CN101295796A - Fuel cell system - Google Patents
Fuel cell system Download PDFInfo
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- CN101295796A CN101295796A CNA2007101018591A CN200710101859A CN101295796A CN 101295796 A CN101295796 A CN 101295796A CN A2007101018591 A CNA2007101018591 A CN A2007101018591A CN 200710101859 A CN200710101859 A CN 200710101859A CN 101295796 A CN101295796 A CN 101295796A
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- 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
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Abstract
The invention relates to a fuel cell system which comprises a cell unit consisting of an anode collector layer, a cathode collector layer, a thin film electrode array clipped between the anode collector layer and the cathode collector layer, a frame around the thin film electrode array, the anode collector layer and the cathode collector layer, a hydrophilic resistive gas layer positioned below the thin film electrode array and the frame and a hydrophobic breathable layer arranged below the hydrophilic resistive gas layer, and at least one gas discharge channel which is embedded in the frame, exposes one part of the hydrophilic resistive gas layer and contacts the environment adjacent to the cell unit so as to discharge the gas generated by the thin film electrode array outside the cell unit.
Description
Technical field
The present invention relates to a kind of fuel cell system, and be particularly related to a kind of fuel cell system that can discharge its internal reaction generation gas.
Background technology
Fuel cell (Fuel Cell, FC) be a kind of Blast Furnace Top Gas Recovery Turbine Unit (TRT) of utilizing chemical energy to be converted into electric energy, under traditional generation mode comparison, fuel cell has low pollution, low noise, high-energy-density and higher advantages such as energy conversion efficiency, be to have following prospective clean energy, applicable scope comprises various fields such as portable electric product, household system, means of transportation, military equipment, space industry and large generating system.
Common fuel cell can be divided into following five kinds substantially according to employed electrolytical kind:
1. alkaline fuel cell (AFC): with potassium hydroxide is electrolyte;
2. carbonic acid fuel cell (PAFC): with the phosphoric acid solution is electrolyte;
3. molten carbonate fuel cell (MCFC): with carbonic acid thing fusion back as electrolyte;
4. solid eleectrolyte fuel cell (SOFC): mainly with zirconium dioxide as electrolyte; And
5. Proton Exchange Membrane Fuel Cells (PEMFC): comprise so-called direct methanol fuel cell (DMFC), be fuel directly, and need do not form hydrogen in advance with methyl alcohol.
Wherein, direct methanol fuel cell (DMFC) is originated as fuel supply because of directly using the methyl alcohol of liquid state or gaseous state, and need not supply the usefulness of generating with other materials such as reorganization methyl alcohol, gasoline and natural gases with generation hydrogen by reformer, it has low temperature and gives birth to characteristics such as electric, that the dangerous low and living electricity of propellant composition is simple in structure, so makes direct methanol fuel cell become the main flow that portable electronic product is used gradually.
Known direct methanol fuel cell mainly is to be made of mea (Membrane ElectrodeAssembly is called for short MEA), anode collector plate and cathode collector plate.Mea be by proton-conductive films (Proton Exchange Membrance), anode catalyst layer, cathode catalysts layer, anode gas diffusion layer (Gas Diffusion Layer, GDL) and cathode gas diffusion layer constitute.Wherein, above-mentioned anode catalyst layer and cathode catalysts layer are disposed at the both sides of proton-conductive films respectively, and anode gas diffusion layer and cathode gas diffusion layer are separately positioned on anode catalyst layer and the cathode catalysts layer.Anode collector plate and cathode collector plate are to be arranged at respectively on anode gas diffusion layer and the cathode gas diffusion layer.The reaction equation of direct methanol fuel cell is as follows:
Positive C H
3OH+H
2O → CO
2+ 6H
++ 6e
-(1)
Negative electrode (3/2) O
2+ 6H
++ 6e
-→ 3H
2O (2)
Full response CH
3OH+ (3/2) O
2→ CO
2+ 2H
2O (3)
Can be understood by reaction equation (1), when direct methanol fuel cell was operated, its anode partly had CO
2Produce, for fear of the excessive gas pressure of anode accumulation, must be in time with CO
2From fuel cell system, get rid of, when anode uses liquid fuel, CO
2Be easy to get rid of with fluid separation applications, but in the battery system that uses fuel gas, fuel gas and CO
2Can't delamination and may make fuel gas along with CO
2Be discharged into outside the system together, cause waste of fuel, influence the fuel conversion efficiency of fuel cell, again, can provide the anode layer of preserving moisture to make gasification of methanol can pass the anode layer of preserving moisture to enter anode gas diffusion layer, but the aqueous vapor of same anode also can be passed preserve moisture layer and diffuse to the fuel storage groove of anode, causes the fuel concentration in the fuel storage groove diluted, and can cause the internal resistance value of membrane electrode resistance to rise, for example the WO2005/112172A1 patent application case discloses.In addition, CO can further be set
2Floss hole is in the sidewall of vaporising fuel reception room, and for example the WO2006/040961A1 patent application case discloses, and the gasification of methanol concentration of this vaporising fuel reception room is only second to the fuel storage groove, but therefore causes more gasification of methanol along with CO
2Discharge, not only pollute surrounding environment, fuel efficiency is descended.
