CA2925498C - Fuel cell separator and manufacturing method of fuel cell separator - Google Patents
Fuel cell separator and manufacturing method of fuel cell separator Download PDFInfo
- Publication number
- CA2925498C CA2925498C CA2925498A CA2925498A CA2925498C CA 2925498 C CA2925498 C CA 2925498C CA 2925498 A CA2925498 A CA 2925498A CA 2925498 A CA2925498 A CA 2925498A CA 2925498 C CA2925498 C CA 2925498C
- Authority
- CA
- Canada
- Prior art keywords
- layer
- tiox
- carbon film
- fuel cell
- separator
- 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.)
- Active
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/403—Manufacturing processes of separators, membranes or diaphragms
-
- 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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0223—Composites
- H01M8/0228—Composites in the form of layered or coated products
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/431—Inorganic material
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/449—Separators, membranes or diaphragms characterised by the material having a layered structure
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/463—Separators, membranes or diaphragms characterised by their shape
-
- 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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0206—Metals or alloys
-
- 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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0213—Gas-impermeable carbon-containing materials
-
- 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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0215—Glass; Ceramic materials
- H01M8/0217—Complex oxides, optionally doped, of the type AMO3, A being an alkaline earth metal or rare earth metal and M being a metal, e.g. perovskites
-
- 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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0223—Composites
- H01M8/0226—Composites in the form of mixtures
-
- 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
- Y02E60/10—Energy storage using batteries
-
- 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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Manufacturing & Machinery (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Composite Materials (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Fuel Cell (AREA)
- Chemical Vapour Deposition (AREA)
Abstract
Description
SEPARATOR
Background Field of the Invention [0001] The present invention relates to a fuel cell separator and a manufacturing method of a fuel cell separator.
Description of Related Art
structure.
Summary
and this peak corresponds to oxidation of TiC. As can be seen from the above result, a TiC adhesion layer is easily oxidized under a fuel cell environment and its corrosion resistance is poor. A novel method for increasing the adhesion between the titanium base substrate and the carbon film and also improving the corrosion resistance has been demanded.
layer and the carbon film. This binder layer provides adhesion between the TiOx layer and the carbon film. In addition, corrosion resistance is ensured by the presence of the TiOx layer.
thickness of 0.1 nm or more is necessary in order to secure adhesion between the TiOx layer and the carbon film via the binder layer, while a thickness of 5 nm or less is necessary in order to secure the conductivity of the binder layer. The binder layer is gradually oxidized under an oxidative condition, resulting in insulating properties; however, the binder layer, if it is as thin as 5 nm or less, can maintain a certain level of conductivity due to the tunneling effect, etc.
Brief Description of the Drawings
Fig. 2 is an enlarged cross-sectional view of a fuel cell separator according to a first embodiment.
Fig. 3 is a flowchart showing the outline of the steps for manufacturing a separator.
Fig. 4 is a flowchart showing the details of a plasma CVD process.
Fig. 5 is an enlarged cross-sectional view of a fuel cell separator according to a second embodiment.
Fig. 6 is a cross-sectional TEM image of a fuel cell separator of Example 1.
Fig. 7 is a chart showing the result of TEM-EELS analysis of the fuel cell separator of Example 1.
Fig. 8 is an enlarged cross-sectional view of a fuel cell separator of Comparative Example 1.
Fig. 9 is an enlarged cross-sectional view of a fuel cell separator of Comparative Example 2.
Detailed Description of Preferred Embodiments
One electrode 7 of the MEA 3 is in surface-to-surface contact with the top part of the separator 4, while the other electrode 8 of the MEA 3 is in surface-to-surface contact with the top part of the separator 5.
If a gas including nitrogen is used as a bombardment gas or a film-forming gas during the plasma CVD process, N will be incorporated into the carbon film 44.
In addition, if a titanium oxide layer is present on the surface of the titanium base substrate 40, a method which reduces the titanium oxide layer through plasma treatment using a reducing substance, such as hydrogen, may be used.
In general, there are three types of titanium oxide (Ti02) and, of these three types, one of the two major types is in a rutile form (stable; a majority of titanium oxide is in this rutile form) and the other is in an anatase form.
