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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
Журнал Catalysis Today
ISSN: 0920-5861 , E-ISSN: 1873-4308
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 Veselovskaya Janna V. 1,2 , Parunin Pavel D. 3 , Okunev Aleksey G. 1,2
Организации
1 Novosibirsk State University, Pirogova Str. 2, 630090 Novosibirsk, Russi
2 Boreskov Institute of Catalysis, Lavrentieva Av., 630090 Novosibirsk, Russia
3 Skolkovo Institute of Science and Technology, Nobel Street 3, 143026 Moscow, Russia

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
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
Цитирование в БД:
БД Цитирований
Web of science 43
Scopus 45
РИНЦ 41
OpenAlex 56
Альметрики: