CN114122461B - Method for activating fuel cell - Google Patents
Method for activating fuel cell Download PDFInfo
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- CN114122461B CN114122461B CN202010897806.0A CN202010897806A CN114122461B CN 114122461 B CN114122461 B CN 114122461B CN 202010897806 A CN202010897806 A CN 202010897806A CN 114122461 B CN114122461 B CN 114122461B
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- fuel cell
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- 239000000446 fuel Substances 0.000 title claims abstract description 57
- 238000000034 method Methods 0.000 title claims abstract description 25
- 230000003213 activating effect Effects 0.000 title claims description 5
- 239000012528 membrane Substances 0.000 claims abstract description 57
- 230000004913 activation Effects 0.000 claims abstract description 32
- 230000009471 action Effects 0.000 claims description 2
- 230000032683 aging Effects 0.000 abstract description 6
- 230000008859 change Effects 0.000 abstract description 3
- 230000000694 effects Effects 0.000 abstract description 3
- 230000002035 prolonged effect Effects 0.000 abstract description 3
- 238000001994 activation Methods 0.000 description 29
- 239000007789 gas Substances 0.000 description 7
- 238000006073 displacement reaction Methods 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 2
- 230000020411 cell activation Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000033228 biological regulation Effects 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000887 hydrating effect Effects 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- -1 hydrogen ions Chemical class 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000006467 substitution reaction Methods 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
- H01M8/04223—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
-
- 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
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1004—Fuel cells with solid electrolytes characterised by membrane-electrode assemblies [MEA]
-
- 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
- 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)
- Inert Electrodes (AREA)
- Fuel Cell (AREA)
Abstract
The invention discloses an activation method of a fuel cell, an anode plate and a cathode plate of the fuel cell are separated by a membrane electrode assembly, an anode inlet and a cathode outlet are positioned at a first end of the membrane electrode assembly, and an anode outlet and a cathode inlet are positioned at a second end of the membrane electrode assembly, and the activation method comprises the following steps: acquiring a first end pressure difference; if the first end pressure differential exceeds a threshold, the cathode inlet pressure is raised to reduce the first end pressure differential. Therefore, the large pressure difference can be prevented from directly acting on the membrane electrode assembly, the mechanical property damage of the membrane electrode assembly is avoided, the aging speed of the membrane electrode assembly is slowed down, the service life of the membrane electrode assembly and the service life of the fuel cell are prolonged, the hydraulic diameter of the cathode side can be prevented from being extruded by the membrane electrode assembly, the change of the hydraulic diameter of the cathode side is avoided, the drainage characteristic of the cathode side is kept stable, the drainage effect of the cathode side is improved, the flooding phenomenon of the cathode side is avoided, and the working stability of the fuel cell is improved.
Description
Technical Field
The invention relates to the technical field of fuel cells, in particular to an activation method of a fuel cell.
Background
Before a fuel cell is put into practical use, it is necessary to perform an activation test on a Membrane Electrode Assembly (MEA), remove residual impurities introduced during the manufacturing process of the MEA and the fuel cell stack, activate catalyst metal reaction sites that cannot participate in the reaction, ensure transfer paths of reactants to the catalyst, and ensure transfer paths of hydrogen ions by sufficiently hydrating electrolyte membranes and electrolytes contained in the electrodes.
In the related art, during the activation process of the fuel cell, the inlet pressure of the cathode plate and the anode plate is kept at a fixed value, and as the current density increases, the gas flow rate continuously increases, so that a pressure drop is generated between the inlet and the outlet of the gas. Particularly, when the gas flow directions of the cathode plate and the anode plate of the fuel cell are opposite, a large pressure difference is formed at two sides of the membrane electrode assembly at the anode inlet and the cathode outlet, and the mechanical properties of the membrane electrode assembly are damaged due to the pressure difference. When the pressure difference exceeds the bearing capacity of the membrane electrode assembly, the aging of the membrane electrode assembly can be accelerated, even the rupture of the membrane electrode assembly can cause the damage of a galvanic pile, and the pressure difference on two sides of the membrane electrode assembly is overlarge, so that the hydraulic diameter of a distribution area on the cathode side of the fuel cell can be reduced, and a flooding phenomenon is generated.
Disclosure of Invention
The present invention aims to solve at least one of the technical problems existing in the prior art. Therefore, an object of the present invention is to provide a method for activating a fuel cell, which can reduce a pressure difference across a membrane electrode assembly, prevent the membrane electrode assembly from aging or even cracking, and improve a drainage performance of a cathode side of the fuel cell during activation.
