WO2022175011A1 - Elektrolysezelle - Google Patents
Elektrolysezelle Download PDFInfo
- Publication number
- WO2022175011A1 WO2022175011A1 PCT/EP2022/051176 EP2022051176W WO2022175011A1 WO 2022175011 A1 WO2022175011 A1 WO 2022175011A1 EP 2022051176 W EP2022051176 W EP 2022051176W WO 2022175011 A1 WO2022175011 A1 WO 2022175011A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- cells
- electrolytic
- electrolysis
- electrolytic cell
- vacuum
- Prior art date
Links
- 239000012528 membrane Substances 0.000 claims abstract description 12
- 125000006850 spacer group Chemical group 0.000 claims abstract description 8
- 238000005868 electrolysis reaction Methods 0.000 claims description 30
- 238000004519 manufacturing process Methods 0.000 claims description 10
- 239000004033 plastic Substances 0.000 claims description 7
- 229920003023 plastic Polymers 0.000 claims description 7
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 6
- 229910052759 nickel Inorganic materials 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 3
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 2
- 229910045601 alloy Inorganic materials 0.000 claims description 2
- 239000000956 alloy Substances 0.000 claims description 2
- 239000010935 stainless steel Substances 0.000 claims description 2
- 229910001220 stainless steel Inorganic materials 0.000 claims description 2
- 239000007858 starting material Substances 0.000 claims description 2
- 239000010936 titanium Substances 0.000 claims description 2
- 229910052719 titanium Inorganic materials 0.000 claims description 2
- 229910052751 metal Inorganic materials 0.000 abstract description 7
- 239000002184 metal Substances 0.000 abstract description 7
- 239000000376 reactant Substances 0.000 abstract 1
- 239000001257 hydrogen Substances 0.000 description 10
- 229910052739 hydrogen Inorganic materials 0.000 description 10
- 239000007789 gas Substances 0.000 description 9
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 238000007789 sealing Methods 0.000 description 7
- 239000011888 foil Substances 0.000 description 4
- 238000003466 welding Methods 0.000 description 4
- 230000006835 compression Effects 0.000 description 3
- 238000007906 compression Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 230000002706 hydrostatic effect Effects 0.000 description 3
- 238000005304 joining Methods 0.000 description 3
- 239000004734 Polyphenylene sulfide Substances 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000005431 greenhouse gas Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 229920000069 polyphenylene sulfide Polymers 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910000990 Ni alloy Inorganic materials 0.000 description 1
- 229920001774 Perfluoroether Polymers 0.000 description 1
- 238000004026 adhesive bonding Methods 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000012777 electrically insulating material Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 239000012943 hotmelt Substances 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000003014 ion exchange membrane Substances 0.000 description 1
- 238000003475 lamination Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 239000000565 sealant Substances 0.000 description 1
- 239000003566 sealing material Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/17—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof
- C25B9/19—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof with diaphragms
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/02—Hydrogen or oxygen
- C25B1/04—Hydrogen or oxygen by electrolysis of water
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B15/00—Operating or servicing cells
- C25B15/08—Supplying or removing reactants or electrolytes; Regeneration of electrolytes
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/17—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof
- C25B9/19—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof with diaphragms
- C25B9/23—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof with diaphragms comprising ion-exchange membranes in or on which electrode material is embedded
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/60—Constructional parts of cells
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/60—Constructional parts of cells
- C25B9/63—Holders for electrodes; Positioning of the electrodes
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/70—Assemblies comprising two or more cells
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/70—Assemblies comprising two or more cells
- C25B9/73—Assemblies comprising two or more cells of the filter-press type
- C25B9/77—Assemblies comprising two or more cells of the filter-press type having diaphragms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C65/00—Joining or sealing of preformed parts, e.g. welding of plastics materials; Apparatus therefor
- B29C65/02—Joining or sealing of preformed parts, e.g. welding of plastics materials; Apparatus therefor by heating, with or without pressure
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Definitions
- the invention is in the field of electrolysis technology and relates to novel term electrolysis cells, electrolysis stacks that contain these cells connected in series, a method for producing these stacks and the use of cells for producing the stacks.