The photocatalytic effect occurs only in the presence of electrons and positive holes generated in an excited state. Since the necessary energy for such excitation is 3.0 eV for the rutile form and 3.2 eV for the anatase form, the rutile form and the anatase form are, in theory, excited by being irradiated with light of 410 nm or less and 390 nm or less, respectively. The TiOx layer is formed by placing TiO2 in the rutile or anatase form in an oxygen-deficient condition, and the necessary energy for excitation of such TiOx layer is assumed to have little difference from that for Ti02. Since the emission peak of nitrogen (N2) plasma is at 410 nm or less, the activation of the TiOx layer 42 can be facilitated through the photocatalytic effect, regardless of whether the TiOx layer 42 corresponds to the rutile form in an oxygen-deficient condition or the anatase form in an oxygen-deficient condition, and the surface free energy on the TiOx layer 42 can be increased.
(step SP4-4). The carbon film 44 is formed by using a hydrocarbon-based gas (e.g. acetylene) as the base of the film-forming gas. In the present embodiment, it is preferable to use a gas including nitrogen as the film-forming gas and, for example, a gas including acetylene and nitrogen is used. Through such use, light arising from a nitrogen plasma (which is light with a wavelength of 390 nm or less) is applied to the surface of the TiOx layer 42 during the formation of the carbon film 44. As a result, for the reason described above, the TiOx layer 42 is further activated by the photocatalytic effect and the surface free energy of the TiOx layer 42 is increased.
contained in the binder layer 43 is derived from the N components contained in the carbon film 44 or derived from nitrogen gas used before or during the film formation by plasma CVD.
When the TiOx layer 42 is exposed to a plasma during the plasma CVD, bonds in the surface layer of the TiOx layer 42 are broken due to radicals generated by the plasma and the TiOx layer 42 therefore has dangling bonds in the surface thereof. Meanwhile, the C included in the film-forming gas also has dangling bonds, since the film-forming gas is a plasma.
Accordingly, in the plasma CVD, not only the C in the film-forming gas but also the surface layer of the TiOx layer 42 are caused to have dangling bonds and, thus, the C is bound with and deposited on the TiOx layer. CVD
processes other than plasma CVD and other methods such as PVD cannot induce dangling bonds on the surface of the TiOx layer 42 and cannot form a binder layer 43 between the TiOx layer 42 and the carbon film 44. Thus, the adhesion strength between the TiOx layer 42 and the carbon film 44 cannot be enhanced.
In the plasma CVD, the titanium base substrate 40 was transferred into a deposition chamber at a temperature of 300 C and a pressure of 10 Pa, and a direct current bias voltage of 2.0 kV was then applied so that a glow discharge plasma was generated between the titanium base substrate 40 and the anode. The anode was placed in a manner such that the anode and the titanium base substrate 40 were arranged parallel and facing each other, and a plasma was caused to be simultaneously generated on the respective surfaces. In addition, for the purpose of increasing the plasma density, a samarium cobalt magnet was placed within the chamber so as to trap electrons generated by the plasma.
Fig. 7 is a chart showing the result of TEM-EELS analysis at points 1 to 5 in the cross-sectional TEM image shown in Fig. 6.
Here, it was confirmed that an amorphous TiO2 layer 41 was formed on the surface of the prepared titanium base substrate 40. Acid pickling means a process of etching a surface typically in nitric hydrofluoric acid after a cold-rolling step. The obtained titanium base substrate 40 was pressed so as to be in the form of a separator, and then cleaned with a hydrocarbon-based cleaning solution and an alkaline cleaning solution (step SP3). After that, using a microwave plasma apparatus, the titanium base substrate 40 was treated in a vacuum for two minutes using H2 gas as a reactant gas and Ar gas as a carrier gas under the conditions of 50 Pa and 1.5 kW (TiOx treatment). As a result, the surface layer of the TiO2 layer 41 was reduced so as to form a TiOx layer 42. After that, a carbon film 44 was formed by plasma CVD in the same manner as in Example 1 (step SP4). In the plasma CVD, the applied voltage was 2.0 kV and glow discharge was caused with a direct current bias. The bombardment gas and the film-forming gas used in the plasma CVD included nitrogen.
layer 45 was formed on a titanium base substrate 40 and a carbon film 44 was formed on such TIC layer 45. The separator of Comparative Example 2 was manufactured in accordance with an ordinary method. Specifically, the separator of Comparative Example 2 was manufactured by forming the carbon film 44 on the bright-annealed titanium base substrate 40.
