MANUFACTURE OF SPHERICAL PARTICLES OUT OF A PLASTIC MELT

• US 20080272508A1
• Filed: 10/22/2007
• Published: 11/06/2008
• Est. Priority Date: 12/11/2001
• Status: Abandoned Application

• Current Assignee: Buhler AG (Buhler Holding AG)
• Original Assignee: Buhler AG (Buhler Holding AG)
• Inventors: Christel, Andreas, Krumpholz, Erhard, Geier, Rudolf, Juergens, Theodor, CULBERT, Brent Allen
• Application Number:
  US11/876,325
• Publication Number:
  US 20080272508A1
• Time in Patent Office: Days
• US Class Current: 264/8
• CPC Class Codes: B01J 2/04 in a gaseous medium if combined with suspending the material in a gas, e.g. fluidised beds B01J2/16
• CPC Class Codes: B01J 2/18 using a vibrating apparatus
• CPC Class Codes: B29B 2009/165 Crystallizing granules
• CPC Class Codes: B29B 2009/166 Deforming granules to give a special form, e.g. spheroidizing, rounding
• CPC Class Codes: B29B 9/10 by moulding the material, i.e. treating it in the molten state
• CPC Class Codes: B29B 9/16 Auxiliary treatment of granules
• CPC Class Codes: B29K 2995/0041 Crystalline
• CPC Class Codes: C08G 63/80 Solid-state polycondensation
• CPC Class Codes: C08J 2367/02 Polyesters derived from dicarboxylic acids and dihydroxy compounds; C08J2367/06 takes precedence
• CPC Class Codes: C08J 3/12 Powdering or granulating

Abstract

The invention relates to a method and a device for producing spherical particles from a melted mass of plastic. According to the invention, said melted mass is transformed into droplets by means of a droplet-forming nozzle (10); after falling a certain distance, the droplets are crystallised at least on the surface thereof; the droplets are then supplied to a crystallisation stage in which they are fully crystallised; and are then supplied to an postcondensation stage wherein solid phase polycondensation takes place. In order to ensure surface crystallisation without the risk of adhesion both among the drops and to parts of the device, the drops fall in a crystallisation stage (45) having a cloth element or a sheet metal element comprising openings or a fluidised bed chamber through which gas flows in order to swirl the drops.

Claims

1. A method for manufacturing spherical particles out of plastic, in particular a prepolymer- or polymer melt of a polycondensate, e.g., PET, PBT, PEN, PA or PC, wherein the melt is dripped into droplets by means of an dripping nozzle with numerous melt outlet holes, and the droplets are solidified into particles after falling at least part of a drop distance, characterized in that, at the end of the drop distance, the particles make their way into a receiving area in which at least some of the particles are swirled in such a way as to generate turbulences to move the particles toward the middle of the area and/or area outlet hole.

2. The method according to claim 1, characterized in that the particles in the receiving area are swirled by vibrating at least part of the receiving area.

3. The method according to claim 1 or 2, characterized in that the particles in the receiving area are swirled by blowing a gas through numerous gassing holes.

4. The method according to one of the preceding claims, characterized in that the particles in the receiving area are swirled by means of a cloth-like element interspersed with gas and made to oscillate and/or routed to an area with an intrinsically stiff element at the end of the drop distance that is pressurized with gas in such a way as to produce turbulences for moving the drops toward the middle of the area and/or area outlet opening.

5. The method according to one of the preceding claims, characterized in that the swirled particles form a fluid bed.

6. The method according to claim 5, characterized in that the particles are relayed to the fluid bed via a fluid bed inlet area from the drop distance, and therein moved to a fluid bed outlet area that accommodates the area outlet hole.

7. The method according to claim 6, characterized in that the particles are deflected to the fluid bed inlet area at the end of the drop distance.

8. The method according to one of the preceding claims, characterized in that the particles in the drop distance are exposed to a fluid, in particular a liquid.

9. The method for manufacturing spherical particles out of plastic, in particular a prepolymer- or polymer melt of a polycondensate, e.g., PET, PDT, PEN, PA or PC, in particular according to one of the preceding claims, wherein the melt is dripped into droplets by means of a dripping nozzle with numerous melt outlet holes, and the droplets are solidified into particles after falling at least part of a drop distance, characterized in that the particles in the drop distance are exposed to a liquid.