- An electrolytic cell is already known from US Pat. No. 5,599,430 B (DOW), which comprises a housing containing at least one pair of electrodes, namely a cathode and an anode, a current collector and a membrane. Also included is an electrically conductive, hydraulically permeable resilient mattress that is substantially coplanar with and contacts the current collector on one side and also coplanar with and contacts an electrode on the other side.
- EP 1451389 B1 (UHDENORA) describes a current collector for electrochemical cells, consisting of a "sandwich" of compressible and elastic layers of metal wires, which imparts a predetermined mechanical load in a wide compression range.
- EP 1766104 B1 (UHDENORA) relates to a conventional electrolytic cell with a sealing system consisting of individual elements, each containing two electrodes which are separated from one another by membranes and the proportion of the inactive membrane surface is minimized by a flange, see above that the ratio between the area of the flange of a half-shell and the active membrane area can be adjusted to less than 0.045.
- EP 1882758 A1 the elastic pressure in an electrolysis cell is transmitted using coils or woven nickel mats or resistant nickel alloys Layers gradually from top to bottom, so that finally a pressure profile is established which is at least similar to the hydrostatic pressure on the anode side, which increases in the same direction.
- EP 2356266 B1 (UHDENORA) describes an electrolysis cell provided with a separator, which has a flat, flexible cathode, which is held in contact with the separator by an elastic, conductive element pressed by a current distributor becomes.
- the cell also contains an anode consisting of a stamped sheet metal or grid supporting the separator.
- the cell can be used in a modular arrangement to form an electrolyser, the end cells of which are connected only to the electrical power supply.
- the EP 2734658 B1 (NEW NEL HYDROGEN) comprises a module for an electrolyser from the filter press type, which comprises at least one closed frame, the at least defines a first opening, wherein the module presents a sealing and electrically insulating material, and this material at least partially covers the surface of the frame.
- EP 2746429 A1 UHDENORA
- an electrolytic cell which contains an anode space with an anode and a cathode gas space with a gas diffusion ka method, the two electrodes being separated from one another by an ion exchange membrane, and a metallic elastic element which is under compression is clamped between the rear wall of the cathode gas space and the gas diffusion cathode, said elastic element being clamped into the cathode gas space in such a way that the distance between the element and the rear wall increases in the direction of gravity.
- EP 2872675 B1 proposes an insulating frame for electrolytic cells which has a geometric shape with corners, the frame being flat and having an anode side and a cathode side as well as an outer and an inner end face .
- the insulating frame has an edge region directly adjoining the inner end face, which has recesses in the form of cutouts in the region of the corners.
- An electrolytic cell consists schematically of an anode and a cathode chamber (AR, KR), each containing the anode (A) and the cathode (K).
- the two electrodes are separated from one another by a diaphragm or separator membrane (S) and fixed in the corresponding housing parts (“half cells”) with the aid of an elastic or rigid spacer (XI, X2), as shown schematically can be seen in Figure 1.
- the figure also shows a seal (D) that connects the two electrode spaces in the perimeter, but electrically insulates and seals to the outside.
- the anode and cathode spaces must be electrically insulated from one another so that a short circuit does not occur.
- the electrodes lie flat over their entire surface - ie without any gaps - on the separator membrane. This is realized by one or more elastic spacers (X1, X2) inside the cell.
- the electrolytic cell is subjected to a slight overpressure atmosphere, which means the seal must be both chemical and pressure resistant.
- electrolytic half-cells are made of metal sheets gefer taken that have a thickness of at least 0.5 mm to give the cells sufficient stability and to ensure that they are not during transport or installation in a electrolyzer or an electrolysis stack.