The details of each evaluation test were as follows.
A: Peeled-area ratio of 1% or less B: Peeled-area ratio of more than 1% but 5% or less
A: 5 macm2 or less B: More than 5 macm2 but 10 macm2 or less
A: No oxidation peak observed B: Oxidation peak observed
Pressure cooker test at Peeled-area ratio:
130 C for one hour Peeled-area ratio: 5% Peeled-area ratio: 1%
Contact resistance B A A
Measured against carbon paper with a load of 1 MPa 10 macm2 5 macm2 5 macm2 Corrosion resistance A B A
Presence/absence of oxidation peak in the No oxidation peak TiC peak observed No oxidation peak range of -0.2 to 0.9 V
HE observed around 0.3 to 0.6 V observed (S
During the test, the potential of the test piece was kept constant by a reference electrode. The period of the test was about 50 hours.
Furthermore, the change of the binding state of the binder layer 43 after the corrosion test was observed through TEM-EELS analysis.
A: Contact resistance of 5 mO.cm2 or less both before and after the corrosion test.
B: Contact resistance of more than 5 macm2 after the corrosion test.
nm 4 macm2 5 macm2 A
nm 4 macm2 46 macm2
Claims (7)
forming a TiOx (1<x<2) layer on a titanium base substrate; and forming a carbon film on the TiOx layer by plasma CVD, so that a binder layer including Ti, O and C is formed between the TiOx layer and the carbon film.
a titanium base substrate;
a TiOx (1<x<2) layer formed on the titanium base substrate;
a carbon film formed on the TiOx layer; and a binder layer including Ti, O and C formed between the TiOx layer and the carbon film.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2015-081646 | 2015-04-13 | ||
| JP2015081646A JP6160877B2 (en) | 2015-04-13 | 2015-04-13 | Manufacturing method of fuel cell separator and fuel cell separator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2925498A1 CA2925498A1 (en) | 2016-10-13 |
| CA2925498C true CA2925498C (en) | 2018-10-02 |
Family
ID=56986226
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA2925498A Active CA2925498C (en) | 2015-04-13 | 2016-03-31 | Fuel cell separator and manufacturing method of fuel cell separator |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US10199661B2 (en) |
| JP (1) | JP6160877B2 (en) |
| KR (1) | KR101908180B1 (en) |
| CN (1) | CN106058280B (en) |
| CA (1) | CA2925498C (en) |
| DE (1) | DE102016105963B4 (en) |
Families Citing this family (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6160584B2 (en) * | 2014-09-19 | 2017-07-12 | トヨタ自動車株式会社 | Manufacturing method of fuel cell separator |
| JP2018104808A (en) * | 2016-12-28 | 2018-07-05 | 新日鐵住金株式会社 | Titanium material, separator, cell, and polymer electrolyte fuel cell |
| KR102291510B1 (en) * | 2016-12-28 | 2021-08-19 | 닛폰세이테츠 가부시키가이샤 | Titanium Material, Separator, Cell, and Polymer Fuel Cell |
| ES2926173T3 (en) | 2017-07-21 | 2022-10-24 | Imerys Graphite & Carbon Switzerland Ltd | Carbon-coated silicon oxide/graphite composite particles, as well as preparation methods and applications thereof |
| JP6878239B2 (en) * | 2017-10-06 | 2021-05-26 | トヨタ自動車株式会社 | Manufacturing method of separator for fuel cell |
| JP6856012B2 (en) * | 2017-12-14 | 2021-04-07 | トヨタ自動車株式会社 | Separator for fuel cells |
| JP7092076B2 (en) * | 2018-03-12 | 2022-06-28 | 三菱マテリアル株式会社 | Titanium base material, manufacturing method of titanium base material, electrode for water electrolysis, water electrolysis device |
| WO2019176956A1 (en) * | 2018-03-12 | 2019-09-19 | 三菱マテリアル株式会社 | Titanium base material, method for producing titanium base material, electrode for water electrolysis, and water electrolysis device |
