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METHOD OF OPERATING AN ELECTROLYSIS SYSTEM, CONTROL UNIT TO CONTROL AN ELECTROLYSIS SYSTEM, ELECTROLYSIS SYSTEM WITH SUCH A CONTROL UNIT, COMPUTER PROGRAM PRODUCT AND A COMPUTER-READABLE STORAGE MEDIUM

Resumen de: EP4811580A1

Method of operating an electrolysis system (2) where-in the method comprising the steps of:(S100) reading in a signal (S) for a faulty stack (12),(S200) providing a control signal (CS1) in order to bypass the faulty stack (12),(S300) providing a second control signal (CS2) in order to provide a first voltage adapted to the n-1 row (6b) with the faulty stack (12), and(S400) providing a third control signal (CS3) in order to provide a second voltage adapted to the n row (6a) without the faulty stack (12).

POROUS HYDROPHILIC SEPARATOR, ITS METHOD OF PRODUCTION AND AN ALKALINE ELECTROLYZER WITH SUCH SEPARATOR

Resumen de: WO2025103558A1

Porous hydrophilic separator, its method of production, and an alkaline electrolyzer with such separator In an alkaline electrolyzer (12), especially for production of hydrogen gas, the separator (11) has larger pores in layers (8, 9) on its outer sides (7A, 7C), facing the electrodes (13, 14), than in the bulk layer (10). In a practical embodiment, the separator (11) is composed of two diaphragms (7, 7'), each with asymmetric pore structure, where the diaphragms (7, 7') are oriented such that largest pores are on the outer sides of the sep- arator (11).

EXCESS HEAT FROM CO2 ELECTROLYSIS TO GENERATE STEAM TO STEAM ELECTROLYSIS

Resumen de: WO2025104292A1

The invention relates to a system and a method for producing a synthesis gas from a carbon dioxide-rich feed stream and a water feedstock via electrolysis, wherein excess heat from CO2 electrolysis is arranged to generate steam to steam electrolysis. More specifically, a system and a process are provided for production of a synthesis gas stream, said system comprising: a carbon dioxide-rich feed stream; a first H2O-rich feed stream; a first solid oxide electrolysis (SOEC) section; a second solid oxide electrolysis (SOEC) section; and a conversion section. Optimal use of heat energy is achieved by heat transfer from the output of the first SOEC section to the input of the second SOEC section.

CARBON NANOTUBE-SUPPORTED NITROGEN-DOPED CATALYST AND PREPARATION METHOD THEREFOR

Resumen de: EP4810670A1

0001 The present invention relates to the field of hydrogen production by water electrolysis, and discloses a carbon nanotube-supported nitrogen-doped catalyst, wherein the catalyst has a carbon nanotube structure as carrier, with cobalt and ruthenium as active components, wherein the content of cobalt element is 30-45wt%, the content of ruthenium element is 1-7wt%, and relative to all ruthenium elements, the proportion of ruthenium element existing in the form of RuN is 60wt%-90wt%. The graphitic structure of this catalyst is conducive to charge conduction. Ru is uniformly loaded on the carrier surface through low-temperature reduction process and interaction with defect sites on the carrier surface, and then forms interactions with N elements and metallic Co after high-temperature calcining, thereby improving the hydrogen evolution catalytic activity of the catalyst.

ELECTROLYSIS ASSEMBLY AND ELECTROLYSIS METHOD

Resumen de: EP4810657A1

Vorliegend wird eine Elektrolyseanordnung (100) mit einem Elektrolyseblock (10) mit einer Vielzahl von Elektrolysezellen (1-3), die Kathodenkammern (C) und Anodenkammern (A) aufweisen, und mit einem Elektrolytsystem (20), das eine Speiseleitungsanordnung (11), eine kathodenseitige Entnahmeleitungsanordnung (12) und eine anodenseitige Entnahmeleitungsanordnung (13) aufweist, vorgeschlagen. Die Elektrolyseanordnung (100) ist dafür eingerichtet, den Kathodenkammern (C) und den Anodenkammern (A) über die Speiseleitungsanordnung (11) Lauge zuzuführen, den Kathodenkammern (C) über die kathodenseitige Entnahmeleitungsanordnung (12) Lauge und in den Kathodenkammern (C) gebildeten Wasserstoff zu entnehmen, und den Anodenkammern (A) über die anodenseitige Entnahmeleitungsanordnung (13) Lauge und in den Anodenkammern (A) gebildeten Sauerstoff zu entnehmen. In der Speiseleitungsanordnung (11), der kathodenseitigen Entnahmeleitungsanordnung (12) und/oder der anodenseitigen Entnahmeleitungsanordnung (13) ist oder sind ein oder mehrere Durchflussrestriktoren (21-27) bereitgestellt und dafür eingerichtet, einen Durchströmungsquerschnitt in Abhängigkeit von einem Mengenstrom der durch die Elektrolysezellen (1-3) geführten Lauge zu verändern. Ein entsprechendes Verfahren wird ebenfalls vorgeschlagen.