- the disadvantage here is that the cells are very heavy and rigid, which causes problems during installation and of course also leads to a high material value.
- the invention relates to an electrolytic cell comprising or consisting of
- a slight negative pressure of, for example, 0.5 to 0.15 bar is applied to the electrolytic cells, so that the cells are present in a vacuum-stiffened state and in this way can be particularly easily and safely transported and then stacked.
- the anode and cathode are preferably arranged in the cell as shown in FIG. 1, namely in such a way that the two electrodes are positioned flat and gap-free relative to one another over their entire surface, with only the separator membrane making direct contact.
- the half-cells are preferably made of stainless steel, nickel or titanium and appropriate alloys, which may also contain other foreign metals such as vanadium.
- the spacers can be resilient elements such as coils, rings, foams, mattresses or rigid structures, as discussed at the outset in the prior art appreciation. They can be static or elastic, it being preferable to equip at least one electrode space with elastic spacers to ensure that the electrodes will lie flat.
- FIG. 2 schematically shows a cross-section of the perimeter (P) over which the sealant (D) is distributed; the separator membrane (S) can be seen in the middle, the ends of which are also enclosed by the sealing compound. In this way, the membrane is simultaneously fixed and stabilized in the cell.
- the plastic mass can be introduced using the usual methods of plastics processing, ie for example by thermal direct joining, gluing, hot melt or lamination. Direct thermal joining is particularly preferred due to its technical undemanding fluidity. It works very similar to the injection molding process: the plastic is liquefied and injected into the sealing surface. There, the polymer returns to its solid state when it cools down and seals the two half-cells.
- thermoplastics can be used as suitable electrically insulating plastics, with perfluoroalkoxy polymers (PFA) and polyphenylene sulfide (PPS) being preferred because of their high chemical resistance.
- connections that are known from the food industry, such as the weld-in spouts made of injection-mouldable plastic, as shown in Figure 3, are particularly suitable here.
- Corresponding connections or spouts are the subject of EP 2644530 A1 (POPPELMANN), whose teaching as far as the nature of the spout is concerned is included by reference.
- connections or spouts have a neck (3) provided with a pouring channel (2) having a vertical longitudinal center axis (1) and two outer side surfaces connected thereto, preferably provided with welding lines (4), which are used for welding to the Sealing of the electrolytic cell are provided and on the inside of the associated side walls a plurality of stiffening webs are arranged.
- the drains or spouts mentioned have a base, also known as a “boat”, the side walls of which have outer side surfaces which merge into one another in their end areas.
- the side surfaces are connected, especially welded, to and between the two foil walls of a container.
- a collar-like area is typically integrally formed on the boat or the side faces, which merges into a neck having a pouring channel having a vertical longitudinal center axis.
- a sol cher is often provided with a thread on the outside to a filled foil bag to be secured with a closure before emptying through the pouring channel.
- the neck can at least partially merge directly into the boat.
- the side surfaces of the boat can be flat, roughened, with or without ribs and/or provided with welding lines.
- the neck can have guide webs that can be used for guidance in a bottling or sealing system.
- connections or spouts are connected to the seal, as a rule, by ultrasonic welding.
- weld-in spouts are preferably incorporated directly into the joining process.
- electrolysis cells can be combined into groups that are referred to as “electrolyzers" or “electrolysis stacks”.
- electrolysis stacks Another subject of the invention therefore relates to an electrolysis stack, comprising or consisting of
- the two pressure plates face each other and are spaced apart movably or rigidly by the at least two tie rods and preferably in the connection by the tie rods there is a high electrical resistance or insulation;
- the at least two electrolytic cells are arranged or stacked between the two pressure plates in such a way that the cathodic rear wall of the first electrolytic cell is in contact with the anodic rear wall of the following electrolytic cell;
- the pressure plates are spaced apart from one another in such a way that there is a firm connection with the at least two vacuum-reinforced electrolytic cells.
