Methods for manufacturing bulked continuous carpet filament

Patent metadata

Field	Value
Publication number	US-10538016-B2
Application number	US-201916432579-A
Country	US
Kind code	B2
Filing date	Jun 5, 2019
Priority date	May 31, 2012
Publication date	Jan 21, 2020
Grant date	Jan 21, 2020

Abstract

A method of manufacturing bulked continuous carpet filament from recycled polymer. In various embodiments, the method includes: (1) reducing recycled polymer material into polymer flakes; (2) cleansing the polymer flakes; (3) melting the flakes into a polymer melt; (4) removing water and contaminants from the polymer melt by dividing the polymer melt into a plurality of polymer streams and exposing those streams to pressures below 5 millibars; (5) recombining the streams; and (6) using the resulting purified polymer to produce bulked continuous carpet filament.

First claim

What is claimed is:

1. A method of manufacturing bulked continuous carpet filament, the method comprising:
melting a plurality of polymer flakes to create a first stream of polymer melt;
routing the first stream of polymer melt through a separation element to generate multiple streams of polymer melt;
exposing the multiple streams of polymer melt to a pressure within a multiple stream section of a melt processing unit to a pressure between about 0 millibars and about 5 millibars;
while maintaining the pressure of the multiple stream section of the melt processing unit between about 0 millibars and about 5 millibars, allowing the multiple streams of polymer melt to pass through the multiple stream section of the melt processing unit into a receiving section of the melt processing unit;
recombining the multiple streams of polymer melt into at least one stream of polymer melt at the receiving section of the melt processing unit; and
providing polymer from the at least one stream of polymer melt to at least one spinning machine configured to form the polymer from the at least one stream of polymer melt into bulked continuous carpet filament.

2. The method of claim 1 , wherein the separation element comprises an extruder having at least eight satellite screws and each of the at least eight satellite screws is respectively dimensioned to produce one of the multiple streams of polymer melt from polymer from the first stream of polymer melt.

3. The method of claim 1 , wherein allowing the multiple streams of polymer melt to pass through the multiple stream section of the melt processing unit into a receiving section of the melt processing unit comprises allowing the multiple streams of polymer melt to fall through the multiple stream section of the melt processing unit under the weight of gravity.

4. The method of claim 3 , wherein exposing the multiple streams of polymer melt to the pressure within the multiple stream section of a melt processing unit comprises exposing a surface area of each of the multiple streams of polymer melt to the pressure within the multiple stream section of the melt processing unit.

5. The method of claim 3 , wherein the pressure within the multiple stream section of the melt processing unit has been selected to produce a desired intrinsic viscosity associated with the at least one stream of polymer melt.

6. The method of claim 5 , further comprising determining an intrinsic viscosity of the at least one stream of polymer melt, and, in response to determining the intrinsic viscosity of the at least one stream of polymer melt, adjusting the pressure within the multiple stream section of the melt processing unit.

7. The method of claim 6 , wherein maintaining the pressure of the multiple stream section of the melt processing unit between about 0 millibars and about 5 millibars comprises maintaining the pressure of the multiple stream section of the melt processing unit between about 0 millibars and about 1.5 millibars.

8. The method of claim 1 , wherein maintaining the pressure of the multiple stream section of the melt processing unit between about 0 millibars and about 5 millibars comprises maintaining the pressure of the multiple stream section of the melt processing unit between about 0 millibars and about 1.5 millibars.

9. The method of claim 1 , wherein the multiple streams of polymer melt comprise at least 100 streams of polymer melt.

10. The method of claim 1 , wherein the separation element comprises a plate defining a plurality of holes that are each respectively dimensioned to produce one of the multiple streams of polymer melt from polymer from the first stream of polymer melt.

11. The method of claim 1 , further comprising:
determining that an intrinsic viscosity of the at least one stream of polymer melt is below a predetermined level; and
in response to determining that the intrinsic viscosity of the at least one stream of polymer melt is below the predetermined level, substantially automatically reducing the pressure of the multiple stream section of the melt processing unit.

12. The method of claim 1 , wherein the plurality of polymer flakes is derived, at least in part, from polyethylene terephthalate (PET) flakes that are derived from recycled PET containers.

13. The method of claim 1 , wherein exposing the multiple streams of polymer melt to the pressure within the multiple stream section of the melt processing unit comprises simultaneously exposing the multiple streams of polymer melt to the pressure within the multiple stream section of the melt processing unit while the multiple streams of polymer melt fall through the multiple stream section of the melt processing unit into the receiving section of the melt processing unit.

14. The method of claim 13 , wherein recombining the multiple streams of polymer melt into the at least one stream of polymer melt at the receiving section of the melt processing unit comprises recombining the multiple streams of polymer melt into the at least one stream of polymer melt using a single screw extruder.

15. A method of manufacturing bulked continuous carpet filament, the method comprising:
melting a plurality of polymer flakes to create a first stream of polymer melt;
routing the first stream of polymer melt through a separation element to generate multiple streams of polymer melt;
exposing the multiple streams of polymer melt to a pressure within a multiple stream section of a melt processing unit to a pressure between about 0.5 millibars and about 1.2 millibars;
while maintaining the pressure of the multiple stream section of the melt processing unit between about 0.5 millibars and about 1.2 millibars, allowing the multiple streams of polymer melt to pass through the multiple stream section of the melt processing unit into a receiving section of the melt processing unit;
recombining the multiple streams of polymer melt into at least one stream of polymer melt at the receiving section of the melt processing unit; and
providing polymer from the at least one stream of polymer melt to at least one spinning machine configured to form the polymer from the at least one stream of polymer melt into bulked continuous carpet filament.

16. The method of claim 15 , wherein the separation element comprises an extruder having at least eight satellite screws and each of the at least eight satellite screws is respectively dimensioned to produce one of the multiple streams of polymer melt from polymer from the first stream of polymer melt.

17. The method of claim 15 , wherein allowing the multiple streams of polymer melt to pass through the multiple stream section of the melt processing unit into a receiving section of the melt processing unit comprises allowing the multiple streams of polymer melt to fall through the multiple stream section of the melt processing unit under the weight of gravity.

18. The method of claim 17 , wherein exposing the multiple streams of polymer melt to the pressure within the multiple stream section of a melt processing unit comprises exposing a surface area of each of the multiple streams of polymer melt to the pressure within the multiple stream section of the melt processing unit.

19. The method of claim 17 , wherein the pressure within the multiple stream section of the melt processing unit has been selected to produce a desired intrinsic viscosity associated with the at least one stream of polymer melt.

20. The method of claim 19 , further comprising determining an intrinsic viscosity of the at least one stream of polym

Assignees

• Aladdin Mfg Corp

Inventors

• Clark Thomas R

Classifications

• B29K2105/0067

  Melt · CPC title

• B29K2105/26

  Scrap {or recycled material} · CPC title

• B29C48/92

  Measuring, controlling or regulating · CPC title

• B29B2017/0289

  Washing the materials in liquids · CPC title

• B29B17/0042

  for shaping parts, e.g. multilayered parts with at least one layer containing regenerated plastic · CPC title