A hydrogen electrolyzer cell includes a shared reservoir, anode and cathode chambers, and a dividing wall. The shared reservoir holds an electrolytic solution. The anode chamber extends up from the shared reservoir and includes an anode electrode for producing oxygen gas during an electrolysis of the electrolytic solution. An oxygen degassing region is integrated into the anode chamber above the anode electrode. The cathode chamber extends up from the shared reservoir and includes a cathode electrode for producing hydrogen gas during the electrolysis. A hydrogen degassing region is integrated into the cathode chamber above the cathode electrode. The dividing wall extends up from the shared reservoir and separates the anode chamber from the cathode chamber. The dividing wall blocks transport of charged ions within the electrolytic solution across the dividing wall and blocks mixing of the hydrogen and oxygen gases released during the electrolysis.

An electrolytic device and to a method for operating an electrolysis of water with at least one electrolysis cell, the electrolysis cell having an anode compartment having an anode and a cathode compartment having a cathode. The anode compartment is separated from the cathode compartment by a proton exchange membrane. The anode compartment is suitable for holding water and oxidising the water on the anode to form a first product including oxygen and the cathode compartment is suitable for holding water and reducing the water on the cathode to a second product including hydrogen. Furthermore, the electrolysis device includes a first gas precipitation device for precipitation of oxygen, the first gas precipitation device for carrying out a natural water circulation being arranged above the electrolysis cell.

Systems and methods for use in extracting oil from solid plant-based materials are described. The systems and methods use an electrolyzed carrier fluid made from a hydroxide brine for contacting with plant-based material to thereby separate oil from solid plant particulate. The electrolyzed carrier fluid can have a reductive oxidation-reduction-potential (ORP) of −700 mV or more, such as in the range of from about −900 mV to about −1000 mV.

A passive dual modulating regulator that responds to a pressure differential between a hydrogen-side and an oxygen-side of one or more proton-exchange membrane (PEM) cells is provided. The passive dual modulating regulator includes a flexible diaphragm that is clamped along its periphery between hemispherical chambers. A bi-directional valve assembly extends through the flexible diaphragm and includes opposing valve plugs for selectively closing the output ports of the respective hemispherical chambers. Large or sustained pressure imbalances between the hydrogen-side and the oxygen-side of a hydrogen generation system are avoided without active control inputs of any kind, and consequently a rupture of the PEM is entirely avoided.

A system includes a high temperature electrolyser, a first line for supplying the electrolyser to supply the electrolyser with steam, a first line for discharging the electrolyser to discharge dihydrogen from the electrolyser, a second line for discharging the electrolyser to discharge dioxygen from the electrolyser, a first heat exchange module to ensure a heat exchange between the first steam supply line and the first dihydrogen discharge line. The system also includes a steam ejector arranged downstream from the first heat exchange module on the first dihydrogen discharge line to inject steam into the first dihydrogen discharge line. The system relates to the field of high temperature electrolysis of water, also with solid oxide and that of solid oxide fuel cells. It applies particularly to optimise the energy consumption of an SOEC electrolyser system.

Methods and systems for production of lithium hydroxide and lithium carbonate are described. One or more embodiments of the method include producing lithium hydroxide from potassium chloride, lithium chloride, and water. One or more embodiments of the method include producing lithium carbonate from potassium chloride, lithium chloride, water, and a carbon dioxide source. One or more embodiments of the method include producing lithium carbonate from sodium chloride, lithium chloride, water, and a carbon dioxide source.

A photovoltaic module has at least one solar cell, wherein the solar cell is enclosed by an encapsulation apparatus, and an electrolysis unit for dehumidifying the interior of the encapsulation apparatus. The electrolysis unit has a cathode, an anode, and an ion conductor connecting the cathode and the anode. The electrolysis unit is designed to cleave water in hydrogen and oxygen. A method for dehumidifying a photovoltaic module is accomplished by the electrolysis unit.

A system and method for treating flue gas of a boiler based on solar energy are provided, wherein a heat pump is connected with a heat collector via first and second valves, a carbon dioxide electrolysis chamber is connected with a flue gas pretreatment chamber and a power distribution control module for electrolyzing and reducing carbon dioxide, a gas phase separation chamber is connected with a gas phase outlet to separate a mixture, and discharge the separated gas phase products; a Fischer-Tropsch reaction chamber is connected with the gas phase separation chamber to pass the separated carbon monoxide and hydrogen into a flowing reaction cell, a liquid phase product separation chamber is connected with a liquid phase outlet to separate the liquid phase hydrocarbon fuel products, and separate and supplement electrolyte; an electrolyte cooling circulation chamber is connected with the liquid phase product separation chamber.

A hydrogen production apparatus including a photocatalyst and generating hydrogen from water includes a wavelength separation unit separating sunlight by wavelength, an infrared light conversion unit converting infrared light separated by the wavelength separation unit to visible light, and an ultraviolet light conversion unit converting ultraviolet light separated by the wavelength separation unit to visible light.

The embodiments of the present disclosure relate to a method and apparatus for producing a CNM product that may comprise carbon nanotubes (CNTs). The method and apparatus employ carbon dioxide (CO.sub.2) and a carbonate electrolyte that is lithium-free as reactants in an electrolysis reaction in order to make CNTs. In some embodiments of the present disclosure, a graphene-defect agent may be introduced into the electrolysis reaction.