Methods for manufacturing bulked continuous filament

• US 10,232,542 B2
• Filed: 03/29/2017
• Issued: 03/19/2019
• Est. Priority Date: 05/31/2012
• Status: Active Grant

• Current Assignee: Aladdin Manufacturing Corporation (Mohawk Industries Incorporated)
• Original Assignee: Mohawk Industries Incorporated
• Inventors: Clark, Thomas R.
• Primary Examiner(s): Tentoni, Leo B
• Application Number:
  US15/473,402
• Publication Number:
  US 20170203487A1
• Time in Patent Office: 720 Days
• Field of Search: 264 401, 264101, 264102, 264140, 2641761, 26421121, 26421122, 26421123
• CPC Class Codes: B29B 13/06 by drying B29B13/08 takes precedence ; drying moulded articles or half products B29C37/0092
• CPC Class Codes: B29B 17/0026 by agglomeration or compacting
• 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 2017/0279 Optical identification, e.g. cameras or spectroscopy
• CPC Class Codes: B29B 2017/0289 Washing the materials in liquids
• CPC Class Codes: B29B 7/485 with three or more shafts provided with screws
• 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 2948/92514 Pressure
• CPC Class Codes: B29C 2948/92857 Extrusion unit
• CPC Class Codes: B29C 48/0022 combined with cutting
• CPC Class Codes: B29C 48/022 characterised by the choice of material
• CPC Class Codes: B29C 48/05 Filamentary, e.g. strands
• CPC Class Codes: B29C 48/144 at the plasticising zone
• CPC Class Codes: B29C 48/255 Flow control means, e.g. valves flow dividers B29C48/695
• CPC Class Codes: B29C 48/2552 provided in the feeding, melting, plasticising or pumping zone, e.g. screw, barrel, gear-pump or ram
• 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 48/425 : using three or more screws serially arranged screws B29C48/38, B29C48/385
• 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 48/525 : Conical screws
• CPC Class Codes: B29C 48/766 : in screw extruders
• CPC Class Codes: B29C 48/767 : through a degassing opening of a barrel
• CPC Class Codes: B29C 48/92 : Measuring, controlling or regulating
• CPC Class Codes: B29D 99/0078 : Producing filamentary materials
• CPC Class Codes: B29K 2067/003 : PET, i.e. poylethylene terephthalate
• CPC Class Codes: B29K 2105/26 : Scrap or recycled material
• CPC Class Codes: B29L 2031/731 : Filamentary material, i.e. comprised of a single element, e.g. filaments, strands, threads, fibres cables B29L2031/707
• CPC Class Codes: C08J 11/04 : of polymers
• CPC Class Codes: C08J 2367/02 : Polyesters derived from dicarboxylic acids and dihydroxy compounds; C08J2367/06 takes precedence
• 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 6/62 : from polyesters
• CPC Class Codes: D02G 3/24 : Bulked yarns or threads, e.g. formed from staple fibre components with different relaxation characteristics
• CPC Class Codes: Y02P 20/143 : the feedstock being recycled material, e.g. plastics
• 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) passing the group of flakes through an expanded surface area extruder while maintaining a pressure within the expanded surface area extruder below about 25 millibars; (E) passing the resulting polymer melt through at least one filter having a micron rating of less than about 50 microns; and (F) 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 a PET crystallizer;

(B) passing a plurality of flakes of recycled PET through the PET crystallizer to at least partially dry a surface of the plurality of flakes of recycled PET;

(C) providing a first extruder, the first extruder comprising;

a first extruder inlet and a first extruder outlet;

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;

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;

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; and

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, wherein the first satellite screw, the second satellite screw, the third satellite screw, and the fourth satellite screw are disposed at least partially within respective extruder barrels;

a satellite screw extruder support system that is adapted to rotate the first, second, third, and fourth satellite screws about a main axis while the first, second, third and fourth satellite screws are rotating about their respective central axes, the main axis being substantially parallel to;

(a) the central axis of the first satellite screw;

(b) the central axis of the second satellite screw;

(c) the central axis of the third satellite screw; and

(d) the central axis of the fourth satellite screw; and

a pressure regulation system that is adapted to maintain a pressure within the first extruder below about 25 millibars;

(D) using the pressure regulation system to reduce a pressure within the first extruder to below about 25 millibars;

(E) after passing the plurality of flakes of recycled PET through the PET crystallizer, while maintaining the pressure within the first extruder below about 18 millibars, passing the plurality of flakes of recycled PET through the first extruder via the first extruder inlet to at least partially melt the plurality of flakes into a polymer melt such that;

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

(F) providing at least one spinning machine comprising at least one spinning machine inlet, wherein the at least one spinning machine inlet is substantially directly coupled to the first extruder outlet;

(G) after the step of passing the polymer melt through the first extruder, substantially immediately forming the polymer melt into bulked continuous carpet filament using the at least one spinning machine.

