Method for electrochemical co2 decomposition

Patent metadata

Field	Value
Publication number	US-2025163588-A1
Application number	US-202318832824-A
Country	US
Kind code	A1
Filing date	Jan 30, 2023
Priority date	Jan 28, 2022
Publication date	May 22, 2025
Grant date	—

Abstract

A method for decomposing CO 2 into O 2 and solid C in an electrochemical reactor includes at least the following steps: i) introducing CO 2 into a cathode chamber containing at least one cathode fluid with electrical conductivity>5 mS/cm; ii) decomposing the CO2 in the cathode chamber by applying an electric field to the solid electrolyte, forming at least oxide ions (O 2− ), which are selectively transported through the solid electrolyte from the cathode chamber to an anode chamber, and solid carbon; iii) extracting, from the anode chamber, the O 2 produced on the anode from the ions transported in step ii); and iv) extracting, from the cathode chamber, the solid C formed in step ii).

First claim

1 . A method for decomposing CO 2 into solid C and O 2 in an electrochemical reactor, which comprises at least the following steps:
i) introducing CO 2 into a cathode chamber containing at least a cathode fluid with electrical conductivity>5 mS/cm; ii) decomposing the CO 2 in the cathode chamber by applying an electric field through a solid electrolyte, forming at least oxide ions (O 2− ), which are selectively transported through the solid electrolyte from the cathode chamber to an anode chamber, and solid carbon; iii) extracting, from the anode chamber, the O 2 produced on an anode from the ions transported in step ii; and iv) extracting, from the cathode chamber, the solid C formed in step ii.

2 . The method according to claim 1 , wherein the cathode fluid comprises at least a metal, a metal alloy or mixtures of two or more molten metals.

3 . The method according to claim 2 , wherein the metal of the cathode fluid is selected from Mg, Cr, Mn, Fe, Co, Ni, Cu, Zn, Mo, Ru, Rh, Ag, W, Pt, Au, Al, Ga, In, Sn, Pb, Sb, Bi, Te, Si, and combinations thereof.

4 . The method according to claim 3 , wherein the metal of the cathode fluid is pure Ag or an alloy containing Ag.

5 . The method according to claim 2 , wherein the cathode fluid further comprises molten metal cation salts below 10% by weight.

6 . The method according to claim 5 , wherein the molten salts are selected from oxides, carbonates, sulphates, nitrates, or combinations thereof.

7 . The method according to claim 1 , wherein the solid electrolyte that transports oxide ions is a ceramic solid.

8 . The method according to claim 7 , wherein the ceramic solid is composed of dense layers of multi-metal oxides including alkali metals, alkaline earth metals, rare earth elements, transition metals and combinations thereof.

9 . The method according to claim 8 , wherein the ceramic solid is a cerium or zirconium oxide with a fluorite-type structure and doped with yttrium, scandium or rare earth elements.

10 . The method according to claim 1 , wherein the electric field applied in step ii is applied using an electrode located in the anode chamber as an anode and an electrode selected from a cathode located in the cathode chamber and the cathode fluid as a cathode.

11 . The method according to claim 10 , wherein the electrode located in the anode chamber is an electrode composed of ceramic materials.

12 . The method according to claim 11 , wherein the anode is an electrode composed of at least one mixed oxide with a perovskite- type structure or mixtures thereof with particles of a material with ionic conductivity.

13 . The method according to claim 10 , wherein the electrode located in the cathode chamber is an electrode composed of metals selected from Ni, Pt, Pd, Cu, ceramic materials based on doped La and/or Sr chromites, doped La and/or Sr titanates, doped Sr molybdates and combinations thereof.

14 . The method wherein according to claim 13 , wherein the electrode located in the cathode chamber further comprises particles of a material with ionic conductivity.

15 . The method according to claim 1 , characterized in that least one of a cathode, the solid electrolyte or the anode has a flat or tubular geometry.

16 . The method according to claim 1 , wherein the solid C extracted in step iv is separated from the cathode fluid mechanically.

17 . The method according to claim 16 , wherein the mechanical process is selected between flotation, filtration, centrifugation, and recovery of the cathode fluid embedded in the solid C through thermal treatments at subatmospheric pressure or magnetically, or combinations thereof.

18 . The method according to claim 1 , wherein the CO 2 introduced in step i is introduced by a method selected between bubbling and adsorbed/absorbed on a solid.

19 . The method according to claim 18 , wherein CO 2 is introduced adsorbed/absorbed on a solid where said solid is porous and is selected from organic polymers, molecular sieves, solid organometallic materials, metal oxides and combinations thereof.

20 . The method according to claim 18 , wherein CO 2 is introduced adsorbed/absorbed on a solid and said solid is selected from activated carbon, activated carbon fibers, carbon nanotubes, graphene, graphene-based materials and combinations thereof.

21 . The method according to claim 1 , wherein the solid C extracted in step iv is used for the adsorption of CO 2 and is reintroduced into the process as a carrier of CO 2 in step i.

22 . The method according to claim 1 , wherein the operating temperature is between 400 and 1600° C.

23 . The method according to claim 1 , wherein the voltage of the electric field applied in step ii is between 0.5 and 4 V.

Assignees

• Consejo Superior Investigacion
• Univ Valencia Politecnica

Inventors

• Serra Alfaro José Manuel
• Siurana Paula Maria

Classifications

• C25B1/02 Primary

  Hydrogen or oxygen · CPC title

• C25B11/047

  Ceramics · CPC title

• C25B13/07

  based on ceramics · CPC title

• C25B15/083

  Separating products · CPC title

• C25B11/033

  Liquid electrodes · CPC title