IP Library › Granted Patent US 11,926,743
Granted Patent B2
US 11,926,743 · App. 16/563,008 · Granted Mar 12, 2024

Systems and methods of making carbon particles with thermal transfer gas

Inventors: Peter L. Johnson (Mountain View, CA); Alexander F. Hoermann (Menlo Park, CA)
Assignee: MONOLITH MATERIALS, INC.
C09C1/50C01B3/24C01B32/05C01B2203/0272C01B2203/085C01B2203/1235C01P2006/12
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Quick Facts
Patent No.
US 11,926,743
App. No.
16/563,008
Granted
Mar 12, 2024
Kind
B2
Abstract

Systems and methods of making carbon particles with thermal transfer gas. A method of making carbon particles may comprise heating a thermal transfer gas by Joule heating and contacting the thermal transfer gas with a reactive hydrocarbon feedstock gas to generate the carbon particles and hydrogen gas. A method of making carbon particles may comprise heating a thermal transfer gas with the aid of Joule heating and mixing the thermal transfer gas with a hydrocarbon feedstock gas to generate the carbon particles.

Claims (23)

1. A method of making carbon particles, comprising:

(a) preheating a thermal transfer gas by resistive heating, thereby obtaining a preheated thermal transfer gas;

(b) in a reactor, heating the preheated thermal transfer gas with a plasma heater, thereby obtaining a heated thermal transfer gas; and

(c) in the reactor, contacting the heated thermal transfer gas with a hydrocarbon feedstock to generate the carbon particles and hydrogen gas.

2. The method of claim 1 , wherein the resistive heating comprises using one or more resistive heating elements selected from the group consisting of graphite, tungsten, molybdenum, rhenium, boron nitride, nickel, chromium, iron, and alloys thereof.

3. The method of claim 1 , further comprising: (d) supplying greater than or equal to about 750 kW of power to one or more resistive heating elements that provide the resistive heating.

4. The method of claim 1 , wherein the contacting is at (i) a thermal transfer gas flowrate greater than or equal to about 500 Nm 3 /hr (normal cubic meter/hour), or (ii) a hydrocarbon feedstock flowrate greater than or equal to about 675 Nm 3 /hr.

5. The method of claim 1 , wherein the hydrocarbon feedstock comprises (i) at least about 70% by weight methane, ethane, propane, or mixtures thereof, or (ii) one or more aromatic hydrocarbons, one or more unsaturated hydrocarbons, one or more oxygenated hydrocarbons, or any combination thereof.

6. The method of claim 1 , wherein the hydrocarbon feedstock comprises methane, ethane, propane, butane, benzene, toluene, xylene, methyl naphthalene, pyrolysis fuel oil, coal tar, coal, heavy oil, oil, bio-oil, bio-diesel, biologically derived hydrocarbon, ethylene, acetylene, butadiene, styrene, ethanol, methanol, propanol, phenol, ketones, ethers, esters, or any combination thereof.

7. The method of claim 1 , wherein more than about 90% of the hydrocarbon feedstock is converted into carbon particles on a weight percent carbon basis.

8. The method of claim 1 , wherein (i) the hydrocarbon feedstock is pre-heated from a first temperature to a second temperature before coming into contact with the heated thermal transfer gas, and wherein the second temperature is between about 100° C. and about 800° C., or (ii) the thermal transfer gas is heated via a heat exchanger prior to the resistive heating.

9. The method of claim 1 , wherein the thermal transfer gas comprises.

10. The method of claim 9 , wherein the thermal transfer gas comprises greater than about 60% hydrogen.

11. The method of claim 1 , wherein more than about 60% of the heat contained in the heated thermal transfer gas is transferred to the hydrocarbon feedstock within about 2 seconds of initial exposure to the heated thermal transfer gas.

12. A method of making carbon particles, comprising:

(a) preheating a thermal transfer gas with aid of resistive heating, thereby obtaining a preheated thermal transfer gas;

(b) in a reactor, heating the preheated thermal transfer gas with a plasma heater, thereby obtaining a heated thermal transfer gas; and

(c) in the reactor, mixing the heated thermal transfer gas with a hydrocarbon feedstock to generate the carbon particles.

13. The method of claim 12 , further comprising, in (c), mixing the heated thermal transfer gas with the hydrocarbon feedstock downstream of the resistive heating.

14. The method of claim 12 , wherein the carbon particles comprise carbon black.

15. The method of claim 14 , wherein the carbon black has a surface area greater than about 20 square meters per gram (m 2 /g).

16. The method of claim 12 , further comprising (i) in the reactor, heating the preheated thermal transfer gas to at least about 2,000° C., (ii) heating the preheated thermal transfer gas in an oxygen free environment, or (iii) a combination thereof.

17. The method of claim 12 , further comprising further heating the preheated thermal transfer gas with aid of an electric arc based plasma heating downstream of the resistive heating.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 25, 2021
From: JOHNSON, PETER L.; TAYLOR, ROSCOE W.; HOERMANN, ALEXANDER F.; MESROBIAN, CHRISTOPHER E.; NOEL, BRIAN T.; MOSS, JOHN JARED
To: MONOLITH MATERIALS, INC.
Reel/Frame 056349/0156 →
Continuity (3)
Continuation PCTUS2018021627 · Mar 8, 2018
Provisional Application 62468824 · Mar 8, 2017
Related Publication 20200239696A1 · Jul 30, 2020
Cited By (3)
US 12,286,540 US 12,497,517 US 12,668,702