SOLID OXIDE ELECTROLYZER CELL AND USE OF SAME

Resumen de: EP4810669A1

0001 Provided is a technique capable of suppressing lowering of current density, while suppressing separation at the interface between an air electrode and a solid electrolyte layer, during use of a solid oxide electrolysis cell. The solid oxide electrolysis cell includes an air electrode, a fuel electrode, and a solid electrolyte layer disposed between the air electrode and the fuel electrode. The air electrode contains: a complex oxide having a perovskite structure represented by a general formula ABO<3>; and ZrO<2>. The ZrO<2> content of the air electrode is 1×10<-3> mass% or greater and 5×10<-1> mass% or less with respect to the entire air electrode.

电解池堆、电解池盒、电解池模块及电解池堆的制造方法

Resumen de: WO2025220485A1

The present disclosure provides an electrolytic cell stack capable of increasing the amount of product generated by electrolysis while suppressing a temperature rise of the cell stack. An electrolytic cell stack (101) according to the present disclosure comprises: a hydrogen generation unit (10) provided with an electrolytic cell (105) having a hydrogen electrode, an oxygen electrode, and a solid electrolyte membrane; a raw material gas supply port (11); a hydrogen gas discharge port (12); a raw material gas supply-side heat exchange unit (13); and a hydrogen gas discharge-side heat exchange unit (14). The raw material gas supply-side heat exchange unit and the hydrogen gas discharge-side heat exchange unit are each composed of a heat transfer unit and a header unit. The heat transfer unit area of the hydrogen gas discharge-side heat exchange unit is larger than the heat transfer unit area of the raw material gas supply-side heat exchange unit.

钌基双氧化物自支撑电极的制备及其析氧反应应用

Resumen de: CN122791421A

本发明涉及清洁能源制备技术领域，具体公开了钌基双氧化物自支撑电极的制备及其析氧反应应用。该方法包括先对钛毡基底进行清洗和碱性水热刻蚀处理，再将刻蚀后的钛毡置于含有钌前驱体盐和铈前驱体盐的酸性混合溶液中进行水热反应，得到Ce‑RuO2自支撑电极。本发明通过将稀土元素Ce原位掺杂引入RuO2晶格中，利用Ce3+/Ce4+的可变价态及其“氧泵”效应，调控催化剂电子结构，优化含氧中间体吸附能，显著提升了析氧催化活性和稳定性。所得电极析氧过电位低，经10000圈加速老化测试后活性基本无衰减。本发明制备方法简单、贵金属用量少、成本低廉，所得电极可直接作为质子交换膜电解水制氢的阳极催化材料，具有良好的工业化应用前景。

层叠体、膜电极接合体、水电解装置及层叠体的制造方法

Resumen de: WO2025183169A1

A laminate according to the present invention comprises a porous metallic body on an electrolyte membrane. Fine metal particles are included at least in pores and/or in the electrolyte membrane-side surface of the porous metallic body. The average pore size of the porous metallic body is preferably 0.5-100 μm. The average particle size of the fine metal particles is preferably 5-200 nm. The thickness of the porous metallic body is preferably 1-500 μm. In addition, a fine metal particle layer is preferably provided between the electrolyte membrane and the porous metallic body. The porous metallic body is preferably a metal foam or a metal fiber mat.

전기화학 시스템을 위한 유체 분리 시스템

Resumen de: WO2025159903A1

A system for separating a fluid in the operation of an electrochemical system includes: a cathode separator configured to separate a fluid into a first stream having hydrogen gas and a second stream having water and dissolved hydrogen; and a makeup water tank. The makeup water tank is configured to: receive the second stream from the cathode separator; operate at a pressure that is greater than atmospheric pressure and less than an operating pressure of the cathode separator; and separate at least a portion of the dissolved hydrogen from the water via a reduction in pressure from the cathode separator to the makeup water tank to provide a purified water stream and hydrogen gas. The hydrogen gas from the makeup water tank is configured to be transferred out of the makeup water tank and the purified water stream is configured to be transferred out the makeup water tank.

