Method of manufacturing bulked continuous filament

• US 9,630,353 B2
• Filed: 11/18/2014
• Issued: 04/25/2017
• 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:
  US14/546,819
• Publication Number:
  US 20150069655A1
• Time in Patent Office: 889 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, said method comprising:

(A) providing a PET crystallizer;

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

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

a first extruder inlet and a first extruder outlet;

a first satellite screw extruder, said first satellite screw extruder comprising

a first satellite screw that is mounted to rotate about a central axis of said first satellite screw;

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

a third satellite screw extruder, said third satellite screw extruder comprising a third satellite screw that is mounted to rotate about a central axis of said third satellite screw; and

a fourth satellite screw extruder, said fourth satellite screw extruder comprising a fourth satellite screw that is mounted to rotate about a central axis of said fourth satellite screw, wherein said first satellite screw, said second satellite screw, said third satellite screw, and said fourth satellite screw are disposed at least partially within respective extruder barrels;

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

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

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

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

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

a pressure regulation system that is adapted to maintain a pressure within said first extruder below about 18 millibars;

(D) using said pressure regulation system to reduce a pressure within said first extruder to below about 18 millibars;

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

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

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

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

2. The method of claim 1, wherein:

said pressure regulation system is adapted to maintain said pressure within said first extruder below about 5 millibars; and

said method further comprises using said pressure regulation system to reduce a pressure within said first extruder to below about 5 millibars.

6. The method of claim 1, wherein:

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

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

7. The method of claim 1, wherein:

said first extruder further comprises;

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

a sixth satellite screw extruder, said sixth satellite screw extruder comprising a sixth satellite screw that is mounted to rotate about a central axis of said sixth screw; and

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

8. The method of claim 7, wherein:

said first extruder further comprises;

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

a eighth satellite screw extruder, said eighth satellite screw extruder comprising a eighth satellite screw that is mounted to rotate about a central axis of said eighth screw; and

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

9. The method of claim 8, wherein said method comprises manufacturing bulked continuous carpet filament from 100% recycled PET substantially immediately after extruding said recycled PET.

10. The method of claim 1, wherein aid PET crystallizer is configured to reduce a moisture content of said plurality of flakes of recycled PET to between about 30 and about 40 parts per million.

11. The method of claim 1, wherein said PET crystallizer comprises:

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

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

12. The method of claim 11, wherein said crystallizer is configured to maintain a temperature of between about 140 degrees Celsius and about 230 Celsius within said crystallizer.

13. The method of claim 12, wherein said PET crystallizer causes said plurality of flakes of recycled PET to at least partially reduce in size.

3. A method of manufacturing bulked continuous carpet filament, said method comprising:

(A) providing a PET crystallizer;

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

(C) providing an expanded surface area extruder, wherein said 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 wherein each respective satellite screw of the plurality of satellite screws is mounted to rotate about its respective central axis; and

a single screw drum mounted to rotate about its central axis, wherein;

said central axis of said single screw drum is parallel to each respective central axis of said plurality of satellite screws;

said plurality of satellite screws are arranged within said single screw drum and at least partially housed within respective extruder barrels; and

each said respective satellite screw is configured to rotate about its said respective axis while said single screw drum rotates about said central axis of said single screw drum;

(D) providing a pressure regulation system configured to reduce a pressure within at least a portion of said expanded surface area extruder below about 12 mbar;

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

(F) using said pressure regulation system to reduce said pressure within said at least a portion of said expanded surface area extruder below about 12 mbar;

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

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

4. The method of claim 3, wherein:

said pressure regulation system is further configured to reduce said pressure within said at least a portion of said expanded surface area extruder below about 6 mbar.

14. The method of claim 3, wherein passing said plurality of flakes consisting essentially of PET flakes through said expanded surface area extruder comprises passing said plurality of flakes consisting essentially of PET flakes through said expanded surface area extruder such that at least a portion of said polymer melt passes through each said respective satellite screw while each said respective satellite screw is rotating about its said respective axis and said single screw drum is rotating about said central axis of said single screw drum.

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

16. The method of claim 3, wherein said PET crystallizer is configured to reduce a moisture content of said plurality of flakes consisting essentially of recycled PET to between about 30 and about 40 parts per million.

17. The method of claim 3, wherein said plurality of satellite screws comprise at least four satellite screws.

18. The method of claim 17, wherein said plurality of satellite screws comprise eight satellite screws.

5. 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 said group of polymer flakes to remove at least a portion of one or more contaminants from a surface of said flakes, said 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 said step of washing said first plurality of flakes;

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

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

(D) providing a PET crystallizer;

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

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

at least four satellite screws wherein each respective satellite screw of the at least four satellite screws is mounted to rotate about its respective central axis; and

a single screw drum mounted to rotate about its central axis, wherein;

said central axis of said single screw drum is parallel to each respective central axis of said at least four satellite screws;

said at least four satellite screws are arranged within said single screw drum and at least partially housed within respective extruder barrels; and

each of said at least four satellite screws is configured to rotate about its said respective axis while said single screw drum rotates about said central axis of said single screw drum;

(G) providing a pressure regulation system configured to reduce a pressure within said expanded surface area extruder between about 0 mbar and about 5 mbar;

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

(I) using said pressure regulation system to reduce said pressure within said expanded surface area extruder between about 0 mbar and about 5 mbar;

(J) while maintaining said pressure within said expanded surface area extruder between about 0 mbar about 5 mbar, passing said first plurality of flakes through said expanded surface area extruder via said fist inlet;

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

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