1991
DOI: 10.1016/0926-860x(91)85002-f
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Selective hydrogenolysis of methyl and ethyl acetate in the gas phase on copper and supported Group VIII metal catalysts

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Cited by 60 publications
(27 citation statements)
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“…Moreover, it has been proved that Cu/ZnO/SiO 2 catalysts are competitive against industrial Cu–Cr . It has been suggested that the anionic vacancies in ZnO are able to increase the electronic density of copper or that ZnO allows for the activation and storage of H 2 by spillover . Besides Cr and Zn, other promoters for Cu‐based catalysts have been mentioned in patents and the open literature.…”
Section: Catalystsmentioning
confidence: 99%
See 1 more Smart Citation
“…Moreover, it has been proved that Cu/ZnO/SiO 2 catalysts are competitive against industrial Cu–Cr . It has been suggested that the anionic vacancies in ZnO are able to increase the electronic density of copper or that ZnO allows for the activation and storage of H 2 by spillover . Besides Cr and Zn, other promoters for Cu‐based catalysts have been mentioned in patents and the open literature.…”
Section: Catalystsmentioning
confidence: 99%
“…Besides Cr and Zn, other promoters for Cu‐based catalysts have been mentioned in patents and the open literature. The addition of Mn on Cu/ZnO/Al 2 O 3 , Cu–Cr and unsupported copper catalysts with multiple promoters has been reported to increase the activity of the catalysts and/or the selectivity towards hydrogenolysis and hydrogenation. Manganese, iron, magnesium, zinc, silica‐supported copper and cobalt have also been tested as additives.…”
Section: Catalystsmentioning
confidence: 99%
“…Methanol can also be carbonylated to methyl acetate, but deactivation of the catalyst by the generated water occurs. The hydrogenation of acetates is a well-known process for which different catalysts have been developed [2][3][4][12][13][14]. In this work, data from various recent developments have been considered: (i) for the hydrocarbonylation cases a combination of a carbonylation (H-Mordenite) and a hydrogenation (Cu-ZnO) catalyst is used.…”
Section: Conceptual Design Of Alternativesmentioning
confidence: 99%
“…The hot mixture is flown through a catalytic bed where the catalyst CuO/Cr 2 O 3 or CuO/ZnO/Al 2 O 3 catalyst is placed. The CuO is reduced with H 2 /N 2 mixtures prior to adding any methyl acetate (Claus et al, 1991 The GHSV (based on H 2 ) of the reaction is comprised between 1,000 and 2,000 h -1 and the methyl acetate conversion reached 95%, with a slightly higher selectivity towards ethanol.…”
Section: Methyl Acetate Hydrogenationmentioning
confidence: 99%