2013
DOI: 10.1016/j.ijhydene.2012.10.063
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Hydrogen and syngas production by methane dry reforming on SBA-15 supported nickel catalysts: On the effect of promotion by Ce0.75Zr0.25O2 mixed oxide

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Cited by 114 publications
(87 citation statements)
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“…In this work, the carbon dioxide conversion was calculated according to the formula reported by several researchers; Albarazi et al, Asencios et al and Oyama et al [23][24][25]. The properties of the carbonaceous coke deposited on the reacted catalysts were determined by temperature-programmed oxidation (TPO) experiments.…”
Section: Gas Analysismentioning
confidence: 99%
“…In this work, the carbon dioxide conversion was calculated according to the formula reported by several researchers; Albarazi et al, Asencios et al and Oyama et al [23][24][25]. The properties of the carbonaceous coke deposited on the reacted catalysts were determined by temperature-programmed oxidation (TPO) experiments.…”
Section: Gas Analysismentioning
confidence: 99%
“…Both conversions increased with temperature, reflecting the endothermic character of the dry reforming reaction. However, the CH 4 conversion was always slightly higher than that of CO 2 , over the entire temperature range, suggesting some (although limited) decomposition of methane into hydrogen and carbon (CH 4 → 2H 2 + C) as side reaction [6,18].…”
Section: Catalytic Activitymentioning
confidence: 98%
“…A suggested solution to inhibit carbon deposition is to promote the catalyst with a metal oxide, especially CeO 2 . The latter is characterized by redox properties (Ce 4+ ↔ Ce 3+ ) that promote oxygen vacancies formation, thus enhancing the mobility of surface oxygen whose presence contributes in lowering carbon deposition on the metallic particles [4][5][6][7]. It was also reported that both metal dispersion and metal-support interaction are improved in presence of CeO 2 [5,7].…”
Section: Introductionmentioning
confidence: 99%
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