Modeling of Hydrogen Production by Diesel Reforming over Rh/Ce0.75Zr0.25O2‐δ‐ƞ‐Al2O3/FeCrAl Wire Mesh Honeycomb Catalytic Module | Sciact - CRIS-система Института катализа

Modeling of Hydrogen Production by Diesel Reforming over Rh/Ce0.75Zr0.25O2‐δ‐ƞ‐Al2O3/FeCrAl Wire Mesh Honeycomb Catalytic Module Научная публикация

Журнал

Catalysis Today
ISSN: 0920-5861 , E-ISSN: 1873-4308

Вых. Данные

Год: 2021, Том: 378, Страницы: 240-248 Страниц : 9 DOI: 10.1016/j.cattod.2020.11.015

Ключевые слова

Hexadecane; Steam conversion; Autothermal reforming; Hydrogen; Wire-mesh catalyst; Modelling

Авторы

Zazhigalov S.V. ¹ , Shilov V.A. ^1,2 , Rogozhnikov V.N. ¹ , Potemkin D.I. ^1,2 , Sobyanin V.A. ¹ , Zagoruiko A.N. ¹ , Snytnikov P.V. ^1,2

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 (1)

Российский научный фонд

19-19-00257

The work is devoted to experimental studies and construction of a mathematical model of n-hexadecane (as the simplest diesel surrogate) reforming over Rh/Ce0.75Zr0.25O2-δ-ƞ-Al2O3/FeCrAl wire mesh honeycomb catalytic module in auto-thermal reforming (ATR) and steam reforming (SR) modes. Experiments were performed using the scalable catalytic modules with recurrent meshy channeled internal geometrical structure. This provided the accurate reproduction of mass transfer limitations and accompanying homogeneous reactions, thus significantly simplifying the following scale-up procedures. Impossibility to apply simple isothermal reactor models was compensated by application of CFD modelling for reproduction of internal distribution of temperature, fluid velocities and composition inside the catalyst module. The earlier proposed reaction scheme was supported by additional reactions to account for the formation of light C2-C5 hydrocarbons. The proposed model provides good description of both ATR and SR process modes, at the same time demonstrating significant difference between them. The proposed model may be used for development, scale-up and optimization of catalytic reformers using SR and ATR modes and their combination for processing diesel and similar liquid hydrocarbon fuels.

Zazhigalov S.V. , Shilov V.A. , Rogozhnikov V.N. , Potemkin D.I. , Sobyanin V.A. , Zagoruiko A.N. , Snytnikov P.V.
Modeling of Hydrogen Production by Diesel Reforming over Rh/Ce0.75Zr0.25O2‐δ‐ƞ‐Al2O3/FeCrAl Wire Mesh Honeycomb Catalytic Module
Catalysis Today. 2021. V.378. P.240-248. DOI: 10.1016/j.cattod.2020.11.015 WOS Scopus РИНЦ CAPlus OpenAlex

Поступила в редакцию:	10 авг. 2020 г.
Принята к публикации:	23 нояб. 2020 г.
Опубликована online:	7 дек. 2020 г.
Опубликована в печати:	15 окт. 2021 г.

Web of science:	WOS:000687125500007
Scopus:	2-s2.0-85099503163
РИНЦ:	45002443
Chemical Abstracts:	2020:2691877
OpenAlex:	W3112632195

БД	Цитирований
Scopus	24
РИНЦ	20
Web of science	20
OpenAlex	25