DE10017058A1 - Bipolar plate used for a PEM fuel cell stack is made from a first metal with a metallic coating of a second metal - Google Patents
Bipolar plate used for a PEM fuel cell stack is made from a first metal with a metallic coating of a second metalInfo
- Publication number
- DE10017058A1 DE10017058A1 DE10017058A DE10017058A DE10017058A1 DE 10017058 A1 DE10017058 A1 DE 10017058A1 DE 10017058 A DE10017058 A DE 10017058A DE 10017058 A DE10017058 A DE 10017058A DE 10017058 A1 DE10017058 A1 DE 10017058A1
- Authority
- DE
- Germany
- Prior art keywords
- bipolar plate
- metal
- plate according
- metallic coating
- metallic
- 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.)
- Withdrawn
Links
Classifications
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- 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
- H01M8/0208—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
-
- 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
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Composite Materials (AREA)
- Fuel Cell (AREA)
Abstract
Description
Bipolarplatten für PEMFC- oder DMFC-Stacks werden bislang üblicherweise entweder aus Metall, aus Graphit oder aus einer mehr oder weniger homogenen Mischung eines kohlenstoffhaltigen Komposits gefertigt. Wichtige Anforderungen sind gute elektrische Leitfähigkeit, Gasdichtheit, gute mechanische Bearbeitbarkeit (drehen, fräsen) oder alternativ die Möglichkeit, der Bipolarplatte in einer Art Prägung die gewünschte Form geben zu können. In einem Brennstoffzellenstapel sind üblicherweise einige der Bipolarplatten darüberhinaus derart ausgebildet, daß mittels eines Kühlmediums, typischerweise Wasser, die während des Betriebs entstehende Wärme abgeführt bzw. für eine evtl. weitere Nutzung ausgekoppelt werden kann.Bipolar plates for PEMFC or DMFC stacks have so far usually been made of either metal, from graphite or from a more or less homogeneous mixture of a carbon-containing Composites made. Important requirements are good electrical conductivity, gas tightness, good mechanical workability (turning, milling) or alternatively the possibility of inserting the bipolar plate in to be able to give the desired shape to a kind of stamping. Are in a fuel cell stack usually some of the bipolar plates are also designed such that by means of a Cooling medium, typically water, dissipates the heat generated during operation or can be decoupled for any further use.
Zur Erzielung einer guten Performance eines PEM-Brennstoffzellenstacks ist die Gestaltung der Bipolarplatten von großer Bedeutung, insbesondere im Hinblick auf eine möglichst gleichmäßige Versorgung der Reaktionszonen mit den Reaktionsgasen Wasserstoff und Sauerstoff bzw. Luft bei gleichzeitig möglichst guter elektrischer Kontaktierung der angrenzenden Gasdiffusionsschichten.To achieve a good performance of a PEM fuel cell stack, the design of the Bipolar plates of great importance, especially with a view to making them as uniform as possible Supply of the reaction zones with the reaction gases hydrogen and oxygen or air at the same time, the best possible electrical contacting of the adjacent gas diffusion layers.
In der elektrochemischen Literatur existieren mehrere konstruktive Lösungen für diese Aufgabe. In den von verschiedenen Unternehmen bisher gefertigten Prototypen wird im allgemeinen eine auf beiden Seiten der Bipolarplatte durchgängige Fräsung paralleler Kanaäle mit rechteckigem Querschnitt, entweder in gleicher Richtung (Vorder- und Rückseite) oder in rechtem Winkel zueinander, eingesetzt. Die reagierenden Gase strömen dabei im wesentlichen von jeweils einer Kante der Bipolarplatte zur gegenüberliegenden. Eine konstruktive Optimierungsaufgabe besteht darin, die Kanalbreiten bzw. Stegbreiten derart auszulegen, daß einerseits eine gute Gasversorgung, andererseits jedoch auch eine gute elektrische Kontaktierung der anliegenden Gasdiffusionselektrode gewährleistet ist. Durch die in diesem Ansatz notwendigerweise vorhandenen Stege ergibt sich hier insbesondere die Schwierigkeit, diejenigen Bereiche der Gasdiffusionselektrode bzw. der angrenzenden katalytischen Reaktionsschicht mit Gas zu versorgen, die unmittelbar auf den Stegen aufliegen, da die Querdiffusion der Gase innerhalb der Gasdiffusionsschicht erheblich erschwert ist. Eine mögliche Lösung besteht darin, zwischen Bipolarplatte und Gasdiffusionsschicht ein oder mehrere Drahtnetze einzufügen, um den Gaszutritt zu den genannten Bereichen zu erleichtern. Abgesehen von der recht umständlichen Montage einer derartigen Struktur, die im Hinblick auf eine automatisierte Fertigung von Nachteil ist, ergeben sich bei Verwendung von Nichtedelmetallen i. a. weitere Nachteile durch die Möglichkeit der Bildung von Oberflächenoden auf dem Drahtnetz bzw. den Drahtnetzen, die den internen elektrischen Widerstand der Zelle bzw. des Stacks erhöhen und somit zu einer Leistungsminderung führen.There are several constructive solutions to this task in electrochemical literature. In The prototypes previously manufactured by various companies are generally based on one continuous milling of parallel channels with rectangular ones on both sides of the bipolar plate Cross-section, either in the same direction (front and back) or at a right angle to each other, used. The reacting gases essentially flow from one edge each the bipolar plate to the opposite. A constructive optimization task consists in the To design channel widths or web widths in such a way that on the one hand a good gas supply and on the other hand however, good electrical contacting of the adjacent gas diffusion electrode is also ensured is. The webs that are necessarily present in this approach result in particular in the Difficulty identifying those areas of the gas diffusion electrode or the adjacent catalytic To supply the reaction layer with gas, which lie directly on the webs, since the cross diffusion the gases within the gas diffusion layer are considerably more difficult. There is a possible solution in inserting one or more wire meshes between the bipolar plate and the gas diffusion layer in order to facilitate gas access to the areas mentioned. Aside from the rather cumbersome Assembly of such a structure, which is disadvantageous with regard to automated production, arise when using base metals i. a. further disadvantages due to the possibility of Formation of surface electrodes on the wire mesh or the wire meshes that cover the internal increase the electrical resistance of the cell or the stack and thus lead to a reduction in performance to lead.
