Absstract of: WO2025006628A2
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.
Absstract of: KR20260114118A
0001a 2단의 이오노머 조성 구배를 갖는 일체형 전극-다공성 확산체 및 이를 제조하는 방법으로서, 구체적으로, PTL(porous transport layer) 상에 이오노머 함량이 낮은 전극층이 형성되고, 상기 이오노머 함량이 낮은 전극층 상에 이오노머 함량이 높은 전극층이 형성된 것을 특징으로 하는, 2단의 이오노머 조성 구배를 갖는 일체형 전극-다공성 확산체, 및 이를 제조하는 방법에 관한 것이다. 본 발명에 따르면, 전극층 하단에는 낮은 함량의 이오노머를 갖는 전극층을 스프레이 코팅하고, 그 위에 얇게 높은 함량의 이오노머를 갖는 전극층을 스프레이 코팅함으로써, 우수한 계면 접합력과 수전해 성능을 동시에 갖는 것을 장점을 한다. 이에 따라, 본 발명의 2단의 이오노머 조성 구배를 갖는 일체형 전극-다공성 확산체를 포함하는 수전해 애노드 전극은 더욱 향상된 내구성과 수전해 성능을 가질 수 있다.
Absstract of: GB2703251A
A process for the manufacture of an anode layer for a polymer electrolyte membrane (PEM) electrolyser (PEMWE) is described together with a CCM (catalyst coated membrane), an electrolyser and an ink for an anode layer. The process comprising the steps of: (i) forming a catalyst ink comprising an iridium- and / or ruthenium-containing OER catalyst, an ionomer, a solvent, and a cellulose compound; (ii) applying the catalyst ink to a substrate to form the anode layer; and (iii) drying the anode layer. The cellulose compound may comprise hydroxyalkylcelluose. The catalyst loading may be less than or equal to 1.2mg/cm2. None
Absstract of: EP4524100A1
0001 Process comprising the production of a hydrogen-containing synthesis gas by the conversion of a hydrocarbon feedstock, said process comprising : - providing a fuel stream of ammonia comprising an ammonia content, - decomposing at least a portion of said ammonia content into hydrogen and nitrogen, thereby obtaining an enhanced fuel, said portion of the ammonia content undergoing said decomposition being greater than 50% of the ammonia content of said fuel stream of ammonia, - combustion of said enhanced fuel in a fired equipment to provide a heat input to the process.
Absstract of: GB2633564A
A method of changing the electrolytic conversion rate within at least one electrolyser cell 10 stack 12 of an electrolyser system (figure 1, 20) is described. The stack 12 has a fluid inlet 114, fluid outlet 116 and a power control system 108. The power control system 108 is used to change the voltage, via a voltage interface 100 across the electrolyser cell stack 12, allowing the fluid outlet temperature 104 to change in response to the voltage change, setting an inlet temperature 106 to substantially match the new outlet temperature, and then allowing the voltage to revert to a substantially thermoneutral value. The electrolyser cell stack 12 is thus operating at a changed stack temperature and changed electrolytic conversion rate. A processor 110 and memory circuit 112 can also be provided for storing information such as preset current, voltage or power delivery changes. The current method may lead to a galvanostatic thermoneutral (GTN) strategy for electrolyzer stack control.
Absstract of: KR20260114100A
전이금속 전구체 및 염화물을 포함하는 전해질을 포함하는 전해액에 산화전극을 침지시켜 전기분해하는 단계를 포함하는 전이금속 수산화물의 제조방법으로서, 상기 전이금속 수산화물은 상기 전이금속 전구체가 상기 염화물 유래 염소 이온에 의해 산화된 것인, 제조방법을 제공한다. 특히, 상기 제조방법은 별도의 산화제를 사용하지 않아 공정이 간단함과 동시에 연속적인 전이금속 산화물 제조 및 수소생성 시스템을 제공할 수 있다.
