Sun et al., 2017 - Google Patents
Vapor-phase hydrogenation of levulinic acid and methyl levulinate to γ-valerolactone over non-noble metal-based catalystsSun et al., 2017
View PDF- Document ID
- 7150340803364180469
- Author
- Sun D
- Ohkubo A
- Asami K
- Katori T
- Yamada Y
- Sato S
- Publication year
- Publication venue
- Molecular Catalysis
External Links
Snippet
Vapor-phase hydrogenation of levulinic acid (LA) and methyl levulinate (ML) to γ- valerolactone (GVL) was performed over non-noble metal-based catalysts such as Cu/Al 2 O 3, Ni/SiO 2 and Co/SiO 2. The catalytic activity and stability of the Cu-, Ni-and Co-based …
- 239000003054 catalyst 0 title abstract description 94
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/132—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group
- C07C29/136—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. -COOH
- C07C29/147—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. -COOH of carboxylic acids or derivatives thereof
- C07C29/149—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. -COOH of carboxylic acids or derivatives thereof with hydrogen or hydrogen-containing gases
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
- C07C2523/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals of the platinum group metals
- C07C2523/44—Palladium
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/15—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
- C07C29/151—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
- C07C29/153—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases characterised by the catalyst used
- C07C29/156—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases characterised by the catalyst used containing iron group metals, platinum group metals or compounds thereof
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/02—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation
- C07C5/08—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of carbon-to-carbon triple bonds
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/32—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Sun et al. | Vapor-phase hydrogenation of levulinic acid and methyl levulinate to γ-valerolactone over non-noble metal-based catalysts | |
| Duarte et al. | Hydrodeoxygenation of 5-hydroxymethylfurfural over alumina-supported catalysts in aqueous medium | |
| Miyazawa et al. | Glycerol hydrogenolysis to 1, 2-propanediol catalyzed by a heat-resistant ion-exchange resin combined with Ru/C | |
| West et al. | Catalytic conversion of biomass-derived carbohydrates to fuels and chemicals by formation and upgrading of mono-functional hydrocarbon intermediates | |
| Guo et al. | Supported Cu catalysts for the selective hydrogenolysis of glycerol to propanediols | |
| Miyazawa et al. | Development of a Ru/C catalyst for glycerol hydrogenolysis in combination with an ion-exchange resin | |
| JP5108979B2 (en) | Direct and selective production of ethyl acetate from acetic acid using a bimetallic supported catalyst | |
| JP5611252B2 (en) | Direct and selective production of ethanol from acetic acid using a platinum / tin catalyst | |
| Akiyama et al. | Dehydration–hydrogenation of glycerol into 1, 2-propanediol at ambient hydrogen pressure | |
| CA2732366C (en) | Ethanol production from acetic acid utilizing a cobalt catalyst | |
| JP5053458B2 (en) | Direct and selective production of acetaldehyde from acetic acid using supported metal catalysts | |
| Baylon et al. | Conversion of ethanol to 1, 3-butadiene over Na doped ZnxZryOz mixed metal oxides | |
| Serrano-Ruiz et al. | Catalytic upgrading of lactic acid to fuels and chemicals by dehydration/hydrogenation and C–C coupling reactions | |
| Vasiliadou et al. | Glycerol transformation to value added C3 diols: reaction mechanism, kinetic, and engineering aspects | |
| Sun et al. | Efficient production of propylene in the catalytic conversion of glycerol | |
| Sun et al. | Selective hydrogenation of γ-valerolactone to 2-methyltetrahydrofuran over Cu/Al2O3 catalyst | |
| Pirmoradi et al. | Continuous hydrogenation of aqueous furfural using a metal-supported activated carbon monolith | |
| Li et al. | Nickel and nickel–platinum as active and selective catalyst for the maleic anhydride hydrogenation to succinic anhydride | |
| Madsen et al. | Deactivation in continuous deoxygenation of C18-fatty feedstock over Pd/Sibunit | |
| Brainer et al. | Wet oxidation of glycerol into fine organic acids: catalyst selection and kinetic evaluation | |
| Auneau et al. | Exploring the reaction conditions for Ru/C catalyzed selective hydrogenolysis of xylitol alkaline aqueous solutions to glycols in a trickle-bed reactor | |
| Onyestyák | Outstanding efficiency of indium in bimetallic catalysts for hydroconversion of bioacids to bioalcohols | |
| Li et al. | Highly active and selective Nickel–Platinum catalyst for the low temperature hydrogenation of maleic anhydride to succinic anhydride and synthesis of succinic acid at 40 C | |
| JPWO2010016462A1 (en) | Process for producing glycol and 1-propanol from glycerin | |
| Li et al. | Vapor-phase deoxydehydration of 1, 2-propanediol to form propylene over Cu-loaded H3PO4/SiO2-Al2O3 catalyst |