Reforming of biomass-derived producer gas using toluene as model tar: Deactivation and regeneration studies in Ni and K-Ni catalysts

Within the syngas production from biomass gasification, tar removal constitutes a chief issue to overcome for advanced catalytic systems. This work investigates the performance of Ni and Ni–K catalysts for reforming of derived-biomass producer gas using toluene as model tar. At 750 °C and 60Lg−1h−1,...

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Detalles Bibliográficos
Autores: Azancot Luque, Lola de las Aguas, González Castaño, Míriam, Bobadilla Baladrón, Luis Francisco, Centeno Gallego, Miguel Ángel, Odriozola Gordón, José Antonio
Tipo de recurso: artículo
Estado:Versión aceptada para publicación
Fecha de publicación:2024
País:España
Institución:Universidad de Sevilla (US)
Repositorio:idUS. Depósito de Investigación de la Universidad de Sevilla
OAI Identifier:oai:dnet:idus________::d8888a1c6ec5498b0f0373bc80b0a6e3
Acceso en línea:https://hdl.handle.net/11441/184575
https://doi.org/10.1016/j.envres.2024.118210
Access Level:acceso abierto
Palabra clave:Biomass-derived producer gas reforming
Catalyst deactivation
Catalyst regeneration
Nickel-potassium catalyst
Descripción
Sumario:Within the syngas production from biomass gasification, tar removal constitutes a chief issue to overcome for advanced catalytic systems. This work investigates the performance of Ni and Ni–K catalysts for reforming of derived-biomass producer gas using toluene as model tar. At 750 °C and 60Lg−1h−1, the stability test (70 h) revealed stable performances (CO2, CH4 and C7H8 conversions of 60, 95 and 100%, correspondingly) uniquely for the Ni–K catalyst. Although the efficient protection towards coking let by K was demonstrated, TPO studies over the post-reacted systems still evidenced the presence of carbon deposits for both samples. Conducting three successive reaction/regeneration cycles with different gasifying agents (air, steam and CO2) at 800 °C for 1h, the capability towards regeneration of both catalytic systems was assessed and the spent catalysts were characterized by XRD, SEM and TEM. While none of the regeneration treatments recovered the performance of the unpromoted catalyst, the Ni–K catalysts demonstrated the capability of being fully regenerated by air and CO2 and exhibited analogous catalytic performances after a series of reaction/regeneration cycles. Hence, it is proved that the addition of K into Ni catalysts not only enhances the resistance against deactivation but enables rather facile regenerative procedures under certain atmospheres (air and CO2).