Process for removal of sulfur and ash from coal

• US 4,272,250 A
• Filed: 06/19/1979
• Issued: 06/09/1981
• Est. Priority Date: 06/19/1979
• Status: Expired due to Term

• Current Assignee: Atlantic Richfield Company Incorporated (BP PLC)
• Original Assignee: Atlantic Richfield Company Incorporated (BP PLC)
• Inventors: Burk, Emmett H. Jr., Troncoso, Nestor J., Sun, Jui-Yuan
• Primary Examiner(s): DEES, CARL
• Application Number:
  US06/050,263
• Time in Patent Office: 721 Days
• Field of Search: 44/1 SR, 44/24, 209/5, 209/49, 209/171, 209/173, 209/164, 209/207
• US Class Current: 44/574
• CPC Class Codes: B03B 9/005 specially adapted for coal
• CPC Class Codes: B03D 1/02 Froth-flotation processes
• CPC Class Codes: B03D 3/06 Flocculation
• CPC Class Codes: C10L 9/00 Treating solid fuels to improve their combustion

Abstract

A process for reducing the sulfur and ash content of coal particles wherein coal particles are treated in an aqueous slurry with a minor amount of hydrocarbon oil to form coal-oil aggregates having modified particle size and density characteristics. The coal-oil aggregates are separated from ash and mineral matter in the slurry by gravitational means. Optionally, the coal particles may be treated with a conditioning agent prior to the aggregation step. Recovered coal particles comprise a substantial part of the feed carbon values.

Claims

1. A process for reducing the sulfur and ash content of coal comprising the steps of:

(a) providing an aqueous slurry of coal particles containing ash and pyritic sulfur mineral matter;

(b) adding to the slurry a minor amount of hydrocarbon oil sufficient to effect aggregation of the coal particles;

(c) incorporating a gas into or on the coal-oil aggregates, whereby the apparent density of the coal-oil aggregates is modified;

(d) gravitationally separating the density-modified coal-oil aggregates from the aqueous slurry; and

(e) recovering coal-oil aggregates of reduced sulfur.

2. The process of claim 1 wherein the hydrocarbon oil is derived from petroleum, shale oil, tar sands or coal.

3. The process of claim 1 wherein the hydrocarbon oil is selected from the group consisting of light cycle oil, heavy cycle oil, gas oil, vacuum gas oil, clarified oil, kerosene, light naphtha, and heavy naphtha.

4. The process of claim 1 wherein the hydrocarbon oil is added to the slurry as an emulsion in water.

5. The process of claim 1 wherein the aggregation of coal particles is effected by adding hydrocarbon oil to the slurry at a temperature within the range from 0°

to 100°

C.

6. The process of claim 5 wherein the aggregation of coal particles is effected by adding hydrocarbon oil to the slurry at a temperature within the range from 20°

to 70°

C.

7. The process of claim 5 wherein the hydrocarbon oil is added to the slurry as an emulsion in water.

8. The process of claim 1 wherein the coal-oil aggregates contain from about 2 wt. % to about 10 wt. %, based on coal, of hydrocarbon oil.

9. The process of claim 1 wherein the coal-oil aggregates contain from about 3 wt. % to about 8 wt. %, based in coal, of hydrocarbon oil.

10. The process of claim 1 wherein the density-modified coal-oil aggregates are separated from the aqueous slurry by differential specific gravity means.

11. The process of claim 1 wherein the density-modified coal-oil aggregates are separated from the aqueous slurry by centrifugal means.

12. The process of claim 1 wherein the density-modified coal-oil aggregates are separated from the aqueous slurry by flotation means.

13. The process of claim 1 wherein the coal-oil aggregates are separated from the aqueous slurry, and a recovered lean aqueous slurry is reprocessed to effect substantially complete recovery of coal heating values.

14. The process of claim 1 wherein the gas is air.

15. The process of claim 1 wherein the coal is selected from the group consisting of bituminous and higher ranked coal.

16. The process of claim 1 wherein the ash content of the recovered coal is reduced by at least about 20%.

17. The process of claim 1 wherein the pyritic sulfur content of the recovered coal is reduced by at least about 40%.

18. The process of claim 1 wherein, prior to aggregation, the slurried coal particles are contacted with a promoting amount of at least one conditioning agent capable of modifying or altering the existing surface characteristics of the ash and pyritic sulfur mineral matter under conditions whereby there is effected modification or alteration of at least a portion of the contained ash and pyritic sulfur mineral matter.

19. The process of claim 18 wherein the conditioning agent is an inorganic compound capable of hydrolyzing in the presence of water.

20. The process of claim 19 wherein the conditioning agent is an inorganic compound hydrolyzable in water to form a high surface area inorganic gel.

21. The process of claim 19 wherein the conditioning agent is selected from the group consisting of metal oxides and hydroxides having the formula M_a O_b.xH₂ O or M(OH)_c.xH₂ O wherein M is Al, Fe, Co, Ni, Zn, Ti, Cr, Mn, Mg, Pb, Ca, Ba, In or Sb;

a, b and c are whole numbers dependent upon the ionic valence of M; and

x is a whole number within the range from 0 to 3.

22. The process of claim 21 wherein the conditioning agent is selected from the group consisting of calcium oxide, magnesium oxide and mixtures thereof.

23. The process of claim 21 wherein the conditioning agent is selected from the group consisting of aluminum oxide, aluminum hydroxide and mixtures thereof, hydrolyzed in water to form an alumina gel.

24. The process of claim 18 wherein the conditioning agent is selected from the group consisting of metal aluminates having the formula M'"'"'_d (AlO₃)_e or M'"'"'_f (AlO₂)_g, wherein M'"'"' is Fe, Co, Ni, Zn, Mg, Pb, Ca, Ba or Mo;

and de, e, f and g are whole numbers dependent upon the ionic valence of M'"'"'.

25. The process of claim 24 wherein the conditioning agent is selected from the group consisting of calcium, magnesium, and iron aluminates and mixtures thereof.

26. The process of claim 18 wherein the conditioning agent is selected from the group consisting of aluminosilicates having the formula Al₂ O₃.xSiO₂, wherein x is a number within the range from about 0.5 to about 5.0.

27. The process of claim 18 wherein the conditioning agent is selected from the group consisting of metal silicates wherein the metal is calcium, magnesium, barium, iron or tin.

28. The process of claim 27 wherein the conditioning agent is selected from the group consisting of calcium silicate, magnesium silicate and mixtures thereof.

29. The process of claim 18 wherein the conditioning agent is selected from the group consisting of inorganic cement materials capable of binding material matter.

30. The process of claim 29 wherein the conditioning agent is selected from the group consisting of portland cement, natureal cement, masonry cement, pozzolan cement, calcined limestone and calcined dolomite.

31. The process of claim 30 wherein the cement material is hydrolyzed portland cement.