Catalytic Process for Methane Production from Atmospheric Carbon Dioxide Utilizing Renewable Energy Научная публикация
Конференция |
Catalytic Science and Technology in Sustainable Energy and Environment : 2nd International Symposium 11-14 окт. 2016 , Tianjin |
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Журнал |
Catalysis Today
ISSN: 0920-5861 , E-ISSN: 1873-4308 |
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Вых. Данные | Год: 2017, Том: 298, Страницы: 117-123 Страниц : 7 DOI: 10.1016/j.cattod.2017.05.044 | ||||||
Ключевые слова | Carbon dioxide, Direct air capture, Heterogeneous catalysis, Power-to-gas, Renewable energy, Sabatier reaction | ||||||
Авторы |
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Организации |
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Информация о финансировании (3)
1 | Российский фонд фундаментальных исследований | 16-33-00198 |
2 | Федеральное агентство научных организаций России | 0303-2016-0010 |
3 | Совет по грантам Президента Российской Федерации | СП-3321.2016.1 |
Реферат:
Kinetics of CO2 methanation reaction over the commercial nickel catalyst NKM-2V was studied in a perfectly mixed reactor at T = 250–350 °C. It has been shown for the stoichiometric mixture of CO2 and H2 that both the catalyst activity and CO2 conversion increase with temperature. The decrease in CO2:H2 ratio at T = 300 °C have led to the rise of CO2 conversion to methane. The composite material K2CO3/Al2O3, which is a promising solid absorbent for direct CO2 capture from ambient air, has been synthesized and studied in the temperature-swing adsorption cycles. It has been shown that the increase in the adsorber temperature from 200 to 325 °C during the thermal regeneration step enhances the utilization extent of the composite sorbent in the cycle with the total CO2 uptake rising from 1.9 to 4.4 wt.%. The process combining thermal regeneration of the composite sorbent in hydrogen atmosphere at T = 325 °C and CO2 methanation reaction over the commercial nickel catalyst NKM-2V at T = 425 °C has been studied using the catalytic reactor connected to the outlet of the adsorber. It has been demonstrated that it is possible to transform CO2 into methane with conversion >99%.
Библиографическая ссылка:
Veselovskaya J.V.
, Parunin P.D.
, Okunev A.G.
Catalytic Process for Methane Production from Atmospheric Carbon Dioxide Utilizing Renewable Energy
Catalysis Today. 2017. V.298. P.117-123. DOI: 10.1016/j.cattod.2017.05.044 WOS Scopus РИНЦ CAPlus OpenAlex
Catalytic Process for Methane Production from Atmospheric Carbon Dioxide Utilizing Renewable Energy
Catalysis Today. 2017. V.298. P.117-123. DOI: 10.1016/j.cattod.2017.05.044 WOS Scopus РИНЦ CAPlus OpenAlex
Даты:
Поступила в редакцию: | 1 дек. 2016 г. |
Принята к публикации: | 11 мая 2017 г. |
Опубликована online: | 16 мая 2017 г. |
Опубликована в печати: | 1 дек. 2017 г. |
Идентификаторы БД:
Web of science: | WOS:000412315000016 |
Scopus: | 2-s2.0-85019496716 |
РИНЦ: | 31027934 |
Chemical Abstracts: | 2017:795262 |
OpenAlex: | W2615848886 |