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전해조 시스템에서의 가스 압력 평형 방법 및 압력 평형 밸브 시스템을 가진 전해조 시스템

Resumen de: AU2024224224A1

In a gas pressure balance method in an electrolyser system a predefined pressure difference between pressures in an oxygen gas separation tank and a hydrogen gas separation tank is maintained by controlled release of gases through an oxygen back pressure valve and a hydrogen back pressure valve. in a first step, for each of the oxygen back pressure valves and the hydrogen back pressure valves, a predefined, calibrated pilot gas pressure is generated and in a second step, the predefined, calibrated pilot gas pressures are forwarded to the respective back pressure valves and in a third step, hydrogen and oxygen gasses are released whenever the gas pressures in the hydrogen and oxygen separation tanks exceeds the predefined, calibrated pilot pressure in the respective pilot gas streams.

TRANSITION METAL-DOPED NICKEL OXYHYDROXIDE CATALYST, PREPARATION METHOD THEREOF, AND USE THEREOF

Resumen de: US20260009149A1

Provided is a transition metal-doped nickel oxyhydroxide catalyst, its preparation method, and its application in seawater electrolysis for hydrogen production. The method includes: (1) constructing a three-electrode system and using a chronoamperometry or chronopotentiometry method to electrodeposit a precatalyst onto a conductive substrate from a mixed metal salt solution containing nickel, iron, and at least one other transition metal salt such as cobalt or chromium; and (2) using the precatalyst-loaded substrate as a working electrode in an alkaline solution and applying a constant current to perform an in-situ conversion, thereby forming the final transition metal-doped nickel oxyhydroxide catalyst. The resulting catalyst exhibits high catalytic activity, high selectivity for oxygen evolution, and exceptional long-term stability under high current densities, making it highly suitable for direct seawater electrolysis systems,

HYDROGEN AND OXYGEN ELECTROLYSIS CELL SYSTEM

Resumen de: WO2026006927A1

The various embodiments described herein generally relate to the production and storage of gasses, such as hydrogen and oxygen, and more particularly to an electrolysis cell for supplying the hydrogen and oxygen gasses as gaseous fuel for clean power generation systems such as linear alternators.

ELECTROLYSIS SYSTEM

Resumen de: US20260009145A1

An electrolysis system has at least two electrolysis installations, a power supply source with a direct voltage output, and a central supply line connected to the direct voltage output. A direct current, at a first direct voltage, can be fed into the central supply line. The electrolysis installations are connected electrically in parallel to the central supply line. For a direct voltage supply from the public power grid a central voltage source converter converts an input-side alternating voltage into the output-side first direct voltage at a direct voltage output. Each electrolysis installation is connected via a DC/DC converter that converts the first direct voltage into a second direct voltage, parallel to the direct voltage output so that the second direct voltage drops across the electrolysis installation. Each of the DC/DC converters can be controlled and/or regulated for adapting a level of its second direct voltage.

METHOD FOR THE PRODUCTION OF DIHYDROGEN USING OXIDIZED NANODIAMONDS AS PHOTOCATALYSTS

Resumen de: US20260008033A1

A method for producing dihydrogen by photodissociation of water, may include bringing an aqueous solution in contact with oxidized nanodiamonds under solar, natural, or artificial illumination (or light). The oxidized nanodiamonds may have an oxygen/carbon ratio of at least 5% atomic, determined by XPS without previous treatment of the oxidized nanodiamonds. The method may further include preparing the oxidized nanodiamonds by subjecting nanodiamonds to an oxidizing treatment. The oxidizing treatment may include annealing at a temperature of 500° C.±50° C. for a duration in a range of from 1 to 5 hours under an oxygenated atmosphere.

COMPOSITIONS AND METHODS FOR TREATING POROUS MATERIALS

Resumen de: US20260008042A1

The present disclosure is directed to a processing solution composition comprising a metal salt, an acid, a solvent, and a non-metal reductant. The present disclosure is also directed to a method of impregnating a porous material by covering or coating the porous material with a processing solution comprising a metal salt, an acid, a solvent, and a non-metal reductant.

POROUS ELECTROLYZER GAS DIFFUSION LAYER AND METHOD OF MAKING THEREOF

Resumen de: US20260008100A1

A porous titanium sheet configured to function as an anode side gas diffusion layer of a proton exchange membrane (PEM) electrolyzer is formed by a powder technique, such as tape casting or powder metallurgy.

