Coal recovery process

Claim 2

A process for recovering coal with a minimum pyrite content from an aqueous slurry containing raw coal, said process comprising the steps of: maintaining an agglomerant in said slurry; maintaining calcium oxide in the slurry in an amount exceeding that sufficient to form a saturated solution with the aqueous phase of the slurry; concomitantly comminuting the raw coal in said slurry to effect a separation of the coal from pyritic sulfur and other mineral matter associated therewith and to expose fresh surfaces on the coal particles; coalescing the separated coal particles into agglomerates while effecting a dispersion of the pyritic sulfur and other mineral matter in the aqueous liquid carrier portion of the slurry; and recovering the agglomerates from the slurry.

Claim 3

A process as defined in claim 1 in which the agglomerant comprises a fluorochloro derivative of methane or ethane.

Claim 4

A process as defined in claim 1 in which the agglomerant comprises a petroleum distillate or solvent; a nitrobenzene; kerosene; a lubricating, fuel, or residual oil; or a chlorinated biphenyl.

Claim 5

A process as defined in claim 1 in which the raw coal, agglomerant, calcium oxide, and water are continuously supplied to the apparatus in which the process is carried out and in which the products of the process are continuously removed therefrom, whereby the coal recovery process is carried out in a continuous as opposed to batch-type fashion.

Claim 6

A process for recovering coal with a minimum pyrite content from an aqueous slurry containing raw coal, said process comprising the steps of: maintaining an agglomerant selected from the group consisting of dichlorofluoromethane; trichlorofluoro-methane; 1,1,2,2-tetrachloro-1,2-difluoroethane; 1,1,2-trichloro-1,2,2-trifluoroethane; 1,1-dichloro-1,2,2,2-tetrafluoroethane; 1,-chloro-2,2,2-trifluoroethane; 1,1-dichloro-2,2,2-trifluoroethane; 1-chloro-2-fluoroethane and mixtures of the foregoing in said slurry; maintaining calcium oxide in the slurry; comminuting the raw coal in said slurry to effect a separation of the coal from pyritic sulfur and other mineral matter associated therewith and to expose fresh surfaces on the coal particles; coalescing the separated coal particles into agglomerates while effecting a dispersion of the pyritic sulfur and other mineral matter in the aqueous liquid carrier portion of the slurry; and recovering the agglomerates from the slurry.

Claim 7

A process for recovering coal with a minimum pyrite content from an aqueous slurry containing raw coal, said process comprising the steps of: maintaining an agglomerant selected from the group consisting of dichlorofluoromethane; trichlorofluoro-methane; 1,1,2,2-tetrachloro-1,2-difluoroethane; 1,1,2-trichloro-1,2,2-trifluoroethane; 1,1-dichloro-1,2,2,2-tetrafluoroethane; 1,-chloro-2,2,2-trifluoroethane; 1,1-dichloro-2,2,2-trifluoroethane; 1-chloro-2-fluoroethane and mixtures of the foregoing in said slurry; maintaining calcium oxide in the slurry; comminuting the raw coal in said slurry to effect a separation of the coal from pyritic sulfur and other mineral matter associated therewith and to expose fresh surfaces on the coal particles; coalescing the separated coal particles into agglomerates while effecting a dispersion of the pyritic sulfur and other mineral matter in the aqueous liquid carrier portion of the slurry; and recovering the agglomerates from the slurry.

Claim 8

A process as defined in claim 5 in which the raw coal, agglomerant, calcium oxide, and water are continuously supplied to the apparatus in which the process is carried out and in which the products of the process are continuously removed therefrom, whereby the coal recovery process is carried out in a continuous as opposed to batch-type fashion.

Claim 9

A process as defined in claim 5 in which the calcium oxide is maintained in said slurry in an amount exceeding that sufficient to form a saturated solution with the aqueous portion of the slurry.

Claim 10

A process for dissociating coal from a composite in which pyritic sulfur and other mineral matter is associated therewith and for recovering said coal in agglomerated form, said process comprising the steps of: forming a slurry of said composite in an aqueous carrier with respect to which said pyritic sulfur and mineral matter is hydrophilic; maintaining a fluorocarbon with respect to which said coal particles are hydrophobic in said slurry in an amount sufficient that agglomeration of the coal can be effected; comminuting the particles of composite while in said slurry to separate the pyritic sulfur and other mineral matter from the coal and to generate coal particles having freshly exposed surfaces in a controlled environment; mechanically effecting the coalescence of the coal particles into product coal agglomerates and the ejection of pyritic sulfur, other mineral matter, and water from the agglomerates into dispersion in said aqueous carrier; maintaining calcium oxide in said slurry in an amount effective to promote the rejection of pyritic sulfur from said agglomerates; and recovering said product coal agglomerates from said slurry.

Claim 11

A process for dissociating coal from a composite in which pyritic sulfur and other mineral matter is associated therewith and for recovering said coal in agglomerated form, said process comprising the steps of: forming a slurry of said composite in an aqueous carrier with respect to which said pyritic sulfur and mineral matter is hydrophilic; maintaining a fluorocarbon with respect to which said coal particles are hydrophobic in said slurry in an amount sufficient that agglomeration of the coal can be effected; comminuting the particles of composite while in said slurry to separate the pyritic sulfur and other mineral matter from the coal and to generate coal particles having freshly exposed surfaces in a controlled environment; mechanically effecting the coalescence of the coal particles into product coal agglomerates and the ejection of pyritic sulfur, other mineral matter, and water from the agglomerates into dispersion in said aqueous carrier; maintaining calcium oxide in said slurry in an amount effective to promote the rejection of pyritic sulfur from said agglomerates; and recovering said product coal agglomerates from said slurry.

Claim 12

A process as defined in claim 8 in which the fluorocarbon is selected from the group consisting of dichlorofluoromethane; trichlorofluoromethane; 1,1,2,2-tetrachloro-1,2-difluoroethane; 1,1,2-trichloro-1,2,2-trifluoroethane; 1,1-dichloro-1,2,2,2-tetrafluoroethane; 1-chloro-2,2,2-trifluoroethane; 1,1-dichloro-2,2,2-trifluoroethane; 1-chloro-2-fluoroethane and mixtures of the foregoing.

Claim 13

A process as defined in claim 8 in which the raw coal, agglomerant, calcium oxide, and water are continuously supplied to the apparatus in which the process is carried out and in which the products of the process are continuously removed therefrom, whereby the coal recovery process is carried out in a continuous as opposed to batch-type fashion.

Claim 14

A process as defined in claim 8 in which, at least once during the course of the process cycle, the aqueous liquid and material dispersed therein is removed and replaced with unburdened aqueous liquid.

Claim 15

A process as defined in claim 8 in which carrier burdened with pyritic sulfur and mineral matter is continuously removed from the slurry and replaced with unburdened aqueous liquid.

Claim 16

A process as defined in claim 8 in which the calcium oxide is dosed to the slurry.

Claim 17

A process as defined in claim 8 in which the calcium oxide is maintained in the slurry in an amount exceeding that sufficient to form a saturated solution with the aqueous portion of the slurry.