Study of Ni/CeO2-ZnO catalysts in the production of H2 from acetone steam reforming

Fecha de publicación

2024-02-08T18:23:25Z

2024-02-08T18:23:25Z

2019

2024-02-08T18:23:25Z

Resumen

This paper reports the study of new Ni/ZnO-based catalysts for hydrogen production from substoichiometric acetone steam reforming (ASR). The effect of CeO2 introduction is analyzed regarding the catalytic behavior and carbon deposits formation. ASR was studied at 600 °C using a steam/carbon ratio S/C = 1. Ni/xCeZnO (x = 10, 20, 30 CeO2 wt %) catalysts showed a better performance than the bare Ni/ZnO. Ni/xCeZnO generated a lower amount and less ordered carbon deposits than Ni/ZnO. The higher the CeO2 content in Ni/xCeZnO, the lower the amount of carbon deposits in the post-reaction catalyst. The highest H2 production under ASR at the experimental conditions used was achieved for the Ni/xCeZnO catalysts. In-situ DRIFTS-MS experiments under ESR conditions showed different reaction pathways over Ni/20CeZnO and Ni/ZnO catalysts.

Tipo de documento

Artículo


Versión aceptada

Lengua

Inglés

Materias y palabras clave

Carbó de coc; Catàlisi; Acetona; Coke; Catalysis; Acetone

Publicado por

Elsevier Ltd

Documentos relacionados

Versió postprint del document publicat a: https://doi.org/10.1016/j.ijhydene.2018.10.191

International Journal of Hydrogen Energy, 2019, vol. 44, p. 12628-12635

https://doi.org/10.1016/j.ijhydene.2018.10.191

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Derechos

cc-by-nc-nd (c) Elsevier Ltd, 2019

http://creativecommons.org/licenses/by-nc-nd/4.0/