Fabrication of small dense silicon carbide spheres

Claim 2

A process for producing sintered spherical or nominally spherical particles of polycrystalline silicon carbide having a density greater than 80% of the theoretical density for silicon carbide and having a diameter ranging from about 5 microns to about 2000 microns which consists essentially of forming a slurry consisting essentially of sinterable silicon carbide powder and a liquid medium which has no significantly deleterious effect thereon, said sinterable silicon carbide powder having an average particle size which is submicron and which consists essentially of silicon carbide, a boron additive selected from the group consisting of boron and boron carbide in an amount equivalent to from about 0.3% by weight to about 3% by weight of boron based on said silicon carbide, and an amount of a carbonaceous additive equivalent to from about 0.1% by weight to about 5% by weight of free carbon based on said silicon carbide, said carbonaceous additive being selected from the group consisting of a carbonaceous organic material which completely decomposes at a temperature ranging from 50° C. up to 450° C. to free carbon and gaseous product of decomposition, and mixtures thereof with free carbon, spray drying said slurry into spherical or nominally spherical agglomerates, at least a portion of said carbonaceous organic material being an agglomerate-forming binder in solution and/or suspension in said liquid medium in said slurry and being present in an amount at least sufficient to form said agglomerate and being at least about 1% by weight of said agglomerate, and sintering said agglomerates at a temperature ranging from about 1900° C. to about 2300° C. at about or below atmospheric pressure in a vacuum or atmosphere which has no significant deleterious effect thereon, said agglomerates being of a size which produces said sintered particles, said slurry being characterized as sprayable into droplets into a hot air spray dryer wherein said droplets are dried into said spherical or nominally spherical agglomerates.

Claim 3

The process according to claim 1 wherein said agglomerates are prefired at a temperature ranging up to about 300° C. in air thermally decomposing said binder and removing gaseous product of decomposition therefrom.

Claim 4

The process according to claim 1 wherein said agglomerates are prefired in a vacuum or in an atmosphere in which they are inert at a temperature below said sintering temperature thermally decomposing said binder and removing gaseous product of decomposition therefrom.

Claim 5

A process for producing sintered spherical or nominally spherical particles of polycrystalline silicon carbide having a density greater than 80% of the theoretical density for silicon carbide and having a diameter ranging from about 5 microns to about 2000 microns which consists essentially of forming a slurry comprised of sinterable silicon carbide powder, a liquid medium and an agglomerate-forming binder in solution and/or suspension in said liquid medium, said sinterable silicon carbide powder having an average particle size which is submicron and which consists essentially of silicon carbide, a boron additive selected from the group consisting of boron and boron carbide in an amount equivalent to from about 0.3% by weight to about 3% by weight of boron based on said silicon carbide, and an amount of a carbonaceous additive equivalent to from about 0.1% by weight to about 5% by weight of free carbon based on said silicon carbide, said carbonaceous additive being selected from the group consisting of free carbon, a carbonaceous organic material which completely decomposes at a temperature ranging from 50° C. up to 450° C. to free carbon and gaseous product of decomposition, and mixtures thereof, spraying said slurry into droplets into a spray dryer wherein said droplets are dried into spherical or nominally spherical agglomerates, said agglomerate-forming binder being present in an amount of at least about 1% by weight of said agglomerate and at least sufficient to form said agglomerate, said agglomerate-forming binder being thermally removable at an elevated temperature ranging up to 450° C. leaving no significant amount thereof, and sintering said agglomerates at a temperature ranging from about 1900° C. to about 2300° C. at about or below atmospheric pressure in a vacuum or atmosphere which has no significant deleterious effect thereon, said agglomerates being of a size which produces said sintered particles, said slurry being characterized as sprayable into droplets into a hot air spray dryer wherein said droplets are dried into spherical or nominally spherical agglomerates.