10. The method according to claim 9, characterized in that the particles at the end of the drop distance get into a receiving area in which at least some of the particles are swirled in such a way as to generate turbulences to move the particles toward the middle of the area and/or area outlet hole.

11. The method according to claim 9 or 10, characterized in that the particles in the receiving area are swirled by vibrating at least part of the receiving area.

12. The method according to one of claims 9 to 11, characterized in that the particles in the receiving area are swirled by blowing in a gas through numerous gassing holes.

13. The method according to one of claims 9 to 12, characterized in that the particles in the receiving area are swirled by means of a cloth-like element interspersed with gas and made to oscillate and/or routed to an area with an intrinsically stiff element at the end of the drop distance that is pressurized with gas in such a way as to produce turbulences for moving the particles toward the middle of the area and/or area outlet opening.

14. The method according to one of claims 9 to 13, characterized in that the swirled particles form a fluid bed.

15. The method according to claim 14, characterized in that the particles are relayed to the fluid bed via a fluid bed inlet area from the drop distance, and therein moved to a fluid bed outlet area that accommodates the outlet hole.

16. The method according to claim 15, characterized in that the particles are deflected to the fluid bed inlet area at the end of the drop distance.

17. The method according to one of the preceding claims, characterized in that the evaporation point of the liquid lies under the melting point of the particles.

18. The method according to at least one of the preceding claims, characterized in that the liquid has water and/or ethylene glycol.

19. The method according to at least one of the preceding claims, characterized in that the liquid is atomized in the form of fine droplets, so that the drops in the drop distance dripped into droplets with the dripping nozzle are pressurized with a spray mist.

20. The method according to claim 19, characterized in that the spray mist is set in such a way that its drop size corresponds to about ⅓

to 1/20 of the drop size of the dripped melt.

21. The method according to one of claims 19 to 20, characterized in that the liquid is supplied in a carrier gas.

22. The method according to claim 21, characterized in that the carrier gas has at least one of the gases air, nitrogen, carbon dioxide, argon, water vapor or ethylene glycol vapor.

23. The method according to one of the preceding claims, characterized in that the drops are at least initially crystallized after falling through at least a portion of the drop distance.

24. The method according to one of the preceding claims, characterized in that the drops are only cooled to a point where their temperature remains over the glass transition temperature T_g of the plastic.

25. The method according to one of the preceding claims, characterized in that the thermal energy of the process gases present in the drop distance, e.g., air, nitrogen, carbon dioxide, argon, water vapor or ethylene glycol vapor, is recovered.

26. The method according to one of the preceding claims, characterized in that the spherical or sphere-like particles are relayed to a crystallization stage after leaving the receiving area.

27. The method according to one of the preceding claims, characterized in that, after going through the one or more crystallization steps, the spherical particles are supplied to the one or more crystallization stages of a post-condensation stage for solid-state polycondensation.

28. The method according to one of the preceding claims, characterized in that the drops are emitted from the dripping nozzle in a cross-shaped outer area of the dripping nozzle.

29. The method according to one of the preceding claims, characterized in that at least some of the drops emitted from the dripping nozzle have a horizontal motion component.

30. The method according to one of the preceding claims, characterized in that the receiving area is pressurized with gas, such as air, in a pulsed fashion.

31. The method according to one of the preceding claims, characterized in that the receiving area is funnel-shaped in design, and has gas-permeated openings on the drip side that run in such a way as to move or swirl the drops tangentially along the inner surface of the funnel-shaped area.

32. The method according to one of the preceding claims, characterized in that the receiving area is pressurized using a gas with a sinusoidal pressure characteristic.

33. The method according to one of the preceding claims, characterized in that the pulsed gas pressurizes the receiving area at a frequency f of preferably 1 Hz≦

f≦

30 Hz, in particular 1 Hz≦

f≦

10 Hz.

34. The method according to one of the preceding claims, characterized in that the gas permeates the receiving area at a maximum velocity v of v≦

4 m/sec, in particular v≦

3 m/sec, preferably v≦

1 m/sec.

