EP1866991A1 - Device and method for heating a fuel cell stack by alternating current supply - Google Patents
Device and method for heating a fuel cell stack by alternating current supplyInfo
- Publication number
- EP1866991A1 EP1866991A1 EP06707503A EP06707503A EP1866991A1 EP 1866991 A1 EP1866991 A1 EP 1866991A1 EP 06707503 A EP06707503 A EP 06707503A EP 06707503 A EP06707503 A EP 06707503A EP 1866991 A1 EP1866991 A1 EP 1866991A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- fuel cell
- voltage
- cell stack
- cell system
- alternating
- 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- Withdrawn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
-
- 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
- H01M8/04223—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells
- H01M8/04268—Heating of fuel cells during the start-up of the fuel cells
-
- 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
- H01M8/04007—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
-
- 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
- H01M8/04007—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
- H01M8/04037—Electrical heating
-
- 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 in the field of fuel cell technology to an apparatus and a method for heating a fuel cell or a fuel cell stack.
- fuel cell stack (or fuel cell stack) will be understood below to mean an arrangement of at least one fuel cell, i. Single cell, but usually several fuel cells, understood. If the fuel cell stack has more than one fuel cell, then the individual fuel cells of the fuel cell stack can be electrically connected in parallel and / or in series.
- Fuel cell stacks or the individual fuel cells are devices in which an electric chemical reaction is used to recover electrical energy.
- Such fuel cell systems have a potentially high energy density and are characterized by the fact that overall the exhaust gases or waste products in energy production compared to other current power generation systems are significantly reduced.
- Fuel cell systems or the individual fuel cells convert chemical energy into electrical energy by means of electrochemical reactions.
- the reactions take place separately from each other in separated by an electrolytic ion conductor reaction spaces.
- PEMFC polymer electrolyte membrane fuel cell
- hydrogen at the anode is oxidized to protons.
- the protons move through the electrolytic membrane to the cathode, while the electrons remain due to the electrical insulation properties of the membrane or forced into an external electrical circuit.
- oxygen is reduced to water with the help of electrons and protons, which is the only emission product of the hydrogen-powered PEMFC.
- the electrochemical reaction at the anode is the conversion of methanol and water to carbon dioxide, hydrogen ions and electrons.
- the hydrogen ions flow e.g. by a polymer or Kunststoffmemb- ran as electrolyte to the cathode, while the free
- Prior art methods for such heating include heating by means of heating foils or heating by means of a heating circuit using water as the heat carrier.
- Another disadvantage relates to the fact that only indirect heating is possible because the heat is not generated in the fuel cell, but is supplied from the outside.
- the object of the present invention is to provide, starting from the prior art, a fuel cell system whose fuel cell stack or its fuel cells are heated simply and reliably and at sufficient speed. you can. It is also an object of the present invention to provide a corresponding heating method for a fuel cell stack or for fuel cells.
- a fuel cell system according to the invention has a fuel cell stack having at least one fuel cell, which is provided with at least one electrical connection per pole, i. positive and negative pole, which can serve in particular for connection of an external electrical load, equipped and is inventively characterized in that the fuel cell stack on the
- the AC voltage generating device here advantageously has an AC voltage source connected in series and a DC voltage source or, connected in series, an AC voltage source and a capacitor.
- the alternating current may in this case be e.g. via terminals in the fuel cell stack or the fuel cells are fed.
- the one used to feed the alternating current by the AC voltage generating device to the fuel cell stack or the fuel cell applied AC voltage can have any curved or rectangular shape.
- These include, for example, a pure sinusoidal AC voltage or a pure rectangular AC voltage.
- an intermediate form between the two extremes of the pure rectangular shape and the pure sinusoidal shape can be used.
- the pure rectangular shape is associated with the advantage that the fuel cell can be brought to the fastest operating or switch-on.
- the disadvantage of the pure rectangular shape is that very high currents flow at the edges of the square-wave voltage. It is therefore preferable to select a waveform having a shape approximated to the rectangular shape, but which is brushed at the edges.