According to an embodiment of the first aspect of the present application, an activation method of a fuel cell in which an anode plate and a cathode plate are spaced apart by a membrane electrode assembly, an anode inlet and a cathode outlet are located at a first end of the membrane electrode assembly, and an anode outlet and a cathode inlet are located at a second end of the membrane electrode assembly, the activation method comprising: acquiring a first end pressure difference; if the first end pressure differential exceeds a threshold, the cathode inlet pressure is raised to reduce the first end pressure differential.
According to the activation method of the fuel cell, the first end pressure difference is obtained in real time, and when the pressure difference exceeds the threshold value, the cathode inlet pressure is raised to reduce the movement amplitude of the membrane electrode assembly towards the cathode side, so that the large pressure difference can be prevented from directly acting on the membrane electrode assembly, mechanical property damage of the membrane electrode assembly is avoided, the aging speed of the membrane electrode assembly is slowed down, the service lives of the membrane electrode assembly and the fuel cell are prolonged, the hydraulic diameter of the cathode side is prevented from being extruded by the membrane electrode assembly, the change of the hydraulic diameter of the cathode side is avoided, the drainage characteristic of the cathode side is kept stable, the drainage effect of the cathode side is improved, flooding phenomenon of the cathode side is avoided, and the working stability of the activated fuel cell is improved.
According to some embodiments of the present application, the cathode inlet pressure is raised while the anode inlet pressure is raised.
In some embodiments, the anode inlet pressure is greater than the cathode inlet pressure.
According to some embodiments of the application, further comprising: and acquiring the current density of the fuel cell, and setting an initial anode inlet pressure and an initial cathode inlet pressure according to the current density.
In some embodiments, if the fuel cell is in a high electrical density condition, setting the initial anode inlet pressure and the initial cathode inlet pressure to high pressure; if the fuel cell is in a low electrical density condition, the initial anode inlet pressure and the initial cathode inlet pressure are set to a low pressure.
Further, the acquiring the first end pressure difference includes: acquiring the initial anode inlet pressure and the anode outlet pressure; acquiring the initial cathode inlet pressure and the cathode outlet pressure; the initial anode inlet pressure-cathode outlet pressure = first end pressure differential.
Optionally, the cathode outlet pressure = initial cathode inlet pressure-cathode drop, and the anode outlet pressure = initial anode inlet pressure-anode drop.
According to some embodiments of the application, further comprising: and continuing to acquire the first end pressure difference.
In some embodiments, the minimum activation voltage during activation of the fuel cell is 0.2v.
Further, the cathode inlet pressure is less than the anode outlet pressure.
Additional aspects and advantages of the invention will be set forth in part in the description which follows, and in part will be obvious from the description, or may be learned by practice of the invention.
Drawings
The foregoing and/or additional aspects and advantages of the invention will become apparent and may be better understood from the following description of embodiments taken in conjunction with the accompanying drawings in which:
FIG. 1 is a schematic representation of membrane electrode assembly displacement during fuel cell activation according to an embodiment of the present application;
fig. 2 is a schematic displacement diagram of a membrane electrode assembly during activation of a fuel cell of the prior art.
Reference numerals:
a membrane electrode assembly 10, an anode inlet 20, an anode outlet 30, a cathode inlet 40, and a cathode outlet 50.
Detailed Description
Embodiments of the present invention are described in detail below, examples of which are illustrated in the accompanying drawings, wherein like or similar reference numerals refer to like or similar elements or elements having like or similar functions throughout. The embodiments described below by referring to the drawings are illustrative only and are not to be construed as limiting the invention.
First, as shown in fig. 2, in the prior art, during the activation of the fuel cell, the pressures of the cathode inlet 40 and the anode inlet 20 remain constant, and as the current density increases, the gas flow rate increases continuously, which causes a pressure drop between the anode inlet 20 and the anode outlet 30, and a pressure drop between the cathode inlet 40 and the cathode outlet 50.
Resulting in a large pressure difference between the anode inlet 20 and the cathode outlet 50, which can cause the membrane electrode assembly 10 to move toward the cathode side (see the dotted line portion of fig. 2), cause damage to the mechanical properties of the membrane electrode assembly, and when the pressure difference exceeds the withstand capability of the membrane electrode assembly 10, accelerate the aging of the membrane electrode assembly 10, even cause the rupture of the membrane electrode assembly 10, and further cause damage to the galvanic pile.
