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Boîte chaude comprenant des empilements de plaques pour électrolyseur à oxyde solide (SOEC) ou pour système de pile à combustible (SOFC) uniformément alimentés, et installation associée

Resumen de: FR3160823A1

L’invention concerne une boîte chaude (1) de stacks (2) d’électrolyse haute température réversible SOEC/SOFC, comportant une cuve (10) accueillant au moins deux stacks, une entrée (14) et une sortie (15) par laquelle des premier et second fluides (32) peuvent entrer et être évacués, ladite boîte chaude comportant en outre une première conduite d’amenée (6) d’un troisième fluide dans chacun desdites au moins deux stacks (2), qui s’étend depuis l’extérieur de ladite cuve jusqu’à un arbre central (60). La boîte chaude comprend des sous-conduites (61) de répartition dudit troisième fluide, qui s’étendent chacune depuis l’arbre central de distribution jusqu’à une entrée d’un stack, lesdits au moins deux stacks étant positionnés à égale distance dudit arbre central. La boîte chaude comprend également des canaux d’évacuation (62) qui s’étendent depuis le fond de chacun des stacks, jusqu’à une seconde conduite d’évacuation qui collecte un quatrième fluide et qui l’évacue hors de ladite cuve. Figure pour l’abrégé : Fig. 1

電解装置および電解方法

Resumen de: AU2025200886A1

An electrolysis device includes: an electrolysis cell; a cathode supply flow path; an anode supply flow path; a cathode discharge flow path; an anode discharge flow path; a cathode flow rate regulator to adjust a flow rate A of a cathode supply fluid; an anode flow rate regulator to adjust a flow rate B of a anode supply fluid; a first flowmeter to measure a 5 flow rate C of a cathode discharge fluid; a second flowmeter to measure a flow rate D of a anode discharge fluid; and a control device to estimate a Faraday efficiency according to a relational expression for approximating the Faraday efficiency to a function including the C and D, and control the cathode flow rate regulator according to the estimated Faraday efficiency to control the A. 10 An electrolysis device includes: an electrolysis cell; a cathode supply flow path; an anode supply flow path; a cathode discharge flow path; an anode discharge flow path; a cathode flow rate regulator to adjust a flow rate A of a cathode supply fluid; an anode flow 5 rate regulator to adjust a flow rate B of a anode supply fluid; a first flowmeter to measure a flow rate C of a cathode discharge fluid; a second flowmeter to measure a flow rate D of a anode discharge fluid; and a control device to estimate a Faraday efficiency according to a relational expression for approximating the Faraday efficiency to a function including the C and D, and control the cathode flow rate regulator according to the estimated Faraday 10 efficiency to c

アンモニア分解用触媒及びこの製造方法

Resumen de: CN120225279A

The invention relates to a catalyst for ammonia decomposition and a preparation method thereof. More specifically, the present invention relates to a catalyst for ammonia decomposition, a method for preparing the same, and a method for ammonia decomposition using the same, the catalyst for ammonia decomposition comprising an MgAl2O4 spinel carrier and ruthenium, the ruthenium content being 0.1-5 wt% based on the total catalyst weight.

アンモニアを分解するためのプロセス及び装置

Resumen de: AU2025201947A1

In a process in which ammonia is cracked to form a hydrogen gas product and an offgas comprising nitrogen gas, residual hydrogen gas and residual ammonia gas, residual ammonia is recovered from the offgas from the hydrogen recovery process by partial condensation and phase separation, and hydrogen is recovered from the resultant ammonia-lean offgas by partial condensation and phase separation. The recovered ammonia may be recycled the cracking process and the recovered hydrogen may be recycled to the hydrogen recovery process to improve hydrogen recovery from the cracked gas. Overall hydrogen recovery from the ammonia may thereby be increased to over 99%. In a process in which ammonia is cracked to form a hydrogen gas product and an offgas comprising nitrogen gas, residual hydrogen gas and residual ammonia gas, residual ammonia is recovered from the offgas from the hydrogen recovery process by partial condensation and phase separation, and hydrogen is recovered from the resultant ammonia-lean offgas by partial condensation and phase separation. The recovered ammonia may be recycled the cracking process and the recovered hydrogen may be recycled to the hydrogen recovery process to improve hydrogen recovery from the cracked gas. Overall hydrogen recovery from the ammonia may thereby be increased to over 99%. ar a r n a p r o c e s s i n w h i c h a m m o n i a i s c r a c k e d t o f o r m a h y d r o g e n g a s p r o d u c t a n d a n o f f g a s c o m p r i s i n g n i t r o

