EDGE AIR NOZZLES FOR BELT-TYPE SEPARATOR DEVICES

• US 20160236206A1
• Filed: 02/13/2015
• Published: 08/18/2016
• Est. Priority Date: 02/13/2015
• Status: Active Grant

• Current Assignee: Separation Technologies LLC (Titan Cement International SA)
• Original Assignee: Separation Technologies LLC (Titan Cement International SA)
• Inventors: Bush, Ted W., Flynn, Kyle P., Leaf, Harry Vincent, Sert, Bulent
• Granted Patent: US 9,764,332 B2
• Time in Patent Office: Days
• US Class Current: 1/1
• CPC Class Codes: B03C 3/34 Constructional details or accessories or operation thereof
• CPC Class Codes: B03C 7/006 Charging without electricity supply, e.g. by tribo-electricity or pyroelectricity
• CPC Class Codes: B03C 7/08 with material carriers in the form of belts

Abstract

An improved belt separator system and an improved method to separate particle mixtures based on triboelectric separation of particles is disclosed. One or more gas nozzles, for example, a plurality of gas nozzles are provided as part of the system or installed into a system, such as an existing system, to improve dispersal of particles during operation.

Claims

1. A belt separator system comprising:

a first electrode and a second electrode arranged on opposite sides of a longitudinal centerline and configured to provide an electric field between the first and second electrodes;

a first roller disposed at a first end of the system;

a second roller disposed at a second end of the system;

a continuous belt disposed between the first and second electrodes and supported by the first roller and the second roller;

a separation zone defined by and between the continuous belt; and

a plurality of gas nozzles positioned at periodic locations along a wall of the system to deliver gas to the separation zone.

2. The belt separator system of claim 1, further comprising a source of gas fluidly connected to an inlet of at least one gas nozzle of the plurality of gas nozzles.

3. The belt separator system of claim 2, wherein the source of gas is a pressurized gas.

4. The belt separator system of claim 2, wherein the source of gas is pressurized air.

5. The belt separator system of claim 3, wherein the source of gas is at a selected relative humidity condition to provide a pre-determined relative humidity in the separation zone.

6. The belt separator system of claim 5, wherein the pre-determined relative humidity is in a range of about 0% to about 75% in the separation zone.

7. The belt separator system of claim 3, wherein the source of gas is at a selected temperature condition to provide a pre-determined temperature in the separation zone.

8. The belt separator system of claim 7, wherein the pre-determined temperature is in a range of about 60°

F. to about 250°

F. in the separation zone.

9. The belt separator system of claim 5, wherein the source of gas is at a selected temperature condition to provide a pre-determined temperature in the separation zone.

10. The belt separator system of claim 9, wherein the pre-determined relative humidity is in a range of about 0% to about 75% and the pre-determined temperature is in a range of about 60°

F. to about 250°

F. in the separation zone.

11. The belt separator system of claim 5, wherein the pre-determined relative humidity is provided through at least one of dehumidification, steam addition, and liquid water addition to the source of gas.

12. The belt separator system of claim 5, wherein the gas is conditioned to have a relative humidity about equal to a relative humidity of a process air in the separation zone.

13. The belt separator system of claim 5, wherein the gas is dry air.

14. The belt separator system of claim 3, wherein the source of pressurized gas is at ambient conditions.

15. The belt separator system of claim 1, wherein the plurality of gas nozzles are configured to deliver pressurized gas on at least one of a continuous basis and an intermittent basis.

16. The belt separator system of claim 15, further comprising a timing device to provide gas at the intermittent basis at a pre-determined interval.

17. The belt separator system of claim 16, wherein the pre-determined interval is between about zero seconds to about 30 seconds.

18. The belt separator system of claim 17, wherein the pre-determined interval is about 10 seconds.

19. The belt separator system of claim 3, wherein the plurality of gas nozzles are configured to deliver pressurized gas at a pressure of about 10 pounds per square inch gauge (psig) to about 100 psig.

20. The belt separator system of claim 18, wherein the plurality of gas nozzles are configured to deliver pressurized gas at a pressure of about 15 psig to about 25 psig.

21. The belt separator system of claim 20, wherein the plurality of gas nozzles are configured to deliver pressurized gas at a pressure of about 25 psig.

22. The belt separator system of claim 19, wherein the plurality of gas nozzles are configured to deliver pressurized gas at a pressure of about 60 psig.

