Abstract:
A process for producing an exhaust-gas-purifying catalyst includes the steps of immersing a porous support into a solution including a noble metal catalyst ingredient, thereby preparing a support with a noble metal catalyst ingredient loaded thereon, and thermally treating the noble-metal-catalyst-ingredient-loaded support at a temperature of 800 °C or more in non-oxidizing atmosphere. In the thermally-treating step, the noble metal catalyst ingredient is prevented from being oxidized to its oxide, and accordingly it is inhibited from migrating in vapor phase. Further, in the thermally-treating step, pores of the porous support are contracted so that they surround the noble metal catalyst ingredient closely therein. All in all, the noble metal catalyst ingredient is prevented from sintering. Thus, the resulting exhaust-gas-purifying catalyst is of superb heat-resistance, and it can be applied to elevated temperatures of 800 °C or more in fuel-lean atmosphere.
Abstract:
A continuous impregnation process for the preparation of a heterogeneous catalyst. A catalytic metal, or metals, is composited with a porous solids support component via the steps of: (i) forming a slurry of porous, particulate solids dispersed in an organic, or hydrocarbon solvent, preferably an organic, or hydrocarbon solvent which forms an azeotrope with water, (ii) adding, in aqueous solution, preferably continuously, one or more of a salt, acid, or compound of the catalytic metal, or metals, which is insoluble in the organic, or hydrocarbon solvent to which it is added; the aqueous solution contacting the porous, particulate support solids wicking into the pores to disperse the salt, acid or compound of the catalytic metal, or metals therein, (iii) stirring, preferably vigorously and continuously, the slurry containing the porous, particulate solids, water, and salt, acid, or compound of the catalytic metal, or metals, and (iv) distilling at a temperature sufficient to vaporize and remove the water from the support component, and slurry, to leave the catalytic metal, or metals, component deposited within the pores of the support component of the catalyst. The catalyst is next recovered, and calcined.
Abstract:
The invention concerns a powder-coating process and device, plus a coating powder for use in the process, the process calling for a suspension of the coating powder to be atomized and sprayed on to the surface to be coated, (1) the powder being suspended in a liquefied gas which is kept liquefied under a pressure of at the most 20 bar and (2) the liquid gas being allowed to vaporize before, during or after the suspension is atomized.
Abstract:
A method of preparing a catalyst particularly useful in the reaction of ethylene, oxygen and acetic acid in the vapor phase to form vinyl acetate comprises impregnating a porous support with water soluble salts of palladium and gold, fixing the palladium and gold on the support as water insoluble compounds by immersing the impregnated support in a reactive solution and tumbling the impregnated support in the reactive solution for at least 1/2 hour to begin precipitation of the insoluble compounds and completing precipitation of the insoluble compounds on the support and reducing the insoluble compounds to free palladium and gold. The catalysts prepared in this manner have been shown to provide improvement with respect to reduced selectivity to CO2 during the vinyl acetate forming reaction.
Abstract:
L'invention concerne un procédé d'hydrogénation avec un catalyseur, comprenant au moins un support, au moins un métal de la famille du groupe VIII, au moins un métal additionnel M choisi parmi le germanium, l'étain, le plomb, le gallium, l'indium, le titane, le fer, le molybdène, le tungstène, le rhénium ou le thallium, catalyseur préparé par introduction d'au moins un composé organique du métal M dilué, in-situ dans le réacteur où sera ensuite traitée la charge hydrocarbonée ou dans un préréacteur directement en contact avec ledit réacteur. Le catalyseur préparé selon l'invention peut également renfermer un halogène ou un sulfuride.
Abstract:
Catalyseur à base d'un support poreux minéral ou organique et du mélange équimolaire constitué par les acides trifluorométhanesulfonique et sulfurique anhydres, et son utilisation en alkylation catalytique d'isobutane et/ou d'isopentane en présence d'au moins une oléfine comportant de 3 à 6 atomes de carbone par molécule.
Abstract:
La présente invention se rapporte à un procédé pour la fabrication de catalyseurs à support métallique dopés fortement actifs, constitués d'un matériau de support organique ou inorganique et d'un précurseur de métal catalytique, caractérisé en ce que l'on dope le matériau de support, en présence de solvants, avant ou pendant l'application du précurseur d'au moins un métal du groupe 6, 7, 8, 9, 10 et/ou 11 de la classification périodique, avec des composés métalliques de basse valence facilement décomposables d'au moins un métal du groupe 4, 5 et/ou 6 de la classification périodique, le métal/les métaux du précurseur de métal catalytique, ainsi que le métal/les métaux des composés métalliques de basse valence étant originaires de différents groupes de la classification périodique, puis, le cas échéant, que l'on retraite le matériau de support et que l'on effectue toutes ces étapes à une température comprise entre -18 et +25 °C. La présente invention se rapporte en outre à l'utilisation des catalyseurs fabriqués selon ce procédé.
Abstract:
Middle distillates are prepared from a hydrocarbon feed obtained by a Fischer-Tropsch synthesis and comprising a fraction having a boiling point above the boiling point range of the middle distillates, by a process which comprises contacting the said hydrocarbon feed at elevated temperature and pressure in the presence of hydrogen with a catalyst comprising platinum supported on a silica-alumina carrier prepared from an amorphous silica-alumina starting material having a pore volume of at least 1.0 ml/g.