WO2002097908A2 - Interconnecteur pour pile a combustible - Google Patents
Interconnecteur pour pile a combustible Download PDFInfo
- Publication number
- WO2002097908A2 WO2002097908A2 PCT/DE2002/001686 DE0201686W WO02097908A2 WO 2002097908 A2 WO2002097908 A2 WO 2002097908A2 DE 0201686 W DE0201686 W DE 0201686W WO 02097908 A2 WO02097908 A2 WO 02097908A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- fuel cell
- gas
- interconnector
- bores
- cell stack
- Prior art date
Links
Classifications
-
- 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
-
- 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 an interconnector for a fuel cell, in particular for a high-temperature fuel cell.
- High-temperature fuel cells typically work with hydrogen as fuel and air as oxidant, with the hydrogen being reformed externally or internally from methane.
- Air and fuel gas are electrochemically burned in a fuel cell to generate electrical energy. In a high-temperature fuel cell, this combustion takes place in the range between 700 and 1000 ° C. It is particularly important that the fuel cell is well defined and evenly supplied with air or fuel gas, so that despite the exothermic and, when using CH 4 , endothermic processes that take place at the Run off fuel cell, a temperature distribution as uniform as possible is given over the entire fuel cell. As a result, a maximum electrical power is delivered for a specific desired operating temperature and the material stress on the stacked materials is minimized.
- the fuel cells are first integrated and sealed in a frame-like interconnector.
- This represents the basic element for the SOFC stack.
- the overall stack is created by stacking the basic elements. With this stacking, the gas supply and disposal rooms are formed by corresponding cutouts in the fuel cell frame.
- the electrical potential is present at the interconnectors, which in turn must be electrically isolated from one another. In this construction, leaks are regularly reduced, since flat seals of the same type can advantageously be used.
- a high-temperature fuel cell is operated in the so-called cross-flow of air and fuel gas.
- the air or the fuel gas enters a distribution space on one side of the cell, flows through the cathode or anode space of the cell and is collected and discharged again in a gas collection space on the other side of the cell. This is sufficient for small cells
- the object of the invention is to provide an interconnector for a fuel cell with which an improved uniform parallel flow distribution of the individual gases can be generated and which at the same time enables a very compact structure of the fuel cell. Furthermore, it is an object of the invention to provide an effective fuel cell stack which enables a compact structure. Another object of the invention is to provide a method for operating such a fuel cell stack. The object is achieved by an interconnector for a fuel cell with the entirety of the features according to main claim, a fuel cell stack according to secondary claim 5, and by a method according to secondary claim 10. Advantageous configurations result from the claims which refer back to them.
- the interconnector according to the invention for a high-temperature fuel cell has two cutouts on the top and two cutouts on the bottom. These recesses result in closed rooms when covering, for example with a metal sheet. When used in a fuel cell, they then form gas distribution rooms or gas collection rooms.
- parallel channels are arranged on the top and bottom sides, which connect the cutouts on one side of the interconnector.
- the interconnector has bores that run almost vertically from the top of the interconnector to the bottom. Each of these holes ends in a recess. According to the invention, two bores open into at least one recess.
- Bores in the sense of the invention are only to be understood as bores that are provided for the gas feedthrough. This should not be understood to mean openings that are only required for the assembly of a fuel cell stack.
- interconnectors For the operation of a fuel cell, several interconnectors are stacked one above the other, which are separated by thin sheets and electrode-electrolyte units.
- the bores are arranged in such a way that when the interconnectors are stacked on top of one another, they find a correspondence in an interconnector arranged above or below.
- the cutouts are advantageously arranged such that a cutout to form a gas distribution space on one side of the interconnector corresponds to a cutout to form a gas collection space on the other side. In this way, identical interconnectors can advantageously be used to construct a fuel cell stack.
- the aim of the arrangement of bores within the interconnector is to provide a fuel cell by stacking several interconnectors and membrane electrode units on top of one another, in which an improved flow of the gases used is achieved. Since the flow is preferably to be carried out in parallel, that is to say in countercurrent, only two sides of the fuel cell stack remain for the supply and discharge of the fuel gas and the supply and discharge of the oxidizing agent.
- the interconnector according to the invention provides at least two bores for a gas distribution space. These are advantageously arranged in the flow direction of the gas on the right and left in the gas distribution space. This arrangement has the effect that the gas in the gas distribution space is advantageously distributed, and so similar conditions at the beginning of each parallel
- the bores of the interconnectors are sensibly arranged in such a way that the gas supply of both gases, both the fuel gas and the oxidizing gas, is ensured when the interconnectors are assembled (stacked one on top of the other).
