EP4355930A1 - Elektrodenplatte für eine elektrolyse-anlage - Google Patents
Elektrodenplatte für eine elektrolyse-anlageInfo
- Publication number
- EP4355930A1 EP4355930A1 EP22726588.1A EP22726588A EP4355930A1 EP 4355930 A1 EP4355930 A1 EP 4355930A1 EP 22726588 A EP22726588 A EP 22726588A EP 4355930 A1 EP4355930 A1 EP 4355930A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- embossed
- strips
- linear
- electrode plate
- embossing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
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
- C25B9/60—Constructional parts of cells
- C25B9/65—Means for supplying current; Electrode connections; Electric inter-cell connections
-
- 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
- C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
- C25B11/02—Electrodes; Manufacture thereof not otherwise provided for characterised by shape or form
- C25B11/036—Bipolar 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
- 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
- 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
- C25B9/75—Assemblies comprising two or more cells of the filter-press type having bipolar electrodes
Definitions
- the invention relates to an electrode plate intended for use in an electrolysis system. Furthermore, the invention relates to a method for producing an electrode plate for an electrolysis system, in particular for the production of hydrogen.
- a device for generating hydrogen by means of electrolysis is described in EP 2 507 410 B1, for example.
- the electrolysis system described should be suitable for being operated with water which is taken from a salt, brackish or fresh water source.
- the water is fed to a carrier gas stream, so that at least part of the water is absorbed in evaporated form in the carrier gas stream.
- the carrier gas stream loaded in this way is finally fed to an electrolyzer.
- An electrolytic cell is known from EP 1 587 760 B1, which comprises several electrolytic plates.
- the electrolytic plates are fastened to groove devices within a housing.
- the housing of the known electrolytic cell has an inlet and an outlet to allow a fluid to flow through.
- a plurality of disks are arranged in a stacked form in the housing.
- An electrolysis plate described in DE 199 56 787 A1 consists of an outer, non-conductive frame and an electrically conductive, bipolar graphite plate mounted therein. Plastic aprons are provided for forcibly guiding electrolyte solutions in the area of an electrolyte feed.
- An arrangement of electrochemical cells known from DE 102013225 159 B4 which is provided, for example, for conducting water or aqueous electrolytes is seen, includes basic elements in the form of flat structures that have a network structure or are formed from a porous material. Several basic elements are arranged one above the other, with edge regions of the basic elements being connected in a fluid-tight manner with the aid of a filling compound.
- electrochemical systems described in the documents WO 2019/121947 A1 and WO 2020/030644 A1 each have arrangements of a plurality of separator plates, which delimit fluid spaces.
- the electrochemical systems described can be fuel cells or electrolytic cells.
- EP 3 725 916 A1 discloses an electrolysis plate intended for use in a device for generating hydrogen, which has an opening for gas to pass through, the edges of the opening being covered with an electrically non-conductive material.
- a bipolar electrical vessel is known from EP 3 575442 A1, which is provided for the production of hydrogen.
- the anode and/or cathode of the vessel is designed as a porous electrode.
- a membrane of the bipolar vessel is a porous membrane with inorganic components.
- the device according to EP 3 575 442 A1 is said to be suitable for alkaline electrolysis.
- the invention is based on the object of further developing the production of electrolysis plates in the form of electrode plates compared to the prior art, whereby production-related as well as electro-technical and flow-technical aspects should be taken into account.
- this object is achieved by an electrode plate having the features of claim 1 .
- the object is also achieved by a method for producing an electrode plate according to claim 10.
- the configurations and advantages explained below in connection with the production method also apply analogously to the device, ie to the electrode plate to be used in an electrolyzer, and vice versa.
- the electrode plate has a frame area that surrounds an active field on which electrochemical reactions take place in the completed system, ie in the electrolyzer.
- the active field is structured in three dimensions. In typical configurations, this does not apply to the frame region. This is designed flat and is formed by undeformed, flat sheet metal, which forms a base plane.
- the active field like the frame area and thus the entire electrode plate, has a rectangular, typically not square, basic shape.
- an embossed structure in the form of individual embossed elements that are raised and recessed starting from the base level, including a large number of linear, i.e. straight, embossed strips.