Summary of the invention
In view of this, the invention provides a kind of fuel cell system, can reduce the loss of anode aqueous vapor, keep the internal resistance value of mea, and can discharge the formed generation gas of its anode-side effectively, reduce the loss outside the fuel gas discharge system, and then improve fuel efficiency.
According to an embodiment, fuel cell system of the present invention comprises:
Battery unit, it comprises the anode current collection layer, the negative electrode current collection layer, be folded in the mea between above-mentioned anode current collection layer and this negative electrode current collection layer, around above-mentioned mea, the framework of anode current collection layer and negative electrode current collection layer, be arranged at the hydrophilic gas barrier layer of this anode current collection layer below, be arranged at the hydrophobic breathable layer of this hydrophilic gas barrier layer below, and be embedded at least one gaseous emission raceway groove in this framework, this gaseous emission raceway groove exposes the environment of an one of this hydrophilic gas barrier layer and contiguous this battery unit of contact, with arrange logical by generation gas that this mea was produced to this battery unit.
According to another embodiment, fuel cell system of the present invention comprises:
Battery unit, fuel supply unit are to supply fuel gas to this battery unit; And the air supply unit with the supply oxygen-containing gas to this battery unit, wherein this battery unit comprises:
The anode current collection layer, the negative electrode current collection layer, be folded in the mea between above-mentioned anode current collection layer and this negative electrode current collection layer, around above-mentioned mea, the framework of anode current collection layer and negative electrode current collection layer, be arranged at the hydrophilic gas barrier layer of this anode current collection layer below, be arranged at the hydrophobic breathable layer of this hydrophilic gas barrier layer below, and be embedded at least one gaseous emission raceway groove in this framework, wherein this gaseous emission raceway groove exposes an one and the environment of contiguous this battery unit of contact of this hydrophilic gas barrier layer, with arrange logical by generation gas that this mea was produced to this battery unit, this fuel supply unit is linked to a side of this hydrophobic breathable layer in contiguous this battery unit, and this air supply unit is linked to the side away from this hydrophobic breathable layer in this battery unit.
For above-mentioned and other purposes of the present invention, feature and advantage can be become apparent, a preferred embodiment cited below particularly, and conjunction with figs. are described in detail below.
Description of drawings
Fig. 1 is a schematic diagram, has shown the cross-section illustration according to the fuel cell system of one embodiment of the invention;
Fig. 2 is a schematic diagram, has shown the cross-section illustration according to the fuel cell system of another embodiment of the present invention;
Fig. 3 is a schematic diagram, has shown the cross-section illustration according to the fuel cell system of another embodiment of the present invention; And
Fig. 4 is a schematic diagram, has shown the cross-section illustration according to the fuel cell system of another embodiment of the present invention.
Description of reference numerals
100,100 ', 100 ", 100 " ' fuel cell system 10 fuel supply units
12 cell body 12a, 12b cell body one one
14 liquid fuels, 16 liquid gas separating layers
18 bogs, 20 battery units
22 anode current collection layers, 24 anode gas diffusion layers
26 anode catalyst, 28 electrolytic thin-membranes
30 cathode catalysts layers, 32 cathode gas diffusion layer
34 negative electrode current collection layers, 36 frameworks
40 mea, 50 hydrophilic gas barrier layers
60 hydrophobic breathable layers, 65 porous plates
70,70 ' gaseous emission raceway groove, 80 air supply unit
The 82 plate 86 air introducing ports of preserving moisture
90 aqua storage tanks 92 layer that catchments
Embodiment
Please refer to the schematic diagram of Fig. 1, it has shown the section situation according to the fuel cell system 100 of one embodiment of the invention.As shown in the figure, fuel cell system 100 mainly comprises battery unit 20, fuel supply unit 10 and air supply unit 80.
