Systems and methods for manufacturing bulked continuous filament

• US 9,550,338 B2
• Filed: 05/13/2013
• Issued: 01/24/2017
• 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
• Primary Examiner(s): SOOHOO, TONY GLEN
• Application Number:
  US13/892,713
• Publication Number:
  US 20130320581A1
• Time in Patent Office: 1,352 Days
• US Class Current: 1/1
• CPC Class Codes: B01D 29/0095 Flat filtering elements B01D25/12, B01D25/26 take precedence
• CPC Class Codes: B07C 2501/0036 Sorting out metallic particles
• 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 17/02 Separating plastics from other materials
• 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 2017/0203 Separating plastics from plastics
• CPC Class Codes: B29B 2017/0224 Screens, sieves
• CPC Class Codes: B29B 7/427 with independently driven screws rotating about the same axis, e.g. oscillating axially; with axially oscillating screws B29B7/423 takes precedence
• CPC Class Codes: B29B 7/485 with three or more shafts provided with screws
• CPC Class Codes: B29B 7/7466 Combinations of similar mixers
• CPC Class Codes: B29C 2791/003 Making articles of indefinite length B29C53/48 takes precedence
• CPC Class Codes: B29C 2791/006 Using vacuum
• CPC Class Codes: B29C 2948/922 Viscosity; Melt flow index [MFI]; Molecular weight
• CPC Class Codes: B29C 2948/9238 Feeding, melting, plasticising or pumping zones, e.g. the melt itself
• CPC Class Codes: B29C 2948/9239 Screw or gear
• 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 37/006 Degassing moulding material or draining off gas during moulding venting means in moulds B29C33/10
• 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 48/70 : comprising means for dividing, distributing and recombining melt flows
• 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 2105/0067 : Melt
• CPC Class Codes: B29K 2105/26 : Scrap or recycled material
• 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 1/103 : De-aerating
• CPC Class Codes: D01D 1/106 : Filtering
• CPC Class Codes: D01D 5/00 : Formation of filaments, threads, or the like
• CPC Class Codes: D01D 5/08 : Melt spinning methods D01D5/0023 takes precedence
• CPC Class Codes: D01F 6/62 : from polyesters
• CPC Class Codes: D10B 2503/04 : Floor or wall coverings; Carpets
• CPC Class Codes: H05K 999/99 : dummy group
• CPC Class Codes: Y02P 20/143 : the feedstock being recycled material, e.g. plastics
• CPC Class Codes: Y02W 30/62 : Plastics recycling; Rubber recycling
• CPC Class Codes: Y02W 30/64 : Paper 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 MRS extruder while maintaining the pressure within the MRS portion of the MRS extruder below about 1.5 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 multi-screw extruder for use in extruding a polymer melt, said extruder comprising:

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 pressure regulation system that is adapted to maintain a pressure within said first and second satellite screw extruders below a pressure of about 1.5 millibars as said polymer melt passes through said first and second screw extruders; and

a controller that operates said pressure regulation system to maintain said pressure within said first and second satellite screw extruders below said pressure of about 1.5 millibars while said multi-screw extruder is extruding said polymer melt.

2. The multi-screw extruder of claim 1, wherein:

said pressure regulation system is adapted to maintain a pressure within said first and second satellite screw extruders below a pressure of about 1 millibar as said polymer melt passes through said first and second screw extruders; and

said controller operates said pressure regulation system to maintain said pressure within said first and second satellite screw extruders below said pressure of about 1 millibar while said multi-screw extruder is extruding said polymer melt.

3. The multi-screw extruder of claim 2, wherein:

said extruder comprises 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;

said pressure regulation system is adapted to maintain a pressure within said third satellite screw extruder below a pressure of about 1.5 millibars as said polymer melt passes through said third screw extruder;

said satellite screw extruder support system is adapted to orbitally rotate said third satellite screw about said main axis as said polymer melt passes through said third screw extruder; and

said main axis is substantially parallel to said central axis of said third satellite screw.

4. The multi-screw extruder of claim 3, wherein:

said extruder comprises 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;

said pressure regulation system is adapted to maintain a pressure within said fourth satellite screw extruder below a pressure of about 1.5 millibars as said polymer melt passes through said fourth screw extruder;

said satellite screw extruder support system is adapted to orbitally rotate said fourth satellite screw about said main axis as said polymer melt passes through said fourth screw extruder; and

said main axis is substantially parallel to said central axis of said fourth satellite screw.

5. The multi-screw extruder of claim 1, wherein said extruder comprises a satellite screw extruder support system that is adapted to orbitally rotate said first and second satellite screws about a main axis as said polymer melt passes through said first and second screw extruders, said main axis being substantially parallel to both:

(1) said central axis of said first satellite screw; and

(2) said central axis of said second satellite screw.

