کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
150924 456459 2011 6 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Active carbon-supported Ni, Ni/Cu and Ni/Cu/Pd catalysed steam reforming of ethanol for the production of hydrogen
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
پیش نمایش صفحه اول مقاله
Active carbon-supported Ni, Ni/Cu and Ni/Cu/Pd catalysed steam reforming of ethanol for the production of hydrogen
چکیده انگلیسی

This work aims at producing hydrogen from ethanol using active carbon-supported nickel based catalysts. Steam reforming of ethanol is carried out in a tubular reactor at a temperature range of 150–700 °C using nickel, nickel/copper and nickel/copper/palladium catalysts supported with active carbon. The selectivity values towards hydrogen obtained from the reactions using the different catalysts are compared. The results show that the selectivity of all the catalysts studied towards hydrogen increases with increase in temperature up to the temperature of 450 °C and the active carbon-supported Ni/Cu/Pd catalyst gives the highest selectivity towards hydrogen. Beyond this temperature, the selectivity values of the catalyst containing palladium continue to decrease. It is concluded that the highest selectivity of hydrogen is given by the catalyst containing palladium at the temperature of 450 °C.


► Ni, Ni/Cu, Ni/Cu/Pd supported with active carbon as catalysts precursors
► Catalysts for steam reforming of ethanol
► The selectivity values using the different catalysts are compared
► Selectivity studied towards H2 increases with increase in temperature up to 450 °C
► The highest selectivity of hydrogen is given by the catalyst containing Pd at 450 °C.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Chemical Engineering Journal - Volume 171, Issue 3, 15 July 2011, Pages 1270–1275
نویسندگان
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