Development of Pilot-Scale CO2 Methanation Using Pellet-Type Catalysts for CO2 Recycling in Sewage Treatment Plants and Its Validation through Computational Fluid Dynamics (CFD) Modeling

被引:5
|
作者
Ahn, Jeongyoon [1 ]
Kim, Heysuk [2 ]
Ro, Yeonhee [1 ]
Kim, Jintae [3 ]
Chung, Woojin [4 ]
Chang, Soonwoong [4 ]
机构
[1] Kyonggi Univ, Grad Sch, Dept Environm Energy Engn, 94 San, Iui Dong 16227, Suwon Si, South Korea
[2] Chungnam Natl Univ, Dept Environm Engn, 99 Daehak Ro, Daejeon 34134, South Korea
[3] Fivetek Co, 177 Kumgang High Tech Valley, Sagimakgol Ro 13217, Seongnam Si, South Korea
[4] Kyonggi Univ, Coll Creat Engn, Dept Environm Energy Engn, 94 San, Iui Dong 16227, Suwon Si, South Korea
关键词
methanation; CO2; Utilization; conversion; pilot plant; synthetic natural gas (SNG); computational fluid dynamics (CFD); GAS;
D O I
10.3390/catal11081005
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
In this study, a pilot-scale reactor was designed and compared using computational fluid dynamics (CFD) for a high-efficiency CO2 methanation reaction. The trends of the CO2 methanation catalyst efficiency at a pilot or industrial scale could be lower than those measured at the laboratory scale, owing to the flow of fluid characteristics. Therefore, the CO2 methanation reactor was designed based on the results of the CFD analysis to minimize the above phenomenon. Ni-Ce-Zr was used to manufacture a CO2 methanation catalyst in the form of pellets. The catalyst successfully produced about 43.3 Nm(3)/d of methane from the reactor. This result shows that CO2 methanation, which is known as an exothermic reaction, was stable at the pilot scale. It is believed that the self-supply of energy will be possible when this CO2 methanation technology is applied to industrial processes generating large amounts of CO2 and H-2 from by-product gases.
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页数:15
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