WO1998045890A1 - Verfahren zum regeln der membranfeuchte einer polymerelektrolyt-brennstoffzelle und polymerelektrolyt-brennstoffzelle - Google Patents
Verfahren zum regeln der membranfeuchte einer polymerelektrolyt-brennstoffzelle und polymerelektrolyt-brennstoffzelle Download PDFInfo
- Publication number
- WO1998045890A1 WO1998045890A1 PCT/EP1997/001793 EP9701793W WO9845890A1 WO 1998045890 A1 WO1998045890 A1 WO 1998045890A1 EP 9701793 W EP9701793 W EP 9701793W WO 9845890 A1 WO9845890 A1 WO 9845890A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- fuel cell
- membrane
- polymer electrolyte
- moisture
- water
- 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
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04291—Arrangements for managing water in solid electrolyte fuel cell systems
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2300/00—Electrolytes
- H01M2300/0017—Non-aqueous electrolytes
- H01M2300/0065—Solid electrolytes
- H01M2300/0082—Organic polymers
-
- 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
- H01M8/04082—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
- H01M8/04119—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with simultaneous supply or evacuation of electrolyte; Humidifying or dehumidifying
-
- 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 a method for regulating the membrane moisture of a polymer electrolyte fuel cell and a polymer electrolyte fuel cell with a device for regulating the membrane moisture.
- the fuel cells contain solid polymer membranes as the electrolyte, and preferably use hydrogen and as the fuel gas
- Oxidizing agents air or oxygen under low pressure.
- Polymer electrolyte fuel cells as are usually used to generate electrical current, contain an anode, a cathode and an ion exchange membrane arranged between them.
- a plurality of fuel cells form a fuel cell stack, the individual fuel cells being separated from one another by bipolar plates which act as current collectors.
- a fuel gas e.g. Hydrogen
- an oxidizing agent e.g. Air or oxygen in which
- Anode and cathode each contain a catalyst layer in the areas in contact with the polymer electrolyte membrane.
- the fuel is oxidized to form cations and free electrons
- the cathode catalyst layer the oxidizing agent is passed through
- Electron absorption reduced The cations migrate through the ion exchange membrane to the cathode and react with the reduced oxidizing agent, water being produced when hydrogen is used as the fuel gas and oxygen as the oxidizing agent. The reaction of fuel gas and oxidant becomes considerable
- the object of the invention is to provide a polymer electrolyte fuel cell or a polymer electrolyte fuel cell stack, the polymer electrolyte membrane of a fuel cell always having the optimum moisture content during operation.
- the object is achieved by the method for regulating the membrane moisture of a polymer electrolyte fuel cell according to claim 1, the polymer electrolyte fuel cell according to claim 7 and the fuel cell stack comprising a plurality of polymer electrolyte fuel cells according to claim 12.
- Polymer electrolyte membranes require a high water content in order to ensure optimal conductivity for H + ions.
- water content must be maintained by supplying water, since otherwise the fuel and oxidant gas streams flowing through the cell dry out the membrane. To counteract possible drying out by adding an excess of water, however, does not make sense, since water leads to flooding of the electrodes in large quantities, ie the pores of the electrodes are blocked. A simple determination and regulation of the amount of water required was previously not possible.
- Fig. 2 shows a circuit for measuring the impedance of a
- Fig. 3 shows the dependence of the conductivity of a Nafion 'membrane on
- Fig. 4a is a schematic representation of the control of the
- Fig. 4b is a schematic representation of the control of the change in working conditions.
- a polymer electrolyte fuel cell according to the invention uses air or oxygen at a slight positive pressure as the oxidizing agent.
- An excess pressure of less than 2 bar is preferred, particularly preferably less than 0.5 bar.
- the required pressure difference can also be achieved by suction.
- Hydrogen is preferably used as the fuel gas, but the use of other fuel gases is also possible in principle.
- Nafion ® is preferably used as the polymer electrolyte membrane. Hydrogen is supplied to the individual fuel cells in a stack and distributed via gas channels in the anode area.
- Reaction product water The water formed evaporates due to the heat of reaction, which results in a certain cooling. On the one hand, the cooling effect is not sufficient, on the other hand, the membrane becomes increasingly poor in moisture during the operation of the fuel cell.
- N (H, O) / N (SO 3 H) denotes the number of water molecules per sulfonic acid residue in the membrane.
- a reduction in the moisture content of the solid polymer electrolyte membrane of a fuel cell therefore has the consequence that its internal resistance increases, that is to say its conductivity decreases.
