Method of manufacturing bulked continuous carpet filament

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

(A) providing a multi-screw extruder that comprises:

(i) an MRS Section comprising a plurality of satellite screws, each of the plurality of satellite screws mounted to rotate about its respective central axis;

(B) providing a first vacuum pump configured to independently maintain a pressure within the MRS Section between about 0 millibars and about 40 millibars, the first vacuum pump being operatively coupled to the MRS Section via a first opening;

(C) providing a second vacuum pump arranged in parallel with the first vacuum pump and configured to independently maintain a pressure within the MRS Section between about 0 millibars and about 40 millibars and cooperate with the first vacuum pump to maintain a pressure within the MRS Section between about 0 millibars and about 5 millibars;

(D) using the first vacuum pump and the second vacuum pump to maintain the pressure within the MRS Section to between about 0 millibars and about 5 millibars;

(E) passing a polymer melt comprising recycled PET through the multi-screw extruder while the first vacuum pump and the second vacuum pump are maintaining the pressure in the MRS Section between about 0 millibars and about 5 millibars; and

(F) after the step of passing the polymer melt through the multi-screw extruder, feeding the polymer melt into a first polymer transfer line and a second polymer transfer line, wherein said first vacuum pump and said second vacuum pump are in operative communication with opposing portions of the MRS section.

2. The method of claim 1 , further comprising:

(G) providing a first spinning machine;

(H) using the first spinning machine to produce bulked continuous carpet filament via the first polymer transfer line;

(I) providing a second spinning machine; and

(J) using the second spinning machine to produce bulked continuous carpet filament via the second polymer transfer line.

3. The method of claim 2 , further comprising:

(K) shutting down the second vacuum pump for cleaning; and

(L) while the second vacuum pump is shut down for cleaning, using the first vacuum pump to maintain the pressure within the MRS Section between about 20 millibars and about 40 millibars.

4. The method of claim 3 , further comprising:

(M) continuing to use the first and second spinning machines to produce bulked continuous carpet filament while the second vacuum pump is shut down for cleaning.

5. The method of claim 3 , further comprising:

(M) shutting down the first vacuum pump for cleaning; and

(N) while the first vacuum pump is shut down for cleaning, using the second vacuum pump to reduce the pressure within the MRS Section to between about 20 millibars and about 40 millibars.

6. The method of claim 5 further comprising:

while the first vacuum pump is shut down for cleaning, using the second vacuum pump to reduce the pressure within the MRS Section to about 30 millibars.

7. The method of claim 5 , wherein shutting down the first vacuum pump for cleaning comprises mechanically isolating the first vacuum pump from the MRS Section.

8. The method of claim 5 , further comprising:

while the first vacuum pump is shut down for cleaning, cleaning one or more components that make up the first vacuum pump.

9. The method of claim 8 , wherein the one or more components are selected from the group consisting of:

one or more catch pots;

one or more pipes; and

one or more elbows.

10. The method of claim 3 , further comprising:

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

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;

after the step of washing the first plurality of flakes:

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

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

melting the first plurality of flakes into the polymer melt prior to passing the polymer melt through the multi-screw extruder.

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

(A) providing a multi-screw extruder that comprises:

a multi-rotating screw (MRS) section housing 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;

(B) providing a pressure regulation system configured to reduce a pressure within the multi-rotating screw section to between about 0 mbar and about 5 mbar, the pressure regulation system comprising at least a first catch pot and a second catch pot, wherein the first catch pot and the second catch pot are both configured to collect one or more volatile organics and other material removed from a polymer melt by a low-pressure vacuum created by the pressure regulation system;

(C) using the pressure regulation system to maintain the pressure within the MRS Section to between about 0 millibars and about 5 millibars;

(D) passing a polymer melt comprising recycled PET through the multi-screw extruder while the pressure regulation system is maintaining the pressure in the MRS Section between about 0 millibars and about 5 millibars;

(E) after the step of passing the polymer melt through the multi-screw extruder, feeding the polymer melt into a first polymer transfer line and a second polymer transfer line;

(F) providing a first spinning machine;

(G) using the first spinning machine to produce bulked continuous carpet filament via the first polymer transfer line;

(H) providing a second spinning machine;

(I) using the second spinning machine to produce bulked continuous carpet filament via the second polymer transfer line;

(J) at least partially shutting down the pressure regulation system;

(K) while the pressure regulation system is at least partially shut down, cleaning at least the first catch pot; and

(L) after cleaning at least the first catch pot, resuming full operation of the pressure regulation system, wherein:

the pressure regulation system comprises a first vacuum pump and a second vacuum pump;

said first vacuum pump and said second vacuum pump are in operative communication with opposing portions of the MRS section; and

at least partially shutting down the pressure regulation system comprises shutting down the first vacuum pump and using the second vacuum pump to maintain a pressure within the MRS Section of between about 20 mbar and about 40 mbar; and

cleaning at least the first catch pot comprises cleaning one or more components of the first vacuum pump.

12. The method of claim 11 , wherein:

the pressure regulation system comprises a first vacuum pump;

at least partially shutting down the pressure regulation system comprises shutting down the first vacuum pump;

the first catch pot and the second catch pot are operably connected to a vacuum chamber of the first vacuum pump; and

cleaning at least the first catch pot comprises cleaning the first catch pot and the second catch pot.

13. The method of claim 11 , wherein:

the first catch pot and the second catch pot are operably connected to a vacuum chamber of the first vacuum pump;

at least partially shutting down the pressure regulation system comprises mechanically isolating the first catch pot from the vacuum chamber of the first vacuum pump;

cleaning at least the first catch pot comprises cleaning the first catch pot; and

the method further comprises:

while the first catch pot is mechanically isolated from the vacuum chamber of the first vacuum pump:

continuing to use the pressure regulation system to maintain the pressure within the MRS Section to between about 0 millibars and about 5 millibars; and

continuing to pass the polymer melt comprising recycled PET through the multi-screw extruder while the pressure regulation system is maintaining the pressure in the MRS Section between about 0 millibars and about 5 millibars, wherein:

the second catch pot is configured to collect the one or more volatile organics and other material removed from the polymer melt by the low-pressure vacuum created by the pressure regulation system while the first catch pot is mechanically isolated from the vacuum chamber of the first vacuum pump.

14. The method of claim 11 , wherein at least partially shutting down the pressure regulation system further comprises mechanically isolating the first vacuum pump from the MRS Section.

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

continuing to produce bulked continuous carpet filament via the first and second polymer transfer lines while the pressure regulation system is at least partially shut down.

16. The method of claim 11 , wherein at least partially shutting down the pressure regulation system comprises using the second vacuum pump to maintain the pressure within the MRS Section at about 30 mbar.

17. The method of claim 11 , further comprising:

providing a viscosity sensor;

using the viscosity sensor to measure an intrinsic viscosity of the polymer melt after the polymer melt passes through the multi-screw extruder; and

using the second vacuum pump to reduce the pressure in the MRS Section in response to the viscosity sensor measuring the intrinsic viscosity to be below a particular viscosity level.

18. The method of claim 17 , wherein the particular viscosity level is below about 0.79 dL/g.

19. The method of claim 11 , wherein the pressure regulation system is configured to remove the one or more volatile organics and other material from the polymer melt.