Dependence of n-Butane Activation on Active Site of Vanadium Phosphate Catalysts

The nature and the role of oxygen species and vanadium oxidation states on the activation of n-butane for selective oxidation to maleic anhydride were investigated. Bi-Fe doped and undoped vanadium phosphate catalysts were used a model catalyst. XRD revealed that Bi-Fe mixture dopants led to formati...

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Published in:Catalysis letters Vol. 130; no. 3-4; pp. 327 - 334
Main Authors: Taufiq-Yap, Y. H, Goh, C. K, Hutchings, G. J, Dummer, N, Bartley, J
Format: Journal Article
Language:English
Published: Boston Boston : Springer US 01.07.2009
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Abstract The nature and the role of oxygen species and vanadium oxidation states on the activation of n-butane for selective oxidation to maleic anhydride were investigated. Bi-Fe doped and undoped vanadium phosphate catalysts were used a model catalyst. XRD revealed that Bi-Fe mixture dopants led to formation of αII-VOPO₄ phase together with (VO)₂P₂O₇ as a dominant phase when the materials were heated in n-butane/air to form the final catalysts. TPR analysis showed that the reduction behaviour of Bi-Fe doped catalysts was dominated by the reduction peak assigned to the reduction of V⁵⁺ species as compared to the undoped catalyst, which gave the reduction of V⁴⁺ as the major feature. An excess of the oxygen species (O²⁻) associated with V⁵⁺ in Bi-Fe doped catalysts improved the maleic anhydride selectivity but significantly lowering the rate of n-butane conversion. The reactive pairing of V⁴⁺-O⁻ was shown to be the centre for n-butane activation. It is proposed that the availability and appearance of active oxygen species (O⁻) on the surface of vanadium phosphate catalyst is the rate determining step of the overall reaction.
AbstractList The nature and the role of oxygen species and vanadium oxidation states on the activation of n-butane for selective oxidation to maleic anhydride were investigated. Bi-Fe doped and undoped vanadium phosphate catalysts were used a model catalyst. XRD revealed that Bi-Fe mixture dopants led to formation of αII-VOPO₄ phase together with (VO)₂P₂O₇ as a dominant phase when the materials were heated in n-butane/air to form the final catalysts. TPR analysis showed that the reduction behaviour of Bi-Fe doped catalysts was dominated by the reduction peak assigned to the reduction of V⁵⁺ species as compared to the undoped catalyst, which gave the reduction of V⁴⁺ as the major feature. An excess of the oxygen species (O²⁻) associated with V⁵⁺ in Bi-Fe doped catalysts improved the maleic anhydride selectivity but significantly lowering the rate of n-butane conversion. The reactive pairing of V⁴⁺-O⁻ was shown to be the centre for n-butane activation. It is proposed that the availability and appearance of active oxygen species (O⁻) on the surface of vanadium phosphate catalyst is the rate determining step of the overall reaction.
The nature and the role of oxygen species and vanadium oxidation states on the activation of n-butane for selective oxidation to maleic anhydride were investigated. Bi-Fe doped and undoped vanadium phosphate catalysts were used a model catalyst. XRD revealed that Bi-Fe mixture dopants led to formation of αII-VOPO₄ phase together with (VO)(2)P(2)O,‡ as a dominant phase when the materials were heated in n-butane/air to form the final catalysts. TPR analysis showed that the reduction behaviour of Bi-Fe doped catalysts was dominated by the reduction peak assigned to the reduction of V⁵⁺ species as compared to the undoped catalyst, which gave the reduction of V´⁺ as the major feature. An excess of the oxygen species (O²) associated with V⁵⁺ in Bi-Fe doped catalysts improved the maleic anhydride selectivity but significantly lowering the rate of n-butane conversion. The reactive pairing of V´⁺-O was shown to be the centre for n-butane activation. It is proposed that the availability and appearance of active oxygen species (O) on the surface of vanadium phosphate catalyst is the rate determining step of the overall reaction.
The nature and the role of oxygen species and vanadium oxidation states on the activation of n -butane for selective oxidation to maleic anhydride were investigated. Bi–Fe doped and undoped vanadium phosphate catalysts were used a model catalyst. XRD revealed that Bi–Fe mixture dopants led to formation of α II -VOPO 4 phase together with (VO) 2 P 2 O 7 as a dominant phase when the materials were heated in n -butane/air to form the final catalysts. TPR analysis showed that the reduction behaviour of Bi–Fe doped catalysts was dominated by the reduction peak assigned to the reduction of V 5+ species as compared to the undoped catalyst, which gave the reduction of V 4+ as the major feature. An excess of the oxygen species (O 2− ) associated with V 5+ in Bi–Fe doped catalysts improved the maleic anhydride selectivity but significantly lowering the rate of n -butane conversion. The reactive pairing of V 4+ -O − was shown to be the centre for n -butane activation. It is proposed that the availability and appearance of active oxygen species (O − ) on the surface of vanadium phosphate catalyst is the rate determining step of the overall reaction.
The nature and the role of oxygen species and vanadium oxidation states on the activation of n-butane for selective oxidation to maleic anhydride were investigated. Bi–Fe doped and undoped vanadium phosphate catalysts were used a model catalyst. XRD revealed that Bi–Fe mixture dopants led to formation of αII-VOPO4 phase together with (VO)2P2O7 as a dominant phase when the materials were heated in n-butane/air to form the final catalysts. TPR analysis showed that the reduction behaviour of Bi–Fe doped catalysts was dominated by the reduction peak assigned to the reduction of V5+ species as compared to the undoped catalyst, which gave the reduction of V4+ as the major feature. An excess of the oxygen species (O2−) associated with V5+ in Bi–Fe doped catalysts improved the maleic anhydride selectivity but significantly lowering the rate of n-butane conversion. The reactive pairing of V4+-O− was shown to be the centre for n-butane activation. It is proposed that the availability and appearance of active oxygen species (O−) on the surface of vanadium phosphate catalyst is the rate determining step of the overall reaction.
Author Taufiq-Yap, Y. H
Hutchings, G. J
Goh, C. K
Dummer, N
Bartley, J
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Issue 3-4
Keywords Activation
Oxygen species
Vanadium phosphate
Butane oxidation
Vanadium
Maleic anhydride
Oxygen
Active site
Transition metal
Selectivity
Air
Conversion
X ray diffraction
n-Butane oxidation
Chemical reduction
Butane
Heterogeneous catalysis
Models
Oxidation
Catalyst
Language English
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CC BY 4.0
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Snippet The nature and the role of oxygen species and vanadium oxidation states on the activation of n-butane for selective oxidation to maleic anhydride were...
The nature and the role of oxygen species and vanadium oxidation states on the activation of n -butane for selective oxidation to maleic anhydride were...
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StartPage 327
SubjectTerms Activation
Anhydrides
Bismuth
Catalysis
Catalysts
Chemistry
Chemistry and Materials Science
Dependence
Exact sciences and technology
General and physical chemistry
Industrial Chemistry/Chemical Engineering
Maleic anhydride
Organometallic Chemistry
Oxidation
Oxygen
Physical Chemistry
Reduction
Selectivity
Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry
Vanadium
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Title Dependence of n-Butane Activation on Active Site of Vanadium Phosphate Catalysts
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