Fe-Cu Bimetallic Catalysts for Selective CO2 Hydrogenation to Olefin-Rich C2+ Hydrocarbons

被引:110
作者
Wang, Wenjia [1 ,2 ,4 ]
Jiang, Xiao [1 ,2 ,4 ]
Wang, Xiaoxing [1 ,2 ]
Song, Chunshan [1 ,2 ,3 ,4 ]
机构
[1] Penn State Univ, EMS Energy Inst, Clean Fuels & Catalysis Program, 209 Acad Projects Bldg, University Pk, PA 16802 USA
[2] Penn State Univ, John & Willie Leone Family Dept Energy & Mineral, 209 Acad Projects Bldg, University Pk, PA 16802 USA
[3] Penn State Univ, Dept Chem Engn, 209 Acad Projects Bldg, University Pk, PA 16802 USA
[4] Dalian Univ Technol, Sch Chem Engn, PSU DUT Joint Ctr Energy Res, Dalian 116024, Peoples R China
关键词
FISCHER-TROPSCH SYNTHESIS; VALUE-ADDED PRODUCTS; CARBON-DIOXIDE; STRUCTURAL-PROPERTIES; K CATALYSTS; METHANATION; IRON; TRANSITION; CONVERSION; NI;
D O I
10.1021/acs.iecr.8b00016
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper reports on Fe-Cu bimetallic catalysts supported on gamma-alumina for selective CO2 hydrogenation to olefin-rich C-2(+) hydrocarbons. A strong synergetic promoting effect on C-2(+) hydrocarbon synthesis was observed over Fe-Cu bimetallic catalysts when the Cu/(Cu + Fe) atomic ratio was 0.17. Compared to monometallic Fe catalyst, the Fe-Cu bimetallic catalyst significantly enhances C-2-C-7 hydrocarbon formation and suppresses the formation of undesired CH4. The addition of K into Fe-Cu bimetallic catalysts inhibits the methanation and further enhances the formation of C-2(+) hydrocarbons in the meantime. The synthesis of olefin-rich C-2-C-4 hydrocarbons from CO2/H-2 was achieved by using K-promoted Fe Cu/Al2O3 catalysts with higher K/Fe atomic ratios (e.g., K/Fe >= 0.5), where the selectivity of C-2-C-4 olefin contents was even higher than K-promoted Fe-Co catalysts under the same reaction conditions.
引用
收藏
页码:4535 / 4542
页数:8
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