OXYGEN-DOMINATED SUPRA-NANO DUAL-PHASE CATALYTIC REACTION MATERIAL ON A SUBSTRATE

Resumen de: US20260009148A1

The present invention provides an oxygen-dominated supra-nano dual-phase catalytic reaction material, which includes a uniform oxygen-enriched amorphous shell and a core encapsulated within the uniform oxygen-enriched amorphous shell. This invention exhibits ultrahigh HER performance, a critical reaction in water splitting, making it suitable for application in hydrogen production industries, battery companies, new energy vehicle enterprises, and large power stations.

A CATALYST FOR GENERATING HYDROGEN AND METHOD OF ITS PRODUCTION

Resumen de: US20260008043A1

The present disclosure provides a catalyst, its preparation and uses thereof, the catalyst comprising a conductive substrate coated by at least two layers including a proximal layer and a distal layer wherein said proximal layer comprises a proximal metal composition and said distal layer comprise a distal metal composition, the proximal metal composition being different from the distal metal composition; wherein said proximal metal composition comprises a metallic M and said distal metal composition comprise a combination of two or more different metal complexes, each having a formula MxLy, wherein M, which may be the same or different in said two or more metal complexes, represents a metal atom; L, which may be the same or different in said two or more metal complexes, represents a moiety comprising at least one atom selected from the group consisting of oxygen (O), phosphorous (P), boron (B) and nitrogen (N); x represents any value between (1) and (6); and y represents any value between (1) and (6); and wherein said metal atom of metallic M and said metal atom in MxLy may be the same or different metal atom.

알칼리 전해조 시스템용 급수 준비 방법 및 급수 준비 시스템

Resumen de: CN120936752A

A feed water preparation system in a water electrolyser, suitable for producing hydrogen and oxygen using alkaline water in one or more pressurized electrolyser stacks (2), and comprising a product gas conditioning system having a safety valve blow-off stream conduit (11) connected to a feed water container (9), and/or a reduced pressure flow conduit (31) connected to a gas cleaning container on the water supply container (9).

환원 장치, 환원 방법 및 환원물의 제조 방법

Resumen de: CN120981281A

Provided is a reduction device which can be manufactured inexpensively and easily, has a wide reaction field, enables a reduction reaction even with low-energy light rays such as visible light, and has a long catalyst life. The reduction device of the present disclosure is characterized by containing diamond particles. It is preferable that the diamond particles are contained in the form of a diamond particle dispersion. It is preferable that the diamond particles include nanodiamond particles having a particle diameter of 1 mu m or less. It is preferable that the diamond particles comprise detonation nanodiamond particles.

수소 가스 생산 어셈블리 및 수소 가스 생산을 위한 방법

Resumen de: WO2024231154A1

The present invention relates to a hydrogen gas production assembly comprised of a hydrogen gas production device, a container comprising an aqueous electrolyte solution, a storage container for storing produced hydrogen gas an input providing the aqueous electrolyte solution from the container to the hydrogen gas production device and an output for transferring produced hydrogen gas from the hydrogen gas production device to the storage container. The present invention further relates to methods for the production of hydrogen gas via the hydrogen gas production assembly.

Elektrolysevorrichtung, Elektrolyseur, Verwendung und Verfahren zum Betrieb einer Elektrolysevorrichtung

Resumen de: DE102024118593A1

Vorgeschlagen werden eine Wasserstoff-Elektrolysevorrichtung 30, welche einen Wasserstoff-Elektrolysestack 12 und auf einer Kathodenseite des Wasserstoff-Elektrolysestacks 12 ein zum Schutz des Wasserstoff-Elektrolysestacks 12 gegen einen kathodenseitigen Druckabfall/-verlust vorgesehenes Differenzdruckventil 28 umfasst, wobei das Differenzdruckventil 28 einerseits zumindest mit einem anodenseitigen Druck des Elektrolysestacks 12 beaufschlagbar ist und beim Betrieb eines die Wasserstoff-Elektrolysevorrichtung 30 umfassenden Elektrolyseurs 10 beaufschlagt wird, nämlich vorspannbar ist bzw. vorgespannt wird, und andererseits mit einem kathodenseitigen Druck des Elektrolysestacks 12 beaufschlagbar ist und beim Betrieb des Elektrolyseurs 10 beaufschlagt wird, sowie ein Elektrolyseur 10 mit einer solchen Vorrichtung 30 sowie eine Verwendung und ein Verfahren zum Betrieb eines solchen Elektrolyseurs 10.