一种焦煤源本征Fe调控多孔碳负载Pt的析氢电催化材料及其制备、应用方法

Resumen de: CN122791414A

0001 本发明公开了一种焦煤源本征Fe调控多孔碳负载Pt的析氢电催化材料及其制备、应用方法，涉及电解水制氢催化材料与电催化技术领域。能够满足低成本、高效率碱性析氢。所述析氢电催化材料包括由焦煤经碱活化形成的多孔碳载体以及分布于所述多孔碳载体表面和/或孔壁上的Pt纳米颗粒；所述多孔碳载体保留焦煤源本征Fe相关位点，所述本征Fe相关位点来源于焦煤前驱体天然赋存铁组分并经活化、酸洗和热处理后保留或转化形成，用于促进Pt的成核与分散，并提高Pt的利用效率。解决了现有技术中Pt基析氢催化剂贵金属利用率低、碳载体界面调控能力有限、外加金属修饰工艺复杂的问题。

一种镍基核壳纳米粉末的制备方法及其电解水制氢应用

Resumen de: CN122791419A

本发明公开了一种镍基核壳纳米粉末的制备方法及其电解水制氢应用。所述制备方法基于化学浸渍法，以纳米铁粉或纳米钴粉为反应基底，二价镍离子水溶液为浸渍剂，通过金属活性差异自发驱动电化学置换反应，并在形成的镍核表面原位构筑LDH壳层。该镍基核壳纳米粉末具有一定磁性，可通过磁吸收集。制得的镍基核壳纳米粉末具有纳米金属镍核与层状双金属氢氧化物外壳，且催化剂颗粒呈高分散状态，其作为水氧化催化剂在阴离子交换膜电解水制氢中表现出良好的催化活性和稳定性。

一种三元合金CrRuIr连续网络结构电催化剂及其制备方法和应用

Resumen de: CN122791416A

0001 本发明公开了一种三元合金CrRuIr连续网络结构电催化剂及其制备方法和应用，涉及电催化材料技术领域，本发明提供的制备方法包括以下步骤：将钌、铱、铬的氯化物或乙酰丙酮配合物、沉淀剂与表面活性剂溶于多元醇，经回流、离心、洗涤、烘干得前驱体，再惰性退火。机理上，亲氧Cr引入Lewis酸性位点增强水解离，并在催化剂表面原位构建局部微碱环境抑制Ru溶出。性能测试显示，该催化剂在10mAcm<‑2>下过电位仅198mV；用于PEM电解槽阳极时，在1Acm<‑2>工业级电流密度下可稳定运行超1000小时。本发明为高性能低成本酸性OER催化剂提供了新路径。

基于多元合金修饰的宽幅pH电解水制氢催化剂制备方法

Resumen de: CN122791422A

本发明公开了一种基于多元合金修饰的宽幅pH电解水制氢催化剂制备方法，包括：取多种非贵金属盐与稳定剂配置成不同的混合溶液，将基底膜电极置于其中浸渍煅烧后，在三电极体系下进行通过添加金属离子的自愈合过程，得到负载的合金型电解水制氢催化剂。本发明于多元合金修饰的宽幅pH电解水制氢催化剂制备方法，通过煅烧耦合电活化的方式，在碱性以及中性溶液中均表现出远超传统催化剂的高活性、高稳定性。

碱性电解水制氢用超薄复合隔膜及其制备方法和应用

Resumen de: CN122791426A

本发明属于电解水制氢隔膜技术领域，尤其涉及一种碱性电解水制氢用超薄复合隔膜及其制备方法和应用；所述复合隔膜包括聚苯硫醚(PPS)支撑网以及设置在所述聚苯硫醚支撑网一侧/两侧的多孔涂层；其中，形成所述多孔涂层的铸膜液包括：聚砜树脂、氧化锆纳米颗粒、聚乙烯吡咯烷酮、聚醚胺和有机溶剂。本发明所述复合隔膜的面电阻低、离子透过性好，且力学性能也能很好地满足电解水制氢的需求。