Meanwhile, the pressure drop between the anode inlet 20 and the anode outlet 30 and the pressure drop between the cathode inlet 40 and the cathode outlet 50 are related to the gas flow rate, the pressure and the hydraulic diameter (the path for discharging the working product of the fuel cell), at the same pressure, the larger the flow rate, the larger the pressure drop, the smaller the pressure drop, the larger the hydraulic diameter and the smaller the pressure drop.
Based on this, in the (stack) activation process of the existing fuel cell, when the current density is low, the flow rate is reduced due to the excessively high voltage, so that the flooding phenomenon (i.e., the working product of the fuel cell cannot be discharged in time and accumulated on the cathode side) occurs in the fuel cell, and when the current density is high, the cathode pressure drop becomes large, so that the pressure difference on both sides of the end portion of the membrane electrode assembly 10 is further increased, the hydraulic diameter is reduced, and the flooding phenomenon is further deteriorated.
A method of activating a fuel cell according to an embodiment of the present invention is described below with reference to fig. 1 to 2.
As shown in fig. 1, according to the activation method of the fuel cell according to the embodiment of the first aspect of the present application, the anode plate and the cathode plate of the fuel cell are spaced apart by the membrane electrode assembly, the anode inlet 20 and the cathode outlet 50 are located at the first end of the membrane electrode assembly, and the anode outlet 30 and the cathode inlet 40 are located at the second end of the membrane electrode assembly.
The activation method comprises the following steps: acquiring a first end pressure difference; if the first end pressure differential exceeds the threshold, the cathode inlet 40 pressure is raised to reduce the first end pressure differential.
It is understood that the threshold represents the threshold of the pressure difference, and the thresholds of the fuel cells with different specifications and sizes are different, so that those skilled in the art can reasonably set during the practical application of the method of the present application,
specifically, in the activation method of the fuel cell of the present application, first, the pressure difference between the anode inlet 20 and the cathode outlet 50 is obtained, and when the pressure difference exceeds the first threshold value, it is determined that the membrane electrode assembly 10 will move towards the cathode side under the action of the pressure difference, and the pressure of the cathode inlet 40 is raised, as described above, the pressure drop between the cathode inlet 40 and the cathode outlet 50 is reduced as the pressure of the cathode inlet 40 rises, so that the pressure of the cathode outlet 50 is higher by raising the pressure of the cathode inlet 40, and the pressure difference between the anode inlet 20 and the cathode outlet 50 is ensured to be within the threshold value, so as to effectively reduce the displacement amount of the membrane electrode assembly 10 towards the cathode side.
According to the activation method of the fuel cell in the embodiment of the invention, the first end pressure difference is obtained in real time, and when the pressure difference exceeds the threshold value, the pressure of the cathode inlet 40 is raised to reduce the movement amplitude of the membrane electrode assembly 10 towards the cathode side, so that the larger pressure difference can be prevented from directly acting on the membrane electrode assembly 10, the mechanical property damage of the membrane electrode assembly 10 is avoided, the aging speed of the membrane electrode assembly 10 is slowed down, the service life of the membrane electrode assembly 10 and the fuel cell is prolonged, the hydraulic diameter of the cathode side is prevented from being extruded by the membrane electrode assembly 10, the change of the hydraulic diameter of the cathode side is avoided, the drainage characteristic of the cathode side is kept stable, the drainage effect of the cathode side is improved, the flooding phenomenon of the cathode side is avoided, and the working stability of the activated fuel cell is improved.
It should be noted that, if the fuel cell is flooded, emergency shutdown of the fuel cell may be required, resulting in an open circuit point of the membrane electrode assembly 10, and further, a life of the membrane electrode assembly 10 may be reduced.
According to some embodiments of the present application, the cathode inlet 40 pressure is raised while the anode inlet 20 pressure is raised and the anode inlet 20 pressure is ensured to be greater than the cathode inlet 40 pressure.
It should be noted that when the pressure of the cathode inlet 40 is raised, the pressure of the cathode inlet 40 may be higher than the pressure of the anode inlet 20, which may cause the gas on the cathode side to diffuse to the anode side, resulting in a hydrogen-air interface on the anode side, causing deterioration of the counter electrode or the membrane electrode assembly.
Further, the anode inlet 20 is raised while the cathode inlet 40 pressure is raised, and it is ensured that the anode inlet 20 pressure is greater than the cathode inlet 40 pressure, so that the gas diffusion phenomenon at the anode side is avoided, thereby improving the operation stability of the fuel cell.
According to some embodiments of the present application, the activation method further comprises: the current density of the fuel cell is obtained, and an initial anode inlet pressure and an initial cathode inlet pressure are set according to the current density.
