Compositions and methods for recycling plastics comprising polymers via solvent treatment

1. A method of treating a material selected from the group consisting of polyvinyl chloride (PVC), polyethylene terephthalate (PET), and mixtures thereof, said method of treating selected from the group consisting of dissolving, dissolving via melting, selective dissolving, and decomposing said material comprising the steps of contacting said material with a plastic dissolving and/or decomposing composition comprising a turpentine liquid to form a dissolution and/or decomposition mixture, wherein said material is contacted with said plastic dissolving and/or decomposing composition at a ratio of greater than 1:1 of said plastic dissolving and/or decomposing composition to said material, wherein said turpentine liquid is selected from the group consisting of synthetic turpentine, mineral turpentine, alpha-terpineol, beta-terpineol, gamma-terpineol, 3-carene, anethole, nopol, pinane, camphene, p-cymene, anisaldehyde, 2-pinane hydroperoxide, 3,7-dimethyl-1,6-octadiene, isobornyl acetate, terpin hydrate, ocimene, 2-pinanol, dihydromyrcenol, isoborneol, alloocimene, alloocimene alcohols, geraniol, 2-methoxy-2,6-dimethyl-7,8-epoxyoctane, camphor, p-menthan-8-ol, alpha-terpinyl acetate, citral, citronellol, 7-methoxydihydrocitronellal, 10-camphorsulphonic acid, p-menthene, p-menthan-8-yl acetate, citronellal, 7-hydroxydihydrocitronellal, menthol, menthone, polymers thereof, and mixtures thereof, and further comprising the step of recovering said material from said composition.

2. The method of claim 1 , wherein the weight of said plastic material is substantially reduced as compared to weight of said plastic sample before treatment with said plastic dissolution and/or decomposing composition.

3. The method of claim 1 , wherein said composition comprises greater than about 0.01% of said turpentine liquid.

4. The method of claim 3 , wherein said composition comprises greater than about 0.1% of said turpentine liquid.

5. The method of claim 4 , wherein said composition comprises about 1% of said turpentine liquid.

6. The method of claim 2 , wherein the weight of said material is reduced by at least about 30%.

7. The method of claim 6 , wherein the weight of said material is reduced by at least about 50%.

8. The method of claim 7 , wherein the weight of said material is reduced by at least about 70%.

9. A method of treating a material selected from the group consisting of polyvinyl chloride (PVC), low density polyethylene (LDPE), high density polyethylene (HDPE), polypropylene (PP), polyethylene terephthalate (PET), and mixtures thereof, said method of treating selected from the group consisting of dissolving, dissolving via melting, selective dissolving, and decomposing said material comprising the steps of contacting said material with a plastic dissolving and/or decomposing composition comprising a turpentine liquid to form a dissolution and/or decomposition mixture, wherein said material is contacted with said plastic dissolving and/or decomposing composition at a ratio of greater than 1:1 of said plastic dissolving and/or decomposing composition to said material, wherein said turpentine liquid is selected from the group consisting of alpha-terpineol, beta-terpineol, gamma-terpineol, 3-carene, anethole, nopol, pinane, camphene, p-cymene, anisaldehyde, 2-pinane hydroperoxide, 3,7-dimethyl-1,6-octadiene, isobornyl acetate, terpin hydrate, ocimene, 2-pinanol, dihydromyrcenol, isoborneol, alloocimene, alloocimene alcohols, geraniol, 2-methoxy-2,6-dimethyl-7,8-epoxyoctane, camphor, p-menthan-8-ol, alpha-terpinyl acetate, citral, citronellol, 7-methoxydihydrocitronellal, 10-camphorsulphonic acid, p-menthene, p-menthan-8-yl acetate, citronellal, 7-hydroxydihydrocitronellal, menthol, menthone, polymers thereof, and mixtures thereof, and further comprising the step of recovering said material from said composition.

10. The method of claim 1 , wherein said composition further comprises a second liquid.

11. The method of claim 1 , wherein said composition further comprises a second liquid selected from the group consisting of lower aliphatic alcohols, alkanes, aromatics, aliphatic amines, aromatic amines, carbon bisulfide, vegetable oils, solvents manufactured in petroleum refining, dry distilling coal, fractionating liquefied coal, and fractionating extracted hydrocarbons from oil sands and oil shale, and mixtures thereof.

12. The method of claim 11 , wherein said solvent is selected from decant oil, light cycle oil, naphtha, or combinations thereof.

13. A method of treating a material selected from the group consisting of polyvinyl chloride (PVC), polyethylene terephthalate (PET), and mixtures thereof, said method of treating selected from the group consisting of dissolving, dissolving via melting, selective dissolving, and decomposing said material comprising the steps of contacting said material with a plastic dissolving and/or decomposing composition comprising a turpentine liquid to form a dissolution and/or decomposition mixture, wherein said material is contacted with said plastic dissolving and/or decomposing composition at a ratio of greater than 1:1 of said plastic dissolving and/or decomposing composition to said material, wherein said turpentine liquid comprises

about 40 to 60% α-terpineol,

about 30 to 40% β-terpineol,

about 5 to 20% β-pinene, and

about 0 to 10% p-cymene, and further comprising the step of recovering said material from said composition.

