Agglomeration of coal fines

Claim 2

Process for the agglomeration of coal fines from an aqueous slurry thereof, with simultaneous ash removal where ash is present in the slurry, comprising: (a) adding an aqueous emulsion of an oil fraction to said slurry, (b) agitating said emulsion and said slurry to form agglomerates and remaining slurry, (c) removing agglomerates formed, from the remaining slurry, (d) adding additional aqueous emulsion of an oil fraction to the remaining slurry, (e) agitating said emulsion and said remaining slurry to form agglomerates and remaining liquid, and (f) removing the agglomerates from the remaining liquid.

Claim 3

The processs of claim 1 wherein the oil fraction comprises a tar, shale, rock oil, or mineral oil fraction.

Claim 4

The process of claim 2 wherein the mineral oil fraction has a boiling point above 200° C.

Claim 5

The process of claim 1 wherein the amount of water present in the aqueous emulsion of an oil fraction is between 30 and 70 percent by weight.

Claim 6

The process of claim 1 wherein the aqueous emulsion of the oil fraction contains a surface active agent.

Claim 7

The process of claim 5 wherein the surface-active agent consists of a cationic, a non-ionic, or an anionic detergent.

Claim 8

The process of claim 6 wherein the surface-active agent consists of alkali metal sulphates or sulphonates of aliphatic or alkyl compounds selected from sodium C 8 -C 20 alkylbenzene sulphonates, sodium C 8 -C 20 alkyl sulphates, and sodium C 8 -C 18 secondary sulphates.

Claim 9

The process of claim 6 wherein the amount of surface-active agent is between 0.01 and 5 percent by weight, based on the weight of the aqueous emulsion, and 200 ppm weight, on total solids, coal fines and ash, present in the feed.

Claim 10

The process of claim 8 wherein the total amount of oil as aqueous emulsion to be added to the fines is between 1 and 10 percent by weight based on the total solids present in the feed.

Claim 11

The process of claim 9 wherein the amount of oil added to the aqueous slurry as aqueous emulsion is between 10 and 80 percent by weight the amount of oil as aqueous emulsion to be added in total to the aqueous slurry and the remaining slurry.

Claim 12

The process of claim 10 wherein the aqueous slurry of fines is agitated by stirring.

Claim 13

Process for the agglomeration of coal fines from an aqueous slurry thereof, with simultaneous ash removal where ash is present in the slurry, comprising: (a) continuously combining an aqueous emulsion of an oil fraction and an aqueous slurry of coal fines in a first agglomeration vessel and continously removing agglomerates and remaining slurry from the first agglomeration vessel, the contents of said first vessel being continuously agitated, (b) removing agglomerates from the remaining slurry, (c) continuously combining an aqueous emulsion of an oil fraction and the remaining slurry in a second agglomeration vessel and continuously removing agglomerates and remaining liquid from the second agglomeration vessel, the contents of said second vessel being continuously agitated, and (d) removing agglomerates from the remaining liquid.

Claim 14

Process for the agglomeration of coal fines from an aqueous slurry thereof, with simultaneous ash removal where ash is present in the slurry, comprising: (a) continuously combining an aqueous emulsion of an oil fraction and an aqueous slurry of coal fines in a first agglomeration vessel and continously removing agglomerates and remaining slurry from the first agglomeration vessel, the contents of said first vessel being continuously agitated, (b) removing agglomerates from the remaining slurry, (c) continuously combining an aqueous emulsion of an oil fraction and the remaining slurry in a second agglomeration vessel and continuously removing agglomerates and remaining liquid from the second agglomeration vessel, the contents of said second vessel being continuously agitated, and (d) removing agglomerates from the remaining liquid.

Claim 15

The process of claim 12 wherein the oil fraction comprises a tar, shale, rock oil, or mineral oil fraction.

Claim 16

The process of claim 12 wherein the mineral oil fraction has a boiling point above 200° C.

Claim 17

The process of claim 12 wherein the amount of water present in the aqueous emulsion of an oil fraction is between 30 and 70 percent by weight.

Claim 18

The process of claim 12 wherein the aqueous emulsion of the oil fraction contains a surface active agent.

Claim 19

The process of claim 16 wherein the surface-active agent consists of a cationic, or an anionic detergent.

Claim 20

The process of claim 17 wherein the surface-active agent consists of alkali metal sulphates or sulphonates of aliphatic or alkyl compounds selected from sodium C 8 -C 20 alkylbenzene sulphonates, sodium C 8 -C 20 alkyl sulphates, and sodium C 8 -C 18 secondary sulphates.

Claim 21

The process of claim 17 wherein the amount of surface-active agent is between 0.01 and 5 percent by weight, based on the weight of the aqueous emulsion, and 200 ppm weight, on total solids, coal fines and ash, present in the feed.

Claim 22

The process of claim 19 wherein the total amount of oil as aqueous emulsion to be added to the fines is between 1 and 10 percent by weight based on the total solids present in the feed.

Claim 23

The process of claim 20 wherein the amount of oil added to the aqueous slurry as aqueous emulsion is between 10 and 80 percent by weight the amount of oil as aqueous emulsion to be added in total to the aqueous slurry and the remaining slurry.

Claim 24

The process of claim 21 wherein the aqueous slurry of fines is agitated by stirring.