水電解スタック

Resumen de: US2025297392A1

A water electrolysis stack includes: a membrane electrode assembly including an electrolyte membrane and a plate-shaped current collector provided on one of both sides of the electrolyte membrane in the thickness direction thereof; a water introduction unit for introducing water from the outside; a water flow path member disposed so as to face the current collector and provided with a water flow path for guiding, along the surface direction of the current collector, the water introduced into the water introduction unit; and a pumping unit for pumping the water to the water introduction unit. The pumping unit continuously changes the pumping amount of the water, thereby pulsating the water flowing through the water flow path along the surface direction of the current collector.

状態診断システム、状態診断方法、および電解システム

Resumen de: AU2025200754A1

A diagnosis system of an electrolysis device, includes: a device to output an impedance data indicating a measurement result of a complex impedance; a first memory unit to store prior data including a relation data indicating a relation between state of the device and a diagnosis result of a state of the device; a first processing unit to analyze the 5 impedance data, judge validity of an analysis result, and output an analysis data indicating the analysis result in which data indicating at least a part of a frequency region of the measurement result is determined valid; a second processing unit to output a state data indicating the state based on first data including the analysis data; a second memory unit to store second data including the state data; and a third processing unit to output a diagnosis 10 data based on data including the prior data and the second data. A diagnosis system of an electrolysis device, includes: a device to output an impedance data indicating a measurement result of a complex impedance; a first memory unit to store prior data including a relation data indicating a relation between state of the 5 device and a diagnosis result of a state of the device; a first processing unit to analyze the impedance data, judge validity of an analysis result, and output an analysis data indicating the analysis result in which data indicating at least a part of a frequency region of the measurement result is determined valid; a second processing unit to output a sta

INTEGRATED SYSTEM FOR CH4 AND NH3 SYNTHESIS

Resumen de: WO2025207369A1

The disclosure presents an integrated system consisting of a wastewater production unit, e- methane reactor, an electrolyzer for producing hydrogen, a cryogenic separation unit and an ammonia production unit, where e-methane is produced by reaction of carbon dioxide obtained from direct air capture/biogenic CCh/captured industrial CO2 emissions/oxidized solid carbon, and from CO2 separated from biogas obtained from wastewater treatment, and hydrogen gas from electrolysis of water. The hydrogen gas is also reacted with nitrogen obtained from the cryogenic unit for the synthesis of ammonia, where heat from ammonia synthesis is transferred to e-methane reactor for energy efficiency. By integrating these units and reactors, the disclosure provides a system for efficient use of energy and by-products.

HYDROGEN GAS GENERATION SYSTEM

Resumen de: AU2024245597A1

A hydrogen gas production system includes a first electrode having an electrocatalyst, a second electrode having an electron donor material including a plurality of active sites, the second electrode being structured to release electrons from the active sites in a predetermined operating potential range lower than an operating potential triggering oxygen evolution reaction; a first electrolyte in contact with the first and second electrodes, the electrolyte being a source of hydrogen protons; and a power source structured to provide the predetermined operating potential range to the system for the release and transfer of the electrons from the second electrode to the first electrode such that the hydrogen protons combine with the electrons to generate hydrogen gas.

METHOD FOR MANUFACTURING CATALYST FILM FOR WATER ELECTROLYSIS CELL AND APPARATUS FOR MANUFACTURING CATALYST FILM

Resumen de: WO2025204163A1

Provided is a method for manufacturing a catalyst film for a water electrolysis cell, said method including: (1) a step for forming a metal-iridium-containing first film on a substrate by sputtering using a metal-iridium-containing target in a first space; and (2) a step for moving the substrate into a second space that contains oxygen plasma, oxidizing the first film, and forming an indium-oxide-containing first oxide film.

HYDROGEN PRODUCTION SYSTEM AND HYDROGEN PRODUCTION METHOD

Resumen de: WO2025204109A1

The purpose of the present invention is to improve the energy efficiency of a hydrogen production system as a whole. A hydrogen production system (1) produces hydrogen. The hydrogen production system (1) is provided with: an SOEC (10) that is supplied with an oxidizing gas and steam and generates hydrogen by electrolyzing the supplied steam; a steam generation unit (20) that generates the steam supplied to the SOEC (10) by heating feed water; and a power supply device (40) that supplies power to the SOEC (10) so that the SOEC (10) operates at an operation point exceeding a thermal neutral point. The steam generation unit (20) uses heat generated in the SOEC (10) to heat the feed water, and generates the steam without using heat supplied from outside of the hydrogen production system (1).

