利用微波辐照从甘油和丙酮合成 Solketal

IF 0.7 Q4 ENGINEERING, CHEMICAL Catalysis in Industry Pub Date : 2024-05-27 DOI:10.1134/s2070050424700053
V. A. Bolotov, A. E. Kibilyuk, V. N. Parmon, V. N. Panchenko, M. N. Timofeeva
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引用次数: 0

摘要

摘要 研究表明,在用 0.25 摩尔/升盐酸水溶液(0.25M HCl/MM)修饰过的蒙脱石(MM)存在下,可以用甘油和丙酮辐照合成索酮醛。在丙酮/甘油摩尔比为 2.45-7.53、催化剂浓度为 1.2-2.8 wt %(基于甘油重量)、温度为 30-56°C 的甲醇溶液中对该反应进行了研究。结果表明,溶酮醛是主要产物,选择性为 96.1-99.2%。在丙酮/甘油摩尔比为 7.53、催化剂负载量为 2.3 wt %(以甘油重量为基准)、温度为 56°C 的条件下,反应 15 分钟内可获得 91.3% 的最高溶酮醛产率和 98.6% 的选择性。比较了 0.25M HCl/MM 在微波和热加热条件下反应的催化特性。结果表明,在微波辐照下反应的溶酮产量是热加热工艺的 2 倍。
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Use of Microwave Irradiation to Synthesize Solketal from Glycerol and Acetone

Abstract

It has been shown that solketal can be synthesized from glycerol and acetone irradiation in the presence of montmorillonite (MM) modified with an aqueous solution of 0.25 mol/L of HCl (0.25M HCl/MM). The reaction has been studied in a methanol solution at an acetone/glycerol molar ratio of 2.45–7.53, a catalyst concentration of 1.2–2.8 wt % (based on glycerol weight), and 30–56°C. It has been shown that solketal is the major product with a selectivity of 96.1–99.2%. The maximum solketal yield of 91.3% with a 98.6% selectivity is obtained within 15 min of reaction at an acetone/glycerol molar ratio of 7.53, a catalyst loading of 2.3 wt % (based on glycerol weight), and 56°C. The catalytic properties of 0.25M HCl/MM in the reaction under microwave and thermal heating conditions have been compared. It has been shown that the solketal yield in the reaction under MW irradiation is 2 times higher than that in the process with thermal heating.

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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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