Specifically, if the fuel cell is in a high-density condition, the initial anode inlet pressure and the initial cathode inlet pressure are set to high pressures; if the fuel cell is in a low electrical density condition, the initial anode inlet pressure and the initial cathode inlet pressure are set to a low pressure. Thus, the pressures at the anode inlet 20, the anode outlet 30, the cathode inlet 40, and the cathode outlet 50 are all more reasonable, and the activation efficiency and activation level can be improved.
It will be appreciated that obtaining the first end pressure differential includes: acquiring an initial anode inlet pressure and an anode outlet 30 pressure; acquiring an initial cathode inlet pressure and a cathode outlet 50 pressure; initial anode inlet pressure-cathode outlet 50 pressure = first end pressure differential.
Wherein cathode outlet 50 pressure = initial cathode inlet pressure-cathode drop, anode outlet 30 pressure = initial anode inlet pressure-anode drop. Thus, in the activation method of the present application, the pressure of the cathode outlet 50, the pressure of the anode inlet 20 and the pressure difference between the two are obtained more accurately in the activation process of the fuel cell, so that the accuracy of pressure regulation of the cathode inlet 40 and the anode inlet 20 can be improved, and the activation stability can be improved.
According to some embodiments of the application, further comprising: the first end pressure differential continues to be obtained. That is, after the cathode inlet 40 and anode inlet 20 pressures are adjusted, the first end pressure difference is continuously obtained, and when the first end pressure difference exceeds the threshold again, the cathode inlet 40 pressure and anode inlet 20 pressure are further adjusted.
In some embodiments, the minimum activation voltage during fuel cell activation is 0.2v. Thereby, the activation efficiency can be accelerated to improve the activation efficiency of the fuel cell.
Further, the cathode inlet 40 pressure is less than the anode outlet 30 pressure.
Next, an explanation will be given of an activation method of the fuel cell of the present application in one specific example.
When the anode inlet 20 pressure was set to 210kPa, the anode pressure drop was 10kPa at the anode plate at the highest flow rate at an electrical density of 2.0A/cm2, and the anode outlet 30 pressure was 200 kPa;
when the cathode inlet 40 pressure is set to 200kapa and the cathode plate pressure drop is set to 100kPaa, the cathode outlet 50 pressure is set to 100kPaa, and the MEA anode inlet 20 pressure difference is 210-100=110 kPa, which is much larger than the operating pressure of a typical MEA.
Further, as the pressure increases, the pressure drop decreases by raising the cathode inlet 40 pressure to 250kPaa, the cathode pressure drop decreases from 100kPa to 50kPa, the cathode outlet 50 pressure is 200kPaa, and the anode inlet 20 pressure is raised to 260kPa, the anode outlet 30 pressure is not lower than 250kPaa.
At this time, the anode inlet 20 pressure-cathode outlet 50 pressure=60 kPaa is smaller than the initial 110kPaa, so that the displacement width of the membrane electrode assembly 10 toward the cathode side can be reduced, the pressure difference across the membrane electrode assembly 10 can be reduced, and the drainage characteristics can be improved.
Based on the above, in the activation method of the application, in the activation process of the fuel cell, the pressure setting is related to the current density, the low electric density is kept at low pressure, flooding caused by insufficient flow rate is improved, the high electric density is set at high pressure, and the inlet pressures of the cathode plate and the anode plate are raised according to the pressure drop, so that the hydraulic diameter deformation is reduced, the deformation of the membrane electrode assembly 10 is reduced, the flooding problem caused by overlarge pressure drop is improved, and the activation process is smoothly carried out.
In the description of the present invention, it should be understood that the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", "axial", "radial", "circumferential", etc. indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings are merely for convenience in describing the present invention and simplifying the description, and do not indicate or imply that the device or element being referred to must have a specific orientation, be configured and operated in a specific orientation, and therefore should not be construed as limiting the present invention.
In the description of the invention, a "first feature" or "second feature" may include one or more of such features.
In the description of the present invention, "plurality" means two or more.
In the description of the invention, a first feature "above" or "below" a second feature may include both the first and second features being in direct contact, and may also include the first and second features not being in direct contact but being in contact with each other by another feature therebetween.
In the description of the invention, a first feature being "above," "over" and "on" a second feature includes the first feature being directly above and obliquely above the second feature, or simply indicates that the first feature is higher in level than the second feature.
In the description of the present specification, reference to the terms "one embodiment," "some embodiments," "illustrative embodiments," "examples," "specific examples," or "some examples," etc., means that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the invention. In this specification, schematic representations of the above terms do not necessarily refer to the same embodiments or examples. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples.
