Synthesis Gas Production by Steam Reforming of Ethanol
Научная публикация
| Общее |
Язык:
Английский,
Жанр:
Статья (Full article),
Статус опубликования:
Опубликована,
Оригинальность:
Оригинальная
|
| Журнал |
Applied Catalysis A: General
ISSN: 0926-860X
, E-ISSN: 1873-3875
|
| Вых. Данные |
Год: 2001,
Том: 220,
Номер: 1-2,
Страницы: 123-127
Страниц
: 5
DOI:
10.1016/S0926-860X(01)00708-6
|
| Ключевые слова |
Ethanol, Steam reforming, Syngas, Two-layer fixed-bed reactor |
| Авторы |
Galvita V.V.
1
,
Semin G.L.
1
,
Belyaev V.D.
1
,
Semikolenov V.A.
1
,
Tsiakaras P.
2
,
Sobyanin V.A.
1
|
| Организации |
| 1 |
Boreskov Institute of Catalysis, Prospekt Akademika Lavrentieva 5, 630090 Novosibirsk, Russia
|
| 2 |
Department of Mechanical and Industrial Engineering, University of Thessaly, Pedion Areos, 38334 Volos, Greece
|
|
Информация о финансировании (1)
|
1
|
International Association for the Promotion of Co-operation with Scientists from the New Independent States of the Former Soviet Union
|
897
|
A two-layer fixed-bed catalytic reactor for syngas production by steam reforming of ethanol has been proposed. In the reactor, ethanol is first converted to a mixture of methane, carbon oxides and hydrogen over a Pd-based catalyst and then this mixture is converted to syngas over a Ni-based catalyst for methane steam reforming. It has been shown that the use of the two-layer fixed-bed reactor prevents coke formation and provides the syngas yield closed to equilibrium.