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首页> 外文期刊>Chemical engineering journal >Enhanced yields of diethyl carbonate via one-pot synthesis from ethanol, carbon dioxide and butylene oxide over cerium (IV) oxide
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Enhanced yields of diethyl carbonate via one-pot synthesis from ethanol, carbon dioxide and butylene oxide over cerium (IV) oxide

机译:通过一锅法由乙醇,二氧化碳和环氧丁烷在氧化铈(IV)上合成,可提高碳酸二乙酯的收率

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There is a considerable industrial interest towards short-chain dialkylcarbonate production technologies due to their attractive properties and apparent commercial applications. Over the years, dimethyl carbonate (DMC), in contrast to diethyl carbonate (DEC), was mainly explored in seeking novel synthesis ideas in academic investigations. Therefore, this work has been devoted to the synthesis of diethyl carbonate. The preliminary results showed that the formation of DEC via direct route starting from ethanol and carbon dioxide (CO2) is limited by the reaction equilibrium and therefore thermodynamics of the reaction has been estimated. Consecutively, butylene oxide was introduced to the reaction system as a dehydrating agent in order to overcome thermodynamic constrains and shift the equilibrium towards diethyl carbonate production. The underlying reason for choosing a longer chain epoxide (i.e. butyl instead of e.g. propyl) was the acute toxicity of short-chain epoxides. A 9-fold enhancement in DEC yield compared to the method without any water removal was achieved over cerium (IV) oxide (CeO2) in the presence of butylene oxide at 180 °C and 9 MPa of total final pressure unequivocally indicating that butylene oxide is an efficient chemical water trap. The highest obtained yield of diethyl carbonate was 2.5 mmol, corresponding to ethanol conversion of 15.6% and selectivity to DEC 10% on ethanol basis. Moreover, kinetic studies were conducted facilitating understanding of the reaction pathway and influence of various parameters on the reaction.
机译:短链碳酸二烷基酯的生产技术因其吸引人的性能和明显的商业应用而引起了相当大的工业兴趣。多年来,与碳酸二乙酯(DEC)相比,碳酸二甲酯(DMC)主要用于在学术研究中寻求新颖的合成思路。因此,这项工作致力于合成碳酸二乙酯。初步结果表明,由乙醇和二氧化碳(CO2)起始的直接途径形成的DEC受反应平衡的限制,因此已估算了反应的热力学。连续地,将环氧丁烷作为脱水剂引入反应体系中,以克服热力学限制并使平衡向碳酸二乙酯的生产转移。选择更长链的环氧化物(即用丁基而不是丙基)的根本原因是短链环氧化物的急性毒性。与氧化铈(IV)相比,在氧化丁烯存在下,在180°C和9 MPa的总最终压力下,与不去除水分的方法相比,DEC收率提高了9倍,明确表明氧化丁烯是一个高效的化学集水器。获得的碳酸二乙酯的最高产率为2.5mmol,对应于乙醇转化率为15.6%和基于乙醇的至DEC 10%的选择性。此外,进行了动力学研究,以促进对反应途径的理解以及各种参数对反应的影响。

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