- this preferred shape is assigned to the rectangular shape.
- a trapezoidal shape is possible.
- resonant methods can also be used to supply the alternating current.
- a preferred embodiment of the fuel cell system according to the invention comprises an AC voltage generating device, which is constructed from an AC voltage source and a DC voltage source connected electrically in series with the AC voltage source.
- the alternating and the DC voltage source are integrated in one unit or the AC voltage generating device contains a single device, which has both functions at the same time.
- AC and DC voltage sources are realized by a power electronic circuit.
- a power electronic circuit This can e.g. consist of a buck converter, a boost converter, an inverting converter, a single-ended primary inductance converter (SEPIC) converter, a Cuk converter and / or a circuit related thereto.
- SEPIC single-ended primary inductance converter
- a bidirectional circuit is used, which can be used both for heating the fuel cell stack, as well as for the conversion of the output voltage (DC / DC converter) ' in the normal fuel cell operation.
- a further preferred variant provides that the AC voltage generating device has an AC voltage source and a capacitor connected electrically in series with the AC voltage source.
- an AC voltage with a frequency of 10 Hz to 10 MHz, preferably from 100 Hz to 1 MHz and more preferably and 1 kHz to 100 kHz, can be generated.
- an AC voltage to the fuel cell stack can be applied.
- the capacitance of the series capacitor is dependent on the fuel cell size and the frequency of the AC voltage and is preferably in the range between 1 ⁇ F to 10 F.
- the inventive fuel cell system has the particular advantages that the heat generation takes place directly in the fuel cell and no heating of additional components or masses is required. This means that for other components, such. a heating element can be dispensed with. Depending on the design of the required voltage converter to stabilize the output voltage, i. To supply the connected consumers, this can be designed bidirectionally and take over the heating of the fuel cell.
- Another advantage of the fuel cell system according to the invention is based on the fact that an air cooling of the fuel cell is possible.
- the invention likewise provides a heating method for heating a fuel cell stack having at least one fuel cell.
- an alternating current is fed into at least one of the individual cells of the fuel cell stack, wherein preferably the fuel cell system described above is used.
- a fuel cell system according to the invention can be designed or used as described in one of the following examples.
- the examples belonging to the example and described below ren have identical reference numerals for the same or similar components or components.
- FIG. 1a schematically shows a first fuel cell system according to the invention with an in-line fuel cell system
- FIG. 1b shows a second example of a fuel cell system according to the invention with an AC voltage source which is connected in series with a capacitor.
- Fig. 2 shows a simple equivalent circuit of a fuel cell stack with two single cells in series.
- FIG. 3a shows a first variant according to the invention of a bidirectional, power-electronic circuit.
- 3b shows a second variant of a bidirectional power electronic circuit according to the invention.
- reference numeral 1 denotes a fuel cell stack, which in the present case has six individual series-connected fuel cells. However, the fuel cell stack can also have more or fewer fuel cells, wherein the fuel cells can also be connected in parallel.
- the fuel cell stack is provided with two electrical connections Ia and Ib in the form of connection terminals, via which an electrical load can be connected to the fuel cell stack.
- the connection Ia Connected via a electrical line 3a to a first terminal of an AC voltage source 2a.
- the other electrical connection of the AC voltage source 2a is connected via a further electrical line 3b to a first terminal of a DC voltage source 2b.
- the second terminal of the DC voltage source 2b is connected via an electrical line 3c to the second terminal Ib of the fuel cell stack 1.
- the AC heating or AC voltage generating device 2 for the fuel cell stack is thus designed so that an AC voltage source 2a and a DC voltage source 2b (which determines the operating point) are connected in series.
- the voltage generated by the voltage sources is applied via the terminals Ia and Ib to the fuel cell stack 1, whereby an alternating current is fed directly through the terminals of the fuel cell stack 1 in the individual fuel cells of the stack. Due to the ohmic resistance of the stack, a heating thus takes place directly in the interior of the fuel cell stack.
