1985
DOI: 10.1016/0021-9517(85)90193-9
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Catalytic properties of La1 $minus; xA$prime;xFeO3(A$prime; = Sr,Ce) and La1 $minus; xCexCoO3

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Cited by 157 publications
(60 citation statements)
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“…This is consistent with the TPD and TPR results, most of which show no desorption peak for β-oxygen up to the highest temperatures probed (1273 K). [38][39][40][41][42][43]46 Instead of surface oxygen vacancies, secondary phases were observed at 850-1250 K, which is also consistent with our predictions. 40,46 For adsorbed oxygen atoms (O low ), the TPD and TPR experiments on LFO generally show two different trends based on the calcination temperature of the ceramic.…”
Section: Relation To Experimental Resultssupporting
confidence: 90%
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“…This is consistent with the TPD and TPR results, most of which show no desorption peak for β-oxygen up to the highest temperatures probed (1273 K). [38][39][40][41][42][43]46 Instead of surface oxygen vacancies, secondary phases were observed at 850-1250 K, which is also consistent with our predictions. 40,46 For adsorbed oxygen atoms (O low ), the TPD and TPR experiments on LFO generally show two different trends based on the calcination temperature of the ceramic.…”
Section: Relation To Experimental Resultssupporting
confidence: 90%
“…In the case of LFO calcined below 923 K, desorption for α-oxygen was clearly observed. In particular, 46 In contrast, at a high calcination temperature of 1123 K, most of the experiments reported no desorption peak of α-oxygen, [41][42][43] even though weak peaks below 773 K were observed by Nitadori et al 39 For convenience, in the following discussion temperatures of 973 K or less will be defined as "low calcination temperatures" and those at 1123 K or higher will be defined as "high calcination temperatures".…”
Section: Relation To Experimental Resultsmentioning
confidence: 97%
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“…For instance, Misono et al [5][6][7] highlighted two peaks upon heating in TPD experiments on perovsiktes: α, due to the low-temperature release from the surface of oxygen deriving from O -and O 2-species, and β, occurring at higher temperature, due to O 2-species from the bulk.…”
Section: Introductionmentioning
confidence: 99%
“…The results confirm the catalytic activity of perovskite oxides because the methane oxidation starts already at 400 • C. In addition, the partial substitution of lanthanum with strontium increase the catalytic activity because at 600 • C the unsubstituted LaFeO 3 leads to a methane conversion of 25%, while the substituted La 0.8 Sr 0.2 FeO 3 and La 0.6 Sr 0.4 FeO 3 leads to a higher methane conversion of 65% and 35% respectivelly. The lower catalytic activity of the higher Sr-substituted perovskite is due to the structural and valece changes, leading to lower reductin/oxidation capability from the relative rate of dissociation and bulk diffusion of oxide ions [32]. Since the initial stage of the sigmoidal curve is related to a kinetically controlled regime [30,33], the rate of methane combustion was calculated from the conversion values lower than 20% accordingly with equation r = (F gas · X CH4 ) / (V ST P · m cat ), where r(mol·s −1 ·g −1 ) is the reaction rate, F gas (L·s −1 ) is the inlet flow of reactants in, X CH4 is the fractional conversion, V ST P (22.414 L·mol −1 ) is the volume occupied by one mole of gas at Standard Temperature and Pressure condition, m cat (g) is the mass of catalyst.…”
Section: -6mentioning
confidence: 99%