Synthesis of Glycerol Carbonate from Glycerol and Dimethyl Carbonate Using Strongly Basic Anion-Exchange Styrene–Divinylbenzene Dowex Resins

IF 0.7 Q4 ENGINEERING, CHEMICAL
A. V. Shvydko, S. A. Prihod’ko, M. N. Timofeeva
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引用次数: 1

Abstract

The synthesis of glycerol carbonate from glycerol and dimethyl carbonate when using strongly basic styrene–divinylbenzene anion-exchange resins Dowex 1 × 2, Dowex 1 × 4, and Dowex 1 × 8 in the OH-form is studied. The resins are characterized by different degrees of crosslinking of their polystyrene matrices (the contents of divinylbenzene are 2, 4, and 8 wt. %, respectively). Synthesis is performed at 90–105°C, and the molar ratio of dimethyl carbonate to glycerol is 2 : 1. The yield of glycerol carbonate is shown to depend on the degree of crosslinking of the anion-exchange resin, since it falls as the degree of crosslinking rises. The highest degree of the conversion of glycerol (95%) and its selectivity toward glycerol carbonate (45.5%) are observed when using Dowex 1 × 2 and the reaction proceeds at 105°C for a period of 5 h. Advantages of considered systems over other anion- and cation-exchange resins proposed in the literature are noted.

Abstract Image

用强碱性阴离子交换苯乙烯-二乙烯基苯树脂由甘油和碳酸二甲酯合成碳酸甘油
研究了以强碱性苯乙烯-二乙烯基苯阴离子交换树脂Dowex 1 × 2、Dowex 1 × 4和Dowex 1 × 8为羟基,以甘油和碳酸二甲酯为原料合成碳酸甘油的工艺。树脂的特点是其聚苯乙烯基体的交联程度不同(二乙烯苯的含量分别为2%、4%和8%)。合成在90-105℃下进行,碳酸二甲酯与甘油的摩尔比为2:1。碳酸甘油的产率取决于阴离子交换树脂的交联度,因为它随着交联度的增加而下降。当使用Dowex 1 × 2时,观察到甘油的最高转化率(95%)和对碳酸甘油的选择性(45.5%),反应在105°C下进行,持续5小时。注意到所考虑的体系比文献中提出的其他阴离子和阳离子交换树脂的优点。
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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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