Light olefins synthesis from CO2 hydrogenation over mixed Fe-Co-K supported on micro-mesoporous carbon catalysts

被引:14
|
作者
Witoon, Thongthai [1 ,2 ]
Numpilai, Thanapha [1 ,2 ,3 ]
Nueangnoraj, Khanin [4 ]
Cheng, Chin Kui [5 ]
Chareonpanich, Metta [1 ,2 ]
Limtrakul, Jumras [6 ]
机构
[1] Kasetsart Univ, Fac Engn, Ctr Excellence Petrochem & Mat Technol, Dept Chem Engn, Bangkok 10900, Thailand
[2] Kasetsart Univ, KU Inst Adv Studies, Ctr Adv Studies Nanotechnol Chem Food & Agr Ind, Bangkok 10900, Thailand
[3] Thammasat Univ, Fac Sci & Technol, Dept Environm Sci, Pathum Thani 12120, Thailand
[4] Thammasat Univ, Sirindhorn Int Inst Technol SIIT, Sch Biochem Engn & Technol, Bangkok, Thailand
[5] Khalifa Univ, Coll Engn, Ctr Catalysis & Separat CeCaS, Dept Chem Engn, POB 127788, Abu Dhabi, U Arab Emirates
[6] Vidyasirimedhi Inst Sci & Technol, Sch Mol Sci & Engn, Dept Mat Sci & Engn, Rayong 21210, Thailand
关键词
CO2; hydrogenation; Light olefins; Fe-based catalysts; Micro-mesoporous carbon; Microporous carbon; FISCHER-TROPSCH SYNTHESIS; IRON-BASED CATALYSTS; DEHYDROGENATION; SELECTIVITY; POTASSIUM; PROMOTER;
D O I
10.1016/j.ijhydene.2021.10.265
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
Recycling CO2 into light olefins is a promising approach to reduce CO2 emissions. To pro-mote this technology, an efficient catalyst with high activity and selectivity towards light olefins is imperative. In this work, a series of Fe-Co-K supported on micro-mesoporous carbon (MMC) and microporous carbon (MC) with different metal loading contents (20-80 wt%) were prepared for CO2 hydrogenation to light olefins. Impregnating mixed metal oxides on both MMC and MC reduced particle sizes and enhanced their dispersion and reducibility, yielding a higher CO2 conversion compared to the unsupported Fe-Co-K catalyst. The metal oxides were highly dispersed inside the micropores of MC support, achieving the highest CO2 conversion. However, the high dispersion of metal oxides inside micropores led to the formation of isolated particles with a low interfacial contact with each other, resulting in a low light olefins selectivity. The MMC support provided a lower degree of metal dispersion, creating more interfacial contact area, promoting the selec-tivity towards olefins. Overall, the 60 wt% Fe-Co-K supported on MMC catalyst exhibited the highest light olefins yield of 10.8% at 400 degrees C and 20 bar and excellent stability. (c) 2021 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:42185 / 42199
页数:15
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