- Mirror-image arrangements for the structures on the top and bottom of an interconnector are therefore particularly advantageous.
- the oxidizing gas has a much larger volume flow than the fuel gas, the corresponding diameter of the holes for the individual types of gas can be adapted to it.
- FIG. 1 shows an interconnector 1 of a fuel cell stack for countercurrent guidance, as is known from the Japanese company Tokio-Gas.
- Air collection space 3 0 collected again and discharged via an air discharge opening 5. It is thereby achieved that the flow lines in the entire flow space are approximately of the same length and thus a uniform flow distribution is to be established. However, since the inflow or outflow from the cathode compartment of the cell are essentially different flow processes (diffusion, nozzle) there are significant flow differences in the individual air channels in the cathode compartment. The same applies to the anode side.
- FIG. 2 shows the problem solution according to the invention for an interconnector of a fuel cell with a parallel flow of air and fuel gas.
- a uniform flow in the individual air channels (or fuel gas channels) 8 0 , 8 U is achieved in that the air is introduced into a gas distribution space 2 0 , 2 U through two bores 4, 4a, 6, 6a and in the gas collection space 3 opposite 0 , 3 U is discharged again through a central bore 5, 7.
- the two inlet openings 4, 4a and 6, 6a are arranged on the right and left, as seen in the direction of flow, of the inlet space 2 a , 2 U , whereas the outlet opening 5, 7 in the gas collection space 3 0 , 3 U is arranged in the center.
- a symmetrical flow formation is given. This is a particular problem when designing the internal gas supply and disposal for countercurrent air and fuel gas at the cells. With the positioning of the inlet and outlet openings (bores), the air can be distributed as evenly as possible over the individual air ducts. A similar but opposite flow guidance is provided for the fuel gas. On the other side of the interconnector, a recess for a gas collection space is opposite a recess for a gas distribution space, as indicated by the dashed lines.
- the distributor lines for the supply and discharge of the fuel and the oxidation gas can thus advantageously be arranged in a simple manner on two sides of the fuel cell stack.
- a corresponding version is also appropriate for cross-current flow when using large cells.
- the air volume is usually flow is a multiple of the fuel gas volume flow. This fact can be taken into account by appropriately designing the distribution and collection spaces for the air or the fuel gas and by the size of the respective inlet and outlet openings.
- FIG. 3 shows a two-line fuel cell stack for a parallel flow, which is constructed from bottom to top as follows. On a lower end plate, a frame-shaped sheet is arranged, in which an electrode-electrolyte unit is located.
- the interconnector according to the invention is arranged above this.
- the conclusion is again a frame-shaped sheet with another electrode-electrolyte unit and an upper end plate.
- the end plates are constructed similarly to the interconnector according to the invention, but have the cutouts and channels only on the side facing the stack. This arrangement results in a two-line fuel cell stack.
- the arrows mark the different paths of the fuel and the oxidizing gas through this fuel cell stack.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Fuel Cell (AREA)
Abstract
La présente invention concerne un interconnecteur pour un empilement de piles à combustible haute température. Il est avantageux que cet interconnecteur comprenne au moins deux orifices d'entrée de gaz (4, 4a), dans un espace de distribution de gaz (2o), et un orifice de sortie de gaz (5), dans un espace de collecte de gaz (3o). Des canaux parallèles (8o) sont montés entre ces deux orifices. Un tel guidage de l'écoulement du gaz lors de son entrée ou de sa sortie permet d'obtenir un écoulement particulièrement homogène dans chaque canal parallèle, puisqu'il n'y a aucune turbulence, ni aucune influence des tuyères aussi bien dans l'espace de distribution de gaz que dans l'espace de collecte de gaz. L'empilement de plusieurs interconnecteurs permet d'obtenir une pile à combustible de construction compacte, conçue pour un écoulement en parallèle, qui présente un meilleur guidage de l'écoulement du gaz, par rapport à la technique antérieure, ce qui permet d'obtenir un rendement plus élevé.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10126723A DE10126723A1 (de) | 2001-05-31 | 2001-05-31 | Interkonnektor für eine Brennstoffzelle |
