1993
DOI: 10.1006/jcat.1993.1105
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Carbon Monoxide and Methane Oxidation Properties of Oxide Solid Solution Catalysts

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Cited by 65 publications
(31 citation statements)
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“…Being the same as for LST415, atomic positions and displacement factors are not reported for clarity. LSTM415 can be compared to the low activity of La 0.8 Sr 0.2 MnO 3 [53]. However, the catalytic activity of LSTM415 remains higher than that of LST3D structure [33] which reinforces the superiority of 2D structure for catalytic activity, what has probably to see with its electronic structure as suggested in Ref.…”
Section: Catalytic Behaviour For Methane Steam Reformingmentioning
confidence: 67%
“…Being the same as for LST415, atomic positions and displacement factors are not reported for clarity. LSTM415 can be compared to the low activity of La 0.8 Sr 0.2 MnO 3 [53]. However, the catalytic activity of LSTM415 remains higher than that of LST3D structure [33] which reinforces the superiority of 2D structure for catalytic activity, what has probably to see with its electronic structure as suggested in Ref.…”
Section: Catalytic Behaviour For Methane Steam Reformingmentioning
confidence: 67%
“…La 1-x Sr x FeO 3-d , possessing mixed ionic and electronic conductivity, is a promising cathode material in solid oxide fuel cells, oxygen sensor, oxygen permeable membrane and catalyst [1][2][3]. Oxygen transport is important for these applications, which calls for fundamental understanding of bulk diffusion and the surface exchange kinetics.…”
Section: Introductionmentioning
confidence: 99%
“…In most cases the oxygen isotope surface exchange coefficient (k o ) is proportional to the partial pressure of oxygen, pO 2 n , where n typically varies between 0.45 and 0.90, at oxidizing conditions [6,7]. The most advanced model for the surface exchange kinetics is based on studies of Fe-doped SrTiO 3 single crystals [8], where dissociation of surface adsorbed O 2 2-intermediates was rate controlling. Measurements on La 1-x Sr x FeO 3-d have proposed that the kinetics are controlled by collision of O 2 (g) and oxygen vacancies giving a rate proportional to dpO 2 [7].…”
Section: Introductionmentioning
confidence: 99%
“…Supported palladium catalysts were extensively investigated for the methane combustion. They show high activity even below 350 • C [1]. However, their commercialization is still limited by: the decrease of the catalytic activity at high temperature [2], the poisoning, and the need to use extremely expensive palladium.…”
Section: Introductionmentioning
confidence: 99%