Zur Lösung der beschriebenen Problematik wird erfindungsgemäß eine Oberflächenstruktur einer Bipolarplatte vorgeschlagen, die sowohl eine gute Gasversorgung der angrenzenden Gasdiffusions struktur (typischerweise ein präpariertes Kohlenstoffvlies) als auch eine gegenüber dem bisherigen Stand der Technik verbesserte elektrische Kontaktierung der Gasdiffusionselektrode bietet. Ein Ausführungsbeispiel ist in Fig. 1 angegeben.To solve the problem described, a surface structure of a bipolar plate is proposed according to the invention, which offers both a good gas supply to the adjacent gas diffusion structure (typically a prepared carbon fleece) and also an improved electrical contacting of the gas diffusion electrode compared to the prior art. An embodiment is shown in Fig. 1.
Die in Fig. 1 gezeigte Bipolarplatte enthält Bohrungen (1) und (1a) zur Versorgung mit Sauerstoff bzw. Luft bzw. Abtransport überschüssiger Luft bzw. O2; ebenso (2) und (2a) zur Versorgung mit Wasserstoff bzw. Ableitung überschüssigen Wasserstoffs, Bohrungen (3) zur Durchführung der (Gewinde-)Stangen oder Schrauben zur Stackmontage, beidseitige gefräste oder geätzte Vertiefungen (4) (ca. 0,5 mm tief gegenüber dem Rand) sowie aus dem Herstellungsprozeß resultierend "stehengebliebene" Inseln (5), die den elektrischen Kontakt zur anliegenden Schicht, i. a. eine Gasdiffusionsschicht, herstellen.The bipolar plate shown in Fig. 1 contains bores ( 1 ) and ( 1 a) for the supply of oxygen or air or removal of excess air or O 2 ; also ( 2 ) and ( 2 a) for the supply of hydrogen or discharge of excess hydrogen, bores ( 3 ) for the passage of the (threaded) rods or screws for stack mounting, milled or etched recesses ( 4 ) on both sides (approx. 0.5 mm deep from the edge), and from the manufacturing process resulting "left standing" islands (5) connecting the electrical contact to the adjacent layer, generally a gas diffusion layer prepared.
Zur Verdeutlichung sind die nach der Fräsung der Kanäle erhaltenen "Inseln" im Querschnitt übertrieben dick eingezeichnet. Die genaue Dicke D des mittleren Bereichs im Verhältnis zur Dicke d der Randzone ergibt sich aus den verwendeten Materialien für das Kohlenstoff-Backing, die Membran sowie das Dichtungsmaterial, welches die MEE (Membran-Elektroden-Einheit) nach außen gasdicht abschließt. Der Quotient d/D ist dabei derart zu optimieren, daß einerseits eine gute elektrische Kontaktierung der Gasdiffusionselektroden erreicht wird, andererseits aber auch die Abdichtung nach außen bzw. zur anderen Seite der Bipolarplatte gewährleistet ist.For clarification, the "islands" obtained after milling the channels are in cross-section drawn in excessively thick. The exact thickness D of the central area in relation to the thickness d the edge zone results from the materials used for the carbon backing, the membrane and the sealing material that makes the MEE (membrane electrode assembly) gas-tight to the outside completes. The quotient d / D is to be optimized such that, on the one hand, a good electrical Contacting of the gas diffusion electrodes is achieved, but also the sealing after outside or to the other side of the bipolar plate is guaranteed.
