Comparison of the catalytic performance of V2O5/γ-Al2O3 in the oxidehydrogenation of propane to propylene in different reactor configurations: i) packed-bed reactor, ii) monolith-like reactor and iii) Catalytic Membrane Reactor
- 1 May 1996
- journal article
- Published by Elsevier in Chemical Engineering Science
- Vol. 51 (10) , 1817-1826
- https://doi.org/10.1016/0009-2509(96)00040-1
Abstract
No abstract availableKeywords
This publication has 18 references indexed in Scilit:
- Oxidative Dehydrogenation of Isobutane over Monoliths at Short Contact TimesJournal of Catalysis, 1995
- The oxidative dehydrogenation of ethane and propane as an alternative way for the production of light olefinsCatalysis Today, 1995
- Effect of pressure on three catalytic partial oxidation reactions at millisecond contact timesCatalysis Letters, 1995
- The porous-wall ceramic membrane reactor: an inherently safer contacting device for gas-phase oxidation of hydrocarbonsJournal of Loss Prevention in the Process Industries, 1995
- Monoliths in Heterogeneous CatalysisCatalysis Reviews, 1994
- Oxidative Dehydrogenation of Propane on γ-Al2O3 Supported Vanadium OxidesJournal of Catalysis, 1994
- The selective oxidative dehydrogenation of propane on vanadium aluminophosphate catalystsCatalysis Letters, 1993
- Physicochemical characterization of V-silicaliteThe Journal of Physical Chemistry, 1992
- Catalytic and Electrocatalytic Methane Oxidation with Solid Gxide MembranesCatalysis Reviews, 1991
- Selective oxidative dehydrogenation of propane over V$z.sbnd;Mg$z.sbnd;O catalystsJournal of Catalysis, 1988