Combined Deoxygenation and Isomerization of Sunflower Oil Fatty Acid Triglycerides on Pt/Al2O3-Zeolite Catalysts

IF 0.7 Q4 ENGINEERING, CHEMICAL
A. A. Nepomnyashchii, E. R. Saibulina, E. A. Buluchevskiy, T. I. Gulyaeva, V. L. Yurpalov, R. M. Mironenko, O. V. Potapenko, A. V. Lavrenov
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Abstract

The authors study the effect of the type of zeolite (SAPO-11, ZSM-22, ZSM-23, and ZSM-12) in a support (ratio zeolite : Al2О3 = 30 : 70) on the physicochemical properties of Pt/Al2O3-zeolite catalysts and the composition of products from the hydrodeoxygenation of sunflower oil on them. The possibility of the complete hydrodeoxygenation of sunflower oil at temperatures of 320–350°C, a pressure of 4 MPa, and a weight hourly space velocity (WHSV) of 1 h−1 is shown with 75–82% yields of liquid products. The fraction of iso-alkanes and the yield of direct hydrodeoxygenation products grow along with the concentration of Brønsted acid sites in a catalyst in the order 1%Pt/Al2O3-ZSM-22 < 1%Pt/Al2O3-ZSM-12 < 1%Pt/Al2O3-ZSM-23 < 1%Pt/Al2O3-SAPO-11.

Abstract Image

铂/Al2O3-沸石催化剂上葵花籽油脂肪酸甘油三酯的联合脱氧和异构化反应
摘要 作者研究了载体中沸石类型(SAPO-11、ZSM-22、ZSM-23 和 ZSM-12)(沸石与 Al2О3 的比例为 30:70)对铂/Al2O3-沸石催化剂的理化性质及其上葵花籽油加氢脱氧产物组成的影响。结果表明,在温度为 320-350°C、压力为 4 兆帕、重量小时空间速度(WHSV)为 1 小时-1 的条件下,葵花籽油可以完全加氢脱氧,液体产物的产率为 75%-82%。异构烷烃的馏分和直接加氢脱氧产物的产率随着催化剂中布氏酸位点浓度的增加而增加,其顺序为 1%Pt/Al2O3-ZSM-22;1%Pt/Al2O3-ZSM-12;1%Pt/Al2O3-ZSM-23;1%Pt/Al2O3-SAPO-11。
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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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