کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
7711857 | 1497421 | 2016 | 8 صفحه PDF | دانلود رایگان |
عنوان انگلیسی مقاله ISI
Hydrogen and syngas production by dry reforming of fermentation products on porous ceramic membrane-catalytic converters
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موضوعات مرتبط
مهندسی و علوم پایه
شیمی
الکتروشیمی
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چکیده انگلیسی
Regularities of the processes of dry reforming of methane (DRM), ethanol (DRE) and modeling mixture of fermentation products (DRFP) to hydrogen and syngas over Ni-Co-containing porous ceramic membrane-catalytic converters(PCMCC), obtained by self-propagating high temperature synthesis (SHS), were studied. The non-additive effect of increasing the catalytic activity in the processes over Ni-Co3O4 (50-50%) PCMCC was discovered. It was shown that in the PCMCC the processes more intensified in comparison to the implementation of the processes in a flow reactor with a fixed bed of granular catalyst of the same composition.
ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: International Journal of Hydrogen Energy - Volume 41, Issue 4, 30 January 2016, Pages 2424-2431
Journal: International Journal of Hydrogen Energy - Volume 41, Issue 4, 30 January 2016, Pages 2424-2431
نویسندگان
Mark V. Tsodikov, Alexey S. Fedotov, Dmitriy O. Antonov, Valeriy I. Uvarov, Victor Yu Bychkov, Francis C. Luck,