2007
DOI: 10.1016/j.jcat.2007.03.002
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Cobalt dispersion, reducibility, and surface sites in promoted silica-supported Fischer–Tropsch catalysts

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Cited by 189 publications
(115 citation statements)
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“…Mauldin et al [25] reported that rhenium promotion increased cobalt oxide dispersion during preparation of Co/TiO 2 supported catalysts. Our previous report [45] also indicates that the presence of noble metals (Ru, Re) enhances cobalt oxide dispersion in silica supported catalysts. One of the reasons responsible of higher cobalt oxide dispersion in the catalysts promoted with noble metals could be related to a higher concentration of cobalt oxide nucleation and crystallization sites.…”
Section: Cobalt Dispersionmentioning
confidence: 77%
“…Mauldin et al [25] reported that rhenium promotion increased cobalt oxide dispersion during preparation of Co/TiO 2 supported catalysts. Our previous report [45] also indicates that the presence of noble metals (Ru, Re) enhances cobalt oxide dispersion in silica supported catalysts. One of the reasons responsible of higher cobalt oxide dispersion in the catalysts promoted with noble metals could be related to a higher concentration of cobalt oxide nucleation and crystallization sites.…”
Section: Cobalt Dispersionmentioning
confidence: 77%
“…The incipient wetness occurs when all pores of the support are filled with the liquid and there is no excess moisture, over and above the liquid required to fill the pores. Our previous works [15,16] have shown that cobalt deposition on silica or alumina using aqueous incipient wetness impregnation with cobalt nitrate results in formation of mononuclear cobalt complexes. Figure 1 displays data obtained by Xray absorption spectroscopy for impregnated and dried cobalt alumina and silica supported catalysts.…”
Section: Structure Of Cobalt Species In Impregnated Catalystsmentioning
confidence: 99%
“…Active sites in cobalt based catalysts are cobalt metal nanoparticles and several studies have shown positive correlations between cobalt dispersion and FTS activity and hydrocarbon selectivity (Iglesia, 1997;Girardon et al, 2007). Thus, maximizing cobalt dispersion on the support is a key objective in the design of Co-based catalysts (Khodakov, 2009).…”
Section: Introductionmentioning
confidence: 99%