SYSTEMS AND METHODS FOR MANUFACTURING BULKED CONTINUOUS FILAMENT FROM COLORED RECYCLED PET

• US 20190360122A1
• Filed: 08/12/2019
• Published: 11/28/2019
• Est. Priority Date: 05/31/2012
• Status: Active Grant

• Current Assignee: Aladdin Manufacturing Corporation (Mohawk Industries Incorporated)
• Original Assignee: Aladdin Manufacturing Corp. (China) (Mohawk Industries Incorporated)
• Inventors: Clark, Thomas R.
• Granted Patent: US 11,007,673 B2
• Time in Patent Office: Days
• CPC Class Codes: B29B 13/022 Melting the material to be shaped
• CPC Class Codes: B29B 13/06 by drying B29B13/08 takes precedence ; drying moulded articles or half products B29C37/0092
• CPC Class Codes: B29B 13/10 by grinding, e.g. by triturating; by sieving; by filtering
• CPC Class Codes: B29B 17/00 Recovery of plastics or other constituents of waste material containing plastics; volume reduction of waste plastics, e.g. by mechanical compacting or melting disposal of solid waste B09B; chemical recovery C08J11/00
• CPC Class Codes: B29B 17/0042 for shaping parts, e.g. multilayered parts with at least one layer containing regenerated plastic
• CPC Class Codes: B29B 17/02 Separating plastics from other materials
• CPC Class Codes: B29B 17/0412 to large particles, e.g. beads, granules, flakes, slices
• CPC Class Codes: B29B 2013/002 Extracting undesirable residual components, e.g. solvents, unreacted monomers, from material to be moulded
• CPC Class Codes: B29B 2013/005 Degassing undesirable residual components, e.g. gases, unreacted monomers, from material to be moulded
• CPC Class Codes: B29B 2017/0015 Washing, rinsing
• CPC Class Codes: B29B 2017/0224 Screens, sieves
• CPC Class Codes: B29B 2017/0289 Washing the materials in liquids
• CPC Class Codes: B29B 2017/042 Mixing disintegrated particles or powders with other materials, e.g. with virgin materials
• CPC Class Codes: B29B 2017/0484 Grinding tools, roller mills or disc mills
• CPC Class Codes: B29B 7/426 with consecutive casings or screws, e.g. for charging, discharging, mixing
• CPC Class Codes: B29B 7/485 with three or more shafts provided with screws
• CPC Class Codes: B29B 7/487 with consecutive casings or screws, e.g. for feeding, discharging, mixing
• CPC Class Codes: B29B 7/7461 Combinations of dissimilar mixers
• CPC Class Codes: B29B 7/748 Plants B29B7/7433, B29B7/7485, B29B7/7495 take precedence
• CPC Class Codes: B29B 7/7485 with consecutive mixers, e.g. with premixing some of the components
• CPC Class Codes: B29B 7/86 : for working at sub- or superatmospheric pressure B01F33/70 takes precedence
• CPC Class Codes: B29C 2948/922 : Viscosity; Melt flow index [MFI]; Molecular weight
• CPC Class Codes: B29C 2948/92257 : Colour
• CPC Class Codes: B29C 2948/92514 : Pressure
• CPC Class Codes: B29C 2948/92876 : Feeding, melting, plasticising or pumping zones, e.g. the melt itself
• CPC Class Codes: B29C 48/05 : Filamentary, e.g. strands
• CPC Class Codes: B29C 48/144 : at the plasticising zone
• CPC Class Codes: B29C 48/17 : the components having different colours
• CPC Class Codes: B29C 48/268 : Throttling of the flow, e.g. for cooperating with plasticising elements or for degassing flow control means B29C48/255
• CPC Class Codes: B29C 48/277 : of materials
• CPC Class Codes: B29C 48/286 : Raw material dosing
• CPC Class Codes: B29C 48/287 : Raw material pre-treatment while feeding B29C48/78 takes precedence
• CPC Class Codes: B29C 48/29 : in liquid form
• CPC Class Codes: B29C 48/38 : using two or more serially arranged screws in the same barrel
• CPC Class Codes: B29C 48/385 : using two or more serially arranged screws in separate barrels
• CPC Class Codes: B29C 48/40 : using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
• CPC Class Codes: B29C 48/43 : Ring extruders
• CPC Class Codes: B29C 48/435 : Sub-screws
• CPC Class Codes: B29C 48/44 : Planetary screws
• CPC Class Codes: B29C 48/766 : in screw extruders
• CPC Class Codes: B29C 48/92 : Measuring, controlling or regulating
• CPC Class Codes: B29K 2067/003 : PET, i.e. poylethylene terephthalate
• CPC Class Codes: B29K 2105/0067 : Melt
• CPC Class Codes: B29K 2105/26 : Scrap or recycled material
• CPC Class Codes: B29L 2031/7158 : Bottles
• CPC Class Codes: C08J 11/04 : of polymers
• CPC Class Codes: C08J 11/06 : without chemical reactions
• CPC Class Codes: C08J 2367/02 : Polyesters derived from dicarboxylic acids and dihydroxy compounds; C08J2367/06 takes precedence
• CPC Class Codes: D01D 1/04 : Melting filament-forming substances
• CPC Class Codes: D01D 1/065 : Addition and mixing of substances to the spinning solution or to the melt; Homogenising
• CPC Class Codes: D01D 1/103 : De-aerating
• CPC Class Codes: D01D 1/106 : Filtering
• CPC Class Codes: D01D 5/08 : Melt spinning methods D01D5/0023 takes precedence
• CPC Class Codes: D01F 1/06 : Dyes
• CPC Class Codes: D01F 6/62 : from polyesters
• CPC Class Codes: D01F 6/92 : of polyesters
• CPC Class Codes: D10B 2331/04 : polyesters, e.g. polyethylene terephthalate [PET]
• CPC Class Codes: D10B 2503/04 : Floor or wall coverings; Carpets
• CPC Class Codes: Y02P 20/143 : the feedstock being recycled material, e.g. plastics
• CPC Class Codes: Y02P 70/10 : Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
• CPC Class Codes: Y02W 30/62 : Plastics recycling; Rubber recycling

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 extrusion system while maintaining the pressure within the extrusion system 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.

