Method for purifying contaminated polymers

Patent metadata

Field	Value
Publication number	US-9890225-B2
Application number	US-201615190236-A
Country	US
Kind code	B2
Filing date	Jun 23, 2016
Priority date	Jun 30, 2015
Publication date	Feb 13, 2018
Grant date	Feb 13, 2018

Abstract

A method for purifying a reclaimed polymer, such as a polymer reclaimed from post-consumer use or post-industrial use, is disclosed. The method involves obtaining the reclaimed polymer and dissolving it in a solvent at an elevated temperature and pressure to produce a polymer solution, which is purified at an elevated temperature and pressure by contacting the polymer solution with solid media to produce a purer polymer solution. A purer polymer is then separated from the purer polymer solution.

First claim

What is claimed is:

1. A method for purifying a reclaimed polymer comprising:
a. obtaining the reclaimed polymer wherein said reclaimed polymer is selected from the group consisting of post-consumer use polymers, post-industrial use polymers, and combinations thereof;
b. dissolving the reclaimed polymer in a solvent selected from the group consisting of a first fluid solvent, a second fluid solvent, and mixtures thereof, wherein the first fluid solvent and the second fluid solvent have standard boiling points of less than about 70° C., at a temperature from about 90° C. to about 220° C. and a pressure from about 350 psig (2.41 MPa) to about 20,000 psig (137.90 MPa) to produce a polymer solution;
c. purifying said polymer solution at a temperature from about 90° C. to about 220° C. and at a pressure from about 350 psig (2.41 MPa) to about 20,000 psig (137.90 MPa) by contacting said polymer solution with solid media to produce a purer polymer solution; and
d. separating a purer polymer from said purer polymer solution;
wherein said second fluid solvent is the same chemical composition as or a different chemical composition than the first fluid solvent.

2. The method of claim 1 , wherein the purer polymer is separated from said purer polymer solution at a temperature from about 0° C. to about 220° C. and a pressure from about 0 psig (0 MPa) to 2,000 psig (13.79 MPa).

3. The method of claim 1 , wherein the reclaimed polymer is post-consumer recycle derived polymer.

4. The method of claim 1 , wherein said reclaimed polymer is polystyrene.

5. The method of claim 1 , wherein said reclaimed polymer is poly(dimethylsiloxane).

6. The method of claim 1 , wherein said reclaimed polymer is a polypropylene homopolymer or a primarily polypropylene copolymer.

7. The method of claim 1 , wherein said polymer is a polyethylene homopolymer or a primarily polyethylene copolymer.

8. The method of claim 1 , wherein said fluid solvent has a standard boiling point less than about 0° C. and greater than about −45° C. and a standard enthalpy change of vaporization of less than about +25 kJ/mol.

9. The method of claim 1 , wherein said fluid solvent is selected from the group consisting of olefinic hydrocarbons, aliphatic hydrocarbons, and mixtures thereof.

10. The method of claim 9 , wherein said fluid solvent is an aliphatic hydrocarbon selected from the group consisting of C 1 -C 6 aliphatic hydrocarbons and mixtures thereof.

11. The method of claim 9 , wherein said fluid solvent comprises primarily C 4 aliphatic hydrocarbons.

12. The method of claim 9 , wherein said fluid solvent consists essentially of C 4 liquefied petroleum gas.

13. The method of claim 10 , wherein said fluid solvent is n-butane, butane isomers, or mixtures thereof.

14. The method of claim 1 , wherein said temperature in steps b and c is from about 110° C. to about 170° C.

15. The method of claim 1 , wherein said reclaimed polymer is polypropylene and said pressure in step b is from about 1,100 psig to about 20,000 psig.

16. The method of claim 1 , wherein said reclaimed polymer is polypropylene and said pressure in step b is from about 2,100 psig to about 20,000 psig.

17. The method of claim 1 , wherein said reclaimed polymer is polyethylene and said pressure in step b is from about 4,500 psig to about 20,000 psig.

18. The method of claim 1 , wherein said reclaimed polymer is polyethylene and said pressure in step b is from about 5,500 psig to about 20,000 psig.

19. The method of claim 1 , wherein said solid media is selected from the group consisting of inorganic substances, carbon-based substances, and mixtures thereof.

20. The method of claim 19 , wherein said inorganic substances are selected from the group consisting of oxides of silicon, oxides of aluminum, oxides of iron, aluminum silicates, amorphous volcanic glasses, and mixtures thereof.

21. The method of claim 19 , wherein said inorganic substances are selected from the group consisting of silica, silica gel, diatomite, sand, quartz, alumina, perlite, fuller's earth, bentonite, and mixtures thereof.

22. The method of claim 19 , wherein said inorganic substances is reclaimed glass.

23. The method of claim 19 , wherein said carbon-based substances are selected from the group consisting of anthracite coal, carbon black, coke, activated carbon, cellulose, and mixtures thereof.

24. The method of claim 1 , wherein the polymer solution is contacted with a packed bed of said solid media.

25. The method of claim 24 , where said packed bed is greater than 20 cm in length.

Assignees

• Procter & Gamble

Inventors

• Layman John Moncrief
• Gunnerson Maggie
• Schonemann Hans
• Williams Kara

Classifications

• C08F6/00 Primary

  Post-polymerisation treatments (C08F8/00 takes precedence; of conjugated diene rubbers C08C) · CPC title

• C08J2323/10

  Homopolymers or copolymers of propene · CPC title

• C08F6/10

  Removal of volatile materials, e.g. solvents {(C08F6/001, C08F6/003, C08F6/005, C08F6/006, C08F6/008, C08F6/02, C08F6/04 take precedence)} · CPC title

• C08F6/02

  Neutralisation of the polymerisation mass, e.g. killing the catalyst (short-stopping C08F2/42 ){also removal of catalyst residues} · CPC title

• B29B2017/0293

  Dissolving the materials in gases or liquids · CPC title