- the stacks of the present invention preferably contain 3, 4, 5 or up to about 200 of said electrolytic cells. Preferably from about 40 to about 150 and more preferably from about 60 to about 120 are included.
- FIG. 4 A typical electrolysis stack is shown in FIG. 4, with the electrolysis cells that can be seen therein each having the structure shown in FIG.
- Also claimed is a method for producing an electrolysis stack, comprising or consisting of the following steps:
- step (b) electrically connecting the vacuum-stiffened electrolytic cells from step (a) in series by arranging or stacking them with one another in such a way that the cathodic rear wall of the first is in contact with the anodic rear wall of the following electrolytic cell;
- step (c) arranging the vacuum-reinforced electrolytic cells connected in series in accordance with step (b) with the aid of the at least two tie rods between the two pressure plates in such a way that a firm bond is formed, and
- a conventional single cell design can now also be applied to cells with a small wall thickness.
- these thin sheets or foils are used as a shell and are electrically separated from one another by the joint and the separator, with the internals being introduced in the manufacturing process.
- a vacuum is applied to the cells, which causes the elastic element or the mattress inside to be precompressed.
- the cells are vacuum-stiffened by this process, which offers the following advantages and has not yet corresponded to the state of the art in this technology:
- the cells By prestressing the elements, the cells can be placed in a stack that does not have to be equipped with a clamping device, but which presses the elastic elements together and offers the possibility of compression, including displacement of the pressure plate.
- the metallic pressure plates can easily be held together by tie rods and brought into simple contact with the vacuum-reinforced elements during initial assembly. By releasing the vacuum, the elastic elements are no longer stretched by the external pressure, but are now held in position by the pressure plates.
- the resulting stacks can be used, for example, in chlor-alkali electrolysis, but the preferred application is the production of hydrogen by water electrolysis.
- Another object of the invention relates to the use of the electrolysis cells according to the invention for the production of electrolysis stacks.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Mechanical Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Fuel Cell (AREA)
- Mechanical Treatment Of Semiconductor (AREA)
- Inert Electrodes (AREA)
- Electrodes For Compound Or Non-Metal Manufacture (AREA)
Abstract
Description
Claims
Priority Applications (7)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2023542491A JP2024506800A (ja) | 2021-02-17 | 2022-01-20 | 電解セル |
EP22702893.3A EP4294966A1 (de) | 2021-02-17 | 2022-01-20 | Elektrolysezelle |
CA3209497A CA3209497A1 (en) | 2021-02-17 | 2022-01-20 | Electrolytic cell |
US18/277,662 US20240218532A1 (en) | 2021-02-17 | 2022-01-20 | Electrolytic cell |
AU2022222172A AU2022222172A1 (en) | 2021-02-17 | 2022-01-20 | Electrolytic cell |
KR1020237031680A KR20230145190A (ko) | 2021-02-17 | 2022-01-20 | 전해 전지 (electrolytic cell) |
CN202280015185.6A CN116917548A (zh) | 2021-02-17 | 2022-01-20 | 电解池 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEDE102021103699.2 | 2021-02-17 | ||