Claims

1. A method of manufacturing bulked continuous carpet filament, the method comprising:

(A) providing an extrusion system that comprises;

(i) a first extruder;

(ii) a second extruder; and

(iii) a pressure regulation system that is adapted to maintain a pressure within the first and second extruders between about 0 millibars and about 5 millibars;

(B) using the pressure regulation system to reduce a pressure within the first and second 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 additives;

(E) adding the one or more color additives 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 additives by weight;

(F) while maintaining the pressure within the first and second extruders between about 0 millibars and about 5 millibars, passing the plurality of polymer flakes and the one or more color additives through the extrusion system to form a polymer melt so that;

(1) a first portion of the polymer melt passes through the first extruder, and (2) a second portion of the polymer melt passes through the second extruder; and

(G) after the step of passing the polymer melt through the extrusion system, 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 types of PET flake 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 additives 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 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.

6. The method of claim 5, wherein the plurality of polymer flakes comprises:

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 additives at least partially offset a coloration of the bulked continuous carpet filament from the colored recycled PET flakes.

8. The method of claim 1, wherein the one or more color additives comprise a solution dye concentrate.

9. The method of claim 1, wherein the extrusion system is one of a twin screw extruder, a multiple screw extruder, or a planetary extruder.

10. 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 additive;

(E) mixing the color additive with the group of polymer flakes to form a color additive-polymer mixture comprising up to about three percent color additive by weight;

(F) melting the color additive-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.

11. The method of claim 10, the method further comprising:

providing polytrimethylene terephthalate (PTT); and

adding the PTT to the color additive-polymer mixture, such that the color additive-polymer mixture comprises;

up to about three percent color additive by weight;

up to about six percent PTT by weight; and

balance the group of polymer flakes.

12. The method of claim 11, wherein adding the PTT to the color additive-polymer mixture increases the dyeability of the resultant color additive-polymer mixture.

13. The method of claim 12, the method further comprising adding the PTT to the color additive-polymer mixture, such that the color additive-polymer mixture comprises:

between about two percent and about three percent color additive by weight;

between about five percent and about six percent PTT by weight; and

balance the group of polymer flakes.

14. The method of claim 10, 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 additive added to the color additive-polymer mixture based at least in part on the determined color of the polymer melt.

15. The method of claim 14, 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.

16. The method of claim 10, wherein the color additive at least partially masks a coloration of the bulked continuous carpet filament caused by the colored polymer flakes.

17. A method of manufacturing bulked continuous carpet filament, the method comprising:

(A) providing an extrusion system that comprises;

(i) a first extruder;

(ii) a second extruder;

(iii) a third extruder;

(iv) a fourth extruder; and

(v) a pressure regulation system that is adapted to maintain a pressure within the first, second, third, and fourth extruders between about 1 millibar and about 18 millibars;

(B) using the pressure regulation system to reduce a pressure within the first, second, third, and fourth extruders to between about 0 millibars and about 18 millibars;

(C) while maintaining the pressure within the first, second, third, and fourth extruders between about 1 millibar and about 18 millibars, passing a polymer melt through the extrusion system so that;

(1) a first portion of the melt passes through the first extruder, (2) a second portion of the melt passes through the second extruder, (3) a third portion of the melt passes through the third extruder, and (4) a fourth portion of the melt passes through the fourth extruder, wherein;

the polymer melt comprises;

between about seven percent and about nine percent colored recycled PET by weight;

between about two percent and about three percent color additive by weight; and

balance recycled substantially clear PET; and

(D) after the step of passing the polymer melt through the extrusion system, forming the polymer melt into bulked continuous carpet filament.

18. The method of claim 17, further comprising:

providing one or more color sensors configured for determining a color of the polymer melt;

using the one or more color sensors to determine the color of the polymer melt;

determining whether the color is a desired color;

at least partially in response to determining that the color is not a desired color, taking an action selected from a group consisting of;

increasing an amount of color additive in said polymer melt; and

decreasing an amount of color additive in said polymer melt.

19. The method of claim 17, wherein the polymer melt comprises:

between about seven percent and about nine percent colored recycled PET by weight;

up to about five percent PTT by weight;

between about two percent and about three percent color additive by weight; and

balance recycled substantially clear PET.

20. The method of claim 17, wherein the color additive at least partially masks a coloration of the bulked continuous carpet filament caused by the colored recycled PET.

21. The method of claim 20, wherein the bulked continuous carpet filament has a color that is substantially the same as a color of bulked continuous carpet filament produced substantially only from recycled substantially clear PET.

22. The method of claim 17, wherein the colored recycled PET is derived essentially from recycled PET bottles having a color selected from a group consisting of:

i. amber;

ii. blue; and

iii. green.