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用于浮动平台的海水电解制氢系统及自适应稳定控制方法

Resumen de: CN122773374A

0001 本发明涉及一种用于浮动平台的海水电解制氢系统及自适应稳定控制方法，所述系统包括：六自由度主动波浪补偿平台、海水电解制氢单元、多源运动感知单元、波浪预测子系统及智能控制器。所述方法包括：信息感知与采集、波浪预测与运动补偿计算、电解参数动态优化、协同执行与闭环反馈；在运动补偿的同时，依据平台运动预测结果实时调节电解槽电流密度、电解质流量、温度与压力，形成“感知‑预测‑补偿‑调控”闭环。本发明实现了机械运动补偿与电化学工艺参数的深度耦合，可在复杂海况下为准静态电解环境提供保障，显著提升制氢效率、气体纯度及设备寿命，填补浮式平台制氢装备在运动‑工艺协同控制领域的技术空白。

适用于超低载量铱基催化层的复合扩散层、复合阳极、复合膜电极

Resumen de: CN122773384A

本发明涉及一种适用于超低载量铱基催化层的复合扩散层，包括纳米多孔金属界面层和阳极多孔传输层；纳米多孔金属界面层为孔隙和韧带呈纳米级双连续结构的金属薄膜；阳极多孔传输层具有微米级孔径；铱基催化层的面载量为≤0.2 mg cm‑2。本发明通过系统研究常规载量和超低载量下影响铱基催化剂催化效果的差异因素和关键瓶颈，探索不同路径下功能界面层在调控超低铱载量关键瓶颈方面的作用，成功通过创新的界面结构设计实现了超低载量铱基催化层达到甚至超越常规载量和高载量体系的性能，为质子交换膜水电解的降本增效开辟了新路径。

单原子光催化剂及其制备方法和应用

Resumen de: CN122769003A

本发明涉及能源技术领域，公开了单原子光催化剂及其制备方法和应用。包括：将密勒胺、硝酸盐、含硫有机物和水混合后进行水热反应，得到S离子‑金属离子‑密勒胺混合物；将S离子‑金属离子‑密勒胺混合物进行第一冷冻干燥，然后放电等离子烧结得到单原子负载的石墨相氮化碳；将单原子负载的石墨相氮化碳与水混合后进行球磨得到混合料，将混合料与水混合后进行超声处理和离心，取上清液进行第二冷冻干燥，得到单原子光催化剂。本发明单原子光催化剂，不仅提高了水分解过程中的反应活性位点数目及活性，还增强了对CO2的吸附和还原过程的催化活性，使得其HER和CO2RR整体性能大大提高。

一种构建二维MOF/MOF异质结材料的方法

Resumen de: CN122769025A

0001 本发明提供一种构建二维MOF/MOF异质结材料的方法，所述方法采用pH值调控的静电组装法制备超薄二维MOF/MOF异质结材料，所述复合材料由层状的纳米片复合而成。所述方法简单易操作，成本经济，环境友好，具有较强的可控性和良好的重复性。同时，所述超薄二维MOF/MOF异质结材料有效缓解单个MOF纳米片易重新团聚的问题，具有更高的比表面积和更多的活性位点，且异质结构促进了光生载流子的分离转移，显著提升了光催化产氢性能。所述光催化材料符合可持续发展需求，具有良好的应用前景。

一种Bi2MoO6/CdS复合光电催化剂的制备方法和应用

Resumen de: CN122773399A

0001 一种Bi<2>MoO<6>/CdS复合光电催化剂的制备方法和应用，将五水硝酸铋和钼酸铵分别溶于乙二醇和去离子水中混合均匀后置于水热反应后将所得样品干燥得到钼酸铋粉体；将醋酸镉、硫代乙酰胺溶于去离子水中，然后再向混合溶液中加入PVP分散剂搅拌得到溶液A；取钼酸铋粉体加入到溶液A中，水热反应后将所得样品干燥得到Bi<2>MoO<6>/CdS复合光电催化剂。本发明通过两步水热法合成Bi<2>MoO<6>/CdS复合光电催化剂，并可通过调节前驱体比例、反应温度与时间等，获得物相纯正、结构稳定的Bi<2>MoO<6>基体，所制备的产品能形成清晰的异质结形貌，可灵活调控材料形貌与组分分布；本发明制备的Bi<2>MoO<6>/CdS复合材料可显著提升光吸收能力、载流子分离效率与表面催化活性，在碱性电解液中表现出优异的光电催化析氧性能。

