EP1328983A2 - Dispositif permettant d'alimenter un ensemble de piles a combustible en gaz de fonctionnement - Google Patents
Dispositif permettant d'alimenter un ensemble de piles a combustible en gaz de fonctionnementInfo
- Publication number
- EP1328983A2 EP1328983A2 EP01987952A EP01987952A EP1328983A2 EP 1328983 A2 EP1328983 A2 EP 1328983A2 EP 01987952 A EP01987952 A EP 01987952A EP 01987952 A EP01987952 A EP 01987952A EP 1328983 A2 EP1328983 A2 EP 1328983A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- fuel cell
- valve
- pressure
- operating gas
- cell arrangement
- 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- Withdrawn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
- 239000000446 fuel Substances 0.000 title claims abstract description 62
- 238000000034 method Methods 0.000 claims description 6
- 239000012528 membrane Substances 0.000 claims description 5
- 230000005611 electricity Effects 0.000 claims description 2
- 230000001105 regulatory effect Effects 0.000 claims description 2
- 230000001276 controlling effect Effects 0.000 claims 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 19
- 239000001257 hydrogen Substances 0.000 description 19
- 229910052739 hydrogen Inorganic materials 0.000 description 19
- 239000007789 gas Substances 0.000 description 15
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 7
- 239000001301 oxygen Substances 0.000 description 7
- 229910052760 oxygen Inorganic materials 0.000 description 7
- 239000007800 oxidant agent Substances 0.000 description 5
- 239000003054 catalyst Substances 0.000 description 4
- 239000003638 chemical reducing agent Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 3
- 239000005518 polymer electrolyte Substances 0.000 description 3
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- 239000003570 air Substances 0.000 description 2
- 230000001419 dependent effect Effects 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 238000003487 electrochemical reaction Methods 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 229910052987 metal hydride Inorganic materials 0.000 description 2
- 150000004681 metal hydrides Chemical class 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000012080 ambient air Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
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
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
-
- 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 present invention relates to a device for feeding
- a fuel cell is an electrochemical device for generating electricity. It has an electrolyte, a cathode and an anode.
- the cathode becomes an oxidizing agent, e.g. B. oxygen
- the anode is a fuel, e.g. B. hydrogen supplied.
- Fuel cells can be manufactured using a polymer electrolyte membrane (PEM). This is catalytically active on both sides Layer and is located between two gas diffusion layers. It is also possible for the two gas diffusion layers to be provided with a catalyst layer instead of the membrane. At the anode, protons form from the hydrogen in the presence of the catalyst, which traverse the electrolyte and coexist in the catalyst layer on the cathode side
- PEM polymer electrolyte membrane
- a fuel gas such as hydrogen
- oxygen as an oxidizing agent for the electrochemical reaction can also come from the ambient air of the fuel cell. This means that there is normal air pressure on the cathode side of the fuel cell.
- a low, well constant hydrogen pressure of about 0.3 to 0.5 bar overpressure must be ensured so as not to destroy the thin polymer electrolyte membrane due to an excessive pressure difference between the anode and cathode gas spaces.
- the oxidizing agent e.g. B. pure oxygen or compressed air, also from a storage device.
- Storage pressure is on the order of 300 bar.
- the pressure is reduced in a first stage when it is fed to the fuel cell by a pressure reducer, which can be integrated in the pressure vessel. It is usually a diaphragm-controlled valve. If you want to integrate this pressure reducer into the pressure vessel, it must be fitted accordingly have small size. The smaller the size of the pressure reducer, the greater the changes in the outlet pressure of the pressure reducer. Depending on the fill level of the pressure vessel, this ranges between 10 and 1 bar. A further pressure regulator is therefore necessary in order to provide the pressure required for the fuel cell. The disadvantages are, especially for mobile applications of the fuel cell system, the weight and the space required for this additional component. If pure oxygen is used as the oxidant of the fuel cell, it is customary to also store it in pressure vessels, which poses the same problems as with hydrogen storage.
- this feed line can also be closed with the aid of a second shut-off valve.
- the object of the invention is to provide gas feeds for fuel cells which, compared to the prior art, have fewer components and thus fewer low volume and weight, while at the same time making it possible to improve the operational safety of the fuel cell.
- a device for supplying an operating gas to a fuel cell in which the shut-off valve
- the fuel cell is designed as a controllable valve which also serves to reduce the non-constant inlet pressure to an operating pressure which is dependent on system parameters of the fuel cell.
- FIG. 1 and 2 each show a schematic representation of a device according to the invention for supplying an operating gas to a fuel cell.
- a fuel cell arrangement 1 has a valve 2, which works in the usual way as a shut-off valve and also as a control valve and one
- Operating gas supply line 3 closes, opens or partially opens.
