Treatment of coal slurries

Claim 2

A process for continuously producing agglomerated coal from coal fines, which comprises treating an aqueous slurry of the coal files by (a) forming an unstable oil-in-water emulsion, (b) continuously mixing in a vessel the unstable oil-in-water emulsion, in an amount of from about 10 to about 25% by weight of the oil, calculated on a dry coal matter basis, into the slurry under conditions of non-intensive agitation corresponding to a Froude number of 2 to 600 with a residence time in the vessel of at least 15 minutes and for a time at least sufficient to reach phase inversion to form dense, large agglomerates of said coal fines, and (c) thereafter essentially stripping the aqueous slurry of coal matter by removing the agglomerated coal fines from the remainder of the aqueous slurry.

Claim 3

A process according to claim 1 in which the aqueous slurry contains at least 12% solids by weight.

Claim 4

A process according to claim 2 in which the aqueous slurry contains at least 25% solids by weight.

Claim 5

A process according to claim 1, wherein the unstable oil-in-water emulsion is mixed into said slurry by an impeller.

Claim 6

A process according to claim 4 in which the Froude number is from 40 to 200.

Claim 7

A process according to claim 1 in which the agglomerates are recoverable on a screen of aperture from 0.15 to 0.5 mm.

Claim 8

In a process for continuously producing agglomerated coal from coal fines, said process comprising treating an aqueous slurry of the coal fines by mixing oil with the aqueous slurry of coal fines in a vessel under conditions of agitation to form fine coal agglomerates, and thereafter removing the agglomerated coal fines from the remainder of the aqueous slurry, the improvement comprising utilizing an oil in the form of an unstable oil-in-water emulsion, and mixing the emulsified oil in an amount of from about 10 to about 25% by weight of the oil, calculated on a dry coal matter basis, into the slurry under conditions of non-intensive agitation corresponding to a Froude number of 2 to 600 for a time at least sufficient to reach phase inversion and for at least 15 minutes residence time in the vessel, to form dense, large fine coal agglomerates which can be readily removed from the remainder of the aqueous slurry.

Claim 9

In a process for continuously producing agglomerated coal from coal fines, said process comprising treating an aqueous slurry of the coal fines by mixing oil with the aqueous slurry of coal fines in a vessel under conditions of agitation to form fine coal agglomerates, and thereafter removing the agglomerated coal fines from the remainder of the aqueous slurry, the improvement comprising utilizing an oil in the form of an unstable oil-in-water emulsion, and mixing the emulsified oil in an amount of from about 10 to about 25% by weight of the oil, calculated on a dry coal matter basis, into the slurry under conditions of non-intensive agitation corresponding to a Froude number of 2 to 600 for a time at least sufficient to reach phase inversion and for at least 15 minutes residence time in the vessel, to form dense, large fine coal agglomerates which can be readily removed from the remainder of the aqueous slurry.

Claim 10

A process according to claim 7 in which the slurry contains at least 35% solids by weight and the Froude number is from 40 to 200.

Claim 11

A process according to 7 in which the agglomerates are recoverable on a screen of aperture from 0.15 to 0.5 mm.

Claim 12

A process according to 7 in which the agglomerates are recoverable on a screen of aperture from 0.15 to 0.5 mm.

Claim 13

The product of a process according to 7.

Claim 14

The product of a process according to 7.

Claim 15

A process according to claim 7, wherein said unstable oil-in-water emulsion contains about 5 to about 20 volume percent of oil, said oil having a viscosity of at least about 1.5 cSt at 100° F.

Claim 16

A process for continuously producing agglomerated coal from bituminous coal fines, which comprises treating an aqueous slurry containing at least 12% by weight of the coal fines by (a) forming an unstable oil-in-water emulsion of an oil having a viscosity of at least about 1.5 cSt at 100° F., (b) continuously mixing in a vessel the unstable oil-in-water emulsion, in an amount of from about 10 to about 25% by weight of oil, calculated on a dry coal matter basis, into the slurry under conditions of non-intensive agitation corresponding to a Froude number of 2 to 600 with a residence time in the vessel of at least 15 minutes and for a time at least sufficient to reach phase inversion, to form dense, large agglomerates of said coal fines, and (c) removing said agglomerates from the remaining aqueous slurry by use of a wedge wire screen having an aperture of at least about 0.15 mm to produce a screen tailing which is essentially stripped of coal matter.

Claim 17

A process for continuously producing agglomerated coal from bituminous coal fines, which comprises treating an aqueous slurry containing at least 12% by weight of the coal fines by (a) forming an unstable oil-in-water emulsion of an oil having a viscosity of at least about 1.5 cSt at 100° F., (b) continuously mixing in a vessel the unstable oil-in-water emulsion, in an amount of from about 10 to about 25% by weight of oil, calculated on a dry coal matter basis, into the slurry under conditions of non-intensive agitation corresponding to a Froude number of 2 to 600 with a residence time in the vessel of at least 15 minutes and for a time at least sufficient to reach phase inversion, to form dense, large agglomerates of said coal fines, and (c) removing said agglomerates from the remaining aqueous slurry by use of a wedge wire screen having an aperture of at least about 0.15 mm to produce a screen tailing which is essentially stripped of coal matter.