Abstract:
The invention relates to the regeneration of inert carrier material of deactivated oxidation catalysts. Said method is characterized in that the deactivated oxidation catalysts are washed in a rotating drum under the effect of ultrasound and dried in a drier through which dried hot air having a temperature of from 80 to 110 °C is passed. The invention also relates to a device for regenerating inert carrier material of deactivated oxidation catalysts.
Abstract:
The invention relates to a device for the mixing, drying and coating of powdered, granular or moulded bulk material in a fluid bed, in particular, a method for the production of supported catalysts for gas phase oxidations, with a container (10), for holding the bulk goods, whereby a dished recess (17) is provided in a lower region (13) of the container (10), a central tube (27) for the introduction of a gas, whereby the central tube enters in an upper region (12) of the container (10), extending essentially axially downwards into the container (10) and opens out in the recess (17), an essentially annular deflector screen (29), fixed to the central tube (27) in the upper region (12) of the container (10), a guide ring (31), arranged in the lower region (13) of the container (10), which surrounds the central tube (27) over a part of the length thereof essentially concentrically with a separation (L) such that a first passage (34) is formed between the wall of the container (10) at the upper edge of the recess and the lower end (33) of the guide ring (31) and a second outlet (36) is formed between the deflector screen (29) and the upper edge (35) of the guide ring (31) and means for introduction of a fluid into the container (10), such as, for example, nozzles (21). Said device is characterised in that the external wall of the central tube (27) is at least partly provided with a non-stick coating (38). In a preferred embodiment the separation (L) between the wall of the central tube (27) and the wall of the guide ring (27) is greater than the open height (H3) of the first passage (34). The invention further relates to a method for the production of supported catalysts using such a device.
Abstract:
THE INVENTION RELATES TO AN APPARATUS FOR MIXING, DRYING AND COATING PULVERULENT, GRANULAR OR SHAPED LOOSE MATERIAL IN A FLUIDIZED BED, IN PARTICULAR FOR USE IN A PROCESS FOR PRODUCING SUPPORTED CATALYSTS FOR GAS-PHASE OXIDATIONS, WHICH COMPRISES A CONTAINER (10) FOR ACCOMMODATING THE LOOSE MATERIAL, WITH A BOWL-LIKE DEPRESSION (17) BEING PROVIDED IN A LOWER REGION (13) OF THE CONTAINER (10), A CENTRAL TUBE (27) FOR INTRODUCING A GAS, WITH THE CENTRAL TUBE ENTERING THE CONTAINER IN AN UPPER REGION (12) OF THE CONTAINER (10), EXTENDING ESSENTIALLY AXIALLY DOWNWARD IN THE CONTAINER (10) AND OPENING INTO THE DEPRESSION (17), AN ESSENTIALLY ANNULAR DEFLECTION SHIELD (29) WHICH IS FIXED TO THE CENTRAL TUBE (27) IN THE UPPER REGION (12) OF THE CONTAINER (10), A GUIDE RING (31) WHICH IS LOCATED IN THE LOWER REGION (13) OF THE CONTAINER (10) AND SURROUNDS THE CENTRAL TUBE (27) ESSENTIALLY CONCENTRICALLY AT A DISTANCE (L) FOR PART OF ITS LENGTH SO THAT A FIRST OPENING (34) IS FORMED BETWEEN THE WALL OF THE CONTAINER (10) AT THE UPPER EDGE (22) OF THE DEPRESSION AND THE LOWER END (33) OF THE GUIDE RING (31) AND A SECOND OPENING (36) IS FORMED BETWEEN THE DEFLECTION SHIELD (29) AND THE UPPER EDGE (35) OF THE GUIDE RING (31),AND MEANS,FOR EXAMPLE VALVES (21),FOR INTRODUCING A FLUID INTO THE CONTAINER (10). IN THE APPARATUS OF THE PRESENT INVENTION, THE OUTER WALL OF THE CENTRAL TUBE (27) IS AT LEAST PARTLY PROVIDED WITH AN ADHESION-REDUCING COATING (38). IN A PREFERRED EMBODIMENT, THE DISTANCE (L) BETWEEN THE WALL OF THE CENTRAL TUBE (27) AND THE WALL OF THE GUIDE RING (27) IS GREATER THAN THE OPEN HEIGHT (H3) OF THE FIRST OPENING (34). THE INVENTION ALSO PROVIDES A PROCESS FOR PRODUCING SUPPORTED CATALYSTS USING SUCH AN APPARATUS.FIG.1
Abstract:
In the preparation of a catalyst for gas phase oxidations, particles for an inert support are weighed into a fluid bed with a total mass (MTrager). A fluid is prepared as an aqueous solution or suspension of a catalytically-active material, or source, preferably TiO 2 and/or V 2O 5, with a content (BSusp) of bonding agents. The inert support particles are fluidized by a gas flow with a controlled temperature (TGas) and flow (QGas). The suspension is sprayed on to the fluidized inert support at a given dosage rate (QSusp). The values are selected to give ranges of 3000=QGas[m3/h]=9000, 1000=QSusp[g/min]=3500, 2=BSusp[wt.%]=18.60=MTrager[kg]=240, 75=TGas[[deg]C]=120. The ranges are such that, for a parameter (K) where K=0.020QGas-0.055QSusp+7.500BSusp-0.667MTrager+2.069TGas-7, the relationship 127.5=K=202 is satisfied.
Abstract:
The invention relates to an apparatus for introducing loose materials, in particular catalysts made up of small bodies, into tubes, containers and the like which has a number of charging units and a transport device ( 1 ) which moves all the charging units simultaneously. To achieve reliable and exact relocation of the filling units, the transport device comprises a baseplate ( 2 ) which can be moved back and forth, at least one piston-cylinder unit ( 3 ) fastened to the baseplate and one or more transport claws ( 5 ), with the transport claws being operatively connected to the piston-cylinder unit, being rotatable about a common axis and having their free end projecting through openings ( 6 ) in the baseplate into tubes ( 7 ), containers and the like and the length of the openings in the direction of movement of the baseplate being equal to or greater than the stroke of the piston-cylinder unit.
Abstract:
Se describe un proceso para producir un catalizador para las oxidaciones en fase de gas, en el cual un suspension de particulas del TiO2 y el V2O5 tienen un diametro de 20 (m o menos, y al menos el 96& en volumen de las particulas de V2O5 tienen un diametro de 30 (m o menos. La distribucion del tamano de particulas definida del V2O5 permite una eficiencia alta del recubrimiento.
Abstract:
The invention relates to a process for producing a catalyst for gas-phase oxidations, which comprises weighing a particulate inert support having a total mass of M support into a fluidized-bed apparatus, providing an aqueous suspension of a catalytically active material or sources therefor and a binder having a binder content of B susp , fluidizing the inert support by introduction of a gas stream heated to a temperature of T gas at a flow rate of Q gas , and spraying the suspension at a rate of Q susp onto the fluidized inert support. When Q gas , Q susp , B susp , M support and T gas are selected within the ranges 3000 gas [m 3 /h] susp [g/min] susp [% by weight] support [kg] gas [° C.] K=0.020 Q gas -0.055 Q susp +7.500 B susp -0.667 M support +2.069 T gas -7 satisfies the relationship 127.5
Abstract:
A process is described for producing a catalyst for gas-phase oxidations, in which a suspension of TiO2 and V2O5 particles is applied to a fluidized inert support, wherein at least 90% by volume of the V2O5 particles have a diameter of 20 mum or less and at least 95% by volume of the V2O5 particles have a diameter of 30 mum or less. The defined particle size distribution of the V2O5 allows a high coating efficiency.