IP Library Granted Patent US 11,041,123
Granted Patent B1
US 11,041,123 · App. 16/913,841 · Granted Jun 22, 2021

Systems and methods for recycling waste plastics, including waste polystyrene

Inventors: Barry Cavinaw (Wilsonville, OR); Sean Crawford (Tigard, OR); Sebastien Lamaze (Tigard, OR); David Allen (Portland, OR); Eric Christenson (Tualatin, OR); Mark Rumford (Tigard, OR)
Assignee: Agilyx Corporation
C10B7/06C07C4/22C08J11/00C10B53/07C10G1/02C10G1/10C10G2300/1003
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 11,041,123
App. No.
16/913,841
Granted
Jun 22, 2021
Kind
B1
Abstract

Systems and methods for recycling waste plastics are provided, including a system for recovering styrene monomer from waste polystyrene. The system includes a mixing, heating and compacting apparatus to receive a supply of waste polystyrene and to output a densified polystyrene containing melt; a pyrolysis reactor configured to receive the densified polystyrene containing melt and a supply of recycled oligomers, pyrolyze the densified polystyrene containing melt and the recycled oligomers, and output a hydrocarbon gas stream and a solids residue stream; a quenching apparatus configured to receive the hydrocarbon gas stream output from the pyrolysis reactor and condense out oligomers for routing upstream to the pyrolysis reactor to be combined as the supply of recycled oligomers with the densified polystyrene containing melt, and to discharge an altered hydrocarbon gas stream for further processing; and a condenser configured to receive the altered hydrocarbon gas stream from the quenching apparatus and condense out styrene to form a styrene monomer oil product.

Claims (25)

1. A method of recovering a monomer from waste polymer, the method comprising:

mixing, heating and compacting a supply of waste polymer to form a densified polymer containing melt;

supplying the densified polymer containing melt to a pyrolysis reactor along with a supply of recycled oligomers;

pyrolyzing the densified polymer containing melt and recycled oligomers within the pyrolysis reactor to generate a hydrocarbon gas stream and a solids residue stream;

condensing out oligomers from the hydrocarbon gas stream output from the pyrolysis reactor with a quenching apparatus and routing the oligomers upstream to the pyrolysis reactor to be combined as the supply of recycled oligomers with the densified polymer containing melt;

discharging an altered hydrocarbon gas stream from the quenching apparatus;

condensing out a monomer from the altered hydrocarbon gas stream with a primary condenser to form a monomer oil product and a discharged gas stream;

condensing out a hydrocarbon fraction from the discharged gas stream with a secondary condenser; and

directing a stream of hydrocarbons from the hydrocarbon fraction output from the secondary condenser upstream to the quenching apparatus to assist in condensing out the oligomers from the hydrocarbon gas stream output from the pyrolysis reactor.

2. The method of claim 1 , wherein the densified polymer containing melt is supplied to the pyrolysis reactor in a continuous manner.

3. The method of claim 1 , wherein pyrolyzing the densified polymer containing melt and recycled oligomers within the pyrolysis reactor includes simultaneously transporting and heating the densified polymer containing melt and recycled oligomers with a dual screw feed mechanism.

4. The method of claim 1 , wherein the supply of waste polymer is predominately polystyrene waste and the monomer is styrene.

5. A method of recovering a monomer from waste polymer, the method comprising:

pyrolyzing a polymer feedstock and a supply of recycled oligomers within a pyrolysis reactor to generate a hydrocarbon gas stream and a solids residue stream;

condensing out oligomers from the hydrocarbon gas stream output from the pyrolysis reactor with a quenching apparatus and routing the oligomers upstream to the pyrolysis reactor to be combined as the supply of recycled oligomers with the polymer feedstock;

discharging an altered hydrocarbon gas stream from the quenching apparatus;

condensing out a monomer from the altered hydrocarbon gas stream with a primary condenser to form a monomer oil product and a discharged gas stream;

condensing out a hydrocarbon fraction from the discharged gas stream with a secondary condenser; and

directing a stream of hydrocarbons from the hydrocarbon fraction output from the secondary condenser upstream to the quenching apparatus to assist in condensing out the oligomers from the hydrocarbon gas stream output from the pyrolysis reactor.

6. The method of claim 5 , further comprising:

mixing, heating and compacting a supply of waste polymer to form the polymer feedstock; and

supplying the polymer feedstock to the pyrolysis reactor along with the supply of recycled oligomers.

7. The method of claim 5 , wherein the polymer feedstock is supplied to the pyrolysis reactor in a continuous manner.

8. The method of claim 5 , wherein pyrolyzing the polymer feedstock and the supply of recycled oligomers within the pyrolysis reactor includes simultaneously transporting and heating the polymer feedstock and the supply of recycled oligomers with a dual screw feed mechanism.

9. The method of claim 5 , wherein the waste polymer is predominately polystyrene waste and the monomer is styrene.

Assignments (2)
SECURITY INTEREST Recorded Dec 27, 2024
From: AGILYX CORPORATION
To: NORDIC TRUSTEE AS
Reel/Frame 069692/0083 →
TERMINATION OF SECURITY INTEREST Recorded Dec 27, 2024
From: NORDIC TRUSTEE AS
To: AGILYX CORPORATION
Reel/Frame 069792/0126 →
Continuity (3)
Continuation 16388706 · Apr 18, 2019
Continuation 15436541 · Feb 17, 2017
Provisional Application 62297723 · Feb 19, 2016
Cited By (9)
US 12,410,370 US 12,435,278 US 12,453,993 US 12,453,994 US 12,473,506 US 12,509,636 US 12,545,840 US 12,595,424 US 12,649,879