- the applied voltage is selected, for example, such that an alternating voltage having an amplitude of 0.4 V per fuel cell of the fuel cell stack 1 is superimposed on the no-load voltage or the operating voltage of the fuel cell stack 1. Since in the present case the stack has six individual fuel cells, an alternating voltage with an amplitude of 2.4 V is thus superimposed on the fuel cell stack. However, larger or smaller amplitude values can also be applied. _
- the waveform of the applied AC voltage can be chosen to be rectangular or sinusoidal or to increase the power.
- Preferred here is a form of the alternating voltage, which is based on a rectangular shape, but is rounded by a sinusoidal superposition on the flanks.
- the frequency of the applied AC voltage is freely selectable in wide ranges, particularly advantageous frequencies between 10 Hz and 10 MHz.
- resonant methods can also be used depending on the capacity of the fuel cell stack.
- FIG. 1b shows a further embodiment of an alternating current heater according to the invention.
- the AC voltage generating device 2 has an AC voltage source 2 a and a capacitor 2 c connected in series with it via the electrical line 3 b.
- the alternating voltage generating device is connected via the two electrical leads 3 a and 3 c to the connection terminals 1 a and 1 c of the fuel cell stack 1.
- One or more consumers which are connected via corresponding electrical connections to the fuel cell or the fuel cell stack, can be connected to the fuel cell via its own circuit.
- FIG. 2 shows an equivalent circuit diagram of a fuel cell stack consisting of two fuel cells, which consists in the simplest form of a series circuit of resistors and capacitors.
- the resistances of the equivalent circuit diagram are determined by the conductivity of the materials used and the capacitor is replaced by the bipolar _ _
- Fig. 3a shows a bidirectional according to the invention
- the DC voltage of the capacitor Cl or a DC voltage source or battery connected in parallel to the CI is transformed by clocking the electronic switches S1 and S2 into a controllable DC voltage with a superimposed alternating voltage.
- the alternating voltage component causes the heating of the stack.
- the stack is the power source and the circuit operates as a boost converter and converts the DC voltage of the stack to a higher output voltage on capacitor C1.
- Parallel to Cl the electrical consumers can be connected.
- Capacitor C2 may optionally be connected in parallel with the fuel cell stack to support the voltage and / or smooth the currents.
- FIG. 3b shows a second variant of a bidirectional circuit according to the invention.
- the bidirectional converter operates as a boost converter to heat the fuel cell stack.
- the DC voltage of the capacitor Cl or a DC voltage source or battery connected in parallel to the CI is transformed by clocking the electronic switches S1 and S2 into a controllable DC voltage with a superimposed alternating voltage.
- the AC voltage component causes the heating of the stack.
- the stack is the power source and the circuit converts the DC voltage of the stack to a lower output voltage across capacitor C1.
- Parallel to C1 the electrical consumers can be connected.
- the capacitor C2 may advertising optionally connected in parallel to the fuel cell stack •, to support the voltage and / or to smooth the currents.
