Apparatus and method of enhancing the quality of high-moisture materials and separating and concentrating organic and/or non-organic material contained therein

• US 8,062,410 B2
• Filed: 04/11/2007
• Issued: 11/22/2011
• Est. Priority Date: 10/12/2004
• Status: Active Grant

• Current Assignee: Rainbow Energy Center LLC
• Original Assignee: Great River Energy
• Inventors: Sarunac, Nenad, Weinstein, Richard S., Bullinger, Charles W., James, Dennis R., Levy, Edward K., Coughlin, Matthew P., Wheeldon, John M., Ness, Mark A.
• Primary Examiner(s): Hopkins; Robert A
• Application Number:
  US11/786,321
• Publication Number:
  US 20080201980A1
• Time in Patent Office: 1,686 Days
• Field of Search: 952/88
• US Class Current: 95/288
• CPC Class Codes: B03B 4/06 using fixed and inclined tables ; using stationary pneumatic tables, e.g. fluidised beds
• CPC Class Codes: C10J 2300/094 Char
• CPC Class Codes: C10J 2300/0956 Air or oxygen enriched air
• CPC Class Codes: C10J 2300/165 integrated with a gas turbine or gas motor gas turbine plants provided with a gas producer F02C3/28; engines using solid fuels F02B43/08
• CPC Class Codes: C10J 2300/1671 with the production of electricity
• CPC Class Codes: C10J 3/482 Gasifiers with stationary fluidised bed
• CPC Class Codes: C10L 9/08 by heat treatments, e.g. calcining
• CPC Class Codes: F23K 1/04 Heating fuel prior to delivery to combustion apparatus
• CPC Class Codes: F23K 2201/20 Drying
• CPC Class Codes: F23K 2201/30 Separating
• CPC Class Codes: F26B 23/001 using waste heat
• CPC Class Codes: F26B 3/084 with heat exchange taking place in the fluidised bed , e.g. combined direct and indirect heat exchange
• CPC Class Codes: Y02P 20/129 Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
• CPC Class Codes: Y02P 70/10 Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Abstract

The present invention harvests and utilizes fluidized bed drying technology and waste heat streams augmented by other available heat sources to dry feedstock or fuel. This method is useful in many industries, including coal-fired power plants. Coal is dried using the present invention before it goes to coal pulverizers and on to the furnace/boiler arrangement to improve boiler efficiency and reduce emissions. This is all completed in a low-temperature, open-air system. Also included is an apparatus for segregating particulate by density and/or size including a fluidizing bed having a particulate receiving inlet for receiving particulate to be fluidized. This is useful for segregating contaminants like sulfur and mercury from the product stream.

Claims

1. A method for heat treating a feed, byproduct, or product stream within an industrial plant operation that produces at least two different types of waste heat, such method comprising:

(a) providing a heat treatment apparatus for receiving the feed, byproduct, or product stream, including means for receiving the heat content of at least two different sources of heat to be applied to the feed, byproduct, or product stream;

(b) providing a first heat exchanger operatively connected to a thermal mixer that is operatively connected to the heat treatment apparatus;

(c) providing a first waste heat source to the first heat exchanger;

(d) providing a second heat exchanger operatively connected to the thermal mixer;

(e) providing a second waste heat source different in type from the first waste heat source to the second heat exchanger;

(f) combining predetermined amounts of heat content contained within the first waste heat source and the second waste heat source within the thermal mixer for delivering an aggregate heat content characterized by a predetermined temperature to or within the heat treatment apparatus; and

(g) maintaining the feed, byproduct, or product stream within the heat treatment apparatus exposed to a desired amount of the aggregate heat content for a sufficient time duration to achieve the desired degree of heat treatment.

2. The method of claim 1, wherein the thermal mixer comprises a mixing box located outside the heat treatment apparatus for blending the first waste heat source and the second waste heat source.