Absstract of: EP4778883A1
Apparatus for producing hydrogen from a cracking reaction of ammonia, said apparatus comprising:- a cracker unit (1) configured for producing a cracked gas from ammonia,- an absorber (2) configured for removing unconverted ammonia from said cracked gas using an absorbent fluid, thereby producing an ammonia depleted gas containing hydrogen, nitrogen and vaporized absorbent fluid,- an adsorption unit (3) comprising at least one adsorber vessel (4), said adsorber vessel or each adsorber vessel comprising a feed end arranged for receiving said ammonia depleted gas, a product end downstream said feed end for discharging a purified hydrogen product from said adsorber vessel, and an adsorbent bed arranged between said feed end and said product end, the adsorbent bed comprising an upstream layer (5) of an adsorbent selectively adsorbent for the vaporized absorbent fluid contained in said ammonia depleted gas and a downstream layer (6) of an adsorbent selectively adsorbent for nitrogen.
Absstract of: KR20260114165A
본 발명은, 양성자 교환막 수전해의 촉매로 사용되는 이리듐 나노 덴드라이트 및 이의 제조방법에 관한 것으로, 본 발명에 따른 이리듐 나노 덴드라이트를 이용하여 우수한 산소 발생 반응 촉매 활성, 내구성 및 고전류 밀도 조건에서 향상된 물질전달 특성 및 감소된 물질전달 과전압을 갖는 양성자 교환막 수전해용 촉매를 제공할 수 있다.
Absstract of: CN122249590A
An electrode for an electrochemical cell designed for electrolysis is a support formed with an open-cell metal structure and provided with a coating that increases the specific surface area on an outward facing surface of a separator facing the electrochemical cell, or with a coating that increases the specific surface area and has improved catalytic activity. The coating is formed from a metal, particles of which are bonded to each other via a sintered bridge and/or an organic binder and to a surface of the perforated metal structure. The coating layer is formed with a plurality of regions between which an uncoated joint is arranged.
Absstract of: US12686931B1
0000 The present invention relates to modular packages of individual electrolyzer stack units arranged to overcome prior art limitations related to power supply costs, as-manufactured stack unit performance variation, operating stack unit performance variation, and operational reliability. The electrolyzer stack module comprises an even number of individual stack units wired in series-parallel and arranged to minimize variation between branches of series-connected stack pairs.
Absstract of: EP4495054A1
0001 Process for producing hydrogen from an ammonia feed stream, comprising the following steps : - non-catalytic partial oxidation of the ammonia feed stream with an oxidant gas, thereby producing steam from the partial oxidation, remaining amounts of ammonia not being oxidized; - endothermic cracking conversion of part of the remaining amounts of ammonia, thereby producing a cracked gas comprising hydrogen, nitrogen and some unconverted ammonia; - mixing of the cracked gas with the steam produced from the partial oxidation, thereby obtaining an effluent gas; - condensing of the steam produced from the partial oxidation, thereby removing at least part of the unconverted ammonia from the effluent gas by absorption.
Absstract of: CN122428316A
一种FeCoNi基稀土高熵电催化剂及其制备方法和应用,属于电解水制氢的新能源技术领域。本发明的FeCoNi高熵电催化剂包括Fe、Co、Ni,以及RE元素中的至少一种,各元素原子百分比at%为Fe:Co:Ni:RE=(5~35):(5~35):(5~35):(5~35),且各元素原子百分比at%的总和为100%,采用恒电位电沉积的方法制备而得。本发明所得FeCoNi基稀土高熵电催化剂形貌为树枝状结构,具有较大比表面积,提高了反应速率和电流密度,并且,该催化剂价格低廉,原材料来源广泛,环境友好,展现出良好的耐腐蚀性、稳定性以及优异的双功能电催化活性,具有较高的工业应用前景。
Absstract of: WO2026155716A2
The present invention relates to a system, which enables a reagent containing aluminum to react with water to generate hydrogen gas with high efficiency and in a controlled manner. In a preferred embodiment, the present invention relates to a system, wherein a reagent containing aluminum powder in the form of pellet (P) is enabled to react with water inside a reactor body (1), at a stoichiometric ratio at every stage of said reaction, wherein, owing to a vibration actuator (2) included in said system, it is made possible to remove the protective oxide layer that is naturally present on the surface of aluminum and accelerate the reaction kinetics, and wherein said system makes a highly efficient, continuous, sustainable, and controllable generation of hydrogen gas possible.
