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2014
DOI: 10.1016/s1872-2067(14)60058-9
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Pure and Ni-substituted Co3O4 spinel catalysts for direct N2O decomposition

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Cited by 58 publications
(33 citation statements)
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References 40 publications
(57 reference statements)
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“…Similarly, N 2 O decomposition is much enhanced by nickel cobaltite (Ni x Co 1-x Co 2 O 4 ) as compared to pure NiO and Co 3 O 4 catalysts with the catalyst activity depending on the ratio of Ni 2+ to Co 2+ . [ 104 ] The improvement of Ni-Co bimetallic oxides is related to the role of Ni content in enhancing the reduction reaction of Co 3+ to Co 2+ , decreasing crystallite sizes, and increasing BET values. Buvaneswari and co-workers found that NiCo 2 O 4 powder effi ciently catalyses the reduction of p-nitrophenol to p-aminophenol by NaBH 4 at room temperature without any solvent.…”
Section: Heterogeneous Catalysismentioning
confidence: 99%
“…Similarly, N 2 O decomposition is much enhanced by nickel cobaltite (Ni x Co 1-x Co 2 O 4 ) as compared to pure NiO and Co 3 O 4 catalysts with the catalyst activity depending on the ratio of Ni 2+ to Co 2+ . [ 104 ] The improvement of Ni-Co bimetallic oxides is related to the role of Ni content in enhancing the reduction reaction of Co 3+ to Co 2+ , decreasing crystallite sizes, and increasing BET values. Buvaneswari and co-workers found that NiCo 2 O 4 powder effi ciently catalyses the reduction of p-nitrophenol to p-aminophenol by NaBH 4 at room temperature without any solvent.…”
Section: Heterogeneous Catalysismentioning
confidence: 99%
“…The low-temperature catalytic decomposition of N 2 O (up to 450°C) to nitrogen and oxygen offers attractive solution for decreasing N 2 O emissions in tail gas from nitric acid production plants. Among a large number of catalysts tested for the decomposition of N 2 O, cobalt spinels presented excellent catalytic activities which makes them promising for practical application in abatement of N 2 O emitted in waste gases from HNO 3 production plants [3][4][5]. To the best of our knowledge, only two research groups reported on manufacturing of shaped cobalt spinel based catalysts in pilot plant scale conditions [6][7][8].…”
Section: Introductionmentioning
confidence: 99%
“…The reported N 2 O decomposition mechanism on various metal oxide catalysts involves the following steps: (i) N 2 O adsorption via electron donation from the catalyst surface to the adsorbate; (ii) N-O bond destabilization, which leads to its scission and the liberation of N 2 molecule and the formation of an adsorbed O´species; and (iii) recombination of two O´species and desorption of one oxygen molecule. Thus, this reaction requires the coexistence of a redox couple on the catalysts surfaces, such as Co 2+ -Co 3+ [7][8][9][10][11][12][13][14][15][16]43], Cu + -Cu ++ [21,22], Ni 0 -Ni 2+ [23,24]. In this respect, our XPS analysis (Figure 7) revealed the presence of Ni 0 -Ni 2+ redox couple on the surfaces of bare NiO and Gd-promoted NiO.…”
Section: Catalytic Activity Measurementsmentioning
confidence: 73%
“…However, the activity of the present catalysts is comparable with the activities of other active catalysts measured at similar reaction conditions. For Cu x Co 1-x Co 2 O 4 and Ni x Co 1-x Co 2 O 4 (0.0 ď x ď 1.0) spinel-oxide catalysts, the highest activity (100% convesion) was obtained at 500˝C by the catalysts with x = 0.75 and 0.50, respectively [7,8]. Among a series of alkali-doped NiO catalysts, the K-and Cs-promoted catalysts (M/Ni molar ratio = 0.05) showed the highest activity levels [24].…”
Section: Introductionmentioning
confidence: 99%