- the conductivity of the membrane is extremely dependent on its water content.
- the polymer electrolyte membrane always has the optimum moisture corresponding to the respective working conditions (temperature, load, air ratio).
- the membrane In order to maintain the optimum humidity, it can be determined according to the invention during operation of the fuel cell, preferably regularly or continuously, whether the membrane is optimally moistened or whether measures are required to set the optimal membrane moisture.
- the optimum membrane moisture can be set, for example, by adding the required amount of water in a liquid or gaseous state.
- the water is preferably added to one of the reaction gases or to both reaction gases. More ways that
- the membrane at an optimal moisture content consists in adapt the working conditions to the determined moisture content.
- the most suitable working conditions are electrode temperatures, volume flows of the reaction gases and load of the fuel cell.
- the optimum membrane moisture is therefore preferably set as follows: after determining to what extent the actual moisture deviates from the nominal moisture, a certain amount of water is fed in or the temperature of at least one of the electrodes or the volume flow of fuel gas and / or oxidizing agent is changed in this way that the actual moisture of the membrane is changed at the
- Working conditions corresponds to the optimal moisture of the membrane.
- a change in the load is also possible in order to ensure that the optimum membrane moisture is brought substantially into agreement with the actual membrane moisture.
- several of the above-mentioned measures can also be combined in order to bring about the setting of the optimal membrane moisture.
- the amount of water added can vary widely. It depends on the respective working conditions of the fuel cell, and in particular also depends on the type of cooling of the fuel cell. Fuel cells are often supplied for cooling, which, depending on the design of the fuel cells, also moistens the membrane to a certain extent. Then, as a rule, less additional water has to be added than in cells with, for example, exclusively air cooling.
- the conductivity of the membrane depends on its water content. However, the conductivity of the membrane cannot be measured directly while a fuel cell is in operation. According to the invention, a measure of the moisture of the membrane, preferably the impedance of the fuel cell (amount of the impedance or particularly preferably real part of the impedance) is determined. Since the conductivity of the membrane is a constant, is monotonous function of these quantities, the required amount of water can also be regulated on the basis of the impedance.
- FIG. 2 A possible circuit for measuring the impedance of a fuel cell is shown in FIG. 2.
- the determination of the measure for the moisture of the membrane according to the invention does not require any auxiliary electrodes, i.e. it uses the working electrodes. Intervention in the cell itself is not necessary.
- the direct measurement of the conductance and thus the moisture content of a polymer electrolyte membrane of a fuel cell by determining the impedance is carried out by modulating the cell voltage with an alternating signal with a frequency of 1 to 20 kHz.
- the average is suitably
- AC voltage source U which is suitable for generating small AC voltages (of the order of about 10 mV) and large currents (of the order of about 10 A).
- the voltage of the fuel cell is modulated by the alternating signal (approximately 1-20 kHz) from the alternating voltage source.
- the alternating voltage component U causes the fuel cell current to be superimposed with an alternating current I.
- the quotient of alternating voltage and alternating current is a measure of the impedance of the fuel cell and thus a measure of the moisture of the polymer electrolyte membrane or of the required amount of water that has to be supplied.
- the amount of the impedance depends, apart from the conductivity of the membrane, on other parameters, namely on the size of the catalyst surface which is in contact with the membrane, on the ohmic resistance of the electrodes and the poisoning of the
- the setpoint of the amount of the impedance to be maintained should be reset in the course of maintenance work.
- the new setpoint is determined by maximizing the performance of the fuel cell.
- the optimum setpoint can alternatively be readjusted by fuzzy logic or similar methods familiar to the person skilled in the art, in accordance with the changed conditions.
- a measure of the conductivity of the membrane that is largely independent of the catalyst surface (whose change is essentially responsible for the change in the setpoint value of the impedance) is obtained if, in addition to the amount of the impedance, its phase angle is also taken into account. If the real part of the impedance determined electronically from this is considered as a controlled variable, a single setpoint value can even be used over the entire service life of the fuel cell.
- the impedance (amount or real part) can be measured continuously or at regular intervals. If the conductivity of the membrane or the membranes is calculated to be too low, water is supplied to the system, for example by opening electronically controlled water inlet valves in a conventional manner until the desired value of the impedance is reached again, or one or more of the Working conditions vary accordingly.
- Membrane to be determined individually, but average values for one To determine a plurality of cells of the stack or even for all cells of the stack together and to adjust the required water addition accordingly.
