Fine particle coal, and systems, apparatuses, and methods for collecting and using the same
Methods, apparatuses, and systems to collect fine particle coal are provided herein. For example, these methods, apparatuses, and systems may be incorporated into a coal processing plant to collect a portion of the fine particle coal that is normally lost in the system. A fine particle coal also is provided. The fine particle coal may have a particle size of 1000 μm or smaller and a water content of from about 5% to about 20%, by weight.
1. A method of collecting fine particle coal, the method comprising:
dewatering a clean coal effluent slurry having a solids content of from about 3% to about 17%, by weight, to produce a fine particle coal having—
(i) a particle size of 1000 μm or smaller, and
(ii) an ash content of from about 3% to about 28%, by weight,
wherein the dewatering of the clean coal effluent slurry comprises centrifuging the slurry in a solid bowl centrifuge, the centrifuge comprising a rotating bowl, an internal scroll, and a weir plate; and
adjusting, based on (i) properties of the clean coal effluent slurry, (ii) properties of the fine particle coal, or (iii) both, at least one parameter selected from the group consisting of centrifugal torque, differential rotational speed between the rotating bowl and the internal scroll, and dam height of the weir plate.
2. The method of claim 1 , wherein the fine particle coal has an ash content of from about 3% to about 15%, by weight.
3. The method of claim 1 , wherein the fine particle coal has an ash content of from about 5% to about 10%, by weight.
4. The method of claim 1 , wherein the fine particle coal has an ash content of less than 6%, by weight.
5. The method of claim 1 , wherein the particle size of the fine particle coal is 100 mesh or smaller.
6. The method of claim 1 , wherein the particle size of the fine particle coal is from about 30 μm to about 150 μm.
7. The method of claim 1 , wherein the step of dewatering occurs in a clean coal circuit of a coal processing plant.
8. The method of claim 1 , wherein the step of dewatering occurs downstream of processing that does not collect fine particle coal having a particle size of 325 mesh or smaller.
9. The method of claim 1 , wherein the step of dewatering occurs upstream of processing that does collect fine particle coal having a particle size of 325 mesh or smaller.
10. The method of claim 1 , wherein the fine particle coal has a BTU of from about 12,000 to about 16,000.
11. The method of claim 1 , wherein the fine particle coal has a BTU of from about 15,000 to about 16,000.
12. The method of claim 1 , wherein the fine particle coal has a total sulfur content of from about 0.3% to about 4.5%, by weight.
13. The method of claim 1 , wherein the fine particle coal has a total sulfur content of less than 0.8%, by weight.
14. The method of claim 1 , wherein the fine particle coal has a volatile matter content of from about 7% to about 37%, by weight.
15. The method of claim 1 , wherein the fine particle coal has a volatile matter content of from about 15% to about 20%, by weight.
16. The method of claim 1 , wherein the fine particle coal has an oxygen content of 20% or less, by weight.
17. The method of claim 1 , wherein the fine particle coal has an oxygen content of 2% or less, by weight.
18. A method of collecting fine particle coal, the method comprising:
dewatering a clean coal effluent slurry having a solids content of from about 3% to about 20%, by weight, to produce a fine particle coal having—
(i) a particle size of 1000 μm or smaller, and
(ii) an ash content of from about 3% to about 28%, by weight,
wherein the dewatering of the clean coal effluent slurry comprises centrifuging the slurry in a solid bowl centrifuge, the centrifuge comprising a rotating bowl, an internal scroll, and a weir plate; and
adjusting, based on (i) properties of the clean coal effluent slurry, (ii) properties of the fine particle coal, or (iii) both, at least one parameter selected from the group consisting of centrifugal torque, differential rotational speed between the rotating bowl and the internal scroll, and dam height of the weir plate.
19. The method of claim 18 , wherein the clean coal effluent slurry has a solids content of from about 3% to about 17%, by weight.
20. The method of claim 18 , wherein the fine particle coal has an ash content of from about 3% to about 15%, by weight.
21. The method of claim 18 , wherein the fine particle coal has a total sulfur content of from about 0.3% to about 4.5%, by weight.
22. The method of claim 18 , wherein the fine particle coal has a volatile matter content of from about 7% to about 37%, by weight.
23. The method of claim 18 , wherein the fine particle coal has a volatile matter content of from about 15% to about 20%, by weight.