催化剂的活性。与支撑在 E 型铝上的样品(2.8-3.6 µmol/m2)相比,支撑在 S 型铝上的钯/WZ 催化剂具有更高的酸度(3.7-6.3 μmol/m2)。Pd/WZ/S 催化剂的高酸度加强了庚烷裂解副反应,形成气态 C1-C4 碳氢化合物。反过来,Pd/WZ/E 催化剂的中等酸度也有助于提高庚烷异构体的选择性(在庚烷转化率为 81.5-83.2% 时为 89.2-89.3%),而以 S 为载体的催化剂(在庚烷转化率为 80.4-81.4% 时为 84.9-85.6% 的异构化选择性)则无法达到这一水平。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Porous Alumina-Supported Tungstated Zirconia Catalysts for Heptane Isomerization

Porous Alumina-Supported Tungstated Zirconia Catalysts for Heptane Isomerization

Porous Alumina-Supported Tungstated Zirconia Catalysts for Heptane Isomerization

Novel WO3–ZrO2 (WZ) catalysts with palladium as an active metal on porous alumina supports of various phase compositions have been synthesized. Aluminas from Sasol molded in the form of extrudates (E) and spherical aluminas (S), in which the phase composition is presented by θ-Al2O3, δ-Al2O3, and α-Al2O3 alumina, have been used as supports. It has been shown that the phase composition of the support has a significant effect on the activity of supported Pd/WZ catalysts based on it. Upon transition from a set of θ- and δ-Al2O3 phases to the θ- and α-Al2O3 phase composition has led to an increase in the activity of the catalysts, as evidenced by a shift of 10–30°C in the temperature dependences of the heptane conversion to lower temperatures. The appearance of the α-Al2O3 phase is accompanied by a decrease in the specific surface area of the catalysts, which leads to an increase in the density of acid sites and, as a consequence, a change in activity. The Pd/WZ catalysts supported on S aluminas are characterized by a higher acidity (3.7–6.3 μmol/m2) as compared to the samples supported on E aluminas (2.8–3.6 µmol/m2). The high acidity of the Pd/WZ/S catalysts intensifies the heptane cracking side reactions to form gaseous C1–C4 hydrocarbons. In turn, the moderate acidity of the Pd/WZ/E catalysts contributes to a higher selectivity to heptane isomers (89.2–89.3% at a heptane conversion of 81.5–83.2%) as compared to the catalysts supported on S supports (isomerization selectivity of 84.9–85.6% at a heptane conversion of 80.4–81.4%).

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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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