CO2 Microwave Plasma-Catalytic Reactor for Efficient Reforming of Methane to Syngas

被引:33
|
作者
Chun, Se Min [1 ]
Shin, Dong Hun [1 ]
Ma, Suk Hwal [1 ,2 ]
Yang, Geon Woo [1 ,3 ]
Hong, Yong Cheol [1 ]
机构
[1] Natl Fus Res Inst, Plasma Technol Res Ctr, 37 Dongjansan Ro, Gunsan 54004, Jeollabuk Do, South Korea
[2] Chonbuk Natl Univ, Dept Appl Plasma Engn Elect Engn, 567 Baekje Daero, Jeonju 54896, Jeollabuk Do, South Korea
[3] Chonbuk Natl Univ, Dept Bio Nano Syst Engn, Div Mech Design Engn, 567 Baekje Daero, Jeonju 54896, Jeollabuk Do, South Korea
关键词
carbon dioxide; reforming; microwave plasma; catalyst; synthesis gas; HYDROGEN-PRODUCTION; TORCH; TEMPERATURES; CAPTURE;
D O I
10.3390/catal9030292
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
CO2 was converted to synthesis gas in a microwave plasma-catalytic reactor by methane reforming at atmospheric pressure. The hybrid system used waste heat from the plasma to heat the catalyst. Conversion degrees were examined as a function of gas temperature, and the reforming efficiency of the plasma-only system was compared with that of the hybrid system. As a result, the hybrid system was shown to be more efficient under catalyst-free conditions. The use of microwave plasma alone resulted in low conversions of CO2 and CH4, which were 32.9% and 42.7%, respectively, at 3 kW microwave power. High CO2 and CH4 conversions of 87.9% and 92.9%, respectively, were achieved in the presence of catalyst at the same microwave power. At constant microwave power, catalyst addition increased the H-2 and CO mass yield rates to 0.27 kg/h and 2.012 kg/h, respectively. Additionally, the H-2 energy yield were 270 g/h, and 91.2 g/kWh. Thus, the developed hybrid system is well suited for efficient and economically viable CO2 reduction and synthesis gas production, paving the way for next-generation CO2 utilization and zero-emission industrial processes.
引用
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页数:18
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