WO2023117087A1 - Procédé de création d'une couche d'oxyde de passivation sur un composant en acier inoxydable d'une cellule électrochimique - Google Patents
Procédé de création d'une couche d'oxyde de passivation sur un composant en acier inoxydable d'une cellule électrochimique Download PDFInfo
- Publication number
- WO2023117087A1 WO2023117087A1 PCT/EP2021/087343 EP2021087343W WO2023117087A1 WO 2023117087 A1 WO2023117087 A1 WO 2023117087A1 EP 2021087343 W EP2021087343 W EP 2021087343W WO 2023117087 A1 WO2023117087 A1 WO 2023117087A1
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- WO
- WIPO (PCT)
- Prior art keywords
- stainless steel
- steel component
- heat treatment
- donor
- component
- Prior art date
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- 229910001220 stainless steel Inorganic materials 0.000 title claims abstract description 59
- 239000010935 stainless steel Substances 0.000 title claims abstract description 57
- 238000000034 method Methods 0.000 title claims abstract description 36
- 238000004519 manufacturing process Methods 0.000 claims abstract description 6
- 238000010438 heat treatment Methods 0.000 claims description 30
- 239000000446 fuel Substances 0.000 claims description 24
- 239000007787 solid Substances 0.000 claims description 19
- 230000001590 oxidative effect Effects 0.000 claims description 17
- 239000007800 oxidant agent Substances 0.000 claims description 15
- 229910052804 chromium Inorganic materials 0.000 claims description 13
- 229910052782 aluminium Inorganic materials 0.000 claims description 11
- 229910052684 Cerium Inorganic materials 0.000 claims description 10
- 229910052735 hafnium Inorganic materials 0.000 claims description 10
- 229910052748 manganese Inorganic materials 0.000 claims description 10
- 229910052750 molybdenum Inorganic materials 0.000 claims description 10
- 229910052758 niobium Inorganic materials 0.000 claims description 10
- 229910052710 silicon Inorganic materials 0.000 claims description 10
- 229910052719 titanium Inorganic materials 0.000 claims description 10
- 229910052720 vanadium Inorganic materials 0.000 claims description 10
- 238000000576 coating method Methods 0.000 claims description 8
- 239000011248 coating agent Substances 0.000 claims description 6
- 239000003792 electrolyte Substances 0.000 claims description 6
- 239000007789 gas Substances 0.000 claims description 4
- 239000001301 oxygen Substances 0.000 claims description 4
- 229910052760 oxygen Inorganic materials 0.000 claims description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 3
- 239000010410 layer Substances 0.000 description 24
- 229910052751 metal Inorganic materials 0.000 description 11
- 239000002184 metal Substances 0.000 description 11
- 239000011651 chromium Substances 0.000 description 9
- 229910000831 Steel Inorganic materials 0.000 description 7
- 239000010959 steel Substances 0.000 description 7
- 239000000203 mixture Substances 0.000 description 6
- 230000007797 corrosion Effects 0.000 description 4
- 238000005260 corrosion Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 239000002243 precursor Substances 0.000 description 3
- 239000011241 protective layer Substances 0.000 description 3
- 239000007784 solid electrolyte Substances 0.000 description 3
- 239000000758 substrate Substances 0.000 description 3
- 229910001233 yttria-stabilized zirconia Inorganic materials 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N Alumina Chemical group [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 125000006850 spacer group Chemical group 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 241000877463 Lanio Species 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical group [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- QAISYPNSOYCTPY-UHFFFAOYSA-N cerium(3+) gadolinium(3+) oxygen(2-) Chemical compound [O--].[O--].[O--].[Ce+3].[Gd+3] QAISYPNSOYCTPY-UHFFFAOYSA-N 0.000 description 1
- 230000007850 degeneration Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 229910021526 gadolinium-doped ceria Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 229910052746 lanthanum Inorganic materials 0.000 description 1
- 229910000480 nickel oxide Inorganic materials 0.000 description 1
- 229910002119 nickel–yttria stabilized zirconia Inorganic materials 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- GNRSAWUEBMWBQH-UHFFFAOYSA-N oxonickel Chemical compound [Ni]=O GNRSAWUEBMWBQH-UHFFFAOYSA-N 0.000 description 1
- -1 oxygen ions Chemical class 0.000 description 1
- 231100000572 poisoning Toxicity 0.000 description 1
- 230000000607 poisoning effect Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000011253 protective coating Substances 0.000 description 1
- 238000010345 tape casting Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
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- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0206—Metals or alloys
- H01M8/0208—Alloys
- H01M8/021—Alloys based on iron
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- C23C10/00—Solid state diffusion of only metal elements or silicon into metallic material surfaces
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- C23C10/34—Embedding in a powder mixture, i.e. pack cementation
- C23C10/36—Embedding in a powder mixture, i.e. pack cementation only one element being diffused
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- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C10/00—Solid state diffusion of only metal elements or silicon into metallic material surfaces