一种扭转应变钨钼镍合金催化剂及其制备方法和应用

Resumen de: CN122787436A

本发明属于功能化材料以及电解海水领域，具体涉及为一种扭转应变钨钼镍合金催化剂及其制备方法和应用。本发明提供的扭转应变钨钼镍合金催化剂的制备方法，包括以下步骤：将镍盐、钼酸盐与水混合，进行水热反应，得到钼酸镍纳米棒前驱体；将所述钼酸镍纳米棒前驱体于保护气体与还原性气体的混合气氛中进行还原反应，得到中间体；将所述中间体与钨盐醇溶液混合进行淬火，得到所述扭转应变钨钼镍合金催化剂。本发明提供的扭转应变钨钼镍合金催化剂能够抗沉淀，具有高活性和耐久性，在工业级电流密度下能够直接电解天然海水。

一种NiCo2S4纳米针阵列催化剂及其应用

Resumen de: CN122791413A

本发明属于电催化技术领域，公开了一种NiCo2S4纳米针阵列催化剂。所述NiCo2S4纳米针阵列通过以下方法制备：对导电基底进行清洗和表面活化预处理；在预处理后的导电基底表面原位生长Ni‑Co前驱体纳米针阵列；将所述Ni‑Co前驱体纳米针阵列进行硫化转化，得到NiCo2S4纳米针阵列。本发明利用纳米针尖端的小曲率半径所产生的尖端效应，增强了局域电场分布和反应界面电荷积累，有利于促进反应物吸附、键活化和电子转移过程，从而提升电催化反应动力学。本发明的制备方法简单、结构可控，可通过调节前驱体生长条件和硫化条件实现纳米针长度、密度及尖端形貌的调控，具有较好的可重复性和放大制备潜力。

电化学反应装置

Resumen de: EP4810663A2

0001 An electrochemical reaction device includes: an electrolysis cell stack including: a plurality of sub-stacks stacked between a pair of clamping plates, each sub-stack including: a plurality of electrolysis cells stacked between a pair of support plates; and at least one fluid manifold completed within one of the plural sub-stacks; a measuring device to measure a physical quantity related to a state of at least one of the plural sub-stacks to acquire physical quantity data; and an information processing unit to process the physical quantity data from the measuring device. Each electrolysis cell includes: a cathode chamber; an anode chamber; a diaphragm between the cathode chamber and the anode chamber; a cathode arranged on the cathode chamber; and an anode arranged on the anode chamber. The pair of support plates includes at least four through holes including an inlet or an outlet of the at least one fluid manifold.

水电解系统

Resumen de: EP4810662A1

A water electrolysis system includes: a power supply unit; a plurality of parallel circuits connected in parallel to the power supply unit; a plurality of water electrolysis stacks disposed in the parallel circuits, respectively; at least one voltage adjustment unit disposed in at least one of the parallel circuits; and a control device configured to control an operation of the at least one voltage adjustment unit. The control device is configured to control the operation of the at least one voltage adjustment unit such that a difference between currents flowing through the water electrolysis stacks is smaller than the difference when the at least one voltage adjustment unit is not operating.

WO3-In2O3/CuO-ZrO2载氧体及其制备方法和应用

Resumen de: CN122787030A

本发明公开了一种WO3‑In2O3/CuO‑ZrO2载氧体及其制备方法和应用，涉及载氧体技术领域。其技术方案包括以下步骤：1）载体CuO‑ZrO2的制备：将ZrO(NO3)2·2H2O、Cu(NO3)2·3H2O溶解于水中，尿素作为沉淀剂，反应，干燥，煅烧，得到双金属氧化物载体CuO‑ZrO2；2）In2O3/CuO‑ZrO2的制备：加入In(NO3)3·4.5H2O，老化，煅烧；得到In2O3/CuO‑ZrO2；3）载氧体WO3‑In2O3/CuO‑ZrO2的制备：加入Na2WO4·2H2O，搅拌，蒸发水得到固体，干燥，煅烧，得到载氧体。本发明实现了NH3分子的高效转化。