Renewable Energy Source Using Pressure Driven Filtration Processes and Systems

Resumen de: AU2025271499A1

Abstract A membrane element configured for filtration of water while simultaneously co- generating hydrogen, wherein the membrane comprises at least one anode electrode and at least one cathode electrode, each is in communication with said membrane; further wherein said membrane is adapted for electrolysis of at least a portion of said water to simultaneously at least partially generate hydrogen therefrom; further wherein at least one electrode selected from a group consisting of at least one anode electrode and at least one cathode electrode comprise at least one selected from a group consisting of at least one feed spacer, at least one permeate spacer and any combination thereof. combination thereof.20 ov b s t r a c t o v c o m b i n a t i o n t h e r e o f

Magnetohydrodynamic electric power generator

Resumen de: AU2025271525A1

MAGNETOHYDRODYNAMIC ELECTRIC POWER GENERATOR A power generator that provides at least one of electrical and thermal power comprising (i) at least one reaction cell for the catalysis of atomic hydrogen to form hydrinos identifiable by unique analytical and spectroscopic signatures, (ii) a reaction mixture comprising at least two components chosen from: a source of H20 catalyst or H20 catalyst; a source of atomic hydrogen or atomic hydrogen; reactants to form the source of H20 catalyst or H20 catalyst and a source of atomic hydrogen or atomic hydrogen; and a molten metal to cause the reaction mixture to be highly conductive, (iii) a molten metal injection system comprising at least one pump such as an electromagnetic pump that causes a plurality of molten metal streams to intersect, (iv) an ignition system comprising an electrical power source that provides low-voltage, high-current electrical energy to the plurality of intersected molten metal streams to ignite a plasma to initiate rapid kinetics of the hydrino reaction and an energy gain due to forming hydrinos, (v) a source of H2 and 0 2 supplied to the plasma, (vi) a molten metal recovery system, and (vii) a power converter capable of (a) converting the high- power light output from a blackbody radiator of the cell into electricity using concentrator thermophotovoltaic cells or (b) converting the energetic plasma into electricity using a magnetohydrodynamic converter. MAGNETOHYDRODYNAMIC ELECTRIC POWER GENERATOR ov o v

METHODS AND APPARATUS FOR PRODUCING HYDROGEN

Resumen de: AU2024265710A1

Disclosed herein is a method of generating molecular hydrogen comprising the steps of: (i) providing a plasma chamber having an inlet and an outlet; (ii) providing a feed of a hydrogen containing molecule through the inlet to a plasma in said plasma chamber wherein said plasma is exposed to at least one electromagnetic frequency whereby said hydrogen containing molecule is disassociated into a hydrogen species and at least one non-hydrogen species; (iii) removing said hydrogen species from the chamber at the outlet; and (iv) then forming molecular hydrogen from said hydrogen species.

ELECTROLYSIS SYSTEM

Resumen de: AU2024312642A1

The present invention relates to an electrolysis system comprising a tank adapted to contain water or an aqueous solution, an electrolytic array comprising electrically conductive plates, a temperature-resistant cathode proximal to, but spaced apart from, a cathodic end of the electrolytic array, a tank anode proximal to, but spaced apart from, an opposing anodic end of the electrolytic array, wherein the cathodic and anodic ends of the electrolytic array are electrically connected to a negative and positive terminal, respectively, of a first power supply adapted to provide direct-current (DC) power thereto, the temperature-resistant cathode and the tank anode are electrically connected to a negative and positive terminal, respectively, of a second power supply adapted to provide DC power thereto and at least the temperature-resistant cathode is adapted to generate a plasma arc within the water or aqueous solution between an end thereof and a closest plate of the electrolytic array.

INTEGRATED PROCESS FOR METHANE PRODUCTION AND DRY METHANE REFORMING

Resumen de: AU2024310412A1

The present disclosure relates generally to integrated processes for the production of methane and its use in dry methane reforming. In one aspect, the present disclosure provides process for producing a stream containing hydrogen and carbon monoxide, the process comprising: providing a methane synthesis feed stream comprising hydrogen and carbon dioxide; contacting the methane synthesis feed stream with a methane synthesis catalyst (e.g., in a methane synthesis reactor) to form a methane synthesis product stream comprising methane and water; providing a dry methane reformation feed stream comprising carbon dioxide and at least a portion of the methane of the methane synthesis product stream; contacting the dry methane reformation feed stream with a dry methane reformation catalyst (e.g., in a dry methane reformation reactor) to produce a dry methane reformer product stream comprising carbon monoxide and hydrogen.

CATALYST AND PROCESS

Resumen de: WO2026008968A1

Oxygen evolution reaction (OER) catalyst materials are provided comprising an iridium- containing compound on a particulate catalyst support, the OER catalyst material having the following characteristics: (i) a BET surface area in the range of and including 5 to 20 m2/g; (ii) an iridium content in the range of and including 25 to 50 wt%; and (iii) a Tmax in the temperature-programmed reduction profile of the OER catalyst material is in the range of and including 145 to 180 °C.