Claim 6

A process for producing sintered spherical or nominally spherical particles of polycrystalline silicon carbide having a density greater than 80% of the theoretical density for silicon carbide and having a diameter ranging from about 5 microns to about 2000 microns which consists essentially of forming a slurry comprised of sinterable silicon carbide powder, a liquid medium and an agglomerate-forming binder in solution and/or suspension in said liquid medium, said sinterable silicon carbide powder having an average particle size which is submicron and which consists essentially of silicon carbide, a boron additive selected from the group consisting of boron and boron carbide in an amount equivalent to from about 0.3% by weight to about 3% by weight of boron based on said silicon carbide, and an amount of a carbonaceous additive equivalent to from about 0.1% by weight to about 5% by weight of free carbon based on said silicon carbide, said carbonaceous additive being selected from the group consisting of free carbon, a carbonaceous organic material which completely decomposes at a temperature ranging from 50° C. up to 450° C. to free carbon and gaseous product of decomposition, and mixtures thereof, spraying said slurry into droplets into a spray dryer wherein said droplets are dried into spherical or nominally spherical agglomerates, said agglomerate-forming binder being present in an amount of at least about 1% by weight of said agglomerate and at least sufficient to form said agglomerate, said agglomerate-forming binder being thermally removable at an elevated temperature ranging up to 450° C. leaving no significant amount thereof, and sintering said agglomerates at a temperature ranging from about 1900° C. to about 2300° C. at about or below atmospheric pressure in a vacuum or atmosphere which has no significant deleterious effect thereon, said agglomerates being of a size which produces said sintered particles, said slurry being characterized as sprayable into droplets into a hot air spray dryer wherein said droplets are dried into spherical or nominally spherical agglomerates.

Claim 7

The process according to claim 4 wherein said agglomerates are prefired at a temperature ranging up to about 300° C. in air thermally decomposing said binder and removing gaseous product of decomposition therefrom.

Claim 8

The process according to claim 4 wherein said agglomerates are prefired in a vacuum or in an atmosphere in which they are inert at a temperature below said sintering temperature thermally decomposing said binder and removing gaseous product of decomposition therefrom.

Claim 9

A process for producing sintered spherical or nominally spherical particles of polycrystalline silicon carbide having a density greater than 80% of the theoretical density for silicon carbide and having a diameter ranging from about 100 microns to about 10,000 microns which consists essentially of cascading or rolling sinterable silicon carbide powder and contacting said powder with an effective amount of a spray or mist of liquid to produce spherical or nominally spherical agglomerates, said sinterable silicon carbide powder having an average particle size which is submicron and which consists essentially of silicon carbide, a boron additive selected from the group consisting of boron and boron carbide in an amount equivalent to from about 0.3% by weight to about 3% by weight of boron based on said silicon carbide, and an amount of a carbonaceous additive equivalent to from about 0.1% by weight to about 5% by weight of free carbon based on said silicon carbide, said carbonaceous additive being selected from the group consisting of free carbon, a carbonaceous organic material which completely decomposes at a temperature ranging from 50° C. up to 450° C. to free carbon and gaseous product of decomposition, and mixtures thereof, and sintering said spherical or nominally spherical agglomerates at a temperature ranging from about 1900° C. to about 2300° C. at or below atmospheric pressure in a vacuum or atmosphere which has no significant deleterious effect thereon, said spherical or nominally spherical agglomerates being of a size which produces said sintered particles.

Claim 10

A process for producing sintered spherical or nominally spherical particles of polycrystalline silicon carbide having a density greater than 80% of the theoretical density for silicon carbide and having a diameter ranging from about 100 microns to about 10,000 microns which consists essentially of cascading or rolling sinterable silicon carbide powder and contacting said powder with an effective amount of a spray or mist of liquid to produce spherical or nominally spherical agglomerates, said sinterable silicon carbide powder having an average particle size which is submicron and which consists essentially of silicon carbide, a boron additive selected from the group consisting of boron and boron carbide in an amount equivalent to from about 0.3% by weight to about 3% by weight of boron based on said silicon carbide, and an amount of a carbonaceous additive equivalent to from about 0.1% by weight to about 5% by weight of free carbon based on said silicon carbide, said carbonaceous additive being selected from the group consisting of free carbon, a carbonaceous organic material which completely decomposes at a temperature ranging from 50° C. up to 450° C. to free carbon and gaseous product of decomposition, and mixtures thereof, and sintering said spherical or nominally spherical agglomerates at a temperature ranging from about 1900° C. to about 2300° C. at or below atmospheric pressure in a vacuum or atmosphere which has no significant deleterious effect thereon, said spherical or nominally spherical agglomerates being of a size which produces said sintered particles.

