초록 ▼

The ash content of raw coals, lignite, and other carbonaceous materials is reduced by leaching the high-ash material with an aqueous acidic waste product produced by a Fischer-Tropsch reaction. The acidic aqueous waste is mixed with coal and process conditions are described. The claim takes advanta

The ash content of raw coals, lignite, and other carbonaceous materials is reduced by leaching the high-ash material with an aqueous acidic waste product produced by a Fischer-Tropsch reaction. The acidic aqueous waste is mixed with coal and process conditions are described. The claim takes advantage of using otherwise uneconomic coal, lignite or other carbonaceous material by upgrading the material to a suitable feedstock for combustion in a power plant or gasifier.

대표청구항 ▼

What is claimed is: 1. A method of leaching soluble ash from a coal comprising: a. contacting a coal with an aqueous Fischer-Tropsch waste; and, b. separating the coal from at least a portion of the aqueous Fischer-Tropsch waste, wherein ash present in the coal is dissolved in the aqueous fischer-T

What is claimed is: 1. A method of leaching soluble ash from a coal comprising: a. contacting a coal with an aqueous Fischer-Tropsch waste; and, b. separating the coal from at least a portion of the aqueous Fischer-Tropsch waste, wherein ash present in the coal is dissolved in the aqueous fischer-Tropsch waste and removed from the coal in the aqueous Fischer-Tropsch waste. 2. The method of claim 1, wherein the coal is selected from the group consisting of lignite, bituminous coal and subbituminous coal. 3. The method of claim 1, wherein the coal has a particle size between about 0.5 mm and about 15 mm in the longest dimension. 4. The method of claim 1, wherein the coal has a particle size between about 1 mm and about 2 mm in the longest dimension. 5. The method of claim 1, wherein the contacting comprises agitating the coal and the aqueous Fischer-Tropsch waste in a vessel. 6. The method of claim 5, wherein the agitating is conducted for a period of time between about 1 minute and about 30 minutes. 7. The method of claim 5, wherein the agitating is conducted for a period of time between about 3 minutes and about 15 minutes. 8. The method of claim 5, wherein the agitating is conducted for a time of about 10 minutes. 9. The method of claim 5, wherein contents of the vessel are maintained at a temperature ranging from about 20째 C. to about 70째 C. 10. The method of claim 5, wherein contents of the vessel are maintained at a temperature ranging from about 40째 C. to about 65째 C. 11. The method of claim 5, wherein contents of the vessel are maintained at a temperature ranging from about 50째 C. to about 60째 C. 12. The method of claim 1, wherein the separating comprises filtering the coal from the aqueous Fischer-Tropsch waste. 13. The method of claim 1, wherein the separating comprises settling the coal in the aqueous Fischer-Tropsch waste. 14. The method of claim 1, wherein the ratio of the weight of the coal to the weight of the aqueous Fischer-Tropsch waste is between about 1:1 and about 1:50. 15. The method of claim 1, wherein the ratio of the weight of the coal to the weight of the aqueous Fischer-Tropsch waste is between about 1:5 and about 1:20. 16. The method of claim 1, wherein the ratio of the weight of the coal to the weight of the aqueous Fischer-Tropsch waste is about 1:10. 17. A method of leaching soluble ash from a coal comprising: a. crushing a raw coal to form a crushed coal having a particle size between about 0.5 mm and about 15 mm in the longest dimension; b. agitating the crushed coal in the presence of an aqueous Fischer-Tropsch waste to promote contact of the aqueous Fischer-Tropsch waste with the crushed coal and to leach ash present in the coal into the aqueous Fischer-Tropsch waste; and, c. separating the crushed coal from the aqueous Fischer-Tropsch waste to isolate a coal having a sodium content lower than the sodium content of the raw coal. 18. The method of claim 17, comprising the additional step of suspending the coal having a lower sodium content than the sodium content of the raw coal in an aqueous solution to prepare a slurry feed for gasification. 19. The method of claim 18, wherein the aqueous solution is an aqueous Fischer-Tropsch waste. 20. A method of leaching soluble ash from a coal comprising: a. contacting a coal with a liquid consisting of an aqueous Fischer-Tropsch waste; and, b. separating the coal from at least a portion of the liquid, wherein ash present in the coal is dissolved in the liquid and removed from the coal in the liquid. 21. A method of leaching soluble ash from a coal comprising: c. contacting a coal with a liquid consisting essentially of an aqueous Fischer-Tropsch waste; and, d. separating the coal from at least a portion of the liquid, wherein ash present in the coal is dissolved in the liquid, and removed from the coal in the liquid.