Resumen de: WO2025231966A1
Disclosed in the present invention are a titanium alloy bipolar plate with a high pitting potential and a low resistivity and a preparation method therefor. The titanium alloy bipolar plate comprises the following components in percentages by mass: 3.0-5.0% of Mo, 0.1-0.3% of Ni, 0.005-0.05% of Ru and the balance being Ti, and the total content of impurity elements (Fe, O, C, N and H) does not exceed 0.01%. According to the titanium alloy bipolar plate of the present invention, on the basis of meeting the electrical conductivity requirement, the pitting potential of the titanium alloy bipolar plate can be improved, such that the problems of a relatively poor corrosion resistance and a low hydrogen production efficiency caused due to the relatively low pitting potential of the titanium alloy bipolar plate in a service environment of a water electrolysis hydrogen production electrolytic bath are fundamentally solved.
Resumen de: US2025347005A1
The present invention relates to a method for the combined electrolytic and thermal production of hydrogen gas, the method comprising: (i) providing a plasma treatment unit having a plasma treatment chamber comprising first and second electrodes, and a first gas outlet in fluid communication with said plasma treatment chamber; wherein a base portion of the plasma treatment chamber forms a reservoir of an aqueous electrolyte; wherein the first electrode is comprised within a plasma torch whereby the plasma torch is arranged at a distance above a surface of the reservoir; and wherein the second electrode is submerged in the aqueous electrolyte; (ii) establishing a DC electric potential between the first and second electrodes whilst providing a flow of non-oxidising ionisable gas between the first electrode and the surface of the reservoir to generate and sustain a plasma arc therebetween, thereby producing hydrogen gas in the plasma treatment chamber; and (iii) recovering the hydrogen gas via the first gas outlet. The present invention also relates to a plasma treatment unit.
Resumen de: US2025347014A1
A photoelectrode includes a fluorine-doped tin oxide (FTO) substrate, and a layer of graphitic-poly(2,4,6-triaminopyrimidine) (g-PTAP) nanoflakes at least partially covering a surface of the FTO substrate. Further, the g-PTAP nanoflakes have a width of 0.1 to 5 micrometers (μm). In addition, a method for producing the photoelectrode, and a method for photocatalytic water splitting, in which the photoelectrode is used.
Resumen de: US2025347008A1
An electrolysis plant includes at least one electrolysis module. The electrolysis module has a plurality of series-connected electrolysis cells. A DC-capable switching device is connected electrically in parallel and has an activatable power resistor such that, in the closed state, a current path through the power resistor can be activated so as to bypass electrolysis cells and to be able to drain excess power through the power resistor. There is also described a method for operating such an electrolysis plant for separating water into hydrogen and oxygen, and to a combination with an electrolysis plant that is connected directly to a wind turbine.
Resumen de: US2025347015A1
The present application relates to components for use in an electrolysis cell and/or stack comprising features, geometry, and materials to overcome prior art limitations related to cell electrical isolation, fluid sealing, and high speed manufacturing. The electrolysis cell comprises a membrane, an anode, a cathode, an anode flow field, a cathode flow field, and a bipolar plate assembly comprising an embedded hydrogen seal and both conductive and non-conductive areas. The components are cut using two-dimensional patterns from substantially flat raw materials capable of being sourced in roll form. These substantially two-dimensional components are processed to create a fully unitized, three-dimensional electrolysis cell with a hermetically sealed cathode chamber.
Resumen de: US2025347013A1
A photoelectrode includes a fluorine-doped tin oxide (FTO) substrate, and a layer of graphitic-poly(2,4,6-triaminopyrimidine) (g-PTAP) nanoflakes at least partially covering a surface of the FTO substrate. Further, the g-PTAP nanoflakes have a width of 0.1 to 5 micrometers (μm). In addition, a method for producing the photoelectrode, and a method for photocatalytic water splitting, in which the photoelectrode is used.
Resumen de: US2025347011A1
An electrode includes a bimetallic ruthenium-cobalt (RuCo) alloy electrocatalyst having a metallic substrate and a layer of a RuCo alloy at least partially covering the surface of the metallic substrate. The layer of the RuCo alloy includes spherical-shaped particles having an average particle size of 0.5 to 5 micrometers (μm). The electrode can be used for electrochemical water splitting applications to generate hydrogen and water.
