Method for recycling polymers and product produced from said method
09688833 ยท 2017-06-27
Assignee
Inventors
- FREDERIC VIOT (Poncin, FR)
- Philippe Le Bot (Saint Nazaire, FR)
- Francois Gueneron (Chalon sur Saone, FR)
Cpc classification
B29B17/02
PERFORMING OPERATIONS; TRANSPORTING
Y02W30/62
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
C08J11/08
CHEMISTRY; METALLURGY
C08J11/02
CHEMISTRY; METALLURGY
International classification
C08J11/02
CHEMISTRY; METALLURGY
C08J11/08
CHEMISTRY; METALLURGY
Abstract
The invention relates to a recycling method for obtaining a polymer from post-consumer materials, and to a material and a part consisting of polymers obtained from the recycling of used polymers.
Claims
1. A method for recycling polymers from ground post-consumer materials, the method comprising a step for extracting volatile organic compounds present within said polymers, wherein said volatile organic compounds are extracted by contacting the ground materials with a solution comprising at least a wetting agent and/or an agent for solubilizing fatty acid esters, at a temperature between 15 C. and 5 C. below the boiling point of said solution.
2. The method for recycling according to claim 1, wherein said wetting agent is an alcohol.
3. The method for recycling according to claim 2, wherein said wetting agent is a C1-C5 aliphatic alcohol.
4. The method for recycling according to claim 2, wherein the alcohol content of said solution is between 4% and 25% by volume.
5. The method for recycling according to claim 1, wherein said agent for solubilizing said fatty acid esters is an acid added to said solution so that the solution pH is greater than or equal to 2 and less than or equal to 5.
6. The method for recycling according to claim 5, wherein said acid is selected from the group of mineral acids.
7. The method for recycling according to claim 1, wherein fragments of the ground material have a thickness of less than 5 mm and have a surface area of between 1 cm.sup.2 and 4 cm.sup.2.
8. The method for recycling according to claim 1, wherein said volatile organic compounds to be extracted are molecules of molar mass less than 400 g/mol.
9. The method according to claim 1, wherein said polymers to be recycled are polyolefins (homopolymers or copolymers of olefins).
10. The method for recycling according to claim 1, wherein said extraction is carried out under atmospheric pressure.
11. The method for recycling according to claim 1, wherein said solution is in liquid state.
12. The method for recycling according to claim 1, wherein said polymer resulting from said method is the same as the polymer contained in said post-consumer material subjected to said method.
13. The material obtained from the method according to claim 1.
14. The part manufactured in the material according to claim 13.
15. The method for recycling according to claim 3, wherein the alcohol content of said solution is between 4% and 25% by volume.
16. The method for recycling according to claim 2, wherein fragments of the ground material have a thickness of less than 5 mm and have a surface area of between 1 cm.sup.2 and 4 cm.sup.2.
17. The method for recycling according to claim 2, wherein fragments of the ground material have a thickness of less than 5 mm and have a surface area of between 1 cm.sup.2 and 4 cm.sup.2.
18. The method for recycling according to claim 2, wherein said volatile organic compounds to be extracted are molecules of molar mass less than 400 g/mol.
19. The method for recycling according to claim 2, wherein said volatile organic compounds to be extracted are molecules of molar mass less than 400 g/mol.
20. The method for recycling according to claim 2, wherein said wetting agent is a C1-C3 alcohol.
21. The method for recycling according to claim 1, wherein said wetting agent is a denatured alcohol containing a mixture of C1, C2 and C3 alcohols.
22. The method for recycling according to claim 1, wherein said agent for solubilizing said fatty acid esters is an acid added to said solution so that the solution pH is between 4 and 5.
23. The method for recycling according to claim 5, wherein said acid is hydrochloric acid or sulphuric acid.
24. The method according to claim 1, wherein said polymers to be recycled is polypropylene.
Description
BRIEF DESCRIPTION OF THE ACCOMPANYING DRAWINGS
(1)
(2)
(3)
(4)
(5)
(6)
(7)
(8)
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
(9)
(10) The facility 10 is designed to recover fragments of polyethylene and polypropylene from shredded post-consumer materials 12. In the example described, the shredded post-consumer materials 12 come from a motor vehicle.
