Process for producing ultrafine silicon carbide powder

Claim 2

In a process for producing an ultrafine silicon carbide powder which comprises charging a particulate material prepared by blending and granulating silica powder, carbon powder and a carbonaceous binder into a reactor from the top thereof, said reactor having a preheating zone, a heating zone and a cooling zone, allowing the charged material to descend under its own weight in the preheating zone of said reactor till reaching the heating zone, heating said material horizontally in the heating zone to effect a SiC forming reaction, allowing the reaction product to further descend in the cooling zone for cooling it under a non-oxidizing atmosphere, and discharging the reaction product from the bottom of the cooling zone of said reactor, a process capable of preventing the disintegration of the particulate material in the course of the reaction, wherein the carbon powder contained in said particulate material is one having a specific surface area within the range from 1 to 1,000 m 2 /g and mixed with a liquid composed principally of a liquid organic compound before or at latest when said carbon powder is granulated, and the reaction temperature in the heating zone is controlled within the range from 1,500° to 2,000° C.

Claim 3

A process according to claim 1, wherein said carbon powder is principally composed of at least one selected from contact black, furnace black, thermal black and lamp black.

Claim 4

A process according to claim 1, wherein said liquid organic compound is composed of at least one selected from benzene, acetone, toluene, hexane, isohexane, heptane, isoheptane, isooctane, cyclohexane, ethylbenzene, chloroform, carbon tetrachloride, dichloroethane, dichloroethylene, trichloroethylene, nonane, xylene, methyl alcohol, ethyl alcohol, butyl alcohol, isobutyl alcohol, propyl alcohol, isopropyl alcohol, ethyl ether, isopropyl ether, ester of formic acid, methyl acetate, ethyl acetate, isopropyl acetate, ethyl propionate, amyl propionate, butyl lactate, diethyl carbonate, fluoroacetic acid, diethylene dimethyl ether, ethyl methyl ketone and quinoline.

Claim 5

A process according to claim 1, wherein said carbonaceous binder is composed of at least one selected from petroleum pitch, coal tar pitch, wood tar pitch, asphalt, phenolic resin, furan resin, petroleum tar, coal tar, wood tar, saccharides, ligninsulfonates and alginates.

Claim 6

A process according to claim 1, wherein the amount of said carbonaceous binder blended is within the range from 3 to 25 parts by weight, in terms of the amount of fixed carbon, to 100 parts by weight of the silica powder and carbon powder combined.

Claim 7

In a process for producing an ultrafine silicon carbide powder which comprises charging a particulate material prepared by blending and granulating silica powder, carbon powder and a carbonaceous binder into a reactor from the top thereof, said reactor having a preheating zone, a heating zone and a cooling zone, allowing the charged material to descend under its own weight in the preheating zone of said reactor until reaching the heating zone, heating the material horizontally in the heating zone to effect a SiC forming reaction, allowing the reaction product to further descend in the cooling zone for cooling it under a non-oxidizing atmosphere, and discharging the reaction product from the bottom of the cooling zone of said reaction, a process capable of preventing the disintegration of the particulate material in the course of the reaction, wherein the carbon powder contained in said particulate material is one having a specific surface area within the range from 1 to 1,000 m 2 /g and mixed with water containing a surfactant before said carbon powder is granulated, and the reaction temperature in the heating zone is controlled within the range from 1,500° to 2,000° C.

Claim 8

In a process for producing an ultrafine silicon carbide powder which comprises charging a particulate material prepared by blending and granulating silica powder, carbon powder and a carbonaceous binder into a reactor from the top thereof, said reactor having a preheating zone, a heating zone and a cooling zone, allowing the charged material to descend under its own weight in the preheating zone of said reactor until reaching the heating zone, heating the material horizontally in the heating zone to effect a SiC forming reaction, allowing the reaction product to further descend in the cooling zone for cooling it under a non-oxidizing atmosphere, and discharging the reaction product from the bottom of the cooling zone of said reaction, a process capable of preventing the disintegration of the particulate material in the course of the reaction, wherein the carbon powder contained in said particulate material is one having a specific surface area within the range from 1 to 1,000 m 2 /g and mixed with water containing a surfactant before said carbon powder is granulated, and the reaction temperature in the heating zone is controlled within the range from 1,500° to 2,000° C.

