Purification of a conventional polymer flow contaminated with PLA
Method for purifying a conventional polymer stream (PE, PP, PET, PVC, etc.) contaminated with not more than 50% PLA, comprising steps for the suspension of the polymer with solubilisation of the PLA fraction and the recovery of the purified polymer after separation.
1. Method for purifying a polymer stream comprising PE, PP, PET and/or PVC and a fraction by weight of not more than 50% poly(lactic acid) (PLA), characterised in that it comprises the steps of:
a) suspending the polymer stream in a lactic ester suitable for dissolving the PLA fraction at a temperature comprised between 50° C. and the melting point of the polymer stream and a pressure comprised between 0.05 and 20 bar; and
b) separating the suspension into a filtrate comprising lactic ester, PLA and other dissolved impurities and a solid fraction comprising recovered polymer.
2. Method according to claim 1 , characterised in that the method further comprises shredding the polymer mixture prior to suspending the polymer mixture.
3. Method according to claim 1 , characterised in that the polymer mixture is suspended in the lactic ester at a ratio of polymer mixture:lactic ester between about 0.1 and about 1 (weight:weight).
4. Method according to claim 3 , characterised in that the ratio is between about 0.5 and about 1.
5. Method according to claim 1 , characterised in that the polymer mixture is suspended in the lactic ester at a temperature between about 50° C. and the boiling point of the lactic ester.
6. Method according to claim 1 , characterised in that the working pressure is between about 1 and about 10 bar.
7. Method according to claim 1 , characterised in that the working pressure is between about 1 and about 5 bar.
8. Method according to claim 1 , characterised in that the lactic ester is an alkyl lactate wherein the alkyl radical contains between 1 to 12 carbon atoms.
9. Method according to claim 6 , characterised in that the alkyl lactate is selected from the group consisting of methyl, ethyl, propyl, butyl and hexyl lactate.
10. Method according to claim 1 , characterised in that the purified polymer mixture is washed subsequent to the separating step.
11. Method according to claim 1 , characterised in that the purified polymer mixture is dried subsequent to the separating step.
12. Method according to claim 1 , characterised in that the polymer mixture is of petrochemical origin.
13. Method according to claim 2 , characterised in that the polymer mixture is suspended in the lactic ester at a ratio of polymer mixture:lactic ester between about 0.1 and about 1 (weight:weight).
14. Method according to claim 11 , characterised in that the ratio is between about 0.5 and about 1.
15. Method according to claim 2 , characterised in that the polymer mixture is suspended in the lactic ester at a temperature between about 50° C. and the boiling point of the lactic ester.
16. Method according to claim 2 , characterised in that the lactic ester is an alkyl lactate wherein the alkyl radical contains between 1 to 12 carbon atoms.