Electrolyzer reactor and related methods

Patent metadata

Field	Value
Publication number	US-11668014-B2
Application number	US-202016845305-A
Country	US
Kind code	B2
Filing date	Apr 10, 2020
Priority date	Jul 23, 2014
Publication date	Jun 6, 2023
Grant date	Jun 6, 2023

Abstract

The disclosure relates to an electrolyzer reactor suitable for the reduction of organic compounds. The reactor includes a membrane electrode assembly with freestanding metallic meshes which serve both as metallic electrode structures for electron transport as well as catalytic surfaces for electron generation and organic compound reduction. Suitable organic compounds for reduction include oxygenated and/or unsaturated hydrocarbon compounds, in particular those characteristic of bio-oil (e.g., alone or a multicomponent mixtures). The reactor and related methods provide a resource- and energy-efficient approach to organic compound reduction, in particular for bio-oil mixtures which can be conveniently upgraded at or near their point of production with minimal or no transportation.

First claim

What is claimed is:

1. An electrolyzer reactor comprising:
(a) a membrane electrode assembly comprising:
(i) a proton exchange membrane (PEM) having a first surface and a second surface opposing the first surface,
(ii) a freestanding first metallic mesh in physical contact with, but not fixedly attached to, the first PEM surface and having electrocatalytic activity for water oxidation and hydrogen ion formation, and
(iii) a freestanding second metallic mesh in physical contact with, but not fixedly attached to, the second PEM surface and having electrocatalytic activity for reduction of one or more organic compounds,
wherein the first metallic mesh and the second metallic mesh are free from catalytic materials thereon, the first metallic mesh and the second metallic mesh are in electrical contact with each other and optionally with a voltage source for driving electrons therebetween, and the second metallic mesh is the only material that is in physical contact with the second PEM surface and that has electrocatalytic activity for reduction of the one or more organic compounds;

(b) a first reaction volume in fluid communication with (i) the first metallic mesh and (ii) the first PEM surface; and
(c) a second reaction volume in fluid communication with (i) the second metallic mesh and (ii) the second PEM surface.

2. An electrolyzer reactor comprising:
(a) a membrane electrode assembly comprising:
(i) a proton exchange membrane (PEM) having a first surface and a second surface opposing the first surface,
(ii) a freestanding first metallic mesh in physical contact with, but not fixedly attached to, the first PEM surface and having electrocatalytic activity for water oxidation and hydrogen ion formation, and
(iii) a freestanding second metallic mesh in physical contact with, but not fixedly attached to, the second PEM surface and having electrocatalytic activity for reduction of one or more organic compounds,
wherein the first metallic mesh and the second metallic mesh are in electrical contact with each other and optionally with a voltage source for driving electrons therebetween, and the second metallic mesh is the only material that is in physical contact with the second PEM surface and that has electrocatalytic activity for reduction of the one or more organic compounds;

(b) a first reaction volume in fluid communication with (i) the first metallic mesh and (ii) the first PEM surface; and
(c) a second reaction volume in fluid communication with (i) the second metallic mesh and (ii) the second PEM surface.

3. The reactor of claim 2 , wherein the first metallic mesh comprises a catalytic material thereon.

4. The reactor of claim 2 , wherein:
(i) the first reaction volume is defined by a first housing; and
(ii) the second reaction volume is defined by a second housing.

5. The reactor of claim 2 , wherein:
(i) the PEM is in the form of a tube, the first PEM surface being the tube interior surface and the second PEM surface being the tube exterior surface;
(ii) the PEM tube defines the first reaction volume as a tubular volume containing the first metallic mesh therein; and
(iii) the second reaction volume is defined by an outer shell as an annular volume between the outer shell and the PEM tube and containing the second metallic mesh therein.

6. The reactor of claim 2 , wherein
(i) the first metallic mesh comprises stainless steel; and
(ii) the second metallic mesh comprises an alloy comprising copper and nickel.

7. The reactor of claim 2 , wherein the second metallic mesh has electrocatalytic activity for catalyzing at least one of (i) electrocatalytic hydrogenation (ECH) of unsaturated carbon-carbon bonds in an organic substrate, (ii) ECH of carbon-oxygen double bonds in an organic substrate, and (iii) electrocatalytic hydrodeoxygenation (ECHDO) of carbon-oxygen single bonds in an organic substrate.

8. The reactor of claim 2 , wherein the second metallic mesh has electrocatalytic activity for reduction of one or more organic compounds comprising one or more functional groups selected from the group consisting of carbonyl carbon-oxygen double bonds, aromatic double bonds, ethylenic carbon-carbon double bonds, acetylenic carbon-carbon triple bonds, hydroxyl carbon-oxygen single bonds, ether carbon-oxygen single bonds, and combinations thereof.

9. The reactor of claim 2 , wherein the first metallic mesh comprises at least one metal component having electrocatalytic activity for reduction of the one or more organic compounds.

10. The reactor of claim 2 , wherein the first metallic mesh and the second metallic mesh each comprise the same metal.

11. The reactor of claim 2 , wherein the proton exchange membrane (PEM) comprises a perfluorocarbon sulfonate polymer.

12. The reactor of claim 2 , further comprising a voltage source in electrical connection with the first metallic mesh and the second metallic mesh, the voltage source being adapted to driving electrons therebetween.

13. The reactor of claim 2 , wherein:
the first metallic mesh is not hot-pressed to the first PEM surface with a binding agent; and
the second metallic mesh is not hot-pressed to the second PEM surface with a binding agent.

14. The reactor of claim 2 , wherein:
the first metallic mesh comprises first metal wires formed from a metal or metal alloy, the first metal wires having sufficient catalytic activity themselves for water oxidation and hydrogen ion formation; and
the second metallic mesh comprises second metal wires formed from a metal or metal alloy, the second metal wires having sufficient catalytic activity themselves for the reduction of one or more organic compounds.

15. The reactor of claim 14 , wherein the second PEM surface is free from catalytic electrode materials fixedly attached thereto.

16. The reactor of claim 2 , wherein the PEM is free from catalytic electrode materials fixedly attached thereto.

17. The reactor of claim 2 , wherein:
the reactor comprises at least one enclosure portion mechanically holding (i) the freestanding first metallic mesh in physical contact with the first PEM surface, and (ii) the freestanding second metallic mesh in physical contact with the second PEM surface; and
the freestanding first metallic mesh and the freestanding second metallic mesh are adapted to be removed from and replaced in the reactor.

Assignees

• Univ Michigan State

Inventors

• Jackson James E
• Lam Chun Ho
• Saffron Christopher M
• Miller Dennis J

Classifications

• C25B3/25 Primary

  Reduction · CPC title

• C25B11/03

  perforated or foraminous · CPC title

• C25B9/015

  Cylindrical cells · CPC title

• C25B9/19

  with diaphragms · CPC title