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在扩孔Cu-Cs催化剂上双引擎驱动合成不饱和酯

Dual-engine-driven synthesis of unsaturated esters over channel-expanding Cu-Cs catalysts.

作者信息

Fan Jiaqi, Shao Lishu, Gao Weizhe, Han Yitong, Xiang Wenjie, Huang Hao, Liu Zhihao, Liu Chufeng, Wang Bo, Wang Kangzhou, Liu Guangbo, Sui Jiancai, Liu Qiang, Li Tao, Xing Tao, Yasuda Shuhei, Yu Zhixin, Yang Guohui, Zhang Peipei, Tsubaki Noritatsu

机构信息

Institute of New Energy, School of Chemistry and Chemical Engineering, Shaoxing University Shaoxing 312000 China

Department of Applied Chemistry, School of Engineering, University of Toyama Gofuku 3190 Toyama 930-8555 Japan

出版信息

Chem Sci. 2025 Jun 11;16(28):12927-12940. doi: 10.1039/d5sc02896e. eCollection 2025 Jul 16.

Abstract

This study presents a one-step catalytic synthesis of unsaturated esters (methyl acrylate, MA; methyl methacrylate, MMA) from methanol (MeOH, C1 source) and methyl acetate (MAc) a Cu-Cs dual-engine-driven (DED) system that integrates four sequential steps-dehydrogenation, aldol condensation, hydrogenation, and secondary aldol condensation. The Cu-engine facilitates proton transfer by capturing protons during MeOH dehydrogenation and donating them in methyl acrylate (MA) hydrogenation, while the Cs-engine activates saturated esters for formaldehyde-mediated aldol condensation. Through systematic optimization of Cu loading methods, deposition sequences, and Cu/Cs ratios, we developed a silicon carrier channel-expanding strategy, enlarging mesopores from 14 nm to 20 nm (30% specific surface area extension) copper phyllosilicate-induced corrosion. Catalytic performance hinges on balanced medium-strength acid-base sites, a 10 : 7 Cs/Cu ratio, and sequential Cu/Cs loading the ammonia evaporation method. The optimized 10Cs/7Cu/Q10 catalyst, combined with a downstream Cs-Al/Q10 system, achieves 64.0% unsaturated ester selectivity (55.3% MeOH and 59.8% methyl acetate conversion). This work establishes a design framework for efficient Cu-Cs catalysts in one-step ester synthesis, emphasizing pore engineering, acid-base synergy, and dual-site cooperativity.

摘要

本研究提出了一种由甲醇(MeOH,C1源)和乙酸甲酯一步催化合成不饱和酯(丙烯酸甲酯,MA;甲基丙烯酸甲酯,MMA)的方法——一种铜-铯双引擎驱动(DED)系统,该系统整合了四个连续步骤:脱氢、羟醛缩合、氢化和二次羟醛缩合。铜引擎通过在甲醇脱氢过程中捕获质子并在丙烯酸甲酯(MA)氢化过程中提供质子来促进质子转移,而铯引擎则激活饱和酯以进行甲醛介导的羟醛缩合。通过系统优化铜负载方法、沉积顺序和铜/铯比例,我们开发了一种硅载体通道扩展策略,将中孔从14纳米扩大到20纳米(比表面积扩展30%),这是由铜层状硅酸盐引起的腐蚀。催化性能取决于平衡的中强度酸碱位点、10∶7的铯/铜比例以及采用氨蒸发法的连续铜/铯负载。优化后的10Cs/7Cu/Q10催化剂与下游的Cs-Al/Q10系统相结合,实现了64.0%的不饱和酯选择性(甲醇转化率为55.3%,乙酸甲酯转化率为59.8%)。这项工作建立了一步酯合成中高效铜-铯催化剂的设计框架,强调了孔工程、酸碱协同作用和双位点协同作用。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/4961/12264903/42d42dbc7b16/d5sc02896e-f1.jpg

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