一种电解制氢系统及动态运行方法

Resumen de: CN122773373A

本发明公开了一种电解制氢系统及动态运行方法，涉及电解制氢技术领域。该系统包括电解槽单元、工艺管道单元、气液分离单元和检测控制单元，各单元结构适配系统动态运行过程。本发明通过搭建一维气液两相动态预测模型预测系统运行状态，以系统能耗、安全风险和控制变量变化量为优化目标，结合模型预测控制算法滚动优化求解控制量并实时调节系统运行。本发明适配波动功率输入场景，兼顾系统运行能效与安全性，解决了波动功率下电解制氢系统能效低、安全风险难管控的问题。

ANION EXCHANGE MEMBRANES HAVING HIGH ION CONDUCTIVITY AND ALKALI RESISTANCE AND METHOD THEREOF

Resumen de: KR20260138165A

본 발명의 일 실시형태에 따르면, 아릴렌 기반 모노머와 서로 다른 두 개의 카보닐 모노머 간의 프리델-크래프트 중합 반응(Friedel-Crafts polymerization)에 의해 제조된 공중합체를 포함하며, 상기 서로 다른 두 개의 카보닐 모노머는 각각 피페리디늄(piperidinium)과 플루오로 작용기(-CF3)를 갖는 것을 특징으로 하는 이온 전도도와 알칼리 내구성이 우수한 음이온 교환막을 제공한다.

전기화학 장치용 통합 조립체

Resumen de: WO2025155652A1

An electrochemical device includes a membrane electrode assembly, a gas diffusion layer positioned on one side of the membrane electrode assembly, and a porous transport layer positioned on an opposite side of the membrane electrode assembly. A thermoplastic film is impregnated within outer peripheral edges of the gas diffusion layer and the porous transport layer to form an electrochemical assembly with a sealed outer edge. A method of forming a an electrochemical device is also disclosed.

SOEC INTEGRATION WITH ULTRA HOT STEAM

Resumen de: US20260275553A1

Systems, devices, and methods for electrolysis at very large scale (e.g., exceeding 100 megawatts (MW), and at gigawatt (GW) scale having a solid oxide electolyzer cell (SOEC) system including one or more SOEC columns, and one or more heat exchangers, each of the heat exchangers configured to receive input stream that is used to heat respective SOEC columns, wherein each of the heat exchangers is located along respective SOEC columns such that the input steam exiting the heat exchanger is directed towards adjacent SOEC columns.

水電解セル、及び水電解装置

Resumen de: JP2026147521A

【課題】イオン交換膜の損傷を適切に抑制することができる水電解セル、及び水電解システムを提供すること。【解決手段】本開示に係る水電解セルは、イオンを選択的に透過する性質を有するイオン交換膜と、イオン交換膜の一方側に配置される負極側触媒層と、イオン交換膜の他方の面側に配置される正極側触媒層と、イオン交換膜の一方の面と負極側触媒層の間と、イオン交換膜の他方の面と正極側触媒層の間との、少なくとも一方に設けられ、親水性を有する有機材料で構成される保護膜と、を備える。【選択図】図１

NATURAL GAS REFORMING SYSTEM AND PROCESS THEREOF

Resumen de: US20260274662A1

The present disclosure relates to a natural gas reforming system capable of reducing, by using a co-electrolysis device, the emission amount of carbon dioxide produced by reforming natural gas, of supplying heat to a reformer through syngas produced by the co-electrolysis, and of producing additional hydrogen, and a process thereof.