| EP3806215A4 (en) | 2018-06-07 | 2022-03-16 | Sunland (Shanghai) Investment Co. Ltd | SILICON POLE PLATE AND METHOD OF PRODUCTION THEREOF, USE OF SILICON IN A FUEL CELL, FUEL CELL STACK STRUCTURE, FUEL CELL AND USE THEREOF |
| JP7167694B2 (en) | 2018-12-20 | 2022-11-09 | 富士通株式会社 | Manufacturing method of compound semiconductor device |
| JP7151471B2 (en) * | 2018-12-26 | 2022-10-12 | 日本製鉄株式会社 | Metal materials, separators, fuel cells, and fuel cell stacks |
| KR102464570B1 (en) * | 2020-11-26 | 2022-11-07 | 충남대학교산학협력단 | FETStretchable mulity-layer graphene device, method for preparing the same, and Stretchable graphene Field-Effect-Transistor using thereof |
| KR102618939B1 (en) * | 2021-10-28 | 2023-12-27 | 충남대학교산학협력단 | Flexible graphene layer, method for preparing the same, and electronic device using thereof |
| KR20250070644A (en) | 2023-11-13 | 2025-05-21 | 현대자동차주식회사 | Ti MATERIAL FOR FUEL CELL SEPARATOR PLATE AND MANUFACTURING METHOD THEREOF |
Family Cites Families (38)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4525381A (en) | 1983-02-09 | 1985-06-25 | Ushio Denki Kabushiki Kaisha | Photochemical vapor deposition apparatus |
| EP0459425A1 (en) | 1990-05-30 | 1991-12-04 | Idemitsu Petrochemical Company Limited | Process for the preparation of diamond |
| JP3347287B2 (en) * | 1997-05-28 | 2002-11-20 | 株式会社田中 | Method for coating glassy carbon on titanium metal |
| JP4689809B2 (en) | 1999-10-21 | 2011-05-25 | 株式会社神戸製鋼所 | Photocatalyst coating material, method for producing the same, pollutant-containing material purification method and contaminant-containing material purification device using the photocatalyst coating material |
| JP2002088465A (en) | 2000-09-11 | 2002-03-27 | Matsushita Electric Ind Co Ltd | Method of forming hard carbon film on metal substrate |
| JP2002285340A (en) | 2001-03-27 | 2002-10-03 | Citizen Watch Co Ltd | Titanium material |
| JP4147925B2 (en) * | 2002-12-04 | 2008-09-10 | トヨタ自動車株式会社 | Fuel cell separator |
| US7150918B2 (en) | 2004-02-27 | 2006-12-19 | General Motors Corporation | Bilayer coating system for an electrically conductive element in a fuel cell |
| US20070003813A1 (en) * | 2005-06-30 | 2007-01-04 | General Motors Corporation | Stable conductive and hydrophilic fuel cell contact element |
| CN101375442B (en) * | 2005-08-12 | 2011-11-16 | 通用汽车环球科技运作公司 | Fuel cell component with coating comprising nanoparticles |
| JP4848546B2 (en) | 2005-09-30 | 2011-12-28 | Dowaサーモテック株式会社 | Hard coating member and method for producing the same |
| US8389174B2 (en) * | 2006-01-27 | 2013-03-05 | GM Global Technology Operations LLC | Super-hydrophilic nanoporous electrically conductive coatings for PEM fuel cells |
| JP4551429B2 (en) | 2006-09-29 | 2010-09-29 | 株式会社神戸製鋼所 | Method for manufacturing fuel cell separator, fuel cell separator and fuel cell |
| JP5180485B2 (en) | 2006-09-29 | 2013-04-10 | 株式会社神戸製鋼所 | Method for manufacturing fuel cell separator, fuel cell separator and fuel cell |
| JP2009127059A (en) | 2007-11-20 | 2009-06-11 | Tokyo Denki Univ | Method for forming diamond-like carbon film |
| JP5185720B2 (en) | 2008-02-27 | 2013-04-17 | 株式会社神戸製鋼所 | Surface treatment method of titanium material for electrodes |
| US9136545B2 (en) * | 2008-02-27 | 2015-09-15 | GM Global Technology Operations LLC | Low cost fuel cell bipolar plate and process of making the same |
| JP5175590B2 (en) | 2008-03-26 | 2013-04-03 | 株式会社神戸製鋼所 | Fuel cell separator and method for producing the same |
| EP2337135B1 (en) * | 2008-09-30 | 2015-07-29 | Nippon Steel & Sumitomo Metal Corporation | Titanium material having low contact resistance for use in separator for solid polymer-type fuel cell and process for producing the titanium material |