流道板及电解装置

Resumen de: CN122791403A

本申请提供一种流道板及电解装置，涉及电解水技术领域，具体技术方案为：流道板包括板体、以及设置于板体上的流道结构，流道结构包括：多个第一流道、流道入口、多个流道出口和多组第二流道，多个第一流道由板体的中心向四周呈发射状延伸；流道入口位于板体的中心，且与多个第一流道连通；多个流道出口与多个第一流道一一对应，且每个流道出口位于对应的第一流道的远离流道入口的一端；相邻的两个第一流道之间设置有一组第二流道，且每组第二流道与相邻两侧的两个第一流道均连通。采用本方案可以使流道板内的流体分布均匀，提高传质效率、减少涡流和气堵风险，并且，该流道板结构简单，有助于降低成本提高生产良率。

稀土元素掺杂的非晶氧化钌催化剂及其制备方法和应用

Resumen de: CN122791423A

0001 本发明属于微纳米材料制备技术领域，具体涉及一种稀土元素掺杂的非晶氧化钌催化剂及其制备方法和应用。本发明提供的制备方法，包括以下步骤：将稀土金属硝酸盐与钌盐混合均匀，得到前驱体；将硝酸锂加热至270‑300℃，得到熔融LiNO<3>；将前驱体加入熔融LiNO<3>中进行反应，反应结束后冷却至室温，将LiNO<3>与产物分离后，即得稀土元素掺杂的非晶氧化钌催化剂。本发明提供的方法通过熔融LiNO<3>提供的富氧环境，同时以熔融盐中的Li<+>辅助合成，不需要精确控制煅烧温度和煅烧时间，就可以稳定得到稀土元素掺杂的非晶氧化钌催化剂。本发明工艺简单、可以大规模生产，制备出的催化剂在电催化析氧反应中表现出较高的活性。

一种Lindqvist型钨钒杂多酸烷氧衍生物及制备方法和应用

Resumen de: CN122789990A

0001 本发明涉及一种Lindqvist型钨钒杂多酸烷氧衍生物及制备方法和应用，其化学式为(C<16>H<36>N)<2>W<3>V<3>O<16>(OCH<2>)<3>CCH<2>OH，由一个金属‑氧簇阴离子W<3>V<3>O<16>(OCH<2>)<3>CCH<2>OH<2‑>和两个四丁基铵阳离子组成。本发明通过简便的溶剂热反应，并控制混合液的pH值在2～3以及反应时间为12～24h，进一步成功合成了一类金属钨钒比例为1:1的Tris‑OH功能化Lindqvist型钨钒杂多酸烷氧衍生物，丰富了钨钒杂多酸的种类，且具有暴露的羟基，有效拓展钨钒杂多酸的后功能化平台。同时，通过该衍生物所制得的析氢电催化剂的催化活性高，而制备成本较低，具备工业应用潜力。

一种碟式光热制氢设备的模块化碟片及支撑龙骨

Resumen de: CN122786929A

0001 本发明涉及制氢设备技术领域，尤其涉及一种碟式光热制氢设备的模块化碟片及支撑龙骨，其技术方案包括固定底座，支撑龙骨，碟片和延伸片，所述固定底座的正面中央位置处固定安装有反射盘；所述固定底座的正面靠近边缘位置处固定安装有若干根支撑龙骨，所述支撑龙骨的前端焊接有固定架，所述支撑龙骨的内侧焊接有若干根安装架；所述安装架的内侧固定安装有若干个碟片。本发明通过采用模块化的反光碟片进行整个蝶式光热制氢设备的搭建，能够在出现局部破损时进行单一碟片的更换，从而提升装置后期维护的便利性，降低设备的维护成本，同时模块化的碟片设计还能降低装置整体的加工、运输和安装难度，减少装置安装过程中的人力物力成本投入。

碱性电解水制氢系统控制方法及装置

Nº publicación: CN122791428A 22/09/2026

Solicitante:

大唐国际发电股份有限公司张家口发电分公司

Resumen de: CN122791428A

本发明提供一种碱性电解水制氢系统控制方法及装置，所述方法包括：采集碱性电解水制氢系统在不同工况下的运行数据；对所述运行数据提取累积贡献率超过预设阈值的主成分特征；构建物理约束方程，并结合所述物理约束方程构建物理信息神经网络模型；在所述物理信息神经网络模型中引入自适应权重调节机制；获得碱性电解槽的衰减系数，并将所述衰减系数作为可学习参数嵌入所述物理约束方程中；利用所述运行数据对引入了所述自适应权重调节机制、衰减系数的物理信息神经网络模型进行训练，得到碱性电解水制氢系统的精细化模型；利用所述精细化模型对所述碱性电解水制氢系统进行控制。