2013
DOI: 10.1016/j.fuel.2012.08.057
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Investigation into the mechanism of NiMg(Ca)bAlcOx catalytic activity for production of solarised syngas from carbon dioxide reforming of methane

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Cited by 8 publications
(2 citation statements)
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“…The specific surface area is calculated by the BET method in the relative pressure range of 0.05-0.30 of the adsorption branch, and the pore volume is calculated from the adsorption isotherm at relative pressure of 0.99; both the results are shown in Table 1. The BET surface increased with the decrease in Mg/Al ratio, indicating that Al plays a vital role in maintaining a large surface area; the same phenomenon was also observed by Sun et al [41]. The pore size distributions become broad then narrow again with the increasing Mg/Al ratio, which implied a slight change in catalysts' structure with the variation in Mg/Al ratios.…”
Section: Characterization Of Fresh Catalystssupporting
confidence: 79%
“…The specific surface area is calculated by the BET method in the relative pressure range of 0.05-0.30 of the adsorption branch, and the pore volume is calculated from the adsorption isotherm at relative pressure of 0.99; both the results are shown in Table 1. The BET surface increased with the decrease in Mg/Al ratio, indicating that Al plays a vital role in maintaining a large surface area; the same phenomenon was also observed by Sun et al [41]. The pore size distributions become broad then narrow again with the increasing Mg/Al ratio, which implied a slight change in catalysts' structure with the variation in Mg/Al ratios.…”
Section: Characterization Of Fresh Catalystssupporting
confidence: 79%
“…NiMg 3 AlO x was selected as a CDRM catalyst in this work, because the catalyst formulation showed the highest performance among a series of NiMg b Al c O x catalysts in our previous work [24]. NiMg 3 AlO x powder was prepared by the co-precipitation method reported [22].…”
Section: Ni-containing Foam Catalystsmentioning
confidence: 99%