Partial oxidation of n-butane to maleic anhydride over VPO in a simulated circulating fluidized bed reactor
The reaction of partial oxidation of n-butane to maleic anhydride, catalyzed by VPO, was experimentally studied in a fluidized bed reactor, operated alternating oxidizing and reducing feeds, simulating in this way a circulating fluidized reactor. The influence of feed composition and oxidation/reduc...
| Autores: | , , |
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| Tipo de recurso: | artículo |
| Estado: | Versión aceptada para publicación |
| Fecha de publicación: | 2010 |
| País: | España |
| Institución: | Consejo Superior de Investigaciones Científicas (CSIC) |
| Repositorio: | DIGITAL.CSIC. Repositorio Institucional del CSIC |
| OAI Identifier: | oai:digital.csic.es:10261/377452 |
| Acceso en línea: | http://hdl.handle.net/10261/377452 https://api.elsevier.com/content/abstract/scopus_id/77649087859 |
| Access Level: | acceso abierto |
| Palabra clave: | VPO catalyst Circulating fluidized bed Fluidized bed reactor Maleic anhydride http://metadata.un.org/sdg/7 http://metadata.un.org/sdg/9 Ensure access to affordable, reliable, sustainable and modern energy for all Build resilient infrastructure, promote inclusive and sustainable industrialization and foster innovation |
| Sumario: | The reaction of partial oxidation of n-butane to maleic anhydride, catalyzed by VPO, was experimentally studied in a fluidized bed reactor, operated alternating oxidizing and reducing feeds, simulating in this way a circulating fluidized reactor. The influence of feed composition and oxidation/reduction time on butane conversion, maleic anhydride selectivity and maleic anhydride production per unit catalyst weight and time was studied. Results for the simulated circulating fluidized bed were compared with that of a conventional fluidized bed. © 2009 Elsevier B.V. All rights reserved. |
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