Automobile shredder residue-synthetic plastic material composite, and method for preparing the same

• US 5,503,788 A
• Filed: 07/12/1994
• Issued: 04/02/1996
• Est. Priority Date: 07/12/1994
• Status: Expired due to Fees

• Current Assignee: Jack Lazareck, Martin Walsh
• Original Assignee: Jack Lazareck, Martin Walsh
• Inventors: Walsh, Martin, Lazareck, Jack
• Primary Examiner(s): Dawson, Robert A.
• Assistant Examiner(s): JONES, KENNETH MITCHELL
• Application Number:
  US08/273,844
• Time in Patent Office: 630 Days
• Field of Search: 264/37, 264/115, 264/118, 264/121, 264/122, 264/126, 264/DIG. 69, 428/542.8, 428/903.3
• US Class Current: 264/115
• CPC Class Codes: B03B 2009/068 Specific treatment of shredder light fraction
• CPC Class Codes: B29B 17/02 Separating plastics from other materials
• CPC Class Codes: B29B 2017/0272 Magnetic separation
• CPC Class Codes: B29K 2023/06 PE, i.e. polyethylene
• CPC Class Codes: B29K 2023/12 PP, i.e. polypropylene
• CPC Class Codes: B29K 2025/00 Use of polymers of vinyl-aromatic compounds or derivatives thereof as moulding material
• CPC Class Codes: B29K 2027/06 PVC, i.e. polyvinylchloride
• CPC Class Codes: B29K 2033/12 Polymers of methacrylic acid esters, e.g. PMMA, i.e. polymethylmethacrylate
• CPC Class Codes: B29K 2055/02 ABS polymers, i.e. acrylonitrile-butadiene-styrene polymers
• CPC Class Codes: B29K 2067/00 Use of polyesters or derivatives thereof, as moulding material
• CPC Class Codes: B29K 2067/006 PBT, i.e. polybutylene terephthalate
• CPC Class Codes: B29K 2075/00 Use of PU, i.e. polyureas or polyurethanes or derivatives thereof, as moulding material
• CPC Class Codes: B29K 2077/00 Use of PA, i.e. polyamides, e.g. polyesteramides or derivatives thereof, as moulding material
• CPC Class Codes: B29K 2105/06 containing reinforcements, fillers or inserts
• CPC Class Codes: B29K 2705/00 Use of metals, their alloys or their compounds, for preformed parts, e.g. for inserts
• CPC Class Codes: B29L 2031/3055 Cars
• CPC Class Codes: Y02W 30/52 Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
• CPC Class Codes: Y02W 30/62 Plastics recycling; Rubber recycling
• CPC Class Codes: Y10S 264/912 From toroidal shapes, e.g. resilient tires
• CPC Class Codes: Y10S 264/913 From fiber or filament, or fiber or filament containing article or product, e.g. textile, cloth fabric, carpet, fiberboard
• CPC Class Codes: Y10S 264/916 : From porous material containing articles, e.g. sponge, foam
• CPC Class Codes: Y10S 264/92 : by extruding material recycled from consumer used article or product

Abstract

A method is provided for processing a mixture raw automobile shredder residue, and virgin and/or contaminated synthetic plastic material, e.g., raw post consumer plastic waste. By means of this method, automobile shredder residue produced by a conventional automobile shredder is formed into a first stream by being ground in a first granulating zone to a reasonable small granular size using conventional equipment. A second stream comprising virgin and/or contaminated synthetic plastics material is ground in a second granulating zones. The two streams are combined to provide a processable mixture. The processable mixture is introduced into a high intensity, mixer. The processable mixtures transformed into a semi-molten discharge stream by the kinetic energy imparted to the processable mixture by the mixer are simultaneously vented from the mixer. The semi-molten mixture emerging from the mixer is then introduced into an extruder or press where it is formed into a mass of desired shape, and cooled. This method allows for the production of useful, shaped masses from two different classes of materials which have been otherwise treated as waste.

Claims

1. A method for processing a mixture of combined raw automobile shredder residue and virgin and/or contaminated synthetic plastic polymer which comprises the steps of:

(a) granulating a first stream comprising raw automobile shredder residue in a first granulating zone to provide granulated automobile shredder residue;

(b) granulating a second stream comprising virgin and/or contaminated synthetic plastic polymer in a second granulating zone to provide granulated plastics material;

(c) combining the granulated automobile shredder residue obtained in step (a) and of granulated plastics material obtained in step (b) to provide a processable mixture;

(d) processing said processable mixture obtained in step (c) in a high intensity mixer, said processing transforming said processable mixture in the mixer into a semi-molten discharge stream by kinetic energy imparted to the processable mixture by the mixer while concurrently venting the mixer to remove particulates therefrom and then directing said particulates vented from said mixer to a particulate recovery system and recovering the particulates therein;

(e) forming said semi-molten discharge stream into a shaped mass of desired form; and

(f) recycling said particulates to said first stream upstream of the mixer.

2. The method of claim 1 wherein said forming step (e) comprises (i) extruding said semi-molten discharge stream through a die to provide said shaped mass of said desired form, and then (ii) cooling said shaped mass.

3. The method of claim 1 wherein said forming step (e) comprises discharging said semi-molten discharge stream into a mold of said desired form, and pressing said semi-molten material in said mold into said shaped mass of said desired form, and then cooling said shaped mass.

4. The method of claim 1 including the intermediate step of granulating said raw automobile shredder residue while simultaneously aspirating particulates from said first granulating zone, and directing said particulates to said particulate recovery system.

5. The method of claim 1 wherein a predetermined weighed amount of granulated automobile shredder residue from step (a) is mixed with a predetermined weighed amount of granulated virgin and/or contaminated synthetic plastic polymer, thereby providing said processable mixture.

6. The method of claim 5 wherein the amount of said granulated virgin and/or contaminated synthetic plastic polymer is from about 10 parts to about 85 parts by weight of said processable mixture.

7. The method of claim 1 wherein the kinetic energy imparted to said processable mixture heats said processable mixture to a temperature of about 265°

F. to about 275°

F.

8. The method of claim 2 wherein said forming step (e) includes extruding said semi-molten discharge stream into a cold water bath thereby simultaneously to provide said shaped mass and to cool said extruded shaped mass.

9. The method of claim 5, wherein said predetermined weighed amount of said granulated automobile shredder residue is provided by the steps of:

(g) feeding said granulated automobile shredder residue from said granulating step (a) to an automobile shredder residue weighing station while aspirating particulates;

(h) weighing said granulated automobile shredder residue;

(i) passing said weighed automobile shredder residue to said combining step (c); and

(j) directing said aspirated particulates to said particulate recovery system.

10. The method of claim 5, wherein said predetermined weighed amount of said virgin and/or contaminate synthetic plastic polymer is provided by the steps of:

(g) feeding said virgin and/or contaminated synthetic plastic polymer from said granulating step (b) to a virgin and/or synthetic plastic polymer weighing station while aspirating particulates;

(h) weighing said virgin and/or contaminated synthetic plastic polymer

(i) passing said weighed virgin and/or contaminated synthetic plastic polymer to said combining step (c); and

(j) directing said aspirated particulates to said particulate recovery system.