Nothing Special   »   [go: up one dir, main page]

Rekha et al., 2017 - Google Patents

Continuous Hydrogenolysis of Glycerol to 1, 2-Propanediol Over Bi-Metallic Ni–Ag Supported on Γ-Al 2 O 3 Catalysts

Rekha et al., 2017

Document ID
5663234129010517979
Author
Rekha V
Raju N
Sumana C
Lingaiah N
Publication year
Publication venue
Catalysis Letters

External Links

Snippet

Continuous hydrogenolysis of glycerol was carried over bimetallic Ni–Ag supported on γ-Al 2 O 3 catalysts. These catalysts were prepared by co-impregnation method. The catalysts surface and structural properties were derived from CO chemisorption, X-ray diffraction …
Continue reading at link.springer.com (other versions)

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts 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
    • B01J23/84Catalysts 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
    • B01J23/85Chromium, molybdenum or tungsten
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/89Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
    • B01J23/8933Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals also combined with metals, or metal oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/46Ruthenium, rhodium, osmium or iridium
    • B01J23/462Ruthenium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/54Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/56Platinum group metals
    • B01J23/64Platinum group metals with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/652Chromium, molybdenum or tungsten
    • B01J23/6527Tungsten
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/03Precipitation; Co-precipitation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/0201Impregnation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/60Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by elimination of -OH groups, e.g. by dehydration
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/15Preparation 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

Similar Documents

Publication Publication Date Title
Fan et al. Pt–WOx on monoclinic or tetrahedral ZrO2: Crystal phase effect of zirconia on glycerol hydrogenolysis to 1, 3-propanediol
Rekha et al. Continuous Hydrogenolysis of Glycerol to 1, 2-Propanediol Over Bi-Metallic Ni–Ag Supported on Γ-Al 2 O 3 Catalysts
Balaraju et al. Catalytic hydrogenolysis of biodiesel derived glycerol to 1, 2-propanediol over Cu–MgO catalysts
Buntara et al. Catalyst studies on the ring opening of tetrahydrofuran–dimethanol to 1, 2, 6-hexanetriol
Jiménez-Morales et al. Hydrogenolysis of glycerol to obtain 1, 2-propanediol on Ce-promoted Ni/SBA-15 catalysts
Mane et al. Cu: Al nano catalyst for selective hydrogenolysis of glycerol to 1, 2-propanediol
Gallegos-Suarez et al. Comparative study of the hydrogenolysis of glycerol over Ru-based catalysts supported on activated carbon, graphite, carbon nanotubes and KL-zeolite
Pudi et al. Selective hydrogenolysis of glycerol to 1, 2‐propanediol over highly active copper–magnesia catalysts: reaction parameter, catalyst stability and mechanism study
US8058484B2 (en) Flexible glycerol conversion process
Yu et al. Hydrogen production by ethanol steam reforming on NiCuMgAl catalysts derived from hydrotalcite-like precursors
Xin et al. Selective hydrogenation of cinnamaldehyde with NixFe1-xAl2O4+ δ composite oxides supported Pt catalysts: CO versus CC selectivity switch by varying the Ni/Fe molar ratios
Gandarias et al. Physicochemical study of glycerol hydrogenolysis over a Ni–Cu/Al2O3 catalyst using formic acid as the hydrogen source
Pudi et al. Selective hydrogenolysis of glycerol to 1, 2-propanediol over bimetallic Cu-Ni catalysts supported on γ-Al2O3
Lin et al. Hydrogenolysis of glycerol by the combined use of zeolite and Ni/Al2O3 as catalysts: A route for achieving high selectivity to 1-propanol
Wu et al. Isobutanol synthesis from syngas over K–Cu/ZrO2–La2O3 (x) catalysts: Effect of La-loading
Bienholz et al. Prevention of catalyst deactivation in the hydrogenolysis of glycerol by Ga2O3-modified copper/zinc oxide catalysts
Zhu et al. Zn promoted Cu–Al catalyst for hydrogenation of ethyl acetate to alcohol
Wang et al. Production of hydrogen by ethanol steam reforming over nickel–metal oxide catalysts prepared via urea–nitrate combustion method
Lee et al. Vapor-phase hydrogenolysis of glycerol to 1, 2-propanediol using a chromium-free Ni-Cu-SiO2 nanocomposite catalyst
Mitta et al. Efficient Vapor‐Phase Selective Hydrogenolysis of Bio‐Levulinic Acid to γ‐Valerolactone Using Cu Supported on Hydrotalcite Catalysts
Rekha et al. Selective Hydrogenolysis of Glycerol Over Cu–ZrO 2–MgO Catalysts
Liu et al. Glycerol hydrogenolysis to 1, 2-propanediol by Cu/ZnO/Al 2 O 3 catalysts
Pandey et al. Production of propylene glycol (propane-1, 2-diol) in vapor phase over Cu–Ni/γ-Al 2 O 3 catalyst in a down flow tubular reactor: Effect of catalyst calcination temperature and kinetic study
Mitta et al. A highly active dispersed copper oxide phase on calcined Mg9Al2. 7-Ga2. 3O2 catalysts in glycerol hydrogenolysis
Li et al. Hydrogenolysis of glycerol to 1, 2-propanediol on copper core-porous silica shell-nanoparticles