Method of calcining green coke agglomerates

Claim 2

In a process of producing a solid agglomerated fuel product suitable for use in an ore reduction furnace comprising (1) agglomerating discrete solid carbonaceous particles to form green coke agglomerates; (2) setting said green agglomerates to enable the shape to be maintained in subsequent handling during carbonization; (3) carbonizing the set agglomerates by heating, the improvement wherein the setting step is accomplished by (1) forming a substantially uniformly mixed stationary bed of the green coke agglomerates and separator particles, such separator particles having a minimum particle size of about 1/8 inch and having a size and being present in sufficient quantities to allow heating gases to pass through the mixture and to prevent the green agglomerates from sticking together while maintaining the mixture as a stationary bed; and (2) maintaining the mixture as a stationary bed during the setting step while passing heating gases through the bed.

Claim 3

Process as in claim 1 wherein said carbonaceous material consists essentially of char from coal which has been carbonized at a temperature below about 1400° F. and wherein the agglomerating step is carried out at substantially atmospheric conditions.

Claim 4

Process of reducing a metal ore comprising combining the carbonized fuel product of claim 1 with a metallic ore and heating the same to yield a metal.

Claim 5

Process as in claim 3 wherein the metallic ore is iron ore.

Claim 6

In a process of producing a solid agglomerated fuel product comprising (1) agglomerating discrete solid carbonaceous particles in a tumbling zone of a rotating vessel by mixing a solid carbonaceous material having a maximum particle size of about 1/4 inch and a liquid hydrocarbon material as a binder to produce a delicate, green, unset agglomerate having a particle size within the range of about 5/8 inch to about 3 inches, said hydrocarbon material being about 10 to about 60 percent by weight of the total materials; (2) setting said green agglomerates to enable the shape to be maintained in subsequent handling during carbonization; (3) carbonizing the set agglomerates by heating at a temperature between about 1200 and about 2300° F., the improvement wherein the setting up is accomplished by (1) forming a mixture of the green agglomerates and separator particles, such separator particles having a minimum particle size of about 1/8 inch and having a size and being present in sufficient quantities to allow heating gases to pass through the mixture and to prevent the green agglomerates from sticking together throughout the depth of a stationary bed; and (2) maintaining the mixture as a stationary bed during the setting step while passing heating gases through the bed.

Claim 7

In a process of producing a solid agglomerated fuel product comprising (1) agglomerating discrete solid carbonaceous particles in a tumbling zone of a rotating vessel by mixing a solid carbonaceous material having a maximum particle size of about 1/4 inch and a liquid hydrocarbon material as a binder to produce a delicate, green, unset agglomerate having a particle size within the range of about 5/8 inch to about 3 inches, said hydrocarbon material being about 10 to about 60 percent by weight of the total materials; (2) setting said green agglomerates to enable the shape to be maintained in subsequent handling during carbonization; (3) carbonizing the set agglomerates by heating at a temperature between about 1200 and about 2300° F., the improvement wherein the setting up is accomplished by (1) forming a mixture of the green agglomerates and separator particles, such separator particles having a minimum particle size of about 1/8 inch and having a size and being present in sufficient quantities to allow heating gases to pass through the mixture and to prevent the green agglomerates from sticking together throughout the depth of a stationary bed; and (2) maintaining the mixture as a stationary bed during the setting step while passing heating gases through the bed.

Claim 8

Process as in claim 5 wherein said carbonaceous material consists essentially of char from coal which has been carbonized at a temperature below about 1400° F. and wherein the agglomerating step is carried out at substantially atmospheric conditions.

Claim 9

Process as in claim 6 wherein said separator particles are carbon particles.

Claim 10

Process as in claim 7 wherein said carbon particles are coke particles of a size which can readily be screened out from the set agglomerates.

Claim 11

Process as in claim 5 wherein the agglomerating step is carried out at a temperature between 150° F. and 750° F. and said setting is performed by heating said agglomerate at a temperature in the range of about 212 to 1000° F.

Claim 12

Process as in claim 5 wherein said setting is performed by heating said agglomerate at a temperature in the range of about 500° to 900° F.

Claim 13

Process as in claim 5 wherein said agglomerating takes place in pelletization equipment.

Claim 14

Process as in claim 5 wherein said agglomerating takes place in balling drum equipment.

Claim 15

Process as in claim 5 wherein said carbonaceous material consists essentially of char having a sulfur content less than 1% and an ash content less than 8.5%.

Claim 16

Process as in claim 13 wherein said char is from a fluidized bed carbonization process in which coal material crushed to less than about 1/8 inch size is carbonized and desulfurized in a hydrogen containing atmosphere at a temperature of about 800° to 1400° F. and at a pressure about atmospheric and up to 300 psia.

Claim 17

Process as in claim 13 wherein said char has a size of less than about 100 mesh.

Claim 18

Process as in claim 14 wherein said char has a size of less than about 200 mesh.

Claim 19

Process as in claim 5 wherein said setting is conducted by heating to a temperature between about 212° F. and about 1000° F. for a time period between about 11/2 and about 3 hours.

Claim 20

Process as in claim 5 wherein said solid fuel product is suitable for substitution for high grade metallurgical coke and has a high abrasion resistance as indicated by a tumbler hardness factor of at least 74 at 1400 revolutions and has a sulfur content less than 0.6%.

