Green approach for sustainable production of paraffin fuel from CO2 hydrogenation on Fe-MOF catalyst

被引:8
|
作者
Ahmed, Hany E. [1 ,2 ,3 ]
Rashed, Ahmed E. [3 ,4 ]
El-Khouly, Mohamed E. [1 ]
Albolkany, Mohamed K. [5 ]
Abd El-Moneim, Ahmed [1 ,3 ,6 ]
机构
[1] Egypt Japan Univ Sci & Technol, Basic & Appl Sci Inst, New Borg El Arab 21934, Egypt
[2] Natl Inst Stand, Tersa St,El Haram,POB 136, Giza 12211, Egypt
[3] Egypt Japan Univ Sci & Technol, Graphene Ctr Excellence Energy & Elect Applicat, New Borg El Arab 21934, Egypt
[4] Alexandria Univ, Fac Sci, Environm Sci Dept, Alexandria 21511, Egypt
[5] Alexandria Univ, Inst Grad Studies & Res, Dept Environm Studies, Alexandria, Egypt
[6] Natl Res Ctr, Phys Chem Dept, Cairo 12622, Egypt
来源
关键词
Carbon dioxide hydrogenation; Paraffin fuel; Natural gas; Kerosene; Iron-based catalyst; Metal-organic frameworks; METAL-ORGANIC FRAMEWORKS; FISCHER-TROPSCH SYNTHESIS; CONVERSION; NANOPARTICLES; TEMPERATURE; PERFORMANCE; METHANATION; MIL-100(FE); PHOTOCATALYST; DEGRADATION;
D O I
10.1016/j.jece.2023.111071
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
With increasing global fuel demand, circular carbon economy and related carbon-neutral fuels are a cleaner way to reduce CO2 emissions significantly. Our work involves utilizing green hydrogen formed by water electrolysis and CO(2)to produce paraffin hydrocarbon (up to C-16) using a well-distributed and small particle size (similar to 3 nm) iron-based metal-organic framework (Fe-MOF) catalyst. The MIL-100(Fe) MOF precursor was synthesized with a green, cost-efficient, large-scale, and facile room temperature method. The highest CO2 conversion (44.1 %) and low CO selectivity (7.5 %) was attained at 340 C and 30 bar. The paraffin hydrocarbon product (99 %, yielding 40.3 %) is composed mainly of natural gas (C-1-C-4) (90 %) and liquid fuel (10 %) in the gasoline range (C-5-C-12). However, adjusting conditions at 300 C and 10 bar directed the liquid fuel to the kerosene range C-5-C-16 (11 %). The catalyst's capacity to function as an industrial catalyst was proved after more than 120 h on a continuous stream without sintering or deactivation. Compared to reference catalyst and earlier work, the unpromoted FeMOF-derived catalyst shows excellent potential for CO2 mitigation and production of combined gas and liquid alkane fuel.
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页数:14
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