Methods for manufacturing bulked continuous filament from recycled PET

Patent metadata

Field	Value
Publication number	US-11911930-B2
Application number	US-202117342047-A
Country	US
Kind code	B2
Filing date	Jun 8, 2021
Priority date	May 31, 2012
Publication date	Feb 27, 2024
Grant date	Feb 27, 2024

Abstract

A method of manufacturing bulked continuous carpet filament that includes providing a polymer melt and separating the polymer melt from the extruder into at least eight streams. The multiple streams are exposed to a chamber pressure within a chamber that is below approximately 25 millibars, or another predetermined pressure. The streams are recombined into a single polymer stream. Polymer from the polymer stream is then formed into bulked continuous carpet filament.

First claim

What is claimed is:

1. A method of manufacturing a PET comprising product, the method comprising:
providing a PET crystallizer;
passing a plurality of flakes of recycled PET through the PET crystallizer to at least partially dry at least a portion of a surface of the plurality of flakes;
after passing the plurality of flakes through the PET crystallizer, at least partially melting the plurality of flakes into a polymer melt;
increasing a surface area of the polymer melt by dividing the polymer melt into at least eight streams;
passing the at least eight streams of polymer melt into an interior of a chamber such that a respective surface area of each of the at least eight streams is exposed to a chamber pressure below atmospheric pressure;
recombining the at least eight streams into a single polymer stream; and
forming the single polymer stream into said PET comprising product.

2. The method of claim 1 , wherein said chamber pressure corresponds to a desired moisture level or a desired intrinsic viscosity associated with a single polymer stream comprising the at least eight streams of the polymer melt.

3. The method of claim 1 , wherein the method comprises maintaining the chamber pressure below atmospheric pressure while the at least eight streams of polymer melt pass from an inlet of the chamber to an outlet of the chamber.

4. The method of claim 1 , wherein the chamber pressure is a pressure between about 0.5 millibars and about 12 millibars.

5. The method of claim 1 , wherein the chamber pressure corresponds to the desired moisture level associated with the single polymer stream.

6. The method of claim 1 , wherein the chamber pressure corresponds to the desired intrinsic viscosity associated with the single polymer stream.

7. The method of claim 1 , wherein dividing the polymer melt into at least eight streams comprises separating the polymer melt into at least eight streams within the chamber.

8. The method of claim 1 , wherein the PET crystallizer comprises:
a hopper screw configured to feed the plurality of flakes into the PET crystallizer; and
a blower configured to blow hot air over the plurality of flakes as the plurality of flakes pass through the crystallizer.

9. The method of claim 8 , wherein the crystallizer is configured to maintain a temperature of between about 140 degrees Celsius and about 180 Celsius within the crystallizer.

10. The method of claim 1 , wherein the crystallizer is configured to at least partially crystallize the plurality of flakes.

11. The method of claim 1 , wherein the crystallizer is configured to reduce a moisture content of the plurality of flakes to between about 30 ppm and about 50 ppm.

12. The method of claim 1 , further comprising:
adding one or more color concentrates to the plurality of polymer flakes or to the single polymer stream.

13. The method of claim 12 , further comprising:
providing a color sensor configured to determine a color of the single polymer stream; and
substantially automatically adjusting an amount of the one or more color concentrates added to the plurality of polymer flakes or the single polymer stream based at least in part on the determined color of the single polymer stream.

14. The method of claim 1 , further comprising:
determining the intrinsic viscosity of the single polymer stream; and
in response to determining the intrinsic viscosity, adjusting the chamber pressure until the single polymer stream comprises the desired intrinsic viscosity.

15. The method of claim 1 , wherein said PET comprising product is a bulked continuous filament; said method further comprising directing the single polymer stream formed from the at least eight streams directly into a spinning machine to form the single polymer stream into said bulked continuous carpet filament.

16. The method of claim 1 , wherein said PET comprising product are PET comprising pellets; said method further comprising cooling said polymer melt into pellets.

17. The method of claim 1 , wherein said polymer melt is provided by extruding PET flakes derived from PET bottles.

18. A method for manufacturing a carpet, the method comprising:
obtaining PET flakes substantially from a mix of both non-clear and clear PET bottles;
providing a PET crystallizer;
passing the PET flakes through the PET crystallizer to at least partially dry at least a portion of a surface of the PET flakes;
after passing the PET flakes through the PET crystallizer, at least partially melting the PET flakes into a polymer melt;
increasing a surface area of the polymer melt by extruding the polymer melt into at least eight streams;
passing the at least eight streams of polymer melt into an interior of a chamber such that a respective surface area of each of the at least eight streams is exposed to a chamber pressure below atmospheric pressure;
recombining the at least eight streams into a single polymer stream;
producing carpet yarn at least by forming the single polymer stream into continuous bulked carpet filament;
dyeing the continuous bulked carpet filament; and
using the carpet yarn for producing said carpet.

19. The method of claim 18 , wherein said carpet yarn has a tenacity of at least 3 gf/den.

20. The method of claim 18 , wherein said non-clear bottles form less than 2% of said mix.

21. The method of claim 18 , wherein said non-clear bottles form between about 6.5% to 9.5% of said mix.

22. The method of claim 18 , wherein said non-clear bottles form more than about 80% of said mix.

23. The method of claim 18 , wherein said continuous bulked carpet filament is dyed by dying said carpet.

24. The method of claim 18 , wherein said carpet yarn is produced by a one threadline spinning machine.

Assignees

• Aladdin Mfg Corp

Inventors

• Clark Thomas R

Classifications

• B01F35/189

  Venting, degassing or ventilating of gases, fumes or toxic vapours during mixing · CPC title

• B01J3/006

  Processes utilising sub-atmospheric pressure; Apparatus therefor · CPC title

• B01F35/2213

  Pressure · CPC title

• B29C48/767

  through a degassing opening of a barrel · CPC title

• B01J2208/00539

  Pressure · CPC title