2015
DOI: 10.1039/c5cy00421g
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Metal–support interactions in surface-modified Cu–Co catalysts applied in higher alcohol synthesis

Abstract: Cu–Co-based model catalysts were prepared by a sophisticated alkali-free synthesis method and tested in the conversion of synthesis gas to higher alcohols. MoO3-coated alumina was used as the support, providing both high specific surface area and strongly interacting sites for the deposition of the active metals.

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Cited by 34 publications
(13 citation statements)
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References 36 publications
(44 reference statements)
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“…Various types of heterogeneous catalysts including Rh noble metal [11][12][13][14][15] , CoCu [16][17][18][19][20][21][22][23][24][25][26][27][28] and CuZn [29,30] mixed metals as well as hydrodesulfurization-type MoS 2 [31][32][33] were all tested for higher alcohols synthesis via CO hydrogenation. CoCu-based catalysts were found to be among the most promising ones for various reasons.…”
Section: Introductionmentioning
confidence: 99%
See 1 more Smart Citation
“…Various types of heterogeneous catalysts including Rh noble metal [11][12][13][14][15] , CoCu [16][17][18][19][20][21][22][23][24][25][26][27][28] and CuZn [29,30] mixed metals as well as hydrodesulfurization-type MoS 2 [31][32][33] were all tested for higher alcohols synthesis via CO hydrogenation. CoCu-based catalysts were found to be among the most promising ones for various reasons.…”
Section: Introductionmentioning
confidence: 99%
“…After the initial reports by IFP, a large number of patents (filed by Mobil Oil, BP and Chem Systems) [40][41][42][43] and papers [17][18][19][20]44,45] catalysts for higher alcohols saw the light of the day. More recently, such catalysts have been examined in detail [21][22][23][24][25][26][27][28][29][30][46][47][48][49][50][51][52][53][54][55][56][57][58][59][60][61][62][63] . It seems to be clear by now that the detailed catalyst formulation as well as the methods of their preparation are key to the performance for higher alcohols synthesis.…”
Section: Introductionmentioning
confidence: 99%
“…The reduction of cobalt oxide to metallic Co 0 requires higher temperatures resulting in a flat and broad peak in the range of 300-650 °C. Obviously, its reduction is favored in the presence of Cu 0 due to hydrogen spillover [34][35][36]. A degree of reduction of about 96.4% derived from the overall H2 consumption confirmed complete reduction of both Co oxide and Cu oxide up to 650 °C.…”
Section: Catalyst Activation In H2 and Comentioning
confidence: 84%
“…Therefore, the modication of F-T synthesis catalysts to synthesize low-carbon alcohols has received extensive attention for research, among which Cu-Co and Cu-Fe are the two types of catalysts widely studied. [24][25][26][27] The modied Fischer-Tropsch Cu-Co catalyst was developed by the French Petroleum Institute, and the synthesis products are mainly C1-C6 linear primary alcohols, whose product distribution is in line with the Anderson-Schulz-Flory (ASF) distribution of F-T. As to the catalytic mechanism, it is generally believed that Cu-Co catalysts for the synthesis of low-carbon alcohols have two types of active centers. Among them, Co is used for dissociative adsorption of CO to generate alkyl chains, and Cu is used for non-dissociative adsorption of CO to oxidize alkyl chains.…”
Section: Modied F-t Catalystmentioning
confidence: 99%