METHODS FOR PRODUCING INDUSTRIAL GASES AND CAPTURING CARBON OXIDE USING FERROUS IRON-CONTAINING MATERIALS

Resumen de: WO2025207367A1

Described are methods for producing industrial gases (e.g., hydrogen, ammonia, and/or methane) using ferrous iron-containing materials (e.g., olivine) while concurrently sequestering carbon dioxide. The process may involve mixing a ferrous iron-containing material with water and, in some examples, a reaction accelerant. The mixture may be heated to 100-300°C to initiate the oxidation of ferrous cations (Fe2+) to ferric cations (Fe3+) while reducing hydrogen (from water) and/or methane (from water and carbon dioxide, when carbon dioxide is introduced into the ferrous iron-containing mixture). In some examples, carbon dioxide may be added later (after recovering hydrogen) to form carbonates. Specifically, carbon dioxide may be injected at a high pressure (e.g., about 200 bar) post-oxidation to facilitate mineralization, using the exothermic reaction to maintain a favorable temperature. In some examples, metal complexing/chelating reagents are added to bind trace metals such as nickel, copper, cobalt, and platinum group metals for recovery.

ELECTROLYSIS MODULE COOLING METHOD AND ELECTROLYSIS SYSTEM

Resumen de: WO2025204074A1

Provided are an electrolysis module cooling method and an electrolysis system capable of reducing an atmospheric temperature inside a container. Provided is a cooling method for an electrolysis module (200) comprising: at least one electrolysis cartridge (220) that includes an electrolysis cell and generates hydrogen by electrolyzing water vapor generated from water supply; and a pressure vessel (210) that accommodates the electrolysis cartridge (220). In the method for cooling the electrolysis module (200), the air is subjected to heat exchange with water supply in order to heat the water supply, and the heat-exchanged air is supplied to the pressure vessel (210) to cool the inside of the pressure vessel (210).

METHANE PRODUCTION REACTOR

Resumen de: WO2025205989A1

Provided is a methane production reactor that exhibits excellent methane yield. A methane production reactor according to an embodiment of the present invention has gas flow paths to which a raw material gas containing ammonia and carbon dioxide is supplied. The methane production reactor comprises: a honeycomb-shaped base material including partition walls that define a plurality of cells, at least some of the plurality of cells including the gas flow paths; and catalyst-containing layers provided on the surfaces of the partition walls so as to face the gas flow paths, the catalyst-containing layers being capable of promoting a reaction for generating methane from the raw material gas.

REACTOR

Resumen de: WO2025205988A1

Provided is a reactor used for a process involving two or more elementary reactions, namely an exothermic reaction and an endothermic reaction, the reactor having excellent reaction efficiency and reduced catalyst degradation. A reactor according to an embodiment of the present invention is used in a process involving two or more elementary reactions, namely an exothermic reaction and an endothermic reaction. The reactor comprises: a gas channel into which a feedstock gas containing a first component and a second component is supplied; and a catalyst-containing part disposed so as to be capable of contacting the feedstock gas supplied to the gas channel. The catalyst-containing part includes an endothermic reaction promoting catalyst capable of promoting an endothermic reaction related to the first component and an exothermic reaction promoting catalyst capable of promoting an exothermic reaction between the reaction product of the first component and the second component. The dispersion ratio of the exothermic reaction promoting catalyst calculated in a cross-sectional analysis of the catalyst-containing part is 0.60 or more.

ELECTROLYSIS CELL AND ELECTROLYSIS DEVICE

Resumen de: WO2025203905A1

In an electrolysis cell according to the present disclosure, an insulating packing material has: an annular packing body; an arc-shaped packing material having an arc shape formed inside the packing body and surrounding a first supply hole and a first discharge hole from the outer peripheral side, respectively; and a triangular packing material. In the arc-shaped packing material, which is in a state prior to elastic deformation by being sandwiched between a separator and an anion exchange membrane, the thickness of the arc-shaped packing material is set to be greater than the gap between a first diffusion guide part and the anion exchange membrane, and in the triangular packing material, the thickness thereof is set to be greater than that of the packing body.

