期刊
PROCESSES
卷 11, 期 2, 页码 -出版社
MDPI
DOI: 10.3390/pr11020628
关键词
SNG; energy; CO2 utilization; CO2 methanation; coexistent CO; Ni catalyst
Greenhouse gases, generated largely in the energy sector, are the main cause of global warming. The need for technology that reduces greenhouse gas emissions while producing energy has led to increased attention on CCU technology, which uses CO2 to produce synthetic natural gas (SNG). This study focused on CO2 methanation and examined the efficiency and durability of CO gas, rather than CO2 and H-2 gas, in the reaction.
Greenhouse gases, the main cause of global warming, are generated largely in the energy sector. As the need for technology that has reduced greenhouse gas emissions while producing energy is on an increase, CCU technology, which uses CO2 to produce CH4 (SNG energy, synthetic natural gas), is drawing attention. Thus, the reaction for converting CO2 to CH4 at a specific temperature using a catalyst is CO2 methanation. The field of CO2 methanation has been actively studied, and many studies have been conducted to enhance the activity of the catalysts. However, there is a lack of research on the variables that may appear when CO2 methanation is attempted using emissions containing CO2 generated from industrial fields and bio-plants. According to previous studies, it is reported that realistic feed gases from gasification or biomass plants contain a significant amount of CO. this study is a follow-up study focused on the application of CO2 methanation in various real processes. In the CO2 methanation reaction, a study was conducted on the catalyst efficiency and durability of CO gas that can coexist in the inlet gas rather than CO2 and H-2 gas. The CO2 methanation activity was observed at 200-350 degrees C when 0-15% CO coexisted using the Ni-Ce-Zr catalyst, and the operating variables were set for optimal SNG production. As a result of adjusting the ratio of inlet gas to increase the yield of CH4 in the produced gas, the final CO2 conversion of 83% and CO conversion of 97% (with 15% CO gas at 280 degrees C) were obtained. In addition, catalytic efficiency and catalyst surface analysis were performed by exposing CO gas during the CO2 methanation reaction for 24 h. It showed high activity and excellent stability. The results of this study can be used as the basic data when applying an actual process.
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