Methods for manufacturing bulked continuous filament from recycled PET

Patent metadata

Field	Value
Publication number	US-10532495-B2
Application number	US-201816220733-A
Country	US
Kind code	B2
Filing date	Dec 14, 2018
Priority date	May 31, 2012
Publication date	Jan 14, 2020
Grant date	Jan 14, 2020

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 5 millibars. The streams are recombined into a single polymer stream and formed into bulked continuous carpet filament.

First claim

I claim:

1. A method of manufacturing bulked continuous carpet filament, the method comprising:
providing a polymer melt from an extruder to a chamber;
separating the polymer melt from the extruder into at least eight streams within the chamber, each stream at least partially exposed to the chamber encompassing the at least eight streams such that a surface area of each of the at least eight streams is exposed to a chamber pressure within the chamber;
reducing a pressure within the chamber to reach the chamber pressure below about 5 millibars corresponding to a desired moisture level or intrinsic viscosity associated with a single polymer stream comprising the at least eight streams of the polymer melt;
recombining the at least eight streams into the single polymer stream; and
forming the single polymer stream into bulked continuous carpet filament.

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

3. The method of claim 2 , further comprising:
providing a plurality of polymer flakes to the extruder; and
adding one or more color concentrates to the plurality of polymer flakes or to the polymer stream.

4. The method of claim 3 , 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.

5. The method of claim 3 , wherein the plurality of polymer flakes comprises between about six percent and about ten percent colored recycled polyethylene terephthalate (PET) flakes and balance substantially clear recycled PET flakes.

6. The method of claim 5 , wherein a resulting mixture of the one or more color concentrates and the plurality of polymer flakes or the polymer stream comprises between about zero percent and about three percent of the one or more color concentrates by weight.

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

8. The method of claim 1 , further comprising directing the single polymer stream from the at least eight streams directly into a spinning machine to form the single polymer stream into bulked continuous carpet filament.

9. A method for manufacturing bulked continuous carpet filament, the method comprising:
providing an extruder;
providing a plurality of polymer flakes to the extruder;
melting the plurality of polymer flakes within the extruder to create a polymer melt;
providing the polymer melt to a chamber;
increasing a surface area of the polymer melt exposed to the chamber utilizing at least eight streams of the polymer melt;
reducing a pressure within the chamber to reach a chamber pressure of below about 5 millibars;
recombining the at least eight streams into a single polymer stream; and
forming the single polymer stream into bulked continuous carpet filament.

10. The method of claim 9 , wherein reducing the pressure within the chamber to reach the chamber pressure of below about 5 millibars comprises reducing the pressure within the chamber to reach the chamber pressure of between about 0 millibars and about 1.5 millibars.

11. The method of claim 9 , further comprising adding one or more color concentrates to the plurality of polymer flakes or to the polymer stream.

12. The method of claim 11 , wherein the plurality of polymer flakes comprises between about six percent and about ten percent colored PET flakes and balance substantially clear recycled PET flakes.

13. The method of claim 12 , wherein a resulting mixture of the one or more color concentrates and the plurality of polymer flakes or the polymer stream comprises between about zero percent and about three percent of the one or more color concentrates by weight.

14. The method of claim 12 , wherein the colored recycled PET flakes consist essentially of colored PET flakes derived from recycled PET bottles.

15. The method of claim 11 , wherein the plurality of polymer flakes comprises:
between about six percent and about ten percent colored recycled PET flakes by weight;
up to about six percent polytrimethylene terephthalate (PTT) by weight; and
balance substantially clear recycled PET flakes.

16. The method of claim 9 , further comprising:
determining the intrinsic viscosity of the single polymer stream; and
in response to determining the viscosity, adjusting the chamber pressure until the single polymer stream comprises a desired intrinsic viscosity.

Assignees

• Aladdin Mfg Corp

Inventors

• Clark Thomas R

Classifications

• B29C48/44

  Planetary screws · CPC title

• B29C48/43

  Ring extruders · CPC title

• B29C48/40

  using two or more parallel screws {or at least two parallel non-intermeshing screws}, e.g. twin screw extruders · CPC title

• B29C48/277

  of materials · CPC title

• B29C48/385

  using two or more serially arranged screws in separate barrels · CPC title