Kraftanlagen Ag

Basf Aktiengesellschaft

Siemens Aktiengesellschaft

Michael Kotter

Friedrich Weyland

Lothar Riekert

Ulrich Hammon

Wolfgang Hoelderich

Wilhelm Ruppel

Ulrike Wegerle

Erich Hums

Hans Martan

Dieter Becker

Lothar Rieckert

In the production of a catalyst containing a catalytically active Mo--V--O phase, the problem exists of keeping the Mo--V--O phase and/or an Mo--V--Ti--O phase substantially free of other catalytically active impurities in order not to catalyze competing reactions at the same time. For this purpose, the invention provides that vanadium oxide and molybdenum oxide are mixed in a ratio of 0.7 to 1% by weight based on V.sub.2 O.sub.5 and MoO.sub.3, the mixture is heated to a temperature above 500.degree. C., the Mo--V--O phase is cooled, ground and then subjected to a reducing treatment, and dispersed on a heated oxidic support, the dispersed material is then ground, and then applied to a suitable macroscopic support, optionally with further additives, and calcined. Alternatively, the material dispersed on the oxidic support can be kneaded with additives to form an extrudable compound, and the compound can be extruded and then calcined so that the honeycomb bodies produced from the compound have crosspiece widths in a range of from 0.1 to 0.6 mm and cell densities of 50 to 1200 cells per square inch.

Process for producing a catalyst

Method for the production of catalytically active mixed phases

A process for the catalytic gas-phase oxidation of propene or isobutene to acrolein or methacrolein in a tubular fixed bed reactor or catalytically active oxides with a .gtoreq.90% conversion of the initial olefin on a single passage, wherein the temperature of the gases containing the reactants in the direction of flow along the tubes from their entrance until the conversion of the initial olefin is from 30 to 70% is from 360.degree. to 420.degree. C. and is then adjusted to from 360.degree. to 300.degree. C. until the conversion of the initial olefin is from 80 to 90% and is thereafter maintained at from 330.degree. to 390.degree. C. until the gases emerge from the tubes, is described.

Preparation of acrolein or methacrolein by actalytic gas-phase oxidation

Method of preparing a plate-like support bearing catalytically active

Method for the selective elimination of nitrogen oxides from exhaust

Process for the selective catalytic removal of nitrogen oxides from the

Hard, fracture-resistant catalysts are prepared from zeolites of the pentasil family by a process in which water, organic additives which increase the viscosity and a silicate are added to the zeolite powder, and the material is molded, dried and calcined. The fracture-resistant zeolites obtained are used as catalyst carriers.

Preparation of hard, fracture-resistant catalysts from zeolite powder

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Bruchsal, Germany

Michael Kotter