Solvent based approach to post-consumer recycling of polyethylene terephthalate

1. A process of treating a feed comprising polyethylene terephthalate, said process comprising dissolving said feed in a polar solvent at a temperature between about 100 to 250° C. to produce a dissolved feed; then cooling the dissolved feed to precipitate a solid comprising precipitation of purified polyethylene terephthalate and further separating solid purified polyethylene terephthalate from remaining liquids, wherein said polar solvent is selected from N-methylpyrrolidone, dimethylsulfoxide, dihydrolevoglucosenone, gamma-valerolactone, dimethyl isosorbide, N-methylcaprolactam, eucalyptol and mixtures thereof.

2. The process of claim 1 further comprising centrifuging said dissolved feed to separate said purified polyethylene terephthalate from said dissolved feed.

3. The process of claim 1 further comprising adding an anti-solvent that is less polar than said polar solvent to said dissolved feed followed by said cooling of said dissolved feed to precipitate said purified polyethylene terephthalate, wherein said remaining liquids comprise said polar solvent and said anti-solvent.

4. The process of claim 3 wherein said remaining liquids are purified by distillation, adsorption or phase separation and separated into said polar solvent and said anti-solvent for reuse.

5. The process of claim 1 wherein said feed comprises a mixture of post-consumer polyethylene terephthalate waste.

6. The process of claim 5 wherein said post-consumer polyethylene terephthalate waste, is selected from used water bottles, soda bottles, food containers and other polyethylene terephthalate articles.

7. The process of claim 1 wherein said feed in said polar solvent is at a temperature from about 150-200° C. and a pressure is about 1-100 atm.

8. The process of claim 1 wherein said feed in said polar solvent is at a temperature from about 150-200° C. and a pressure is about 1-5 atm.

9. The process of claim 1 wherein said polyethylene terephthalate and said polar solvent are at a weight ratio from about 1:100 to 1:1.

10. The process of claim 1 wherein said polyethylene terephthalate and said polar solvent are at a weight ratio of about 1:50 to 1:1.

11. The process of claim 2 wherein said solvent and said anti-solvent are present at a weight ratio of from about 10:1 to 1:10.

12. The process of claim 1 wherein said polyethylene terephthalate remains in said polar solvent from about 1 minute to 2 hours.

13. The process of claim 1 wherein said polar solvent has Hansen solubility parameter of about δd=15-20, δp=4-20, δh=3-10.

14. The process of claim 1 wherein said anti-solvent has a Hansen solubility parameter of about δd=12-20, δp=0-4 δh=−0-4.

15. The process of claim 1 wherein said anti-solvent is selected from alkanes, alkenes, aromatic hydrocarbons, and mixtures thereof.

16. The process of claim 1 wherein said dissolved feed is filtered prior to addition of said anti-solvent to separate any undissolved material or dyes.

17. The process of claim 1 wherein said process is a batch, continuous or semicontinuous process.

18. The process of claim 1 wherein said feed further comprises other thermoplastics and polyolefins and said process further comprises separating said other thermoplastics and polyolefins from said polyethylene terephthalate prior to dissolution of said polyethylene terephthalate and either sending said other thermoplastics and polyolefins to a pyrolysis reactor or to be mechanically sorted for further processing.

19. The process of claim 17 wherein said separation of said other plastics from said polyethylene terephthalate is by density difference or hand sorting.

20. The process of claim 17 wherein said polyolefins are sent to a pyrolysis reactor or are mechanically recycled for further processing.