| JP2010135232A (en) | 2008-12-05 | 2010-06-17 | Kobe Steel Ltd | Titanium substrate for fuel cell separator, and fuel cell separator |
| JP2010218899A (en) | 2009-03-17 | 2010-09-30 | Toyota Motor Corp | Manufacturing method of fuel cell separator and fuel cell separator |
| JP2010248572A (en) | 2009-04-15 | 2010-11-04 | Toyota Motor Corp | Titanium-based material, method for producing the same, and fuel cell separator |
| JP4825894B2 (en) | 2009-04-15 | 2011-11-30 | トヨタ自動車株式会社 | Fuel cell separator and method for producing the same |
| WO2011016465A1 (en) * | 2009-08-03 | 2011-02-10 | 新日本製鐵株式会社 | Titanium material for solid polymer fuel cell separator, and process for production thereof |
| CN102054993A (en) | 2009-11-04 | 2011-05-11 | 逢甲大学 | Metal material covered with carbon film |
| WO2011077755A1 (en) * | 2009-12-25 | 2011-06-30 | トヨタ自動車株式会社 | Separator for fuel cell and method for producing same |
| JP5370188B2 (en) | 2010-02-04 | 2013-12-18 | 株式会社村田製作所 | Method for producing anodized film |
| JP5816891B2 (en) | 2010-07-23 | 2015-11-18 | 株式会社ユーテック | Method for depositing thin film on substrate for deposition and sputtering apparatus |
| CN101972650A (en) * | 2010-10-22 | 2011-02-16 | 烟台大学 | Nanometer noble metal catalyst with high reaction stability and preparation method thereof |
| JP5573610B2 (en) | 2010-11-05 | 2014-08-20 | 日本軽金属株式会社 | Fuel cell separator and method for producing the same |
| JP5108976B2 (en) * | 2011-02-14 | 2012-12-26 | 株式会社神戸製鋼所 | Fuel cell separator |
| JP5378552B2 (en) | 2012-01-30 | 2013-12-25 | 株式会社豊田中央研究所 | Amorphous carbon film, method for forming amorphous carbon film, conductive member provided with amorphous carbon film, and separator for fuel cell |
| JP6122589B2 (en) | 2012-07-20 | 2017-04-26 | 株式会社神戸製鋼所 | Fuel cell separator |
| US10074857B2 (en) | 2012-07-31 | 2018-09-11 | Nippon Steel & Sumitomo Metal Corporation | Titanium or titanium alloy material for fuel cell separator having high contact conductivity with carbon and high durability, fuel cell separator including the same, and manufacturing method therefor |
| JP5753830B2 (en) * | 2012-10-04 | 2015-07-22 | 株式会社神戸製鋼所 | Fuel cell separator and manufacturing method thereof |
| US20160281216A1 (en) | 2013-03-19 | 2016-09-29 | Taiyo Yuden Chemical Technology Co., Ltd. | Structure having stain-proofing amorphous carbon film and method of forming stain-proofing amorphous carbon film |
| JP6349985B2 (en) | 2014-06-09 | 2018-07-04 | トヨタ自動車株式会社 | Separator for fuel cell and fuel cell |
| JP6160584B2 (en) | 2014-09-19 | 2017-07-12 | トヨタ自動車株式会社 | Manufacturing method of fuel cell separator |
-
2015
- 2015-04-13 JP JP2015081646A patent/JP6160877B2/en active Active
-
2016
- 2016-03-31 CA CA2925498A patent/CA2925498C/en active Active
- 2016-04-01 DE DE102016105963.3A patent/DE102016105963B4/en active Active
- 2016-04-07 US US15/092,920 patent/US10199661B2/en active Active
- 2016-04-08 KR KR1020160043161A patent/KR101908180B1/en active Active
- 2016-04-12 CN CN201610224747.4A patent/CN106058280B/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| CN106058280B (en) | 2018-10-09 |
| JP2016201300A (en) | 2016-12-01 |
| KR101908180B1 (en) | 2018-10-15 |
| CN106058280A (en) | 2016-10-26 |
| US20160301087A1 (en) | 2016-10-13 |
| DE102016105963A1 (en) | 2016-10-13 |
| US10199661B2 (en) | 2019-02-05 |
| CA2925498A1 (en) | 2016-10-13 |
| JP6160877B2 (en) | 2017-07-12 |
| DE102016105963B4 (en) | 2020-10-01 |
| KR20160122071A (en) | 2016-10-21 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CA2925498C (en) | Fuel cell separator and manufacturing method of fuel cell separator | |
