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Impregnated and Co-precipitated Pd–Ga(2)O(3), Pd–In(2)O(3) and Pd–Ga(2)O(3)–In(2)O(3) Catalysts: Influence of the Microstructure on the CO(2) Selectivity in Methanol Steam Reforming
ABSTRACT: To focus on the influence of the intermetallic compound—oxide interface of Pd-based intermetallic phases in methanol steam reforming (MSR), a co-precipitation pathway has been followed to prepare and subsequently structurally and catalytically characterize a set of nanoparticulate Ga(2)O(3...
Autores principales: | , , , , , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
Springer US
2018
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Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6191075/ https://www.ncbi.nlm.nih.gov/pubmed/30393448 http://dx.doi.org/10.1007/s10562-018-2491-4 |
Sumario: | ABSTRACT: To focus on the influence of the intermetallic compound—oxide interface of Pd-based intermetallic phases in methanol steam reforming (MSR), a co-precipitation pathway has been followed to prepare and subsequently structurally and catalytically characterize a set of nanoparticulate Ga(2)O(3)- and In(2)O(3)-supported GaPd(2) and InPd catalysts, respectively. To study the possible promoting effect of In(2)O(3), an In(2)O(3)-doped Ga(2)O(3)-supported GaPd(2) catalyst has also been examined. While, upon reduction, the same intermetallic compounds are formed, the structure of especially the Ga(2)O(3) support is strikingly different: rhombohedral and spinel-like Ga(2)O(3) phases, as well as hexagonal GaInO(3) and rhombohedral In(2)O(3) phases are observed locally on the materials prior to methanol steam reforming by high-resolution transmission electron microscopy. Overall, the structure, phase composition and morphology of the co-precipitated catalysts are much more complex as compared to the respective impregnated counterparts. However, this induces a beneficial effect in activity and CO(2) selectivity in MSR. Both Ga(2)O(3) and In(2)O(3) catalysts show a much higher activity, and in the case of GaPd(2)–Ga(2)O(3), a much higher CO(2) selectivity. The promoting effect of In(2)O(3) is also directly detectable, as the CO(2) selectivity of the co-precipitated supported Ga(2)O(3)–In(2)O(3) catalyst is much higher and comparable to the purely In(2)O(3)-supported material, despite the more complex structure and morphology. In all studied cases, no deactivation effects have been observed even after prolonged time-on-stream for 12 h, confirming the stability of the systems. GRAPHICAL ABSTRACT: The presence of a variety of distinct supported intermetallic InPd and GaPd(2) particle phases is not detrimental to activity/selectivity in methanol steam reforming as long as the appropriate intermetallic phases are present and they exhibit optimized intermetallic-support phase boundary dimensions. [Image: see text] |
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