- C23C10/28—Solid state diffusion of only metal elements or silicon into metallic material surfaces using solids, e.g. powders, pastes
- C23C10/34—Embedding in a powder mixture, i.e. pack cementation
- C23C10/36—Embedding in a powder mixture, i.e. pack cementation only one element being diffused
- C23C10/38—Chromising
- C23C10/40—Chromising of ferrous surfaces
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- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C10/00—Solid state diffusion of only metal elements or silicon into metallic material surfaces
- C23C10/28—Solid state diffusion of only metal elements or silicon into metallic material surfaces using solids, e.g. powders, pastes
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- C23C10/48—Aluminising
- C23C10/50—Aluminising of ferrous surfaces
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- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C10/00—Solid state diffusion of only metal elements or silicon into metallic material surfaces
- C23C10/28—Solid state diffusion of only metal elements or silicon into metallic material surfaces using solids, e.g. powders, pastes
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- C23C10/52—Embedding in a powder mixture, i.e. pack cementation more than one element being diffused in one step
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- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
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- C23C10/52—Embedding in a powder mixture, i.e. pack cementation more than one element being diffused in one step
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- C23C10/52—Embedding in a powder mixture, i.e. pack cementation more than one element being diffused in one step
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- C23C8/00—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
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- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C8/00—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
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- C23C8/08—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases only one element being applied
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- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
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- C23C8/10—Oxidising
- C23C8/12—Oxidising using elemental oxygen or ozone
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- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
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- C25B11/02—Electrodes; Manufacture thereof not otherwise provided for characterised by shape or form
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- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/12—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/12—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
- H01M8/1286—Fuel cells applied on a support, e.g. miniature fuel cells deposited on silica supports
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/12—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
- H01M2008/1293—Fuel cells with solid oxide electrolytes
-
- 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
- Y02E60/50—Fuel cells
Definitions
- the invention relates to the field of electrochemical cells, and, in particular, relates to metal-supported electrochemical cells. More specifically, the invention relates to the field of solid oxide cells, including metal-supported solid oxide cells.
- Solid oxide cells comprise three basic parts: a fuel electrode, a solid electrolyte, and an air or oxidant electrode, which are commonly arranged in layers. They may be tubular or planar in configuration. Multiple planar solid oxide cell units may be arranged overlying one another to form a "stack", with the individual cell units arranged electrically in series. SOCs typically operate at temperatures ranging from 600 °C to 1000 °C.
- SOCs can be run as solid oxide fuel cell (SOFC) or as solid oxide electrolyser cell (SOEC).
- SOFCs are energy conversion devices that allow for conversion of electrochemical fuel to electricity. More specifically, SOFCs use an electrochemical conversion process that oxidises fuel to produce electricity. For this, a fuel, or reformed fuel, contacts the fuel electrode and an oxidant, such as air or an oxygen rich fluid, contacts the oxidant electrode. The solid oxide electrolyte then conducts negative oxygen ions from the oxidant electrode to the fuel electrode.
- the fuel electrode constitutes the anode and the air or oxidant electrode constitutes the cathode.
- SOECs are SOCs run in reverse mode compared to SOFCs and are commonly used for the electrolysis of water, in particular for generating hydrogen and oxygen gas.
- the fuel electrode constitutes the cathode and the air or oxidant electrode constitutes the anode.
- Fuel electrode, solid electrolyte and air or oxidant electrode may be selfsupported ("electrolyte-supported", “cathode-supported”, or “anode-supported” SOC) or arranged in layers on a mechanical support.
- the mechanical support and also other components forming part of the cell repeat unit are preferably made of stainless steel which offers several advantages over conventionally used materials such as ceramics.
- mechanical supports made from stainless steel allow for a more compact design of the SOC and, thus, for a higher power density.
- Such SOCs are commonly referred to as metal-supported SOCs ("MS-SOC").