ALUMINUM RECYCLING METHOD FOR METALLIC ALUMINUM ENERGY STORAGE AND HYDROGEN PRODUCTION

Resumen de: AU2025400693A1

Disclosed herein is an aluminum recycling method for metallic aluminum energy storage and hydrogen production, comprising: electrolyzing aluminum oxide to obtain molten metallic aluminum; processing the molten metallic aluminum to obtain an aluminum-based hydrogen production material; under the action of a catalyst, chemically reacting the aluminum-based hydrogen production material with water to obtain hydrogen gas and an aluminum oxide hydrate slurry; subjecting the aluminum oxide hydrate slurry to solid-liquid separation to obtain an aluminum oxide hydrate and an aqueous solution containing the catalyst; calcining the aluminum oxide hydrate to obtain aluminum oxide; and recycling the aluminum oxide to the step of electrolyzing the aluminum oxide, and recycling the aqueous solution containing the catalyst to the step of chemically reacting the aluminum-based hydrogen production material with water, thereby forming a closed-loop cycle.

POROUS TRANSPORT LAYER

Resumen de: US20260279846A1

A porous transport layer for an electrolyser or for a fuel cell, comprising a first nonwoven layer of metal fibers provided for contacting a proton exchange membrane, wherein the first nonwoven layer of metal fibers comprises metal fibers of a first equivalent diameter, wherein the first nonwoven layer of metal fibers has a first surface roughness and a first porosity, a second nonwoven layer of metal fibers, wherein the second nonwoven layer of metal fibers comprises metal fibers of a second equivalent diameter, wherein the second nonwoven layer of metal fibers has a second surface roughness and a second porosity, wherein the first surface roughness is below 10 μm, the first equivalent diameter is smaller than the second equivalent diameter, the first surface roughness is smaller than the second surface roughness for at least 20%, e.g., in a range of 20% to 120%.

Ironmaking method and associated plant

Resumen de: US20260275433A1

Method to produce hot metal in a blast furnace including at least two levels of gas injection wherein the blast furnace top gas is recovered and subjected to an oxidation step using water-gas shift reaction to transform at least a part of the carbon monoxide from the recovered blast furnace top gas into carbon dioxide and hydrogen, the carbon dioxide is then separated to obtain a CO2-rich stream and a H2-rich stream, at least a part of it being injected into the blast furnace at the second level of gas injection.

METHOD FOR PRODUCING HYDROGEN AND APPARATUS FOR PRODUCING HYDROGEN

Resumen de: US20260275546A1

A method for producing hydrogen comprises providing water and a gaseous substance, the gaseous substance comprising hydrogen atoms and carbon atoms, producing a mixture comprising the water and bubbles comprising the gaseous substance, decreasing a diameter of the bubbles comprising the gaseous substance, and producing gaseous hydrogen by decomposing the gaseous substance in the bubbles having the decreased diameter. An apparatus is configured for producing hydrogen gas.

음이온-전도성 막, 상기 막의 제조 방법, 상기 막을 포함하는 전기화학 셀, 및 상기 셀을 포함하는 설비

Resumen de: AU2025207661A1

The invention relates to a layer of catalytic material for an anion-conducting membrane (10) for an electrochemical device; the layer of catalytic material comprises metal nanoparticles bound by a polymer binder. In one embodiment, the metal nanoparticles comprise a mixture of nickel nanoparticles and cobalt nanoparticles. The invention also relates to a membrane comprising a layer of catalytic material and to a method for preparing and depositing a catalytic layer.

Methods of PFAS Destruction using UV Irradiation at 222 Nanometers

Resumen de: US20260274731A1

0000 Methods, systems and devices for PFAS destruction including adding a sulfite salt to an aqueous solution containing PFAS and then irradiating the aqueous solution with light at 222 nm. The method may include adding a base to the aqueous solution in an amount sufficient to raise a pH of the aqueous solution including PFAS to about 10 or more. It may also include adding a halide salt such as a bromide salt or an iodine salt, and further adding a carbonate. Greater than 90%, or greater than 99%, of the PFAS in the solution may be destroyed by irradiating the aqueous solution in this way.

