Coated catalysts and their preparation

Claim 2

A coated catalyst, comprising a non-porous or slightly porous carrier and a layer of catalytic material, containing vanadium compounds, applied thereto, which is obtained by atomizing a mixture of water and a vanadium compound, with or without other metal compounds, and applying this mixture as a coating onto carrier particles which are themselves in constant motion, at from 20° to 90° C. and with a rate of application of from 0.001 to 0.02 part by weight of solids per part by volume of carrier beads per minute, then drying the coated catalysts thus obtained and, by flame heating or plasma heating of the coated catalyst particles which are themselves in constant motion, repeatedly heating all parts of the catalyst surface briefly to above 700° C. and cooling to below 650° C.

Claim 3

A process for the preparation of a coated catalyst, comprising a non-porous or slightly porous carrier and a layer of catalytic material, containing vanadium compounds, applied thereto, wherein a mixture of water and a vanadium compound with or without other metal compounds is atomized and this mixture is applied as a coating onto carrier particles which are themselves in constant motion, at from 20° to 90° C. and with a rate of application of from 0.001 to 0.02 part by weight of solids per part by volume of carrier beads per minute, the coated catalysts thus obtained are then dried and all parts of the catalyst surface are repeatedly heated briefly to above 700° C., by flame heating or plasma heating of the coated catalyst particles which are themselves in constant motion, and cooled to below 650° C.

Claim 4

A process for the preparation of a coated catalyst, comprising a non-porous or slightly porous carrier and a layer of catalytic material, containing vanadium compounds, applied thereto, wherein a mixture of water and a vanadium compound with or without other metal compounds is atomized and this mixture is applied as a coating onto carrier particles which are themselves in constant motion, at from 20° to 90° C. and with a rate of application of from 0.001 to 0.02 part by weight of solids per part by volume of carrier beads per minute, the coated catalysts thus obtained are then dried and all parts of the catalyst surface are repeatedly heated briefly to above 700° C., by flame heating or plasma heating of the coated catalyst particles which are themselves in constant motion, and cooled to below 650° C.

Claim 5

Use of a coated catalyst as claimed in claim 1 for the preparation of an anthraquinone by oxidation of an indan of the formula ##STR4## where R 1 , R 2 and R 3 may be identical or different and each is alkyl, R 1 and/or R 3 may in addition also each be hydrogen and X and Y may be identical or different and each is halogen or hydrogen, by means of oxygen in the gas phase in the presence of a vanadium compound and, if desired, one or more compounds of other metals.

Claim 6

A process as claimed in claim 2, wherein the catalyst is prepared with vanadium pentoxide and/or vanadates of elements of groups Ia, IIb, IIIa, IIIb, IVa, IVb, Va, Vb, VIa, VIb, VIIb and VIIIb of the periodic table.

Claim 7

A process as claimed in claim 2, wherein the catalyst is prepared with an atomic ratio of vanadium to the added elements of group Ia of from 2,000 to 0.5 atom of vanadium per atom of added element, a ratio of vanadium to added elements of group IIIa of from 4,000 to 1 atom of vanadium per atom of added element, a ratio of vanadium to added elements of group IVa of from 2,000 to 0.1 atom of vanadium per atom of added element, a ratio of vanadium to added elements of group Va of from 2,000 to 1 atom of vanadium per atom of added element, a ratio of vanadium to added elements of group VIa of from 2,000 to 1 atom of vanadium per atom of added element, a ratio of vanadium to added elements of group VIIb of from 2,000 to 3 atoms of vanadium per atom of added element, a ratio of vanadium to added elements of group VIIIb of from 100,000 to 0.5 atom of vanadium per atom of added element, a ratio of vanadium to added elements of group IIb of from 2,000 to 3 atoms of vanadium per atom of added element, a ratio of vanadium to added elements of group IIIb of from 2,000 to 1 atom of vanadium per atom of added element, a ratio of vanadium to added elements of group IVb of from 2,000 to 0.1 atom of vanadium per atom of added element, a ratio of vanadium to added elements of group Vb of from 4,000 to 5 atoms of vanadium per atom of added element or a ratio of vanadium to added elements of group VIb of from 2,000 to 4 atom sof vanadium per atom of added element.

Claim 8

A process as claimed in claim 2, wherein the catalyst is prepared with sodium aluminum silicate, a magnesium silicate, calcium aluminum silicate, a bleaching earth, a fuller's earth, a clay, kaolin, meerschaum, an allophane, a zeolite, montmorillonite, pumice, Florida earth, quartz, asbestos, mulite, steatite, bentonite, precipitated silica, silica gel, kieselguhr, silicon carbide, corundum, γ-alumina, hydrargillite, boehmite, bauxite, titanium dioxide, zirconium dioxide, tin dioxide, thorium dioxide, magnesite, zinc oxide, mullite, α-alumina, steatite, titanium(IV) oxide or iron(III) oxide as the carrier.

Claim 9

A process as claimed in claim 2, wherein the catalyst is prepared with from 0.02 to 0.5 part by weight of catalytic material per part by volume of carrier.

Claim 10

A process as claimed in claim 2, wherein the catalyst is prepared using rotating dishes, rotating drums, coating dishes, impregnating drums, coating drums, helical ribbon impellers or mixing vessels as the rotating vessel with a disk-shaped bottom.

Claim 11

A process as claimed in claim 2, wherein the catalyst is prepared using a coating dish or rotating dish, with the bottom of the vessel, containing the carrier particles, being at an angle of from 30° to 70° to the horizontal.

Claim 12

A process as claimed in claim 2, wherein the catalyst is prepared with the suspension at from 10° to 90° C. during atomizing and with the temperature within the loose mass during application of the active material being from 20° to 90° C.

Claim 13

A process as claimed in claim 2, wherein the catalyst is prepared using a rate of application of from 0.001 to 0.02 part by weight of solids per part by volume of carrier beads per minute.

Claim 14

A process as claimed in claim 2, wherein the catalyst is prepared in an apparatus which, during coating, is filled to the extent of from 20 to 80 percent by volume with carrier particles, the bottom of the vessel rotating at from 2 to 70 rpm.

Claim 15

A process as claimed in claim 2, wherein drying is effected entirely or partially during coating by blowing air or inert gas at from 100° to 300° C. into the loose mass.

Claim 16

A process as claimed in claim 2, wherein the catalyst is prepared, in the case of flame heating or plasma heating of the coated catalysts, with the temperature within the loose mass at from 650° to 300° C.

Claim 17

A process as claimed in claim 2, wherein the catalyst is prepared, in the case of flame heating or plasma heating of the coated catalyst, with each part (segment) of the surface of each individual coated catalyst particle being brought to from 700° to 3,000° C.

Claim 18

A process as claimed in claim 2, wherein the preparation is carried out with from 10 to 1,000 kg of coated catalyst both in the coating step and in the flame or plasma heating step, and with a total treatment time of the coated catalysts by means of the gas torch or plasma torch of from 2 to 60 minutes.

Claim 19

A process as claimed in claim 2, wherein the catalyst is prepared, when using a rotating dish, with a diameter of the vessel bottom of from 0.5 to 5 meters, the distance of the torch from the surface of the loose mass being from 2 to 70 centimeters and the flame temperature being from 700° to 2,000° C.