- the mechanical support may be an intrinsically porous metal substrate formed from a powder metal precursor (for example, by tape casting), or, more preferably, is formed from a metal support plate provided with a porous region in the form of through holes or small apertures surrounded by a non-porous (solid) region.
- the porous region is provided through the metal support plate, and a fuel electrode layer is coated over that region, and then successive layers coated on top, which layers are thus supported by the metal support plate.
- the invention relates to a method for creating a passivating oxide layer on a stainless steel component of an electrochemical cell.
- the method comprises a step (i) of enriching a surface zone of the stainless steel component with at least one oxide-forming donor element selected from the list consisting of Cr, Mn, Si, Mo, Nb, Ti, V, Al, Hf, and Ce.
- the concentration of at least one donor element selected from the list consisting of Cr, Mn, Si, Mo, Nb, Ti, V, Al, Hf, and Ce is increased in a region near the surface of the stainless steel component.
- This step (i) of enriching the surface zone comprises a step of heat treating the stainless steel component in an enclosure, e.g. in a vacuum oven.
- at least one donor component is present together with the stainless steel component.
- the at least one donor component comprises, preferably consists of, one or more of the donor elements Cr, Mn, Si, Mo, Nb, Ti, V, Al, Hf, and Ce.
- the heat treatment is conducted at a temperature of at least 900°C and at most 1300°C.
- the heat treatment is conducted under a pressure of at least 5 mbar and at most 500 mbar.
- the at least one donor element contained in the at least one donor component partially evaporates. This results in a certain partial pressure of the at least one donor element being present in the enclosure and, consequently, to adsorption of the at least one donor element at the surface of the stainless steel component.
- the at least one donor element diffuses into the stainless steel component creating a surface zone with an increased (enriched) concentration of the at least one donor element compared to the bulk.
- the stainless steel component is oxidized in a step (ii) by a second heat treatment.
- the at least one donor element enriched in the surface zone of the stainless steel component is oxidized to form a passivating oxide layer on the stainless steel component.
- the second heat treatment of step (ii) may be performed in the same enclosure as the heat treatment of step (i). Alternatively, the second heat treatment may be performed in a different enclosure, e.g. in a vacuum oven.
- the proposed method allows for cheap manufacturing of a protective layer that is highly oxidation resistant and prevents chromium evaporation from the stainless steel component.
- the method does not require expensive coating equipment, which reduces process costs.
- the proposed method does not rely on coating a full layer of an oxide-forming donor element on the stainless steel component, but is based on increasing the concentration of the at least one donor elements in a surface zone of the stainless steel component.
- process parameters e.g. elemental composition of the at least one donor component, pressure in the enclosure and temperature in the enclosure, the amount of material diffusing into the stainless steel component can be precisely tuned, e.g. dependent on the elemental composition of the stainless steel component.
- a further advantage of the proposed method is that the process of adsorption of the at least one donor element on the surface of the stainless steel component is not directed, i.e. not limited to surfaces exposed to a certain coating direction. This allows protective coatings to also be formed on complex shaped components, e.g. in undercuts or holes.
- the stainless steel component may be a ferritic steel component.
- the stainless steel component may be a mechanical support, a gas permeable carrier or an interconnector component of an electrochemical cell.
- the stainless steel component may be any plate or sheet stainless steel component forming part of the electrochemical cell (for example, a spacer plate, or current collection plate).
- the stainless steel component is a component of a solid oxide fuel cell or a solid oxide electrolyser cell.
- the stainless steel component may be a mechanical support or a gas permeable support layer of a metal-supported electrochemical cell, such as, for example, a SOC.
- the stainless steel component may be an intrinsically porous metal substrate formed from a powder metal precursor or may be formed from a metal support plate provided with a porous region in the form of through holes or small apertures surrounded by a non-porous (solid) region.
- the method is not limited to such components, but can be applied to other stainless steel components as well.
- step (i) the heat treatment is conducted at a temperature of at least 1000°C and at most 1150°C.
- step (i) the heat treatment is conducted for at least 1h and at most 24h.
- the heat treatment may be conducted in an inert gas atmosphere.
- the heat treatment is conducted in an atmosphere containing, in particular consisting of, one or more of Ar, He or N2.
