2014
DOI: 10.1016/j.apcatb.2014.01.003
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Corrigendum to “Selective hydrogenation of CO2 and CO to useful light olefins over octahedral molecular sieve manganese oxide supported iron catalysts” [Appl. Catal. B: Environ. 132–133 (2013) 54–61]

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Cited by 16 publications
(17 citation statements)
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“…Several promoters such as potassium, copper and manganese have been previously proposed 10,[50][51][52][53] to improve the performance of iron FT catalysts. In our work, we present a new strategy focused on the improvement of the catalytic performance of iron catalysts for FT synthesis, which is based on mobile and versatile promoters, such as bismuth.…”
Section: Versatility Of Bismuth-promoted Iron Catalysts For Ft Synthesismentioning
confidence: 99%
“…Several promoters such as potassium, copper and manganese have been previously proposed 10,[50][51][52][53] to improve the performance of iron FT catalysts. In our work, we present a new strategy focused on the improvement of the catalytic performance of iron catalysts for FT synthesis, which is based on mobile and versatile promoters, such as bismuth.…”
Section: Versatility Of Bismuth-promoted Iron Catalysts For Ft Synthesismentioning
confidence: 99%
“…4 Currently, petroleum resources continue to decrease, which raises barriers for the traditional synthesis of light olens from naphtha cracking. 5,6 To solve this problem, considerable studies on the conversion of syngas (synthesis gas, CO + H 2 ) to light olens by the Fischer-Tropsch synthesis have been reported due to the costeffective feeding stock as compared to crude oil, which is called Fischer-Tropsch to olens (FTTO). [7][8][9][10][11][12][13] CO can be connected to H 2 on the surface of the catalyst and the formation of CH x (x ¼ 1, 2, 3) takes place to convert to C n H m by C-C coupling; nally, the alkane or olen products are formed by the hydrogenation or dehydrogenation of C n H m .…”
Section: Introductionmentioning
confidence: 99%
“…26 The Co-Na-Mo catalysts supported on SiO2 and ZSM-5 show very small selectivity towards unsaturated products, probably to be related to the presence of cobalt crystallite sizes in the order of 14-16 nm as discussed above. Amongst the catalysts with cobalt crystallite sizes between 22-35 nm, the one supported on TiO2 shows the highest C2-C4 olefin selectivity, with similar olefin selectivity values shown by other reducible oxide supports such as ZrO2, CeO2 and the Al2O3.…”
Section: Effect Of Support On Co2 Conversion and Selectivitymentioning
confidence: 99%