Methane Steam Reforming in a Pd-Ru Membrane Reactor

Methane steam reforming has been carried out in a Pd-Ru membrane reactor at 500-600°C. The membrane reactor consisted of a Pd-6%Ru tube of 100 μm wall thickness and commercial catalysts packed outside of the membrane. The methane conversion was significantly enhanced in the membrane reactor in which reaction equilibrium was shifted by selective permeation of hydrogen through the membrane. The methane conversion at 500°C was improved as high as 80% in the membrane reactor, while equilibrium conversion in a fixed-bed reactor was 57%. The effect of gas flow rate and temperature on the performance of the membrane reactor was investigated and the results were compared with the simulated result from the model. The model prediction is in good agreement with the experimental result. In order to apply the membrane in practice, however, the thickness of the membrane has to be reduced. Therefore, the effect of membrane thickness on performance of the membrane reactor was estimated using the model.

Авторы
Nam S.W.1 , Yoon S.P.1 , Ha H.Y.1 , Hong S.-A.1 , Maganyuk A.P. 2
Редакторы
-
Издательство
Korean Institute of Chemical Engineers
Номер выпуска
3
Язык
Английский
Страницы
288-291
Статус
Опубликовано
Подразделение
-
Номер
-
Том
17
Год
2000
Организации
  • 1 Battery and Fuel Cell Res. Center, Korea Inst. of Sci. and Technology, Seoul 136-791, South Korea
  • 2 Russia People's Friendship Univ., Moscow, Russian Federation
Ключевые слова
Inorganic Membrane; Membrane Reactor; Methane Steam Reforming; Palladium; Pd Membrane
Дата создания
19.10.2018
Дата изменения
19.10.2018
Постоянная ссылка
https://repository.rudn.ru/ru/records/article/record/473/