If you want to distinguish your goods, services or both from those of another company, you may need a trademark or trade name. Find out what they are, what their registration procedure is and what it involves.
Information on the deadlines for filing applications for transformation of European Union trademarks into Spanish national trademarks. See more
If you have a new device, product or procedure that solves a technical problem or has a practical advantage, there are different ways to protect it in Spain and other countries. Find out how.
Does your innovation lie in the aesthetics, ornamentation or appearance of your product? Protect it through industrial design. Find out what rights registration confers and how to proceed.
Geographical indications protect the name of a product that has a specific geographical origin and owes its qualities, characteristics or reputation to its particular origin. Find out what they are, how the registration process works and what benefits they provide.
Patents published worldwide are a valuable source of scientific, technical and commercial information.
El Bono 3 del Fondo para PYMEs 2025, que cubre la elaboración de Informes Tecnológicos de Patentes (ITP) y Búsquedas Retrospectivas se cerrará el lunes 10 de febrero de 2025 al cierre de la jornada laboral. Próximamente se informará sobre su reapertura. Puede consultar más información aquí.
If you are an entrepreneur or a company and you want to boost and improve the profitability of your business by adequately protecting the intangible assets of your organisation, in this space you will find what you need.
529
results.
Updated on
18/12/2025 [07:07:00]
Results 325 to 350 of 529
Absstract of: DE102024112692A1
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.
Absstract of: US2025236972A1
Electrolyzer for production of hydrogen gas and comprising a stack of bipolar electrodes sandwiching ion-transporting membranes between each two of the bipolar electrodes. Each bipolar electrode comprises two metal plates welded together back-to-back forming a coolant compartment in between and having a respective anode surface and an opposite cathode surface, each of which is abutting one of the membranes. The plates are embossed with a major vertical channel and minor channels in a herringbone pattern for transport of oxygen and hydrogen gases. The embossed herringbone pattern is provided on both sides of the metal plates so as to also provide coolant channels in a herringbone pattern inside the coolant compartment.
Absstract of: JP2025166457A
【課題】水の電気分解において、反応が進行する場所は電極表面の気体と液体の界面－すなわち固体、気体、液体の三相の界面の極めて限られた領域で反応が進む。つまり反応が進行する場所は電極表面の気体と液体の界面の狭い範囲に限定される。この狭い反応領域の一点に水の二分子もしくは水酸基の４分子が同時に接触しなければ水素分子もしくは酸素分子は発生せず極めて限定された反応機構となる。【解決手段】負極と正極と中間電極を有し、負極と正極との間に中間電極を配した少なくとも２組の電極群において、一方の電極群の負極と他方の電極群の正極との間に中間電極が配された水電解装置とすることにより反応面が線から面に広がり効率の良い水電解が可能となる。【選択図】図１Ａ
Absstract of: JP2025166415A
【課題】浄水器の劣化をおさえながら、水電解用の水を冷却および浄化し、十分な量を水電解セルに供給すること。【解決手段】水電解装置１は、水電解反応により水素および酸素を生成する水電解セルと、前記水電解セルで使用された水を貯蔵する水タンクと、前記水タンクに接続され前記水タンクから供給された水を冷却する熱交換器と、前記熱交換器に接続され前記熱交換器で冷却された水を浄化する浄水器と、前記水タンクから供給された水が前記熱交換器および前記浄水器を介して前記水電解セルに流れる第１流路９２と、前記水タンクから供給された水が前記熱交換器および前記浄水器を介さずに直接前記水電解セルに流れる第２流路９３と、前記水電解セルから前記水タンクに水が流れる第３流路と、を備える。【選択図】図１
Absstract of: JP2025166373A
【課題】水の電気分解を利用した二酸化炭素の回収方法であって、回収を確実に見込める方法を提供すること。【解決手段】本発明の回収方法は、水を電気分解した電解装置の陰極室３２Ｂから取り出したアルカリ性の陰極側電解液３５Ｂを、二酸化炭素を含む気体で曝気する曝気工程と、曝気した陰極側電解液３５Ｂを酸性にする酸性化工程と、酸性にした陰極側電解液３５Ｂを加熱して、気体で放出された二酸化炭素を回収する二酸化炭素回収工程とを有する。各工程において陰極側電解液３５Ｂに対する二酸化炭素の溶解と放出を制御することで、二酸化炭素を効率的に回収することができる。【選択図】図１
Absstract of: KR20250158219A
본 발명은 전해공간이 형성되고, 좌우 및 전후로 각각 다수로 배치되는 본체부; 상기 본체부 각각의 전해공간을 제 1 및 제 2 공간으로 양분하도록 설치되는 분리막; 상기 분리막을 사이에 두고 상기 제 1 및 제 2 공간 내에 각각 설치되고, 산소전극과 수소전극 중 어느 하나와 다른 하나에 각각 해당되는 제 1 및 제 2 전극; 상기 본체부 사이마다 개재되어 접하게 되는 전해공간의 일측을 차단시키고, 일측에 위치하는 본체부의 제 2 전극과 타측에 위치하는 본체부의 제 1 전극 각각에 전기적으로 접속되는 양극판; 상기 본체부, 상기 분리막, 상기 제 1 및 제 2 전극, 그리고 상기 양극판이 좌우 및 전후로 배열되는 집합체의 양측에 각각 마련되고, 접하게 되는 전해공간의 일측을 차단시키며, 상기 양극판을 매개로 상기 제 1 및 제 2 전극에 전기분해를 위한 전원이 인가되도록 하는 배전부; 한 쌍으로 이루어져서 각각의 사이에 상기 집합체와 함께 상기 배전부가 개재되어 밀착되도록 고정되는 커버; 상기 전해공간에 전해액을 공급하도록 형성되는 공급유로부; 및 상기 전해공간으로부터 생성되는 가스를 배출시키도록 형성되는 배출유로부;를 포함하는, 다중 연결방식의 스택 전기분해 시스템에 관한 것이다.
