Low Temperature Catalytic Steam Reforming of Propane-Methane Mixture into Methane-Rich Gas: Experiment and Macrokinetic Modeling
Научная публикация
Общее |
Язык:
Английский,
Жанр:
Статья (Full article),
Статус опубликования:
Опубликована,
Оригинальность:
Оригинальная
|
Журнал |
Fuel
ISSN: 0016-2361
, E-ISSN: 1873-7153
|
Вых. Данные |
Год: 2014,
Том: 135,
Страницы: 76-82
Страниц
: 7
DOI:
10.1016/j.fuel.2014.06.032
|
Ключевые слова |
Catalytic steam prereforming, Macrokinetic modeling, Methane-rich gas, Propane, Utilization of associated petroleum gas |
Авторы |
Zyryanova M.M.
1,2,3
,
Snytnikov P.V.
1,2,3
,
Shigarov A.B.
1,2,3
,
Belyaev V.D.
1,2,3
,
Kirillov V.A.
1,2,3
,
Sobyanin V.A.
1,2,3
|
Организации |
1 |
Boreskov Institute of Catalysis, SB RAS, Pr. Lavrentieva, 5, Novosibirsk, Russia
|
2 |
Novosibirsk State University, Pirogova St., 2, Novosibirsk, Russia
|
3 |
‘‘UNICAT’’ Ltd, Pr. Lavrentieva, 5, Novosibirsk, Russia
|
|
Информация о финансировании (2)
1
|
Совет по грантам Президента Российской Федерации
|
МК-2199.2013.3
|
2
|
Министерство образования и науки Российской Федерации
|
|
Steam reforming of propane–methane mixture into methane-rich gas was studied in a fixed-bed continuous-flow reactor in a temperature interval of 150–325 °C under atmospheric pressure over Ni-based catalyst. It was found that the catalyst had good performance under low steam-to-carbon ratio of 0.39–0.58 and provided equilibrium product distribution at GHSV = 670–3100 h−1. Macrokinetic modeling of the experimental data obtained was performed in the framework of isothermal plug-flow reactor model. For the first time the two-step macro-kinetic scheme was suggested, that includes the reactions of irreversible propane steam reforming (first-order on propane): C3H8 + 6H2O → 3CO2 + 10H2 with activation energy 112 kJ/mole and reversible CO2 methanation (first-order on hydrogen): CO2 + 4H2⇄ CH4 + 2H2O with activation energy 50 kJ/mole. It was shown that the proposed scheme describes quantitatively all the experimental results.