Pre-burning, dry process methodology and systems for enhancing metallurgical solid fuel properties

• US 8,579,998 B2
• Filed: 08/06/2008
• Issued: 11/12/2013
• Est. Priority Date: 12/12/2003
• Status: Expired due to Fees

• Current Assignee: JY Capital Investment, LLC
• Original Assignee: Coaltek, Inc.
• Inventors: Weinberg, Jerry L., Ginther, Neil E., Aten, Jed A., Wang, Ru T.
• Primary Examiner(s): Toomer, Cephia D
• Application Number:
  US12/186,804
• Publication Number:
  US 20090038213A1
• Time in Patent Office: 1,924 Days
• Field of Search: 446/20, 446/26, 446/27, 449/03, 449/04
• US Class Current: 44/620
• CPC Class Codes: C10B 57/10 Drying
• 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: F23K 1/00 Preparation of lump or pulverulent fuel in readiness for delivery to combustion apparatus
• CPC Class Codes: F26B 3/347 Electromagnetic heating, e.g. induction heating or heating using microwave energy
• CPC Class Codes: Y02P 20/129 Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
• CPC Class Codes: Y10S 44/903 Method including measuring, testing or automatic control
• CPC Class Codes: Y10S 44/904 Method involving electric or wave energy

Abstract

Measurements are taken of moisture, BTU/lb (British Thermal Units per pound), ash, forms of sulfur, volatile material, grindability, and absorption properties of any of a wide variety of mine-run solid fuels. Using that information, a dry electromagnetic process technology has been developed that can be controlled and monitored to selectively alter and enhance metallurgical solid fuel properties. Specific changes include altering the mechanical structure and chemical composition of solid fuels such as coal, coal coke or petroleum coke, increasing the BTU/lb to optimum levels, decreasing all forms of sulfur, and decreasing ash, while maintaining the BTU/lb of the fuels. A new family of solid fuel designer coals not found in nature can be produced via these methods and apparatus.

Claims

1. A method comprising:

receiving a desired end condition of a solid fuel;

determining a duration and a power level of a microwave emission for each of a series of microwave generators based on the desired end condition; and

sequentially irradiating the solid fuel with the microwave emissions from the series of microwave generators at the determined power levels for the determined durations, thereby processing the solid fuel to the desired end condition, wherein said determining of the duration and the power level of the microwave emissions for each of the series of microwave generators is changed based on maintaining a measured solid fuel temperature not exceeding about 100 degrees Celsius during processing.

2. The method of claim 1, wherein the solid fuel temperature during treatment is about 70 degrees Celsius to about 100 degrees Celsius.

3. The method of claim 1, wherein a plurality of power levels are employed in a pre-determined sequence to obtain a targeted release of different components from solid fuel.

4. The method of claim 1, wherein the solid fuel is coal.

5. The method of claim 4, wherein the solid fuel is not in the form of a slurry.

6. The method of claim 4, wherein the solid fuel is crushed or screened to limit the solid fuel to particles having a diameter of about 8 inches or less.

7. The method of claim 1, further comprising pre-heating the solid fuel before irradiation, wherein the pre-heat and irradiation are applied to control a targeted property of the solid fuel.

8. The method of claim 7, wherein the targeted property is the release of moisture.

9. The method of claim 7, wherein pre-heating the solid fuel includes pre-heating the air in a chamber into which the solid fuel is disposed.

10. The method of claim 7, wherein pre-heating comprises the use of microwave energy.

11. The method of claim 1, wherein the solid fuel is processed in a chamber, the method comprising flowing air through the chamber during processing.

12. The method of claim 11, wherein the air is supplied at a sufficient flow rate to carry away moisture-laden gas.

13. The method of claim 1, wherein the electromagnetic radiation processing increases the BTU/pound of the solid fuel by at least 200 BTU/pound.

14. The method of claim 1, wherein the solid fuel is processed in a chamber, the method further comprising flowing inert gas through the chamber during processing.

15. The method of claim 1, wherein the desired end condition of the solid fuel comprises percent moisture.

16. The method of claim 1, wherein the processing selectively reduces the percent moisture in the solid fuel from at least about one percent up to ninety-eight percent.

17. The method of claim 1, wherein the irradiating is applied to promote release of at least some ash from the solid fuel.

18. The method of claim 1, wherein the irradiating is applied to obtain a release of sulfur from the solid fuel.

19. The method of claim 1, wherein the irradiating reduces a percent pyrite in the solid fuel by at least about three percent.

20. A system comprising:

means for receiving a raw solid organic fuel;

means for receiving a desired end condition of the raw solid organic fuel;

means for determining a duration and a power level of a microwave emission for each of a series of microwave generators based on the desired end condition; and

means for sequentially irradiating the raw solid fuel with the microwave emissions from the series of microwave generators at the determined power levels for the determined durations, thereby processing the raw solid organic fuel to the desired end condition, wherein the duration and the power level of the microwave emission for each of the series of microwave generators is changed based on a measurement of one or more properties of the raw solid organic fuel during said processing.

21. A method comprising:

receiving a desired end condition of a solid organic fuel;

determining a duration and a power level of a microwave emission for each of a series of microwave generators based on the desired end condition; and

sequentially irradiating the solid organic fuel with the microwave emissions from the series of microwave generators at the determined power levels for the determined durations, thereby processing the solid organic fuel to the desired end condition, wherein said determining of the duration and the power level of the microwave emissions for each of the series of microwave generators is changed based on maintaining a measured solid organic fuel temperature not exceeding about 100 degrees Celsius during processing.