催化作用
选择性
水煤气变换反应
产量(工程)
化学工程
串联
材料科学
化学
碳氢化合物
工作(物理)
合成气
甲烷化
一氧化碳
碳纤维
联轴节(管道)
多相催化
二氧化碳
光化学
无机化学
科技与社会
分子动力学
反应条件
作者
Hao Huang,Chengwei Wang,Yingluo He,Xinze Bi,Yang Wang,Prasert Reubroycharoen,Yao Deng,Ao Zhang,Peng Qin,Guohui Yang,Mingbo Wu,Noritatsu Tsubaki
出处
期刊:ACS Catalysis
[American Chemical Society]
日期:2026-09-21
卷期号:16 (19): 19301-19312
标识
DOI:10.1021/acscatal.6c04738
摘要
Abstract Achieving a high yield of liquid fuels from CO2 hydrogenation remains a significant challenge due to the limited CO2 conversion and the dominant formation of undesired C1 byproducts. Herein, we report a carbon-confined Fe-Co interfacial catalyst that establishes a kinetically coupled reverse water gas shift (RWGS) and Fischer–Tropsch synthesis (FTS) pathway, enabling efficient conversion of CO2 to long-chain hydrocarbons. The introduction of highly dispersed Co species promotes continuous CO generation via RWGS at the Fe3O4 and Co3Fe7 sites, while the carbon encapsulation layer modulates the binding energetics of CO and stabilizes surface intermediates on the reconstructed Fe5C2 phases. This dual regulation ensures a dynamic balance between CO supply and hydrogenation kinetics, leading to increased surface coverage of CHx intermediates and enhanced C–C coupling probability. As a result, the optimized K-Fe/Co@C catalyst, composed of Fe3O4, Co3Fe7, and Fe5C2, achieves a CO2 conversion of 55.1% with a C5+ selectivity of 60.1% and a low CO selectivity of 3.8%, delivering an ultra-high single-pass yield of 31.9% for liquid fuels. This work demonstrates an effective approach to tandem catalyst design through the synergistic integration of CO formation and chain propagation kinetics.
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