- the heat treatment in step (i) may be conducted in a reducing atmosphere, e.g. in an atmosphere containing, in particular consisting of, H2. It is also possible that the heat treatment in step (i) is conducted in an atmosphere consisting of a mixture of two or more of Ar, He, N2 and H2.
- the concentration of the at least one donor element in the donor component is at least twice as high as the initial concentration of the at least one donor element in the stainless steel component before the step of enriching the surface zone.
- the material composition of the surface zone of the stainless steel component and, thus, the material composition of the passivating oxide layer formed after heat treatment in step (ii) may be tuned depending on the configuration of the at least one donor component, e.g. depending on the number and elemental composition of donor components present in the enclosure.
- a single donor component may be present in the enclosure, wherein the single donor component comprises or consists of one or more of the donor elements selected from the list consisting of Cr, Mn, Si, Mo, Nb, Ti, V, Al, Hf, Ce.
- two or more donor components may be present in the enclosure.
- a first donor component may be present consisting of a first donor element selected from the list consisting of Cr, Mn, Si, Mo, Nb, Ti, V, Al, Hf, Ce and a second donor component may be present consisting of a second donor element selected from from the list consisting of Cr, Mn, Si, Mo, Nb, Ti, V, Al, Hf, Ce, said first donor element and said second donor element being different.
- the second heat treatment is conducted at a temperature of at least 700°C and at most 1000°C.
- the second heat treatment step is conducted in an oxygen donating atmosphere.
- the second heat treatment step is conducted in an H2O and/or O2 containing atmosphere.
- the second heat treatment may be conducted for at least 30 min and at most 16h. Preferably, the second heat treatment is conducted for at least 30 min and at most 3h.
- the invention also relates to a method for manufacturing an electrochemical cell.
- the electrochemical cell comprises at least a fuel electrode, an electrolyte, an air or oxidant electrode, and at least one component made of stainless steel.
- the fuel electrode may be composed of nickel oxide or Ni-YSZ (Yttria-stabilized zirconia).
- the solid electrolyte layer may be composed of Yttria- stabilized zirconia (YSZ), Gadolinia-doped Ceria or Cerium Gadolinium Oxide (CGO).
- the air or oxidant electrode may be composed of (La,Sr)MnOs, (La, Sr)CoOs, LaNiOs, or LaFeOs.
- the method for manufacturing the electrochemical cell comprises a step of providing the at least one stainless steel component and creating a passivating oxide layer on said at least one stainless steel component by a method as described above.
- the features and advantages explained above in connection with the method of creating a passivating oxide layer are also applicable to the method for manufacturing the electrochemical cell. After creating the passivating oxide layer on the at least one stainless steel component, that is to say, after performing at least step (i) and step (ii) as discussed above, the electrochemical cell is assembled in a subsequent step.
- the step of assembling the electrochemical cell comprises steps of applying a fuel electrode, an electrolyte, and an air or oxidant electrode (where the order of the electrode layers may be reversed depending on the type of cell), in particular on the at least one stainless steel component.
- the electrochemical cell may be a solid oxide cell, preferably a metal-supported solid oxide cell.
- the electrochemical cell may be a solid oxide fuel cell (SOFC). Then, the fuel electrode constitutes an anode and the air or oxidant electrode constitutes a cathode of the cell.
- the electrochemical cell may be a solid oxide electrolyser cell (SOEC). Then, the fuel electrode constitutes a cathode and the air or oxidant electrode constitutes an anode of the cell.
- the at least one stainless steel component may be a mechanical support of the electrochemical cell, more preferably a gas permeable carrier, for example, of a solid oxide cell.
- the step of assembling the electrochemical cell may comprise steps of coating the mechanical support having the passivating oxide layer thereon with a fuel electrode layer, an electrolyte layer, and an air or oxidant electrode layer (where the order of the electrode layers may be reversed depending on the type of cell).