2. The method of claim 1, wherein:

the pressure regulation system is adapted to maintain the pressure within the first extruder below about 18 millibars; and

the method further comprises using the pressure regulation system to reduce a pressure within the first extruder to below about 18 millibars.

3. The method of claim 1, wherein:

the pressure regulation system is adapted to maintain the pressure within the first extruder below about 12 millibars; and

the method further comprises using the pressure regulation system to reduce a pressure within the first extruder to below about 12 millibars.

4. The method of claim 1, wherein:

the first extruder further comprises;

a fifth satellite screw extruder, the fifth satellite screw extruder comprising a fifth satellite screw that is mounted to rotate about a central axis of the second fifth screw; and

a sixth satellite screw extruder, the sixth satellite screw extruder comprising a sixth satellite screw that is mounted to rotate about a central axis of the sixth screw, wherein the fifth satellite screw extruder and the sixth satellite screw extruder are disposed at least partially within respective extruder barrels; and

the satellite screw extruder support system is adapted to rotate the first, second, third, fourth, fifth, and sixth satellite screws about a main axis while the first, second, third, fourth, fifth, and sixth satellite screws are rotating about their respective central axes.

5. The method of claim 4, wherein:

the first extruder further comprises;

a seventh satellite screw extruder, the seventh satellite screw extruder comprising a seventh satellite screw that is mounted to rotate about a central axis of the second seventh screw; and

a eighth satellite screw extruder, the eighth satellite screw extruder comprising a eighth satellite screw that is mounted to rotate about a central axis of the eighth screw, wherein the seventh satellite screw extruder and the eighth satellite screw extruder are disposed at least partially within respective extruder barrels; and

the satellite screw extruder support system is adapted to rotate the first, second, third, fourth, fifth, sixth, seventh, and eighth satellite screws about a main axis while the first, second, third, fourth, fifth, sixth, seventh, and eighth satellite screws are rotating about their respective central axes.

6. The method of claim 5, wherein the method comprises manufacturing bulked continuous carpet filament from 100% recycled PET substantially immediately after extruding the recycled PET.

7. The method of claim 1, wherein substantially immediately forming the polymer melt into bulked continuous carpet filament comprises substantially immediately forming the polymer melt into bulked continuous carpet filament without substantially cooling the polymer melt.

8. The method of claim 1, wherein the PET crystallizer comprises:

a hopper screw configured to feed the plurality of flakes of recycled PET into the PET crystallizer; and

a blower configured to blow hot air over the plurality of flakes of recycled PET as the plurality of flakes of recycled PET pass through the crystallizer.

9. The method of claim 8, wherein the crystallizer is configured to maintain a temperature of between about 140 degrees Celsius and about 230 Celsius within the crystallizer.

10. The method of claim 9, wherein the PET crystallizer causes the plurality of flakes of recycled PET to at least partially reduce in size.

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

(A) providing a PET crystallizer;

(B) passing a plurality of flakes consisting essentially of recycled PET through the PET crystallizer to at least partially dry a surface of the plurality of flakes of recycled PET;

(C) providing an expanded surface area extruder, wherein the expanded surface area extruder defines an expanded surface area extruder inlet and an expanded surface area extruder outlet and comprises;

a plurality of satellite screws, each of the plurality of satellite screws being at least partially housed within a respective extruder barrel and mounted to rotate about its respective central axis; and

a satellite screw extruder support system that is adapted to orbitally rotate each of the plurality of satellite screws about a main axis as each of the plurality of satellite screws rotate about its respective central axis, the main axis being substantially parallel to each respective central axis;

(D) providing a pressure regulation system configured to reduce a pressure within at least a portion of the expanded surface area extruder below about 25 mbar;

