Electrifying Ba0.5Sr0.5Co0.8Fe0.2O3-δ
[EN] Industry decarbonization requires the development of highly efficient and flexible technologies relying on renewable energy resources, especially biomass and solar/wind electricity. In the case of pure oxygen production, oxygen transport membranes (OTMs) appear as an alternative technology for...
| Autores: | , , , , , , , , |
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| Tipo de recurso: | artículo |
| Fecha de publicación: | 2024 |
| País: | España |
| Institución: | Universitat Politècnica de València (UPV) |
| Repositorio: | RiuNet. Repositorio Institucional de la Universitat Politécnica de Valéncia |
| Idioma: | inglés |
| OAI Identifier: | oai:riunet.upv.es:10251/204823 |
| Acceso en línea: | https://riunet.upv.es/handle/10251/204823 |
| Access Level: | acceso abierto |
| Palabra clave: | Oxygen permeation Oxidative dehydrogenation of ethane Oxygen transport membranes Joule effect Mixed ionic-electronic conductors Catalytic membrane reactors |
| Sumario: | [EN] Industry decarbonization requires the development of highly efficient and flexible technologies relying on renewable energy resources, especially biomass and solar/wind electricity. In the case of pure oxygen production, oxygen transport membranes (OTMs) appear as an alternative technology for the cryogenic distillation of air, the industrially-established process of producing oxygen. Moreover, OTMs could provide oxygen from different sources (air, water, CO2, etc.), and they are more flexible in adapting to current processes, producing oxygen at 700-1000 degrees C. Furthermore, OTMs can be integrated into catalytic membrane reactors, providing new pathways for different processes. The first part of this study was focused on electrification on a traditional OTM material (Ba(0.5)Sr(0.5)Co(0.8)Fe(0.2)O3(-delta)), imposing different electric currents/voltages along a capillary membrane. Thanks to the emerging Joule effect, the membrane-surface temperature and the associated O-2 permeation flux could be adjusted. Here, the OTM is electrically and locally heated and reaches 900 degrees C on the surface, whereas the surrounding of the membrane was maintained at 650 degrees C The O-2 permeation flux reached for the electrified membranes was similar to 3.7 NmL. min(-1) cm(2), corresponding to the flux obtained with an OTM non-electrified at 900 degrees C. The influence of depositing a porous Ce0.8Tb0.2O2-delta catalytic/protective layer on the outer membrane surface revealed that lower surface temperatures (830 degrees C) were detected at the same imposed electric power. Finally, the electrification concept was demonstrated in a catalytic membrane reactor (CMR) where the oxidative dehydrogenation of ethane (ODHE) was carried out. ODHE reaction is very sensitive to temperature, and here, we demonstrate an improvement of the ethylene yield by reaching moderate temperatures in the reaction chamber while the O-2 injection into the reaction can be easily fine-tuned. |
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