Recovered carbon black obtained by solvolysing tyres
US-2025206955-A1 · Jun 26, 2025 · US
US9441113B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9441113-B2 |
| Application number | US-201313945239-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 18, 2013 |
| Priority date | Jul 18, 2013 |
| Publication date | Sep 13, 2016 |
| Grant date | Sep 13, 2016 |
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A method of recovering carbon black includes the step of providing a carbonaceous source material containing carbon black. The carbonaceous source material is contacted with a sulfonation bath to produce a sulfonated material. The sulfonated material is pyrolyzed to produce a carbon black containing product comprising a glassy carbon matrix phase having carbon black dispersed therein. A method of making a battery electrode is also disclosed.
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We claim: 1. A method of recovering carbon black, comprising the steps of: providing a carbonaceous source material containing carbon black; contacting the carbonaceous source material with a sulfonation bath to produce a sulfonated material, wherein the sulfonation bath comprises sulfonation agent is chlorosulfonic acid in 1,2 dichloroethane solution; and, pyrolyzing the sulfonated material to produce a carbon black containing product comprising a glassy carbon matrix phase having carbon black dispersed therein. 2. The method of claim 1 , wherein the sulfonation bath is an oleum bath. 3. The method of claim 1 , wherein the sulfonation bath comprises between 0.1-65 wt. % SO 3 . 4. The method of claim 1 , wherein pyrolysis step is conducted at a temperature that is greater than 1000° C. 5. The method of claim 1 , wherein pyrolysis step is conducted at a temperature that is between 200-1000° C. 6. The method of claim 1 , further comprising the steps of reducing the carbonaceous source material to a powder prior to contacting the carbonaceous source material with the oleum bath. 7. The method of claim 6 , wherein the powder has an average maximum dimension of less than 100 nm to 10 cm. 8. The method of claim 1 , wherein the carbonaceous source material comprises carbon reinforced composites. 9. The method of claim 8 , wherein the carbon reinforcing agent is at least one selected from the group consisting of carbon black, carbon particles, nanoparticles, mesoparticles and fibers. 10. The method of claim 1 , wherein the carbonaceous source material is a waste material. 11. The method of claim 10 , wherein the waste material is rubber tires. 12. The method of claim 1 , wherein the carbon black containing product has a specific surface area of less than 1000 m 2 /g. 13. The method of claim 1 , wherein the pyrolyzing step occurs after the contacting step. 14. The method of claim 1 , wherein the pyrolyzing step occurs before the contacting step. 15. A method of recovering carbon black, comprising the steps of: providing a carbonaceous source material containing carbon black; contacting the carbonaceous source material with a sulfonation bath to produce a sulfonated material, pyrolyzing the sulfonated material to produce a carbon black containing product comprising a glassy carbon matrix phase having carbon black dispersed therein; and wherein the carbon black product has an average pore size of less than 8 nm. 16. The method of claim 15 , wherein the sulfonation bath is an oleum bath. 17. The method of claim 15 , wherein the sulfonation bath comprises between 0.1-65 wt. % SO 3 . 18. The method of claim 15 , wherein pyrolysis step is conducted at a temperature that is greater than 1000° C. 19. The method of claim 15 , wherein pyrolysis step is conducted at a temperature that is between 200-1000° C. 20. The method of claim 15 , further comprising the steps of reducing the carbonaceous source material to a powder prior to contacting the carbonaceous source material with the oleum bath. 21. The method of claim 20 , wherein the powder has an average maximum dimension of less than 100 nm to 10 cm. 22. The method of claim 15 , wherein the carbonaceous source material comprises carbon reinforced composites. 23. The method of claim 22 , wherein the carbon reinforcing agent is at least one selected from the group consisting of carbon black, carbon particles, nanoparticles, mesoparticles and fibers. 24. The method of claim 15 , wherein the carbonaceous source material is a waste material. 25. The method of claim 24 , wherein the waste material is rubber tires. 26. The method of claim 15 , wherein the carbon black containing product has a specific surface area of less than 1000 m 2 /g. 27. The method of claim 15 , wherein the pyrolyzing step occurs after the contacting step. 28. The method of claim 15 , wherein the pyrolyzing step occurs before the contacting step. 29. A method of recovering carbon black, comprising the steps of: providing a carbonaceous source material containing carbon black; contacting the carbonaceous source material with a sulfonation bath to produce a sulfonated material, pyrolyzing the sulfonated material to produce a carbon black containing product comprising a glassy carbon matrix phase having carbon black dispersed therein; and wherein the carbon black product has an average pore size of between 2 and 120 nm. 30. The method of claim 29 , wherein the sulfonation bath is an oleum bath. 31. The method of claim 29 , wherein the sulfonation bath comprises between 0.1-65 wt. % SO 3 . 32. The method of claim 29 , wherein pyrolysis step is conducted at a temperature that is greater than 1000° C. 33. The method of claim 29 , wherein pyrolysis step is conducted at a temperature that is between 200-1000° C. 34. The method of claim 29 , further comprising the steps of reducing the carbonaceous source material to a powder prior to contacting the carbonaceous source material with the oleum bath. 35. The method of claim 34 , wherein the powder has an average maximum dimension of less than 100 nm to 10 cm. 36. The method of claim 29 , wherein the carbonaceous source material comprises carbon reinforced composites. 37. The method of claim 36 , wherein the carbon reinforcing agent is at least one selected from the group consisting of carbon black, carbon particles, nanoparticles, mesoparticles and fibers. 38. The method of claim 29 , wherein the carbonaceous source material is a waste material. 39. The method of claim 38 , wherein the waste material is rubber tires. 40. The method of claim 29 , wherein the carbon black containing product has a specific surface area of less than 1000 m 2 /g. 41. The method of claim 29 , wherein the pyrolyzing step occurs after the contacting step. 42. The method of claim 29 , wherein the pyrolyzing step occurs before the contacting step. 43. A method of recovering carbon black, comprising the steps of: providing a carbonaceous source material containing carbon black; contacting the carbonaceous source material with a sulfonation bath to produce a sulfonated material, pyrolyzing the sulfonated material to produce a carbon black containing product comprising a glassy carbon matrix phase having carbon black dispersed therein; and wherein the carbon black product is further surface activated and the carbon black product has an average pore size between 1 and 20 nm and a density of pores having an average pore size between 1 and 20 nm is increased. 44. The method of claim 43 , wherein the sulfonation bath is an oleum bath. 45. The method of claim 43 , wherein the sulfonation bath comprises between 0.1-65 wt. % SO 3 . 46. The method of claim 43 , wherein pyrolysis step is conducted at a temperature that is greater than 1000° C. 47. The method of claim 43 , wherein pyrolysis step is conducted at a temperature that is between 200-1000° C. 48. The method of claim 43 , further comprising the steps of reducing the carbonaceous
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