- the linear embossed ledges are positioned in a row and column arrangement in such a way that alternating raised and recessed linear embossed ledges are formed both in the row and in the column direction, with all linear embossed ledges of a row facing the long sides of the active field and one in the same way parallel direction of flow for fluids are inclined and the linear embossed strips of the next line have the opposite, equal amount in terms of inclination.
- the embossed strips contribute both to the mechanical stability of the electrode plate and to flow conduction.
- the arrangement of the linear embossed strips which takes place in a herringbone pattern, enables a particularly uniform flow and fluid distribution with regard to the fluids flowing past in the area of the surface of the electrode plate. Furthermore, the reshaping of the sheet metal from the base plane in both directions perpendicular to the base plane results in an enormous gain in mechanical stability of the electrode plate, which allows the use of particularly thin metal sheets, particularly in the range from 150 ⁇ m to 500 ⁇ m.
- Further components of the electrolytic cells can adjoin the linear embossed strips of the electrode plate.
- the boundary areas between the elongated, linear embossing strips and the other components are flat in this case, which is advantageous both with regard to mechanical loads and with regard to the flow of electrical charges. This is particularly relevant in large-scale electrolysis plants for the production of hydrogen.
- a sub-cluster of the embossing structure is formed by two rows of linear embossing strips, with a total of at least four such sub-clusters being connected in series, for example.
- the series connection refers to the direction of flow of the fluid or electrolyte, which in a typical configuration corresponds to the longitudinal direction of the electrode plate.
- Variants can also be implemented in which a sub-cluster is made up of more than two rows of linear embossing strips.
- the distance between two sub-clusters can correspond, for example, to at least 5% and at most 10% of the projected length of the linear embossing strips arranged in a row, to be measured in the longitudinal direction of the electrode plate.
- the embossing elements which in addition to linear embossing strips can also represent embossing points in particular, have comparatively small dimensions compared to the length and width of the active field in numerous possible designs of the electrode plate made of sheet metal, for example stainless steel or titanium. sung.
- the electrode plate made of sheet metal, for example stainless steel or titanium. sung.
- at least three raised and at least three recessed embossed elements, in particular linear embossed strips, are arranged in each row.
- the raised linear embossed ledges can have the full length, which is also the case for the linear embossed ledges of the other lines, whereas the recessed linear embossed ledges have the same length greatly shortened, in particular at most half as long, linear embossing ledges are formed, the shortening of the recessed linear embossing ledges being given towards the edge of the embossing structure.
- the raised linear embossed ridges on the input-side and/or output-side edge of the embossed structure can be shorten.
- the one-sided shortening of the linear embossing strips can be used in any case to bring a component of the electrolysis stack, for example a frame or a seal, into surface contact with the electrode plate.
- the height of the raised linear embossing ledges differs from the height of the recessed linear embossing ledges, with the appearance of a linear embossing ledge as “raised” or “recessed” always depending on which side of the metal sheet the linear embossing ledge is viewed from will.
- the term “embossing depth” is also used.
- the embossing depth shall be measured orthogonally to the base plane of the undeformed metal sheet.
- the embossing structure is asymmetric because of the different embossing depths on one side and the other side of the sheet metal.
- the electrode plate can be produced efficiently by forming methods by producing a large number of individual embossed elements which protrude to different extents from the surfaces of the undeformed metal sheet on both sides of the electrode plate and together describe a herringbone pattern on each side of the electrode plate.
- the electrode plate including the structure present as a herringbone pattern, can be provided with a single-layer or multi-layer coating.
- the entire electrode plate is not necessarily coated in a uniform manner.
- a coating can only be provided in the active field, but not in the frame area. It is also possible to coat the frame area in a way that differs from the active field.
- an advantage of the electrode plate is, in particular, that a three-dimensional, double-sided design supports a laminar media flow that is evenly distributed over the active field.
- the elevations and depressions in the active field provided they do not merely protrude from the surface in a punctiform manner, can be strongly modified and based on a sinusoidal shape.
