Granted Patent B2

US 12,404,454 · App. 18/467,217 · Granted Sep 2, 2025

Inventors: Anthony F. Tenore (Yonkers, NY); David Fowler (Yonkers, NY); Oluwadare Oluwaseun (Yonkers, NY); Anthony N. Tenore (Yonkers, NY)

Assignee: Braven Environmental, LLC

C10B47/44B01D53/002B30B9/121C10B31/08C10B53/07C10G1/02C10G1/10C10K1/026C10K1/04B01D2257/702C10G2300/1003C10G2400/02C10G2400/04Y02P20/133Y02P20/143

Abstract

Claims (25)

1. A pyrolysis system for processing plastic, comprising:

an extruder comprising an elongate cantilevered drive shaft connected to a drive coupling, the drive shaft being housed in a tubular barrel housing surrounded at least partially by one or more clamshell heaters, wherein the drive shaft includes auger flights; and

a reactor configured to process pre-processed material supplied via the extruder at an input end, the reactor comprising:

a hollow upper reactor tube including a first screw conveyor within the hollow portion of the upper reactor tube, configured to receive the pre-processed material;

a hollow lower reactor tube connected to the upper reactor tube via a connecting collar, including a second screw conveyor within the hollow portion of the lower reactor tube, configured to receive partially pyrolyzed material from the upper reactor tube; and

a plurality of clamshell heaters surrounding the upper and lower reactor tubes, defining a plurality of individual heating zones.

2. The system of claim 1 , wherein the extruder comprises a heated airlock.

3. The system of claim 2 , further comprising a material supply assembly configured to supply plastic feedstock material to the heated airlock for pre-processing.

4. The system of claim 1 , further comprising a vapor processing system comprising an ash separator or char separator, configured to receive vapor produced in the reactor.

5. The system of claim 1 , wherein the first and second screw conveyors are configured to wipe melted material from a wall and move it downstream through the reactor.

6. The system of claim 5 , wherein the first and second screw conveyors are further configured to carry char to a char discharge system attached proximate to an output end of the reactor.

7. The system of claim 1 , wherein a subset of the plurality of individual heating zones positioned proximate to an output end of the reactor are at a higher temperature than the other individual heating zones.

8. The system of claim 1 , further comprising a thermal expansion system connected to at least one of the reactor and the extruder.

9. The system of claim 1 , wherein the individual heating zones are separately regulated.

10. The system of claim 1 , wherein the individual heating zones are separately powered.

11. The system of claim 1 , wherein the extruder is configured to process the material to a liquid or molten state, and the reactor is configured to process the liquid or molten material received from the extruder into a gaseous state.

12. The system of claim 1 , wherein the upper reactor tube is above the lower reactor tube.

13. The system of claim 1 , wherein the reactor comprises a stacked reactor.

14. The system of claim 1 , wherein the first screw conveyor is configured to convey material in a first direction.

15. The system of claim 14 , wherein the second screw conveyer is configured to convey material in a second direction different from the first direction.

16. The system of claim 1 , wherein the first and second screw conveyors comprise double flighted screws.

17. The system of claim 16 , wherein the double flighted screws include cut and fold slots.

18. The system of claim 1 , wherein the first and second screw conveyors are driven at variable revolutions-per-minute via variable frequency drive motors.

19. The system of claim 1 , wherein the one or more clamshell heaters of the extruder produce heat that allows the extruder to seal and start vaporization of plastic inside the extruder.

20. The system of claim 1 , wherein the one or more clamshell heaters of the extruder are configured to heat first and second sections of the tubular barrel housing to different temperatures.

Continuity (4)

References Cited (337)