Production of light olefins by catalytic hydrogenation of CO2 over Y2O3/Fe-Co modified with SAPO-34

被引:10
|
作者
Oni, Babalola Aisosa [1 ]
Sanni, Samuel Eshorame [2 ]
Ibegbu, Anayo Jerome [3 ]
机构
[1] China Univ Petr, Chem Engn Dept, Beijing City, Peoples R China
[2] Covenant Univ, Chem Engn Dept, Ota, Ogun State, Nigeria
[3] Madonna Univ, Dept Mech Engn, Elele, Nigeria
关键词
Y2O3/Fe-Co-SAPO-34; CO2-hydrogenation; CO2-conversion; Light olefins; Catalyst selectivity; HIGHLY SELECTIVE CONVERSION; THERMAL-CRACKING; CARBON-DIOXIDE; SYNTHESIS GAS; METHANOL; NANOPARTICLES; DEACTIVATION; OPTIMIZATION; HYDROCARBONS;
D O I
10.1016/j.apcata.2022.118784
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Direct conversion of CO2 to hydrocarbons by hydrogenation was used in the production of light olefins. Hydrothermal coating and physical blending procedures were used to synthesize Y2O3/Fe-Co-SAPO-34 in this study. Based on the results from characterization, a unique micro-mesoporous structural composite with co-existing basic and acidic sites was obtained without any excessive close-fitting between the active sites in the physically blended composite. The catalyst's overall selectivity for the light olefins was 82.6% with CO2 conversion of 19.9% for H-2/CO2 of 3.0, with space velocity of 10 L.g.(cat)-1 h(-1) at 400 ? and 20 bars. Furthermore, an increase in the number of acidic-basic sites, meso-microporous structures, alongside the synergetic effects of the compositephases over the catalyst without any support, improved the catalyst's activity for CO2 conversion which in turn yielded higher C-2=-C-4= selectivity. The hybrid catalyst had a commendable stability within 80-hours of operation without losing its activity
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页数:13
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