IP Library › Granted Patent US 10,112,837
Granted Patent B2
US 10,112,837 · App. 15/794,965 · Granted Oct 30, 2018

Carbon allotropes

Inventors: Daniel Cook (Woodside, CA); Hossein-Ali Ghezelbash (Santa Clara, CA); Bryce H. Anzelmo (Mountain View, CA); David Tanner (San Jose, CA); Shreeyukta Singh (Sunnyvale, CA)
Assignee: Lyten, Inc.
C01B32/152B22F1/0025B82Y30/00B82Y40/00C01B32/182C08J5/005C22C1/058G01N21/65C07C2604/00
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Quick Facts
Patent No.
US 10,112,837
App. No.
15/794,965
Granted
Oct 30, 2018
Kind
B2
Abstract

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.

Claims (45)

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.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 26, 2017
From: COOK, DANIEL; GHEZELBASH, HOSSEIN-ALI; ANZELMO, BRYCE H.; TANNER, DAVID; SINGH, SHREEYUKTA
To: LYTEN, INC.
Reel/Frame 043963/0072 →
Continuity (3)
Continuation 15594032 · May 12, 2017
Continuation In Part 15470450 · Mar 27, 2017
Related Publication 20180273386A1 · Sep 27, 2018