Anordnung elektrochemischer Zellen und Verfahren zum Betrieb eines Stapels elektrochemischer Zellen

Resumen de: DE102024108733A1

Eine Anordnung (1) elektrochemischer Zellen (2), insbesondere Elektrolysezellen, umfasst eine mehrere, jeweils in einem Zylinder (15, 16) geführte Kolben (18) aufweisende hydraulische Kompressionsvorrichtung (7), welche zur Ausübung einer Druckkraft auf die gestapelten Zellen (2) ausgebildet ist. Die Zylinder (15, 16) sind durch mindestens eine zum Druckausgleich vorgesehene Querverbindung (12, 13) miteinander verbunden.

Vorrichtung und Verfahren zur Herstellung von Wasserstoff

Resumen de: DE102024108849A1

Die Erfindung betrifft eine Vorrichtung zur Herstellung von Wasserstoff mittels eines Elektrolyseurs (1), wobei dem Elektrolyseur (1) Wasser aus einer Wassererzeugungsvorrichtung (6) zugeführt wird, wobei die Wassererzeugungsvorrichtung (6) Mittel zum Entziehen und Verflüssigen der Feuchtigkeit der Umgebungsluft (5), insbesondere in Form eines Wärmetauschers der die Feuchtigkeit der Umgebungsluft kondensieren lässt, aufweist, wobei die Energie der Abwärme (2) des Elektrolyseurs (1) der Umgebungsluft (5) vor dem Feuchtigkeitsentzug zugeführt wird, um diese zu erwärmen.

IMPROVED SYNGAS PRODUCTION WITH IMPROVED INTEGRATED HYDROGEN PRODUCTION

Resumen de: WO2025201610A1

The invention relates to a method for producing syngas from carbonaceous feedstock comprising two or more different compositions of carbonaceous material (e.g. plastics, textiles, biomass, organic matter, natural gas, biogas, carbon dioxide, waste gases), the method comprising: Gasification of the waste feedstock by feeding the feedstock into a primary reaction zone, hereby generating a first output stream; Feeding the first output stream from the first reactor into a secondary reaction zone hereby generating a second output stream; Feeding the second output stream into a cleaning and conditioning reaction zone, hereby generating a third output stream Feeding the third output stream from the cleaning and conditioning reaction zone into a product synthesis reaction zone hereby generating a fourth output stream; Separating the fourth output stream from the product reaction into a fifth liquid crude product stream which is sent for further treatment (e.g., distillation) and at least a sixth and a seventh gas stream; At least part of the sixth gas stream is recycled to the product synthesis reaction zone; At least part of the seventh gas stream is looped back to the primary reaction zone for further conversion; Gasification parameters for the first and the second reaction zones are controlled to take into account the composition and amount of the recycled gas streams; and Providing a solid oxide electrolysis system (SOEC) to create a hydrogen and oxygen input to the process; Prov

ARRANGEMENT OF ELECTROCHEMICAL CELLS AND METHOD OF OPERATING A STACK OF ELECTROCHEMICAL CELLS

Resumen de: WO2025201590A1

An arrangement (1) of electrochemical cells (2), in particular electrolysis cells, comprises a hydraulic compression device (7) which has a plurality of pistons (18) each guided within a cylinder (15, 16) and which is designed to exert a compressive force on the stacked cells (2). The cylinders (15, 16) are connected to one another by at least one transverse connection (12, 13) provided for pressure equalization.

BYPASSABLE CIRCUITRY ARRANGEMENTS FOR ELECTROLYZERS WITH BYPASSABLE BIPOLAR PLATES

Resumen de: WO2025202430A1

Various examples are directed to an electrolyzer system comprising an electrolyzer stack and a control circuit. The electrolyzer stack may comprise a first bipolar plate, a second bipolar plate parallel to the first bipolar plate and a third bipolar plate parallel to the second bipolar plate. The electrolyzer stack may further comprise a first switch electrically coupled between the first bipolar plate and the second bipolar plate to selectively electrically couple the first bipolar plate and the second bipolar plate, and a second switch electrically coupled between the first bipolar plate and the second bipolar plate to selectively electrically coupled the second bipolar plate and the third bipolar plate. The controller circuit may be configured to actuate the first switch to electrically couple the first bipolar plate and the second bipolar plate.

