Recovery of asphalt shingle components by solvent extraction

• US 4,222,851 A
• Filed: 11/06/1978
• Issued: 09/16/1980
• Est. Priority Date: 11/06/1978
• Status: Expired due to Term

• Current Assignee: DAVY Mckee Corporation
• Original Assignee: Dravo Corporation
• Inventors: Quenin, Paul P., Good, deceased, Robert D.
• Primary Examiner(s): O'Keefe, Veronica
• Application Number:
  US05/958,172
• Time in Patent Office: 680 Days
• Field of Search: 208/45, 208/39, 423/658.5
• US Class Current: 208/45
• CPC Class Codes: C10C 3/007 winning and separation of asphalt from mixtures with aggregates, fillers and other products, e.g. winning from natural asphalt and regeneration of waste asphalt

Abstract

This invention relates to the treatment of a multi-component material to separate and recover the components thereof, and more particularly to the solvent extraction or treatment of waste asphalt shingles to recover, in reusable form, the filler, fiber, granules and like solid components as well as asphalt therefrom.

Claims

1. A process for treating a solid waste material obtained in a process for manufacturing asphalt shingles and comprised of asphalt and solid components including filler and granules to recover asphalt and said components which comprise:

(a) shredding said solid waste material

(b) introducing said solid waste material into a contact zone;

(c) introducing extraction solvent streams of successively increasing solvent concentrations into said contact zone;

(d) intimately contacting said solid waste material with said extraction solvent for a time sufficient to dissolve said asphalt and form an asphalt-enriched miscella;

(e) separating said asphalt-enriched miscella from solid components; and

(f) separating and recovering by evaporation techniques asphalt and extraction solvent from said asphalt-enriched miscella.

2. The process as defined in claim 1, wherein said residual solid components are separated into filler and granules.

3. The process as defined in claim 1 wherein said extraction solvent is a fraction obtained in refining of petroleum.

4. The process as defined in claim 1 step (b), wherein each contact is effected for a time of from about 15 to 25 minutes.

5. The process as defined in claim 1 step (b), wherein said residual solid material is steamed prior to removal from said contact zone.

6. The process as defined in claim 1, wherein said extraction-solvent is returned to said contact zone.

7. The process as defined in claim 1 step (b), wherein asphalt-enriched miscella resulting from each contact step is passed to three successive storage zones.

8. The process as defined in claim 7, wherein the asphalt-enriched miscella from the first of said successive storage zones is continuously passed to said separation and recovery step of step (e).

9. The process as defined in claim 8 wherein a liquid bottoms including solid filler are withdrawn from each successive storage zone and wherein said liquid bottoms from the first and second storage zones are passed to said second and third storage zones, respectively, and wherein said liquid bottoms from said third storage zone is treated to recovery filler therefrom.

10. The process as defined in claim 9, wherein said filler is contacted with solvent vapors to remove adsorbed solvent prior to filler recovery.

11. The process as defined in claim 10, wherein filler separated from miscella is contacted with fresh extraction solvent.

12. The process as defined in claim 1, wherein said asphalt-enriched miscella is treated in a plurality of multiple evaporation steps to form an asphalt-enriched stream which is stripped to remove residual solvent prior to asphalt recovery.

13. The process as defined in claim 12, wherein the vapors from said multiple evaporation steps is contacted in a rectifying zone with extraction solvent to form a solvent stream which is returned to step (b).

14. The process as defined in claim 13, wherein a vapor stream withdrawn from said rectifying zone is contacted with subcooled condensate to reheat said subcooled condensate and desuperheat said vapor stream thereby to facilitate solvent water separation.