- flanks of the linear embossing strips are inclined at an angle of 30° to 60° to the plane in which the surface of the metal sheet that is not deformed or not significantly deformed is located, resulting in a trapezoidal cross-sectional configuration in both the longitudinal and transverse directions direction can be given.
- the individual linear embossing strips can be set at an angle of 45° ⁇ 15° relative to the longitudinal sides of the electrode plate, which is uniform in amount, for example. Together with the described longitudinal and cross-sectional design, this results in a streamlined tender effect designed to avoid dead spaces during operation of the electrolyser, with the formation of stationary vortices in depressions in particular being minimized.
- the arrangement, in particular herringbone-like arrangement, of the linear embossing strips positioned at an angle to the flow direction of the fluid or electrolyte is flanked by two sensitive rows of embossed elements, for example embossed points, on the long sides of the active field, which are aligned in the column direction of the embossed structure.
- embossed elements for example embossed points
- These embossing elements which are small compared to the linear embossing strips and are almost punctiform in particular and which are each located in a strip at the edge of the active field, i.e. at the transition to the frame area, have the effect that the flow is calmed in the narrow areas concerned occurs, in particular flow components are damped tivfeldes orthogonal to the longitudinal direction of the electrode plate compared to the middle of the Ak.
- embossed elements can also be present in the lateral areas of the active field, which extend from the inflow area to the outflow area of the fluid or electrolyte, which each describe a V-shape, with at the beginning and at the end of each line such a V-shaped embossing element is located on linear embossing.
- the V-legs of the embossing elements are directed towards the linear embossing strips arranged in cells. This means that each line of slanted linear embossing bars is enclosed by two V-shaped embossing elements in the manner of an "open angle bracket” character and a "close angle bracket” character.
- the V-shaped embossed elements appearing as pointed brackets can be dimensioned in such a way that they are only partially covered by a component of the electrolysis stack resting on the electrode plate.
- the component, through which a frame step can be formed, is located outside of the active surface, with the channel-like depressions, which are given in the form of the V-legs, protruding from the cover, while the central bend of each V-shaped Embossing element under the cover is located.
- This constellation achieves two advantages: on the one hand, a non-functional media flow at the edge of the active field is largely prevented; on the other hand, a small flow of media is permitted through the channels, which are formed by the V-shaped embossed elements, with which the accumulation of fluids in dead spaces is avoided.
- the structuring of the electrode plate ensures that the flowing electrolyte or the fluid also experiences a movement component normal to the plane that is defined by the base plane.
- These flow components away from the base level - or also towards the base level - are generated, among other things, by the fact that rows of linear embossed ridges that follow one another in the direction of flow are made up of alternating embossed ridges, which in a first row are at a uniform angle to the longitudinal direction of the active field and are also slanted in the following line with the opposite orientation and the same amount of angle, whereby the flank angles already mentioned, which are given with every linear embossed strip and also with the punctiform and any other embossed elements, also play a role.
- Fig. 1 shows a first embodiment of an electrode plate for an Elektroly se plant in plan view
- Fig. 2 shows a second embodiment of an electrode plate for an electrolysis system in a view analogous to Fig. 1,
- FIG. 3 shows a detail of an embossed structure of an electrode plate in plan view, 4 and 5 the embossing structure in sectional views,
- FIGS. 4 and 5 shows a further top view of the embossed structure with schematic marking of the cutting lines (to FIGS. 4 and 5),
- FIG. 7 a perspective view of an electrode plate with V-shaped embossed elements on the long sides of the active field
- FIG. 8 a perspective rear view of an electrode plate with greatly shortened embossed strips in the inlet and outlet area of the active field
- FIG. 9 shows the electrode plate according to FIG. 7 in a schematic view analogous to FIG. 6,
- FIG. 10 shows the electrode plate according to FIG. 8 in a schematic view analogous to FIG.
- An electrode plate is made of sheet steel and is provided for use in an electrolysis system for hydrogen production, not shown in further detail, also known as the electrolysis system 10 for short.
- an electrolysis system for hydrogen production not shown in further detail, also known as the electrolysis system 10 for short.
- the electrode plate 1 is formed of a metal sheet and has a rectangular non-square shape with a planar frame portion 2 having a three-dimensional shape structured active surface 3 surrounds.
