Negative emission, large scale carbon capture for clean fossil fuel power generation

Patent metadata

Field	Value
Publication number	US-11613817-B2
Application number	US-202217889120-A
Country	US
Kind code	B2
Filing date	Aug 16, 2022
Priority date	Aug 18, 2021
Publication date	Mar 28, 2023
Grant date	Mar 28, 2023

Abstract

Systems and methods for eliminating carbon dioxide and capturing solid carbon are disclosed. By eliminating carbon dioxide gas, e.g., from an effluent exhaust stream of a fossil fuel fired electric power production facility, the inventive concepts presented herein represent an environmentally-clean solution that permanently eliminates greenhouse gases while at the same time producing captured solid carbon products that are useful in various applications including advanced composite material synthesis (e.g., carbon fiber, 3D graphene) and energy storage (e.g., battery technology). Capture of solid carbon during the disclosed process for eliminating greenhouse gasses avoids the inefficiencies and risks associated with conventional carbon dioxide sequestration. Colocation of the disclosed reactor with a fossil fuel fired power production facility brings to bear an environmentally beneficial, and financially viable approach for permanently capturing vast amounts of solid carbon from carbon dioxide gas and other greenhouse gases that would otherwise be released into Earth's biosphere.

First claim

What is claimed is:

1. A method for producing solid carbon from carbon dioxide gas and water, the method comprising:
receiving carbon dioxide and water in a reactor configured to generate a plasma;
dissociating the carbon dioxide and the water using the plasma to form one or more dissociated species;
exposing the dissociated species to an electric field configured to facilitate one or more chemical reactions, wherein the electric field comprises a pulsed direct current (DC) field;
generating solid carbon via the chemical reactions; and
outputting the solid carbon from the reactor.

2. The method as recited in claim 1 , comprising separating the solid carbon from one or more byproducts of dissociating the carbon dioxide and the water, and/or from one or more byproducts of the one or more chemical reactions.

3. The method as recited in claim 1 , wherein facilitating the chemical reactions using the electric field comprises modulating a frequency and/or a duty cycle of a control signal generated by a control circuit coupled to the reactor.

4. The method as recited in claim 1 , wherein the chemical reactions include:
a first reaction configured to generate solid carbon from carbon monoxide and water in a single step; and
a second reaction configured to generate solid carbon from carbon monoxide and water in two steps.

5. The method as recited in claim 1 , wherein the carbon dioxide and the water are components of an effluent exhaust stream received from a power generation facility coupled to the reactor.

6. The method as recited in claim 5 , wherein generating the solid carbon reduces a carbon footprint of the power generation facility.

7. The method as recited in claim 1 , wherein the plasma is characterized by an energy of approximately 100 electron volts (eV).

8. The method as recited in claim 1 , wherein the plasma is characterized by a frequency in a range from about one gigahertz to about five gigahertz.

9. The method as recited in claim 1 , wherein the solid carbon comprises one or more materials selected from the group consisting of: carbon black, carbon nano-onions (CNOs), necked CNOs, carbon nanospheres, graphite, pyrolytic graphite, graphene, graphene nanoparticles, graphene platelets, fullerenes, hybrid fullerenes, single-walled nanotubes, and multi-walled nanotubes.

10. The method as recited in claim 1 , comprising removing oxygen from the reactor.

11. The method as recited in claim 1 , comprising: generating the electric field using a plurality of electrodes coupled to the reactor, wherein the plurality of electrodes are configured, via being positioned at an angle relative to a principal dimension of a reaction zone in which the plasma is generated, to generate variations in a strength of the electric field within the reaction zone.

12. The method as recited in claim 11 , wherein at least two of the plurality of electrodes are characterized by an approximately 180-degree phase difference;
wherein the at least two of the plurality of electrodes are positioned on opposing sides of the reaction zone and substantially aligned with each other along the principal dimension of the reaction zone.

13. The method as recited in claim 1 , wherein the electric field is characterized by a variable strength along a length of a reaction zone of the reactor.

14. The method as recited in claim 1 , wherein the electric field further comprises an alternating current (AC) field.

15. The method as recited in claim 1 , wherein the dissociating is driven by electron(s) impacting the carbon dioxide and the water; and wherein the electron(s) are characterized by a kinetic energy in a range from about 28 electron volts (eV) to about 100 eV.

16. The method as recited in claim 1 , comprising controlling temperatures within an extended length plasma zone of the reactor and/or an extended length afterglow zone of the reactor using the pulsed DC field and/or an alternating current (AC) field.

17. The method as recited in claim 1 , comprising controlling temperature contours within a plasma zone of the reactor using one or more thermal plume energy sources.

18. The method as recited in claim 17 , wherein the one or more thermal plume energy sources are selected from the group consisting of: an ohmic heating device, a dielectric heating device, an electromagnetic energy source, a phonon heating device, a light energy source, and combinations thereof.

19. The method as recited in claim 1 , wherein the plasma comprises a plurality of electrons characterized by a kinetic energy of approximately 100 electron volts (eV);
wherein the dissociated species are formed by impacting at least some of the electrons with the received carbon dioxide and the received water; and
wherein the chemical reactions comprise:
a first reaction configured to generate the solid carbon (C (s) ) by reacting carbon monoxide (CO) formed within the plasma with dissociated water (H 2 O + ) formed within the plasma, in a single step; and
a second reaction configured to generate the solid carbon (C (s) ) in two steps;

wherein a first step of the second reaction comprises reacting carbon monoxide (CO) formed within the plasma with dissociated hydroxyl (OH + ) formed within the plasma to form carbon dioxide (CO 2 ) and hydrogen (H); and
wherein a second step of the second reaction comprises reducing carbon monoxide (CO) formed within the plasma with the hydrogen (H) formed within the plasma to form the solid carbon (C (s) ) and water (H 2 O).

20. The method as recited in claim 1 , wherein the solid carbon comprises graphene;
wherein the method comprises functionalizing one or more surfaces of the graphene with one or more functional groups; and
wherein the one or more functional groups comprise: fluorine, oxygen, nitrogen, or combinations thereof.

Assignees

• Lyten Inc

Inventors

• Stowell Michael W
• Sienko Lauren

Classifications

• B01J2219/0884

  Gas-liquid · CPC title

• B01J2219/0809

  employing two or more electrodes · CPC title

• B01J19/088

  giving rise to electric discharges (for heating purposes H05B7/00; for the production of ozone C01B13/11, H01T19/00) · CPC title

• C01B32/40

  Carbon monoxide · CPC title

• C01B32/184 Primary

  Preparation · CPC title