Resumen de: AU2025213224A1
A system and method of making hydrogen from water. A reaction vessel is provided with an outer shell, a central shaft, and concentric inner tubes separated by annular spaces. Water is delivered to the annular spaces by a water pump through an inlet defined in the reaction vessel. The water courses along a tortuous flow path. That path begins at an inner annular space around a central shaft. It ends at an outer annular space. The water emerges from the reaction vessel through an outlet associated with a manifold. A vibratory stimulus is applied to the reaction vessel and water. Water molecules are dissociated into hydrogen molecules and oxygen atoms. These reaction products are delivered through the manifold along an effluent flow path to a receiving pressure vessel before deployment to a sub-assembly for harnessing clean energy.
Resumen de: WO2026158060A1
A recovery method and a recovery device. The recovery method comprises: a recovery process of phosphorus and iron elements in an iron phosphate system and a hydrochloric acid reuse process, wherein the recovery process of the phosphorus and iron elements comprises: an acid leaching step: subjecting the iron phosphate system to acid pickling by using an acid containing hydrochloric acid, so as to obtain an acid pickling solution; and the hydrochloric acid reuse process comprises: a chloride ion removal step: subjecting the acid pickling solution to electrolytic oxidation to remove chloride ions, so as to generate chlorine gas; a hydrochloric acid regeneration step: reacting the chlorine gas with hydrogen gas to generate hydrochloric acid; and a hydrochloric acid reuse step: reusing the hydrochloric acid in the acid pickling step.
Resumen de: WO2026161687A1
Disclosed is an electrolyzer, comprising: a cathode, comprising a cathode catalyst and a cathode separator; an anode, comprising an anode catalyst and an anode separator; a cathode flow field, comprising an inlet and an outlet; wherein the cathode flow field is in contact with the cathode; an anode flow field, comprising an inlet and an outlet; wherein the anode flow field is in contact with the anode; and an electrolyte wherein the cathode separator and the anode separator each independently comprise a porous hydrophobic material. Also disclosed are methods of producing H2 and O2 using the electrolyzer.
Resumen de: US20260218403A1
An ion separator is used to produce a stream of positively charged electrolytes and another stream of negatively charged electrolytes with adequate potential difference between the two streams. Short-circuiting these two streams in gas generation chambers produces hydrogen and oxygen gases. This setup of equipment is assembled as a containerized hydrogen and oxygen production cell. An x-y grid layout of many containerized hydrogen and oxygen production cells is used to outline a scalable plant for manufacturing oxygen and green hydrogen in large quantities.
Resumen de: WO2026160583A1
The water electrolysis separation membrane according to the present invention comprises a support mesh and a functional layer in which the support mesh is included, wherein the functional layer includes an ion-conducting material and a hydrogen-oxygen recombination catalyst.
Resumen de: US20260218396A1
A system includes an electrolyzer cell system configured to receive a steam inlet stream and an air inlet stream and to generate a hydrogen containing product stream and an air exhaust stream, and an absorption chiller fluidly connected to the electrolyzer cell system. The absorption chiller is configured to receive the air exhaust stream and to cool the hydrogen containing product stream using heat from the air exhaust stream.
Resumen de: WO2026159932A1
Provided are: an electrolysis cell stack in which a methanation reaction of a product gas that is generated at a hydrogen electrode by co-electrolysis can be suppressed even in cases where a methanation catalyst is contained in a flow passage through which the product gas flows; an electrolysis cell cartridge; an electrolysis cell module; and a method for suppressing methanation in an electrolysis cell stack. An electrolysis cell stack (101) according to the present disclosure comprises: an electrolysis cell (105) in which a hydrogen electrode, a solid electrolyte, and an oxygen electrode are stacked in sequence; a flow passage (117) through which a gas that is generated at the hydrogen electrode flows; and a hollow tube (140) which is disposed in the flow passage (117) so that the gas that is generated at the hydrogen electrode can flow therethrough. A member (103) that defines the outer contour of the flow passage (117) contains a methanation catalyst, and the hollow tube (140) does not contain a methanation catalyst.