(E) providing a spinning machine defining a spinning machine inlet, wherein the spinning machine inlet is operatively coupled to the expanded surface area extruder outlet;

(F) using the pressure regulation system to reduce the pressure within the at least a portion of the expanded surface area extruder below about 25 mbar;

(G) after passing the plurality of flakes consisting essentially of recycled PET through the PET crystallizer, passing the plurality of flakes consisting essentially of PET flakes through the expanded surface area extruder via the expanded surface area extruder inlet to at least partially melt the plurality of flakes to form a polymer melt such that at least a portion of the polymer melt passes through each the respective satellite screw;

(F) substantially immediately after passing the plurality of flakes through the expanded surface area extruder, using the spinning machine to form the polymer melt into bulked continuous carpet filament.

12. The method of claim 11, wherein using the spinning machine to form the polymer melt into bulked continuous carpet filament substantially immediately after passing the plurality of flakes through the expanded surface area extruder comprises using the spinning machine to form the polymer melt into bulked continuous carpet filament without substantially cooling the polymer melt.

13. A method of manufacturing carpet filament comprising the steps of:

(A) grinding a plurality of recycled PET bottles into a group of polymer flakes;

(B) washing the group of polymer flakes to remove at least a portion of one or more contaminants from a surface of the flakes, the group of flakes comprising a first plurality of flakes that consist essentially of PET and a second plurality of flakes that do not consist essentially of PET;

(C) after the step of washing the first plurality of flakes;

(i) scanning the washed group of flakes to identify the second plurality of flakes,

(ii) separating the second plurality of flakes from the first plurality of flakes;

(D) providing a PET crystallizer;

(E) passing the first plurality of flakes through the PET crystallizer to at least partially dry a surface of the first plurality of flakes;

(F) providing an expanded surface area extruder having an extruder inlet and an extruder outlet and comprising;

at least six satellite screws, each of the at least six of satellite screws being at least partially housed within a respective extruder barrel and mounted to rotate about its respective central axis; and

a satellite screw extruder support system that is adapted to orbitally rotate each of the at least six of satellite screws about a main axis as each of the at least six of satellite screws rotate about its respective central axis, the main axis being substantially parallel to each respective central axis;

(G) providing a pressure regulation system configured to reduce a pressure within the expanded surface area extruder between about 0 mbar and about 25 mbar;

(H) providing a spinning machine having a spinning machine inlet, wherein the spinning machine inlet is directly coupled to the extruder outlet;

(I) using the pressure regulation system to reduce the pressure within the expanded surface area extruder between about 0 mbar and about 25 mbar;

(J) while maintaining the pressure within the expanded surface area extruder between about 0 mbar about 25 mbar, passing the first plurality of flakes through the expanded surface area extruder via the first inlet;

(K) melting the first plurality of flakes using the expanded surface area extruder to produce a polymer melt so that at least a portion of the polymer melt passes through each of the at least six satellite screws; and

(L) substantially immediately after passing the second plurality of flakes through the expanded surface area extruder, spinning the polymer melt into bulked continuous carpet filament using the spinning machine.

14. The method of claim 13, wherein passing the plurality of flakes consisting essentially of PET flakes through the expanded surface area extruder comprises passing the plurality of flakes consisting essentially of PET flakes through the expanded surface area extruder such that at least a portion of the polymer melt passes through each respective extruder barrel while each of the at least six satellite screws is rotating about its the respective axis and the satellite screw support system is rotating about the main axis.

15. The method of claim 14, wherein the method comprises manufacturing bulked continuous carpet filament from 100% recycled PET substantially immediately after extruding the recycled PET.

16. The method of claim 15, wherein manufacturing bulked continuous carpet filament from 100% recycled PET substantially immediately after extruding the recycled PET comprises spinning the polymer melt into bulked continuous carpet filament without substantially cooling the polymer melt.

17. The method of claim 16, wherein the PET crystallizer is configured to reduce a moisture content of the plurality of flakes consisting essentially of recycled PET to between about 30 and about 40 parts per million.

18. The method of claim 13, wherein the at least six satellite screws comprise at least eight satellite screws.

19. The method of claim 18, wherein each of the at least eight satellite screws is at least partially disposed within a respective extruder barrel.

20. The method of claim 13, wherein the pressure regulation system is configured to reduce the pressure within the expanded surface area extruder to between about 0 mbar and about 18 mbar.