Alumina particles

Claim 2

Friable particles having an alumina content of at least about 98.5 weight percent, a surface area of less than about 1 m 2 /g, an attrition resistance of less than about 0.3 weight % per hour when tested in an air jet apparatus, a particle size ranging from about 30 to about 110 microns, a tap density of about 1.3 to about 1.9 g/cc, a generally spherical shape, and sufficient porosity to hold catalytic quantities of catalytic metals.

Claim 3

The particles of claim 1, wherein they contain about 1.0 weight percent or less of silica and about 0.1 weight percent or less each of iron and alkali metals.

Claim 4

The particles of claim 1, wherein the surface area is less than about 0.3 m 2 /g.

Claim 5

The particles of claim 1, wherein the particles have an attrition resistance of less than about 0.2 weight %/hr.

Claim 6

The particles of claim 1, wherein the particles have an attrition resistance of less than about 0.15 weight %/hr.

Claim 7

The particles of claim 1 having an average particle size of about 40 to about 70 microns.

Claim 8

The particles of claim 1, wherein the tap density is less than about 1.8 g/cc.

Claim 9

The particles of claim 1, wherein the tap density is less than about 1.75 g/cc.

Claim 10

The particles of claim 1, wherein they have sufficient porosity to hold catalytic metals without increasing the amount of attrited material in an air jet attrition test by more than about 30 percent as compared to non-metal coated particles.

Claim 11

The particles of claim 1, wherein they have sufficient porosity to hold catalytic metals without increasing the amount of attrited material in an air jet attrition test by more than about 20 percent as compared to non-metal coated particles.

Claim 12

A process for preparing friable particles having an alumina content of at least about 98.5 weight percent, a surface area of less than about 1 m 2 /g, an attrition resistance of less than about 0.3 weight percent per hour when tested in an air jet apparatus, a particle size ranging from about 30 to about 110 microns, a tap density of about 1.3 to about 1.9 g/cc, a generally spherical shape, and sufficient porosity to hold catalytic quantities of catalytic metals, said process comprising the steps of (i) forming an aqueous slurry having about 15 to about 50 weight percent solids wherein the solids comprise about 85 to about 99 weight percent -325 U.S. mesh of a high fired alumina having an ultimate crystallite size of greater than about 25 microns, and about 1 to about 15 weight percent of a material selected from the group consisting of (a) a super ground alpha alumina having a particle size less than about 5 microns, (b) a clay, and (c) a mixture of (a) and (b); (ii) spray drying the slurry to produce substantially spherical particles having an average particle size of about 30 to about 110 micron; (iii) heat treating the spray dried particles at a temperature below their melting points to form agglomerates of alumina particles having a surface area below about 1 m 2 /g and an attrition resistance of less than about 0.3 weight %/hour in an air jet apparatus; and (iv) deagglomerating the agglomerates to produce the particles.

Claim 13

A process for preparing friable particles having an alumina content of at least about 98.5 weight percent, a surface area of less than about 1 m 2 /g, an attrition resistance of less than about 0.3 weight percent per hour when tested in an air jet apparatus, a particle size ranging from about 30 to about 110 microns, a tap density of about 1.3 to about 1.9 g/cc, a generally spherical shape, and sufficient porosity to hold catalytic quantities of catalytic metals, said process comprising the steps of (i) forming an aqueous slurry having about 15 to about 50 weight percent solids wherein the solids comprise about 85 to about 99 weight percent -325 U.S. mesh of a high fired alumina having an ultimate crystallite size of greater than about 25 microns, and about 1 to about 15 weight percent of a material selected from the group consisting of (a) a super ground alpha alumina having a particle size less than about 5 microns, (b) a clay, and (c) a mixture of (a) and (b); (ii) spray drying the slurry to produce substantially spherical particles having an average particle size of about 30 to about 110 micron; (iii) heat treating the spray dried particles at a temperature below their melting points to form agglomerates of alumina particles having a surface area below about 1 m 2 /g and an attrition resistance of less than about 0.3 weight %/hour in an air jet apparatus; and (iv) deagglomerating the agglomerates to produce the particles.

Claim 14

The process of claim 11, wherein the high fired alumina is a tabular alumina

Claim 15

The process of claim 11, wherein the alpha alumina has a particle size of less than about 3 microns.

Claim 16

The process of claim 11, wherein the clay is a montmorillonite.

Claim 17

The process of claim 14, wherein the clay is bentonite and it is used in an amount up to about 2 weight percent of the solids of the aqueous slurry.

Claim 18

The process of claim 11, wherein the spray dried particles have an average particle size of about 40 to about 70 microns.

Claim 19

The process of claim 11, wherein the heat treating is performed at a temperature of up to about 1540° C.

Claim 20

The process of claim 11, wherein the aqueous slurry further contains a dispersant.

Claim 21

The process of claim 18, wherein the dispersant is an ammonium polymethacrylate.

Claim 22

The process of claim 11, wherein the spray drying is performed at a temperature of about 100° to about 350° C.

Claim 23

A process for producing friable particles having an alumina content of at least about 99.5 weight percent, a surface area of less than about 1 m 2 /g, an attrition resistance of less than about 0.3 weight percent per hour when tested in an air jet apparatus, a particle size ranging from about 30 to about 110 microns, a tap density of about 1.3 to about 1.9 g/cc, a generally spherical shape, and sufficient porosity to hold catalytic quantities of catalytic metals, said process comprising (i) heating hydrated alumina particles having a particle size of about 35 to about 150 microns to remove at least about 90 weight percent of the bound water and to convert the hydrate to at least gamma alumina and (ii) entraining the particles in a carrier gas and passing them through a high temperature zone of a plasma spray at a temperature sufficient to at least partially melt the particles and to cause them to have the properties.

Claim 24

A process for producing friable particles having an alumina content of at least about 99.5 weight percent, a surface area of less than about 1 m 2 /g, an attrition resistance of less than about 0.3 weight percent per hour when tested in an air jet apparatus, a particle size ranging from about 30 to about 110 microns, a tap density of about 1.3 to about 1.9 g/cc, a generally spherical shape, and sufficient porosity to hold catalytic quantities of catalytic metals, said process comprising (i) heating hydrated alumina particles having a particle size of about 35 to about 150 microns to remove at least about 90 weight percent of the bound water and to convert the hydrate to at least gamma alumina and (ii) entraining the particles in a carrier gas and passing them through a high temperature zone of a plasma spray at a temperature sufficient to at least partially melt the particles and to cause them to have the properties.

Claim 25

The process of claim 21, wherein the hydrated alumina is gibbsite.

Claim 26

The process of claim 21, wherein the heating is at a temperature of at least about 600° C.

Claim 27

The process of claim 21, wherein the heating converts at least a portion of the hydrate to alpha alumina and the heating is at a temperature of at least about 1100° C.

Claim 28

The process of claim 21, wherein the plasma spray is performed formed with a nitrogen torch gas at a torch gas flow of about 50 to 500 SCFH; torch power of at least 10 KW; nitrogen enthalpy of about 10,000 to about 30,000 BTU/lb; and a particle feed rate of about 10 to about 75 lb/hr.

Claim 29

The process of claim 21, wherein the plasma spray is performed under the following conditions: nitrogen torch gas; torch gas flow of about 100 to 150 SCFH; torch power of 60 KW; nitrogen enthalpy of about 12,000 to about 16,000 BTU/lb; and a particle feed rate of about 30 to about 50 lb/hr.