2012
DOI: 10.1016/j.apcata.2012.09.035
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Effect of catalyst preparation conditions on the performance of eggshell cobalt/SiO2 catalysts for Fischer–Tropsch synthesis

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Cited by 22 publications
(30 citation statements)
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“…Gaderzi et al [63] examined the effect of calcination conditions on the performance of a cobalt/silica catalyst and also considered the metal crystallites distribution affected by solvent, during catalyst preparation via solution impregnation; they achieved higher active surface area and better dispersed metal, in the case of alcohol as a primary solvent compared to water. Song et al [64] considered the effect of support pore size on catalyst characterization and its activity in the F-T hydrogenation process; and concluded higher activity and productivity for the catalyst with pore sizes ranging 6-10 nm.…”
Section: Catalyst Carrier Materialsmentioning
confidence: 99%
“…Gaderzi et al [63] examined the effect of calcination conditions on the performance of a cobalt/silica catalyst and also considered the metal crystallites distribution affected by solvent, during catalyst preparation via solution impregnation; they achieved higher active surface area and better dispersed metal, in the case of alcohol as a primary solvent compared to water. Song et al [64] considered the effect of support pore size on catalyst characterization and its activity in the F-T hydrogenation process; and concluded higher activity and productivity for the catalyst with pore sizes ranging 6-10 nm.…”
Section: Catalyst Carrier Materialsmentioning
confidence: 99%
“…This is particularly important for reactions where diffusional limitations strongly affect the conversion, when striving to improve the selectivity to a primary product or for high temperature reactions, where proper heat transport in the catalyst layer is required [31]. There is a large number of reactions where the importance of having an egg-shell distribution has already been recognized: Fisher-Tropsch synthesis [40], selective oxidation reactions [31] (e.g. production of acrolein from propene and of phthalic anhydride from o-xylene), volatile organic compounds abatement [41], purification of automobile exhaust gases [42,43], selective hydrogenation of pyrolysis gasoline [44], and autothermal decomposition of liquid hydrocarbons on NiO/ɣ-Al 2 O 3 [45].…”
Section: Introductionmentioning
confidence: 99%
“…Both of these distributions are sought when the catalyst surface is prone to deactivation through poisoning or abrasion mechanisms [38] and for reactions that are negative order in reactant concentration [39]. The egg-shell distribution is characterized by having a thin active phase profile in the outer-shell of the support body [31,40]. This is particularly important for reactions where diffusional limitations strongly affect the conversion, when striving to improve the selectivity to a primary product or for high temperature reactions, where proper heat transport in the catalyst layer is required [31].…”
Section: Introductionmentioning
confidence: 99%
“…at approximately 493 K (ΔT ≈ 20K) 6,14 . Likewise, there are conflicting 4 arguments on whether an eggshell catalyst design improves both the selectivity and activity, however, it 5 is generally accepted that selectivity does improves with egg-shell morphology (as discussed in Section 2) 6 1,9 . Here, we develop a strategy to identify the ideal eggshell thickness for a given set of process 7…”
mentioning
confidence: 96%
“…active material needs to be deposited close to the surface. Prior 38 work by the authors has shown that a slab model is adequate for characterizing thin egg-shell coatings 39 whereas the sphere model is better at for FTS catalysts for a thicker shell 1 . Under a typical fixed bed 1 reactor operation, using cobalt catalyst, the preference towards eggshell design becomes debatable since 2 the operational envelope is very narrow e.g.…”
mentioning
confidence: 98%