- the stainless steel component may be an intrinsically porous metal substrate formed from a powder metal precursor or may be formed from a metal support plate provided with a porous region in the form of through holes or small apertures surrounded by a non-porous (solid) region.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Metallurgy (AREA)
- Mechanical Engineering (AREA)
- Electrochemistry (AREA)
- Sustainable Energy (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Manufacturing & Machinery (AREA)
- Composite Materials (AREA)
- Fuel Cell (AREA)
- Cell Electrode Carriers And Collectors (AREA)
- Primary Cells (AREA)
- Chemical Treatment Of Metals (AREA)
Abstract
L'invention concerne un procédé de création d'une couche d'oxyde de passivation sur un composant en acier inoxydable d'une cellule électrochimique et un procédé de fabrication d'une cellule électrochimique.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/EP2021/087343 WO2023117087A1 (fr) | 2021-12-22 | 2021-12-22 | Procédé de création d'une couche d'oxyde de passivation sur un composant en acier inoxydable d'une cellule électrochimique |
TW111148862A TW202336248A (zh) | 2021-12-22 | 2022-12-20 | 電化電池不鏽鋼組件鈍化氧化物層之製作方法 |
Applications Claiming Priority (1)
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PCT/EP2021/087343 WO2023117087A1 (fr) | 2021-12-22 | 2021-12-22 | Procédé de création d'une couche d'oxyde de passivation sur un composant en acier inoxydable d'une cellule électrochimique |
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WO2023117087A1 true WO2023117087A1 (fr) | 2023-06-29 |
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PCT/EP2021/087343 WO2023117087A1 (fr) | 2021-12-22 | 2021-12-22 | Procédé de création d'une couche d'oxyde de passivation sur un composant en acier inoxydable d'une cellule électrochimique |
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WO (1) | WO2023117087A1 (fr) |
Citations (7)
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GB1156621A (en) * | 1963-12-05 | 1969-07-02 | Wmf Wuerttemberg Metallwaren | Improvements in or relating to Metal Fibres |
US20060234112A1 (en) * | 1999-07-31 | 2006-10-19 | The Regents Of The University Of California | Structures and fabrication techniques for solid state electrochemical devices |
EP1942539B1 (fr) * | 2006-12-07 | 2010-03-17 | Ansaldo Fuel Cells S.p.A. | Brides pour la plaque de séparation de piles à combustible en carbonate fondu |
US20110117384A1 (en) * | 2008-05-16 | 2011-05-19 | Samir Biswas | Aluminide Barrier Layers and Methods of Making and Using Thereof |
US20120126485A1 (en) * | 2008-10-08 | 2012-05-24 | David Fairbourn | Honeycomb Seal And Method To Produce It |
US20150079498A1 (en) * | 2004-11-30 | 2015-03-19 | Sandvik Intellectual Property Ab | Strip Product Forming a Surface Coating of Perovskite or Spinel for Electrical Contacts |
US20210262098A1 (en) * | 2020-02-26 | 2021-08-26 | Treadstone Technologies, Inc. | Component having improved surface contact resistance and reaction activity and methods of making the same |
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2021
- 2021-12-22 WO PCT/EP2021/087343 patent/WO2023117087A1/fr unknown
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2022
- 2022-12-20 TW TW111148862A patent/TW202336248A/zh unknown
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GB1156621A (en) * | 1963-12-05 | 1969-07-02 | Wmf Wuerttemberg Metallwaren | Improvements in or relating to Metal Fibres |
US20060234112A1 (en) * | 1999-07-31 | 2006-10-19 | The Regents Of The University Of California | Structures and fabrication techniques for solid state electrochemical devices |
US20150079498A1 (en) * | 2004-11-30 | 2015-03-19 | Sandvik Intellectual Property Ab | Strip Product Forming a Surface Coating of Perovskite or Spinel for Electrical Contacts |
EP1942539B1 (fr) * | 2006-12-07 | 2010-03-17 | Ansaldo Fuel Cells S.p.A. | Brides pour la plaque de séparation de piles à combustible en carbonate fondu |
US20110117384A1 (en) * | 2008-05-16 | 2011-05-19 | Samir Biswas | Aluminide Barrier Layers and Methods of Making and Using Thereof |
US20120126485A1 (en) * | 2008-10-08 | 2012-05-24 | David Fairbourn | Honeycomb Seal And Method To Produce It |
US20210262098A1 (en) * | 2020-02-26 | 2021-08-26 | Treadstone Technologies, Inc. | Component having improved surface contact resistance and reaction activity and methods of making the same |
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FRUTOS E ET AL: "Development of hard intermetallic coatings on austenitic stainless steel by hot dipping in an Al-Si alloy", SURFACE AND COATINGS TECHNOLOGY, ELSEVIER, NL, vol. 203, no. 19, 25 June 2009 (2009-06-25), pages 2916 - 2920, XP026117544, ISSN: 0257-8972, [retrieved on 20090317], DOI: 10.1016/J.SURFCOAT.2009.03.015 * |
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