Method for reclaiming thermoplastic materials intended for recycling

Patent metadata

Field	Value
Publication number	US-11794378-B2
Application number	US-201917266983-A
Country	US
Kind code	B2
Filing date	Aug 6, 2019
Priority date	Aug 6, 2018
Publication date	Oct 24, 2023
Grant date	Oct 24, 2023

Abstract

Presented and described is a method for reclaiming thermoplastic materials intended for recycling, such as, for example, polyethylene terephthalate (PET), in the form of flakes. According to the invention, in a first step, the flakes are exposed to an oxidative fluid and heat until contaminated flakes are modified such that, in a second step, they are separated from the remaining flakes as a result of this modification.

First claim

The invention claimed is:

1. A method for reclaiming thermoplastic materials for recycling, comprising:
exposing thermoplastic flakes containing contaminations to an oxidative fluid and heat until contaminated flakes are sufficiently chemically and/or physically modified to cause discoloration of the contaminated flakes;
determining a level of the discoloration of the contaminated flakes using a CIEL*A*B* color model;
using one or more optical sensors to identify the contaminated flakes based on the CIEL*A*B* color model; and
separating identified contaminated flakes having a color “b” value greater than 0, a color “a” value less than minus 4 or a color “L” value less than 50 from any remaining thermoplastic flakes.

2. The method according to claim 1 , wherein the contaminated flakes are separated when they are above 90° C.

3. The method according to claim 1 , wherein the contaminated flakes are forced to react and/or outgas while the method is being carried out by process conditions, and contaminations from the contaminated flakes are separated from a reaction space together with the oxidative fluid.

4. The method according to claim 1 , wherein the thermoplastic flakes are washed before the thermoplastic flakes are exposed to the oxidative fluid.

5. The method according to claim 3 , wherein the separation of the contaminations from the contaminated flakes takes place prior to extrusion and granulation.

6. The method according to claim 1 , wherein agglomerates or flakes, which are stuck or crumbled as a result of exposure to the oxidative fluid, are separated by sifting.

7. The method according to claim 1 , wherein the oxidative fluid is an air-gas mixture with an oxygen content of at least 5%.

8. The method according to claim 1 , wherein the thermoplastic flakes are exposed to a temperature in a range of 160° C. to 240° C.

9. The method according to claim 3 , wherein the oxidative fluid has a relative moisture content in the order of magnitude of 10-6% and 10 −2 % when it is fed to the reaction space.

10. The method according to claim 3 , wherein the oxidative fluid has a dew point of −10° C. to −100° C. when it is fed to the reaction space, and the thermoplastic flakes are dried to a water content below 50 ppm while passing through the reaction space.

11. The method according to claim 1 , wherein a temperature profile during the process is chosen so that more than 30% of the thermoplastic flakes crystallize and wherein low molecular weight contaminations less than 350 Da are expelled by crystallization of the thermoplastic flakes.

12. The method according to claim 3 , further comprising stirring the thermoplastic flakes in the reaction space in a stirrer to reduce clumping of the thermoplastic flakes.

13. The method according to claim 1 , further comprising separating agglomerations and clumped flakes by at least one mechanical sorting processes.

14. The method according to claim 3 , wherein gaseous reaction products and gases which form or migrate out of the flakes are discharged from the reaction space together with the oxidative fluid.

15. The method according to claim 1 , further comprising separating solid contaminants including PET mixtures with radical scavengers, adhesives, PVC and/or polystyrene.

16. The method according to claim 1 , further comprising washing and pre-sorting the thermoplastic flakes before the thermoplastic flakes are exposed to the oxidative fluid and heat.

17. The method according to claim 1 , wherein the thermoplastic material comprises polyethylene terephthalate (PET), polyactide (PLA), polyethylene furanoate (PEF), polypropylene furanate (PPF), high density polyethylene (HDPE) or polypropylene (PP).

18. The semi-finished product or plastic packaging according to claim 1 , wherein the thermoplastic material contains less than 0.3 ppm benzene, toluene or xylene and less than 0.03 ppm phenols.

19. A method for reclaiming thermoplastic materials for recycling, comprising:
exposing thermoplastic flakes containing contaminations to an oxidative fluid and heat until contaminated flakes are sufficiently chemically and/or physically modified to cause discoloration of the contaminated flakes;
determining a level of the discoloration of the contaminated flakes using a CIEL*A*B* color model;
using one or more optical sensors to identify the contaminated flakes based on the CIEL*A*B* color model;
selecting a temperature profile to increase crystallinity of the thermoplastic flakes to an extent of more than 30% to obtain free-flowing granules; and
separating identified contaminated flakes having a color “b” value greater than 0, a color “a” value less than minus 4 or a color “L” value less than 50 from any remaining thermoplastic flakes.

20. The method of claim 19 , further comprising selecting a temperature profile to increase crystallinity of the thermoplastic flakes to an extent of at least 40%.

21. The method of claim 19 , further comprising using the oxidative fluid with a dew point of −10° C. to −100° C. to dry the thermoplastic flakes and to have a water content of less than 50 ppm.

22. The method according to claim 19 , wherein the contaminated flakes are separated when they are above 90° C.

23. The method according to claim 19 , wherein agglomerates or flakes, which are stuck or crumbled as a result of exposure to the oxidative fluid, are separated by sifting.

24. The method according to claim 19 , wherein the oxidative fluid is an air-gas mixture with an oxygen content of at least 5%.

25. The method according to claim 19 , wherein the thermoplastic flakes are exposed to a temperature in a range of 160° C. to 240° C.

26. The method according to claim 19 , wherein the oxidative fluid has a relative moisture content in the order of magnitude of 10 −6 % and 10 −2 % when it is fed to the reaction space.

27. The method according to claim 19 , wherein low molecular weight contaminations less than 350 Da are expelled by crystallization of the thermoplastic flakes.

28. The method according to claim 19 , further comprising stirring the thermoplastic flakes in the reaction space in a stirrer to reduce clumping of the thermoplastic flakes.

29. The method according to claim 19 , wherein the thermoplastic material comprises polyethylene terephthalate (PET), polyactide (PLA), polyethylene furanoate (PEF), polypropylene furanate (PPF), high density polyethylene (HDPE) or polypropylene (PP).

Assignees

• Alpla Werke Alwin Lehner Gmbh & Co Kg

Inventors

• Siegl Robert

Classifications

• B29B17/02 Primary

  Separating plastics from other materials · CPC title

• B29B2017/001

  Pretreating the materials before recovery · CPC title

• B29B2017/0015

  Washing, rinsing · CPC title

• B29B2017/0224

  Screens, sieves · CPC title

• B29B2017/0279

  Optical identification, e.g. cameras or spectroscopy · CPC title