Filter-press photoelectrochemical water oxidation and CO2 reduction cell

Patent metadata

Field	Value
Publication number	US-10626510-B2
Application number	US-201515537046-A
Country	US
Kind code	B2
Filing date	Dec 18, 2015
Priority date	Dec 19, 2014
Publication date	Apr 21, 2020
Grant date	Apr 21, 2020

Abstract

The present disclosure relates to methods and devices for use in photoelectrochemical reduction of CO2. In particular, it is disclosed a filter-press photoelectrochemical cell for producing a reduction product from CO2 and a method for the photoelectrochemical reduction of CO2.

First claim

The invention claimed is:

1. A filter-press photoelectrochemical cell comprising:
a) a cathodic compartment which comprises a cathode support frame comprising a cathodic material which acts as a cathode; a first fluid and gaseous CO 2 distribution frame and a second fluid and gaseous CO 2 distribution frame; cathodic gaskets, the cathodic gaskets being placed between the cathode support frame and the distribution frames, and as lateral ends of the cathodic compartment; wherein the cathode support frame is disposed between the first and second distribution frames;
b) an anodic compartment which comprises an anode support frame comprising an anodic material which acts as an anode; a fluid distribution frame arranged such that the fluid distribution frame is on a portion of the anodic compartment closer to an ion-exchange membrane than the anode support frame; and anodic gaskets, the anodic gaskets being placed between the anode support frame and the distribution frame, and as lateral end of the anodic compartment; and
c) the ion-exchange membrane disposed between the cathodic compartment and the anodic compartment;
wherein
i) the cathodic material is a conductive porous electrode with immobilized CO 2 electrocatalyst material;
ii) the first and second fluid and gaseous CO 2 distribution frames and cathodic gaskets are arranged such that in use they allow introducing a catholyte and gaseous CO 2 separately into the cathodic compartment through different inlet ports and they allow exiting the catholyte, liquid and gaseous products and/or unreacted CO 2 jointly through an outlet port;
iii) the fluid distribution frame, the anode support frame and anodic gaskets are arranged in such a way that in use they allow introducing an anolyte into the anodic compartment through an inlet port, and they allow exiting the anolyte and oxidation products jointly through an outlet port;
iv) the anodic material, is a photocatalytic anodic material, and is located on a side facing the membrane of an optical window of the anode support frame; and is arranged such that in use is able to be in contact with the anolyte which is introduced into the anodic compartment via the inlet port and, is able to be activated when a radiation used to irradiate the anodic compartment reaches the optical window by its opposite side which is not facing the membrane; and
v) the photocatalytic anodic material and the gas diffusion cathodic material have a surface area ratio comprised from 1:1 to 1:0.1.

2. The filter-press photoelectrochemical cell according to claim 1 , wherein the immobilized CO 2 electrocatalyst material of the cathodic material is selected from the group consisting of
a) a metal with a high overpotential to hydrogen evolution, low CO adsorption and high overpotential for CO 2 to CO 2 radical ion, selected from the group consisting of Pb, Hg, In, Sn, Cd, Tl and Bi;
b) a metal with a medium overpotential to hydrogen evolution and low CO adsorption, selected from the group consisting of Au, Ag, Zn, Pd and Ga;
c) a metal with a high CO adsorption and a medium overpotential to hydrogen evolution, selected from the group consisting of Cu;
d) a metal with a relatively low overpotential to hydrogen evolution and a high CO adsorption, selected from the group consisting of Ni, Fe, Pt, Ti;
e) an oxide of any of the metals of a), b), c) or d) type; and
f) combinations thereof;

the material being deposited on a highly porous and conductor support.

3. The filter-press photoelectrochemical cell according to claim 2 , wherein the highly porous and conductor support is selected from the group consisting of carbon paper, carbon based nanofibers, metallic meshes, and metal foams.

4. The filter-press photoelectrochemical cell according to claim 1 , wherein the immobilized CO 2 electrocatalyst material of the cathodic material is selected from the group consisting of Sn, Pb, Hg, Bi, In, Cd, Tl, Cu, CuO, Cu 2 O, Au, Ag, Zn, Pd, Ga and combinations thereof, the material being deposited on a highly porous and conductor support.