Claim 9

A process according to claim 6, wherein said carbon powder is principally composed of at least one selected from contact black, furnace black, thermal black and lamp black.

Claim 10

A process according to claim 6, wherein said surfactant is composed of at least one selected from amines, organic compounds having a carboxyl group, organic compounds having a sulfo group, esters, ammonium compounds, organic compounds having an ether linkage, and alcohols.

Claim 11

A process according to claim 6, wherein said surfactant is added in an amount of at least 0.05 parts by weight to 100 parts by weight of the carbon powder.

Claim 12

A process according to claim 6, wherein said carbonaceous binder is composed of at least one selected from petroleum pitch, coal tar pitch, wood tar pitch, asphalt, phenolic resin, furan resin, petroleum tar, coal tar, wood tar, saccharides, ligninsulfonates and alginates.

Claim 13

A process according to claim 6, wherein the amount of said carbonaceous binder blended is within the range from 3 to 25 parts by weight, in terms of the amount of fixed carbon, to 100 parts by weight of the silica powder and carbon powder combined.

Claim 14

In a process for producing an ultrafine silicon carbide powder which comprises charging a particulate material prepared by blending and granulating silica powder, carbon powder and a carbonaceous binder into a reactor from the top thereof, said reactor having a preheating zone, a heating zone and a cooling zone, allowing the charged material to descend under its own weight in the preheating zone of said reactor until reaching the heating zone, heating the material horizontally in the heating zone to effect a SiC forming reaction, allowing the reaction product to further descend in the cooling zone for cooling it under a non-oxidizing atmosphere, and discharging the reaction product from the bottom of the cooling zone of said reactor, a process capable of preventing the disintegration of the particulate material in the course of the reaction, wherein the carbon powder contained in said particulate material is a carbon powder having a specific surface area within the range from 1 to 1,000 m 2 /g and mixed with water before or at the latest when it is granulated, said carbon powder having been improved in water wettability by oxidizing the powder particle surfaces by heating in an oxidizing atmosphere, and the reaction temperature in the heating zone is controlled within the range from 1,500° to 2,000° C.

Claim 15

In a process for producing an ultrafine silicon carbide powder which comprises charging a particulate material prepared by blending and granulating silica powder, carbon powder and a carbonaceous binder into a reactor from the top thereof, said reactor having a preheating zone, a heating zone and a cooling zone, allowing the charged material to descend under its own weight in the preheating zone of said reactor until reaching the heating zone, heating the material horizontally in the heating zone to effect a SiC forming reaction, allowing the reaction product to further descend in the cooling zone for cooling it under a non-oxidizing atmosphere, and discharging the reaction product from the bottom of the cooling zone of said reactor, a process capable of preventing the disintegration of the particulate material in the course of the reaction, wherein the carbon powder contained in said particulate material is a carbon powder having a specific surface area within the range from 1 to 1,000 m 2 /g and mixed with water before or at the latest when it is granulated, said carbon powder having been improved in water wettability by oxidizing the powder particle surfaces by heating in an oxidizing atmosphere, and the reaction temperature in the heating zone is controlled within the range from 1,500° to 2,000° C.

Claim 16

A process according to claim 12, wherein said carbon powder is principally composed of at least one selected from contact black, furnace black, thermal black and lamp black.

Claim 17

A process according to claim 12, wherein the heating temperature under said oxidizing atmosphere is 200° C. at the lowest

Claim 18

A process according to claim 12, wherein the oxygen content of said carbon powder is at least 0.2% by weight.

Claim 19

A process according to claim 12, wherein said carbonaceous binder is composed of at least one selected from petroleum pitch, coal tar pitch, wood tar pitch, asphalt, phenolic resin, furan resin, petroleum tar, coal tar, wood tar, saccharides, ligninsulfonates and alginates.

Claim 20

A process according to claim 12, wherein the amount of said carbonaceous binder blended is within the range from 3 to 25 parts by weight, in terms of the amount of fixed carbon, to 100 parts by weight of the silica powder and carbon powder combined.