23. The belt separator system of claim 1, wherein the plurality of air nozzles are positioned to maximize fluidizing a powder to be separated in the system, without exposing the air nozzles to an abrasive high shear zone created by the continuous belt.

24. The belt separator system of claim 23, wherein the plurality of gas nozzles are positioned at an angle in a range of about 90 degrees to a direction of travel of the continuous belt to 45 degrees from normal relative to the direction of travel of the belt.

25. The belt separator system of claim 1, further comprising an abrasion resistant, electrically insulating, ceramic material positioned on the wall of the system, internally to the separation zone.

26. The belt separator system of claim 1, wherein the plurality of air nozzles are installed through the wall of the system and an abrasion resistant liner positioned adjacent the wall and the separation zone.

27. The belt separator system of claim 5, wherein the source of gas is fluidly connected to at least one of a dehumidification system, a source of steam, and a source of liquid water.

28. The belt separator system of claim 1, wherein the continuous belt comprises periodic notches formed within a longitudinal edge at periodic locations in the longitudinal edge of the belt, the periodic notches configured for conveying components of a difficult-to-fluidize material in a direction along a longitudinal direction of the belt separator system.

29. The system of claim 28, wherein the notches formed in the longitudinal edge of the belt have a beveled edge.

30. The system of claim 29, wherein the bevel edge of each notch has a radius in a range of 4-5 mm.

31. The system of claim 28, wherein the notches formed in the longitudinal edge of the belt have a triangular-shape.

32. The system of claim 28, wherein a leading edge of the notch has an angle in a range from about 12°

to about 45°

with respect to the longitudinal edge.

33. The system of claim 28, wherein a trailing edge of the notch is perpendicular with respect to the longitudinal edge.

34. The system of claim 28, wherein the belt includes counter-current belt segments traveling in opposite directions along the longitudinal direction.

35. The system of claim 28, wherein the notches in the longitudinal edges have dimensions selected to maximize throughput of the belt separator system for a difficult-to-fluidize material.

36. The system of claim 28, wherein the notch in the longitudinal edge has dimensions selected to maximize an operating lifetime of the belt for a difficult-to-fluidize material.

37. The system of claim 28, wherein the belt has a width about 1 to 5 millimeters short of a width of the inside of the belt separator system and the edges in the longitudinal edges of the belt are configured to sweep components of the difficult-to-fluidize material away from the inside edge of the separation system.

38. A method of fluidizing a particle mixture within a belt separator system comprising:

introducing the particle mixture to a feed port of the belt separator system, the system comprising;

a first electrode and a second electrode arranged on opposite sides of a longitudinal centerline and configured to provide an electric field between the first and second electrodes;

a first roller disposed at a first end of the system;

a second roller disposed at a second end of the system;

a continuous belt disposed between the first and second electrodes and supported by the first roller and the second roller; and

a separation zone defined by and between the continuous belt; and

delivering a gas through a gas nozzle positioned along a wall of the system to deliver gas to the separation zone.

39. The method of claim 38, wherein delivering the gas through the gas nozzle comprises delivering a pressurized gas.

40. The method of claim 38, wherein delivering the gas through the gas nozzle comprises delivering a gas intermittently, for a pre-determined interval.

41. The method of claim 40, further comprising delivering the gas through the gas nozzle intermittently at a pre-determined interval of between about zero seconds to about 30 seconds.

42. The method of claim 41, wherein the pre-determined interval is about 10 seconds.

43. The method of claim 38, wherein delivering a gas through a gas nozzle comprises delivering the gas through a gas nozzle at a pressure of about 10 pounds per square inch gauge (psig) to about 100 psig.

44. The method of claim 43, wherein the plurality of gas nozzles are configured to deliver pressurized gas at a pressure of about 15 psig to about 25 psig.

45. The method of claim 44, wherein the pressure is about 25 psig.

46. The method of claim 43, wherein the pressure is about 60 psig.

47. The method of claim 38, further comprising operating the continuous belt at a velocity between about 10 feet per second (3.0 meters per second) and about 100 feet per second (30.5 meters per second).

48. The method of claim 38, wherein delivering a gas through the gas nozzle provides for an at least 10% decrease in a belt motor torque.

49. The method of claim 46, wherein delivering a gas through the gas nozzle provides for an at least 100% increase in belt life of the continuous belt.

