2002
DOI: 10.1006/jcat.2002.3648
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The Preparation, Characterization, and Catalytic Behavior of MoVTeNbO Catalysts Prepared by Hydrothermal Synthesis

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Cited by 157 publications
(150 citation statements)
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“…Electron-accepting sites must be easily available to avoid pre-mature reduction of the adaptive binding site. This means that the number of surface locations where several active sites (if assumed that dimers are the units of active sites and not oligomers thereof) are at the same time available in the correct oxidation state will be quite low, giving a hint to the low levels of productivity [94,95] observed for such catalysts.…”
Section: Size and Functions Of Active Sitesmentioning
confidence: 99%
“…Electron-accepting sites must be easily available to avoid pre-mature reduction of the adaptive binding site. This means that the number of surface locations where several active sites (if assumed that dimers are the units of active sites and not oligomers thereof) are at the same time available in the correct oxidation state will be quite low, giving a hint to the low levels of productivity [94,95] observed for such catalysts.…”
Section: Size and Functions Of Active Sitesmentioning
confidence: 99%
“…By now, three classes of catalyst systems, VPO-type catalysts [1,2], heteropoly compounds catalysts (HPC) [3,4] and multi-component metal oxides catalysts (MMO) [5][6][7][8][9][10], have been studied for the selective oxidation of propane to acrylic acid. MMO catalysts are commonly considered to have a possibility to substitute the traditional catalysts in the existing industrial two-step process via propylene.…”
Section: Introductionmentioning
confidence: 99%
“…MMO catalysts are commonly considered to have a possibility to substitute the traditional catalysts in the existing industrial two-step process via propylene. Among those catalyst systems, Mo-V-Te-Nb oxide catalyst is the most promising one [7][8][9][10]. An appropriate MoVTeNb metal ratio is critical to the formation of catalyst active phase, according to the two patents of Ushikubo and Lin [7,8], the catalysts with metal ratio of 12 O x catalyst for propane oxidation is mainly due to its the intrinsic characteristics.…”
Section: Introductionmentioning
confidence: 99%
“…Usually the synthesis is performed at T = 448 K in nitrogen atmosphere applying a synthesis time of 48 h [23][24][25][26][27][28][29].…”
mentioning
confidence: 99%
“…López Nieto and co-workers conducted the synthesis under these conditions in a Teflon-lined stainless-steel autoclave using different metal-containing compounds and various nominal metal stoichiometries [23,24,[27][28][29]. Generally, phase mixtures including Mo 5 MO 3.33 (M = Mo, V, Nb) were obtained after heat treatment for 2 h at 873 K in nitrogen of the hydrothermally prepared precursor.…”
mentioning
confidence: 99%