Methods for manufacturing bulked continuous filament

Patent metadata

Field	Value
Publication number	US-10744681-B2
Application number	US-201916684490-A
Country	US
Kind code	B2
Filing date	Nov 14, 2019
Priority date	May 31, 2012
Publication date	Aug 18, 2020
Grant date	Aug 18, 2020

Abstract

A method for manufacturing bulked continuous carpet filament, the method comprising: (1) reducing a chamber pressure within a chamber to below about 5 millibars; (2) after reducing the chamber pressure to below about 5 millibars, providing a polymer melt to the chamber; (3) separating the polymer melt into at least eight streams; (4) while the at least eight streams of the polymer melt are within the chamber, exposing the at least eight streams of the polymer melt to the chamber pressure of below about 5 millibars; (5) after exposing the at least eight streams of the polymer melt to the chamber pressure of below about 5 millibars, recombining the at least eight streams into a single polymer stream; and (6) forming polymer from the single polymer stream into bulked continuous carpet filament.

First claim

What is claimed is:

1. A method for manufacturing bulked continuous carpet filament, the method comprising:
reducing a pressure within a chamber to reach a chamber pressure of below about 5 millibars;
melting a plurality of polymer flakes to create a polymer melt;
transferring the polymer melt to an interior of the chamber;
separating the polymer melt into a plurality of different streams, the plurality of different streams comprising at least four streams of the polymer melt;
exposing each of the at least four streams of the polymer melt to the chamber pressure of below about 5 millibars while the at least four streams of the polymer melt are in the chamber;
after exposing the at least four streams of the polymer melt to the chamber pressure of below about 5 millibars, recombining the at least four streams into a single polymer stream; and
forming polymer from the single polymer stream into bulked continuous carpet filament.

2. The method of claim 1 , wherein the step of recombining the at least four streams into a single polymer stream comprises recombining the at least four streams into a single polymer stream via a single screw extruder.

3. The method of claim 2 , wherein the single screw extruder is used to transport the polymer within the single polymer stream away from the chamber.

4. The method of claim 1 , wherein the at least four streams of the polymer melt comprise more than eight streams of polymer melt.

5. The method of claim 1 , wherein exposing the at least four streams of the polymer melt to the chamber pressure while the at least four streams of the polymer melt are in the chamber comprises exposing the at least four streams of the polymer melt to a chamber pressure that is below about 1.5 millibars.

6. A method of manufacturing bulked continuous carpet filament, the method comprising:
separating a polymer melt into at least eight streams such that each of the at least eight stream is at least partially exposed to a chamber pressure within a chamber of less than about 5 millibars;
after the at least eight streams are exposed to the chamber pressure of less than about 5 millibars, recombining the at least eight streams into a single polymer stream; and
forming polymer from the single polymer stream into bulked continuous carpet filament.

7. The method of claim 6 , wherein the chamber pressure is below about 1.5 millibars.

8. The method of claim 6 , wherein the chamber pressure is below about 1 millibar.

9. The method of claim 6 , wherein the chamber pressure is between about 0.5 millibars and about 5 millibars.

10. The method of claim 6 , wherein the chamber pressure is between about 0.5 millibars and about 1.2 millibars.

11. The method of claim 6 , further comprising:
determining an intrinsic viscosity associated with the single polymer stream; and
in response to determining the intrinsic viscosity associated with the single polymer stream, substantially automatically adjusting the chamber pressure.

12. The method of claim 11 , further comprising:
determining the intrinsic viscosity of the single polymer stream; and
in response to determining that the intrinsic viscosity of the single polymer stream is below a predetermined level, lowering the chamber pressure in the chamber.

13. The method of claim 12 , wherein the predetermined level is about 0.8 g/dL.

14. The method of claim 6 , wherein forming the polymer from the single polymer stream into bulked continuous carpet filament comprises forming the polymer from the single polymer stream into bulked continuous carpet filament that comprises between about 80% and about 100% recycled PET.

15. A method for manufacturing bulked continuous carpet filament, the method comprising:
providing a pressure regulation system;
using the pressure regulation system to reduce a chamber pressure within a chamber to below about 5 millibars;
after using the pressure regulation system to reduce the chamber pressure to below about 5 millibars, providing a polymer melt to the chamber;
increasing a surface area of the polymer melt exposed to an interior of the chamber utilizing at least eight different streams of the polymer melt;
while the at least eight streams of the polymer melt are within the chamber, exposing the at least eight streams of the polymer melt to the chamber pressure of below about 5 millibars;
after exposing the at least eight streams of the polymer melt to the chamber pressure of below about 5 millibars, recombining the at least eight streams into a single polymer stream; and
forming polymer from the single polymer stream into bulked continuous carpet filament.

16. The method of claim 15 , wherein exposing the at least eight streams of the polymer melt to the chamber pressure while the at least eight streams of the polymer melt are within the chamber comprises exposing the at least eight streams of the polymer melt to a chamber pressure that is below about 1.8 millibars.

17. The method of claim 15 , wherein exposing the at least eight streams of the polymer melt to the chamber pressure while the at least eight streams of the polymer melt are within the chamber comprises exposing the at least eight streams of the polymer melt to a chamber pressure that is between about 0.5 millibars and about 5 millibars.

18. The method of claim 15 , wherein exposing the at least eight streams of the polymer melt to the chamber pressure of below about 5 millibars within the chamber removes at least a portion of interstitial water from the polymer melt.

19. The method of claim 18 , wherein the at least a portion of the interstitial water comprises substantially all of the interstitial water from the polymer melt.

20. The method of claim 15 , wherein exposing the at least eight streams of the polymer melt to the chamber pressure of below about 5 millibars within the chamber removes volatile organics present in the polymer melt.

Assignees

• Aladdin Mfg Corp

Inventors

• Clark Thomas R

Classifications

• B29C2948/9239

  Screw or gear · CPC title

• B29C2948/9238

  Feeding, melting, plasticising or pumping zones, e.g. the melt itself · CPC title

• B29C2791/006

  Using vacuum · CPC title

• B29C2791/003

  Making articles of indefinite length (B29C53/48 takes precedence) · CPC title

• B29C37/006

  Degassing moulding material or draining off gas during moulding (venting means in moulds B29C33/10) · CPC title