Resumen de: WO2026159944A1
The purpose of the present invention is to suppress a methanation reaction of a product gas in a co-electrolysis system and a method for operating same. A co-electrolysis system (120) according to the present disclosure comprises an electrolysis cell stack (101) and a control unit (123). The electrolysis cell stack (101) includes: an electrolysis cell (105) in which a hydrogen electrode, a solid electrolyte, and an oxygen electrode are laminated in this order; a raw material gas flow path (124) through which a raw material gas containing H2O and CO2 supplied to the hydrogen electrode flows; and a product gas flow path (125) through which a product gas produced at the hydrogen electrode flows. The control unit (123) includes a methane concentration suppression unit (135) by which the concentration of methane in the off-gas discharged from the product gas flow path (125) is maintained below a threshold.
Resumen de: US20260216467A1
A breathing equipment for providing a positive pressure gas includes a gas channel, a hydrogen generating device, a pressurizing device, a mixing device, an atomizing device, and an output device. The hydrogen generating device, the pressurizing device, the mixing device, the atomizing device, and the output device are all coupled to the gas channel. The hydrogen generating device is configured to electrolyze water to generate a gas comprising hydrogen. The pressurizing device selectively accelerates an external gas to generate an accelerating gas. The mixing device is configured to mix the gas comprising hydrogen and the accelerating gas to generate a positive pressure gas. The atomizing device is configured to selectively generate an atomizing gas. The output device is configured to selectively output the gas comprising hydrogen, the positive pressure gas, the gas comprising hydrogen with the atomizing gas, or the positive pressure gas with the atomizing gas.
Resumen de: US20260217633A1
Systems and methods for E-methanol production may comprise capturing carbon dioxide from an exhaust gas, the exhaust gas being a byproduct of a gas processing plant; hydrogenating the carbon dioxide with a hydrogen gas to produce a syngas; synthesizing a stream comprising methanol and water from the syngas; and separating at least a portion of the water from the stream to produce an E-methanol.
Resumen de: US20260218400A1
0000 For renewable energy technology to become ubiquitous, it is imperative to develop catalysts useful reactions such as, for example, efficient oxygen evolution reaction (OER) and hydrogen evolution (HER). In accordance with the purpose(s) of the present disclosure, described herein are compounds having one of the following the formula: ABX, ABCX, ABCDX, ABCDEX, ABCDEFX, or ABCDEFGX, wherein (1) A, B, C, D, E, F, and G are, independently, Cr, Mn, Fe, Co, Ni, Cu, and Zn, (2) A, B, C, D, E, F, and G are not the same element, and (3) X is absent or X is C, O, S, P, N, Te, Se, or As. The compounds described herein possess unique electrochemical properties.
Resumen de: US20260217634A1
A method for processing flowback may comprise: providing flowback fluid comprising produced water, methane, hydrogen sulfide, and carbon dioxide; separating the flowback fluid into produced water, methane, hydrogen sulfide, carbon dioxide streams; producing a hydrogen stream and a carbon dioxide stream from the methane stream; producing a hydrogen stream from the hydrogen sulfide stream; and producing a hydrogen stream from the produced water stream. A flowback fluid processing system may comprise: a flowback fluid separator; a water splitting unit; a methane conversion unit; a hydrogen sulfide converter; a carbon dioxide reducing unit; and a synthesis unit.
Resumen de: DE102025103132A1
Um einen Wasserstofffilter bereitzustellen, mit dem in Elektrolyseverfahren zur Herstellung von Wasserstoff eine Separierung des Wasserstoffs von Wasserdampf ohne aufwändige Kühl-, Kondensations-, Adsorbtionstechnik ermöglicht wird, wird ein Wasserstofffilter (100) für eine Elektrolysezelle (10) oder für einen Verbund (300) aus Elektrolysezellen (10) vorgeschlagen, umfassend ein Metallblech (11), wobei auf mindestens einer Oberfläche (15) des Metallblechs (11) eine Schicht (16) aus einem keramischen Material angeordnet ist, wobei eine Schicht (17) aus einem wasserstoffpermeablen Metall oder einer wasserstoffpermeablen Metalllegierung auf dem keramischen Material angeordnet ist.
