Method of making metal carbide and nitride powders

Claim 2

A process for forming a metal nitride powder which comprises: reacting at least one metal oxide composition with a binder and a material capable of supplying carbon to said reaction, or with a binder capable of supplying said carbon so as to produce granules having a controlled pore volume ranging from about 0.1 to 3 cm 3 /g; subjecting said granules to a carbothermal reduction reaction at a temperature ranging between about 1300°-1600° C. in an atmosphere containing nitrogen or which is capable of releasing nitrogen so as to form said metal nitride powder wherein said powder contains an excess of said carbon; heating said powder so as to decarbonize said metal nitride until substantially all of said excess carbon is eliminated; and collecting said metal nitride powder in the form of particles or agglomerates, said metal nitride powder having a specific surface area of at least about 30 m 2 /g.

Claim 3

A process for forming a metal carbide power which comprises: reacting at least one metal oxide composition with a binder and a material capable of supplying said carbon to said reaction, or with a binder which is capable of supplying said carbon so as to produce granules having a controlled pore volume ranging from about 0.1 to 3 cm 3 /g; subjecting said granules to a carbothermal reduction reaction at a temperature ranging between about 1300° and 1600° C. in a neutral atmosphere so as to form said metal carbide powder wherein said powder contains an excess of carbon; heating said powder so as to decarbonize said metal carbide until substantially all of said excess carbon is eliminated; and collecting said metal carbide powder in the form of articles or agglomerates, said metal carbide powder having a specific surface area of at least about 30 m 2 /g.

Claim 4

A process for forming a metal carbide power which comprises: reacting at least one metal oxide composition with a binder and a material capable of supplying said carbon to said reaction, or with a binder which is capable of supplying said carbon so as to produce granules having a controlled pore volume ranging from about 0.1 to 3 cm 3 /g; subjecting said granules to a carbothermal reduction reaction at a temperature ranging between about 1300° and 1600° C. in a neutral atmosphere so as to form said metal carbide powder wherein said powder contains an excess of carbon; heating said powder so as to decarbonize said metal carbide until substantially all of said excess carbon is eliminated; and collecting said metal carbide powder in the form of articles or agglomerates, said metal carbide powder having a specific surface area of at least about 30 m 2 /g.

Claim 5

The method of claim 2 wherein said atmosphere is comprised of hydrogen.

Claim 6

The method of claim 2 wherein said atmosphere comprises a noble gas.

Claim 7

The method of claim 1 or 2 wherein said at least one metal oxide is selected from the group consisting of SiO 2 , Al 2 O 3 , TiO 2 ZrO 2 , HfO 2 and B 2 O 3 .

Claim 8

The method of claim 5 wherein the particle size of said metal oxides is less than 10 micrometers.

Claim 9

The method of claim 6 wherein the particle size of said metal oxides ranges between about 0.1-5 micrometers.

Claim 11

The method of claim 8 wherein said resin is a thermosetting resin of phenol formaldehyde, epoxy, polyimide, polyurea or polycarbonate.

Claim 12

The method of claim 1 or 2 which further comprises adding said binder in an amount such that the carbon/metal oxide molar ratio is greater than 1.

Claim 13

The method of claim 10 wherein said molar ratio ranges between about 2-60:1.

Claim 14

The method of claim 1 or 2 which further comprises kneading said reaction mixture of said metal oxide and said binder to facilitate the formation of said granules, prior to subjecting then to said carbothermal reduction reaction, at a temperature between ambient and 200° C.

Claim 15

The method of claim 1 or 2 wherein the pore volume of said granules may be more precisely regulated by varying the amount of binder used in the reaction or by varying the temperature or pressure conditions utilized during the formation of said granules.

Claim 16

The method of claim 1 or 2 which further comprises coking said binder at between about 350°-500° C. prior to mixing said binder with said at least one metal oxide.

Claim 17

The method of claim 1 wherein the amount of nitrogen used ranges from about 2-10 times the stoichiometric requirement for said reaction.

Claim 18

The method of claim 1 or 2 which further comprises controlling the emission of carbon monoxide produced as a result of said decarbonizing reaction.

Claim 19

The method of claim 1 or 2 wherein said decarbonization step is carried out at between about 500°-800° C.

Claim 20

The method of claim 1 or 2 which further comprises grinding or screening said agglomerates so as to render the dimensions of said agglomerates more uniform in size.