While embodiments of the present invention have been shown and described, it will be understood by those of ordinary skill in the art that: many changes, modifications, substitutions and variations may be made to the embodiments without departing from the spirit and principles of the invention, the scope of which is defined by the claims and their equivalents.
Claims (5)
1. A method of activating a fuel cell, wherein an anode plate and a cathode plate of the fuel cell are separated by a membrane electrode assembly, an anode inlet (20) and a cathode outlet (50) are located at a first end of the membrane electrode assembly, an anode outlet (30) and a cathode inlet (40) are located at a second end of the membrane electrode assembly, the method comprising:
acquiring a first end pressure differential, the acquiring the first end pressure differential comprising: acquiring an initial anode inlet pressure and an anode outlet (30) pressure; acquiring an initial cathode inlet pressure and a cathode outlet (50) pressure; -the initial anode inlet pressure-cathode outlet (50) pressure = first end pressure difference;
if the first end pressure difference exceeds a threshold value, the membrane electrode assembly (10) is judged to move towards the cathode side under the action of the pressure difference, the cathode inlet (40) pressure is raised to reduce the first end pressure difference, the anode inlet (20) pressure is raised while the cathode inlet (40) pressure is raised, the cathode inlet (40) pressure is smaller than the anode outlet (30) pressure, and the anode inlet (20) pressure is larger than the cathode inlet (40) pressure.
2. The activation method of a fuel cell according to claim 1, characterized by further comprising: and acquiring the current density of the fuel cell, and setting an initial anode inlet pressure and an initial cathode inlet pressure according to the current density.
3. The method of activation of a fuel cell according to claim 1, characterized in that the cathode outlet (50) pressure = initial cathode inlet pressure-cathode drop and the anode outlet (30) pressure = initial anode inlet pressure-anode drop.
4. The activation method of a fuel cell according to claim 1, characterized by further comprising: and continuing to acquire the first end pressure difference.
5. The activation method of a fuel cell according to claim 1, wherein the minimum activation voltage during activation of the fuel cell is 0.2v.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010897806.0A CN114122461B (en) | 2020-08-31 | 2020-08-31 | Method for activating fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010897806.0A CN114122461B (en) | 2020-08-31 | 2020-08-31 | Method for activating fuel cell |
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| Publication Number | Publication Date |
|---|---|
| CN114122461A CN114122461A (en) | 2022-03-01 |
| CN114122461B true CN114122461B (en) | 2024-04-16 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202010897806.0A Active CN114122461B (en) | 2020-08-31 | 2020-08-31 | Method for activating fuel cell |
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005150090A (en) * | 2003-10-24 | 2005-06-09 | Toyota Motor Corp | Fuel cell system |
| JP2006147336A (en) * | 2004-11-19 | 2006-06-08 | Nissan Motor Co Ltd | Fuel cell system |
| JP2009140672A (en) * | 2007-12-05 | 2009-06-25 | Honda Motor Co Ltd | Fuel cell |
| JP2009181964A (en) * | 2009-05-18 | 2009-08-13 | Toyota Motor Corp | Fuel cell system |
| KR20130083278A (en) * | 2012-01-12 | 2013-07-22 | 지에스칼텍스 주식회사 | Membrane electrode assembly for fuel cell |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3832802B2 (en) * | 2000-07-25 | 2006-10-11 | 本田技研工業株式会社 | Fuel cell system and control method thereof |
| JP4901913B2 (en) * | 2009-06-05 | 2012-03-21 | 本田技研工業株式会社 | Fuel cell |
| KR102478090B1 (en) * | 2017-10-30 | 2022-12-16 | 현대자동차주식회사 | Cell frame for fuel cell and fuel cell stack using the same |
-
2020
- 2020-08-31 CN CN202010897806.0A patent/CN114122461B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005150090A (en) * | 2003-10-24 | 2005-06-09 | Toyota Motor Corp | Fuel cell system |
| JP2006147336A (en) * | 2004-11-19 | 2006-06-08 | Nissan Motor Co Ltd | Fuel cell system |
| JP2009140672A (en) * | 2007-12-05 | 2009-06-25 | Honda Motor Co Ltd | Fuel cell |
| JP2009181964A (en) * | 2009-05-18 | 2009-08-13 | Toyota Motor Corp | Fuel cell system |
| KR20130083278A (en) * | 2012-01-12 | 2013-07-22 | 지에스칼텍스 주식회사 | Membrane electrode assembly for fuel cell |
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| Publication number | Publication date |
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| CN114122461A (en) | 2022-03-01 |
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