- FIG. 4b schematically shows a specific example for controlling the change in working conditions (air volume flow and load) in a fuel cell stack 20 which is operated with hydrogen 21 and air 22. If a non-optimal membrane moisture value is measured, the control device 30 controls the stronger opening or closing of the valve 31 as required until the required air volume flow is reached. Alternatively, the hydrogen volume flow 21 or both flows can be changed. Especially with air-cooled
- Fuel cells is also the control of the air flow 22
- Water in liquid form is introduced immediately. Alternatively, you can the water can also be introduced directly into the gas channels for the fuel gas.
- the liquid water evaporates in the hot fuel cell and, due to the phase change taking place, causes efficient cooling of the
- the simplest way to add the required amount of water to the air flow or the air and / or hydrogen flow is to use a metering pump to distribute the water in numerous thin lines, e.g. Capillaries to insert into the gas channels. There is no significant mixing of the water with the air or the fuel gas, so the free water surface available for evaporation is relatively small.
- Aerosol and possibly the water in fuel gas Aerosol contain water in the form of droplets of 2 to 20 ⁇ m in size, which ensure rapid evaporation or evaporation.
- the aerosol can be produced, for example, with the aid of ultrasonic atomizers or nozzles. The simplest and at the same time the least energy-intensive generation of the aerosol takes place by means of ultrasonic atomizers at frequencies of at least 100 kHz.
- a particularly advantageous embodiment of the invention is the design of the channels for receiving water in air aerosol or water-in-fuel gas aerosol, as shown in FIG. 1.
- each fuel cell is delimited on the anode and cathode sides by a bipolar plate 10, 6.
- the anode-side bipolar plate is simultaneously the cathode-side bipolar plate of a neighboring cell and the cathode-side bipolar plate is simultaneously the anode-side bipolar plate of the other neighboring cell.
- the bipolar plate has corrugated sheet structure at least in a partial area, so it alternately has elevations and depressions.
- a surface of the bipolar plate 6 touches with its elevations 7 the cathode region 2 of the fuel cell, as a result of which the depressions 8 between the two adjacent elevations form channels 5 with the cathode region for receiving water in air aerosol.
- the surface of the bipolar plate 10 touches the anode region 3 of the cell, so that the depressions 12 located between two adjacent anode-side elevations 11 also form channels 9 with the anode region 3. These can be used to absorb water in fuel aerosol.
- Fuel gas is fed through holes perpendicular to the plate surface.
- the hydrogen first enters channel 9, which is connected to the feed opening, and diffuses or flows from there into the adjacent porous anode region. From here, the hydrogen diffuses partly to the anode catalyst layer, partly in the
- cooling water is also to be fed in together with the fuel gas, it is generally more advantageous to choose the same type of supply as in the cathode region, that is to say to feed fuel and water into each individual channel 9. Because of the poor diffusion properties of water compared to hydrogen, little else would
- the construction has no separate cooling channels.
- a particular advantage is that the path of the aerosol through the channels 5 of the cell is a straight line.
- the corrugated sheet structure of the bipolar plate with straight gas paths makes it possible to minimize aerosol precipitation and to conduct the necessary volume flows with a small pressure drop.
- the "corrugated metal plate” is very simple and inexpensive to manufacture.
- the anode and cathode regions are each formed as a suitable catalyst-carrying diffusion layers which are arranged on the opposite sides of the polymer electrolyte membrane 4.
- the walls of the gas channels 5 and / or the gas channels 9 can be covered with a hydrophilic absorbent layer, for example with felt.
- the hydrophilic, absorbent layer distributes the amount of water introduced evenly and holds it until it evaporates.
- the amount of water required to achieve optimal membrane moistening can, as stated above, be electronic
- Paths are determined and regulated.
- the amount of water introduced into the fuel cell can perform two tasks: cooling the cell and moistening the membrane. However, only the setting of the suitable membrane moisture is taken into account to regulate the necessary amount of water. Depending on the
- the optimal parameters are temperature, load, air ratio and others Membrane moisture and thus the optimal conductivity of the membrane determined experimentally.
- the water addition varies depending on the conductivity to be achieved.
- the cell temperature varies widely depending on the operating conditions. However, as long as sufficient water is introduced to ensure optimal membrane moisture, an adequate cooling effect is guaranteed. However, cooling can also be ensured in a different way, for example by sufficient air flow.