As shown in Figure 1, battery unit 20 comprise anode current collection layer 22, negative electrode current collection layer 34, be folded between anode current collection layer 22 and this negative electrode current collection layer 34 mea (MEA) 40 and around the framework 36 of above-mentioned mea, anode current collection layer 22 with negative electrode current collection layer 34.In addition, battery unit 20 also comprises the hydrophilic gas barrier layer 50 that is arranged at anode current collection layer 22 belows, and the hydrophobic breathable layer 60 that is arranged at these hydrophilic gas barrier layer 50 belows.Wherein, 40 of mea comprise and pile up the anode gas diffusion layer 24 that is formed on the anode current collection layer 22, anode catalyst layer 26, electrolytic thin-membrane 28, cathode catalysts layer 30 and cathode gas diffusion layer 32 in regular turn.Moreover, then embedding in framework 36 have a gaseous emission raceway groove 70, the environment that it exposes an one of hydrophilic gas barrier layer 50 and contacts adjacent cells unit 20, it is provided with quantity, aperture and shape and does not exceed with the situation of Fig. 1, and visual actual state changes it quantity, its profile and its aperture is set.In addition, the material of the hydrophilic gas barrier layer 50 in the battery unit 20 comprises as weaving cotton cloth, adhesive-bonded fabric, stationery, bubble is continuous, hydrophilic porous material such as polyurathamc, it has the characteristic of adsorptive liquid, and after moistening, has the choke effect as the liquid of water, its aperture must be little of forming moisture film, generally speaking, aperture size at least must be less than the twice of its thickness moisture film of just having an opportunity to form, and then the carbon dioxide that can blocking anode produces penetrates, so necessary enough little or structure of non-clear opening in aperture, for example the hydrophilic gas barrier layer thickness of present embodiment use is 100 μ m, and the aperture is 0.1 μ m.The material of hydrophobic breathable layer then comprises polytetrafluoroethylene (PTFE, poly-tetrafluoroethylene) etc. heat-resisting, anti-corrosion and not with the material of fuel cell chemically reactive, must possess the above pressure that blocks water (Waterproof Pressure) of 10kPa, the product " Poreflon MembraneFP-010-60 " that the material of present embodiment hydrophobic breathable layer uses SUMITOMOELECTRIC FINE POLYMER INC. to produce, its aperture is 0.1 μ m, and has the pressure that blocks water of 220kPa.
Still please refer to Fig. 1, fuel supply unit 10 is arranged at a side of hydrophobic breathable layer 60 in the adjacent cells unit 20, using provides the anode-side of fuel gas to battery unit, and air supply unit 80 is arranged at the side away from this hydrophobic breathable layer in this battery unit, and using provides oxygen or the airborne oxygen molecule cathode side to battery unit.At this, fuel supply unit 10 comprises cell body 12, includes liquid fuel 14 and bog 18 in it, and bog 18 is formed by liquid fuel 14 direct boilings.In addition, 80 of air supply unit comprise the plate 82 of preserving moisture, and this plate 82 of preserving moisture is provided with several air introducing ports 86.
The operation of the fuel cell system 100 of Fig. 1 is then as described below, be arranged in the bog 18 through vaporization of fuel supply unit, it for example is the bog of methyl alcohol, after by hydrophobic breathable layer 60, arrive at hydrophilic gas barrier layer 50 places, because hydrophilic gas barrier layer 50 is by being formed through moistening film, for example be through water-moistened film, so aforesaid fuel gas 18 will be dissolved in the hydrophilic gas barrier layer 50 once more, and then contacted anode current collection layer 22 and anode gas diffusion layer 24 backs with liquid kenel and reacted with anode catalyst layer 26, oxygen or airborne oxygen molecule then enter via air introducing port 86 in the air supply unit 80, are reacting with cathode catalysts layer 30 by negative electrode current collection layer 34 and cathode gas diffusion layer 32 backs.Via above-mentioned reaction, fuel cell system 100 will react gives birth to, the gas that generates of anode place wherein, the carbon dioxide that is generated when for example adopting methanol fuel, then can transmit and arrive at gaseous emission raceway groove 70 places that are embedded in the framework 36 this moment along the border of 50 of anode current collection layer 22 and hydrophilic gas barrier layers, thereby be disposed in the context of fuel cell system 100, and can loss to below vaporized fuel concentration higher position, the vaporized fuel ratio of therefore discharging gas will be lower.In addition, because hydrophilic gas barrier layer 50 belows in the battery unit 20 are provided with hydrophobic breathable layer 60, therefore in case hydrophilic gas barrier layer 50 after moistening, contained humidity will be stopped by hydrophobic breathable layer 60 in it, therefore can avoid the liquid fuels 14 in the cell body 12 to be diluted.So, via aforesaid operations, fuel cell system 100 its internal resistance value after long-time operation can remain on still that (operating time is about 6 hours in the proper range, interior resistance value lifting capacity 0%), therefore fuel cell system 100 utmost points are applicable to the application of non-active fuel cell system, the for example application of non-active direct methanol fuel cell just can continue for a long time to produce electric power as long as can continue supply liquid fuel 14, and not have power breakdown or change considering of battery.