Claim 11

The process according to claim 7 wherein said liquid is water.

Claim 12

A polycrystalline spherical or nominally spherical particle having a density greater than 80% of the theoretical density for silicon carbide and consisting essentially of silicon carbide, from about 0.2 part to about 3 parts by weight of boron based on 100 parts by weight of silicon carbide, and up to about 5 parts by weight of free uncombined carbon based on 100 parts by weight of silicon carbide, said polycrystalline particle ranging in diameter from about 5 microns to about 10,000 microns.

Claim 13

A polycrystalline spherical or nominally spherical particle having a density greater than 80% of the theoretical density for silicon carbide and consisting essentially of silicon carbide, from about 0.2 part to about 3 parts by weight of boron based on 100 parts by weight of silicon carbide, and up to about 5 parts by weight of free uncombined carbon based on 100 parts by weight of silicon carbide, said polycrystalline particle ranging in diameter from about 5 microns to about 10,000 microns.

Claim 14

The particle according to claim 9 wherein said silicon carbide is α-silicon carbide.

Claim 15

The particle according to claim 9 wherein said silicon carbide is β-silicon carbide.

Claim 16

The particle according to claim 9 wherein said silicon carbide is a mixture of α- and β-silicon carbide.

Claim 17

Particles according to claim 9 having an average diameter ranging from about 10 microns to about 5000 microns.

Claim 18

Particles according to claim 9 having a diameter ranging from about 5 microns to about 2000 microns and having an average diameter ranging from about 10 microns to about 1000 microns.

Claim 19

Particles according to claim 9 having a diameter ranging from about 100 microns to about 10,000 microns and having an average diameter ranging from about 250 microns to about 5000 microns.

Claim 20

A polycrystalline spherical or nominally spherical particle having a density greater than 80% of the theoretical density for silicon carbide and consisting essentially of silicon carbide, from about 0.3 part to about 3 parts by weight of boron based on 100 parts by weight of silicon carbide, and from a detectable amount up to about 5 parts by weight of free uncombined carbon based on 100 parts by weight of silicon carbide, said polycrystalline particle ranging in diameter from about 5 microns to about 10,000 microns.

Claim 21

A polycrystalline spherical or nominally spherical particle having a density greater than 80% of the theoretical density for silicon carbide and consisting essentially of silicon carbide, from about 0.3 part to about 3 parts by weight of boron based on 100 parts by weight of silicon carbide, and from a detectable amount up to about 5 parts by weight of free uncombined carbon based on 100 parts by weight of silicon carbide, said polycrystalline particle ranging in diameter from about 5 microns to about 10,000 microns.

Claim 22

The particle according to claim 16 wherein said silicon carbide is α-silicon carbide.

Claim 23

The particle according to claim 16 wherein said silicon carbide is β-silicon carbide.

Claim 24

The particle according to claim 16 wherein said silicon carbide is a mixture of α- and β-silicon carbide.

Claim 25

Particles according to claim 16 having an average diameter ranging from about 10 microns to about 5000 microns.

Claim 26

Particles according to claim 16 having a diameter ranging from about 5 microns to about 2000 microns and having an average diameter ranging from about 10 microns to about 1000 microns.

Claim 27

Particles according to claim 16 having a diameter ranging from about 100 microns to about 10,000 microns and having an average diameter ranging from about 250 microns to about 5000 microns.

