IP Library Granted Patent US 10,683,620
Granted Patent B1
US 10,683,620 · App. 16/789,219 · Granted Jun 16, 2020

Methods of forming an asphalt shingle waste powder from asphalt shingle waste

Inventors: Dale Kelley (Flower Mound, TX); James Svec (Kearney, NJ); Michael T. Ferraro (Savannah, GA); Kirby Erickson (Waxahachie, TX); Paul Richardson (Euless, TX); Kris Edelsward (Lockport, NY)
Assignee: Building Materials Investment Corporation
E01C19/05B02C19/0056B02C23/08C08L95/00E01C19/1004C08L2555/34
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Quick Facts
Patent No.
US 10,683,620
App. No.
16/789,219
Granted
Jun 16, 2020
Kind
B1
Abstract

Non-limiting embodiments of the present disclosure relate to a method comprising: obtaining asphalt shingle waste (ASW) and performing grinding, screening, and separating steps on the ASW. In some embodiments, granules are removed from the ASW. In some embodiments, the method transforms ASW into ASW powder. In some embodiments, the ASW powder is formed into a plurality of briquettes. In some embodiments, at least one of: the ASW powder, the plurality of briquettes, or any combination thereof is fed into a mixing process that results in an ASW powder filled coating.

Claims (174)

1. A method comprising:

obtaining asphalt shingle waste (ASW),

wherein the ASW comprises:

asphalt,

limestone,

granules, and

impurities;

grinding the ASW to form ground ASW;

screening the ground ASW with a rotary screener,

wherein the screening of the ground ASW with the rotary screener results in:

a first set of ASW particles,

wherein the first set of ASW particles has an average particle size of 425 microns to 6350 microns, and

a second set of ASW particles,

wherein the second set of ASW particles has an average particle size of 2 microns to 425 microns;

removing at least some of the granules from at least one of: the first set of ASW particles, the second set of ASW particles, or a combination thereof with a granule liberator;

grinding the first set of ASW particles,

wherein the grinding of the first set of ASW particles results in a third set of ASW particles,

wherein the third set of ASW particles has an average particle size of 2 microns to 425 microns;

separating the second and third sets of ASW particles using an air separator,

wherein the separating using the air separator results in:

a fourth set of ASW particles,

wherein the fourth set of ASW particles have an average particle size of 250 microns to 450 microns; and

a fifth set of ASW particles,

wherein the fifth set of ASW particles have an average particle size of 2 microns to 250 microns;

grinding the fourth set of ASW particles;

wherein the grinding of the fourth set of ASW particles results in a sixth set of ASW particles,

wherein the sixth set of ASW particles have an average particle size of 2 microns to 250 microns;

wherein each of the fifth set of ASW particles and the sixth set of ASW particles is an ASW powder having the following composition:

5 wt % to 40 wt % asphalt based on a total weight of the ASW powder, and

60 wt % to 95 wt % of limestone, granules, and

impurities based on the total weight of the ASW powder,

wherein the method does not comprise a wet extraction step.

2. The method of claim 1 , wherein the rotary screener is a trommel screener.

3. The method of claim 1 , wherein the method does not comprise a grinding step after the step of grinding the fourth set of ASW particles.

4. The method of claim 1 , wherein the method does not comprise any grinding steps other than the steps of: grinding the ASW, grinding the first set of ASW particles and grinding the fourth set of ASW particles.

5. The method of claim 1 , wherein the impurities comprise least one of: fiberglass mat sand, fines, marker paint, sealant, one or more adhesives, tape, plastic debris, paper debris, soil, woods, nails, or any combination thereof.

6. The method of claim 1 , wherein the method does not comprise any steps of screening with a vibratory screener.

7. The method of claim 1 , wherein the method does not comprise any steps of screening with a screening device that comprises at least one ball tray.

8. The method of claim 1 , wherein the method does not comprise any steps of screening with a sizing shaker.

9. The method of claim 1 , wherein the method does not comprise a screening step after the step of separating the second and third sets of ASW particles using the air separator.

10. The method of claim 1 , wherein the second and third sets of ASW particles are combined prior to the step of separating the second and third sets of ASW particles using the air separator.

11. The method of claim 1 , wherein the fifth set of ASW particles and the sixth set of ASW particles are combined to form the ASW powder.

12. The method of claim 1 , wherein the method further comprises forming the ASW powder into a plurality of briquettes.

13. The method of claim 12 , wherein forming the ASW powder into the plurality of briquettes comprises adding limestone powder to the ASW powder.

14. The method of claim 12 , wherein the forming the ASW powder into the plurality of briquettes comprises compressing the ASW powder at a pressure sufficient to form the plurality of briquettes.

15. The method of claim 14 , wherein the pressure sufficient to form the plurality of briquettes ranges from 200 psi to 20,000 psi.

16. The method of claim 12 , wherein each briquette of the plurality of briquettes is an oblate spheroid.

17. The method of claim 16 , wherein each briquette of the plurality of briquettes has a first diameter and a second diameter, wherein at least one of: the first diameter, the second diameter or any combination thereof ranges from 0.5 inches to 2 inches.

