2021
DOI: 10.1021/acssuschemeng.1c05609
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Effect of Precursors of Fe-Based Fischer–Tropsch Catalysts Supported on Expanded Graphite for CO2 Hydrogenation

Abstract: Expanded graphite as a type of hydrophobic functional carbon material was innovatively selected as support for Fe-based Fischer–Tropsch catalysts. Through catalytic activity evaluation, ferric ammonium citrate was selected as the most suitable iron precursor for expanded graphite among ferric nitrate, ferric ammonium oxalate, ferric citrate, and ferric ammonium citrate. The catalyst with ferric ammonium citrate as the precursor and expanded graphite as support achieved the best CO2 hydrogenation performance wi… Show more

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Cited by 18 publications
(7 citation statements)
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“…[ 117 ] Furthermore, 3D carbonaceous frameworks may enable the confinement of Fe actives sites, tuning deposit size and dispersion, which can be preserved by framework stability under reducing environments to restrict Fe sintering. [ 118,119 ]…”
Section: Catalyst Designmentioning
confidence: 99%
See 1 more Smart Citation
“…[ 117 ] Furthermore, 3D carbonaceous frameworks may enable the confinement of Fe actives sites, tuning deposit size and dispersion, which can be preserved by framework stability under reducing environments to restrict Fe sintering. [ 118,119 ]…”
Section: Catalyst Designmentioning
confidence: 99%
“…[117] Furthermore, 3D carbonaceous frameworks may enable the confinement of Fe actives sites, tuning deposit size and dispersion, which can be preserved by framework stability under reducing environments to restrict Fe sintering. [118,119] Wu et al explored honeycomb-structured graphene (HSG) as a support framework for K-promoted Fe catalysts. In their study, a 1.5 wt% K loading on Fe 3 O 4 supported by HSG (FeK1.5/HSG) produced a light olefin selectivity of 59% with a CO 2 conversion of 46% and a Fe time yield (FTY) of 123 μmol CO2 g Fe À1 s À1 .…”
Section: Porous Carbon Frameworkmentioning
confidence: 99%
“…The results indicate that the formation of Fe 3 C was inhibited during CO 2 hydrogenation, which could explain the high selectivity of CO. The reasons for the promotion of CO 2 conversion, O/P ratio, and [17] 320 2.5 10000 43 15.7 22.8 61.5 / Fe2Zn1Al1 [35] 350 1.5 15000 34.5 27.9 24.55 47.55 nanoparticle FeZnK-NC [36] 320 3.0 7200 34.6 21.2 19.1 59.7 hollow sphere NaÀ Zn-Fe [37] 340 2.5 15000 38 15 15.29 69.71 nanoparticle Fe/C-KOH [38] 320 1.0 2400 34.6 20.7 15.51 63.79 nanoparticle FeNa/EG-A [39] 320 3.0 2000 42.4 8.3 13.74 77.96 film Note: T: reaction temperature (°C), P: reaction pressure (MPa), GHSV: gas hour space velocity (ml • g cat À 1 • h À 1 ), C: CO 2 conversion (%), S: products selectivity (%). The mole ratio of H 2 and CO 2 in the reaction process over all above catalysts was set as 3 : 1.…”
Section: Co 2 Hydrogenation Mechanism Investigationmentioning
confidence: 99%
“…The authors have cited additional references within the Supporting Information. [62][63][64][65][66][67][68][69][70][71]…”
Section: Supporting Informationmentioning
confidence: 99%