Abstract:
SUPPORTED CATALYSTS FOR THE OXIDATION OF AROMATIC OR UNSATURATED ALIPHATIC HYDROCARBONS TO CARBOXYLIC ACIDS OR ANHYDRIDES, CONSISTING OF AN INERT NONPOROUS CARRIER AND AN ACTIVE COMPOSITION OF 1 TO 40 PARTS BY WEIGHT OF VANADIUM PENTOXIDE AND 60 TO 90 PARTS BY WEIGHT OF TITANIUM DIOXIDE AND ALSO 0.01 TO 10% BY WEIGHT (WITH REFERENCE TO THE AMOUNT OF VANADIUM PENTOXIDE) OF A PHOSPHOROUS COMPOUND, THE VANADIUM PENTOXIDE CONTENT OF THE WHOLE SUPPORTED CATALYST BEING 0.05 TO 3% BY WEIGHT. THE CATALYSTS ARE USED ESPECIALLY FOR THE PRODUCTION OF PHTHALIC ANHYDRIDE FROM O-XYLENE.
Abstract:
SUPPORTED CATALYSTS CONTAINING VANADIUM PENTOXIDE AND TITANIUM DIOXIDE FOR OXIDATION REACTION, FOR EXAMPLE FOR THE PRODUCTION OF PHTHALIC ANHYDRIDE FROM O-XYLENE, WHICH CONTAIN ADDITIONS OF ALUMINUM OXIDE AND/OR LITHIUM OXIDE AND/OR ZIRCONIUM DIOXIDE.
Abstract:
A supported catalyst for the oxidation of o-xylene or naphthalene into phthalic anhydride which contains in the catalytically active material (in addition to from 1 to 40% by weight of V2O5 and from 60 to 99% by weight of anatase) from 0.01 to 0.15% by weight, based on the anatase, of sodium or potassium in the form of a compound devoid of sulfur.
Abstract translation:用于将邻二甲苯或萘氧化成邻苯二甲酸酐的负载催化剂,其含有催化活性材料(除了1至40重量%的V 2 O 5和60至99重量%的锐钛矿),0.01至0.15 基于锐钛矿的重量百分数为无硫化合物形式的钠或钾。
Abstract:
THE PRODUCTION OF A SUPPORTED CATALYST CONTAINING VANADIUM PENTOXIDE AND TITANIUM DIOXIDE FOR THE OXIDATION OF AROMATIC HYDROCARBONS TO CARBOXYLIC ACIDS OR THEIR ANHYDRIDES WITH OXYGEN OR GASES CONTAINING OXYGEN IN A FLUIDIZED BED, BY TREATING AN INERT CARRIER SUBSTANCE WITH A SOLUTION OR SUSPENSION OF A TITANIUM COMPOUND, THEN HEATING IT IN THE PRESENCE OF OXYGEN TO A TEMPERATURE OF 130* TO 1100*C., TREATING THE CARRIER THUS PRETREATED WITH A SOLUTION OR MELT OF A VANADIUM COMPOUND AND HEATING IT IN THE PRESENCE OF OXYGEN AT 350* TO 1100*C.
Abstract:
CATALYSTS CONTAINING VANADIUM PENTOXIDE AND TITANIUM DIOXIDE FOR THE OXIDATION OF AROMATIC AND UNSATURATED HYDROCARBONS TO CARBOXYLIC ACIDS, CONSISTING OF AN INERT NON-POROUS CARRIE WHICH IS COATED WITH A POROUS COMPOSITION CONTAINING 1 TO 15% BY WEIGHT OF VANADIUM PENTOXIDE AND 85 TO 99% BY WEIGHT OF TITANIUM DIOXIDE IN A LAYER HAVING A THICKNESS OF 0.02 TO 2 MM., PARTICULARLY 0.05 TO 1 MM., THE CATALYSTS HAVING A CONTENT OF VANADIUM PENTOXIDE OF 0.05 TO 3% BY WEIGHT AND THE COMPOSITION CONTAINING VANADIUM PENTOXIDE AND TITANIUM DIOXIDE HAVING BEEN APPLIED IN DISSOLVED OR SUSPENDED FORM TO A CARRIER WHICH HAS BEEN HEATED TO A TEMPERATURE OF 160* TO 500*C., PARTICULARLY 270* TO 500*C.
Abstract:
Cyclohexanone, or a homologue containing 1 or 2 alkyl groups of up to 4 carbon atoms each, obtained by the dehydrogenation of the corresponding cyclohexanol, is freed from unsaturated ketonic impurities by dispersing in the crude cyclohexanone about 0.01-1% by weight of an alkali-metal or alkaline-earth metal compound of alkaline reaction, and distilling the cyclohexanone in the presence of the alkali or alkaline-earth metal compound. Specified compounds of alkaline reaction are alkali and alkaline-earth (other than magnesium) hydroxides, alcoholates of 1-4 carbon atoms, phenolates and naphtholates, and alkali-metal carbonates, a number of suitable compounds being specified. The alkali or alkaline-earth metal compound may be taken as such or formed in situ, e.g. from an oxide, hydride or carbide. Conventional dehydrogenation catalysts may be used for the conversion of the cyclohexanol into cyclohexanone, and a number of suitable catalysts are specified. The dehydrogenation may be carried out in a single stage or in a number of stages, and the cyclohexanol starting material may have been obtained by the hydrogenation of the corresponding phenol, or by the hydrogenation and hydrolysis of aniline, the toluidines, the xylidines or the corresponding nitro compounds, or by the atmospheric oxidation of cyclohexane. The distillation of the cyclohexanone product is preferably effected in at least two stages, the compound of alkaline reaction being added before the first stage or at a later stage. In the first stage low-boiling impurities may be removed at a pressure between 300 mm. and 5 atm., and cyclohexanone then distilled from the residue at a pressure of 1-200 mm. Examples are given of the treatment of (1) methylcyclohexanol, obtained by hydrogenation of cresol, and (2) cyclohexanol, obtained by passing a mixture of aniline, steam and hydrogen over a hydrogenation catalyst.