Absstract of: US2025376776A1
Embodiments of the present disclosure relate to a core-shell structure, a preparing method of the same, and an electrode including the same, and the core-shell structure may include a core comprising a perovskite nanocrystal; and a shell surrounding the core, thereby exhibiting improved optical, electrical, and catalytic properties and ensuring stable operating stability, thereby exhibiting excellent photoelectrochemical activity, compared to commercial catalysts such as conventional transition metal oxides.
Absstract of: WO2025230304A1
The present invention relates to an electrode catalyst for water electrolysis and a method for producing same, and provides an electrode catalyst for water electrolysis and a method for producing same, the electrode catalyst comprising: a support composed of two-dimensional structured MXene; and a hetero-joined transition metal compound located on the support, wherein the transition metal compound employs a phosphide of two or more types of metals selected from the group consisting of nickel, iron, molybdenum, cobalt, and tungsten, so that the electrode catalyst, compared with conventional commercial catalysts, exhibits improved driving stability and increased electrochemical activity through an increased surface area of the catalyst.
Absstract of: WO2025227539A1
The present invention belongs to the technical field of carbon dioxide capture. Provided is a decoupling type electrochemical carbon dioxide capture system. The system comprises an electrolysis reactor, a carbon dioxide absorption tower and a carbon dioxide desorption tower. The system can achieve the electrochemical capture and purification of ultralow-concentration carbon dioxide in an oxygen-containing carbon dioxide environment. In practical use, an external power supply can be used for supplying power to the system, and the pH environments of a solution at a cathode and an anode are changed by means of an electrochemical PCET reaction to promote the enrichment of OH- in a cathode region and the enrichment of H+ in an anode region, thereby achieving the absorption of ultralow-concentration carbon dioxide and the release of high-purity carbon dioxide; and an anode liquid is reduced and regenerated outside the system by means of hydrogen generated by the cathode, thereby achieving low-energy-consumption continuous stable carbon dioxide capture and purification.
Absstract of: WO2025227188A1
Described herein is a process for splitting water into molecular hydrogen (H2) and oxygen (O2), comprising: contacting water molecules with a catalyst, wherein the catalyst or at least portion thereof in contact with the water molecules is irradiated with microwave radiation, and wherein the catalyst comprises a compound of a metal (M) and at least one Lewis acidic element (X) different to the metal, whereby on contact, the water molecules split to form molecular hydrogen (H2) and oxygen (O2).
Absstract of: KR20250158472A
본 개시의 일 실시예에 따른 선박용 개질 수소 공급 시스템은, 암모니아를 수소로 개질하는 개질기(200), 상기 개질기에서 생산된 개질 수소를 저장할 수 있는 버퍼 탱크(100), 상기 개질기에서 생산된 개질 수소를 상기 버퍼 탱크에 공급하는 공급라인(SL), 상기 공급라인에서 분기하여, 개질 수소를 상기 개질기로 다시 공급하는 순환라인(CL), 및 상기 순환라인에 도입되는 개질 수소의 유량을 조절하는 순환밸브(301)를 포함할 수 있다.
Absstract of: WO2025230390A1
A ruthenium-nickel foam catalyst composite, a preparation method therefor, and a hydrogen extraction system (10) using same are disclosed. Specifically, provided is the method for preparing a catalyst composite used for ammonia decomposition, comprising the steps of: (a) making a porous support, which is in the form of a three-dimensional structure having pores and includes a first metal, come into contact with an acidic aqueous solution so as to pretreat the porous support; (b) preparing a second metal precursor aqueous solution comprising water and a second metal precursor that includes a second metal; and (c) using the pretreated porous support and the second metal precursor aqueous solution so as to support a catalyst including the second metal on a part or all of the surface of the porous support, thereby preparing a catalyst composite. The present invention provides a low-loading noble metal catalyst by maximizing the utilization of supported noble metals through selective adsorption of Ru metal.
