2019
DOI: 10.1016/j.jcat.2019.09.024
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CO2 hydrogenation to methanol over Cu-In intermetallic catalysts: Effect of reduction temperature

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Cited by 118 publications
(82 citation statements)
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“…4a and Figure S17a), which con rmed that isolated Cu 1 -O 3 active sites in Cu/ZrO 2 were really stable. However, the local Cu particles with 0.21nm spacing for Cu (111) planes 15,48,50,51 detected in used CAZ-15 by HRTEM (Fig. 4b, Figure S17b) revealed that Cu species were partially aggregated and reduced during the catalytic process, consistent with the XPS results (Fig.…”
Section: Resultssupporting
confidence: 82%
See 1 more Smart Citation
“…4a and Figure S17a), which con rmed that isolated Cu 1 -O 3 active sites in Cu/ZrO 2 were really stable. However, the local Cu particles with 0.21nm spacing for Cu (111) planes 15,48,50,51 detected in used CAZ-15 by HRTEM (Fig. 4b, Figure S17b) revealed that Cu species were partially aggregated and reduced during the catalytic process, consistent with the XPS results (Fig.…”
Section: Resultssupporting
confidence: 82%
“…3. In comparison to the CAZ-15, the absence of Cu 2p satellite peaks between 940eV and 945eV implied that no Cu 2+ species exited in the fresh and used CAZ-1 catalysts 15,44 . Identical peaks situated at 932.9eV between Cu 0 (932.4eV) and Cu 2+ (934.6eV) were observed in CAZ-1 and CAZ-1-U (U: used), indicating the Cu species were at cationic Cu δ+ state 31,45 .…”
Section: Resultsmentioning
confidence: 97%
“…89 Shi et al found that the Cu 11 In 9 phase is formed by controlled reduction of CuO-In 2 O 3 mixed oxides, and the synergy between Cu 11 In 9 and In 2 O 3 gives a CH 3 OH STY of 0.2 g MeOH g cat –1 h –1 with a selectivity of 80.5% at CO 2 conversion of 11.4% under 280 °C, 3.0 MPa, 7500 mL g –1 h –1 , and H 2 /CO 2 = 3. 69 Bavykina et al combined Co and In 2 O 3 to prepare In@Co catalysts, which significantly enhanced methanol productivity due to the formation of Co-supported In 2 O 3– x films. The CH 3 OH STY is as high as 0.86 g MeOH g cat –1 h –1 with above 80% selectivity and ∼12% conversion at 300 °C, 5.0 MPa, 27 500 mL g –1 h –1 , and H 2 /CO 2 = 4.…”
Section: Co 2 Hydrogenation To Methanolmentioning
confidence: 99%
“…[261][262][263] The production of H 2 O enhances also the sintering of the catalyst. [70][71][72][73][74]263 To overcome these challenges, different support materials, which can promote structural and electronic properties and stabilize smaller Cu particles, 264 were investigated, including ZrO 2 , 265,266 La 2 O 3 , 267 MoC 2 , 267 CeO 2 , 268 and La 2 O 2 CO 3 (ref. 267) and ZnO-ZrO 2 .…”
Section: Co 2 Hydrogenation To Methanolmentioning
confidence: 99%