3. The method of claim 1, wherein the thermal mixer comprises a heat transfer loop including a third heat exchanger and a fourth heat exchanger, wherein the first waste heat source is provided to the third heat exchanger, and the second waste heat source is provided to the fourth heat exchanger.

4. The method of claim 1 further comprising at least one additional heat source delivered to the heat treatment apparatus by means of an associated heat exchanger to which was provided an additional heat source.

5. The method of claim 4, wherein the additional heat source is a waste heat source.

6. The method of claim 4, wherein the additional heat source is a principal heat source.

7. The method of claim 1 further comprising delivery of the first waste heat source, the second waste heat source, or the combined waste heat source to a further heat exchanger for preheating the feed, byproduct, or product stream supplied to the heat treatment apparatus.

8. The method of claim 1 further comprising a cooler operatively connected to the downstream end of the heat treatment apparatus, wherein the heat-treated feed, byproduct, or product is delivered by the heat treatment apparatus to the cooler for a sufficient time to reduce the heat treated product to a predetermined temperature.

9. The method of claim 8, wherein the cooler comprises an integral part of the heat treatment apparatus.

10. The method of claim 8, wherein the cooler comprises a separate cooling apparatus.

11. The method of claim 1, wherein the heat treatment apparatus comprises a fixed bed dryer.

12. The method of claim 1, wherein the heat treatment apparatus comprises a fluidized bed dryer utilizing a fluidizing medium.

13. The method of claim 12, wherein the fluidizing medium that is supplied to the fluidized bed dryer is heated by the aggregate heat content delivered by the thermal mixer.

14. The method of claim 8 further comprising a fluidizing medium delivered to the cooler at a predetermined temperature.

15. The method of claim 14, wherein the predetermined temperature of the fluidizing medium is achieved by treatment by at least one waste heat source.

16. The method of claim 1, wherein the waste heat sources are selected from the group consisting of hot condenser cooling water, hot stack gas, hot flue gas, spent process stream, and discarded heat from operating equipment.

17. The method of claim 1, wherein the product is coal.

18. The method of claim 17, wherein the coal product is lignite coal.

19. The method of claim 17, wherein the coal product is subbituminous coal.

20. The method of claim 17, wherein the heat treatment process comprises a reduction in moisture content of the coal.

21. The method of claim 20, wherein the coal product is lignite coal whose moisture content is reduced by about 20-26% wt on a relative basis and by about 7-9% wt on an absolute basis.

22. The method of claim 1, wherein the temperature delivered to the heat treatment apparatus by the aggregate heat content does not exceed about 300°

F.

23. The method of claim 1, wherein the industrial plant operation is an electric power plant.

24. The method of claim 23, wherein the waste heat source delivered to the first heat exchanger and the second heat exchanger constitute the same waste heat source within the industrial plant operation.

25. The method of claim 12, wherein the fluidizing medium comprises air.

26. The method of claim 12, wherein the fluidizing medium comprises steam.

27. The method of claim 12, wherein the fluidizing medium comprises an inert gas.

28. The method of claim 1, wherein the feed, byproduct, or product stream material is treated in the heat treatment apparatus in the presence of atmospheric air.

29. The method of claim 1, wherein the feed, byproduct, or product stream material is treated in the heat treatment apparatus in the absence of an inert gas.

30. The method of claim 1, wherein the feed, byproduct, or product stream material is treated in the heat treatment apparatus without the delivery of steam to the heat treatment apparatus.

31. The method of claim 20, wherein the moisture-reduced coal is combusted to produce an increase in higher heating value (HHV) of about 14-21%.

32. The method of claim 1, wherein the thermal mixer comprises a third heat exchanger and a fourth heat exchanger positioned in series, wherein the first waste heat source is provided to the third heat exchanger, and the second waste heat source is provided to the fourth heat exchanger, and a fluidizing stream passing through the third heat exchanger followed by the fourth heat exchanger has its temperature cumulatively increased by the aggregate heat content before it is delivered to the heat treatment apparatus.

