Claims
- 1. A process for producing a coal-water slurry, which comprises wet-grinding coal by means of a wet vertical ring-roll mill and recycling a part of the coal ground by the mill, as it is, without classifying it, to the mill through a splitter and discharging the coal-water slurry.
- 2. A process for producing a coal-water slurry according to claim 1 wherein said mill is a wet vertical ball-race mill.
- 3. A process for producing a coal-water slurry according to claim 1 wherein the quantity by weight of slurry recycled from said splitter to said ring-roll mill is 10 to 30 times the quantity of raw material coal fed to said mill on the basis of dry coal.
- 4. A process for producing a coal-water slurry according to claim 1 wherein a surfactant is added inside said vertical ring-roll mill to the ground coal.
- 5. A process for producing a coal-water slurry according to claim 4 wherein the proportion of coal is 50 to 80% and that of said surfactant is 0.05 to 3.0%, each based on the total weight of coal, water and surfactant at the time of grinding.
- 6. A process for producing a coal-water slurry according to claim 1 wherein said wet-grinding is carried out without adding any surfactant, followed by dehydrating the resulting slurry by means of a dehydrator until the coal concentration reaches 50 to 80% by weight, adding a surfactant in a quantity of 0.05 to 3.0% by weight based on the weight of coal to the dehydrated mixture of coal with water and agitating the resulting mixture.
- 7. A process for producing a coal-water slurry according to claim 1 wherein after said wet-grinding, the resulting slurry is subjected to a deashing operation, followed by dehydrating the deashed slurry until the coal concentration reaches 50 to 80% by weight, adding a surfactant in a quantity of 0.05 to 3% by weight based on coal to the dehydrated mixture of coal with water and agitating the resulting mixture.
- 8. A process for producing a coal-water slurry according to claim 3, wherein the quantity by weight of slurry recycled from said splitter to said ring-roll mill is 15 to 25 times the quantity of raw material coal fed to said mill on the basis of dry coal.
- 9. A process for producing a coal-water slurry according to claim 1, wherein, before the coal-water slurry is discharged, it is fed to a coarse particle-separator to remove coal particles having a size greater than about 300 to 1,000 .mu.m contained in the slurry, said coarse particles then being recycled to the ring-roll mill.
- 10. A process for producing a coal-water slurry according to claim 9, wherein the ratio of coal-water slurry flowing into the coarse particle-separator to the coal-water slurry recyling to the ring-roll mill is in the range of 1 to 1-35.
- 11. A process for producing a coal-water slurry according to claim 10, wherein the ratio is 1 to 10-25.
- 12. A process for producing a coal-water slurry according to claim 5, wherein the amount of coal recycled from the splitter to the ring-roll mill is 10 to 30 times the quantity of raw maerial coal fed.
- 13. A process for processing a coal-water slurry according to claim 12, wherein the amount of coal recycled is 15 to 25 times the quantity of raw material coal fed.
- 14. A process for producing a coal-water slurry according to claim 9, wherein the amount of coal ground in the mill is about 40% by weight and the proportion of 200 mesh pass coal particles in the discharged coal-water slurry is about 70% and further wherein water is added to the resulting slurry until the coal concentration is about 5% by weight, followed by deashing the resulting slurry, concentrating the deashed slurry until the coal concentration is about 80% by weight and adding 0.5% by weight of a surfactant, based on the weight of the coal.
- 15. A process for producing a coal-water slurry according to claim 12, wherein, before the coal-water slurry is discharged, it is fed to a coarse particle-separator to remove coal particles having a size greater than about 300 to 1,000 .mu.m contained in the slurry, said coarse particles then being recycled to the ring-roll mill.
- 16. A process for producing a coal-water slurry according to claim 15, wherein the quantity by weight of slurry recycled from said splitter to said ring-roll mill is 15 to 25 times the quantity of raw material coal fed to said mill on the basis of dry coal.
- 17. A process for producing a coal-water slurry according to claim 5, wherein, before the coal-water slurry is discharged, it is fed to a coarse particle-separator to remove coal particles having a size greater than about 300 to 1,000 .mu.m contained in the slurry, said coarse particles then being recycled to the ring-roll mill.
- 18. A process for producing a coal-water slurry according to claim 17, wherein the ratio of coal-water slurry flowing into the coarse particle-separator to the coal-water slurry recyling to the ring-roll mill is in the range of 1 to 1-35.
- 19. A process for producing a coal-water slurry according to claim 9, wherein the quantity by weight of slurry recycled from said splitter to said ring-roll mill is 10 to 30 times the quantity of raw material coal fed to said mill on the basis of dry coal.
- 20. A process for producing a coal-water slurry according to claim 19, wherein the amount of coal recycled is 15 to 25 times the quantity of raw material coal fed.
- 21. A process for producing a coal-water slurry product, comprising:
- minimizing the power consumption for grinding coal to product said product, said product having a broad coal particle size distribution and a 50% to 80% by weight concentration of coal, by grinding the coal with water and a surfactant present in the amoount of 0.05% to 3% by weight based upon the weight of the coal in a wet vertical ring-roll mill to obtain a coal-water slurry, providing a splitter for splitting off a portion of said slurry before classifying the slurry and discharging the remainder of said slurry, and increasing the concentration of fine coal particles in said slurry by recycling said portion of said slurry to said wet vertical ring-roll mill; and
- separating the coarse particles from said discharged coal-water slurry by removing the coal particles having a size greater than aobut 300 to 1,000 .mu.m to obtain said coal-water slurry product.
Priority Claims (1)
Number |
Date |
Country |
Kind |
59-203761 |
Sep 1984 |
JPX |
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Parent Case Info
This application is a continuation of application Ser. No. 781,011, filed 9/27/85.
US Referenced Citations (14)
Foreign Referenced Citations (2)
Number |
Date |
Country |
0370763 |
Oct 1983 |
ATX |
3121979 |
Feb 1982 |
DEX |
Continuations (1)
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Number |
Date |
Country |
Parent |
781011 |
Sep 1985 |
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