18. The method of claim 1 , wherein the at least one granule liberator comprises a rotary impact separator.

19. The method of claim 1 , wherein the method further comprises using a scalping screen to separate particles having an average particle size of 4 microns to 425 microns from the ground ASW.

20. The method of claim 19 , wherein the step of using the scalping screen is performed between the steps of: grinding the ASW and screening the ground ASW.

21. The method of claim 1 , wherein the method comprises deagglomerating the ground ASW using a lump breaker.

22. The method of claim 21 , wherein the step of deagglomerating the ground ASW is performed between the steps of: grinding the ASW and screening the ground ASW.

23. A method comprising:

obtaining asphalt shingle waste (ASW),

wherein the ASW comprises:

asphalt,

limestone,

granules, and

impurities;

grinding the ASW to form ground ASW;

screening the ground ASW with a rotary screener,

wherein the screening of the ground ASW with the rotary screener results in:

a first set of ASW particles,

wherein the first set of ASW particles has an average particle size of 425 microns to 6350 microns, and

a second set of ASW particles,

wherein the second set of ASW particles has an average particle size of 2 microns to 425 microns;

removing at least some of the granules from at least one of: the first set of ASW particles, the second set of ASW particles, or a combination thereof with a granule liberator;

grinding the first set of ASW particles,

wherein the grinding of the first set of ASW particles results in a third set of ASW particles,

wherein the third set of ASW particles has an average particle size of 2 microns to 425 microns;

separating the second and third sets of ASW particles using an air separator,

wherein the separating using the air separator results in:

a fourth set of ASW particles,

wherein the fourth set of ASW particles have an average particle size of 250 microns to 450 microns; and

a fifth set of ASW particles,

wherein the fifth set of ASW particles have an average particle size of 2 microns to 250 microns;

grinding the fourth set of ASW particles;

wherein the grinding of the fourth set of ASW particles results in a sixth set of ASW particles,

wherein the sixth set of ASW particles have an average particle size of 2 microns to 250 microns;

wherein each of the fifth set of ASW particles and the sixth set of ASW particles is an ASW powder having the following composition:

5 wt % to 40 wt % asphalt based on a total weight of the ASW powder, and

60 wt % to 95 wt % of limestone, granules, and impurities based on the total weight of the ASW powder,

forming the ASW powder into the plurality of briquettes;

wherein the method does not comprise a wet extraction step.

24. The method of claim 23 , wherein forming the ASW powder into the plurality of briquettes comprises adding limestone powder to the ASW powder.

25. The method of claim 23 , wherein the forming the ASW powder into the plurality of briquettes comprises compressing the ASW powder at a pressure sufficient to form the plurality of briquettes.

26. A method comprising:

obtaining asphalt shingle waste (ASW),

wherein the ASW comprises:

asphalt,

limestone,

granules, and

impurities;

grinding the ASW to form ground ASW;

screening the ground ASW with a rotary screener,

wherein the screening of the ground ASW with the rotary screener results in:

a first set of ASW particles,

wherein the first set of ASW particles has an average particle size of 425 microns to 6350 microns, and

a second set of ASW particles,

wherein the second set of ASW particles has an average particle size of 2 microns to 425 microns;

removing at least some of the granules from at least one of: the first set of ASW particles, the second set of ASW particles, or a combination thereof with a granule liberator;

grinding the first set of ASW particles,

wherein the grinding of the first set of ASW particles results in a third set of ASW particles,

wherein the third set of ASW particles has an average particle size of 2 microns to 425 microns;

separating the second and third sets of ASW particles using an air separator,

wherein the separating using the air separator results in:

a fourth set of ASW particles,

wherein the fourth set of ASW particles have an average particle size of 250 microns to 450 microns; and

a fifth set of ASW particles,

wherein the fifth set of ASW particles have an average particle size of 2 microns to 250 microns;

grinding the fourth set of ASW particles;

wherein the grinding of the fourth set of ASW particles results in a sixth set of ASW particles,

wherein the sixth set of ASW particles has an average particle size of 2 microns to 250 microns;

wherein at least one of: the second set of ASW particles, the third set of ASW particles, the fourth set of ASW particles, the fifth set of ASW particles, the sixth set of ASW particles or any combination thereof comprises an ASW powder having the following composition:

5 wt % to 40 wt % asphalt based on a total weight of the ASW powder, and

60 wt % to 95 wt % of limestone, granules, and impurities based on the total weight of the ASW powder,

obtaining the ASW powder from at least one of: the second set of ASW particles, the third set of ASW particles, the fourth set of ASW particles, the fifth set of ASW particles, the sixth set of ASW particles, or any combination thereof,

wherein the ASW powder has an average particle size of 2 microns to 425 microns;

feeding a sufficient amount of the ASW powder and a sufficient amount of an asphalt coating into at least one first mixer to form a mixture of the ASW powder and the asphalt coating;

wherein the mixture of the ASW powder and the asphalt coating has the following composition:

0.1 wt % to 50 wt % ASW powder based on a total weight of the mixture, and

50 wt % to 99.9 wt % of the asphalt coating based on a total weight of the mixture;

heating the mixture of the ASW powder and the asphalt coating to form a heated mixture;

wherein the heated mixture has a temperature in a range of 400° F. to 500° F.;

conveying the heated mixture of the ASW powder and the asphalt coating to at least one second mixer;

mixing a sufficient amount of at least one filler material with the heated mixture in the second mixer to obtain an ASW powder filled coating;

wherein the ASW powder filled coating has the following composition:

30 wt % to 50 wt % asphalt based on the total weight of the ASW powder filled coating, and

50 wt % to 70 wt % of: limestone powder, granules, impurities, and the at least one filler material based on the total weight of the ASW powder filled coating.

