Reduction potentials of H3+PMo12–V O40 and H6+P2Mo18−V O62 heteropolyacid (HPA) catalysts and their catalytic activity for the vapor-phase oxidative dehydrogenation of isobutyric acid

2008 ◽  
Vol 9 (2) ◽  
pp. 293-298 ◽  
Author(s):  
Dong Ryul Park ◽  
Heesoo Kim ◽  
Ji Chul Jung ◽  
Sang Hee Lee ◽  
In Kyu Song
Keyword(s):  
Catalytic Activity ◽  
Oxidative Dehydrogenation ◽  
Vapor Phase ◽  
Isobutyric Acid ◽  
Reduction Potentials

Effects of valence states of iron in iron phosphates on the catalytic activity in oxidative dehydrogenation of isobutyric acid

1994 ◽  
Vol 24 (3-4) ◽  
pp. 355-362 ◽  
Author(s):  
Mamoru Ai ◽  
Etsuhiro Muneyama ◽  
Atsuhiro Kunishige ◽  
Kyoji Ohdan
Keyword(s):  
Catalytic Activity ◽  
Oxidative Dehydrogenation ◽  
Isobutyric Acid ◽  
Iron Phosphates ◽  
Valence States

scholarly journals Role of CO2 During Oxidative Dehydrogenation of Propane Over Bulk and Activated-Carbon Supported Cerium and Vanadium Based Catalysts

2021 ◽  
Author(s):  
Petar Djinović ◽  
Janez Zavašnik ◽  
Janvit Teržan ◽  
Ivan Jerman
Keyword(s):  
Catalytic Activity ◽  
Activated Carbon ◽  
Oxidative Dehydrogenation ◽  
Active Phase ◽  
Lattice Oxygen ◽  
Chemisorbed Oxygen ◽  
Catalytically Active ◽  
Temperature Programmed ◽  
Propane Cracking

AbstractCeO2, V2O5 and CeVO4 were synthesised as bulk oxides, or deposited over activated carbon, characterized by XRD, HRTEM, CO2-TPO, C3H8-TPR, DRIFTS and Raman techniques and tested in propane oxidative dehydrogenation using CO2. Complete oxidation of propane to CO and CO2 is favoured by lattice oxygen of CeO2. The temperature programmed experiments show the ~ 4 nm AC supported CeO2 crystallites become more susceptible to reduction by propane, but less prone to re-oxidation with CO2 compared to bulk CeO2. Catalytic activity of CeVO4/AC catalysts requires a 1–2 nm amorphous CeVO4 layer. During reaction, the amorphous CeVO4 layer crystallises and several atomic layers of carbon cover the CeVO4 surface, resulting in deactivation. During reaction, V2O5 is irreversibly reduced to V2O3. The lattice oxygen in bulk V2O5 favours catalytic activity and propene selectivity. Bulk V2O3 promotes only propane cracking with no propene selectivity. In VOx/AC materials, vanadium carbide is the catalytically active phase. Propane dehydrogenation over VC proceeds via chemisorbed oxygen species originating from the dissociated CO2. Graphic Abstract

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