2013
DOI: 10.1016/j.cattod.2013.03.004
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Fischer–Tropsch synthesis: Activity of metallic phases of cobalt supported on silica

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Cited by 151 publications
(117 citation statements)
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“…Gnanamani et al [83] produced hcp (hexagonal closepacked) and fcc (face-centred cubic) cobalt metal particles over silica support by employing different pre-treatments and observed higher carbon cobalt dispersion (5.06% in the case of hcp and 3.84% in the case of fcc) for the catalyst containing the hcp metallic phase; and subsequently higher carbon monoxide conversion (about 28 mol%) was achieved in this study, compared to that of fcc. Since the cobalt catalyst used in Fischer-Tropsch synthesis is expensive, hence, Loosdrecht et al [84] investigated the oxidation of nano-sized metallic cobalt during realistic F-T synthesis to cobalt oxide and concluded that this type of oxidation is independent of the support materials and could prevent the correct combination of reactor partial pressure of H 2 O and H 2 (P H2O /P H2 ).…”
Section: Overview Of Previous Work Regarding the Fischer-tropsch Synsupporting
confidence: 51%
“…Gnanamani et al [83] produced hcp (hexagonal closepacked) and fcc (face-centred cubic) cobalt metal particles over silica support by employing different pre-treatments and observed higher carbon cobalt dispersion (5.06% in the case of hcp and 3.84% in the case of fcc) for the catalyst containing the hcp metallic phase; and subsequently higher carbon monoxide conversion (about 28 mol%) was achieved in this study, compared to that of fcc. Since the cobalt catalyst used in Fischer-Tropsch synthesis is expensive, hence, Loosdrecht et al [84] investigated the oxidation of nano-sized metallic cobalt during realistic F-T synthesis to cobalt oxide and concluded that this type of oxidation is independent of the support materials and could prevent the correct combination of reactor partial pressure of H 2 O and H 2 (P H2O /P H2 ).…”
Section: Overview Of Previous Work Regarding the Fischer-tropsch Synsupporting
confidence: 51%
“…This may provide new insight for designing better catalyst; it is, however, important to note that the metalreactant/intermediate interaction and metal-support interaction may lead to rearrangement of the surface, which means that the dominating surfaces for hcp Co and fcc Co may change and correspondingly effect the mechanism. Moreover, whether the hcp or fcc phase is dominating in FTS depends on the activation conditions [134,135] and the rearrangement of the surface during real FT reaction condition has been demonstrated by both experimental and theoretical methods [136,137]. It is therefore hard to verify which phase (i.e.…”
Section: Co Activationmentioning
confidence: 99%
“…Despite the different proposals regarding the CO activation mechanism, it is agreed that hydrogenassisted CO activation is more kinetically favorable on ideal Co (0001). It is reported that hcp Co catalysts show higher FTS activity than fcc Co [134,135,[138][139][140][141]. Moreover, the larger sized Co catalysts, exposing mainly Co (0001) facets, exhibit higher FTS intrinsic reactivity compared to the smaller sized Co catalysts below 6 nm, possibly because the latter has strongly bonded carbon and oxygen surface species acting as site blocking species, and small particles may also be easily oxidized by the water vapor [6,92,142], suggesting a large contribution of Co (0001) to the reaction under reaction condition.…”
Section: Co Activationmentioning
confidence: 99%
“…Surface defect sites such as kinks and steps have beeen shown via DFT calculations to allow carbon monoxide (CO) and other gas molecules to bind to the site more easily [41]. The high binding energy possibly encourages CO dissociation and consequently increases the FTS turnover rate [42].…”
mentioning
confidence: 99%