- This valve 2 is designed so that the mass flow passing through is continuously controllable. This valve 2 can thus reduce a relatively high, fluctuating inlet pressure to an operating pressure suitable for the fuel cell.
- the back pressure of the valve is measured by a pressure sensor 4 in the back pressure chamber 5 and the measurement signal is passed on to an electronic control 6, which controls the opening of the valve and thus enables a mass flow through the valve, in such a way that a specific setpoint for the back pressure of the Valve.
- the valve 2 can be closed completely and thus still take on the function of a shut-off valve, that is to say to prevent the supply of operating gas to the fuel cell.
- a pressure vessel 11 with an integrated first pressure reducing stage 12 is used for hydrogen storage.
- this operating gas storage in pressure vessels 11 it is necessary to use the pressure reducing stage 12 integrated in the vessel because of the high pressure difference between the storage pressure and the operating pressure.
- the function of the fuel cell arrangement 1 is controlled or regulated in the usual way by a microprocessor.
- the regulation of the pressure is implemented in the electronic control 6 either by an electronic analog circuit or preferably digitally by means of a microprocessor. In the latter case, this task is preferably carried out by the microprocessor, which also controls the functions of the fuel cell arrangement.
- microprocessor control for example, a pulsed, electrical signal sent to an electromagnetic valve, the duration of the pulses being variable. This means that a pulse width modulated signal is used.
- the valve is partially or fully opened, which causes the mass flow to be set by the valve.
- the valve 2 can be actuated by means of an electromagnet, piezoelectrically or by other electromechanical actuators. Low mass of the mechanically moving parts is advantageous in order to achieve short reaction times.
- the electronic control 6 of the fuel cell arrangement 1 receives z. B. an electrical signal indicating the electrical current requirement that the fuel cell assembly is to provide.
- z. B. an electrical signal indicating the electrical current requirement that the fuel cell assembly is to provide In the event of a sudden increase in current draw and thus increased hydrogen consumption, by now increasing the setpoint of the input pressure of the fuel cell arrangement 1 by the controller 6 in accordance with the current requirement, it can be ensured that the operating pressure does not decrease significantly.
- the fuel cell arrangements according to FIGS. 1 and 2 each have a flushing valve 18, which serves to briefly release the hydrogen which is under pressure in the fuel cell arrangement 1 in order to flush out liquid water and the inert gases contaminating the hydrogen with it have accumulated in the fuel cell. If the purge valve 18 is now opened, the input pressure of the fuel cell is simultaneously increased briefly, and after the valve 18 is closed, the pressure increases adjusted to normal operating pressure again.
- the hydrogen mass flow through the fuel cell is proportional to the electrical current delivered.
- hydrogen gas escapes from the fuel cell arrangement without being involved in the electrochemical reaction. In this way, a leak in the arrangement is ascertained and the fuel cell arrangement 1 is automatically switched off in order to avoid excessive leakage of hydrogen gas.
- the shutdown takes place by closing the operating gas line 3 with the controllable valve 2.
- a control valve if present, closes the oxygen supply line if oxygen from a storage device is used as the oxidizing agent and a leakage of oxygen is determined.
- the electronic control 6 can also other system parameters of the fuel cell, such as. B. measured temperatures are made available to achieve optimal control behavior. These signals are symbolized by the connection 11.
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 dispositif permettant d'alimenter un pile à combustible (1) en gaz de fonctionnement. Ce dispositif comprend une soupape d'arrêt (2) qui est pourvue dans la conduite d'alimentation en gaz de fonctionnement et est conçue de façon que le flux massique traversant soit commandé de manière continue, ce qui peut également permettre de réduire et de stabiliser une pression d'alimentation non constante. La pression secondaire de la soupape est mesurée par un détecteur de pression (4) et un système électronique de commande (6) règle la soupape de façon à fixer pour la pression de fonctionnement une valeur réelle définie correspondant à une valeur théorique. La valeur théorique de la pression de fonctionnement peut varier en fonction de paramètres de système de la pile à combustible. Par exemple lorsque la demande en flux au niveau de la pile à combustible augmente, la pression de fonctionnement peut connaître une augmentation correspondante. On peut également améliorer la sécurité de fonctionnement de la pile à combustible en déterminant le flux massique qui traverse la soupape de la conduite d'alimentation en combustible, à partir du signal de commande, puis en déconnectant la pile à combustible lorsque la valeur du courant électrique fourni ne correspond pas au courant estimé en fonction du flux massique de combustible mesuré, ce qui indique une fuite.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE10050981 | 2000-10-16 | ||