14. A method of treating a material selected from the group consisting of polyvinyl chloride (PVC), polyethylene terephthalate (PET), and mixtures thereof, said method of treating selected from the group consisting of dissolving, dissolving via melting, selective dissolving, and decomposing said material comprising the steps of contacting said material with a plastic dissolving and/or decomposing composition comprising a turpentine liquid to form a dissolution and/or decomposition mixture, wherein said material is contacted with said plastic dissolving and/or decomposing composition at a ratio of greater than 1:1 of said plastic dissolving and/or decomposing composition to said material, wherein said turpentine liquid comprises

about 40 to 60% α-terpineol or β-terpineol,

about 5 to 40% α-pinene or β-pinene, and

about 0 to 20% p-cymene, and further comprising the step of recovering said material from said composition.

15. The method of claim 1 , wherein said material comprises at least one of a thermoplastic and a thermosetting polymer.

16. The method of claim 1 , further comprising the step of heating said dissolution and/or decomposition mixture.

17. The method of claim 16 , where said heating is at a temperature that the turpentine liquid remains stable.

18. The method of claim 17 , wherein said temperature is below about 250° C.

19. The method of claim 18 , wherein said temperature is between about 60° C. and about 200° C.

20. The method of claim 1 , wherein said method is performed under ambient or near ambient pressure.

21. The method of claim 20 , wherein said pressure is between about 1×10 4 Pascals (0.1 atm) and about 10×10 5 Pascals (10 atm).

22. The method of claim 1 , wherein said turpentine liquid is not boiling.

23. The method of claim 1 , wherein said turpentine liquid is boiling.

24. The method of claim 23 , wherein said turpentine liquid is boiling with no reflux.

25. The method of claim 23 , wherein said turpentine liquid is boiling with partial reflux.

26. The method of claim 23 , wherein said turpentine liquid is boiling with total reflux.

27. The method of claim 1 , further comprising the step of obtaining one or more polymers from said material dissolved in said composition.

28. The method of claim 1 , wherein said recovery step is performed by flash evaporation.

29. The method of claim 28 , further comprising adding impact modifiers and/or stabilizers to the reaction mixture prior to said recovery step.

30. The method of claim 1 , wherein said plastic material comprises a single polymeric material.

31. The method of claim 9 , wherein said material contains a mixture of a plurality of physically commingled plastics selected from the group consisting of polyvinyl chloride (PVC), low density polyethylene (LDPE), high density polyethylene (HDPE), polypropylene (PP), polyethylene terephthalate (PET), and a combination thereof.

32. The method of claim 31 , wherein at least one of said plastics comprises at least two different polymers.

33. The method of claim 32 , wherein said plastics are separated sequentially, the method comprising at least two contacting and heating steps.

34. The method of claim 33 , wherein said dissolution and/or decomposition mixture is heated to at least to a temperature appreciably greater than the melting point of a first plastic having the lowest melting point, but less than the melting point of any other plastics contained in said plastic material.

35. The method of claim 34 , wherein exclusively said first plastic becomes dissolved in said dissolution and/or decomposition mixture and a remaining plastic material remains in solid form.

36. The method of claim 35 , further comprising separating said remaining plastic material from said dissolution and/or decomposition mixture, transferring said remaining plastic material to a second plastic dissolving and/or decomposing composition to form a second dissolution and/or decomposition mixture, and heating said second dissolution and/or decomposition mixture to a temperature greater than the melting point of a second plastic contained in said plastic material, but less than the melting point of any other plastics contained in said plastic material.

37. The method of claim 36 , further comprising repeating said method steps until all plastics contained in said plastic material are separated.

38. The method of claim 1 , wherein said turpentine liquid is alpha-terpineol, beta-terpineol or a mixture thereof.

39. The method of claim 38 , wherein said turpentine liquid's boiling point is greater than the melting points of plastics contained in said plastic material.

40. The method of claim 39 , wherein said boiling point is greater under ambient pressure.

41. The method of claim 39 , wherein said boiling point is elevated with pressurization.

42. The method of claim 1 , further comprising the step of removing and separating impurities commingled with said material from said material, comprising the steps of heating the material until fillers and/or impurities are released into the dissolution and/or decomposition mixture, and separating said materials from said dissolution and/or decomposition mixture by liquid-solid separation.

43. The method of claim 42 , wherein said liquid-solid separation is performed by hydrocycloning, sieving, sedimentation, flotation, filtration, or centrifugation.

44. The method of claim 10 , wherein said plastic dissolving and/or decomposing composition contains a ratio of said turpentine liquid to said second liquid of greater than or equal to 1:1.

45. The method of claim 44 , wherein said ratio is greater than or equal to about 3:1.

46. The method of claim 1 , wherein said ratio is about 2:1 to 5:1.