- the frame area 2 there are several circular openings 4, 5 of different sizes in the exemplary embodiment, which can be used, among other things, for the passage of media or for the insertion of tie rods to hold together a stack of electrolytic cells.
- the sheet metal is present in the frame area 2 undeformed in a flat plate shape.
- the undeformed, flat metal sheet forms a base plane E (compare FIG. 5), from which the embossed structures 6 are formed upwards and downwards out of the base plane E.
- the embossed structure 6 which protrudes from the base plane E of the electrode plate 1 on both sides.
- the embossed structure 6 is designated as a raised embossed area 8 (compare FIG. 4), which rises out of the base plane E towards the viewer.
- the raised NEN embossed areas 8 alternate with deepened embossed areas 9, which also rise out of the base plane E, but away from the viewer.
- the embossed structure 6 is divided in the form of sub-clusters 11, as can be seen in particular from FIG. 3, which relates both to the exemplary embodiment according to FIG. 1 and to the exemplary embodiment according to FIG. Overall, there is a row-column pattern of the embossed structure 6, with each sub-cluster 11 comprising two rows of linear embossed strips 14, 15.
- the flow direction of the electrolyte corresponds to the longitudinal direction of the active field 3 and of the entire electrode plate 1 .
- the individual embossing strips 14, 15 are set at an angle a of 45° ⁇ 15°, which is uniform in amount, relative to the direction of flow DR.
- the full length of each embossing bar 14, 15 is denoted by L, and the length projected transversely to the flow direction DR, ie optically shortened, is denoted by L'.
- the distance between two sub-clusters 11 denoted by A' is to be measured in the flow direction DR, like the length L', and is 5% to 10% of the projected length L'.
- the lengths L, L' are also referred to as lamella length or projected lamella length.
- embossed points 16, 17 in the form of raised points 16 and recessed points 17 starting from the base plane E are also formed in the active surface 3 in the embodiments according to FIGS .
- the linear embossing strips 14, 15 and embossing points 16, 17 are also referred to as embossing elements.
- the embossed elements 14, 16 attributable to the raised embossed area 8 are identified by solid lines and the recessed embossed elements 15, 17 by dashed lines.
- embossing points 16, 17, raised embossing elements 14, 16 and recessed embossing elements 15, 17 are arranged alternately in each row.
- a raised linear embossing strip 14 and a recessed linear embossing strip 15 always alternate, so that in all cases overall, the embossing strips 14, 15 are arranged in a herringbone pattern.
- a number of sub-clusters 11 of at least 2, in particular more than 5, is preferably present
- a first edge cluster 13 could also be formed from—starting from the base plane E—raised embossing points 16 and recessed embossing points 17 in alternation be.
- the embossing points 16, 17, from which the edge clusters 13, which are either completely the raised embossing area 8 or completely the recessed embossing area 9 are to be attributed are constructed, linienför mig lined up next to those embossing points 16, 17, the mark the beginning and end of each line of linear embossing strips 14, 15 in the manner already described.
- the embossing depth of the raised embossing area 8, denoted by hi differs, i.e. the fleas of the embossing elements 14, 16 , Clearly, namely by more than the plate thickness of the electrode plate 1, designated s, from the embossing depth, designated h2, of the depressed embossing area 9.
- the first side 7 of the electrode plate 1 lies in the present cases in the x-y plane.
- the embossed elements 14, 15, 16, 17 extend in the z-direction.
- the designated 18 flanks at the two ends of each embossing bar 15, 16 are at an angle ß of 45 ° ⁇ 15 ° obliquely to the x-y plane is ge.
- FIG. 5 which shows a section BB transverse to the extension of the embossing bar 15, 16 (compare FIG. 6), the structure width in the raised embossed area 8 is indicated with Bi and the structure width in the recessed embossed area 9 with B2. 5 also shows an angle g, with the inclination of the flanks 18 on the longitudinal sides of the embossing strip 15, 16 in this case corresponding to the difference between 180° and the angle g and, like the angle ⁇ , in the range of 30° up to 60°.