| DE10050981A DE10050981A1 (de) | 2000-10-16 | 2000-10-16 | Vorrichtung zur Zuführung eines Betriebsgases zu einer Brennstoffzellenanordnung |
| PCT/EP2001/011935 WO2002033763A2 (fr) | 2000-10-16 | 2001-10-16 | Dispositif permettant d'alimenter un ensemble de piles a combustible en gaz de fonctionnement |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| EP1328983A2 true EP1328983A2 (fr) | 2003-07-23 |
Family
ID=7659800
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP01987952A Withdrawn EP1328983A2 (fr) | 2000-10-16 | 2001-10-16 | Dispositif permettant d'alimenter un ensemble de piles a combustible en gaz de fonctionnement |
Country Status (4)
| Country | Link |
|---|---|
| EP (1) | EP1328983A2 (fr) |
| AU (1) | AU2002218240A1 (fr) |
| DE (1) | DE10050981A1 (fr) |
| WO (1) | WO2002033763A2 (fr) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE10200058B4 (de) * | 2002-01-02 | 2019-05-29 | General Motors Llc ( N. D. Ges. D. Staates Delaware ) | Liefersystem zur Lieferung eines gasförmigen Brennstoffs an einen Brennstoffstapel, Brennstoffzellensystem sowie Verfahren zur Lieferung eines gasförmigen Brennstoffs |
| FR2857630B1 (fr) * | 2003-07-18 | 2006-10-27 | Gie Psa Peugeot Citroen | Vehicule automobile muni d'un reservoir de gaz, a securite renforcee |
| JP4788945B2 (ja) | 2005-04-06 | 2011-10-05 | トヨタ自動車株式会社 | 燃料電池システム |
| WO2007022155A2 (fr) * | 2005-08-15 | 2007-02-22 | Parker Hannifin Corporation | Ensemble collecteur d'alimentation en combustible |
| WO2008069007A1 (fr) | 2006-12-07 | 2008-06-12 | Toyota Jidosha Kabushiki Kaisha | Soupape de commande de fluide et système à piles à combustible |
| DE102008010711B4 (de) * | 2008-02-21 | 2018-04-26 | Audi Ag | Verfahren zum Betreiben eines Brennstoffzellensystems sowie Brennstoffzellensystem mit einer Regleranordnung |
| DE102009026590A1 (de) * | 2009-05-29 | 2010-12-02 | Robert Bosch Gmbh | Erkennung des Verlassens eines Betriebsbereiches eines Brennstoffzellensystems und Einleiten der notwendigen Schritte |
| DE102009036435A1 (de) * | 2009-08-06 | 2011-02-10 | Daimler Ag | Versorgungsanordnung für ein Brennstoffzellenpack, Brennstoffzellenmodul sowie Verfahren zum Betreiben des Brennstoffzellenmoduls |
| DE102012023215B3 (de) | 2012-11-28 | 2014-03-13 | Meadwestvaco Calmar Gmbh | Manuell betätigbarer Spender für Medien |
| DE102017213944A1 (de) * | 2017-08-10 | 2019-02-14 | Robert Bosch Gmbh | Verfahren zum Betreiben einer Brennstoffzellenanordnung und Vorrichtung zur Durchführung des Verfahrens |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6472466A (en) * | 1987-09-11 | 1989-03-17 | Toshiba Corp | Combustion air flow controller |
| JPH06203860A (ja) * | 1993-01-11 | 1994-07-22 | Fuji Electric Co Ltd | 積層燃料電池のガス流量制御装置 |
| DE4322765C1 (de) * | 1993-07-08 | 1994-06-16 | Daimler Benz Ag | Verfahren und Vorrichtung zur dynamischen Leistungsregelung für ein Fahrzeug mit Brennstoffzelle |
| US6096449A (en) * | 1997-11-20 | 2000-08-01 | Avista Labs | Fuel cell and method for controlling same |
-
2000
- 2000-10-16 DE DE10050981A patent/DE10050981A1/de not_active Withdrawn
-
2001
- 2001-10-16 AU AU2002218240A patent/AU2002218240A1/en not_active Abandoned
- 2001-10-16 EP EP01987952A patent/EP1328983A2/fr not_active Withdrawn
- 2001-10-16 WO PCT/EP2001/011935 patent/WO2002033763A2/fr not_active Ceased
Non-Patent Citations (1)
| Title |
|---|
| See references of WO0233763A2 * |
Also Published As
| Publication number | Publication date |
|---|---|
| AU2002218240A1 (en) | 2002-04-29 |
| WO2002033763A2 (fr) | 2002-04-25 |
| DE10050981A1 (de) | 2002-04-25 |
| WO2002033763A3 (fr) | 2003-02-27 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
| 17P | Request for examination filed |
Effective date: 20030509 |
|
| AK | Designated contracting states |
Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE TR |
|
| AX | Request for extension of the european patent |
Extension state: AL LT LV MK RO SI |
|
| RBV | Designated contracting states (corrected) |
Designated state(s): AT BE CH DE FR GB LI |
|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN |
|
| 18D | Application deemed to be withdrawn |
Effective date: 20080501 |