MEMBRANE ELECTRODE FOR ALKALINE WATER ELECTROLYSIS FOR HYDROGEN PRODUCTION AND PREPARATION METHOD THEREFOR, AND ELECTROLYTIC CELL

Resumen de: US20260275542A1

The present disclosure provides a membrane electrode for hydrogen production by alkaline water electrolysis, a preparation method therefor, and an electrolytic cell. According to the method provided by the present disclosure, a membrane electrode with catalyst layers uniformly and firmly adhered to the surfaces of a membrane can be obtained via a direct coating and hot pressing. The membrane electrode is endowed with good stability, and the obtained membrane electrode exhibits a significantly reduced overpotential for water electrolysis. The method comprises the following steps: directly applying a catalyst slurry (catalyst slurries) onto both sides of a membrane, followed by drying and hot pressing the catalyst slurry (catalyst slurries) to form catalyst layers on each surface of the membrane to obtain the membrane electrode. The membrane is selected from a porous membrane or an alkaline anion exchange membrane; the catalyst slurry comprises a binder solution and a catalyst, wherein the binder solution is one or more selected from a perfluorosulfonic acid resin solution and a perfluorosulfonic acid ionomer dispersion, and the mass concentration of the binder solution is 5% to 30%; and the mass ratio of the binder solution to the catalyst is 1:1 to 4:1.

閉ループ炭素サイクル

Resumen de: EP4491770A1

0001 Method for operating a closed-loop carbon cycle (100), comprising: - creating synthetic methane (106) from renewable energy (114) in a first geographical area (101), comprising: ∘ producing hydrogen (123) via electrolysis (113), ∘ feeding CO2 (109) and produced hydrogen (123) into Sabatier reactors (300) of an eNG production plant (110), - transporting said synthetic methane (106) to a second geographical area (102); - converting synthetic methane into usable energy (112) in said second geographical area (102), comprising: ∘ distributing synthetic methane (107) to one or more eNG conversion facilities (111); ∘ using said synthetic methane in said eNG conversion facilities (111), producing an output comprising CO2; ∘ capturing CO2 from said output; - transporting said captured CO2 (108) to said first geographical area (101); - establishing said closed-loop carbon cycle (100) by feeding said captured CO2 (109) received from said second geographical area (102) to said eNG production plant (110).

SYSTEMS, METHODS AND TECHNIQUES FOR HYDROGEN PRODUCTION FROM CHEMICAL LOOPING SYSTEMS WITH PARTICLE HEATING

Resumen de: US20260274663A1

0000 A reactor system may include at least one first type reactor, at least one second type reactor, a heat source unit, a heat exchange unit, and one or more separation units. The at least one first type reactor reacts a fuel, which may comprise biogas, with metal oxide particles. The at least one second type reactor receives reduced metal oxide particles from the at least one first type reactor and reacts those particles with steam, generating hydrogen (H<2>) and oxidized metal oxide particles. The oxidized metal oxide particles are heated up in a heat exchange unit that is heated by the heat source. The heat source may generate heat by combusting air and oxidation products from the at least one first type reactor. The heated oxidized metal oxide particles may be provided to the separation unit(s) and then to the at least one first type reactor.

DIRECT AIR CAPTURE OF CARBON DIOXIDE

Resumen de: US20260273467A1

A cyclic process for the capture of carbon dioxide (CO2) directly from air utilizing a three-compartment electrolytic cell coupled with a hydroxide-based CO2 capture system as well as a carbonate-based CO2 capture system. Air is passed over a hydroxide compound in the hydroxide-based CO2 capture system to extract carbon dioxide from the air and produce a carbonate compound which is transferred to the carbonate-based CO2 capture system, where air is passed over the carbonate compound to extract carbon dioxide from the air and produce a bicarbonate compound. The bicarbonate is then passed into the three-compartment electrolytic cell where CO2, hydrogen and oxygen gases are separately released and the bicarbonate solution is transformed into a hydroxide solution that is reused in the hydroxide-based CO2 capture system. The flow of input compounds from one system to the other enables efficient operation of the direct air capture of carbon dioxide system.

