Cracking of a process gas
US-9862602-B1 · Jan 9, 2018 · US
US10112837B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10112837-B2 |
| Application number | US-201715794965-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 26, 2017 |
| Priority date | Mar 27, 2017 |
| Publication date | Oct 30, 2018 |
| Grant date | Oct 30, 2018 |
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A nanoparticle or agglomerate which contains connected multi-walled spherical fullerenes coated in layers of graphite. In different embodiments, the nanoparticles and agglomerates have different combinations of: a high mass fraction compared to other carbon allotropes present, a low concentration of defects, a low concentration of elemental impurities, a high Brunauer, Emmett and Teller (BET) specific surface area, and/or a high electrical conductivity. Methods are provided to produce the nanoparticles and agglomerates at a high production rate without using catalysts.
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What is claimed is: 1. A carbon aggregate comprising: at least two connected multi-walled spherical fullerenes; and layers of graphene coating the connected multi-walled spherical fullerenes. 2. The carbon aggregate of claim 1 , wherein: a ratio of carbon to other elements, except H, in the carbon aggregate is greater than 99.9%. 3. The carbon aggregate of claim 1 , wherein: a Raman spectrum of the carbon aggregate using 532 nm incident light has a first Raman peak at approximately 1350 cm −1 and a second Raman peak at approximately 1580 cm −1 ; and a ratio of an intensity of the first Raman peak to an intensity of the second Raman peak is from 0.9 to 1.1. 4. The carbon aggregate of claim 1 , wherein: the multi-walled spherical fullerenes do not comprise a seed particle or a void at the center of the multi-walled spherical fullerenes. 5. The carbon aggregate of claim 1 , wherein: a diameter across the carbon aggregate is from 10 microns to 500 microns. 6. The carbon aggregate of claim 1 , wherein: the ratio of graphene to multi-walled spherical fullerenes in the carbon aggregate is from 10% to 80%. 7. The carbon aggregate of claim 1 , wherein: a Brunauer, Emmett and Teller (BET) specific surface area of the carbon aggregate is from 10 m 2 /g to 200 m 2 /g. 8. The carbon aggregate of claim 1 , wherein: a plurality of the carbon aggregates are compressed into a pellet, and the pellet has an electrical conductivity from 500 S/m to 20000 S/m. 9. A mixture comprising a liquid and a plurality of the carbon aggregates of claim 1 . 10. An ink comprising a plurality of the carbon aggregates of claim 1 , wherein the ink is a conductive ink. 11. A method comprising: flowing a hydrocarbon feedstock process gas into a reaction zone; thermally cracking molecules of the feedstock process gas in the reaction zone; reacting the thermally cracked molecules to form carbon aggregates, each comprising at least two connected multi-walled spherical fullerenes coated in layers of graphene; and collecting the carbon aggregates. 12. The method of claim 11 , wherein: a ratio of carbon to other elements, except H, in the carbon aggregates is greater than 99.9%. 13. The method of claim 11 , wherein: a Raman spectrum of the carbon aggregates using 532 nm incident light has a first Raman peak at about 1350 cm −1 and a second Raman peak at about 1580 cm −1 , and a ratio of an intensity of the first Raman peak to an intensity of the second Raman peak is from 0.9 to 1.1. 14. The method of claim 11 , wherein: the multi-walled spherical fullerenes do not comprise a seed particle or a void at the center of the multi-walled spherical fullerenes. 15. The method of claim 11 , wherein: an average diameter across the carbon aggregates is from 10 microns to 500 microns. 16. The method of claim 11 , wherein: a ratio of graphene to multi-walled spherical fullerenes is from 10% to 80%. 17. The method of claim 11 , wherein: a Brunauer, Emmett and Teller (BET) specific surface area of the carbon aggregates is from 10 m 2 /g to 200 m 2 /g. 18. The method of claim 11 , further comprising: compressing the carbon aggregates into a pellet, wherein the pellet has an electrical conductivity from 500 S/m to 20000 S/m. 19. The method of claim 11 , further comprising: the flow rate of the hydrocarbon feedstock process gas is from 1 slm to 10 slm; and the carbon aggregates are formed at a production rate from 10 g/hr to 200 g/hr. 20. The method of claim 11 , further comprising: post-processing the collected carbon aggregates using a method selected from group consisting of milling, grinding, exfoliating, annealing, sintering, steaming, filtering, lypolizing, doping, and adding elements.
Nanofibres or nanotubes · CPC title
Surface area · CPC title
Submicrometer sized, i.e. from 0.1-1 micrometer · CPC title
Preparation · CPC title
by IR- or Raman-data · CPC title
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