5. The filter-press photoelectrochemical cell according to claim 1 , wherein the immobilized CO 2 electrocatalyst material of the cathodic material is selected from the group consisting of Pb, Hg, In, Sn, Cd, Tl, Bi and combinations thereof, the material being deposited on a highly porous and conductor support.

6. The filter-press photoelectrochemical cell according to claim 1 , wherein the photocatalytic anodic material is selected from semiconductor materials with a bandgap between 1.1 and 3.4 eV and valence band edge equal to or higher than 1.23 V vs RHE.

7. The filter-press photoelectrochemical cell according to claim 6 , wherein the photocatalytic anodic material is selected from the group consisting of TiO 2 , WO 3 , BiVO 4 , Fe 2 O 3 , SrTiO 3 , Si, amorphous Si, GaAs, GaN, MoS 2 , WSe 2 , MoSe 2 and combinations thereof.

8. The filter-press photoelectrochemical cell according to claim 1 , wherein the anolyte comprises:
a) at least one polar protic solvent comprising at least one supporting electrolyte, and
b) optionally a buffer solution;

the supporting electrolyte is a salt of the formula M m Y n in which M is selected from the group consisting of lithium, potassium, sodium, magnesium, calcium, and strontium; and Y is either a hydroxide ion or a counter ion coming from mineral acids selected from the group consisting of halides, sulfates, nitrates, chlorates and phosphates.

9. The filter-press photoelectrochemical cell according to claim 8 , wherein the salt included as a supporting electrolyte is selected from the group consisting of NaOH, KOH, H 2 SO 4 , KCl, HCl, H 3 PO 4 , NaHCO 3 , K 2 HPO 4 , K 2 SO 4 , and Na 2 SO 4 .

10. The filter-press photoelectrochemical cell according to claim 1 , wherein the catholyte comprises:
a) at least one polar protic solvent comprising at least one supporting electrolyte, and
b) optionally a buffer solution;

the supporting electrolyte is a salt of the formula M m X n in which: M is selected from the group consisting of magnesium, calcium, lithium, potassium and sodium; and X is selected from anions of weak or strong acids selected from the group consisting of carbonates, bicarbonates, sulfates, chlorates, hydroxides and halides.

11. The filter-press photoelectrochemical cell according to claim 10 , wherein the salt included as a supporting electrolyte is selected from the group consisting of NaHCO 3 , KHCO 3 , K 2 CO 3 , Na 2 SO 4 , K 2 SO 4 , KCl, and KClO 4 .

12. The filter-press photoelectrochemical cell according to claim 1 , wherein the ion-exchange membrane is an ion-exchange membrane that permits selected ions to cross the membrane to balance the process stoichiometry.

13. The filter-press photoelectrochemical cell according to claim 1 , wherein the ion-exchange membrane is a cation exchange membrane.

14. A method for reducing carbon dioxide comprising the steps of:
i) providing an filter-press photoelectrochemical cell as defined in claim 1 ;
ii) feeding the filter-press photoelectrochemical cell with an anolyte through an inlet port into the anodic compartment, a catholyte through an inlet port into the cathodic compartment and a gas containing CO 2 through a different inlet port into the cathodic compartment;
iii) applying to the cell an external electrical potential between the cathode and the anode with bias capacity ranging from 0 to 4 volts;
iv) irradiating the photoanode with a radiation, thus radiation includes on the optical window activating the photocatalytic anodic material by its opposite side which is not facing the membrane; and
v) c

Assignees

• Repsol Sa
• Enagas Services Solutions S L U

Inventors

• Hernández Alonso María Dolores
• Penelas Pérez Germán
• Andreu Teresa
• Irtem Erdem
• Parra Andrés
• Fábrega Cristián
• Morante Juan Ramón

Classifications

• B01J23/38

  of noble metals · CPC title

• B01J23/70

  of the iron group metals or copper · CPC title

• C01B32/50

  Carbon dioxide · CPC title

• C25B1/00

  Electrolytic production of inorganic compounds or non-metals · CPC title

• C25B9/20 Primary

  Chemistry & Metallurgy · mapped topic