- a trapezoidal profiling of the linear embossing strips 14, 15 can be seen both in FIG. 4 and in FIG. Plateaus of the linear embossing strips 14, 15, which lie in planes parallel to the first side 7 and spaced apart from this by h1 or h2, are denoted by 19 in FIG. Deviating from the idealized depiction according to FIGS. 4 and 5, the transitions between the plateaus 19 and the flanks 18 as well as the transitions between the flanks 18 and the first th page 7 be rounded. All embossing elements 14, 15, 16, 17 are made by forming methods. The application of coatings to the active surface 3 is possible before and/or after the forming.
- the edge clusters 13 are provided by V-shaped embossed elements 20, 21.
- the embossed element 20 appears as a typographic symbol "open angle bracket” and the embossed element 20 as a typographic symbol “close angle bracket” at the beginning and end of each line on inclined linear embossed bars 14, 15.
- the flow direction DR corresponds to Fig. 9 , as in Fig. 6, the x-direction.
- the V-shaped embossing elements 20, 21 directly next to the V-shaped embossing elements 20, 21, there are shortened, recessed or raised embossing ridges 22, 23 compared to the embossing ridges 14, 15.
- the length of these shortened ones Stamping strips 22, 23 is more than half the full length L of the remaining stamping strips 14, 15.
- FIGS. 8 and 10 there are also modifications in the entry area and in the exit area of the active field 3.
- Figure 8 shows the side of the electrode plate 1 arbitrarily referred to as the "back side".
- Figure 10 is the "front side" of the electrode plate 1 represented in a symbolized way.
- a greatly shortened, recessed linear embossing strip 24 is arranged in the inlet area of the active field 3 between two raised linear embossing strips 14 .
- the length of the shortened linear embossing strips 24 is less than half the otherwise uniform length L of the linear embossing strips 14, 15 component shown and the first side 7 of the electrode plate 1 can be produced, where there is an overlap between the unabridged linear embossing strips 14 and the ge-mentioned component.
- all four edge areas of the overall rectangular embossed structure 6 are modified in comparison to the central area of the embossed structure 6 formed exclusively from the linear embossed strips 14 15 .
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Electrodes For Compound Or Non-Metal Manufacture (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
Description
Claims
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102021115582 | 2021-06-16 | ||
| DE102022112593.9A DE102022112593A1 (de) | 2021-06-16 | 2022-05-19 | Elektrodenplatte für ein Elektrolysesystem |
| PCT/DE2022/100387 WO2022262894A1 (de) | 2021-06-16 | 2022-05-20 | Elektrodenplatte für eine elektrolyse-anlage |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| EP4355930A1 true EP4355930A1 (de) | 2024-04-24 |
| EP4355930C0 EP4355930C0 (de) | 2025-04-30 |
| EP4355930B1 EP4355930B1 (de) | 2025-04-30 |
Family
ID=81854643
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP22726588.1A Active EP4355930B1 (de) | 2021-06-16 | 2022-05-20 | Elektrodenplatte für eine elektrolyse-anlage |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US20240279827A1 (de) |
| EP (1) | EP4355930B1 (de) |
| JP (1) | JP7615355B2 (de) |
| WO (1) | WO2022262894A1 (de) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115852413B (zh) * | 2022-12-26 | 2023-12-08 | 张家港氢云新能源研究院有限公司 | 一种电解制氢用非均匀双极式乳突板 |
| DK181744B1 (en) * | 2023-01-13 | 2024-11-20 | Stiesdal Hydrogen As | Electrolyser and method for its operation |
