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Composite Rh/Zr0.25Ce0.75O2-δ-ƞ-Al2O3/Fecralloy Wire Mesh Honeycomb Module for Natural Gas, LPG and Diesel Catalytic Conversion to Syngas Научная публикация

Журнал International Journal of Hydrogen Energy
ISSN: 0360-3199 , E-ISSN: 1879-3487
Вых. Данные Год: 2019, Том: 44, Номер: 20, Страницы: 9941-9948 Страниц : 8 DOI: 10.1016/j.ijhydene.2018.12.148
Ключевые слова Structured catalyst; Steam and autothermal reforming; Partial oxidation; Hexadecane; Natural gas; Liquid petroleum gas
Авторы Shoynkhorova T.B. 1 , Rogozhnikov V.N. 1 , Ruban N.V. 1,2 , Shilov V.A. 1,2 , Potemkin D.I. 1,2 , Simonov P.A. 1 , Belyaev V.D. 1,2 , Snytnikov P.V. 1,2 , Sobyanin V.A. 1
Организации
1 Boreskov Institute of Catalysis, Pr. Akademika Lavrentieva, 5, Novosibirsk 630090, Russia
2 Novosibirsk State University, Pirogova St., 2, Novosibirsk 630090, Russia

Информация о финансировании (2)

1 Федеральное агентство научных организаций России 0303-2016-0011
2 Российский научный фонд 17-79-30071

Реферат: The reactions of catalytic autothermal and steam conversion of n – C16H34 (model compound simulating diesel fuel), and partial oxidation of natural gas and LPG were studied using 0.24wt%Rh/(12wt%Zr0.25Ce0.75O2-δ-ƞ-Al2O3)/Fecralloy wire mesh honeycomb modules. The experiments were carried out in a flow setup in the temperature range of 550–960 °C and at atmospheric pressure. It was shown that the observed syngas (CO + H2) productivities were 65 and 53 m3Lcat−1h−1 (STP) at GHSV of 100,000 and 80,000 h−1 in natural gas and liquid petroleum gas catalytic partial oxidation processes, respectively. The product distributions were still close to the calculated equilibrium values. The catalyst activity was very high and, potentially, the maximum syngas productivity may even exceed experimentally demonstrated values. It was shown also that 0.24wt%Rh/(12wt%Zr0.25Ce0.75O2-δ-ƞ-Al2O3)/Fecralloy catalyst provided complete n-hexadecane conversion with the maximum syngas (CO + H2) productivity of 6.2 m3Lcat−1h−1 (STP) at GHSV of 13,300 h−1. The proposed concept of hydrogen-rich gas production from various hydrocarbon feedstocks in a multi-fuel catalytic reformer over single composite catalyst was proved feasible. The produced synthesis gas can be supplied as a fuel for power generation units based on high-temperature solid oxide fuel cells.
Библиографическая ссылка: Shoynkhorova T.B. , Rogozhnikov V.N. , Ruban N.V. , Shilov V.A. , Potemkin D.I. , Simonov P.A. , Belyaev V.D. , Snytnikov P.V. , Sobyanin V.A.
Composite Rh/Zr0.25Ce0.75O2-δ-ƞ-Al2O3/Fecralloy Wire Mesh Honeycomb Module for Natural Gas, LPG and Diesel Catalytic Conversion to Syngas
International Journal of Hydrogen Energy. 2019. V.44. N20. P.9941-9948. DOI: 10.1016/j.ijhydene.2018.12.148 WOS Scopus РИНЦ CAPlus OpenAlex
Даты:
Поступила в редакцию: 10 окт. 2018 г.
Принята к публикации: 12 дек. 2018 г.
Опубликована online: 12 янв. 2019 г.
Опубликована в печати: 19 апр. 2019 г.
Идентификаторы БД:
Web of science: WOS:000466455000031
Scopus: 2-s2.0-85059743979
РИНЦ: 38643380
Chemical Abstracts: 2019:50301
OpenAlex: W2910292759
Цитирование в БД:
БД Цитирований
Scopus 31
Web of science 29
РИНЦ 35
OpenAlex 29
Альметрики: