Reactor for continuously treating polymeric material
A system for continuously treating recycled polymeric material includes a hopper configured to feed the recycled polymeric material into the system. An extruder can turn the recycled polymeric material in a molten material. In some embodiments, the extruder uses thermal fluids, electric heaters, and/or a separate heater. The molten material is depolymerized in a reactor. In some embodiments, a catalyst is used to aid in depolymerizing the material. In certain embodiments, the catalyst is contained in a permeable container. The depolymerized molten material can then be cooled via a heat exchanger. In some embodiments, multiple reactors are used. In certain embodiments, these reactors are connected in series. In some embodiments, the reactor(s) contain removable static mixer(s) and/or removable annular inserts.
1. A method for continuously treating recycled polymeric material comprising:
continuously feeding a recycled polymeric material into a system using a hopper;
heating said recycled polymeric material in an extruder to continuously turn said recycled polymeric material into a molten material;
continuously filtering said molten material with a filter system;
continuously depolymerizing said molten material into a first wax using a first reactor; and
continuously depolymerizing said molten material into a second wax using a second reactor.
2. The method of claim 1 wherein said first wax has a melting point between 106 degrees Celsius and 135 degrees Celsius.
3. The method of claim 1 wherein said recycled polymeric material comprises crosslinked polyethylene.
4. The method of claim 1 wherein said method further comprises degassing said first wax with nitrogen.
5. The method of claim 1 wherein said recycled polymeric material comprises polyethylene.
6. The method of claim 1 wherein said recycled polymeric material comprises polypropylene.
7. The method of claim 1 wherein said recycled polymeric material comprises polystyrene.
8. The method of claim 1 wherein said depolymerization utilizes a catalyst.
9. The method of claim 1 wherein said first wax has a melting point between 86 degrees Celsius to 105 degrees Celsius.
10. The method of claim 1 further comprising:
continuously cooling said first wax via a heat exchanger.
11. The method of claim 1 further comprising:
continuously purifying said first wax via a purifier system.
12. The method of claim 1 further comprising:
wherein said second wax is different from said first wax,
wherein said first reactor and said second reactor are connected in parallel.
13. The method of claim 1 further comprising:
continuously depolymerizing said molten material into a third wax using a third reactor
wherein said second wax is different from said first wax, and
wherein said first reactor, said second reactor, and said third reactor are connected in parallel.
14. The method of claim 13 wherein said second reactor has a first dimension and said third reactor has a second dimension, wherein said first dimension and said second dimension differ such that said second wax is different from said third wax.
15. The method of claim 13 wherein said first reactor, said second reactor, and said third reactor are in a vertical configuration.
16. The method of claim 13 , wherein said first wax has a melting point between 86 degrees Celsius to 105 degrees Celsius and wherein said second wax has a melting point between 106 degrees Celsius and 135 degrees Celsius.
17. The method of claim 8 wherein said recycled polymeric material comprises polyethylene.
18. The method of claim 8 wherein said recycled polymeric material comprises polypropylene.
19. The method of claim 8 wherein said recycled polymeric material comprises polystyrene.