Claim 28

The process according to claim 7 wherein said sinterable silicon carbide powder is in the form of agglomerates.

Claim 29

The process according to claim 7 wherein said sinterable silicon carbide powder is in the form of agglomerates and said liquid is water.

Claim 30

The process according to claim 7 wherein said sinterable silicon carbide powder is in the form of spray dried agglomerates, said spray dried agglomerates consisting essentially of said sinterable silicon carbide powder with at least a portion of said carbonaceous organic material being an agglomerate-forming binder present in an amount at least sufficient to form said spray dried agglomerate and being at least about 1% by weight of said spray dried agglomerate.

Claim 31

The process according to claim 7 wherein said sinterable silicon carbide powder is in the form of spray dried agglomerates and said liquid is water, said spray dried agglomerates consisting essentially of said sinterable silicon carbide powder with at least a portion of said carbonaceous organic material being an agglomerate-forming binder present in an amount at least sufficient to form said spray dried agglomerate and being at least about 1% by weight of said spray dried agglomerate.

Claim 32

The process according to claim 7 wherein said sinterable silicon carbide powder is in the form of spray dried agglomerates, said spray dried agglomerates consisting essentially of said sinterable silicon carbide powder and agglomerate-forming binder, said agglomerate-forming binder being present in an amount of at least about 1% by weight of said agglomerate and at least sufficient to form said agglomerate, said agglomerate-forming binder being thermally removable at an elevated temperature ranging up to 450° C. leaving no significant amount thereof.

Claim 33

The process according to claim 7 wherein said sinterable silicon carbide powder is in the form of spray dried agglomerates and said liquid is water, said spray dried agglomerates consisting essentially of said sinterable silicon carbide powder and agglomerate-forming binder, said agglomerate-forming binder being present in an amount of at least about 1% by weight of said agglomerate and at least sufficient to form said agglomerate, said agglomerate-forming binder being thermally removable at an elevated temperature ranging up to 450° C. leaving no significant amount thereof.

Claim 34

The process according to claim 7 wherein agglomerates are cascaded or rolled with said sinterable silicon carbide powder and contacted with an effective amount of spray or mist of liquid to produce spherical or nominally spherical agglomerates, said agglomerates being selected from the group consisting of agglomerates of said sinterable silicon carbide powder; first spray dried agglomerates consisting essentially of said sinterable silicon carbide powder with at least a portion of said carbonaceous organic material being an organic agglomerate-forming binder present in an amount at least sufficient to form said first spray dried agglomerate and being at least about 1% by weight of said first spray dried agglomerate; second spray dried agglomerates consisting essentially of said sinterable silicon carbide powder and agglomerate-forming binder, said agglomerate-forming binder being present in an amount of at least about 1% by weight of said second spray dried agglomerate and at least sufficient to form said second spray dried agglomerate, said agglomerate-forming binder being thermally removable at an elevated temperature ranging up to 450° C. leaving no significant amount thereof; and mixtures thereof.

Claim 35

The process according to claim 7 wherein agglomerates are cascaded or rolled with said sinterable silicon carbide powder and contacted with an effective amount of spray or mist of water to produce spherical or nominally spherical agglomerates, said agglomerates being selected from the group consisting of agglomerates of said sinterable silicon carbide powder; first spray dried agglomerates consisting essentially of said sinterable silicon carbide powder with at least a portion of said carbonaceous organic material being an organic agglomerate-forming binder present in an amount at least sufficient to form said first spray dried agglomerate and being at least about 1% by weight of said first spray dried agglomerate; second spray dried agglomerates consisting essentially of said sinterable silicon carbide powder and agglomerate-forming binder, said agglomerate-forming binder being present in an amount of at least about 1% by weight of said second spray dried agglomerate and at least sufficient to form said second spray dried agglomerate, said agglomerate-forming binder being thermally removable at an elevated temperature ranging up to 450° C. leaving no significant amount thereof; and mixtures thereof.