催化作用
化学
反应中间体
基质(水族馆)
氧化还原
组合化学
反应机理
催化氧化
催化循环
氧气
化学工程
多相催化
焊剂(冶金)
光化学
过程(计算)
协同催化
反应速率
纳米技术
化学反应
析氧
作者
Xiaolin Yuan,胡凌霜,Zhicheng Jiang,Yingdong Zhou
标识
DOI:10.1021/acscatal.6c03816
摘要
Abstract The selective oxidation of 5-hydroxymethylfurfural (HMF) to 2,5-furandicarboxylic acid (FDCA) is a key catalytic transformation for the production of renewable polymers. Although near-quantitative FDCA yields can be achieved under dilute conditions, increasing substrate concentration fundamentally alters the reaction regime, where catalytic oxidation pathways become strongly coupled with oxygen transfer, intermediate accumulation, and catalyst stability. Under concentrated conditions, intensified side reactions, humin formation, and catalyst deactivation collectively disrupt selective oxidation and severely limit process scalability. In this review, we define a concentration greater than 1 wt % as high concentration and present a mechanism-oriented perspective on high-concentration HMF oxidation, focusing on how substrate concentration reshapes catalytic reaction networks and governs the competition between desired oxidation pathways and parasitic reactions. Rather than classifying catalysts by composition, we establish a unified conceptual framework linking catalytic oxygen activation, reaction kinetics, mass transport, and microenvironment effects. Recent advances in noble metal, non-noble metal, and carbon-based catalytic systems are critically re-evaluated through this framework, together with emerging solvent-regulation and dynamic protection–deprotection strategies. Particular emphasis is placed on how catalytic systems regulate reaction flux under concentrated conditions through oxygen activation, intermediate stabilization, and pathway selection. Finally, key challenges and future opportunities are discussed, highlighting reaction network regulation as a central strategy for scalable biomass oxidation.
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