2008
DOI: 10.1016/j.cattod.2007.12.081
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CO2 reforming of methane over Ni/Mg/Al/Ce mixed oxides

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Cited by 134 publications
(71 citation statements)
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“…T max was shifted from 810 to 835°C and from 780 to 820°C for HTNi25-Ce and HTNi5-Ce, respectively when compared to the unpromoted samples. These results are in good agreement with those reported in the literature [19][20][21]. The different trend for samples with or without Mg in its structure (HTNi100-Ce as compared to other catalysts) also suggests that the reducibility is an overlapping effect originating from the presence of both ceria and magnesium in the catalysts.…”
Section: Resultssupporting
confidence: 92%
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“…T max was shifted from 810 to 835°C and from 780 to 820°C for HTNi25-Ce and HTNi5-Ce, respectively when compared to the unpromoted samples. These results are in good agreement with those reported in the literature [19][20][21]. The different trend for samples with or without Mg in its structure (HTNi100-Ce as compared to other catalysts) also suggests that the reducibility is an overlapping effect originating from the presence of both ceria and magnesium in the catalysts.…”
Section: Resultssupporting
confidence: 92%
“…In this temperature region, the reduction process is quite complicated to explain since both processes of the reduction of NiO and ceria may have overlapped. The reduction of pure CeO 2 occurs in three stages: (i) the reduction of surface oxygen or oxygen capping species (250-300°C) [44], (ii) the reduction of surface lattice oxygen (450-600°C) [23] and total bulk reduction up to 900°C [21]. On the other hand, the reduction of Ni species from the framework of Mg(Ni,Al)O mixed oxides to metallic nickel is realized in two steps: (i) the reduction of surface NiO (ca.…”
Section: Resultsmentioning
confidence: 99%
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“…18,19 The catalysts were not previously reduced and reactants were injected from room temperature, increasing to 700 °C at 10 k min -1 . Flow of reactants used was CH 4 /CO 2 …”
Section: Catalytic Testsmentioning
confidence: 99%
“…[13][14][15] We have reported the use of different types of hydrotalcites and natural clays as catalyst precursors for CO 2 reforming of methane. [16][17][18][19][20][21][22] Specifically, in our work with hydrotalcites we have focused on the study of hydrotalcites of Ce-containing Ni-Mg-Al obtained by coprecipitation, 19,22 reconstruction 17,18 and self-combustion methods. 21 The work led to highly active catalysts that are both selective and stable, with strong basic properties, low particle sizes and low coke formation.…”
Section: Introductionmentioning
confidence: 99%