- the reaction gas in particular the air
- the reaction gas can be passed through the cell stack several times. This is done by recycling the air / water mixture leaving the fuel cells or the fuel gas / water mixture leaving the fuel cells into the corresponding intake flow.
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- 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)
- Manufacture Of Macromolecular Shaped Articles (AREA)
Abstract
Description
Claims
Priority Applications (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA002286700A CA2286700C (en) | 1997-04-10 | 1997-04-10 | Method for regulating membrane moisture of a polymer electrolyte fuel cell, and a polymer electrolyte fuel cell |
JP54228298A JP2001519081A (ja) | 1997-04-10 | 1997-04-10 | ポリマー電解質燃料電池の膜水分の調節法およびポリマー電解質燃料電池 |
CNB97182102XA CN1160819C (zh) | 1997-04-10 | 1997-04-10 | 高分子电解质-燃料电池膜片湿度的调节方法与高分子电解质-燃料电池 |
DE59710703T DE59710703D1 (de) | 1997-04-10 | 1997-04-10 | Verfahren zum regeln der membranfeuchte einer polymerelektrolyt-brennstoffzelle und polymerelektrolyt-brennstoffzelle |
EP97917303A EP1008200B1 (de) | 1997-04-10 | 1997-04-10 | Verfahren zum regeln der membranfeuchte einer polymerelektrolyt-brennstoffzelle und polymerelektrolyt-brennstoffzelle |
PCT/EP1997/001793 WO1998045890A1 (de) | 1997-04-10 | 1997-04-10 | Verfahren zum regeln der membranfeuchte einer polymerelektrolyt-brennstoffzelle und polymerelektrolyt-brennstoffzelle |
US09/402,661 US6376110B1 (en) | 1997-04-10 | 1997-04-10 | Method for regulating membrane moisture of a polymer electrolyte fuel cell, and a polymer electrolyte fuel cell |
AT97917303T ATE249103T1 (de) | 1997-04-10 | 1997-04-10 | Verfahren zum regeln der membranfeuchte einer polymerelektrolyt-brennstoffzelle und polymerelektrolyt-brennstoffzelle |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/EP1997/001793 WO1998045890A1 (de) | 1997-04-10 | 1997-04-10 | Verfahren zum regeln der membranfeuchte einer polymerelektrolyt-brennstoffzelle und polymerelektrolyt-brennstoffzelle |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1998045890A1 true WO1998045890A1 (de) | 1998-10-15 |
Family
ID=8166580
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP1997/001793 WO1998045890A1 (de) | 1997-04-10 | 1997-04-10 | Verfahren zum regeln der membranfeuchte einer polymerelektrolyt-brennstoffzelle und polymerelektrolyt-brennstoffzelle |
Country Status (8)
Country | Link |
---|---|
US (1) | US6376110B1 (de) |
EP (1) | EP1008200B1 (de) |
JP (1) | JP2001519081A (de) |
CN (1) | CN1160819C (de) |
AT (1) | ATE249103T1 (de) |
CA (1) | CA2286700C (de) |
DE (1) | DE59710703D1 (de) |
WO (1) | WO1998045890A1 (de) |
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WO2001091216A2 (en) * | 2000-05-23 | 2001-11-29 | Nissan Motor Co., Ltd. | Fuel cell system and method of controlling the same |
JP2003086220A (ja) * | 2001-09-12 | 2003-03-20 | Denso Corp | 燃料電池システム |
WO2003098769A2 (en) * | 2002-05-17 | 2003-11-27 | Greenlight Power Technologies, Inc. | Methods and apparatus for indicating a fault condition in fuel cells and fuel cell components |
EP1487043A1 (de) * | 2002-03-20 | 2004-12-15 | Sony Corporation | Brennstoffbatterieneinrichtung und verfahren zur steuerung einer brennstoffbatterie |
US6872480B2 (en) * | 2000-09-25 | 2005-03-29 | Sulzer Hexis Ag | Method for operating a fuel cell battery |
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CN106797040A (zh) * | 2014-10-30 | 2017-05-31 | 日产自动车株式会社 | 燃料电池的状态估计装置、状态估计方法、以及燃料电池系统 |