DE10126723.1 | 2001-05-31 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2002097908A2 true WO2002097908A2 (fr) | 2002-12-05 |
WO2002097908A3 WO2002097908A3 (fr) | 2003-10-16 |
Family
ID=7686894
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/DE2002/001686 WO2002097908A2 (fr) | 2001-05-31 | 2002-05-10 | Interconnecteur pour pile a combustible |
Country Status (2)
Country | Link |
---|---|
DE (1) | DE10126723A1 (fr) |
WO (1) | WO2002097908A2 (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7816050B2 (en) | 2007-02-16 | 2010-10-19 | Daimler Ag | Unit cell header flow enhancement |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6878477B2 (en) * | 2001-05-15 | 2005-04-12 | Hydrogenics Corporation | Fuel cell flow field plate |
US20050186458A1 (en) | 2003-09-22 | 2005-08-25 | Ali Rusta-Sallehy | Electrolyzer cell stack system |
US20050183948A1 (en) | 2003-09-22 | 2005-08-25 | Ali Rusta-Sallehy | Apparatus and method for reducing instances of pump de-priming |
FR2874129A1 (fr) * | 2004-08-04 | 2006-02-10 | Helion Sa | Systeme de distribution des fluides dans une pile a combustible |
DE102010020178A1 (de) | 2010-05-11 | 2011-11-17 | Schaeffler Technologies Gmbh & Co. Kg | Verfahren zur Herstellung einer metallischen Biopolarplatte, Bipolarplatte sowie Brennstoffzellenstapel und Verfahren zu dessen Herstellung |
EP3376575B1 (fr) | 2017-03-16 | 2020-04-29 | Hexis AG | Procédé de fabrication d'un interconnecteur métallique pour un empilement de piles à combustible, interconnecteur métallique fabriqué selon le procédé |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0668622A1 (fr) * | 1994-02-19 | 1995-08-23 | ROLLS-ROYCE plc | Une batterie de pile à combustible à base d'oxydes solides |
DE19607947C1 (de) * | 1995-11-09 | 1997-06-19 | Mtu Friedrichshafen Gmbh | Schmelzkarbonat-Brennstoffzelle |
EP1020942A1 (fr) * | 1997-05-14 | 2000-07-19 | SANYO ELECTRIC Co., Ltd. | Cellule electrochimique a polymere solide permettant de fournir de maniere constante d'excellentes caracteristiques de production d'energie |
WO2002023645A2 (fr) * | 2000-09-14 | 2002-03-21 | H Power Enterprises Of Canada Inc. | Ensemble plaque bipolaire de separation pour piles a combustible |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6210867A (ja) * | 1985-07-05 | 1987-01-19 | Ishikawajima Harima Heavy Ind Co Ltd | 燃料電池用セパレ−タ |
JPS6276260A (ja) * | 1985-09-30 | 1987-04-08 | Ishikawajima Harima Heavy Ind Co Ltd | 燃料電池用セパレ−タ |
-
2001
- 2001-05-31 DE DE10126723A patent/DE10126723A1/de not_active Withdrawn
-
2002
- 2002-05-10 WO PCT/DE2002/001686 patent/WO2002097908A2/fr active Application Filing
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0668622A1 (fr) * | 1994-02-19 | 1995-08-23 | ROLLS-ROYCE plc | Une batterie de pile à combustible à base d'oxydes solides |
DE19607947C1 (de) * | 1995-11-09 | 1997-06-19 | Mtu Friedrichshafen Gmbh | Schmelzkarbonat-Brennstoffzelle |
EP1020942A1 (fr) * | 1997-05-14 | 2000-07-19 | SANYO ELECTRIC Co., Ltd. | Cellule electrochimique a polymere solide permettant de fournir de maniere constante d'excellentes caracteristiques de production d'energie |
WO2002023645A2 (fr) * | 2000-09-14 | 2002-03-21 | H Power Enterprises Of Canada Inc. | Ensemble plaque bipolaire de separation pour piles a combustible |
Non-Patent Citations (2)
Title |
---|
PATENT ABSTRACTS OF JAPAN vol. 011, no. 174 (E-513), 4. Juni 1987 (1987-06-04) -& JP 62 010867 A (ISHIKAWAJIMA HARIMA HEAVY IND CO LTD), 19. Januar 1987 (1987-01-19) * |
PATENT ABSTRACTS OF JAPAN vol. 011, no. 275 (E-537), 5. September 1987 (1987-09-05) -& JP 62 076260 A (ISHIKAWAJIMA HARIMA HEAVY IND CO LTD), 8. April 1987 (1987-04-08) * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7816050B2 (en) | 2007-02-16 | 2010-10-19 | Daimler Ag | Unit cell header flow enhancement |
Also Published As
Publication number | Publication date |
---|---|
WO2002097908A3 (fr) | 2003-10-16 |
DE10126723A1 (de) | 2002-12-12 |
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