Resumen de: US2025347010A1
A method of making NiO nanoparticles is described, as well as a method of using NiO nanoparticles as an electrocatalyst component to a porous carbon electrode. The carbon electrode may be made of carbonized filter paper. Together, this carbon-supported NiO electrode may be used for water electrolysis. Using a pamoic acid salt in the NiO nanoparticle synthesis leads to smaller and monodisperse nanoparticles, which support higher current densities.
Resumen de: WO2025233819A1
An AEM electrolyzer comprises end structural elements (20, 30) and an electrolytic structure (22) comprising a plurality of electrolytic cells (40) to which are associated respective structural support and sealing assemblies (50) completely made of elastomeric material and in which are obtained portions of anode side inlet channels (23) and outlet channels (24) and of cathode side inlet channels (25) and outlet channels (26), while a pressurizable chamber is obtained between at least one of the end elements (20, 30) and the electrolytic structure (22) to compensate the gas pressure in the electrolytic structure itself. An AEM electrolyzer is obtained with reduced production costs and high electrical efficiency.
Resumen de: WO2025233484A1
An apparatus (1) for generating hydrogen, the apparatus (1) comprising a housing (10) containing a first electrode (11) and a second electrode (12), each of the first electrode (11) and second electrode (12) being for submersion within water located within the housing (10), the first electrode (11) surrounding the second electrode (12), wherein the first electrode (11) is of cylindrical form and the second electrode (12) is of at least part-conical or frusto-conical form.
Resumen de: WO2025233816A1
An AEM electrolyzer comprises structural end elements (20, 30) and an electrolytic structure (22) comprising a plurality of electrolytic cells (40) to which respective gasket assemblies (50) completely made of elastomeric material are associated and in which portions of anode side inlet channels (23) and outlet channels (24) and of cathode side inlet channels (25) and outlet channels (26) are obtained, while a pressurisable chamber is obtained between at least one of the end elements (20, 30) and the electrolytic structure (22) to compensate for the gas pressure in the electrolytic structure itself. An AEM electrolyzer is obtained with reduced production costs and high electrical efficiency.
Resumen de: KR20250160293A
본 발명의 일 실시예에 따른 암모니아를 이용한 메탄올 생산 방법은, a) 선박에 저장된 암모니아가 접안 부두에 정차된 탱크로리로 운송 및 저장되는 단계; b) 상기 탱크로리에 저장된 암모니아의 일부가 친환경 연료로서 발전소로 공급된 후에 상기 발전소의 발전에 사용되는 단계; c) 상기 발전소가 암모니아를 기반으로 발전하는동안 생성되는 이산화탄소를 포집, 분리 및 액화시킨 후 저장하는 단계; d) 상기 발전소로 공급되지 않고 상기 탱크로리에 남은 나머지 암모니아가 수소 생산소로 운송되며, 상기 수소 생산소에서 수소와 질소로 분해됨으로써 수소를 생산하는 단계; 및 e) 메탄올 생산소가 상기 c) 단계에서 저장된 이산화탄소와, 상기 d) 단계에서 생산된 수소를 이용하여 메탄올을 생산하는 단계;를 포함할 수 있다.
Resumen de: EP4647532A2
The present disclosure advantageously provides an improved cooling system for an electrochemical plant. The configurations disclosed herein provide advantages and improvements in a cooling system for the electrochemical plant. The cooling system advantageously cools multiple subsystems within the plant using dry coolers, thereby easing maintenance and access to various components within the plant, minimizing or reducing the amount of process piping within the plant used to cool the multiple subsystems, and reducing the complexity of the overall plant.
Resumen de: AR133932A2
En esta divulgación, se introduce un proceso de reciclado de ácido, base y los reactivos de sal requeridos en el proceso de recuperación de Li. Se implementa una celda electrolítica de membrana que incorpora un cátodo de oxígeno despolarizado para generar los productos químicos requeridos en el sitio. El sistema puede utilizar una porción de la salmuera de salares u otra salmuera o residuo sólido que contiene litio para generar ácido clorhídrico o sulfúrico, hidróxido de sodio y sales de carbonato. La generación simultánea de ácido y base permite tomar ventaja de ambos productos químicos durante la recuperación convencional de Li de salmueras y rocas minerales. El agua desalinizada también se puede usar en los pasos de lavado en el proceso de recuperación o regresar a los estanques de evaporación. El método también se puede usar para la conversión directa de sales de litio en el producto LiOH con alto valor. El método no produce ningún efluente sólido lo cual lo torna de fácil adopción para su uso en las plantas industriales de recuperación de Li existentes.