Resumen de: DE102025102714A1
Die vorgestellte Erfindung betrifft ein Verfahren (100) zum Betreiben eines Elektrolysesystems (200). Das Verfahren (100) umfasst:- Betreiben (101) des Elektrolysesystems (200) an einem Betriebspunkt, bei dem ein Kathodendruck in einem Kathodenraum (203) des Elektrolysesystems (200) größer ist als ein Anodendruck in einem Anodenraum (205) des Elektrolysesystems (200),- Ermitteln (103) eines Öffnungszustands sämtlicher Sicherheitsventile (207a, 207b, 207c) des Elektrolysesystems (200) in einem vorgegebenen Zeitraum und- Ausgeben (105) einer Warnmeldung für den Fall, dass der Öffnungszustand mindestens eines der Sicherheitsventile (207a, 207b, 207c) sich in dem vorgegebenen Zeitraum mehrfach ändert oder sämtliche Sicherheitsventile (207a, 207b, 207c) sich in dem vorgegebenen Zeitraum in einem geöffneten Zustand befinden.
Resumen de: WO2026159939A1
A hydrogen production method according to the present disclosure includes a supply step for supplying water to a hydrogen boride member containing a two-dimensional arrangement of hydrogen boride, wherein hydrogen is generated as a result of the water contacting the hydrogen boride member.
Resumen de: DE102025103146A1
Um eine Elektrolysezelle, insbesondere eine Hochtemperaturelektrolysezelle, bereitzustellen, die eine verbesserte Gasdichtigkeit und einen erhöhten Wirkungsgrad aufweist, wird eine Elektrolysezelle (100), insbesondere Hochtemperaturelektrolysezelle (10), umfassend eine erste Endplatte (12) und eine zweite Endplatte (13) vorgeschlagen, wobei die erste Endplatte (12) und die zweite Endplatte (13) einen Zwischenraum (14) ausbildend übereinander angeordnet sind, wobei in dem Zwischenraum (14) eine Elektrolyseanordnung (16) umfassend eine Kathode (17), eine Anode (18) und ein Elektrolyt (19) angeordnet ist, wobei der Zwischenraum (14) mittels einer Dichtung (20) abgedichtet ist, wobei die Dichtung (20) ein Aerogel umfasst oder aus einem Aerogel besteht.
Resumen de: DE102025103028A1
Es wird ein Verfahren zur Herstellung einer SiC-Elektrode 1 angegeben. Das Verfahren weist auf: Bereitstellen eines SiC-Pulvers und Sintern des SiC-Pulvers zu einem SiC-Sinterkörper.Des Weiteren wird eine SiC-Elektrode 1 angegeben, die ein gesintertes Elektrodenmaterial 3a,3b aufweist.
Resumen de: KR20260118138A
본 발명은 세척 공정이 간소화된 폴리벤즈이미다졸 전해질막의 제조방법에 관한 것으로, 보다 상세하게는 기존의 물과 알코올을 사용한 2단계의 세척 공정을 물만을 사용하는 1단계의 공정으로 단축함으로써, 기존의 공정으로 세척한 전해질막과 비교했을 때 성능이 저하되지 않고 우수한 성능을 갖는 전해질막을 대량 생산할 수 있는 새로운 제조방법에 관한 것이다.
Resumen de: JP2026123786A
0001 【課題】炭材や炭素化合物の過剰消費を抑制しつつ、カルシウム含有物を用いて効率的に水素ガスを製造する方法を提供する。 【解決手段】容器内にカルシウム含有粉末を装入する工程と、前記容器の外部から、前記容器内の前記カルシウム含有粉末に対して、水蒸気と一酸化炭素ガスとを含有する原料ガスを供給することで、前記水蒸気と前記一酸化炭素ガスとを反応させて二酸化炭素ガス及び水素ガスを生成しつつ、前記カルシウム含有粉末に前記二酸化炭素ガスを固定させる、水素ガス生成工程と、を有する、水素ガスの製造方法。 【選択図】なし
Resumen de: KR20260117878A
본 발명은 액체 혼합 금속 기반 암모니아 분해반응을 통한 수소 생산 장치 및 이를 활용한 생산방법에 관한 것이다. 본 발명은 이종액체 금속을 이용한 버블칼럼 반응기를 활용하여 암모니아를 수소로 전환하는 기술로 종래 기술에서 활용하고 있는 고체 촉매 방식이 아닌 액체금속이 촉매 역할을 하게 된다. 구체적으로, 본 발명은 암모니아 열화학 분해 반응을 통해 수소와 질소로 열분해하는 시스템으로서 암모니아를 해외에서 수입하여 국내에서 수소로 활용하려는 수소 수입, 저장, 운송, 발전 사업에 적용 가능하며, 반도체 및 디스플레이 산업 등에서 배출되는 암모니아 저감을 위한 스크러버로 사용 가능하다.