Absstract of: US2025341280A1
The storage apparatus according to the invention, a geo hydrogen storage system, is a system consisting of a plurality of groundwater wells drilled into the ground. Hydrogen is produced by electrolysis using green energy. The hydrogen and the associated oxygen are stored in and recovered from cartridges installed in said wells being flooded by the groundwater and located at appropriate distances from each other. The system uses closed-circuit circulating water to transport the gases generated in electrolysis in the form of bubbles. The gases are separated from the circulating water by volume expansion and form gas bubbles when they reach the corresponding cartridge. This gas bubble will, with continued operation, squeeze larger and larger volume of water from the groundwater in the cartridge, thereby pressurizing the system.
Absstract of: US2025341001A1
An electrode configuration and system useful for performing electrolysis, including one or more pairs of non-planar electrodes each comprising a first electrode having a first base and a second electrode comprising a second base. A mount can be used to mount the first electrode and the second electrode in each of the pairs with a spacing between the first base and the second base, so that an electric current may flow through a fluid between the first base and the second base to drive an electrochemical reaction of the fluid. A surface area of the bases (the base of the first electrode and the base of the second electrode) exposed to the fluid are dimensioned to support a current density of the electric current of at least 10 A/cm2 or in a range of 10 A/cm2 and 14 A/cm2. An electrolysis system including the electrodes can be used for the electrolysis of seawater to produce hydrogen at higher rates and with reduced chlorine evolution.
Absstract of: US2025341007A1
An electrochemical cell comprises a first electrode, a second electrode, and a proton-conducting membrane between the first electrode and the second electrode. The first electrode comprises a layered perovskite having the general formula: DAB2O5+δ, wherein D consists of two or more lanthanide elements; A consists of one or more of Sr and Ba; B consists of one or more of Co, Fe, Ni, Cu, Zn, Mn, Cr, and Nd; and δ is an oxygen deficit. The second electrode comprises a cermet material including at least one metal and at least one perovskite. Related structures, apparatuses, systems, and methods are also described.
Absstract of: US2025341004A1
A device for preparing high-purity hydrogen and/or high-purity oxygen by electrolysis of water, wherein the hydrogen and/or oxygen produced has an argon content of less than 5 ppb by weight. Including, in sequence, a desalination water treatment system, a desalination water storage tank, a degasser feed water pump, a desalinated and degassed water heat exchanger, a degasser for degassing desalinated water, an electrolyzer feed water pump, and an electrolyzer. The degasser is configured to produce water that has an argon content of less than 10 ppb by weight after being degassed. The electrolyzer is an alkaline electrolyzer, and includes an electrolytic cell, and anode lye separator, a cathode lye separator, and a lye cooler. The electrolyzer also includes a lye heat exchanger and a hot lye recirculation stream. Also involved is a method of preparing high-purity hydrogen and/or oxygen by using the device.
Absstract of: US2025341003A1
A method for the generation of a gas mixture including carbon monoxide, carbon dioxide and optionally hydrogen for use in hydroformylation plants or in carbonylation plants, including mixing an optional steam with carbon dioxide in the desired molar ratio, feeding the resulting gas to a solid oxide electrolysis cell (SOEC) or an SOEC stack at a sufficient temperature for the cell or cell stack to operate while effecting a partial conversion of carbon dioxide to carbon monoxide and optionally of steam to hydrogen, removing some or all the remaining steam from the raw product gas stream by cooling the raw product gas stream and separating the remaining product gas from a liquid, and using the gas mixture containing CO and CO2 for liquid phase synthesis reactions utilizing carbon monoxide as one of the reactants while recycling CO2 to the SOEC or SOEC stack.
Absstract of: US2025341002A1
A direct impure water electrolysis (DIWE) approach generates green hydrogen in a modified proton-exchange membrane pure water electrolyzer (PEM-PWE), that avoids fouling, corrosion, deactivation, and side reactions normally caused by the ions in impure or saline waters. Conventional electrolyzers require ultrapure deionized (DI) water as feed because: 1) the proton-exchange membrane (PEM) and electrocatalysts are readily poisoned by the anions, e.g., chloride, and cations, e.g., sodium, calcium, and magnesium that are present in seawater or brackish water; and 2) the chloride anions readily form chlorine at the PEM-electrolyzer anode, which is toxic and corrosive. This adds substantially to the cost and complexity of the electrolyzer plant due to the water treatment plant needed for producing ultrapure DI water. The tolerance of impure water as described herein avoids reverse osmosis and deionization requirements steps which is beneficial for use in semi-arid regions with a paucity of fresh water.
