IP Library › Granted Patent US 12,122,672
Granted Patent B2
US 12,122,672 · App. 17/966,513 · Granted Oct 22, 2024

Methods for preparing hydrogen and solid carbon from a gaseous hydrocarbon source using microwaves and/or radio waves

Inventors: Murray Thomson (Toronto, CA); Erin Bobicki (Edmonton, CA)
Assignee: AURORA HYDROGEN INC.
C01B3/24C01B32/05C10B19/00C10B57/16C01B2203/0272C01B2203/049C01B2203/06C01B2203/0855C01B2203/1241C01B2203/1604C01B2203/1614C01B2203/80
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Quick Facts
Patent No.
US 12,122,672
App. No.
17/966,513
Granted
Oct 22, 2024
Kind
B2
Abstract

Provided are methods for preparing hydrogen and solid carbon. Illustrative methods comprise providing a feedstock comprising gaseous hydrocarbons to a microwave-inert reaction vessel and/or a radio wave-inert reaction vessel. The reaction vessel has solid carbon, about 0% water and about 0% molecular oxygen inside the reaction vessel and the carbon inside the reaction vessel is operable to heat the feedstock comprising gaseous hydrocarbons. The carbon is then exposed to microwaves and/or radio waves until the solid carbon is at a temperature of at least 1200 Kelvin, thereby forming hydrogen and solid carbon. Once formed, the hydrogen and solid carbon are separated.

Claims (27)

1. A method for preparing hydrogen and solid carbon, the method comprising:

a) providing a reaction vessel so that the reaction vessel has 0 wt % water and 0 wt % molecular oxygen inside the reaction vessel;

b) providing a feedstock comprising gaseous hydrocarbons to the reaction vessel, the reaction vessel having a starting solid carbon, 0 wt % water and 0 wt % molecular oxygen inside the reaction vessel, and the starting solid carbon being operable to heat the feedstock comprising gaseous hydrocarbons;

c) exposing the starting solid carbon in the reaction vessel to microwaves until the starting solid carbon is at a temperature of at least 1200 Kelvin, wherein the starting solid carbon is the primary microwave susceptor;

d) breaking carbon-hydrogen bonds of the gaseous hydrocarbons of the feedstock by heat transfer between the starting solid carbon and the gaseous hydrocarbons, thereby forming hydrogen and a prepared solid carbon in the reaction vessel; and

e) separating the hydrogen and the prepared solid carbon,

wherein the reaction vessel is microwave inert; and

wherein the method is conducted in a single-reactor system, wherein the single reactor is the reaction vessel.

2. The method of claim 1 wherein the reaction vessel comprises microwave transparent materials.

3. The method of claim 1 wherein the reaction vessel comprises microwave reflective materials.

4. The method of claim 1 wherein the reaction vessel is made from quartz and a high temperature metal alloy.

5. The method of claim 1 wherein the feedstock is natural gas.

6. The method of claim 1 wherein the feedstock is a gaseous feedstock.

7. The method of claim 1 wherein the feedstock is substantially devoid of non-hydrocarbon gases.

8. The method of claim 1 wherein the feedstock contains 0 wt % of an inert gas.

9. The method of claim 1 wherein the feedstock consists essentially of gaseous hydrocarbons.

10. The method of claim 1 wherein the prepared solid carbon is solid carbon produced by pyrolysis of gaseous hydrocarbons.

11. The method of claim 1 wherein, after exposing the starting solid carbon in the reaction vessel to microwaves, the starting solid carbon is at a temperature in the range of from 1200 Kelvin to about 2000 Kelvin or the starting solid carbon and the prepared solid carbon is at a temperature range of from 1200 Kelvin to about 2000 Kelvin.

12. The method of claim 1 wherein, after exposing the starting solid carbon in the reaction vessel to microwaves, the starting solid carbon is at a temperature in the range of from about 1300 Kelvin to about 1900 Kelvin, or the starting solid carbon and the prepared solid carbon is at a temperature in the range of from about 1300 Kelvin to about 1900 Kelvin.

13. The method of claim 1 wherein, after exposing the starting solid carbon in the reaction vessel to microwaves, the starting solid carbon is at a temperature in the range of from about 1400 Kelvin to about 1800 Kelvin, or the starting solid carbon and the prepared solid carbon is at a temperature in the range of from about 1400 Kelvin to about 1800 Kelvin.

14. The method of claim 1 wherein, after exposing the starting solid carbon in the reaction vessel to microwaves, the starting solid carbon is at a temperature in the range of from about 1500 Kelvin to about 1700 Kelvin, or the starting solid carbon and the prepared solid carbon is at a temperature in the range of from about 1500 Kelvin to about 1700 Kelvin.

15. The method of claim 1 wherein, after exposing the starting solid carbon in the reaction vessel to microwaves, the starting solid carbon is at a temperature of about 1600 Kelvin, or the starting solid carbon and the prepared solid carbon is at a temperature of about 1600 Kelvin.

16. The method of claim 1 wherein the method does not use a catalyst.

17. The method of claim 1 wherein the hydrogen and the prepared solid carbon are produced in the absence of plasma formation by the microwaves.

18. The method of claim 1 wherein the starting solid carbon is free of metal impurities and oxygen-containing species.

19. The method of claim 1 wherein the hydrogen and the prepared solid carbon are formed without substantial formation of carbon monoxide.

20. The method of claim 1 wherein the feedstock has less than or equal to 2 wt % water.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 8, 2022
From: THOMSON, MURRAY; BOBICKI, ERIN
To: AURORA HYDROGEN INC.
Reel/Frame 061695/0430 →
Priority Claims (1)
SE 21505763 · May 6, 2021 · national
Continuity (2)
Continuation PCTCA2022050710 · May 6, 2022
Related Publication 20230202839A1 · Jun 29, 2023