CO2 hydrogenation to methanol over Al2O3-supported Co, Mn OR Zn modified CuGa-LDH catalysts

被引:0
|
作者
Luo, Mingsheng [1 ,2 ]
Li, Ziyuan [1 ,2 ]
Yang, Zhi [1 ,3 ]
Fang, Yuanyuan [1 ,2 ]
Rahman, Roshni [1 ,4 ]
机构
[1] Beijing Inst Petrochem Technol, Coll New Mat & Chem Engn, Beijing 102617, Peoples R China
[2] Beijing Key Lab Clean Fuels & Efficient Catalyt Em, Beijing 102617, Peoples R China
[3] Beijing Univ Technol, Sch Mat Sci & Engn, Beijing 100124, Peoples R China
[4] Beijing Univ Chem Technol, Sch Chem Engn, Beijing 100029, Peoples R China
关键词
CO; 2; hydrogenation; CuGa-LDH/Al; O; 3; catalyst; MOF/LDH composite catalyst; 2-to-methanol; utilization; CONVERSION; OXIDATION; PHASE; ZR; MO;
D O I
10.1016/j.fuel.2025.134895
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
CO2 hydrogenation to methanol is gaining wide attraction as a sustainable approach for carbon utilization. In this study, a cost-effective and highly efficient ZnCuGa-LDH/Al2O3 catalyst was innovatively synthesized to achieve a remarkable 19.54 % CO2 conversion under optimized conditions at 230 degrees C, 3.0 MPa and a space velocity of 3600 mL center dot gcat - 1 center dot h- 1. The catalyst also exhibits outstanding stability, maintaining consistent performance over 70 h of continuous operation with no marked deactivation. Detailed investigation of reaction parametric studies suggested 230 degrees C as the optimal temperature for maximizing catalytic activity. In-situ DRIFTS results prove the formate synthesis mechanism in CO2 hydrogenation pathway over the synthesized ZnCuGa-LDH/Al2O3 catalyst. This study highlights the potential future application of the ZnCuGa-LDH/Al2O3 catalyst for efficient and durable methanol production.
引用
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页数:13
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