MODULAR ASSEMBLY FOR A SOLID OXIDE ELECTROLYSIS SYSTEM

Resumen de: WO2025202210A1

The invention relates to a modular assembly for a solid oxide electrolysis system for producing hydrogen. The assembly comprises at least one module (1) comprising at least one stack (2) of solid oxide plates positioned in a heat chamber (3), pipes for supplying fluids into the stack (2), pipes for discharging fluids from the stack (2), and at least one fluid-heating device allowing the fluid to reach a temperature that is compatible with the operation of the stack (2). The module (1) comprises a first removable part (10) provided with first connectors (4) for fluid pipes, which part comprises the stack (2) of solid oxide plates positioned in the heat chamber (3), and a second fixed part (11) provided with second connectors (5) capable of being connected to and disconnected from the first connectors (4). The second fixed part (11) comprises a distribution network (13) comprising the fluid supply pipes (14) and fluid discharge pipes (15).

HOT BOX COMPRISING UNIFORMLY POWERED STACKS OF PLATES FOR SOLID OXIDE ELECTROLYZER (SOEC) OR FOR FUEL CELL SYSTEM (SOFC), AND ASSOCIATED INSTALLATION

Resumen de: WO2025202201A1

The invention relates to a hot box (1) of reversible high-temperature SOEC/SOFC electrolysis stacks (2), comprising a tank (10) accommodating at least two stacks, an inlet (14) and an outlet (15) through which first and second fluids (32) can enter and be discharged, said hot box further comprising a first supply pipe (6) for supplying a third fluid to each of said at least two stacks (2), and which extends from outside said tank to a central shaft (60). The hot box comprises sub-pipes (61) for distributing said third fluid, these each extending from the central distribution shaft to an inlet of a stack, said at least two stacks being positioned at equal distances from said central shaft. The hot box also includes discharge channels (62) which extend from the bottom of each of the stacks, to a second discharge pipe that collects a fourth fluid and discharges it out of said tank.

GASEOUS-SUBSTANCE PYROLYSIS APPARATUS AND GASEOUS-SUBSTANCE PYROLYSIS APPARATUS STACK

Resumen de: WO2025206204A1

Problem To provide a gaseous-substance pyrolysis apparatus and a gaseous-substance pyrolysis apparatus stack that have high heat transfer efficiency, high temperature controllability in a catalyst layer, low pressure loss, a small size, and a low heat capacity. Solution A gaseous-substance pyrolysis apparatus 100 comprises: a heat transfer substrate structure 10; a spray catalyst carrier 12 formed on one main surface of the heat transfer substrate structure 10; a catalyst material 14 supported by the spray catalyst carrier 12, the catalyst material 14 breaking down at least some of a gaseous substance using heat energy from the heat transfer substrate structure 10; and a casing 16 covering the heat transfer substrate structure 10, the spray catalyst carrier 12, and the catalyst material 14, the casing 16 forming a space through which the gaseous substance passes. Additionally, this gaseous-substance pyrolysis apparatus stack is formed by stacking a plurality of layers of the aforementioned gaseous substance pyrolysis apparatus 100.

SEPARATOR FOR HYDROGEN PRODUCTION, ALKALINE WATER ELECTROLYSIS MEMBER USING SAME, ALKALINE WATER ELECTROLYSIS CELL USING SAME, ALKALINE WATER ELECTROLYSIS DEVICE USING SAME, METHOD FOR PRODUCING HYDROGEN USING SAME, AND METHOD FOR PRODUCING SEPARATOR FOR HYDROGEN PRODUCTION

Resumen de: WO2025205502A1

Provided are: a separator for hydrogen production, the separator containing a woven fabric support and a porous material that contains an organic polymer, wherein the calender ratio of the woven fabric support calculated by the formula below is 73% or less; an alkaline water electrolysis member, an alkaline water electrolysis cell, an alkaline water electrolysis device, and a method for producing hydrogen, each using the same; and a method for producing a separator for hydrogen production.　Calender ratio = (d2/(2 × d1)) × 100% In the formula, d1 represents the fiber diameter of the woven fabric support, and d2 represents the thickness of the woven fabric support.

POROUS SEPARATOR FOR ALKALINE WATER ELECTROLYSIS, ALKALINE WATER ELECTROLYSIS MEMBER USING SAME, ALKALINE WATER ELECTROLYSIS CELL, ALKALINE WATER ELECTROLYSIS DEVICE, AND HYDROGEN PRODUCTION METHOD

Nº publicación: WO2025205501A1 02/10/2025

Solicitante:

FUJIFILM CORP [JP]
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