Absstract of: CN122428309A
0001 本申请公开了一种基于镍普鲁士蓝氧化还原电对电极的酸性分步电解水制氢装置及方法,属于电解水技术领域,该装置包括电解槽、酸性电解液、以及置于电解槽内的析氢催化电极、析氧催化电极和镍普鲁士蓝衍生物电极,方法包括产氧步骤和产氢步骤:产氧时,析氧催化电极作为阳极氧化水生成氧气,镍普鲁士蓝衍生物电极作为阴极被还原;产氢时,还原后的镍普鲁士蓝衍生物电极作为阳极被氧化,析氢催化电极作为阴极还原氢离子生成氢气,本发明利用镍普鲁士蓝衍生物作为氧化还原中间体,实现了酸性条件下水电解析氢与析氧过程在时间和空间上的解耦,无需使用质子交换膜,有效避免了氢氧混合,具有成本低、环境友好、操作灵活等优点。
Absstract of: CN122428324A
0001 本发明公开了一种自支撑异质结构复合材料及其制备方法与应用,复合材料,包括泡沫镍和附着其上的异质结构,异质结构为Ni<3>S<2>和1T相的MoS<2>形成的异质结构,异质结构的微观形貌为纳米棒状纤维,表面附着褶皱、卷曲的片层状包裹物。制备方法包括以下步骤:将泡沫镍与钼酸盐溶液、镍盐溶液进行水热反应,冷却至室温后取出泡沫镍,清洗后在惰性气体中升温到440~460℃并保温,获得自支撑NiMoO<4>@NF前驱体;将NiMoO<4>@NF前驱体、水合肼、硫代乙酰胺溶液进行溶剂热反应,通过水合肼辅助的硫化形成1T相的MoS<2>并形成异质结构材料,冷却至室温,取出产物,清洗烘干。本发明能实现高效全解水,合成方法简便易行。
Absstract of: CN122428287A
本发明涉及一种基于工业余热的中高温碱性电解海水制氢方法,属于电解水制氢技术领域。该方法包括:海水经粗滤后,依次通过阴极氢气换热器和阳极气体换热器进行两级预热;预热海水经辅助热源加热蒸发并过热,产生过热蒸汽;过热蒸汽进入电解槽阴极室,与熔融态碱在150~300℃条件下电解生成氢气和阳极气体;阴极产出的高温氢气返回预热海水,阳极产出的高温气体返回预热海水,实现余热回收。本发明采用过热蒸汽作为电解原料,从源头避免了海水氯离子腐蚀;电解温度提升至150~300℃,电流密度可达0.6~0.8A/cm2,产氢率较传统低温电解提高2倍以上,系统综合能效提升15~20%。
Absstract of: CN122428319A
0001 本申请公开了一种钐掺杂镍铁金属磷化物自支撑阳极及其制备方法、应用,属于电解水制氢阳极材料领域。所述钐掺杂镍铁金属磷化物自支撑阳极由钐掺杂镍铁金属磷化物原位生长在基底上。所述制备方法包括:S1、通过电化学沉积法在基底表面原位生长钐掺杂镍铁金属氢氧化物;S2、将钐掺杂镍铁金属氢氧化物进行磷化,得到所述钐掺杂镍铁金属磷化物自支撑阳极。该制备方法简单,反应周期短,制备成本可控。所制备电极对电解水制氢阳极反应具有优良的催化活性,同时具备良好的催化稳定性,具有规模应用的潜力和优势。
Absstract of: WO2026155715A2
The invention relates to a reagent developed for use in the generation of hydrogen gas, said reagent releasing the hydrogen gas in a controlled manner upon contact with water or a similar medium, said reagent being obtained via a mechano-chemical method, and said reagent comprising a mixture of aluminum, sodium stannate (Na2SnO3) and/or potassium stannate (K2SnO3), and an inorganic hydroxide.
