Modular electrochemical cells

• US 10,637,068 B2
• Filed: 12/21/2017
• Issued: 04/28/2020
• Est. Priority Date: 07/31/2013
• Status: Active Grant

• Current Assignee: EDAC Labs, Inc.
• Original Assignee: Aquahydrex, Inc.
• Inventors: Swiegers, Gerhard Frederick, Beirne, Stephen Thomas, Chen, Jun, Wang, Caiyun
• Primary Examiner(s): Walls, Cynthia K
• Application Number:
  US15/850,279
• Publication Number:
  US 20180138517A1
• Time in Patent Office: 859 Days
• CPC Class Codes: C25B 1/13 Ozone
• CPC Class Codes: C25B 1/14 Alkali metal compounds
• CPC Class Codes: C25B 1/245 Fluorine; Compounds thereof
• CPC Class Codes: C25B 1/26 Chlorine; Compounds thereof by simultaneous production of alkali metal hydroxides and chlorine, oxyacids or salts of chlorine C25B1/34
• CPC Class Codes: C25B 1/265 Chlorates
• CPC Class Codes: C25B 1/30 Peroxides
• CPC Class Codes: C25B 11/031 Porous electrodes
• CPC Class Codes: C25B 15/02 Process control or regulation
• CPC Class Codes: C25B 3/00 Electrolytic production of organic compounds
• CPC Class Codes: C25B 9/19 with diaphragms
• CPC Class Codes: C25C 7/00 Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells for the production of aluminium C25C3/06 - C25C3/22
• CPC Class Codes: H01M 2300/0011 Sulfuric acid-based
• CPC Class Codes: H01M 4/8605 Porous electrodes
• CPC Class Codes: H01M 4/8626 characterised by the form
• CPC Class Codes: H01M 4/8807 Gas diffusion layers
• CPC Class Codes: H01M 8/04104 Regulation of differential pressures
• CPC Class Codes: H01M 8/08 Fuel cells with aqueous electrolytes
• CPC Class Codes: H01M 8/083 Alkaline fuel cells
• CPC Class Codes: Y02E 60/36 Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
• CPC Class Codes: Y02E 60/50 Fuel cells

Abstract

A gas diffusion electrode for an electro-synthetic or electro-energy cell, for example a fuel cell, including one or more gas permeable layers, a first conductive layer provided on a first side of the gas diffusion electrode, and a second layer, which may be a second conductive layer, provided on a second side of the gas diffusion electrode. The one or more gas permeable layers are positioned between the first conductive layer and the second layer, which may be a second conductive layer, and the one or more gas permeable layers provide a gas channel. The one or more gas permeable layers are gas permeable and substantially impermeable to the liquid electrolyte. The porous conductive material is gas permeable and liquid electrolyte permeable. The gas diffusion electrode can be one of a plurality of alternating anode/cathode sets.

Claims

1. An electrochemical reactor, comprising:

gas diffusion electrodes;

at least one of the gas diffusion electrodes separately comprising;

a first electrically conductive layer and a second electrically conductive layer, wherein the first conductive layer and the second conductive layer are gas permeable and liquid electrolyte permeable,

a gas-permeable liquid-impermeable layer positioned between the first conductive layer and the second conductive layer, wherein the gas-permeable liquid-impermeable layer provides at least part of a gas channel to transport a gas internally in the at least one of the gas diffusion electrodes; and

,

an electrolyte spacer layer positioned between the gas diffusion electrodes,

wherein the electrolyte spacer layer is liquid electrolyte permeable.

2. The electrochemical reactor of claim 1, wherein the electrolyte spacer layer is electrically insulating.

3. The electrochemical reactor of claim 1, wherein the electrolyte spacer layer provides at least part of a liquid electrolyte channel that is in fluid communication with an electrolyte inlet and an electrolyte outlet.

4. The electrochemical reactor of claim 1, further including a spacer positioned between the first conductive layer and the second conductive layer, and positioned adjacent to the gas-permeable liquid-impermeable layer, the spacer providing at least part of the gas channel.

5. The electrochemical reactor of claim 1, wherein the first conductive layer and the second conductive layer comprise a porous conductive material.

