Abstract:
PROBLEM TO BE SOLVED: To provide a method for producing an epoxide from the corresponding olefin. SOLUTION: This method comprises epoxidation of an olefin-based compound using hydrogen peroxide in the presence of titanium silicalite catalyst; wherein a base or its mixture with at least one starting material is introduced under pH control into an epoxidation reactor; in this case, the pH value is adjusted to 4-9.5, esp. 5-9.5 in the reaction mixture or base-contg. starting material and the pH level is maintained. It is advantageous that the epoxidation is conducted in a fixed bed reactor using an aqueous-organic hydrogen peroxide solution with pH 8-9.
Abstract:
PROBLEM TO BE SOLVED: To provide the subject method which enables, in particular, the sol production process to be simplified by crystallizing at high temperature the effluent from the reaction of a mixture of tetraalkylorthosilicate and tetraalkylorthotitanate sealed in a reaction vessel with an aqueous template solution added to the mixture, and then firing the solid product after it is separated. SOLUTION: This method adds an aqueous template solution to a mixture of tetraalkylorthosilicate and tetraalkylorthotitanate sealed in a reaction vessel, and supplies the effluent to an autoclave without distilling off the alcohol produced as a result of the hydrolysis, where a solid product is crystallized at > 100 deg.C under a self-developed pressure; then separates, washes and fires the solid product at 400 to 1000 deg.C, to obtain the objective titanium-containing molecular sieve whose composition is shown by the formula (SiO2 ) 1-x (TiO2 )x (0.0001
Abstract:
PROBLEM TO BE SOLVED: To produce a pure-phase crystalline, micro- and mesoporous metallic silicate having high catalyst activities by carrying out the hydrothermal reaction using a pyrolytic metal-silicon mixed oxide as a source for silicon and a metal. SOLUTION: A pyrolytic metal-silicon-mixed oxide, preferably (SiO2 )1-x (TiO2 )x , (SiO2 )1-x (Al2 O3 )x , (SiO2 )1-x (B2 O3 )x , (SiO2 )1-x (V2 O5 )x or (SiO2 )1-x (ZrO2 )x [(x) is 0.0001-0.25] is used as a source for silicon and a metal and the hydrothermal reaction is carried out in the presence of a tetraalkylammonium hydroxide compound as a template compound at 0.05-2.0 molar ratio of OH /SiO2 . The hydrothermal reaction is conducted at 1-200 molar ratio of the H2 O/SiO2 at 100-220 deg.C temperature in the case of producing a microporous metallic silicate and 25-200 deg.C temperature in the case of producing a mesoporous metallic silicate for 1-50hr. The template compound is removed by extraction or calcining at 300-1,000 deg.C.
Abstract:
Mikro- und mesoporöse Metallsilicate werden durch hydrothermale Umsetzung einer Quelle für Silicium und das Metall in Gegenwart eines Templats hergestellt. Die Rohstoffauswahl beeinflußt die Reinheit und damit die katalytische Aktivität der Produkte. Erfindungsgemäß wird als Quelle für Silicium und das Metall ein pyrogenes Mischoxid eingesetzt. Bevorzugte Produkte haben die Zuammensetzung (SiO2)1-x(AmOn)x mit A gleich Ti, Al, B, V, Zr und x gleich 0,005 bis 0,1. Bei Verwendung eines Formkörpers des pyrogenen Mischoxids werden unmittelbar Formkörper der mikro- und mesoporösen Metallsilicate erhalten. Erfindungsgemaß erhältliche Produkte werden als Oxidationskatalysator verwendet.
Abstract:
THE PRESENT INVENTION RELATES TO A PROCESS FOR THE PURIFICATION OF A CRUDE PROPENE OXIDE CONTAINING METHANOL AND ACETALDEHYDE BY A CONTINUOUSLY OPERATED EXTRCATIVE DISTILLATION USING AN EXTRACTION SOLVENT LOWERING THE VOLATILITY OF METHANOL AND FEEDING A COMPOUND CONTAINING AN UNSUBSTITUTED NH2 GROUP CAPABLE OF REACTING WITH ACETALDEHYDE TO A DISTILLATION COLUMN AT A POINT ABOVE THE FEEDING POINT OF THE CRUDE PROPENE OXIDE TO GIVE A PURIFIED PROPENE OXIDE CONTAINING LESS THAN 100 PPM METHANOL AND LESS THAN 100 PPM ACETALDEHYDE. THE INVENTION ALSO RELATES TO A PROCESS FOR THE CATALYTIC EPOXIDATION OF PROPENE THAT INCLUDES THIS PURIFICATION EPOXIDATION OF PROPENE THAT INCLUDES THIS PURIFICATION STAGE.
Abstract:
Production of granulates containing titanium silicalite-1 (I) comprises hydrothermal crystallization of a synthesis gel containing a silica source, a titanium dioxide source, a tetra-n-propylammonium compound, a base and water; spray drying or fluidized bed spray granulation drying the resultant (I) suspension, optionally after concentration and/or addition of other substances; and calcining the (I) granulate at 400-1000, preferably 500-750degreesC. An Independent claim is also included for (I) granulates per se.
Abstract:
A process for production of epoxides by epoxidation of olefins with hydrogen peroxide in presence of titanium silicalite catalyst and base, in which the base is fed into the reactor directly or with starting material(s) so as to control pH and the pH value in the reaction mixture or the base-containing mixture(s) is kept essentially constant in the range 4-9.5.
Abstract:
Catalyst composed of the oxides of silicon, aluminium and titanium, characterised in that the catalyst particles are made up of a core of the composition (SiO2)x(AlO2)yMy where x/y = 10 - INFINITY and M = H, Na, K, NH4, NR4, where R = C1-C8-alkyl, and a shell of the composition (SiO2)n(TiO2)m where n/m = 12 - 1000 and both core and shell have a crystal structure of the type MFI or MEL. The catalyst can be produced by preparing in a known manner a synthesis gel for the preparation of a titanosilicalite, introducing into this synthesis gel an aluminosilicate of the structural type MFI or MEL and further processing the synthesis gel in a known manner.
Abstract:
Proceso para la producción de granulados que contienen titaniosilicalita-1, caracterizado porque se cristaliza en condiciones hidrotérmicas un gel de síntesis, que contiene una fuente de SiO2, una fuente de TiO2, un compuesto que contiene iones tetra-n-propilamonio, una base y agua, la suspensión de titaniosilicalita-1 resultante, opcionalmente después de concentración y/o adición de otros materiales, se somete a un secado por pulverización o un secado por pulverización-granulación en lecho fluidizado y el granulado de titaniosilicalita-1 así formado se calcina a una temperatura de 400 a 1000ºC, preferiblemente de 500 a 750ºC.