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
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102005012617A DE102005012617B4 (en) | 2005-03-18 | 2005-03-18 | Device and method for heating a fuel cell or a fuel cell stack |
PCT/EP2006/002194 WO2006097242A1 (en) | 2005-03-18 | 2006-03-09 | Device and method for heating a fuel cell stack by alternating current supply |
Publications (1)
Publication Number | Publication Date |
---|---|
EP1866991A1 true EP1866991A1 (en) | 2007-12-19 |
Family
ID=36293301
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP06707503A Withdrawn EP1866991A1 (en) | 2005-03-18 | 2006-03-09 | Device and method for heating a fuel cell stack by alternating current supply |
Country Status (5)
Country | Link |
---|---|
US (1) | US20080193815A1 (en) |
EP (1) | EP1866991A1 (en) |
JP (1) | JP2008533675A (en) |
DE (1) | DE102005012617B4 (en) |
WO (1) | WO2006097242A1 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102008025967A1 (en) | 2008-05-30 | 2009-12-03 | Elcomax Membranes Gmbh | The fuel cell system |
DE102008056604B4 (en) * | 2008-11-10 | 2011-02-03 | Continental Automotive Gmbh | Supply network for switchable consumers, in particular high-performance consumers in vehicles |
DE102009015619A1 (en) * | 2008-11-13 | 2010-05-27 | Tedatex Industrie Gmbh Beratung-Planung-Entwicklung | Fuel cell without bipolar plates |
DE102021106835A1 (en) | 2021-03-19 | 2022-09-22 | Audi Aktiengesellschaft | Method for operating a fuel cell device, fuel cell device and fuel cell vehicle |
Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58129785A (en) * | 1982-01-29 | 1983-08-02 | Toshiba Corp | Starting system for fused carbonate fuel cell layer body |
US5089700A (en) * | 1990-01-30 | 1992-02-18 | Amdata, Inc. | Apparatus for infrared imaging inspections |
DE19710819C1 (en) * | 1997-03-15 | 1998-04-02 | Forschungszentrum Juelich Gmbh | Fuel cell with anode-electrolyte-cathode unit |
US6340879B1 (en) * | 1999-02-03 | 2002-01-22 | Nokia Mobile Phones Ltd. | Device for reactivating an electric battery |
AT408160B (en) * | 1999-03-17 | 2001-09-25 | Vaillant Gmbh | COOLING DEVICE OF A FUEL CELL STACK AND ITS INVERTER |
DE19945668B4 (en) * | 1999-09-23 | 2004-10-07 | Siemens Ag | Method for starting a PEM fuel cell system and PEM fuel cell system for performing the method |
DE19954306B4 (en) * | 1999-11-11 | 2004-09-02 | Ballard Power Systems Ag | Device for generating electrical energy with a fuel cell in a vehicle and method for operating such a device |
JP2003051332A (en) * | 2001-08-07 | 2003-02-21 | Nissan Motor Co Ltd | Fuel cell and fuel cell power generating system |
JP4828056B2 (en) * | 2001-09-10 | 2011-11-30 | 三菱重工メカトロシステムズ株式会社 | Reduction device and denitration device |
DE10154366A1 (en) * | 2001-11-06 | 2003-05-22 | Zsw | System for producing a single phase alternating current comprises a fuel cell arrangement which delivers an electrical current, and an inverter |
DE60215700T2 (en) * | 2001-12-27 | 2007-02-08 | Nissan Motor Co., Ltd., Yokohama | HEATING OF A FUEL CELL POWER PLANT WITH POLYMER ELECTROLYTES |
JP2003285069A (en) * | 2002-03-28 | 2003-10-07 | Hitachi Metals Ltd | Fluid cleaning device |
JP4048900B2 (en) * | 2002-10-03 | 2008-02-20 | 株式会社デンソー | Fuel cell system |
US7192666B2 (en) * | 2003-12-05 | 2007-03-20 | Microsoft Corporation | Apparatus and method for heating fuel cells |
-
2005
- 2005-03-18 DE DE102005012617A patent/DE102005012617B4/en not_active Expired - Fee Related
-
2006
- 2006-03-09 EP EP06707503A patent/EP1866991A1/en not_active Withdrawn
- 2006-03-09 WO PCT/EP2006/002194 patent/WO2006097242A1/en active Application Filing
- 2006-03-09 US US11/908,453 patent/US20080193815A1/en not_active Abandoned
- 2006-03-09 JP JP2008501204A patent/JP2008533675A/en active Pending
Non-Patent Citations (1)
Title |
---|
See references of WO2006097242A1 * |
Also Published As
Publication number | Publication date |
---|---|
WO2006097242A1 (en) | 2006-09-21 |
DE102005012617B4 (en) | 2006-12-14 |
US20080193815A1 (en) | 2008-08-14 |
JP2008533675A (en) | 2008-08-21 |
DE102005012617A1 (en) | 2006-10-12 |
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Inventor name: ZEDDA, MARIO Inventor name: HESSELMANN, JAN Inventor name: BURGER, BRUNO |
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