6. The multi-screw extruder of claim 5, wherein:

said satellite screw extruder support system comprises a drum that is adapted to rotate about said main axis;

said drum defines a first screw barrel having a central axis that is substantially parallel to said main axis;

said drum defines a second screw barrel having a central axis that is substantially parallel to said main axis;

said first satellite screw is rotatably mounted within said first screw barrel; and

said second satellite screw is rotatably mounted within said second screw barrel.

7. The multi-screw extruder of claim 6, wherein said pressure regulation system is adapted to maintain a pressure within said first and second satellite screw extruders below a pressure of about 1 millibar as said polymer melt passes through said first and second screw extruders;

and

said controller operates said pressure regulation system to maintain said pressure within said first and second satellite screw extruders below said pressure of about 1 millibar while said multi-screw extruder is extruding said polymer melt.

8. The multi-screw extruder of claim 7, wherein said pressure regulation system comprises at least one vacuum pump.

9. The multi-screw extruder of claim 1, further comprising a viscosity sensor adapted to measure an intrinsic viscosity of said polymer melt after said polymer melt has passed through said first and second screw extruders.

10. The multi-screw extruder of claim 9, wherein, in response to determining that said measured intrinsic viscosity is below a particular intrinsic viscosity, said controller operates said pressure regulation system to lower said pressure within said first and second satellite screw extruders.

11. The multi-screw extruder of claim 10, wherein said particular intrinsic viscosity is 0.8 g/dL.

12. A multi-screw extruder for at least partially removing impurities from a polymer melt, wherein said extruder comprises:

at least six satellite screw extruders, each of said at least six satellite screw extruders comprising a satellite screw that is mounted to rotate about a respective central axis of each said satellite screw;

at least one vacuum pump that is adapted to maintain a pressure within said at least six satellite screw extruders below a pressure of about 5 millibars as said polymer melt passes through said at least six satellite screw extruders;

a viscosity sensor that measures a melt viscosity of said polymer melt after said polymer melt has assed through said at least six satellite screw extruders;

a computer-controller that operates said at least one vacuum pump to maintain said pressure within said at least six satellite screw extruders below said pressure of about 5 millibars as said polymer melt passes through said at least six satellite screw extruders and further operates in a feedback control loop with said viscosity sensor to operate said at least one vacuum pump to further reduce said pressure within said at least six satellite screw extruders in response to using said viscosity sensor to measure an intrinsic viscosity of said polymer melt that is below a predetermined level; and

a satellite screw drum that houses said at least six satellite screw extruders orbitally rotates said at least six satellite screw extruders about a main axis as said polymer melt passes through said at least six satellite screw extruders, said main axis being substantially parallel to each said central axis.

13. The multi-screw extruder of claim 12, wherein said extruder is adapted to separate said polymer melt into at least six different streams and feed said at least six different streams into said at least six satellite screw extruders.

14. The multi-screw extruder of claim 13, wherein each of said at least six satellite screw extruders is adapted to rotate in a direction that is the same as a direction in which said satellite screw drum is adapted to rotate.

15. The multi-screw extruder of claim 13, wherein each of said at least six satellite screw extruders is adapted to rotate in a direction that is opposite to a direction in which said satellite screw drum is adapted to rotate.

16. The multi-screw extruder of claim 13, wherein said multi-screw extruder:

comprises a single screw extruder adjacent said satellite screw drum; and

is adapted to recombine said at least six different streams into a single stream in said single screw extruder.

17. The multi-screw extruder of claim 12, wherein:

said at least one vacuum pump is configured to maintain a pressure within said at least six satellite screw extruders below a pressure of about 1.5 millibars; and

said computer-controller operates said at least one vacuum pump to maintain said pressure within said at least six satellite screw extruders below said pressure of about 1.5 millibars as said polymer melt passes through said at least six satellite screw extruders.

18. The multi-screw extruder of claim 17, wherein said at least one vacuum pump comprises a jet vacuum pump.

19. An apparatus for at least partially removing impurities from a recycled polymer comprising:

a first satellite screw extruder that is mounted to rotate about a central axis of said first satellite screw and adapted to at least substantially melt said recycled polymer into molten recycled polymer;

a multi-screw extruder comprising a plurality of satellite screws, each of said plurality of satellite screws being mounted to rotate about a respective central axis, wherein said multi-screw extruder is adapted to orbitally rotate said plurality of satellite screws about a main axis and to separate said polymer melt into a plurality of streams;

at least one vacuum pump adapted to maintain a pressure within said multi-screw extruder below a pressure of about 1.4 millibars as said molten recycled polymer passes through said multi-screw extruder;

a computer-controller that operates said at least one vacuum pump to reduce and maintain said pressure within said multi-screw extruder below a pressure of about 1.4 millibars during extrusion of said molten recycled polymer through said multi-screw extruder; and

a second satellite screw extruder that is mounted to rotate about a central axis of said first satellite screw and adapted to recombine said plurality of streams into a single stream.

20. The apparatus of claim 19, wherein a number of said plurality of satellite screws is the same as a number of said plurality of streams.

21. The apparatus of claim 19, wherein said plurality of satellite screws comprises at least eight satellite screws.