Methods for manufacturing bulked continuous filament from colored recycled pet

Patent metadata

Field	Value
Publication number	US-10487422-B2
Application number	US-201715419955-A
Country	US
Kind code	B2
Filing date	Jan 30, 2017
Priority date	May 31, 2012
Publication date	Nov 26, 2019
Grant date	Nov 26, 2019

Abstract

A method of manufacturing bulked continuous carpet filament which, in various embodiments, comprises: (A) grinding recycled PET bottles into a group of flakes; (B) washing the flakes; (C) identifying and removing impurities, including impure flakes, from the group of flakes; (D) adding one or more color concentrates to the flakes; (E) passing the group of flakes through an MRS extruder while maintaining the pressure within the MRS portion of the MRS extruder below about 25 millibars; (F) passing the resulting polymer melt through at least one filter having a micron rating of less than about 50 microns; and (G) forming the recycled polymer into bulked continuous carpet filament that consists essentially of recycled PET.

First claim

I claim:

1. A method of manufacturing bulked continuous carpet filament, the method comprising:
(A) providing a multi-screw extruder that comprises:
(i) a first satellite screw extruder, the first satellite screw extruder comprising a first satellite screw that is mounted to rotate about a central axis of the first satellite screw;
(ii) a second satellite screw extruder, the second satellite screw extruder comprising a second satellite screw that is mounted to rotate about a central axis of the second satellite screw; and
(iii) a pressure regulation system that is adapted to maintain a pressure within the first and second satellite screw extruders between about 0 millibars and about 5 millibars;

(B) using the pressure regulation system to reduce a pressure within the first and second satellite screw extruders to between about 0 millibars and about 5 millibars;
(C) providing a plurality of polymer flakes, the plurality of polymer flakes comprising between about six percent and about ten percent colored recycled polyethylene terephthalate (PET) flakes and balance substantially clear recycled PET flakes;
(D) providing one or more color concentrates;
(E) adding the one or more color concentrates to the plurality of polymer flakes such that the resulting mixture comprises between about zero percent and about three percent of the one or more color concentrates by weight;
(F) while maintaining the pressure within the first and second satellite screw extruders between about 0 millibars and about 5 millibars, passing the plurality of polymer flakes and the one or more color concentrates through the multi-screw extruder to form a polymer melt so that: (1) a first portion of the polymer melt passes through the first satellite screw extruder, and (2) a second portion of the polymer melt passes through the second satellite screw extruder; and
(G) after the step of passing the polymer melt through the multi-screw extruder, forming the recycled polymer into bulked continuous carpet filament.

2. The method of claim 1 , wherein the colored recycled PET flakes consist essentially of colored PET flakes derived from recycled PET bottles.

3. The method of claim 2 , wherein the colored recycled PET flakes comprise one or more colors selected from a group consisting of:
i. amber PET flake;
ii. blue PET flake; and
iii. green PET flake.

4. The method of claim 1 , further comprising:
providing a color sensor configured to determine a color of the polymer melt; and
substantially automatically adjusting an amount of the one or more color concentrates added to the plurality of polymer flakes based at least in part on the determined color of the polymer melt.

5. The method of claim 4 , wherein the plurality of polymer flakes comprise:
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.

6. The method of claim 5 , wherein the plurality of polymer flakes comprise:
between about seven percent and about nine percent colored recycled PET flakes by weight;
between about five percent and about six percent PTT by weight; and
balance substantially clear recycled PET flakes.

7. The method of claim 1 , wherein the one or more color concentrates at least partially offset a coloration of the bulked continuous carpet filament from the colored recycled PET flakes.

8. A method of manufacturing carpet filament from clear and colored recycled PET bottles comprising the steps of:
(A) providing a plurality of recycled PET bottles;
(B) grinding the plurality of recycled PET bottles into a group of polymer flakes, the group of polymer flakes comprising up to about ten percent colored polymer flakes and balance substantially clear polymer flakes;
(C) washing the group of polymer flakes;
(D) providing a color concentrate;
(E) mixing the color concentrate with the group of polymer flakes to form a concentrate-polymer mixture comprising up to about three percent color concentrate by weight and balance the group of polymer flakes;
(F) melting the concentrate-polymer mixture to produce a polymer melt;
(G) providing an extruder that extrudes material in a plurality of different extrusion streams;
(H) reducing a pressure within the extruder to between about 0 millibars and about 12 millibars;
(I) while maintaining the pressure within the extruder between about 0 millibars and about 12 millibars, passing the polymer melt through the extruder so that the polymer melt is divided into a plurality of extrusion streams, each having a pressure between about 0 millibars and about 12 millibars;
(J) after passing the polymer melt through the extruder, filtering the polymer melt through at least one filter; and
(K) after passing the polymer melt through the filter, forming the polymer melt into bulked continuous carpet filament.

9. The method of claim 8 , the method further comprising:
providing polytrimethylene terephthalate (PTT); and
adding the PTT to the concentrate-polymer mixture, such that the concentrate-polymer mixture comprises:
up to about three percent color concentrate by weight;
up to about six percent PTT by weight; and
balance the group of polymer flakes.

10. The method of claim 9 , wherein adding the PTT to the concentrate-polymer mixture increases the dyeability of the resultant concentrate-polymer mixture.

11. The method of claim 10 , the method further comprising adding the PTT to the concentrate-polymer mixture, such that the concentrate-polymer mixture comprises:
between about two percent and about three percent color concentrate by weight;
between about five percent and about six percent PTT by weight; and
balance the group of polymer flakes.

12. The method of claim 8 , the method further comprising:
providing one or more color sensors configured to determine a color of the polymer melt; and
substantially automatically adjusting an amount of the color concentrate added to the concentrate-polymer mixture based at least in part on the determined color of the polymer melt.

13. The method of claim 12 , wherein the one or more color sensors comprise one or more color sensors selected from a group consisting of:
one or more cameras; and
one or more spectrographs.

14. The method of claim 8 , wherein the color concentrate at least partially masks a coloration of the bulked continuous carpet filament caused by the colored polymer flakes.

15. A method of manufacturing bulked continuous carpet filament, the method comprising:
(A) providing a multi-screw extruder that comprises:
(i) a first satellite screw extruder, the first satellite screw extruder comprising a first satellite screw that is mounted to rotate about a central axis of the first satellite screw;
(ii) a second satellite screw extruder, the second satellite screw extruder comprising a second satellite screw that is mounted to rotate about a central axis of the second satellite screw;
(iii) a third satellite screw extruder, the third satellite screw extruder comprising a third satellite screw that is mounted to rotate about a central axis of the third satellite screw;
(iv) a fourth satellite screw extruder, the fourth satellite screw extruder comprising a fourth satellite screw that is mounted to rotate about a central axis of the fourth satellite screw; and
(v) a pressure regulation system that is adapted to maintain a pressure within the first, second, third, and fourth satellite screw extruders between about 1 millibar and about 18 millibars;

(B) using the pressure regulatio

Assignees

• Aladdin Mfg Corp

Inventors

• Clark Thomas R

Classifications

• 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

• D01F6/92

  of polyesters · CPC title

• B29K2105/26

  Scrap {or recycled material} · CPC title

• B29C2948/92876

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