35. The method according to one of the preceding claims, characterized in that the gas pressurizes the receiving area with a pressure p of 0 mbar≦

p≦

200 mbar, in particular 0 mbar≦

p≦

150 mbar over atmospheric pressure.

36. The method according to one of the preceding claims, characterized in that the receiving area uses openings with a mesh size of d≦

80%, in particular d≦

30% of the average particle diameter.

37. The method according to one of the preceding claims, characterized in that a portion of the particles crystallized into spheres or at least initially crystallized is removed from the crystallization device and returned to the drops falling through the drop distance above the receiving area.

38. The method according to one of the preceding claims, characterized in that about 10 to 50% of the spheres removed from the crystallization device are returned to the receiving area.

39. The method according to one of the preceding claims, characterized in that a chain lengthener that accelerates postcondensation is added to the melt immediately prior to dripping.

40. The method according to one of the preceding claims, characterized in that the share of chain lengthener in the melt to be dripped measures <

0.5% w/w.

41. The method according to one of the preceding claims, characterized in that the chain lengthener is preferably added to the melt in an amount in which it becomes active after a time t₁ of t₁≦

10 min, in particular 1 min≦

t₁≦

10 min.

42. The method according to one of the preceding claims, characterized in that chain lengtheners include those based on polyol, dianhydride of a tetracarbonic acid, pentaerythrite or oxazolines.

43. Method according to one of the preceding claims, characterized in that the drops are exposed over at least part of the drop distance to a countercurrent, which is preferably laminar.

44. The method according to one of the preceding claims, characterized in that the drops are exposed over at least part of the drop distance to a cocurrent, which is preferably laminar.

45. The method according to one of the preceding claims, characterized in that the countercurrent is withdrawn at a velocity of less than 0.2 m/sec, preferably less than 0.1 m/sec.

46. The method according to one of the preceding claims, characterized in that the cocurrent is withdrawn at a velocity of less than 1 m/sec, preferably less than 0.5 m/sec.

47. The method according to one of the preceding claims, characterized in that the gas permeating the receiving area flows through a first cycle, wherein a portion of the gas is routed to a cleaning station, in which the gas is cleaned and cooled, after which it is returned to the cycle once again.

48. The method according to one of the preceding claims, characterized in that the gas is here preferably guided in the cleaning station countercurrently or cocurrently to a glycol cycle.

49. A device for manufacturing spherical particles out of plastic, in particular a prepolymer- or polymer melt of a polycondensate, e.g., PET, PBT, PEN, PA or PC, with a nozzle array that drips the plastic melt along with a downstream drop distance in a drop tower, characterized in that the drop distance passes over into a receiving area in which at least some of the particles can be swirled in such a way as to generate turbulences to move the particles toward the middle of the area and/or area outlet hole.

51. The device according to one of claims 49 or 50, characterized in that the receiving area is designed as a funnel.

52. The device according to one of claims 49 to 51, characterized in that at least part of the receiving area can be vibrated by vibration means.

53. The device according to one of claims 49 to 52, characterized in that the receiving area can be exposed to a gas via numerous gassing holes.

54. The device according to one of claims 49 to 52, characterized in that the drop distance passes over into a funnel-shaped receiver (45) peripherally bordered by a pulsating, cloth-like element (50) and/or intrinsically stiff element with holes.

55. The device according to one of claims 49 to 54, characterized in that the receiving area has an inlet area and outlet area.

56. The device according to claim 55, characterized in that the end of the drop distance or the lower end of the drop tower has deflection means that can guide the particles to the inlet area.

57. The device according to claim 55, characterized in that the melt outlet holes of the nozzle array (10) can be arranged in an area of the nozzle array (10) that is situated vertically above the inlet area and has essentially the same layout as the inlet area.

58. The device according to claim 55, characterized in that at least some of the melt outlet holes of the nozzle array (10) are angled relative to the vertical.

59. The device according to one of claims 49 or 58, characterized in that the drop tower incorporates atomizing means that can be used to introduce an atomized liquid into the drop distance.

60. The device according to one of claims 49 to 59, characterized in that it has means for recovering thermal energy, which can be used to recover the process heat contained in the process gases present in the drop tower.

61. The device according to one of claims 49 to 60, characterized in that a crystallization stage (62) follows the receiving area.

