Process for heat-treating carbon blocks

Claim 2

In a method for heat-treating carbonaceous products weighing more than 100 kg wherein the carbonaceous product contains from 12-20 kg of tar binder per 100 kg of coke plus binder in which the products are heated to a temperature between 900° and 1400° C. with the heating pattern being such that the surface of the product does not exceed 700° C. until the core thereof has reached 450° C., the improvement comprising heating the product until the core temperature of the product is brought to between 120° and 170° C., heating the product to raise the core temperature to beyond 450° C. in less than 10 hours, with the heating pattern being such that the surface of the product does not exceed 700° C. until the core thereof has reached 450° C., and continuing the heating of the product at a rate of 50° to 100° C. per hour until the calcination temperature within the range of 900° to 1400° C. is reached.

Claim 3

A method according to claim 1 in which when the core temperature of the product is between 120° and 170° C., the product is quickly placed in a furnace heated to a temperature between 500° and 700° C.

Claim 4

A method according to claim 1 wherein the core temperature of the product is brought to between 120° and 170° C. by heating it, after prior cooling to ambient temperature, to a temperature between 120° and 170° C. at a rate below a limit which varies between 6° C./h for a product extruded or compression-molded at 500 bars, to 30° C./h for a product compression-molded at 50 bars or molded by a vibro-compression.

Claim 5

A method according to claim 1 wherein the product is subjected to heating which brings the core temperature up to between 120° and 170° C. immediately after molding.

Claim 6

A method according to claim 1 wherein the core temperature of the product is raised to between 120° and 170° C. during the molding operation.

Claim 7

In a method for heat-treating carbon electrodes formed of from 12-20 kg of tar binder per 100 kg of binder plus coke in which the electrodes are heated to a temperature between 900° to 1400° C. with the heating pattern being such that the surface of the electrode does not exceed 700° C. until the core thereof has reached 450° C., the improvement comprising heating the electrode until the core temperature of the electrode is brought to between 120° and 170° C., heating the electrode to raise the core temperature to beyond 450° C. in less than 10 hours, with the heating pattern being such that the surface of the electrode does not exceed 700° C. until the core has reached 450° C., and continuing the heating of the electrode at a rate of 50° to 100° C. per hour until the calcination temperature within the range of 900° to 1400° C. is reached.

Claim 8

In a method for heat-treating carbon electrodes formed of from 12-20 kg of tar binder per 100 kg of binder plus coke in which the electrodes are heated to a temperature between 900° to 1400° C. with the heating pattern being such that the surface of the electrode does not exceed 700° C. until the core thereof has reached 450° C., the improvement comprising heating the electrode until the core temperature of the electrode is brought to between 120° and 170° C., heating the electrode to raise the core temperature to beyond 450° C. in less than 10 hours, with the heating pattern being such that the surface of the electrode does not exceed 700° C. until the core has reached 450° C., and continuing the heating of the electrode at a rate of 50° to 100° C. per hour until the calcination temperature within the range of 900° to 1400° C. is reached.

Claim 9

In a method for heat-treating carbonaceous products weighing more than 100 kg formed of from 12-20 kg of tar binder per 100 kg of binder plus coke in which the products are heated to a temperature between 900° and 1400° C. with the heating pattern being such that the surface of the product does not exceed 700° C. until the core thereof has reached 450° C., the improvement comprising placing the product in a furnace heated to a temperature between 120° and 170° C. for a time sufficient to heat the core of the product to a temperature within 120° to 170° C., heating the product to raise the core temperature to beyond 450° C. in less than 10 hours, with the heating pattern being such that the surface of the product does not exceed 700° C. until the core thereof has reached 450° C., and continuing the heating of the product at rate of 50° to 100° per hour until the calcination temperature within the range of 900° to 1400° C. is reached.

Claim 10

In a method for heat-treating carbonaceous products weighing more than 100 kg formed of from 12-20 kg of tar binder per 100 kg of binder plus coke in which the products are heated to a temperature between 900° and 1400° C. with the heating pattern being such that the surface of the product does not exceed 700° C. until the core thereof has reached 450° C., the improvement comprising placing the product in a furnace heated to a temperature between 120° and 170° C. for a time sufficient to heat the core of the product to a temperature within 120° to 170° C., heating the product to raise the core temperature to beyond 450° C. in less than 10 hours, with the heating pattern being such that the surface of the product does not exceed 700° C. until the core thereof has reached 450° C., and continuing the heating of the product at rate of 50° to 100° per hour until the calcination temperature within the range of 900° to 1400° C. is reached.

Claim 11

A method as defined in claim 7 wherein the product is heated to a temperature between 120° and 170° C. at a rate ranging from 6° C. per hour to 30° C. per hour.

Claim 12

A method as defined in claim 7 wherein the products, at a temperature below 120° C., are heated after molding.

Claim 13

A method as defined in claim 7 wherein the product is heated to raise the core temperature to a temperature within the range of 120° to 170° C. during molding of the product.