50. The method of claim 46, further comprising delivering a gas to provide the gas at a pre-determined relative humidity equal to that of a process air, which provides for an at least about 75% decrease in an electrode coating by the particle mixture.

51. The method of claim 38, further comprising conditioning the gas to have a relative humidity about equal to a relative humidity of a process air.

52. The method of claim 38, further comprising conditioning the gas to have a relative humidity of dry air in the separation zone, prior to delivering the gas.

53. The method of claim 38, further comprising at least one of humidifying or dehumidifying the gas prior to delivering the gas.

54. The method of claim 38, further comprising operating at an increased voltage as compared to a system without air nozzles, thereby improving separation of electrically insulating powders.

55. The method of claim 38, further comprising operating at a decreased electrode gap as compared to a system without air nozzles, thereby improving separation of the particle mixture.

56. A method for facilitating an operating life of a belt separation system comprising:

installing a plurality of gas nozzles positioned along a wall of the belt separation system, the system comprising;

a first electrode and a second electrode arranged on opposite sides of a longitudinal centerline and configured to provide an electric field between the first and second electrodes;

a first roller disposed at a first end of the system;

a second roller disposed at a second end of the system; and

a continuous belt disposed between the first and second electrodes and supported by the first roller and the second roller.

57. The method of claim 56, further comprising connecting the plurality of gas nozzles to a source of gas.

58. The method of claim 56, further comprising connecting the plurality of gas nozzles to a source of pressurized gas.

59. The method of claim 56, further comprising connecting the plurality of gas nozzles to a source of pressurized gas conditioned to at least one of a pre-determined relative humidity and a pre-determined temperature.

60. The method of claim 59, further comprising connecting the source of pressurized gas to at least one of dehumidifier, a source of steam, and a source of liquid water.

61. The method of claim 59, further comprising conditioning the gas to have a relative humidity about equal to a relative humidity of a process air.

62. The method of claim 59, further comprising conditioning the gas to have a relative humidity of dry air in the separation zone, prior to delivering the gas.

63. The method of claim 56, further comprising operating at an increased voltage as compared to a system without air nozzles, thereby improving separation of electrically insulating powders.

64. The method of claim 56, further comprising operating at a decreased electrode gap as compared to a system without air nozzles, thereby improving separation of the particle mixture.

65. The method of claim 56, further comprising introducing the particle mixture to a feed port of the belt separator system.

66. The method of claim 65, further comprising operating the continuous belt at a velocity between about 10 feet per second (3.0 meters per second) and about 100 feet per second (30.5 meters per second).

67. The method of claim 66, further comprising delivering the gas through a gas nozzle positioned along a wall of the system to deliver gas to the separation zone.

68. The method of claim 67, wherein delivering the gas through the gas nozzle comprises delivering a pressurized gas.

69. The method of claim 67, wherein delivering the gas through the gas nozzle comprises delivering a gas intermittently, for a pre-determined interval.

70. The method of claim 69, wherein delivering the gas through the gas nozzle comprises delivering a gas intermittently, for a pre-determined interval of about zero seconds to about 30 seconds.

71. The method of claim 70, wherein the pre-determined interval is about 10 seconds.

72. The method of claim 67, wherein delivering the gas through a gas nozzle comprises delivering the gas through a gas nozzle at a pressure of about 10 pounds per square inch gauge (psig) to about 100 psig.

73. The method of claim 68, wherein the plurality of gas nozzles are configured to deliver pressurized gas at a pressure of about 15 psig to about 25 psig.

74. The method of claim 73, wherein the pressure is about 25 psig.

75. The method of claim 72, wherein the pressure is about 60 psig.

76. The method of claim 67, wherein delivering a gas through the gas nozzle provides for an at least 10% decrease in a belt motor torque.

77. The method of claim 67, wherein delivering a gas through the gas nozzle provides for an at least 100% increase in belt life of the continuous belt.

78. The method of claim 67, further comprising delivering a gas to provide the gas at a pre-determined relative humidity equal to that of a process air, which provides for an at least about 75% decrease in an electrode coating by the particle mixture.

79. The method of claim 56, wherein the plurality of gas nozzles are positioned at an angle in a range of about 90 degrees to a direction of travel of the continuous belt to 45 degrees from normal relative to the direction of travel of the belt.