Claim 21

A process of producing a solid agglomerated fuel product suitable for substitution for high grade metallurgical coke comprising: a. Agglomerating by mixing together in tumbling zone of a rotating vessel under substantially atmospheric pressure a finely divided solid carbonaceous material having a maximum particle size of about 1/4 inch and a liquid hydrocarbon material at a temperature sufficient to form green, unset homogeneous agglomerates having a normal size distribution within the range of about 5/8 inch to 3 inches and wherein said hydrocarbon material has a minimum normal boiling point about 250° F. and a viscosity of 10 poise or less at temperatures up to 750° F., said hydrocarbon material being about 10 to 60 percent by weight of the total materials; b. Mixing said green agglomerates with separator particles having a particle size between about 1/8 inch to about 3/4 inch to form a substantially uniformly mixed stationary bed of said agglomerates and separator particles; c. Setting the mixture of green coke agglomerates and separator particles in a stationary bed to enable the shape of said agglomerate to be maintained during subsequent handling for carbonization by heating said agglomerates at a temperature in the range of about 212° to about 1000° F. by passing hot gases through the mixture; and then d. Carbonizing said agglomerates by heating at a temperature of between about 1200° and about 2300° F.

Claim 22

A process of producing a solid agglomerated fuel product suitable for substitution for high grade metallurgical coke comprising: a. Agglomerating by mixing together in tumbling zone of a rotating vessel under substantially atmospheric pressure a finely divided solid carbonaceous material having a maximum particle size of about 1/4 inch and a liquid hydrocarbon material at a temperature sufficient to form green, unset homogeneous agglomerates having a normal size distribution within the range of about 5/8 inch to 3 inches and wherein said hydrocarbon material has a minimum normal boiling point about 250° F. and a viscosity of 10 poise or less at temperatures up to 750° F., said hydrocarbon material being about 10 to 60 percent by weight of the total materials; b. Mixing said green agglomerates with separator particles having a particle size between about 1/8 inch to about 3/4 inch to form a substantially uniformly mixed stationary bed of said agglomerates and separator particles; c. Setting the mixture of green coke agglomerates and separator particles in a stationary bed to enable the shape of said agglomerate to be maintained during subsequent handling for carbonization by heating said agglomerates at a temperature in the range of about 212° to about 1000° F. by passing hot gases through the mixture; and then d. Carbonizing said agglomerates by heating at a temperature of between about 1200° and about 2300° F.

Claim 23

Process as in claim 19 wherein said separator particles are carbon particles.

Claim 24

Process as in claim 20 wherein said agglomerating is carried out in pelletization equipment.

Claim 25

Process as in claim 20 wherein said finely divided carbonaceous material consists essentially of char.

Claim 26

Process as in claim 22 wherein said char has a size less than about 100 mesh.

Claim 27

Process as in claim 22 wherein said char is produced by carbonizing coal and wherein said stationary bed has a depth of from about 15 to about 20 inches.

Claim 28

Process as in claim 19 comprising the additional step subsequent to the setting step of separating the separator particles from the set coke agglomerates and recycling these separator particles and mixing with green coke agglomerates and using in the setting of step (c).

Claim 29

A process for producing a solid agglomerated fuel product suitable for substitution for high grade metallurgical coke comprising: a. Agglomerating by mixing together in a tumbling zone of a rotating vessel under substantially atmospheric pressure a finely divided solid carbonaceous material consisting essentially of low density coal char having a maximum particle size of about 100 mesh and a liquid hydrocarbon material at a temperature sufficient to form green, unset homogeneous coke agglomerates having a normal size distribution within the range of about 5/8 inch to 3 inches and wherein said hydrocarbon material has a minimum normal boiling point about 250° F. and a viscosity of 10 poise or less at temperatures up to 750° F., said hydrocarbon material being about 10 to 60 percent by weight of the total materials; b. Forming a substantially uniformly mixed bed of green coke agglomerates with separator particles of sufficient size and present in sufficient quantities to prevent fusing of adjacent agglomerates while allowing heating gases to pass through the mixture while maintaining the mixture as a stationary bed during the setting step; c. Setting the mixture of green coke agglomerates and separator particles in a stationary bed to enable the shape of said agglomerate to be maintained during subsequent handling for carbonization by heating said agglomerates at a temperature in the range of about 212° to about 1000° F. and then d. Carbonizing said agglomerate by heating at a temperature of between about 1200° and about 2300° F.

Claim 30

A process for producing a solid agglomerated fuel product suitable for substitution for high grade metallurgical coke comprising: a. Agglomerating by mixing together in a tumbling zone of a rotating vessel under substantially atmospheric pressure a finely divided solid carbonaceous material consisting essentially of low density coal char having a maximum particle size of about 100 mesh and a liquid hydrocarbon material at a temperature sufficient to form green, unset homogeneous coke agglomerates having a normal size distribution within the range of about 5/8 inch to 3 inches and wherein said hydrocarbon material has a minimum normal boiling point about 250° F. and a viscosity of 10 poise or less at temperatures up to 750° F., said hydrocarbon material being about 10 to 60 percent by weight of the total materials; b. Forming a substantially uniformly mixed bed of green coke agglomerates with separator particles of sufficient size and present in sufficient quantities to prevent fusing of adjacent agglomerates while allowing heating gases to pass through the mixture while maintaining the mixture as a stationary bed during the setting step; c. Setting the mixture of green coke agglomerates and separator particles in a stationary bed to enable the shape of said agglomerate to be maintained during subsequent handling for carbonization by heating said agglomerates at a temperature in the range of about 212° to about 1000° F. and then d. Carbonizing said agglomerate by heating at a temperature of between about 1200° and about 2300° F.

Claim 31

Process as in claim 26 wherein said coal char has been carbonized at a temperature below about 1400° C. and wherein the char has a maximum particle size of about 200 mesh.