Manufacture of cement by intergrinding carbonaceous fuel

Claim 2

A continuous method of manufacturing Portland cement clinker comprising: (1) forming an intimate mixture by intergrinding (a) unsintered Portland cement raw materials and (b) a low volatile carbonaceous fuel having a high ignition temperature, (2) passing said intimate mixture through a set of preheating cyclones wherein said intimate mixture is preheated prior to passing into a calcining zone, and (3) passing said preheated intimate mixture into said calcining zone wherein said intimate mixture (a) is maintained in a substantial fluidized condition, and (b) is heated rapidly up to a calcination temperature of from about 1000° to about 2000° F. to accomplish calcination of said Portland cement raw material in said calcining zone and to accomplish the ignition of said carbonaceous fuel such that the heating in said calcining zone is effected at least in part by combustion of said carbonaceous fuel within said calcining zone, said calcination temperature being below the temperature of insipient fusion of said Portland cement raw materials to effect thermal decomposition of calcium carbonate with evolution of carbon dioxide.

Claim 3

Method as in claim 1 wherein the calcined Portland cement raw materials are introduced from said calcining zone into an inclined rotary vessel comprising a clinkering zone wherein said Portland cement raw materials are heated at sintering temperatures generally ranging from about 2300° to about 2900° F., said sintering temperature being at or above the insipient fusion temperature of said Portland cement raw materials to effect clinkering.

Claim 4

Method as in claim 2 wherein said set of preheating cyclones are in the form of a four-stage cyclonic preheater, and wherein said intimate mixture from said intergrinding step is passed countercurrently into a stream of hot gases emanating from said rotary kiln to the first stage, then on through the other stages of said calcining zone, and finally to said rotary kiln.

Claim 5

Method as in claim 3 wherein said carbonaceous fuel is coke and wherein calcination takes place in a separate calcination vessel between said set of cyclones and said rotary kiln.

Claim 6

Method as in claim 4 wherein said coke is coke breeze.

Claim 7

Method as in claim 4 wherein the particle size of the Portland cement raw materials and carbonaceous fuel after intergrinding is less than about 300 micrometers.

Claim 8

Method as in claim 3 wherein said carbonaceous fuel has an ignition temperature of between about 1000° and about 1500° F.

Claim 9

In a continuous method for the manufacture of Portland cement clinker comprising: (1) introducing unsintered Portland cement raw materials comprising calcium carbonate containing material, silica containing material, alumina containing material and iron containing material into a four-stage cyclonic preheater where said materials are preheated; (2) heating the preheated Portland cement raw materials in a calcining zone under conditions of agitation and in a substantial fluidized condition due to a countercurrent stream of hot gases from an attached rotary kiln said calcining zone being at calcination temperatures generally ranging between about 1000° F. and about 2000° F., said calcination temperatures being below the temperature of insipient fusion of said cement materials to effect thermal decomposition of calcium carbonate with evolution of carbon dioxide; (3) continuously transferring calcined material from said calcining zone to a rotary kiln including a clinkering zone; and (4) heating said calcined material in said clinkering zone at sintering temperatures generally ranging between about 2300° and about 2900° F., said sintering temperatures being at or above the temperature of insipient fusion of said Portland cement materials to effect clinkering; the improvement comprising intimately mixing into said Portland cement raw materials by intergrinding prior to the preheating step a finely divided, solid carbonaceous fuel having a volatiles content not more than about 40%, the ignition temperature of the non-volatile portion being greater than the temperature reached prior to said calcining zone and less than about 1500° F.; said carbonaceous fuel having an ash content of less than about 30% to provide at least 5% of the heat required for said process in said calcination zone, said volatiles content and said non-volatiles ignition temperature of said carbonaceous fuel being such that oxidation of said carbonaceous fuel occurs primarily in said calcination zone.

Claim 10

In a continuous method for the manufacture of Portland cement clinker comprising: (1) introducing unsintered Portland cement raw materials comprising calcium carbonate containing material, silica containing material, alumina containing material and iron containing material into a four-stage cyclonic preheater where said materials are preheated; (2) heating the preheated Portland cement raw materials in a calcining zone under conditions of agitation and in a substantial fluidized condition due to a countercurrent stream of hot gases from an attached rotary kiln said calcining zone being at calcination temperatures generally ranging between about 1000° F. and about 2000° F., said calcination temperatures being below the temperature of insipient fusion of said cement materials to effect thermal decomposition of calcium carbonate with evolution of carbon dioxide; (3) continuously transferring calcined material from said calcining zone to a rotary kiln including a clinkering zone; and (4) heating said calcined material in said clinkering zone at sintering temperatures generally ranging between about 2300° and about 2900° F., said sintering temperatures being at or above the temperature of insipient fusion of said Portland cement materials to effect clinkering; the improvement comprising intimately mixing into said Portland cement raw materials by intergrinding prior to the preheating step a finely divided, solid carbonaceous fuel having a volatiles content not more than about 40%, the ignition temperature of the non-volatile portion being greater than the temperature reached prior to said calcining zone and less than about 1500° F.; said carbonaceous fuel having an ash content of less than about 30% to provide at least 5% of the heat required for said process in said calcination zone, said volatiles content and said non-volatiles ignition temperature of said carbonaceous fuel being such that oxidation of said carbonaceous fuel occurs primarily in said calcination zone.

Claim 11

Method as in claim 8 wherein said carbonaceous fuel is petroleum coke or coal coke.

Claim 12

Method as in claim 8 wherein said carbonaceous fuel is coke breeze having a particle size of less than about 3/16 inch prior to the intergrinding step.

Claim 13

Method as in claim 10 wherein said coke breeze has an ignition temperature of between about 1000° and about 1500° F.

Claim 14

Method as in claim 8 wherein between about 5 and about 60 percent of the heat required in said calcination zone is provided by combustion of said carbonaceous fuel.

Claim 15

Method as in claim 12 wherein between about 30 and about 50 percent of the heat required in said calcination zone is provided by combustion of said carbonaceous fuel.

Claim 16

Method as in claim 8 wherein the intimate mixture of said Portland cement raw materials and said carbonaceous fuel after the intergrinding step has a particle size of less than about 300 micrometers.