Claims (8)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10017058A DE10017058A1 (en) | 2000-04-05 | 2000-04-05 | Bipolar plate used for a PEM fuel cell stack is made from a first metal with a metallic coating of a second metal |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10017058A DE10017058A1 (en) | 2000-04-05 | 2000-04-05 | Bipolar plate used for a PEM fuel cell stack is made from a first metal with a metallic coating of a second metal |
Publications (1)
Publication Number | Publication Date |
---|---|
DE10017058A1 true DE10017058A1 (en) | 2001-10-11 |
Family
ID=7637759
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE10017058A Withdrawn DE10017058A1 (en) | 2000-04-05 | 2000-04-05 | Bipolar plate used for a PEM fuel cell stack is made from a first metal with a metallic coating of a second metal |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE10017058A1 (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1148566A2 (en) * | 2000-04-19 | 2001-10-24 | Toyota Jidosha Kabushiki Kaisha | Fuel cell separator, manufacturing method thereof and fuel cell |
WO2003092139A2 (en) * | 2002-04-26 | 2003-11-06 | President And Fellows Of Harvard College | Durable bipolar plates for fuel cells |
AT412879B (en) * | 2003-08-12 | 2005-08-25 | Karl Dipl Ing Gruber | POLYMER ELECTROLYTE ELECTROLYSIS |
AT412931B (en) * | 2003-08-12 | 2005-08-25 | Karl Dipl Ing Gruber | BIPOLAR PLATE FOR PEM FUEL CELL BZW PEM ELECTROLYSIS |
WO2009108102A1 (en) | 2008-02-27 | 2009-09-03 | Impact Coatings Ab | Electrode with a coating, method in production thereof and use of a material |
CN101814615B (en) * | 2009-02-19 | 2012-10-31 | 株式会社神户制钢所 | Separator for fuel cell and method for producing same |
WO2014173750A1 (en) * | 2013-04-26 | 2014-10-30 | Bayerische Motoren Werke Aktiengesellschaft | Process for producing a bipolar plate and also a layer structure, bipolar plate and layer structure having a bipolar plate |
-
2000
- 2000-04-05 DE DE10017058A patent/DE10017058A1/en not_active Withdrawn
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7052794B2 (en) | 2000-04-19 | 2006-05-30 | Toyota Jidosha Kabushiki Kaisha | Fuel cell separator, manufacturing method thereof and fuel cell |
US7422815B2 (en) | 2000-04-19 | 2008-09-09 | Toyota Jidosha Kabushiki Kaisha | Fuel cell separator, manufacturing method thereof and fuel cell |
EP1148566A3 (en) * | 2000-04-19 | 2004-12-15 | Toyota Jidosha Kabushiki Kaisha | Fuel cell separator, manufacturing method thereof and fuel cell |
EP1148566A2 (en) * | 2000-04-19 | 2001-10-24 | Toyota Jidosha Kabushiki Kaisha | Fuel cell separator, manufacturing method thereof and fuel cell |
WO2003092139A3 (en) * | 2002-04-26 | 2005-03-24 | Harvard College | Durable bipolar plates for fuel cells |
WO2003092139A2 (en) * | 2002-04-26 | 2003-11-06 | President And Fellows Of Harvard College | Durable bipolar plates for fuel cells |
AT412931B (en) * | 2003-08-12 | 2005-08-25 | Karl Dipl Ing Gruber | BIPOLAR PLATE FOR PEM FUEL CELL BZW PEM ELECTROLYSIS |
AT412879B (en) * | 2003-08-12 | 2005-08-25 | Karl Dipl Ing Gruber | POLYMER ELECTROLYTE ELECTROLYSIS |
WO2009108102A1 (en) | 2008-02-27 | 2009-09-03 | Impact Coatings Ab | Electrode with a coating, method in production thereof and use of a material |
CN101814615B (en) * | 2009-02-19 | 2012-10-31 | 株式会社神户制钢所 | Separator for fuel cell and method for producing same |
US8367241B2 (en) | 2009-02-19 | 2013-02-05 | Kobe Steel, Ltd. | Separator for fuel cell and manufacturing method therefor |
DE102010007624B4 (en) * | 2009-02-19 | 2017-07-06 | Kabushiki Kaisha Kobe Seiko Sho (Kobe Steel, Ltd.) | Separator for a fuel cell and method for its production |
WO2014173750A1 (en) * | 2013-04-26 | 2014-10-30 | Bayerische Motoren Werke Aktiengesellschaft | Process for producing a bipolar plate and also a layer structure, bipolar plate and layer structure having a bipolar plate |
WO2014173751A1 (en) * | 2013-04-26 | 2014-10-30 | Bayerische Motoren Werke Aktiengesellschaft | Process for producing a bipolar plate and also a layer structure, bipolar plate and layer structure |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
8122 | Nonbinding interest in granting licences declared | ||
8139 | Disposal/non-payment of the annual fee |