27. A method comprising:

obtaining asphalt shingle waste (ASW),

wherein the ASW comprises:

asphalt,

limestone,

granules, and

impurities;

grinding the ASW to form ground ASW;

screening the ground ASW with a rotary screener,

wherein the screening of the ground ASW with the rotary screener results in:

a first set of ASW particles,

wherein the first set of ASW particles has an average particle size of 425 microns to 6350 microns, and

a second set of ASW particles,

wherein the second set of ASW particles has an average particle size of 2 microns to 425 microns;

removing at least some of the granules from at least one of: the first set of ASW particles, the second set of ASW particles, or a combination thereof with a granule liberator;

grinding the first set of ASW particles,

wherein the grinding of the first set of ASW particles results in a third set of ASW particles,

wherein the third set of ASW particles has an average particle size of 2 microns to 425 microns;

separating the second and third sets of ASW particles using an air separator,

wherein the separating using the air separator results in:

a fourth set of ASW particles,

wherein the fourth set of ASW particles have an average particle size of 250 microns to 450 microns; and

a fifth set of ASW particles,

wherein the fifth set of ASW particles have an average particle size of 2 microns to 250 microns;

grinding the fourth set of ASW particles;

wherein the grinding of the fourth set of ASW particles results in a sixth set of ASW particles,

wherein the sixth set of ASW particles has an average particle size of 2 microns to 250 microns;

wherein at least one of: the second set of ASW particles, the third set of ASW particles, the fourth set of ASW particles, the fifth set of ASW particles, the sixth set of ASW particles or any combination thereof comprises an ASW powder having the following composition:

5 wt % to 40 wt % asphalt based on a total weight of the ASW powder, and

60 wt % to 95 wt % of limestone, granules, and impurities based on the total weight of the ASW powder,

obtaining the ASW powder from at least one of: the second set of ASW particles, the third set of ASW particles, the fourth set of ASW particles, the fifth set of ASW particles, the sixth set of ASW particles, or any combination thereof,

wherein the ASW powder has an average particle size of 2 microns to 425 microns;

forming the ASW powder into a plurality of briquettes;

feeding a sufficient amount of the plurality of briquettes and a sufficient amount of an asphalt coating into at least one first mixer to form a mixture of the ASW powder and the asphalt coating;

wherein the mixture of the ASW powder and the asphalt coating has the following composition:

0.1 wt % to 50 wt % ASW powder based on a total weight of the mixture, and

50 wt % to 99.9 wt % of the asphalt coating based on a total weight of the mixture;

heating the mixture of the ASW powder and the asphalt coating to form a heated mixture;

wherein the heated mixture has a temperature in a range of 400° F. to 500° F.;

conveying the heated mixture of the ASW powder and the asphalt coating to at least one second mixer;

mixing a sufficient amount of at least one filler material with the heated mixture in the second mixer to obtain an ASW powder filled coating;

wherein the ASW powder filled coating has the following composition:

30 wt % to 50 wt % asphalt based on the total weight of the ASW powder filled coating, and

50 wt % to 70 wt % of: limestone powder, granules, impurities, and the at least one filler material based on the total weight of the ASW powder filled coating.

Assignments (4)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 28, 2024
From: BMIC LLC
To: BMRC LLC
Reel/Frame 066593/0512 →
SECURITY INTEREST Recorded Sep 23, 2021
From: BMIC LLC; ELKCORP; ELK COMPOSITE BUILDING PRODUCTS, INC.; ELK PREMIUM BUILDING PRODUCTS, INC.; HBP ACQUISITION LLC; GAF ENERGY LLC; SIPLAST, INC.; SPECIALTY GRANULES INVESTMENTS LLC
To: DEUTSCHE BANK AG NEW YORK BRANCH
Reel/Frame 057572/0607 →
CHANGE OF NAME Recorded Aug 24, 2021
From: BUILDING MATERIALS INVESTMENT CORPORATION
To: BMIC LLC
Reel/Frame 057292/0184 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 3, 2020
From: KELLEY, DALE; SVEC, JAMES; FERRARO, MICHAEL T.; ERICKSON, KIRBY; RICHARDSON, PAUL; EDELSWARD, KRIS
To: BUILDING MATERIALS INVESTMENT CORPORATION
Reel/Frame 052303/0431 →
Cited By (8)
US 1,088,283 US 12,214,358 US 12,305,396 US 12,391,883 US 12,571,213 US 12,607,013 US 12,617,972 US 12,624,184