| EP4456209A1 (de) * | 2023-04-24 | 2024-10-30 | Oberland Mangold GmbH | Geprägte bipolarplatte |
| DE102024111490A1 (de) * | 2024-04-24 | 2025-10-30 | Schaeffler Technologies AG & Co. KG | Bipolarplatte, Plattenanordnung und Elektrolyseur |
| DE102024126587A1 (de) * | 2024-09-16 | 2026-03-19 | Oberland Mangold Gmbh | Geprägte Bipolarplatte |
Family Cites Families (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3062540B2 (ja) * | 1997-10-27 | 2000-07-10 | 工業技術院長 | 水電解槽用複極板及びそれを用いたセル |
| DE19956787A1 (de) | 1999-11-25 | 2001-05-31 | Bayer Ag | Elektrolyseplatte |
| US6586128B1 (en) * | 2000-05-09 | 2003-07-01 | Ballard Power Systems, Inc. | Differential pressure fluid flow fields for fuel cells |
| GB2387476B (en) * | 2002-06-24 | 2004-03-17 | Morgan Crucible Co | Flow field plate geometries |
| BRPI0406590A (pt) | 2003-01-21 | 2006-01-17 | Sev Trent De Nora Llc | Célula eletrolìtica |
| BRPI0920161A2 (pt) * | 2008-10-30 | 2020-08-11 | Emefcy Limited | eletrodos para utilização em, células de combustível bacterianas e células de eletrólise bacterianas e células de combustível bacterianas e células de eletrólise bacterianas que empregam tais eletrodos |
| JP4796639B2 (ja) * | 2009-02-26 | 2011-10-19 | 本田技研工業株式会社 | 電気化学装置 |
| WO2011066841A1 (de) | 2009-12-01 | 2011-06-09 | Neubert, Susanne | Verfahren und vorrichtung zum erzeugen von wasserstoff mittels elektrolyse |
| DE202011102525U1 (de) | 2011-06-28 | 2011-10-20 | Udo Mürle | Steuereinheit zur Regelung von Wasserstoffelektrolyse, Wasserstoffspeicherung und Stromerzeugung aus Wasserstoffspeichern am Stromnetz |
| CN105121808A (zh) | 2013-03-15 | 2015-12-02 | Nrg物流有限公司 | 氢按需电解燃料电池系统 |
| DE102013225159B4 (de) | 2013-12-06 | 2016-02-25 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Anordnung elektrochemischer Zellen |
| FR3049392B1 (fr) * | 2016-03-24 | 2018-04-20 | Commissariat A L'energie Atomique Et Aux Energies Alternatives | Plaque bipolaire de cellule electrochimique a tenue mecanique amelioree |
| JP6746721B2 (ja) | 2017-01-26 | 2020-08-26 | 旭化成株式会社 | 複極式電解槽、アルカリ水電解用複極式電解槽、及び水素製造方法 |
| AU2018256429B2 (en) * | 2017-04-20 | 2023-04-27 | Axine Water Technologies Inc. | Electrochemical cell for wastewater treatment with improved electrical protection |
| DE202017107797U1 (de) | 2017-12-20 | 2019-03-25 | Reinz-Dichtungs-Gmbh | Elektrochemisches System |
| FR3076953A1 (fr) * | 2018-01-18 | 2019-07-19 | Commissariat A L'energie Atomique Et Aux Energies Alternatives | Ensemble de cellules pour adaptation de puissance de reacteurs electrochimiques |
| US11670780B2 (en) * | 2018-04-28 | 2023-06-06 | Enomoto Co., Ltd. | Fuel cell gas supply and diffusion layer, fuel cell separator and fuel cell stack |
| DE202018104628U1 (de) | 2018-08-10 | 2019-11-14 | Reinz-Dichtungs-Gmbh | Elektrochemisches System |
| EP3725916A1 (de) | 2019-04-19 | 2020-10-21 | Ecovitus B.V. | Verbesserte elektrolyseplatte |
| CN110571451A (zh) * | 2019-09-30 | 2019-12-13 | 天津商业大学 | 一种燃料电池的流场结构 |
-
2022
- 2022-05-20 JP JP2023570400A patent/JP7615355B2/ja active Active
- 2022-05-20 US US18/571,125 patent/US20240279827A1/en active Pending
- 2022-05-20 WO PCT/DE2022/100387 patent/WO2022262894A1/de not_active Ceased
- 2022-05-20 EP EP22726588.1A patent/EP4355930B1/de active Active
Also Published As
| Publication number | Publication date |
|---|---|
| JP7615355B2 (ja) | 2025-01-16 |
| EP4355930C0 (de) | 2025-04-30 |
| JP2024517357A (ja) | 2024-04-19 |
| EP4355930B1 (de) | 2025-04-30 |
| WO2022262894A1 (de) | 2022-12-22 |
| US20240279827A1 (en) | 2024-08-22 |
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