Crystallizing conveyor

• US 7,790,840 B2
• Filed: 05/24/2006
• Issued: 09/07/2010
• Est. Priority Date: 05/24/2006
• Status: Active Grant

• Current Assignee: Alpek Polyester SA de CV
• Original Assignee: Eastman Chemical Company
• Inventors: Bonner, Richard Gill, DeBruin, Bruce Roger
• Primary Examiner(s): Hess; Douglas A
• Application Number:
  US11/440,142
• Publication Number:
  US 20070274789A1
• Time in Patent Office: 1,567 Days
• Field of Search: 406/197, 264/69, 264/142, 425/68, 425/311, 425/445, 528/480
• US Class Current: 528/480
• CPC Class Codes: B01D 9/0027 by means of conveying fluid, e.g. spray-crystallisation spray-drying F26B
• CPC Class Codes: B01D 9/0059 General arrangements of crystallisation plant, e.g. flow sheets
• CPC Class Codes: B01J 2219/00006 Large-scale industrial plants
• CPC Class Codes: B29B 2009/165 Crystallizing granules
• CPC Class Codes: B29B 9/06 in the form of filamentary material, e.g. combined with extrusion
• CPC Class Codes: B29B 9/065 under-water, e.g. underwater pelletizers
• CPC Class Codes: B29B 9/16 Auxiliary treatment of granules
• CPC Class Codes: C08F 6/28 Purification
• CPC Class Codes: C08G 63/88 Post-polymerisation treatment

Abstract

A method of crystallizing a plurality of polymeric pellets includes a step of introducing the pellets into a pneumatic conveying system with an initial average temperature. The plurality of polymeric pellets are pneumatically transferred from the inlet to an outlet with a conveying gas. While residing within the conveying system, the pellets have a sufficient temperature for crystallization to occur. A pneumatic conveying system implementing the methods of the invention is also provided.

Claims

1. A method of crystallizing a plurality of polymeric pellets, the method comprising:

a) introducing the plurality of polymeric pellets into a pneumatic conveying system at an inlet, the plurality of polymeric pellets comprising a crystallizable polymer having a crystallization temperature and a melting temperature; and

b) pneumatically transferring the plurality of polymeric pellets from the inlet to an outlet with a conveying gas, the conveying gas having a temperature sufficient to maintain the plurality of polymeric pellets within a temperature range such that the plurality of polymeric pellets obtain a degree of crystallinity greater than about 30% prior to removal of the plurality of polymeric pellets from the outlet of the pneumatic conveying system.

2. The method of claim 1 wherein a portion of the plurality of polymeric pellets have a spherical shape or a cylindrical shape.

3. The method of claim 1 wherein a portion of the plurality of polymeric pellets have a rectangular cross section.

4. The method of claim 1 wherein the plurality of polymeric pellets comprise a component selected from the group consisting of polyester, polyolefins, polystyrenes, nylons, and polyketones.

5. The method of claim 1 wherein the plurality of polymeric pellets comprise a polyester.

6. The method of claim 5 wherein the polyester is a polyethylene terephthalate polymer or copolymer.

7. The method of claim 1 wherein the plurality of polymeric pellets have a degree of crystallinity of at least 40% after removal from the outlet of the pneumatic conveying system.

8. The method of claim 1 wherein the degree of crystallinity of the plurality of polymeric pellets introduced into the pneumatic conveying system is increased by at least 10%.

9. The method of claim 1 wherein the degree of crystallinity of the plurality of polymeric pellets introduced into the pneumatic conveying system is increased by at least 20%.

10. The method of claim 1 wherein the degree of crystallinity of the plurality of polymeric pellets introduced into the pneumatic conveying system is less than 30%.

11. The method of claim 1 wherein the degree of crystallinity of the plurality of polymeric pellets introduced into the pneumatic conveying system is less than 20%.

12. The method of claim 1 wherein the crystallizable polymer comprises PET and the temperature range is from about 135°

C. to about 200°

C.

13. The method of claim 1 wherein the crystallizable polymer comprises a polyalkylene terephthalate or polyalkylene naphthalate polymer or copolymer and the temperature range is from about 135°

C. to about 190°

C.

14. The method of claim 1 wherein the residence time of the plurality of polymeric pellets within the pneumatic conveying system is from 30 seconds to 20 minutes.

15. The method of claim 1 wherein the pneumatic conveying system is a dense phase conveying system.

16. The method of claim 1 wherein the pneumatic conveying system is a dilute phase conveying system.

17. The method of claim 1 wherein the plurality of polymeric pellets comprise regions having a temperature greater than or equal to the crystallization temperature of the polymer.

18. The method of claim 1 wherein the conveying gas is selected from the group consisting of air, nitrogen, carbon dioxide, and argon.

19. The method of claim 1 wherein the conveying gas is introduced into the pneumatic conveying system at a temperature ranging from 0 to 220°

C.