METHOD AND SYSTEM FOR PRODUCING A SYNTHETIC FUEL FROM BIOMASS

Resumen de: AU2025240709A1

The invention relates to a method for producing a synthetic fuel (F), comprising the steps (S1): carrying out a first reaction process, wherein the first reaction process creates a gas mixture of synthesis gas (SG) and carbon dioxide (CO2) with the addition of biomass (BM), oxygen (O2), wherein the synthesis gas (SG) contains carbon monoxide (CO) and hydrogen (H2); (S2): separating carbon dioxide (CO2) from the gas mixture and supplying hydrogen (H2) to separated carbon dioxide (CO2) for a second reaction process; (S3): carrying out a second reaction process, wherein in the second reaction process methanation is carried out using the reactants carbon dioxide (CO2) and hydrogen (H2), wherein methane (CH4) and water (H2O) are produced as an intermediate product; (S4): feeding back methane (CH4) and water (H2O) obtained from the second reaction process into the first reaction process, wherein a gas mixture containing synthesis gas (SG) is produced; and (S5): discharging synthesis gas (SG) and converting synthesis gas into a synthetic fuel (F). The invention further relates to a system (1) for producing a synthetic fuel (F), which is designed in particular to carry out the method.

METHOD FOR OPERATING AN AMMONIA SYNTHESIS PROCESS AT PARTIAL LOAD, AND PARTIAL-LOAD-CAPABLE AMMONIA SYNTHESIS PROCESS

Resumen de: AU2025241436A1

The invention relates to a method and a device for synthesizing ammonia (8), wherein a gas mixture (make-up gas) (1), which comprises hydrogen and nitrogen and is supplied with a temporally fluctuating flow rate, is provided after being compressed in a first compressor (make-up gas compressor) (V1) in order to form an ammonia synthesis gas (3) that is compressed with the aid of a second compressor (recycle compressor) (V2) and is then reacted in an ammonia reactor (R) in order to form an ammonia-containing synthesis product (5), from which a recycled gas (2) comprising hydrogen and nitrogen is separated in order to be recirculated in order to form the ammonia synthesis gas (3). The flow rate of the recycled gas (2) is controlled via the recycle compressor (V2), which is integrated into a control circuit as an actuator and the conveying capacity of which can be set independently of the conveying capacity of the make-up gas compressor (V1). The invention is characterized in that the control circuit is designed with a higher-level control system which outputs a control signal that is based on the load of the ammonia reactor in order to change the conveying capacity of the recycle compressor (V2), said control signal being corrected by a PID control circuit in such a way that the pressure in the ammonia reactor (R) is always within a specified value range.

AMMONIA GENERATION SYSTEM AND AMMONIA GENERATION METHOD

Resumen de: AU2025228469A1

An ammonia generation system (1) is provided with: an electrolysis cell (10) which generates ammonia from nitrogen and water, and is provided with a solid electrolyte (13) that contains a phosphoric acid compound which is a proton conductor; an ammonia separator (40) which is provided in a cathode outlet-side flow path (21) and separates ammonia from the cathode off gas; and a cathode-side circulation flow path (60) which is connected to the ammonia separator (40), and which returns, to the cathode (12), the residual gas that remains after the separation of ammonia by means of the ammonia separator (40) and contains nitrogen and hydrogen.

POROUS CATALYTIC MEMBRANE, MEMBRANE ELECTRODE ASSEMBLY AND WATER ELECTROLYSIS DEVICE

Nº publicación: US20260275550A1 17/09/2026

Solicitante:

THE HONG KONG UNIV OF SCIENCE AND TECHNOLOGY GUANGZHOU [CN]
The Hong Kong University of Science and Technology (Guangzhou)

Resumen de: US20260275550A1

Provided are a porous catalytic membrane, a membrane electrode assembly and a water electrolysis device. The porous catalytic membrane includes a porous polymer membrane formed by interweaving randomly arranged nanofibers and a catalyst coated on a surface of the nanofibers. The porous polymer membrane has a self-supporting structure and a large specific surface area, providing a large number of loading sites for the catalyst. The catalyst can be directly anchored onto the nanofibers of the porous polymer membrane through a physical or chemical method to achieve uniform dispersion without the need for coating by ionomers, thereby avoiding high costs and performance degradation caused by the adoption of ionomers. The exposure degree of the catalytic active sites is significantly increased, thereby enhancing utilization efficiency of the catalyst and reducing the amount of noble metal catalysts.