High-Efficiency Direct Esterification of CO2 and Methanol over Co-Doped CeO2 Catalysts

IF 3.9 3区 工程技术 Q2 ENGINEERING, CHEMICAL
Chen Xue, Libin Liu, Yuxi Si, Yangqiang Huang, Shengdong Yang, Kuanrong Xue, Jun Xi, Youwei Cheng
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Abstract

The direct esterification reaction of CO2 with methanol to produce dimethyl carbonate (DMC) provides a sustainable pathway for the resourceful utilization of CO2. However, the chemical stability of CO2 makes the reaction kinetically difficult with low methanol conversion and DMC yields. In this study, a series of catalysts (denoted as M-CeO2, M = Fe, Cu, Co, La, Zr, Ni, and Al) with oxygen vacancy defects were constructed by a doping strategy, which provided critical sites for the adsorption and activation of methanol and CO2. Additionally, 2-cyanopyridine (2-CP) was employed as a dehydrating agent to facilitate the esterification reaction through dehydration. Under the optimized experimental conditions, the conversion of methanol was 61.9% and the DMC yield was 61.6%. The experimental and characterization results show that the extensive oxygen vacancies and base sites on the surface of the 5% Co-CeO2 catalyst are crucial for activating methanol and CO2, which is the main reason for the high catalytic activity of the catalyst. In situ diffuse reflectance infrared Fourier transform spectroscopy (DRIFTS) effectively demonstrated the efficient activation of methanol and CO2 on the catalyst and further confirmed the formation of monomethyl carbonate species during the reaction process. The high catalytic performance was also demonstrated in the direct esterification of other monohydric alcohols, thus confirming the broad applicability of the catalyst. This study presents a viable approach for the efficient utilization of CO2 resources, offering a promising solution for the sustainable management of greenhouse gas.

Abstract Image

共掺杂CeO2催化剂上CO2和甲醇的高效直接酯化反应
二氧化碳与甲醇直接酯化反应生成碳酸二甲酯(DMC)为二氧化碳的资源化利用提供了一条可持续发展的途径。然而,由于 CO2 的化学稳定性,该反应在动力学上很难进行,甲醇转化率和 DMC 收率都很低。本研究通过掺杂策略构建了一系列具有氧空位缺陷的催化剂(标记为 M-CeO2,M = Fe、Cu、Co、La、Zr、Ni 和 Al),为甲醇和 CO2 的吸附和活化提供了关键位点。此外,还采用了 2-氰基吡啶(2-CP)作为脱水剂,通过脱水促进酯化反应。在优化的实验条件下,甲醇的转化率为 61.9%,DMC 收率为 61.6%。实验和表征结果表明,5% Co-CeO2 催化剂表面广泛的氧空位和碱基位点是活化甲醇和 CO2 的关键,这也是催化剂具有高催化活性的主要原因。原位漫反射红外傅立叶变换光谱(DRIFTS)有效地证明了催化剂对甲醇和 CO2 的高效活化,并进一步证实了反应过程中碳酸一甲酯物种的形成。在其他一元醇的直接酯化反应中也证明了该催化剂的高催化性能,从而证实了该催化剂的广泛适用性。这项研究提出了一种高效利用二氧化碳资源的可行方法,为温室气体的可持续管理提供了一种前景广阔的解决方案。
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来源期刊
Industrial & Engineering Chemistry Research
Industrial & Engineering Chemistry Research 工程技术-工程:化工
CiteScore
7.40
自引率
7.10%
发文量
1467
审稿时长
2.8 months
期刊介绍: ndustrial & Engineering Chemistry, with variations in title and format, has been published since 1909 by the American Chemical Society. Industrial & Engineering Chemistry Research is a weekly publication that reports industrial and academic research in the broad fields of applied chemistry and chemical engineering with special focus on fundamentals, processes, and products.
文献相关原料
公司名称
产品信息
麦克林
Methanol
麦克林
Ethanol
麦克林
n-propanol
麦克林
n-butanol
麦克林
n-pentanol
麦克林
Cyclohexanol
麦克林
Dimethyl carbonate
麦克林
Methyl carbamate
麦克林
Sodium hydroxide
麦克林
Ce(NO3)3·6H2O
麦克林
Co(NO3)2·6H2O
麦克林
Fe(NO3)3·9H2O
麦克林
Cu(NO3)2·3H2O
麦克林
Zr(NO3)4·5H2O
麦克林
La(NO3)3·6H2O
麦克林
Al(NO3)3·9H2O
阿拉丁
Diethyl carbonate
阿拉丁
Dipropyl carbonate
阿拉丁
Dicyclohexyl carbonate
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