METHOD OF PRODUCING GREEN STEEL

Resumen de: WO2026008847A1

The present invention relates to a method of producing green steel by reduction of iron oxides using hydrogen. The inventive method makes use of mining waste as starting material for H2 generation by SDE process or a sulfur-iodine-process. Side products can be utilized in the steelmaking process. This is achieved by a method according to the present invention comprising the following steps: a) a part or all of the iron oxide used as raw material for steelmaking is reduced by hydrogen, b) a part or all hydrogen required for the reduction of iron oxide is generated via a SO2-depolarized electrolyzer (SDE) process or a sulfur-iodine-process, and c) a part or all of the diluted sulfuric acid obtained from step b) is used for at least one of i. steel pickling, ii. reaction with steel mill dust for generation of iron sulfate (FeSO4 or Fe2(SO4)3), and iii. increasing the concentration of said diluted sulfuric acid by vacuum evaporation of water using off-heat from steelmaking or pyrite roasting.

OFFSHORE HYDROGEN PRODUCTION SYSTEMS AND METHODS

Resumen de: WO2026008367A1

An offshore hydrogen production system is described comprising: a hydrogen production facility (10) comprising a power generator (70) configured to convert a source of renewable energy to electrical power and at least one electrolyser (16). The capacity of the at least one electrolyser (16) corresponds to a power output of the power generator (70). The hydrogen production facility (10) is configured to be supplied with utilities for the production of hydrogen from a utilities system (11) which is located remote from the offshore hydrogen production facility (10). Also described is a method of producing hydrogen, a method of designing an offshore hydrogen production system, a method for the production of an offshore hydrogen production system.

プラントの制御装置、プラント、プラントの制御方法、およびプログラム

Resumen de: WO2025263002A1

This plant control device comprises: a signal reception unit that receives a signal including at least one demand from among a power demand, a hydrogen demand and a production process steam demand; and a control unit that, on the basis of the received signal, adjusts at least one among the generation amount of steam in an exhaust heat recovery boiler, the flow rate in a steam supply pipe of a steam turbine, the flow rate in a steam supply pipe of an ammonia decomposition device, and the flow rate in a steam supply pipe of the production process so as to satisfy the demand indicated by a signal at a current load of the gas turbine.

アンモニア分解システム

Resumen de: WO2025263071A1

An ammonia decomposition system includes: a first decomposition part for thermally decomposing ammonia into nitrogen and hydrogen; a steam supply part for generating steam and supplying the steam to the first decomposition part as a heat source; a recovery line for recovering steam after passage through the first decomposition part; a turbine driven by the steam recovered by the recovery line; and a power generation part for generating electric power by being driven by the turbine.

プラントの制御装置、プラント、プラントの制御方法、およびプログラム

Resumen de: WO2025263000A1

A plant control device according to the present invention comprises: a signal reception unit that receives a signal including at least one of a power demand, a hydrogen demand, and a steam demand of a production process; and a control unit that, on the basis of the received signal, adjusts at least one of the amount of steam generated by a boiler, the amount of steam supplied to a steam turbine, the amount of steam supplied to an ammonia decomposition device, and the amount of steam supplied to the production process, such that a decrease in the load of the boiler is suppressed.

電気化学触媒用複合体およびその調製方法

Nº publicación: JP2026002777A 08/01/2026

Solicitante:

ハイドロライザードゥ

Resumen de: CA3273968A1

5 10 15 20 25 30 35 Abstract The present invention relates to a method of preparing a composite material, in particular one useful as a catalyst in an electrolytic hydrogen evolution reaction and/or the oxygen evolution reaction and/or urea oxidation-assisted water electrolysis. Provided is a method of preparing a composite material, the method comprising the steps of: (i) electrochemically depositing material onto a substrate from a deposition solution comprising a nickel (II) salt and graphene oxide, to obtain a nickel-reduced graphene oxide composite material comprising nickel dispersed on reduced graphene oxide, said composite material being deposited on the substrate; (ii) after step (i), placing the substrate, having the nickel-reduced graphene oxide composite deposited thereon, in an alkaline solution along with a counter electrode; and (iii) after step (ii), partially electrochemically oxidising the nickel, to obtain a partially oxidised nickel-reduced graphene oxide composite material comprising partially oxidised nickel dispersed on reduced graphene oxide, said composite material being deposited on the substrate. The composite of the invention demonstrates high catalytic activity for electrolytic hydrogen production under alkaline water electrolysis conditions (for example, a hydrogen evolution current of up to 500 mA cm-2 at -1.35 V against a Reversible Hydrogen Electrode). High activity is demonstrated even when the substrate (on which the composite is deposited)