20. The method of claim 1 wherein the conveying gas temperature as introduced into the pneumatic conveying system is less than the temperature of the plurality of polymeric pellets introduced into the inlet.

21. The method of claim 1 wherein the plurality of polymeric pellets are introduced into the inlet of the pneumatic conveying system by a differential pressure separation device.

22. The method of claim 1 further comprising continuously separating a liquid from the plurality of polymeric pellets, and continuously introducing the plurality of polymeric pellets into the inlet of the pneumatic conveying system.

23. The method of claim 22 wherein the plurality of polymeric pellets, when introduced into the inlet of the pneumatic conveying system, have a moisture content less than 1 wt %.

24. The method of claim 22 wherein the plurality of polymeric pellets, when introduced into the inlet of the pneumatic conveying system, have a moisture content less than 0.2 wt %.

25. The method of claim 1 further comprising, in a continuous process, melt phase polymerizing virgin polyester molten polymer, solidifying the molten polymer to form the plurality of polymeric pellets in contact with water, and separating at least a portion of the water from the plurality of polymeric pellets before introducing the plurality of polymeric pellets into the pneumatic conveying system.

26. The method of claim 25 wherein the plurality of polymeric pellets formed from the solidification process have an It.V. of at least 0.70 dL/g and up to 1.2 dL/g.

27. The method of claim 26 wherein the It.V. is at least 0.72 dL/g.

28. The method of claim 26 wherein the It.V. is at least 0.76 dL/g.

29. The method of claim 25 wherein the plurality of polymeric pellets exiting the outlet of the pneumatic conveying system are continuously fed to a vessel in which the residual acetaldehyde level of the plurality of polymeric pellets is reduced.

30. The method of claim 29 wherein the reduction of the residual acetaldehyde level within the vessel is at least 4 ppm.

31. The method of claim 29 wherein the residual acetaldehyde level of the plurality of polymeric pellets upon exiting the vessel is less than 2 ppm.

32. The method of claim 1 wherein the pneumatic conveying system comprises an upwardly inclined section having an angle such that the plurality of polymeric pellets travel upwardly when transported through the upwardly inclined section.

33. The method of claim 32 wherein the angle is sufficient to cause a portion of the plurality of polymeric pellets entering the upwardly inclined section to fall downwardly thereby mixing the plurality of polymeric pellets.

34. The method of claim 33 wherein the angle is from about 25°

to 65°

.

35. The method of claim 1 wherein the plurality of polymeric pellets are introduced into the pneumatic conveying system in an amount of 5,000 lb/hr to 200,000 lb/hr.

36. The method of claim 1 wherein the temperature of the conveying gas is sufficient to reduce the residual acetaldehyde from the plurality of polymeric pellets by at least 4 ppm.

37. The method of claim 36 wherein the concentration of acetaldehyde in the conveying gas is less than the equilibrium concentration of the residual acetaldehyde in the plurality of polymeric pellets at the temperatures and pressures present in the pneumatic conveying system.

38. The method of claim 1 wherein the temperature of the conveying gas is sufficient to reduce the residual acetaldehyde from the plurality of polymeric pellets by at least 2 ppm.

39. The method of claim 1 wherein the temperature of the conveying gas is sufficient to reduce the residual acetaldehyde from the plurality of polymeric pellets by at least 1 ppm.

40. The method of claim 1 further comprising contacting the plurality of polymeric pellets in the pneumatic conveying system with a fluid at a temperature sufficient to cool the plurality of polymeric pellets.

41. The method of claim 40 wherein the fluid is liquid that boils upon contact with the plurality of polymeric pellets.

42. The method of claim 41 wherein the liquid comprises water.

43. The method of claim 1 wherein a portion of the plurality of polymeric pellets are three-dimensional objects characterized by a largest size dimension, the largest size dimension being less than about 0.25 inches.

44. The method of claim 1 wherein the length of the pneumatic conveying system is at least 50 feet.

45. The method of claim 1 further comprising packaging the plurality of polymeric pellets into a shipping container, wherein the plurality of polymeric pellets are not polymerized in the solid state.

46. The method of claim 1, wherein the plurality of polymeric pellets are obtained by cutting molten polyester polymer.

47. The method of claim 1, wherein the plurality of polymeric pellets are obtained by cutting molten polyester polymer with a die face cutter.

48. A method of crystallizing a plurality of PET pellets, the method comprising:

a) introducing the plurality of PET pellets into a pneumatic conveying system at an inlet, the plurality of PET pellets being crystallizable and having a crystallization temperature and a melting temperature; and

b) pneumatically transferring the plurality of PET pellets from the inlet to an outlet with a conveying gas, the conveying gas having a temperature sufficient to maintain the plurality of PET pellets within a temperature range such that the plurality of PET pellets obtain a degree of crystallinity greater than about 30% prior to removal of the plurality of PET pellets from the outlet of the pneumatic conveying system.