DE102021103699.2A DE102021103699A1 (de) | 2021-02-17 | 2021-02-17 | Elektrolysezelle |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2022175011A1 true WO2022175011A1 (de) | 2022-08-25 |
Family
ID=80222438
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2022/051176 WO2022175011A1 (de) | 2021-02-17 | 2022-01-20 | Elektrolysezelle |
Country Status (9)
Country | Link |
---|---|
US (1) | US20240218532A1 (de) |
EP (1) | EP4294966A1 (de) |
JP (1) | JP2024506800A (de) |
KR (1) | KR20230145190A (de) |
CN (1) | CN116917548A (de) |
AU (1) | AU2022222172A1 (de) |
CA (1) | CA3209497A1 (de) |
DE (1) | DE102021103699A1 (de) |
WO (1) | WO2022175011A1 (de) |
Citations (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4664770A (en) * | 1985-01-16 | 1987-05-12 | Uhde Gmbh | Electrolyzer |
DE19526545A1 (de) * | 1994-07-20 | 1996-03-14 | Permelec Spa Nora | Elektrolyseur mit Ionenaustausch-Membran- oder Diaphragma |
US5599430A (en) | 1992-01-14 | 1997-02-04 | The Dow Chemical Company | Mattress for electrochemical cells |
JP2003041388A (ja) | 2001-07-31 | 2003-02-13 | Association For The Progress Of New Chemistry | イオン交換膜電解槽および電解方法 |
EP1766104B1 (de) | 2004-06-16 | 2007-11-28 | Uhdenora S.p.A | Elektrolysezelle |
US20070272549A1 (en) * | 2006-05-25 | 2007-11-29 | Davis James E | Electrolysis cell assembly |
EP1882758A1 (de) | 2005-05-17 | 2008-01-30 | Toagosei Co., Ltd. | Elektrolysezelle mit ionenaustauschmembran |
DE102011053142A1 (de) * | 2011-08-31 | 2013-02-28 | Kumatec Sondermaschinenbau & Kunststoffverarbeitung Gmbh | Elektrolyseur |
EP2644530A1 (de) | 2012-03-30 | 2013-10-02 | Pöppelmann Holding GmbH & Co. KG. | Einschweißausgießer |
EP2746429A1 (de) | 2012-12-19 | 2014-06-25 | Uhdenora S.p.A | Elektrolysezelle |
EP2356266B1 (de) | 2008-11-17 | 2015-06-24 | Uhdenora S.p.A | Elementarzelle und relevante modulare elektrolyseapparatur für elektrolytische verfahren |
EP1451389B1 (de) | 2001-12-03 | 2016-03-02 | Thyssenkrupp Uhde Chlorine Engineers (Italia) S.r.l. | Elastischer stromkollektor |
EP2872675B1 (de) | 2012-07-13 | 2018-12-19 | Thyssenkrupp Uhde Chlorine Engineers (Italia) S.r.l. | Elektrolysezellen umfassend einen dämmrahmen mit eckgekoppelten dehnfugen |
EP2734658B1 (de) | 2011-07-20 | 2019-06-05 | New Nel Hydrogen As | Rahmenkonzept für einen elektrolyseur, verfahren dafür und verwendung davon |
EP3575439A1 (de) * | 2017-01-26 | 2019-12-04 | Asahi Kasei Kabushiki Kaisha | Elektrolytisches bad, elektrolysevorrichtung, elektrolyseverfahren und verfahren zur herstellung von wasserstoff |
CN111663149A (zh) * | 2019-03-05 | 2020-09-15 | 湖南早晨纳米机器人有限公司 | 一种纳米发动机及其提供动力的方法和应用 |
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2021
- 2021-02-17 DE DE102021103699.2A patent/DE102021103699A1/de active Pending
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2022
- 2022-01-20 CA CA3209497A patent/CA3209497A1/en active Pending
- 2022-01-20 EP EP22702893.3A patent/EP4294966A1/de active Pending
- 2022-01-20 AU AU2022222172A patent/AU2022222172A1/en active Pending
- 2022-01-20 KR KR1020237031680A patent/KR20230145190A/ko active Search and Examination
- 2022-01-20 CN CN202280015185.6A patent/CN116917548A/zh active Pending
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CA3209497A1 (en) | 2022-08-25 |
EP4294966A1 (de) | 2023-12-27 |
AU2022222172A9 (en) | 2024-07-11 |
DE102021103699A1 (de) | 2022-08-18 |
US20240218532A1 (en) | 2024-07-04 |
KR20230145190A (ko) | 2023-10-17 |
AU2022222172A1 (en) | 2023-07-20 |
JP2024506800A (ja) | 2024-02-15 |
CN116917548A (zh) | 2023-10-20 |
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