Claim 21

A process for forming a metal nitride powder which comprises: mixing at least one metal oxide composition, selected from the group consisting of SiO 2 Al 2 O 3 , TiO 2 , ZrO 2 , HfO 2 and B 2 O 3 and having a particle size between about 0.1-5 micrometers with a binder which has been coked at between about 350°-500° C., wherein said binder/metal oxide molar ratio is between about 2-60:1, said binder being a coal tar, a thermosetting resin or an organic, polymer at between ambient temperature and 200° C. to produce a paste; extruding said paste; heating said extrudate to a temperature between about 50°-250° C. so as to dry said binder, forming granules from said extrudate having a pore volume ranging between about 0.1-3 cm 3 /g; subjecting said granules to a carbothermal reduction reaction at a temperature between about 1300°-1600° C. in a nitrogen atmosphere or an atmosphere capable of releasing nitrogen, wherein the amount of nitrogen used ranges from about 2-10 times the stoichiometric requirement for the reaction so as to form agglomerates of a metal nitride powder wherein said powder contains an excess of carbon; grinding or screening said agglomerates so as to render the dimension of said powder more uniform in size and wherein the largest dimension of each of said granules ranges between about 1-30 mm; heating said uniformly dimensioned powder to a temperature between about 500°-800° C. until substantially all of said excess carbon is reacted with oxygen so as to form a carbon monoxide gas; controlling said gaseous carbon monoxide emission produced as a result of said decarbonization step; and collecting said metal nitride powder in the form of particles or agglomerates, said metal nitride powder having a specific source area of at least about 30 m 2 /g.

Claim 22

A process for forming a metal nitride powder which comprises: mixing at least one metal oxide composition, selected from the group consisting of SiO 2 Al 2 O 3 , TiO 2 , ZrO 2 , HfO 2 and B 2 O 3 and having a particle size between about 0.1-5 micrometers with a binder which has been coked at between about 350°-500° C., wherein said binder/metal oxide molar ratio is between about 2-60:1, said binder being a coal tar, a thermosetting resin or an organic, polymer at between ambient temperature and 200° C. to produce a paste; extruding said paste; heating said extrudate to a temperature between about 50°-250° C. so as to dry said binder, forming granules from said extrudate having a pore volume ranging between about 0.1-3 cm 3 /g; subjecting said granules to a carbothermal reduction reaction at a temperature between about 1300°-1600° C. in a nitrogen atmosphere or an atmosphere capable of releasing nitrogen, wherein the amount of nitrogen used ranges from about 2-10 times the stoichiometric requirement for the reaction so as to form agglomerates of a metal nitride powder wherein said powder contains an excess of carbon; grinding or screening said agglomerates so as to render the dimension of said powder more uniform in size and wherein the largest dimension of each of said granules ranges between about 1-30 mm; heating said uniformly dimensioned powder to a temperature between about 500°-800° C. until substantially all of said excess carbon is reacted with oxygen so as to form a carbon monoxide gas; controlling said gaseous carbon monoxide emission produced as a result of said decarbonization step; and collecting said metal nitride powder in the form of particles or agglomerates, said metal nitride powder having a specific source area of at least about 30 m 2 /g.

Claim 23

A process for forming a metal carbide powder which comprises: mixing at least one metal oxide composition selected from the group consisting of Al 2 O 3 , TiO 2 , ZrO 3 , HfO 2 and B 2 O 3 and having a particle size between about 0.1-5 micrometers with a binder which has been coked at between about 350°-500° C., wherein said binder-metal oxide ratio is between about 2-60:1, said binder being a coal tar, a thermosetting resin or an organic polymer, at between ambient temperature and 200° C. to produce a paste; extruding said paste; heating said extrudate to a temperature between about 50°-250° C. so as to dry said binder; forming granules from said extrudate having a pore volume ranging between about 0.1-3 cm 3 /g. subjecting said granules to a carbothermal reduction reaction at a temperature between about 1300°-1500° C. in a neutral atmosphere so as to form agglomerates of a metal carbide powder wherein said powder contains an excess of carbon; grinding or screening said agglomerates so as to render the dimension of said powder more uniform in size and wherein the largest dimension of each of said granules ranges between 1-30 mm; heating said uniformly dimensioned powder to a temperature of between about 500°-800° C. until substantially all of said excess carbon is reacted with oxygen so as to from a carbon monoxide gas; controlling said gaseous carbon monoxide emissions produced as a result of said decarbonization step; and collecting said metal carbide powder in the form of particles or agglomerates, said metal carbide powder having a specific surface area of at least about 30 m 2 /g.

