Methods and systems for briquetting solid fuel

• US 8,585,786 B2
• Filed: 10/07/2008
• Issued: 11/19/2013
• Est. Priority Date: 03/31/2006
• Status: Expired due to Fees

• Current Assignee: JY Capital Investment, LLC
• Original Assignee: Coaltek, Inc.
• Inventors: Drozd, J. Michael, Lawson, Steven L., Druga, Michael C., Lang, Frederick Christopher, Surma, Jan M., Bullis, Herbie L.
• Primary Examiner(s): Toomer, Cephia D
• Application Number:
  US12/247,004
• Publication Number:
  US 20090119981A1
• Time in Patent Office: 1,869 Days
• Field of Search: 445/53, 445/77, 445/79, 445/92, 445/96, 446/08, 446/20, 446/26, 449/04
• US Class Current: 44/553
• CPC Class Codes: C10L 5/361 Briquettes
• CPC Class Codes: C10L 5/363 Pellets or granulates
• CPC Class Codes: C10L 9/00 Treating solid fuels to improve their combustion
• CPC Class Codes: C10L 9/08 by heat treatments, e.g. calcining
• CPC Class Codes: F23G 2900/50206 Pelletising waste before combustion
• CPC Class Codes: F23K 1/00 Preparation of lump or pulverulent fuel in readiness for delivery to combustion apparatus
• CPC Class Codes: F23K 2201/101 to a specific particle size
• CPC Class Codes: F23K 2201/20 Drying
• CPC Class Codes: F23K 2201/505 with additives
• CPC Class Codes: F23K 2900/01001 Cleaning solid fuel before combustion to achieve reduced emissions
• CPC Class Codes: F23K 2900/01002 Treating solid fuel with electromagnetic fields before combustion

Abstract

In embodiments of the present invention improved capabilities are described for a system and method for briquetting solid fuel before or after treatment with electromagnetic energy. In the system and method, solid fuel is transported through a continuous feed solid fuel treatment facility, treated using electromagnetic energy, and briquetted after treatment.

Claims

1. A method of forming a solid fuel briquette, comprising:

transporting solid fuel through a continuous feed solid fuel treatment facility;

treating the solid fuel using energy from an electromagnetic energy system of the solid fuel treatment facility as it is moved through the treatment facility; and

briquetting the treated solid fuel by applying pressure to the treated solid fuel with a briquetting facility to form a solid fuel briquette;

wherein;

the solid fuel is at an elevated temperature of between 160 degrees F. and about 240 degrees F. as it enters the briquetting facility, and

the briquetting facility variable adjusts at least one or more properties in order to obtain a desired characteristic of a briquette, the one or more properties selected from a group consisting of;

roll-torque, screw-torque, roll force, and screw force.

2. The method of claim 1 further comprising reducing the size of the solid fuel prior to briquetting.

3. The method of claim 2, wherein reducing the size comprises grinding and/or crushing the solid fuel before entering the treatment facility.

4. The method of claim 2, wherein reducing the size comprises grinding and/or crushing the solid fuel to less than ⅛

inch.

5. The method of claim 1, wherein a binder is added to the solid fuel.

6. The method of claim 5, wherein the binder is at least one of a starch, a wheat starch, a corn starch, a sugar, molasses, saw dust, gilsonite, ground asphalt, rosin, plastic, guar gum, lignin and polyethylene terephthalate (PET).

7. The method of claim 5, wherein the binder is added before sizing the solid fuel.

8. The method of claim 5, wherein the binder is added after sizing the solid fuel but prior to treatment.

9. The method of claim 5, wherein the binder is added after treatment but prior to briquetting.

10. The method of claim 1, wherein the solid fuel is at least one of a wood-based product, an agro-forestry product, a biomass product, and coal.

11. The method of claim 10, wherein the coal is at least one of sub-bituminous coal, lignite coal, peat, anthracite, metallurgical coal, and bituminous coal.

12. The method of claim 10 wherein the coal is coal fines.

13. The method of claim 12, wherein the size of the coal fines is less than 28 mesh.

14. The method of claim 12, wherein the coal fines are in at least one of a slurry, sludge, or paste.

15. The method of claim 12, wherein the fines are from a metallurgic coal wash process.

16. The method of claim 12, wherein the fines are from a waste coal area or impoundment.

17. The method of claim 1, wherein the electromagnetic energy is microwave energy.

18. The method of claim 1, wherein the electromagnetic energy is RF energy.

19. The method of claim 1, wherein the electromagnetic energy operates at a frequency between about 900 and 930 MHz.

20. The method of claim 1, wherein the electromagnetic energy operates at a power of about 50 kW or greater.

21. The method of claim 1, further comprising, elevating the temperature of the solid fuel as it enters the briquetting facility.

22. The method of claim 21, wherein the temperature is at least 60°

F.

23. The method of claim 21, wherein when the solid fuel is sub-bituminous coal, the temperature is at least 150°

F.

24. The method of claim 21, wherein when the solid fuel is bituminous coal, the temperature is at least 200°

F.

25. The method of claim 1, wherein the solid fuel is processed to a desired moisture content prior to entering the briquetting facility.

26. The method of claim 25, wherein the moisture content is below 12%.

27. The method of claim 25, wherein when the solid fuel is sub-bituminous coal, the moisture content is below 10%.

28. The method of claim 25, wherein when the solid fuel is sub-bituminous coal, the moisture content is above 2%.

29. The method of claim 25, wherein when the solid fuel is bituminous coal, the moisture content is below 5%.

30. The method of claim 1, further comprising adding a coating to the briquette.

31. The method of claim 30, wherein the coating is wax.

32. The method of claim 1, further comprising mixing additional solid fuel material with the treated solid fuel material.

33. The method of claim 32, wherein the additional solid fuel material is at least one of sub-bituminous coal, lignite coal, peat, anthracite, metallurgical coal, and bituminous coal.

34. The method of claim 32, wherein the additional solid fuel material has been treated using energy from an electromagnetic energy system.

35. The method of claim 1, wherein both of a binder and a coating are added to the briquette.

36. The method of claim 35, wherein the binder is at least one of saw dust, a starch, a wheat starch, a corn starch, a sugar, molasses, gilsonite, ground asphalt, rosin, plastic, guar gum, lignin, and polyethylene terephthalate (PET).

37. The method of claim 35, wherein the coating is wax.

38. The method of claim 10, wherein the solid fuel is at least one of a wood-based product, an agro-forestry product, and a biomass product.

39. The method of claim 38, further comprising adding a starch to the solid fuel prior to treatment in an amount between 0.5 to 5% by weight.

40. The method of claim 39, wherein the electromagnetic energy is microwave energy.

41. The method of claim 12, further comprising adding a starch to the solid fuel prior to treatment in an amount between 0.5 to 5% by weight.

42. The method of claim 41, wherein the electromagnetic energy is microwave energy.