Absstract of: CN122428334A
0001 本发明提供了一种金属有机框架异质结光电极材料及其制备方法和应用,涉及光电催化技术领域。该材料由导电衬底、BiVO<4>纳米棒及表面负载的Co
MOF构成,二者形成异质结结构。制备采用电化学沉积结合水热法,先在衬底上制得BiVO<4>纳米棒,再水热负载Co
MOF形成异质结。本发明有效提升电子输运效率、增加氧原子活性位点,抑制载流子复合,显著提高光电催化水分解性能,光电流密度远高于纯BiVO<4>电极,具备高效、稳定、工艺简便等优点,可用于光电水解制氢体系。
Absstract of: CN122428308A
0001 本发明公开了一种三维多孔空腔CrN‑c纳米笼电催化剂及其制备方法和应用,属于三维纳米材料合成和电解水催化技术领域。本发明通过溶剂热法制备氢氧化铬纳米笼作为前驱体,并在高温氮化过程中利用二氧化硅保护,而后刻蚀除去二氧化硅,制备三维多孔空腔CrN‑c纳米笼。本发明提供的三维多孔空腔CrN‑c纳米笼,由于多孔空腔的限域及不饱和配位边缘,不仅能在反应界面富集羟基反应物,还能促进氧气泡的形成与释放,并降低溶解氧产物的浓度,使得该三维多孔空腔CrN‑c纳米笼在阴离子交换膜电解水制氢阳极析氧反应中展示出优于商用氧化钌催化剂的催化活性和长期稳定性。
Absstract of: CN122428298A
0001 本发明公开了一种热电协同的离网型压缩空气储能制氢系统及控制方法,系统包括电解水制氢子系统、混合能源输入子系统、复合储能调频子系统和综合热管理耦合子系统。混合能源输入子系统汇集风电、光伏电能经高压直流母线供电制氢;复合储能调频子系统含电化学储能与压缩空气储能单元,接入母线平抑波动;综合热管理耦合子系统通过高温回路存储压缩储能压缩热并用于电解槽冷启动供热,低温回路回收电解槽运行余热用于压缩空气膨胀侧预热。本发明通过多能互补与热电协同控制,提升压缩空气储能发电效率,延缓电解槽性能衰减,消除冷却塔与启动加热能耗,显著提高离网系统整体能效与经济性。
Absstract of: CN122426711A
本发明公开了一种基于摩擦电材料—水摩擦电效应的氢气制备方法。本发明针对现有氢能制备技术碳排放高、成本高、系统复杂,以及现有摩擦电产氢技术依赖中间环节、材料类型单一的问题,提供了一种无需外部电能输入、无需催化剂修饰,利用金属与水的摩擦电效应直接产氢的方法,实现低成本、绿色、高效的氢气制备。
Absstract of: CN122428303A
本发明提供了一种超薄有序一体化膜电极构建方法及应用,涉及电解水制氢技术领域,膜电极含有:离子交换膜、超薄有序催化层、气液扩散层和阴极催化层;其中,所述超薄有序催化层构建于离子交换膜的底面,并与所述离子交换膜的底面形成连续致密的一体化界面;所述离子交换膜的顶面设置有阴极催化层,所述阴极催化层的表面设置有气液扩散层;超薄有序催化层的另一面具有有序排列的微结构单元,气液扩散层与微结构单元直接接触。
Absstract of: KR20260113438A
0001a 본 발명은 액상의 수소화합물을 연소보조재로 이용하는 증기 생산용 가열로에 관한 것으로, 하단의 버너로부터 공급되는 열과 내부 연소열을 축열실에서 축열하도록 하고, 상기 축열실의 축열에 의해 외부로부터 적당한 양이 지속적으로 공급되는 액상의 수소화합물을 분자 구조로 변환하면서 연소가 가능한 활성증기화 하여 공급하도록 하고, 상기의 축열실에서 공급되는 활성증기와 내부에서 증기를 변환한 활성증기를 연소실에서 연소시키도록 하고, 연소 시에 발생하는 열로 발전용 증기와 전기분해용 증기를 생산하도록 함으로써 최소의 연료비로 내부 연소용 증기와 발전용 증기 및 전기분해용 증기를 얻으면서 최대의 열량을 얻을 수 있도록 구성됨을 특징으로 한다.
Nº publicación: CN122428291A 21/07/2026
Applicant:
浙江明深科技有限公司
Absstract of: CN122428291A
0001 本发明涉及电解水制氢技术领域,特别是涉及一种分布式制氢装置,包括筒体以及开设在筒体顶部的进料口,还包括:电极管,安装在筒体底部内壁;转动筒,转动安装在筒体内部;搅拌杆,由上到下环形阵列安装在转动筒外侧,数量设置多个;叶轮,活动安装在转动筒外侧;升降组件,设在转动筒上,用于带动叶轮上下移动。本发明提供的分布式制氢装置通过竖槽、升降块、连接杆的配合,带动叶轮随转动筒同步旋转的同时实现上下往复移动,形成旋流与竖向脉冲复合的流场,对筒体底部电解液进行全面、充分的扰动,彻底消除电解槽底部边角、转动部件下方的静态死水区。