62. The device according to one of claims 49 to 61, characterized in that the one or more crystallization stages has a downstream post-condensation stage (18) for solid-state polycondensation.

63. The device according to one of claims 49 to 62, characterized in that the receiving area can be exposed to a pulsating gas, such as air.

64. The device according to one of claims 49 to 63, characterized in that the receiving area is a cloth-like element (50) secured to a funnel (46), e.g., a metal or special steel funnel, and can be spaced apart relative to its inner surface (48) in such a way that a line (54, 56) incorporating a shut-off element (66) that releases or blocks said line empties into the gap (52) between the cloth-like element and funnel.

65. The device according to one of claims 49 to 63, characterized in that receiving area is an intrinsically stiff element, which is enveloped at a distance by a funnel element in such a way that a line (54, 56) incorporating a shut-off element (66) that releases or blocks said line empties into the gap (52) between the intrinsically stiff element and the funnel element.

66. The device according to one of claims 49 to 63, characterized in that the receiving area is a fluid-bed chamber.

67. The device according to claim 66, characterized in that the fluid-bed chamber is connected by numerous gassing holes with a gas inlet chamber, into which empties a line incorporating a shut-off element that releases of blocks said line.

68. The device according to one of claims 49 to 67, characterized in that the gas can be relayed to the gap (52) pulsating at a frequency f, wherein the frequency f in particular measures 1 Hz≦

f≦

30 Hz, preferably 1 Hz≦

f≦

10 Hz.

69. The device according to one of claims 49 to 68, characterized in that the holes of the receiving area are designed in such a way that the gas penetrating them flows along the inner surface of the receiving area, in particular in a turbulent manner.

70. The device according to one of claims 49 to 69, characterized in that the holes are designed in such a way that the gas passing through them flows tangentially to the inner surface of the intrinsically stiff element.

71. The device according to one of claims 49 to 70, characterized in that the gas can be supplied to the gap (52) of the arrangement with a sinusoidal pressure progression.

72. The device according to one of claims 49 to 71, characterized in that the receiving area is anti-adhesive, and consists in particular of polytetrafluoroethylene.

73. The device according to one of claims 49 to 72, characterized in that the receiving area preferably has holes with a mesh size d of d≦

0.6 mm, in particular d≦

0.3 mm.

74. The device according to one of claims 49 to 73, characterized in that it has a first cycle (64) through which the gas penetrating the receiving area flows, and from which a branch running along the drop distance exits the drop distance at distance A, wherein a ring element (20) that emits a spray mist, envelops the drop distance and is equipped with spray nozzles is located above distance A.

75. The device according to claim 74, characterized in that the ring element (20) with spray nozzles is preferably situated in a second cycle (30), which itself is routed out of the drop distance below the nozzle array (10) that drips the melt.

76. The device according to one of claims 75 or 75, characterized in that a portion of the gas carried in the first cycle (64) is routed to a cleaning station (74) that encompasses a glycol cycle.

77. The device according to one of claims 49 to 76, characterized in that the crystallization device (62) preferably has an inlet hole, which is simultaneously the outlet hole of the funnel (46).

78. The device according to one of claims 49 to 77, characterized in that the crystallization device (62) is placed in another cycle (84), through which some of the spheres crystallized in the crystallization device above the funnel (46) or intrinsically stiff element can be returned to the drop distance.

79. The device according to one of claims 62 to 78, characterized in that the post-condensation stage (18) preferably has an upstream and/or downstream transfer channel (88, 98), which can be sealed at the inlet and/or outlet by a shut-off element preferably (90, 92, 100, 102) designed as an iris diaphragm.

80. The device according to one of claims 49 to 79, characterized in that the nozzle array (10) designed in particular as a vibratable nozzle plate is connected to a line (14) that supplies the melt, in which another line (16) connected with a container for a plastic chain lengthener empties immediately before the nozzle element or into the nozzle element itself.

50. The device for manufacturing spherical particles out of plastic, in particular a prepolymer- or polymer melt of a polycondensate, e.g., PET, PBT, PEN, PA or PC, with a nozzle array that drips the plastic melt along with a downstream drop distance in a drop tower, characterized in that a device for exposing the particles to a liquid is allocated to the drop tower.