6. The electrochemical reactor of claim 1, wherein the reactor is a multilayered

reactor comprising:

a plurality of electrolyte spacer layers;

a plurality of gas diffusion electrodes;

wherein each electrolyte spacer layer of the plurality of electrolyte spacer layers is interleaved between adjacent gas diffusion electrodes of the plurality of gas diffusion electrodes.

7. The electrochemical reactor of claim 6, wherein the multi-layered reactor includes a plurality of the gas channels that are connected into a single gas inlet/outlet.

8. The electrochemical reactor of claim 1, wherein the gas-permeable liquid-impermeable layer is selected from the group of PTFE, ePTFE, polypropylene, polyethylene, polyethersulfone and polysulfone.

9. The electrochemical reactor of claim 4, wherein the spacer is a nonconductive polymer, a polyolefin mesh, an electrically insulating polymer net or is provided by embossed polymer structures.

10. The electrochemical reactor of claim 1, further including a barrier layer that limits an undesired gas permeating into the gas channel.

11. The electrochemical reactor of claim 1, wherein the at least one of the gas diffusion electrodes is partially sealed to gas by heat sealing, laser sealing or potting at least part of the edges of the at least one of the gas diffusion electrodes.

12. The electrochemical reactor of claim 1, wherein the reactor is part of a modular reactor that is able to be attached to another modular reactor.

13. The electrochemical reactor of claim 1, wherein the reactor does not have a diaphragm or a proton-exchange membrane (PEM) positioned between the gas diffusion electrodes.

14. The electrochemical reactor of claim 1, the gas diffusion electrodes

comprising:

a first gas diffusion electrode comprising a first conductive layer, a second conductive layer, and a first gas-permeable liquid-impermeable layer positioned between the first conductive layer and the second conductive layer, wherein the first gas-permeable liquid-impermeable layer provides at least part of a first gas channel; and

,

a second gas diffusion electrode comprising a third conductive layer, a fourth conductive layer, and a second gas-permeable liquid-impermeable layer positioned between the third conductive layer and the fourth conductive layer, wherein the second gas-permeable liquid-impermeable layer provides at least part of a second gas channel.

15. The electrochemical reactor of claim 14, wherein the first gas channel is able to transport a first gas internally in the first gas diffusion electrode, and the second gas channel is able to transport a second gas internally in the second gas diffusion electrode.

16. The electrochemical reactor of claim 14, wherein the first conductive layer and the second conductive layer comprise a porous conductive material, and wherein the third conductive layer and the fourth conductive layer comprise a porous conductive material.

17. The electrochemical reactor of claim 14, further including:

a first spacer positioned between the first conductive layer and the second conductive layer, and positioned adjacent to the first gas-permeable liquid-impermeable layer, the first spacer providing at least part of the first gas channel; and

a second spacer positioned between the third conductive layer and the fourth conductive layer, and positioned adjacent to the second gas-permeable liquid-impermeable layer, the second spacer providing at least part of the second gas channel.

18. The electrochemical reactor of claim 1, wherein:

the electrochemical reactor is a fuel cell;

the electrochemical reactor is a reversible fuel cell electrolyzer;

the electrochemical reactor is a half fuel cell;

or,

the electrochemical reactor is a direct methane fuel cell.

19. The electrochemical reactor of claim 15, wherein:

the first gas is methane;

the first gas is methane and the second gas is oxygen;

the first gas is chlorine;

the first gas is chlorine and the second gas is oxygen;

the first gas is oxygen and the second gas is hydrogen;

or,

the first gas or the second gas is a depolarising gas.

20. The electrochemical reactor of claim 1, wherein the gas diffusion electrodes are:

stacked as flat-sheets;

formed as plate and frame;

flexible;

flexible, stacked and then spiral-wound;

or, formed as hollow fibres.

21. The electrochemical reactor of claim 1, wherein the first conductive layer and the second conductive layer are electrically connected to each other.

22. The electrochemical reactor of claim 21, wherein electrochemical reactor is a hollow-fibre electrochemical reactor and the first conductive layer and the second conductive layer are part of a single conductive layer.

23. The electrochemical reactor of claim 1, wherein the first conductive layer and the second conductive layer are not electrically connected to each other.