Resumen de: AR133930A2
En esta divulgación, se introduce un proceso de reciclado de ácido, base y los reactivos de sal requeridos en el proceso de recuperación de Li. Se implementa una celda electrolítica de membrana que incorpora un cátodo de oxígeno despolarizado para generar los productos químicos requeridos en el sitio. El sistema puede utilizar una porción de la salmuera de salares u otra salmuera o residuo sólido que contiene litio para generar ácido clorhídrico o sulfúrico, hidróxido de sodio y sales de carbonato. La generación simultánea de ácido y base permite tomar ventaja de ambos productos químicos durante la recuperación convencional de Li de salmueras y rocas minerales. El agua desalinizada también se puede usar en los pasos de lavado en el proceso de recuperación o regresar a los estanques de evaporación. El método también se puede usar para la conversión directa de sales de litio en el producto LiOH con alto valor. El método no produce ningún efluente sólido lo cual lo torna de fácil adopción para su uso en las plantas industriales de recuperación de Li existentes.
Resumen de: EP4647534A1
Eine Plattenanordnung (1) eines Stapels elektrochemischer Zellen (2) umfasst ein zumindest teilweise als 3D-Druck-Element ausgebildetes Plattenelement (3), in welchem mehrere Schichten (6, 7, 8) parallel zueinander angeordnet sind, die jeweils durchbrochene, zur Durchleitung eines Fluids geeignete Strukturen aufweisen, wobei die Feinheit der Durchbrechungen (17) von Schicht (6, 7, 8) zu Schicht (6, 7, 8) variiert, und wobei ein Temperatursensor (19), der an ein Kabel (20) angeschlossen ist, welches durch mehrere der genannten Schichten (6, 7, 8) verläuft, an diejenige Schicht (8) grenzt, welche die feinsten Durchbrechungen (17) aufweist.
Resumen de: EP4647161A1
The present disclosure relates to a catalyst for decomposition of ammonia and a method for decomposition of ammonia.
Resumen de: WO2024129657A1
The present invention provides a device for carbon dioxide recovery from alkaline water using a module having at least three compartments where each compartment is separated by an electrode pair (anode and cathode) with electrochemical reactions occurring at the electrodes. The electrodes can be in a unipolar or bipolar configuration. Multiple electrochemical modules can be electrically connected in series, in parallel, or in a combination of both series and parallel. Also disclosed it the related process for recovering carbon dioxide from alkaline water.
Resumen de: CN120226171A
The present disclosure relates to an electrochemical cell stack comprising solid state electrochemical cells (20), an electrically conductive separator (30); and a sealing element (40). The separator comprises: a central portion (31) having an oppositely recessed support surface (32) supporting the solid oxide cell, and a contact surface (34) opposite the recessed support surface contacting an adjacent solid state electrochemical cell; and a boundary portion (36) providing a relatively elevated top (37) and upstanding side walls (38). A sealing element (40) extends between an elevated top surface of the boundary portion and an opposing support surface (39) of an adjacent bulkhead. The spacing distance between the concave support surface and the contact surface of the adjacent separator, defined by the combined height of the sealing element and the upstanding side wall, is matched to the thickness of the solid state electrochemical cell.