Claim 24

A process for forming a metal carbide powder which comprises: mixing at least one metal oxide composition selected from the group consisting of Al 2 O 3 , TiO 2 , ZrO 3 , HfO 2 and B 2 O 3 and having a particle size between about 0.1-5 micrometers with a binder which has been coked at between about 350°-500° C., wherein said binder-metal oxide ratio is between about 2-60:1, said binder being a coal tar, a thermosetting resin or an organic polymer, at between ambient temperature and 200° C. to produce a paste; extruding said paste; heating said extrudate to a temperature between about 50°-250° C. so as to dry said binder; forming granules from said extrudate having a pore volume ranging between about 0.1-3 cm 3 /g. subjecting said granules to a carbothermal reduction reaction at a temperature between about 1300°-1500° C. in a neutral atmosphere so as to form agglomerates of a metal carbide powder wherein said powder contains an excess of carbon; grinding or screening said agglomerates so as to render the dimension of said powder more uniform in size and wherein the largest dimension of each of said granules ranges between 1-30 mm; heating said uniformly dimensioned powder to a temperature of between about 500°-800° C. until substantially all of said excess carbon is reacted with oxygen so as to from a carbon monoxide gas; controlling said gaseous carbon monoxide emissions produced as a result of said decarbonization step; and collecting said metal carbide powder in the form of particles or agglomerates, said metal carbide powder having a specific surface area of at least about 30 m 2 /g.

Claim 25

A process for forming a silicon nitride powder which comprises: reacting a silicon oxide composition with a material capable of supplying carbon to said reaction to produce granules having a controlled pore volume ranging from about 0.1 to 3 cm 3 /g; subjecting said granules to a carbothermal reduction reaction at a temperature ranging between about 1300°-1600° C. in an atmosphere which contains or is capable of releasing nitrogen to form a silicon nitride powder containing excess carbon; heating said powder until said excess carbon is substantially eliminated to produce a silicon nitride powder having a specific surface area of at least 30 m 2 /g; and collecting said silicon nitride powder in the form of particles or agglomerates.

Claim 26

A process for forming a silicon nitride powder which comprises: reacting a silicon oxide composition with a material capable of supplying carbon to said reaction to produce granules having a controlled pore volume ranging from about 0.1 to 3 cm 3 /g; subjecting said granules to a carbothermal reduction reaction at a temperature ranging between about 1300°-1600° C. in an atmosphere which contains or is capable of releasing nitrogen to form a silicon nitride powder containing excess carbon; heating said powder until said excess carbon is substantially eliminated to produce a silicon nitride powder having a specific surface area of at least 30 m 2 /g; and collecting said silicon nitride powder in the form of particles or agglomerates.

Claim 27

A process for forming an aluminum nitride powder which comprises: reacting an aluminum oxide composition with a material capable of supplying carbon to said reaction to produce granules having a controlled pore volume ranging form aobut 0.1 to 3 cm 3 /g; subjecting said granules to a carbothermal reduction reaction at a temperature ranging between about 1300°-1600° C. in an atmosphere containing or capable of releasing nitrogen so as to form aluminum nitride powder containing excess carbon; heating said powder until said excess carbon is substantially eliminated to produce an aluminum nitride powder having a specific surface area of at least 30 m 2 /g; and collecting said aluminum nitride powder in the form of particles or agglomerates.

Claim 28

A process for forming an aluminum nitride powder which comprises: reacting an aluminum oxide composition with a material capable of supplying carbon to said reaction to produce granules having a controlled pore volume ranging form aobut 0.1 to 3 cm 3 /g; subjecting said granules to a carbothermal reduction reaction at a temperature ranging between about 1300°-1600° C. in an atmosphere containing or capable of releasing nitrogen so as to form aluminum nitride powder containing excess carbon; heating said powder until said excess carbon is substantially eliminated to produce an aluminum nitride powder having a specific surface area of at least 30 m 2 /g; and collecting said aluminum nitride powder in the form of particles or agglomerates.