2007
DOI: 10.1016/j.cattod.2006.09.038
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Production of hydrogen by steam reforming of glycerin over alumina-supported metal catalysts

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Cited by 205 publications
(139 citation statements)
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“…Zhang et al (2007) produced H 2 through the glycerol steam reforming over ceria-supported metal catalysts and found that a glycerol conversion of 100% could be achieved at 400C. Adhikari et al (2007b) studied steam reforming of glycerol using an alumina-supported metal catalyst over a range of conditions and showed that, at high temperatures, high gas yield was reached and selectivity of up to 70% was obtained. Steam reforming of glycerol was evaluated on Ni/CeO 2 , Ni/MgO, and Ni/TiO 2 catalysts (Hirai, et al, 2005).…”
Section: Introductionmentioning
confidence: 99%
See 1 more Smart Citation
“…Zhang et al (2007) produced H 2 through the glycerol steam reforming over ceria-supported metal catalysts and found that a glycerol conversion of 100% could be achieved at 400C. Adhikari et al (2007b) studied steam reforming of glycerol using an alumina-supported metal catalyst over a range of conditions and showed that, at high temperatures, high gas yield was reached and selectivity of up to 70% was obtained. Steam reforming of glycerol was evaluated on Ni/CeO 2 , Ni/MgO, and Ni/TiO 2 catalysts (Hirai, et al, 2005).…”
Section: Introductionmentioning
confidence: 99%
“…To date, although there have been a few studies on the use of catalysts active for methane and/or ethanol steam reforming such as Ni-based catalysts for steam reforming of glycerol (Adhikari, et al, 2007a;2007b and2008;Czernik, et al, 2002;Douette, et al, 2007;Hirai, et al, 2005;Zhang, et al, 2007), little has been found in the literature on glycerol steam reforming with in-situ CO 2 removal. This forms the main motivation for carrying this study on the use of a commercial Ni-based catalyst and a calcined dolomite sorbent to investigate the feasibility of sorption enhanced steam reforming of glycerol for hydrogen production.…”
Section: Introductionmentioning
confidence: 99%
“…Beside that, glycerol can be degraded into other compounds that have economic value as a fuel that is hydrogen (Byrd et al, 2008) or methanol (Tsukuda et al, 2007) and other chemical products that have added value such as acrolein (Wang et al, 2009), propane (Murata et al, 2008), and lactic acid (Yuksel et al, 2009) to degrade glycerol. The degradation of glycerol can be done in various processes such as pyrolysis (Vallyapan et al, 2008), steam reforming (Adhikari et al, 2007), and catalytic hydrogenation (Murata et al, 2008). Vol.…”
Section: Introductionmentioning
confidence: 99%
“…The commercial viability of biodiesel is complicated because now the market has an absorption limit for growing supply of glycerin. It is necessary to find new applications for this product, [9][10][11] and value added to glycerin generated, otherwise this by-product could undermine the economic viability of any production process of biodiesel as renewable fuel. 5,7 The utilization of glycerol as a chemical platform represents an opportunity to obtain value added products from a highly functionalized and cheap raw material, and much research has been recently dedicated to find new chemical pathway for the glycerol transformation to value added products.…”
Section: Introductionmentioning
confidence: 99%