Catalytic Activity of Tandem Catalysts in CO2 Hydrogenation to Olefins Depending on Component Arrangement Научная публикация
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Petroleum Chemistry
ISSN: 0965-5441 , E-ISSN: 1555-6239 |
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| Вых. Данные | Год: 2025, Том: 65, Номер: 4, Страницы: 440-449 Страниц : 10 DOI: 10.1134/s0965544125600675 | ||||
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Реферат:
A series of tandem catalysts based on indium, zinc, and gallium oxides were synthesized, with a CHA-type silicoaluminophosphate and an MFI-type zeolite as acidic components. These catalysts were tested in the conversion of carbon dioxide to olefins at 380°C and 27 bar, with the component arrangement being varied. The physicochemical properties of the catalysts and their components were characterized by low-temperature nitrogen adsorption, X-ray diffraction analysis (XRD), X-ray fluorescence spectrometry (XRF), scanning electron
microscopy (SEM), and temperature-programmed desorption of ammonia (NH3-TPD). It is shown that the optimal arrangement of the hydrogenating and acidic components in the reactor depends on the type of the hydrogenating component. The best catalytic performance (33% CO2 conversion and 5.6% yield of hydrocarbons) was achieved in the presence of a ZnGa2O4/MFI catalyst with the components being mechanically mixed.
Библиографическая ссылка:
Ivanov G.K.
, Maerle A.A.
, Bachurina D.O.
, Roshchina T.M.
, Ivanova I.I.
Catalytic Activity of Tandem Catalysts in CO2 Hydrogenation to Olefins Depending on Component Arrangement
Petroleum Chemistry. 2025. V.65. N4. P.440-449. DOI: 10.1134/s0965544125600675 РИНЦ OpenAlex
Catalytic Activity of Tandem Catalysts in CO2 Hydrogenation to Olefins Depending on Component Arrangement
Petroleum Chemistry. 2025. V.65. N4. P.440-449. DOI: 10.1134/s0965544125600675 РИНЦ OpenAlex
Даты:
| Поступила в редакцию: | 14 мар. 2025 г. |
| Принята к публикации: | 10 апр. 2025 г. |
| Опубликована online: | 29 апр. 2025 г. |
Идентификаторы БД:
| ≡ РИНЦ: | 82650543 |
| ≡ OpenAlex: | W4409920951 |