Resumen de: US20260217524A1
Among other things, a process for generating hydrogen by valorizing iron ore tailings (IOT) through the oxidation of remnant ferrous iron phases in the tailings is described. The IOT may be either wet (i.e., containing water) or dry (i.e., not containing water). The reaction may be performed using untreated IOT and may generate hydrogen gas capable of being used on site.
Resumen de: US20260217525A1
A system and method for producing low-cost, low to zero-carbon, and emission-free hydrogen (H2) is provided. The system includes an auto-thermal reformer which uses electrolytic oxygen (O2), a hydrocarbon fuel source, and water (H2O) to perform a partial oxidation reaction and produce auto-thermal reformed hydrogen and carbon dioxide (CO2). The system also includes a carbon dioxide electrolyzer for receiving electricity and the carbon dioxide from the auto-thermal reformer, and performing electrolysis on the carbon dioxide. The carbon dioxide electrolyzer produces electrolytic carbon monoxide (CO) and a portion of the electrolytic oxygen provided to the auto-thermal reformer. The system also typically includes a water electrolyzer, which performs water electrolysis to produce electrolytic hydrogen and more electrolytic oxygen which can be provided to the auto-thermal reformer. In addition, the carbon monoxide produced by the carbon dioxide electrolyzer can be combined with the hydrogen produced by the auto-thermal reformer to form syngas.
Resumen de: WO2025012271A1
The invention relates to a plant for preparing H2 by catalytically decomposing NH3. The plant according to the invention can be operated in a start-up mode in order to heat apparatuses of the plant to an increased operating temperature using a heat-transfer medium, e.g. following interruption of a continuous operation of the plant due to maintenance work. After heating to the operating temperature, the plant according to the invention can be operated in a production mode for continuous production of H2. The invention also relates to a method for starting up a plant for preparing H2 by catalytically decomposing NH3.
Resumen de: WO2025023918A1
The present disclosure relates to an electrochemical method that comprises the direct production of hydrogen from boron compound types by reduction-oxidation reactions, the simultaneous production of boron hydride compounds and the production of hydrogen by oxidation-reduction reactions of boron hydride compounds, which does not require any additional pH adjustment or purification procedure in a solution system containing low-cost boron compounds (boric acid, boron salts, etc.), and which provides direct production of high purity hydrogen in a single step and at room temperature in an environmentally friendly and low-cost manner.
Nº publicación: GB2703483A 29/07/2026
Solicitante:
H3 ENERGY LTD [GB]
H3 ENERGY LIMITED
Resumen de: GB2703483A
A method and membrane reactor for production of pressurised hydrogen are disclosed, the method comprises providing a catalyst for conversion of ammonia to hydrogen and nitrogen; contacting a pressurised reaction stream comprising ammonia with the catalyst to convert at least a portion of the ammonia into hydrogen in a reaction zone; and obtaining a hydrogen product stream comprising pressurised hydrogen by selectively driving hydrogen from the reaction zone through a hydrogen-selective membrane under a pressure differential between a reaction-side pressure of the reaction stream and a product-side pressure of the hydrogen product stream; wherein the product-side pressure is at least 30 bara. The membrane reactor comprises a feed vessel comprising a catalyst bed comprising a catalyst for conversion of ammonia to hydrogen and nitrogen; a hydrogen collection vessel for collecting hydrogen at a pressure of at least 30 bara; and a hydrogen-selective membrane separating the feed vessel and the hydrogen collection vessel for selective removal of hydrogen. Figure 1