| US11588168B2 (en) | Separator for fuel cell or current collecting member for fuel cell, and solid polymer electrolyte fuel cell | |
| Yi et al. | Microstructure and properties of aC films deposited under different argon flow rate on stainless steel bipolar plates for proton exchange membrane fuel cells | |
| CN102171874B (en) | Titanium material having low contact resistance for use in separator for solid polymer-type fuel cell and process for producing titanium material | |
| Ji et al. | Application of dense nano-thin platinum films for low-temperature solid oxide fuel cells by atomic layer deposition | |
| US10181603B2 (en) | Manufacturing method of separator for fuel cell | |
| JP2010248572A (en) | Titanium-based material, method for producing the same, and fuel cell separator | |
| JP5192908B2 (en) | Titanium substrate for fuel cell separator, fuel cell separator, and fuel cell separator manufacturing method | |
| WO2024169350A1 (en) | Coating and preparation method therefor, bipolar plate, and fuel cell | |
| CN115133059B (en) | Surface coating of a fuel cell metal flow field plate and preparation method thereof | |
| CN116960381A (en) | A fuel cell metal bipolar plate protective coating and its preparation method and application | |
| CN108531856A (en) | A kind of preparation method of electrode coating | |
| US11189845B2 (en) | Method and device for producing fuel cell separator | |
| JP7726120B2 (en) | Manufacturing method of fuel cell separator | |
| KR20250069250A (en) | Method for manufacturing metal separator and metal separator manufactured therefrom | |
| KR20250104747A (en) | Metal separator and method for manufacturing the same | |
| JP6229771B2 (en) | Fuel cell separator or fuel cell current collector | |
| KR20250118888A (en) | Method for manufacturing metal separator and metal separator manufacutred therefrom | |
| CN118176317A (en) | Parts coated with a carbon base layer | |
| CN110661012A (en) | Separator for fuel cell and fuel cell | |
| JP2017016929A (en) | Titanium material for separator of polymer electrolyte fuel cell | |
| KR20100122361A (en) | Bipolar plate for polymer electrolyte membrane fuel cell and the methods for fabricating the same | |
| JP2018109203A (en) | Formation method of conductive carbon film, production method of conductive carbon film-coated member, and production method of separator for fuel cell |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| MPN | Maintenance fee for patent paid |
Free format text: FEE DESCRIPTION TEXT: MF (PATENT, 9TH ANNIV.) - STANDARD Year of fee payment: 9 |
|
| U00 | Fee paid |
Free format text: ST27 STATUS EVENT CODE: A-4-4-U10-U00-U101 (AS PROVIDED BY THE NATIONAL OFFICE); EVENT TEXT: MAINTENANCE REQUEST RECEIVED Effective date: 20241224 |
|
| U11 | Full renewal or maintenance fee paid |
Free format text: ST27 STATUS EVENT CODE: A-4-4-U10-U11-U102 (AS PROVIDED BY THE NATIONAL OFFICE); EVENT TEXT: MAINTENANCE FEE PAYMENT DETERMINED COMPLIANT Effective date: 20241224 Free format text: ST27 STATUS EVENT CODE: A-4-4-U10-U11-U102 (AS PROVIDED BY THE NATIONAL OFFICE); EVENT TEXT: MAINTENANCE FEE PAYMENT PAID IN FULL Effective date: 20241224 |
|
| MPN | Maintenance fee for patent paid |
Free format text: FEE DESCRIPTION TEXT: MF (PATENT, 10TH ANNIV.) - STANDARD Year of fee payment: 10 |
|
| U00 | Fee paid |
Free format text: ST27 STATUS EVENT CODE: A-4-4-U10-U00-U101 (AS PROVIDED BY THE NATIONAL OFFICE); EVENT TEXT: MAINTENANCE REQUEST RECEIVED Effective date: 20260203 |
|
| U11 | Full renewal or maintenance fee paid |
Free format text: ST27 STATUS EVENT CODE: A-4-4-U10-U11-U102 (AS PROVIDED BY THE NATIONAL OFFICE); EVENT TEXT: MAINTENANCE FEE PAYMENT PAID IN FULL Effective date: 20260203 |