Resumen de: AU2025202385A1
The present invention is an adhesive-fixed electrolysis module comprising a single stack, the single stack having a separator, a pair of bipolar plates, a pair of gaskets, a pair of diffusion layers, a pair of electrodes, and a cell frame, wherein the bipolar plates, the gaskets, 5 the diffusion layers, and the electrodes are sequentially arranged on the cathode and anode sides, respectively, with respect to the separator, forming a symmetrical structure, wherein the separator, the bipolar plates, the gaskets, the diffusion layers, and the electrodes are stacked in a zero-gap manner within the cell frame, and wherein the bipolar plates are adhered and fixed to the cell frame using an adhesive, thereby simplifying product assembly 10 and reducing assembly costs compared to a single stack fixing method using welding, riveting, bolting, etc. between conventional parts. The present invention is an adhesive-fixed electrolysis module comprising a single stack, the single stack having a separator, a pair of bipolar plates, a pair of gaskets, a pair of 5 diffusion layers, a pair of electrodes, and a cell frame, wherein the bipolar plates, the gaskets, the diffusion layers, and the electrodes are sequentially arranged on the cathode and anode sides, respectively, with respect to the separator, forming a symmetrical structure, wherein the separator, the bipolar plates, the gaskets, the diffusion layers, and the electrodes are stacked in a zero-gap manner within the cell frame, and wher
Resumen de: JP2025169014A
【課題】水を満遍なく分散させることにより、局所的な温度上昇が生じにくく、水素ガス及び酸素ガスを効率よく発生させやすい水素・酸素発生装置用の電極板と、該電極板を備える水素・酸素発生装置とを提供する。【解決手段】電極板10の一端側に形成された少なくとも一つの水供給孔101aと、電極板10の他端側に形成された少なくとも一つの水排出孔101bと、少なくとも一つの水供給孔101aから供給された水が電極板10に沿って少なくとも一つの水排出孔101bへと流れる途中で通過する領域において、少なくとも一つの水供給孔101aと少なくとも一つの水排出孔101bとを結ぶ仮想直線VSLを基準として、仮想直線VSLの近くには流水に与える抵抗が大きい大抵抗部113を有し、仮想直線VSLから遠くには流水に与える抵抗が小さい小抵抗部114を有する水整流部と、を備える、水素・酸素発生装置用の電極板10である。【選択図】図3
Resumen de: EP4647396A1
There is described a hydrogen production system comprising: a gasification sub-system to produce a syngas stream from a biomass and/or refuse derived fuel feed stream; and a steam methane reformer (SMR) sub-system to produce an SMR syngas stream from a hydrocarbon feed, and to produce a low carbon hydrogen final product by integrating the syngas stream from the gasification sub-system and the SMR syngas stream.
Resumen de: KR20250160290A
본 발명의 일 실시예에 따른 수소 충전 시스템은, 복수의 수소 튜브 트레일러에 수소를 순차적으로 충전하기 위한 수소 충전 시스템에 있어서, 외부로부터 투입되는 물을 분해하여 수소를 생성하는 수전해기; 상기 수전해기에서 생성된 수소를 일시적으로 저장하는 버퍼탱크; 상기 버퍼탱크로부터 배출되는 수소의 압력인 제1 압력값을 측정하는 제1 압력센서; 상기 버퍼탱크로부터 분기된 후 이송되는 수소를 압축시키는 압축기; 상기 압축기로부터 압축되되, 상기 수소 튜브 트레일러에 충전될 수소를 저장하는 저장탱크; 상기 버퍼탱크로부터 분기된 후 상기 압축기를 향하지 않는 수소 또는 상기 압축기에서 압축된 후 상기 저장탱크로 저장되기 전에 우회되는 수소를 내측에 수용하는 수소배관; 상기 수소배관의 내측에 수용된 수소의 압력인 제2 압력값을 측정하는 제2 압력센서; 상기 제1 압력값과 제2 압력값을 이용하여 수소의 이송방향을 제어하는 제어부; 및 상기 복수의 수소 튜브 트레일러에 수소가 충전되도록 상기 저장탱크가 일측에 배치되는 충전 스테이션;을 포함할 수 있다.
Resumen de: AU2024214359A1
Feedwater preparation system in a water electrolyser adapted to produce hydrogen and oxygen in one or more pressurised electrolyser stacks (2) using alkaline water and comprising a product gas conditioning system that has a safety valve out-blow material stream pipe (11) which is connected to a feedwater vessel (9), and/or has a depressurisation stream pipe (31) from a gas cleaning vessel which is connected to the feedwater vessel (9).
Nº publicación: CN120936421A 11/11/2025
Solicitante:
蒂森克虏伯新纪元股份有限及两合公司
Resumen de: AU2024237545A1
A method for generating and treating a two-phase outflow from one or more pressurised electrolyser stacks which are adapted to electrolyse water into hydrogen and oxygen, whereby a pump supplies a catholytic fluid flow from one first gas liquid gravitational separator vessel to the electrolyser stacks and whereby a further pump supplies an anolytic fluid flow from one second gas liquid gravitational separator vessel to the electrolyser stacks, and whereby at least one cyclone type gas liquid separator receives combined outflows from the catholytic chambers and/or receives combined outflows from anolytic chambers respectively inside corresponding gravitational gas liquid separator vessel whereby further, the at least one cyclone type gas liquid separator separates the gas from the liquid along a generally horizontal cyclonic rotation axis inside the gas liquid gravitational separator vessel. An electrolyser system is also provided.