2017
DOI: 10.1016/j.ijhydene.2016.10.012
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Hydrogen production from glucose by supercritical water gasification with Ni/Zr(Ce,Y)O2-δ catalysts

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Cited by 16 publications
(9 citation statements)
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“…Huang et al (2017) studied the catalytic supercritical water gasification of glucose over Ni/Zr(Ce,Y)O2-δ catalysts at 500°C, 23-24 MPa, and feed concentration of 10 wt.%, and reported that carbon gasification efficiency was improved as Ni concentration was increased from 0.1 to 0.7. In this same work, a hydrogen yield of 22 mol kg -1 was obtained using Ni0.5Zr0.8Y0.2O2.8 (NZY582) catalyst which was 10 times greater than that of the catalyst-free conditions.…”
Section: Tablementioning
confidence: 99%
“…Huang et al (2017) studied the catalytic supercritical water gasification of glucose over Ni/Zr(Ce,Y)O2-δ catalysts at 500°C, 23-24 MPa, and feed concentration of 10 wt.%, and reported that carbon gasification efficiency was improved as Ni concentration was increased from 0.1 to 0.7. In this same work, a hydrogen yield of 22 mol kg -1 was obtained using Ni0.5Zr0.8Y0.2O2.8 (NZY582) catalyst which was 10 times greater than that of the catalyst-free conditions.…”
Section: Tablementioning
confidence: 99%
“…. , n j (9) and the optimum mole numbers of the product gases at the equilibrium state can be found as…”
Section: Simulation Modelmentioning
confidence: 99%
“…As an alternative to the conventional gasification, the supercritical water gasification (SCWG) process uses water over 22 MPa and 374 • C (critical point) as the gasifying agent to decompose the wet biomass feedstock, allowing to achieve a much higher ratio of gasification and hydrogen generation [1][2][3][4][5]. Although the high cost of the feedstock is a challenging issue in utilizing the SCWG, low-cost feedstocks like sewage sludges are widely available to be used as a heavily moisture-laden feedstock in this process [6][7][8][9]. Organic wastewater and kitchen waste are considered as possible sewage sludge which do not need any drying steps, resulting in economically beneficial characteristics in the production of hydrogen [10].…”
Section: Introductionmentioning
confidence: 99%
“… 10 , 11 SCW gasification, in fact, is considered the most cost-effective thermochemical conversion technology to convert biomass into hydrogen. 12 Most of the studies carried out on SCW gasification involved the use of biomass model compounds, 13 including cellulose, 14 18 lignin, 14 , 19 , 20 starch, 15 fructose, 21 , 22 and glycerol. 23 , 24 The use of model biomass provides a better understanding of the reaction mechanisms undergoing in the SCW gasification process.…”
Section: Introductionmentioning
confidence: 99%
“…Besides, it features high reaction efficiency and H 2 selectivity among nearly any type of biomass, with no restriction on moisture content like in the classical gasification process. , SCW gasification, in fact, is considered the most cost-effective thermochemical conversion technology to convert biomass into hydrogen . Most of the studies carried out on SCW gasification involved the use of biomass model compounds, including cellulose, lignin, ,, starch, fructose, , and glycerol. , The use of model biomass provides a better understanding of the reaction mechanisms undergoing in the SCW gasification process. However, lignocellulosic compounds in real biomass undergo complex interaction reactions during gasification that cannot be apprehended with model biomass.…”
Section: Introductionmentioning
confidence: 99%