(11) Shredded motor vehicle materials consist of a mixture of shredded components of a motor vehicle, once the battery, tires and metal have been recovered.
(12) In general, shredded post-consumer materials 12 include fragments 14 of metallic materials, mineral materials, polymer materials and wood.
(13) The density of wood fragments is generally less than 1 due to the wood structure comprising cavities filled with gas.
(14) In addition, the shredded post-consumer materials 12 may also include fragments of metallic materials such as copper, this material having a density greater than 1.
(15) To separate the fragments of polyethylene and polypropylene from the other fragments, the facility 10 comprises a hammermill 16.
(16) Grinding of the shredded post-consumer materials 12 results in ground materials 28. In these ground materials 28, the dimensions of most of the fragments of polypropylene and polyethylene are greater than 80 mm while those of the other fragments are much less than 80 mm.
(17) To separate the fragments of polyethylene and polypropylene from first ground materials 28, the facility 10 also comprises a screening device 32 to screen the first ground materials 28.
(18) The screening device 32 comprises a sieve 34 whose mesh has an elementary pattern of dimension equal to 80 mm so as to recover second ground materials 36, essentially comprising the fragments of polyethylene and polypropylene of dimensions greater than 80 mm, and remove residual fragments of dimensions less than 80 mm.
(19) The second ground materials 36 may possibly include residual fragments of wood and polymers.
(20) To remove the residual fragments of wood from the second ground materials 36 by densification, the facility 10 comprises a first container 38 containing a liquid medium 40 comprising a basic solution.
(21) This basic solution is designed in particular to densify the wood by hydrolysis.
(22) The container 38 containing the liquid 40 allows the separation of a supernatant portion forming third ground materials 42 from a portion 44, which sinks, containing the densified wood fragments as well as other residual fragments of heavy materials such as, for example, polyethylene and polypropylene.
(23) The facility 10 also comprises a second container 46 containing a liquid medium 48, for cleaning the fragments of the third ground materials 42 obtained previously.
(24) In addition, to remove the foam fragments and recover the fragments of polyethylene and polypropylene in the third ground materials 42, the facility 10 further comprises means 50 for separation by ventilation.
(25) The means for separation by ventilation 50 comprise fans 52.
(26) The facility 10 further comprises a third container 54 for recovering fourth ground materials 56 comprising at least the fragments of polyethylene and polypropylene and from which the foam fragments have been removed.
(27) To convey the ground materials to the containers 38, 46 and 54, the facility 10 also comprises: an upstream conveyor belt 58 for conveying the second ground materials 36 to the first container, an intermediate conveyor belt 60 for conveying the third ground materials 42 to the second container 46, and a downstream conveyor belt 62 for conveying the fourth ground materials 56 to the third container 54.
(28) The extraction method according to the invention is preferably applied to the fourth ground materials 56. It may also be applied to the ground materials 28, 36 and 42. It may also be applied to ground materials from a recycling facility comprising variants of the equipment described with reference to
(29) In one embodiment of the method, the ground materials are contacted with the extraction solution for 15 minutes while stirring in order to homogenize the temperature between the liquid and solid phases. The ground materials are then dried by centrifuging. The extraction method can be repeated in several successive tanks.
(30)
(31)
(32)
(33)
(34)
(35)
(36) The invention is not limited to the embodiments described above.
(37) The volatile organic compounds can be extracted by using another wetting agent and another agent for solubilizing the fatty acid esters.
(38) Also, the recycling method can be used to manufacture parts other than bodywork parts for motor vehicles and even parts for sectors other than the automotive sector.
(39) Lastly, the recycling method can be applied to polymers other than polypropylene.
(40) While the process and method herein described constitute preferred embodiments of this invention, it is to be understood that the invention is not limited to this precise process and method, and that changes may be made therein without departing from the scope of the invention which is defined in the appended claims.