2017
DOI: 10.1007/s10562-017-2152-z
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An Efficient Catalyst for Light Olefins Production from CO Hydrogenation: Synergistic Effect of Zn and Ce Promoters on Performance of Co–Mn/SiO2 Catalyst

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Cited by 9 publications
(4 citation statements)
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“…This added value effect has been observed in various catalytic systems [11,[15][16][17][18][19][20][21]. For example, the co-action of Cu and K in the iron catalyst used for the CO 2 hydrogenation process [15], Na and S in the Fe-based catalyst used for Fischer-Tropsch synthesis [16,17] or Zn and Ce in a bimetallic Co-Mn system for CO hydrogenation [18]. However, it is sometimes difficult to understand the interaction between individual promoters or promoters and metal in the active phase and to explain the synergistic effect.…”
Section: Of 17mentioning
confidence: 69%
See 1 more Smart Citation
“…This added value effect has been observed in various catalytic systems [11,[15][16][17][18][19][20][21]. For example, the co-action of Cu and K in the iron catalyst used for the CO 2 hydrogenation process [15], Na and S in the Fe-based catalyst used for Fischer-Tropsch synthesis [16,17] or Zn and Ce in a bimetallic Co-Mn system for CO hydrogenation [18]. However, it is sometimes difficult to understand the interaction between individual promoters or promoters and metal in the active phase and to explain the synergistic effect.…”
Section: Of 17mentioning
confidence: 69%
“…When it occurs, the catalytic properties of a system promoted with at least two compounds are much more favourable than would result from the properties of the sum of each individually promoted system component. This added value effect has been observed in various catalytic systems [11,[15][16][17][18][19][20][21]. For example, the co-action of Cu and K in the iron catalyst used for the CO 2 hydrogenation process [15], Na and S in the Fe-based catalyst used for Fischer-Tropsch synthesis [16,17] or Zn and Ce in a bimetallic Co-Mn system for CO hydrogenation [18].…”
Section: Of 17mentioning
confidence: 90%
“…The characterization results are given in Table . The degree of reduction is calculated by Equation , which is defined as the ratio of hydrogen consumption of metal oxides to the amount of hydrogen consumption in the complete reduction process DR0.25em()%-0.6em=Total0.25emH20.25emconsumption0.25em()mmol/normalg0.25emcat.Total0.1emH20.1emfor complete reduction of catalyst0.15em()mmol/normalg0.1emcat., …”
Section: Resultsmentioning
confidence: 99%
“…The degree of reduction is calculated by Equation (4), which is defined as the ratio of hydrogen consumption of metal oxides to the amount of hydrogen consumption in the complete reduction process. [24] F I G U R E 1 XRD pattern of prepared catalyst T A B L E 1…”
Section: H 2 -Tprmentioning
confidence: 99%