Aquahydrex Pty Ltd

Aquahydrex, Inc.

Aquahydrez Pty Ltd

Gerhard Frederick Swiegers

Stephen Thomas Beirne

Steven DuWayne Kloos

Andrew Nattestad

Jun Chen

Caiyun Wang

Fletcher William Thompson

Dennis Antiohos

Gordon George Wallace

David Leslie Officer

Paul Brendan Denis Michael Barrett

Mark Bown

Peter Gordon Symons

Mark S Romano

Wen Zheng

Anton Launikonis

Peter Osvath

John Kraft

A method and/or electrochemical cell for utilising one or more gas diffusion electrodes (GDEs) in an electrochemical cell, the one or more gas diffusion electrodes have a wetting pressure and/or a bubble point exceeding 0.2 bar. The one or more gas diffusion electrodes can be subjected to a pressure differential between a liquid side and a gas side. A pressure on the liquid side of the GDE over the gas side does not exceed the wetting pressure of the GDE during operation (in cases where a liquid electrolyte side has higher pressure), and/or a pressure on the gas side of the GDE over the liquid side, does not exceeds the bubble point of the GDE (in cases where the gas side has the higher pressure).

Method and electrochemical cell for managing electrochemical reactions

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.

Modular electrochemical cells

Water-splitting devices and methods for manufacturing water-splitting devices or solar cells is disclosed. The method seeks to provide a relatively high-volume, low-cost mass-production method. In one example, the method facilitates simultaneous co-assembly of one or more sub-units and two or more polymer films or sheets to form a water-splitting device. According to another aspect, there is provided an improved water-splitting device. In one example form, there is provided a water-splitting device which includes a first electrode for producing oxygen gas and a second electrode for producing hydrogen gas from water. The first electrode and the second electrode are positioned between a first outer polymer layer and a second outer polymer layer, and at least one spacer layer is positioned between the first outer polymer layer and the second outer polymer layer.

Multi-layer water-splitting devices

There is provided a new type of electro-synthetic (electrochemical) or electro-energy cell, such as a fuel cell. The cell includes a liquid electrolyte and at least one gas diffusion electrode (GDE). The GDE operates as a gas depolarized electrode and includes a gas permeable material that is substantially impermeable to the liquid electrolyte, as well as a porous conductive material provided on a liquid electrolyte facing side of the gas diffusion electrode. The porous conductive material can be attached to the gas permeable material by being laminated. Alternatively, the porous conductive material is deposited or coated on at least part of the gas permeable material. A depolarizing gas can be received by the at least one gas diffusion electrode to gas depolarize the electrode. The depolarizing gas changes a half-reaction that would occur at the gas diffusion electrode to a half-reaction that is energetically more favorable.

Electro-synthetic or electro-energy cell with gas diffusion electrode(s)

A method and/or electrochemical cell for utilizing one or more gas diffusion 5 electrodes (GDEs) in an electrochemical cell, the one or more gas diffusion electrodes have a wetting pressure and/or a bubble point exceeding 0.2 bar. The one or more gas diffusion electrodes can be subjected to a pressure differential between a liquid side and a gas side. A pressure on the liquid side of the GDE over the gas side does not exceed the wetting pressure of the GDE during 10 operation (in cases where a liquid electrolyte side has higher pressure), and/or a pressure on the gas side of the GDE over the liquid side, does not exceeds the bubble point of the GDE (in cases where the gas side has the higher pressure).

Disclosed are gas permeable 3D electrodes, preferably that have practical utility in, particularly, electro-energy and electro-synthetic applications. Gas permeable materials, such as non-conductive porous polymer membranes, are attached to one or more porous conductive materials. In another aspect there is provided a method for the fabrication of gas permeable 3D electrodes, for example gas diffusion electrodes (GDEs). The 3D electrodes can be utilized in electrochemical cells or devices.

Composite three-dimensional electrodes and methods of fabrication

Growing community of inventors

Woonona, Australia

Gerhard Frederick Swiegers