2017
DOI: 10.1016/j.jcat.2017.04.021
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Ag addition to CuO-ZrO 2 catalysts promotes methanol synthesis via CO 2 hydrogenation

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Cited by 109 publications
(85 citation statements)
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“…It is clear that all the catalysts show broad reduction peaks with a shoulder peak. The shoulder peak at low temperature is assignable to the reduction of highly dispersed CuO, and the reduction peak at high temperature can be attributed to the reduction of bulk CuO . For the CZA catalyst, the reduction peak appears at 265 °C.…”
Section: Resultsmentioning
confidence: 99%
“…It is clear that all the catalysts show broad reduction peaks with a shoulder peak. The shoulder peak at low temperature is assignable to the reduction of highly dispersed CuO, and the reduction peak at high temperature can be attributed to the reduction of bulk CuO . For the CZA catalyst, the reduction peak appears at 265 °C.…”
Section: Resultsmentioning
confidence: 99%
“…Therefore, the catalyst performance depends on the right "deal" between the two catalytic functionalities [3,38,45,46,[49][50][51].…”
Section: Discussionmentioning
confidence: 99%
“…normalized yield at the varying of MSA/SAR discloses the structure-activity relationship of these catalytic materials, and at the same time, reflects the effect of chemical composition. In addition, the existence of a maximum value of methanol yield, which should be achieved at 5.0 MPa at an "ideal" ratio of MSA/SAR near to 0.3, clearly signs the need of a perfect synergism between the two catalytic functionalities, available through a proper design of the catalyst [51][52][53][54].…”
Section: Discussionmentioning
confidence: 99%
“…So far, various catalysts for this reaction, such as Cu/ZrO 2 , Cu‐Ag/ZrO 2 , Cu/ZrO 2 /SiO 2 , Cu/ZnO/ZrO 2 , Cu/CeO 2 /TiO 2 , MnO x /m‐CoO x , InO 2 /ZrO 2 , Cu‐In/SiO 2 , Ni‐Ga/SiO 2 , ZnO/ZrO 2 , Pd/ZnO, Pd‐Cu/SiO 2 , and Cu/ZnO/Al 2 O 3 , have been proposed. Among them, the Cu/ZrO 2 catalyst would be a promising candidate because of its activity and selectivity for CO 2 hydrogenation to methanol (S. Tada et al, unpublished data) …”
Section: Introductionmentioning
confidence: 99%
“…In CO 2 hydrogenation to methanol (CO 2 + 3H 2 → CH 3 OH + H 2 O) by Cu/ZrO 2 catalyst, the interface of Cu‐ZrO 2 is considered the active site . In contrast, the metallic Cu surface is known as an active center for direct reduction of CO 2 to undesirable CO via reverse water gas shift reaction (CO 2 + H 2 → CO + H 2 O) . Thus, smaller Cu particles on ZrO 2 are more favorable for selective methanol generation via CO 2 hydrogenation because of the higher ratio of the interface of Cu‐ZrO 2 sites to the metallic Cu sites .…”
Section: Introductionmentioning
confidence: 99%