Process for making a silicon carbide whisker reinforced alumina ceramic composite precursor

Claim 2

A process for preparing a ceramic composite which is comprised of alpha silicon carbide whiskers and alpha aluminum oxide powder, comprising the steps of sequentially: (a) providing a slurry comprised of from about 80 to about 92 volume percent of solid material and from about 20 to about 8 volume percent of non-aqueous liquid, wherein:

Claim 3

said solid material comprises from about 17 to about 22 weight percent of aluminum material, from about 19 to about 24 weight percent of amorphous carbon, and from about 56 to about 65 weight percent of silica; 2. said aluminum material has a specific surface area of from about 0.2 to about 1.1 square meters per gram, has a particle size distribution which ranges from about 4 to about 28 microns, and has at least 80 weight percent of its particles being in the range of from about 6 to about 12 microns; 3. said amorphous carbon has a specific surface area of at least 4 square meters per gram: 4. said silica has a specific surface area of from about 1.2 to about 400 square meters per gram;

Claim 4

said solid material comprises from about 17 to about 22 weight percent of aluminum material, from about 19 to about 24 weight percent of amorphous carbon, and from about 56 to about 65 weight percent of silica; 2. said aluminum material has a specific surface area of from about 0.2 to about 1.1 square meters per gram, has a particle size distribution which ranges from about 4 to about 28 microns, and has at least 80 weight percent of its particles being in the range of from about 6 to about 12 microns; 3. said amorphous carbon has a specific surface area of at least 4 square meters per gram: 4. said silica has a specific surface area of from about 1.2 to about 400 square meters per gram;

Claim 5

said non-aqueous liquid is volatile at a temperature of 80 degrees centigrade; 6. said slurry is comprised of from about 1 to about 5 weight percent of a source of carbon monoxide which, when it is subjected to a temperature of from about 700 to about 1,600 degrees centigrade, generates carbon monoxide; 7. said slurry is comprised of from about 1 to about 5 weight percent of a source of hydrogen fluoride which, when subjected to a temperature of from about 200 to about 400 degrees centigrade, generates hydrogen fluoride; (b) pelletizing said slurry to provide a multiplicity of pellets comprised of from about 80 to about 92 volume percent of solids; (c) drying said pellets to a moisture content of from about 0.1 to about 2.0 weight percent; (d) preheating said dried pellets to a temperature of from about 200 to about 300 degrees centigrade, and (f) igniting said pellets.

Claim 6

said non-aqueous liquid is volatile at a temperature of 80 degrees centigrade; 6. said slurry is comprised of from about 1 to about 5 weight percent of a source of carbon monoxide which, when it is subjected to a temperature of from about 700 to about 1,600 degrees centigrade, generates carbon monoxide; 7. said slurry is comprised of from about 1 to about 5 weight percent of a source of hydrogen fluoride which, when subjected to a temperature of from about 200 to about 400 degrees centigrade, generates hydrogen fluoride; (b) pelletizing said slurry to provide a multiplicity of pellets comprised of from about 80 to about 92 volume percent of solids; (c) drying said pellets to a moisture content of from about 0.1 to about 2.0 weight percent; (d) preheating said dried pellets to a temperature of from about 200 to about 300 degrees centigrade, and (f) igniting said pellets.

Claim 7

The process as recited in claim 1, wherein said slurry is pelletized by sieving.

Claim 8

The process as recited in claim 2, wherein said slurry is pelletized by being passed through a twin-deck sieve, wherein the top sieve has sieve openings of from about 8 to about 14 millimeters; and the bottom sieve has sieve openings smaller than those of the top sieve but no smaller than about 4 millimeters.

Claim 9

The process as recited in claim 3, wherein said dried pellets are preheated by being contacted with hot nitrogen at a temperature of from about 300 to about 400 degrees centigrade.

Claim 10

The process as recited in claim 1, wherein said source of carbon monoxide is a fatty acid containing from about 10 to about 24 carbon atoms.

Claim 11

The process as recited in claim 1, wherein said source of hydrogen fluoride is selected from the group consisting of potassium hydrogen fluoride, sodium hydrogen fluoride, and ammonium hydrogen fluoride.

Claim 12

The process as recited in claim 6, wherein said source of hydrogen fluoride is potassium hydrogen fluoride.

Claim 13

The process as recited in claim 1, wherein said non-aqueous liquid is selected from the group consisting of acetone, benzene, toluene, and n-petroleum ether.

Claim 14

The process as recited in claim 1, wherein said dried pellets are preheated for from about 10 to about 40 minutes.

Claim 15

The process as recited in claim 9, wherein said dried pellets are preheated for from about 15 to about 25 minutes.