2018
DOI: 10.1016/j.jcat.2017.12.022
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Effect of different alumina supports on performance of cobalt Fischer-Tropsch catalysts

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Cited by 62 publications
(20 citation statements)
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“…The MA was used as the support material for Fischer−Tropsch synthesis and CO 2 hydrogenation. 24,25 Herein, the four MA samples are prepared by varying the molar H 2 O/AIP ratio (r) such as 2:1, 5:1, 10:1, and 15:1 (denoted as MA-w2, MA-w5, MA-w10, and MA-w15, respectively), and used as a support for Pt loading of 1 wt %. The so-obtained Pt catalysts are tested in the HDO of palm oil under one of the conditions that we reported recently.…”
Section: ■ Introductionmentioning
confidence: 99%
See 1 more Smart Citation
“…The MA was used as the support material for Fischer−Tropsch synthesis and CO 2 hydrogenation. 24,25 Herein, the four MA samples are prepared by varying the molar H 2 O/AIP ratio (r) such as 2:1, 5:1, 10:1, and 15:1 (denoted as MA-w2, MA-w5, MA-w10, and MA-w15, respectively), and used as a support for Pt loading of 1 wt %. The so-obtained Pt catalysts are tested in the HDO of palm oil under one of the conditions that we reported recently.…”
Section: ■ Introductionmentioning
confidence: 99%
“…The original synthesis was developed by Huang et al , and further studied by Xie et al The pore structure and morphology of the prepared MA were controlled by the molar ratio of water to aluminum alkoxide because the added water could determine the hydrolysis rate and the produced alcohol was able to change the morphology of boehmite precursor. The MA was used as the support material for Fischer–Tropsch synthesis and CO 2 hydrogenation. , Herein, the four MA samples are prepared by varying the molar H 2 O/AIP ratio ( r ) such as 2:1, 5:1, 10:1, and 15:1 (denoted as MA-w2, MA-w5, MA-w10, and MA-w15, respectively), and used as a support for Pt loading of 1 wt %. The so-obtained Pt catalysts are tested in the HDO of palm oil under one of the conditions that we reported recently .…”
Section: Introductionmentioning
confidence: 99%
“…Alumina supported catalysts have been synthesised using a wet co-impregnation method similar to the one documented in the literature for iron 39 , cobalt 40 and palladium 41 precursors. The bimetallic catalysts were prepared with three salts, purchased from…”
Section: Catalyst Preparationmentioning
confidence: 99%
“…Despite its higher cost, supported cobalt is preferred over iron catalysts for the FT reaction when the emphasis is on making fuels, due to its high per pass activity, high C5+ selectivity, longer catalyst lifetime, low oxygenate and CO2 selectivity and at present it accounts for a combined estimated world production capacity of 250 000 barrels per day. [5][6][7][8][9] Supporting cobalt on metal oxides usually achieves high dispersions, but the for-mation of hard-to-reduce small Co nanoparticles and mixed compounds (such as Co2AlO4, CoTiO4 or Co2SiO4) can result in under utilization of Co because of the strong metal-support interactions associated with these materials.…”
Section: Introductionmentioning
confidence: 99%