Absstract of: US2025340500A1
The invention relates to a method for producing methanol via a synthesis gas produced by combining electrolysis of a water feedstock for producing a stream comprising hydrogen, and electrolysis of carbon dioxide rich stream for producing a stream comprising CO and CO2 in which the synthesis gas has a molar ratio CO/CO2 greater than 2. The invention relates also to a method for producing a synthesis gas by once-through co-electrolysis in a SOEC unit of a feed gas stream combining CO2 and steam.
Absstract of: US2025340433A1
A method for ammonia (NH3) decomposition to hydrogen (H2) and nitrogen (N2) using a ruthenium-doped alumina-supported cobalt/nickel (Ru—CoNi/Al2O3) catalyst. The method includes introducing and passing an NH3-containing feed gas stream into a reactor to contact the NH3-containing feed gas stream with a reduced Ru—CoNi/Al2O3 catalyst at a temperature of 100 to 1000° C. thereby converting at least a portion of the NH3 to H2 and regenerating the Ru—CoNi/Al2O3 catalyst particles to form a regenerated Ru—CoNi/Al2O3 catalyst, and producing a residue gas stream leaving the reactor.
Absstract of: US2025341010A1
A method of operating an electrolyzer includes changing a current density associated with operation of the electrolyzer based on one or more electricity input factors, or one or more hydrogen output factors, or both.
Absstract of: WO2025230473A1
The present disclosure relates broadly to ammonia electrochemical cells. The ammonia electrolysis cell may comprise: a chamber for containing an electrolyte; two electrodes disposed within the chamber; and an anion exchange membrane disposed between the electrodes, wherein each electrode comprises a bifunctional catalyst having ammonia oxidation reaction activity and hydrogen evolution reaction activity, and wherein each electrode is capable of alternating in polarity when subjected to an alternating potential. There is also disclosed herein a method of operating an ammonia electrolysis cell as well as the use of an ammonia electrolysis cell to produce hydrogen from ammonia.
Absstract of: WO2025231331A1
A direct impure water electrolysis (DIWE) approach generates green hydrogen in a modified proton-exchange membrane pure water electrolyzer (PEM-PWE), that avoids fouling, corrosion, deactivation, and side reactions normally caused by the ions in impure or saline waters. Conventional electrolyzers require ultrapure deionized (DI) water as feed because: 1) the proton-exchange membrane (PEM) and electrocatalysts are readily poisoned by the anions, e.g., chloride, and cations, e.g., sodium, calcium, and magnesium that are present in seawater or brackish water; and 2) the chloride anions readily form chlorine at the PEM-electrolyzer anode, which is toxic and corrosive. This adds substantially to the cost and complexity of the electrolyzer plant due to the water treatment plant needed for producing ultrapure DI water. The tolerance of impure water as described herein avoids reverse osmosis and deionization requirements steps which is beneficial for use in semi-arid regions with a paucity of fresh water.
Absstract of: WO2025231104A1
A contained hydrogen generation system ("system") comprises a high-pressure containment vessel ("vessel"), one or more proton-exchange membrane ("PEM") cells, an oxygen-water separator, and a passive dual regulator with relative differential venting ("regulator"). The vessel defines a hydrogen plenum. The PEM and the oxygen-water separator are disposed in the hydrogen plenum. The regulator includes a hydrogen fluid path in fluid communication with the hydrogen plenum, an exterior hydrogen storage vessel, and an exterior of the vessel, and also includes an oxygen fluid path in fluid communication with the oxygen-water separator, an exterior oxygen storage vessel, and an exterior of the vessel. The regulator regulates pressure imbalances between an oxygen-side of the system and a hydrogen-side of the system, and vents oxygen and hydrogen to an exterior of the vessel to allow collection of both hydrogen and oxygen and avoid rupture of a PEM in the one or more PEM cells.
Nº publicación: US2025343422A1 06/11/2025
Applicant:
OHMIUM INT INC [US]
Ohmium International, Inc
Absstract of: US2025343422A1
The present disclosure relates to circuits for connecting components of a hydrogen plant to a power grid to power the components in an efficient manner. In one implementation, power-side alternate current (AC) to direct current (DC) converters may be connected to a source power grid without the need for an isolation transformer by providing separate buses between the power-side AC-DC converters and load-side DC-DC converters instead of a shared DC bus between the converters. Other implementations for connecting components of a hydrogen plant to a power grid may include an adjustable transformer, such as a tappable transformer or an autotransformer, to connect any number of auxiliary loads of the plant to the power grid. The adjustable transformer may provide for various types of auxiliary load devices to connect to the power provided by the transformer at the same time, including both three-phase devices and one-phase devices.
BOPI
Electronic site
