Method and System for Removing Polychlorinated Biphenyls from Plastics

• US 20100013116A1
• Filed: 07/21/2009
• Published: 01/21/2010
• Est. Priority Date: 07/21/2008
• Status: Abandoned Application

• Current Assignee: MTD America Ltd.
• Original Assignee: MTD America Ltd.
• Inventors: Blyth, Peter C., Bangs, David L.
• Application Number:
  US12/506,907
• Publication Number:
  US 20100013116A1
• Time in Patent Office: Days
• US Class Current: 264/141
• CPC Class Codes: C08J 11/08 using selective solvents for polymer components
• CPC Class Codes: Y02W 30/62 Plastics recycling; Rubber recycling

Abstract

Removing PCBs from recycled plastic materials. A reactor can volatilize the PCBs from interior portions of the plastic materials under pressure conditions below atmospheric pressure and temperatures sufficient to melt the plastic material. The reactor typically includes agitation that exposes the plastic material to the atmosphere within the reactor to promote the volatilization of the PCBs.

Claims

1. A method for removing polychlorinated biphenyls (PCBs) from plastic material comprising the steps of:

receiving a waste stream comprising plastic material contaminated with PCBs;

adding the waste stream to a reactor, wherein the pressure within the reactor is maintained at or below 100 millibars;

establishing a temperature of the reactor above the melting point of the plastic material and the boiling point of the PCBs at the pressure within the reactor to create a molten plastic material;

agitating the molten plastic material; and

extruding the molten plastic material following volatilization of at least a fraction of the PCBs from the plastic material.

2. The method of claim 1 wherein the pressure within the reactor is maintained at or below 10 millibars.

3. The method of claim 1 wherein the pressure within the reactor is maintained at approximately 1 millibar.

4. The method of claim 1 further comprising the step of cleaning the waste stream prior to adding the waste stream to the reactor.

5. The method of claim 1 wherein the waste stream comprises residue from shredding an automobile.

6. The method of claim 1 further comprising the step of pelletizing the extruded plastic material.

7. The method of claim 1 wherein the step of agitating the waste material comprises exposing the entire the volume of plastic material to the atmosphere in the reactor.

8. The method of claim 1 further comprising the step of introducing a solvent into the reactor, wherein the solvent distills PCBs from the molten plastic material.

9. The method of claim 8 wherein the solvent is selected from a group consisting of water vapor, 50/50 acetone/hexane or methylene chloride.

10. The method of claim 1 further comprising the step of screening the molten plastic material while extruding the molten plastic material from the reactor.

11. The method of claim 1 wherein the step of extruding the molten plastic material comprises directly forming the molten plastic into a finished product.

12. A method for removing polychlorinated biphenyls (PCBs) from plastic material comprising the steps of:

receiving a waste stream comprising a volume of plastic material contaminated with PCBs;

cleaning the volume of plastic material;

adding the plastic material to a kneader reactor, wherein the pressure within the kneader reactor is maintained at or below 10 millibars;

establishing a temperature of the kneader reactor above the melting point of the volume of plastic material and the boiling point of the PCBs at the pressure within the kneader reactor to form a molten plastic material;

agitating the molten plastic material to expose the volume of plastic material to the atmosphere in the kneader reactor; and

extruding the molten plastic material following volatilization of at least a fraction of the PCBs from the plastic material.

13. The method of claim 12 wherein the waste stream comprises residue from shredding an automobile.

14. The method of claim 12 further comprising the step of pelletizing the extruded plastic material.

15. The method of claim 12 further comprising the step of introducing a solvent into the kneader reactor, wherein the solvent distills PCBs from the molten plastic material.

16. The method of claim 15 wherein the solvent is selected from a group consisting of water vapor, 50/50 acetone/hexane or methylene chloride.

17. The method of claim 12 wherein the step of extruding the molten plastic material comprises directly forming the molten plastic into a finished product.

18. The method of claim 12 further comprising the step of screening the molten plastic material while extruding the molten plastic material from the kneader reactor.

19. The method of claim 12 further comprising the step of pre-processing the waste stream to concentrate the plastic material in the waste stream.

20. The method of claim 12 wherein the step of agitating the waste material to expose the volume of plastic material to the atmosphere in the kneader reactor comprises forming thin segments of the plastic material.