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Catalytic Esterification of Carbon Dioxide and Methanol for the Preparation of Dimethyl Carbonate

机译:二氧化碳和甲醇制备二甲基酯的催化酯化

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Dimethyl carbonate (DMC) is an important methylating agent and potential additive for clean fuel production. Several processes have been developed for the manufacture of DMC. The direct synthesis of DMC from CO_2 and methanol is especially attractive and important. In this work, the continuous synthesis of DMC from methanol and CO_2 in the region near the critical point of CO_2, with methyl iodide and potassium carbonate as the promoters, was investigated. The reactions were performed in a stainless steel autoclave with an inner volume of 500 mL equipped with a magnetic stirrer and an electric heater. The effects of the reaction temperature and pressure were determined first. It was shown that the yield of DMC increases with the increase of the reaction pressure. When the pressure approaches the critical pressure of CO_2, the optimal yield of DMC is obtained. Then the reaction characteristic was discussed from the unique characteristics of supercritical CO_2. Finally, a new process for the production of DMC has been proposed, for which water is used as an extractant for the separation of DMC from the reaction mixture.
机译:碳酸二甲酯(DMC)是一种重要的甲基化剂和用于清洁燃料生产的潜在添加剂。已经开发了用于制造DMC的几个过程。来自CO_2和甲醇的DMC的直接合成尤其具有吸引力和重要。在这项工作中,研究了在CO_2临界点附近的区域中从甲醇和CO_2的甲醇和CO_2的连续合成,用甲基碘和碳酸钾作为启动子。在不锈钢高压釜中进行反应,内部容积为500ml,配备有磁力搅拌器和电加热器。首先确定反应温度和压力的影响。结果表明,随着反应压力的增加,DMC的产率增加。当压力接近CO_2的临界压力时,获得DMC的最佳产量。然后从超临界CO_2的独特特征讨论了反应特性。最后,已经提出了一种用于生产DMC的新方法,其中水用作从反应混合物中分离DMC的萃取剂。

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