33. The method of claim 1, wherein the thermal mixer comprises a third heat exchanger located inside the heat treatment apparatus, wherein the first waste heat source is provided to the third heat exchanger, and the second waste heat source is provided to the third heat exchanger with the aggregate heat content within the third heat exchanger exposed to the feed, byproduct, or product stream maintained within the heat treatment apparatus.

34. A method for reducing the moisture of a particulate material within an industrial plant operation that produces at least two sources of waste heat, such method comprising:

(a) providing a dryer bed for receiving the particulate material, including means for receiving a source of heat to be applied to the particulate material;

(b) providing a first heat exchanger and a first thermal carrier medium operatively connected to a thermal mixer that is operatively connected to the dryer;

(c) providing a first waste heat source to the first heat exchanger whereby a desired amount of heat content contained within the first waste heat source is transferred to the first thermal carrier medium which is delivered as one of the heat sources to the thermal mixer;

(d) providing at least one additional heat exchanger and associated thermal carrier media operatively connected to the thermal mixer;

(e) providing at least one additional waste heat source different in type from the first waste heat source to the additional heat exchanger whereby heat content contained within the additional waste heat source is transferred to the additional thermal carrier medium which is delivered as an additional heat source to the thermal mixer;

(f) blending the first waste heat source and the additional waste heat source(s) within the thermal mixer to produce an aggregate heat content characterized by a predetermined temperature that is about 300°

F. or less; and

(g) maintaining the particulate material within the dryer bed exposed to the aggregate heat content for a sufficient time duration to achieve the desired degree of moisture reduction.

35. A method used within an industrial plant operation for heat treating a feed, byproduct, or product stream comprising a heat input, wherein a source of waste heat at a temperature of about 300°

F. or less supplies the heat input further comprising;

(a) a heat treatment apparatus for receiving the feed, byproduct, or product stream, including means for receiving the heat content of at least two different sources of waste heat to be applied to the feed, byproduct, or product stream;

(b) providing a first heat exchanger operatively connected to a thermal mixer that is operatively connected to the heat treatment apparatus;

(c) providing a first waste heat source to the first heat exchanger;

(d) providing at least one additional heat exchanger operatively connected to the thermal mixer;

(e) providing at least one additional waste heat source different in type from the first waste heat source to the additional heat exchanger;

(f) said thermal mixer including a third heat exchanger and a fourth heat exchanger, wherein a predetermined amount of heat content of the first waste heat source is provided to the third heat exchanger, and a predetermined amount of heat content of the additional waste heat source is provided to the fourth heat exchanger;

(g) combining predetermined amounts of heat content contained within the first waste heat source and the additional waste heat source within the thermal mixer to produce an aggregate heat content characterized by a predetermined temperature;

(h) maintaining the feed, byproduct, or product stream within the heat treatment apparatus exposed to a desired amount of the aggregate heat content for a sufficient time duration to achieve the desired degree of heat treatment; and

(i) removing the feed, byproduct, or product stream from the heat treatment apparatus.

36. The method of claim 35, wherein the waste heat source is selected from the group consisting of hot condenser cooling water, hot stack gas, hot flue gas, spent process stream, and discarded heat from operating equipment.

37. The method of claim 35, wherein the industrial plant operation comprises a regeneration process for amines or other extractants used in carbon dioxide or organic acid sequestration.

38. The method of claim 35, wherein the industrial plant operation comprises a pulping mill.

39. The method of claim 35, wherein the industrial plant operation comprises a refuse-derived fuel combustion plant.

40. The method of claim 35, wherein the industrial plant operation comprises a food processing facility.

41. The method of claim 35, wherein the industrial plant operation comprises a green house.

42. The method of claim 35, wherein the industrial plant operation comprises heating or district heating of a factory or building.

43. The method of claim 35, wherein the industrial plant operation comprises a drying operation for grains or other agricultural materials.