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US7029775B2 (en) * | 1997-12-22 | 2006-04-18 | Kabushikikaisha Equos Research | Fuel cell system |
FR2786027B1 (fr) * | 1998-11-12 | 2006-04-28 | Commissariat Energie Atomique | Plaques bipolaires pour pile a combustible et pile a combustible comprenant ces plaques |
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US7022426B2 (en) * | 2000-09-22 | 2006-04-04 | Honda Giken Kogyo Kabushiki Kaisha | Solid polymer fuel cell |
CA2379363A1 (en) | 2001-03-28 | 2002-09-28 | Ballard Power Systems Inc. | Methods and apparatus for improving the cold starting capability of a fuel cell |
US6620538B2 (en) * | 2002-01-23 | 2003-09-16 | Avista Laboratories, Inc. | Method and apparatus for monitoring equivalent series resistance and for shunting a fuel cell |
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US8658322B2 (en) * | 2005-03-09 | 2014-02-25 | Toyota Jidosha Kabushiki Kaisha | Fuel cell system |
JP5017783B2 (ja) * | 2005-03-09 | 2012-09-05 | トヨタ自動車株式会社 | 燃料電池システム |
JP4924790B2 (ja) * | 2005-06-30 | 2012-04-25 | トヨタ自動車株式会社 | 燃料電池システム |
JP4892888B2 (ja) * | 2005-08-18 | 2012-03-07 | トヨタ自動車株式会社 | 燃料電池システムおよび燃料電池システムの運転方法 |
JP5083709B2 (ja) * | 2007-06-14 | 2012-11-28 | トヨタ自動車株式会社 | 燃料電池システム |
US20090191351A1 (en) * | 2008-01-28 | 2009-07-30 | Gm Global Technology Operations, Inc. | Fuel cell bipolar plate with variable surface properties |
US7901832B2 (en) * | 2008-05-13 | 2011-03-08 | GM Global Technology Operations LLC | Bipolar plate with inlet and outlet water management features |
DE102008052945B4 (de) * | 2008-10-23 | 2014-06-12 | Staxera Gmbh | Brennstoffzellenstapel und Verfahren zu dessen Herstellung |
FR2938978B1 (fr) * | 2008-11-26 | 2010-12-10 | St Microelectronics Tours Sas | Dispositif et procede controle de l'humidification d'une pile a combustible |
JP4640661B2 (ja) * | 2009-01-13 | 2011-03-02 | トヨタ自動車株式会社 | 燃料電池システム |
US8932775B2 (en) | 2010-05-28 | 2015-01-13 | Toyota Jidosha Kabushiki Kaisha | Method and apparatus for controlling the operation of a fuel cell |
WO2015005034A1 (ja) * | 2013-07-11 | 2015-01-15 | 日産自動車株式会社 | 燃料電池システム及び燃料電池システムの制御方法 |
KR101592704B1 (ko) * | 2014-06-11 | 2016-02-15 | 현대자동차주식회사 | 연료전지 스택의 상태 진단 방법 및 연료전지 시스템의 제어방법 |
JP6508161B2 (ja) | 2016-10-18 | 2019-05-08 | トヨタ自動車株式会社 | 燃料電池システム |
JP6597566B2 (ja) | 2016-11-21 | 2019-10-30 | トヨタ自動車株式会社 | 燃料電池システム |
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1997
- 1997-04-10 CN CNB97182102XA patent/CN1160819C/zh not_active Expired - Fee Related
- 1997-04-10 AT AT97917303T patent/ATE249103T1/de not_active IP Right Cessation
- 1997-04-10 EP EP97917303A patent/EP1008200B1/de not_active Expired - Lifetime
- 1997-04-10 JP JP54228298A patent/JP2001519081A/ja active Pending
- 1997-04-10 DE DE59710703T patent/DE59710703D1/de not_active Expired - Lifetime
- 1997-04-10 US US09/402,661 patent/US6376110B1/en not_active Expired - Fee Related
- 1997-04-10 WO PCT/EP1997/001793 patent/WO1998045890A1/de active IP Right Grant
- 1997-04-10 CA CA002286700A patent/CA2286700C/en not_active Expired - Fee Related
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Also Published As
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EP1008200A1 (de) | 2000-06-14 |
CA2286700A1 (en) | 1998-10-15 |
JP2001519081A (ja) | 2001-10-16 |
US6376110B1 (en) | 2002-04-23 |
CN1251690A (zh) | 2000-04-26 |
EP1008200B1 (de) | 2003-09-03 |
CN1160819C (zh) | 2004-08-04 |
ATE249103T1 (de) | 2003-09-15 |
CA2286700C (en) | 2008-12-02 |
DE59710703D1 (de) | 2003-10-09 |
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