Fig. 2 and Fig. 3 are a series of schematic diagrames, shown profile according to the fuel cell system of other embodiments of the invention, fuel cell system 100 ' and 100 wherein " be resultant via improvement fuel cell system as shown in Figure 1; in Fig. 2 and member shown in Figure 3; identical label has shown the member that is same as among Fig. 1, in the difference place between descriptive system and be not repeated in this description identical components once more only hereinafter.
Please refer to Fig. 2, in the fuel system 10 in fuel cell system 100 ' gas-liquid separation film 16 is set optionally, to separate liquid fuel 14 and the bog 18 that is generated by liquid fuel 14.As shown in Figure 2, gas-liquid separation film 16 partly is embedded in the cell body 12, and cell body is divided into two partly 12a and 12b, wherein 12a partly institute be to be used to be provided with liquid fuel 14 around the zone that forms, 12b partly then be provided with bog 18 around the zone of formation.In addition, the framework 36 embedding gaseous emission raceway grooves 70 ' that another kenel is arranged in battery unit 12, it is formed at the edge of hydrophilic gas barrier layer 50 and framework 36, and the along continuous straight runs extension is arranged in the framework 36.Perhaps, between the end face of fuel cell feeding unit 10 and battery unit 20, porous plate 65 also is set optionally, with the transmission quantity of control fuel gas 18 and as the supporting construction of battery unit 20 with gas supply unit 80, it has the percent opening between 0.1～20%, discharging current according to mea decides the percent opening size, its material then comprises polyester or TPO material, for example: poly terephthalic acid second two fat (PET, polyethylene terephthalate), polypropylene cyanogen (PAN, Polyacrylonitrile), polyethylene (PE, polyethylene), polypropylene (PP, polypropylene) etc., possess airtight, anti-corrosion and not with the fuel cell chemically reactive and characteristic.
Fig. 4 is a schematic diagram, shown profile according to the fuel cell system of another embodiment of the present invention, wherein fuel cell system 100 " ' be resultant via as shown in Figure 2 fuel cell system of improvement; in member shown in Figure 4; identical label has shown the member that is same as among Fig. 2, the difference place between descriptive system and be not repeated in this description identical member once more only hereinafter.
Please refer to Fig. 4, at fuel cell system 100 " ' in aqua storage tank 90 can more be set, it is to be independent of fuel system 10 and battery unit 20.And the plate 82 of preserving moisture in air supply unit 80 can more be embedded with the layer 92 that catchments.Layer 92 the material of catchmenting is the porous hydrophilic material, for example weave cotton cloth, porous materials such as adhesive-bonded fabric, stationery, bubble silk floss, polyurathamc, and its be entity be linked to aqua storage tank 90.In addition, as shown in Figure 4, the side that this hydrophilic gas barrier layer 50 protrudes in framework 36 is embedded in the aqua storage tank 90 outward and partly.Via setting like this, can adopt artificial supply mode to add the water of appropriate amount at aqua storage tank 90, or be condensed in its inboard aqueous vapor and flow in the aqua storage tank 90 replenishing, and moisture is supplemented to is arranged at hydrophobic breathable layer 60 and partly locates with the hydrophilic gas barrier layer 50 of 40 of mea by partly being embedded in hydrophilic gas barrier layer 50 in the aqua storage tank 90 by being arranged at layer 92 absorption of catchmenting in the plate 82 of preserving moisture.So, can avoid the backwater amount to be subjected to environmental influence and cause the situation of hydrophilic gas barrier layer 50 lacks of water to take place, and then promote its operating time and performance.Above-mentioned water charging system can be performed in as in Fig. 1 and the fuel cell system shown in Figure 3 and limited its invention with the execution mode of Fig. 4.
Though the present invention discloses as above with preferred embodiment; right its is not in order to qualification the present invention, those skilled in the art, without departing from the spirit and scope of the present invention; when can being used for a variety of modifications and variations, so protection scope of the present invention is when looking being as the criterion that accompanying Claim defines.
Claims (31)
1. fuel cell system comprises:
Battery unit comprises:
The anode current collection layer;
The negative electrode current collection layer;
Mea is folded between this anode current collection layer and this negative electrode current collection layer;
Framework is around this mea, this anode current collection layer and this negative electrode current collection layer;
Hydrophilic gas barrier layer is arranged at the below of this mea and this framework;
Hydrophobic breathable layer is arranged at the below of this hydrophilic gas barrier layer; And
At least one gaseous emission raceway groove is embedded in this framework, exposes the environment of an one of this hydrophilic gas barrier layer and contiguous this battery unit of contact, with arrange logical by generation gas that this mea was produced to this battery unit.
2. fuel cell system as claimed in claim 1 also comprises fuel supply unit, is linked to a side of this hydrophobic breathable layer in contiguous this battery unit.
3. fuel cell system as claimed in claim 1 also comprises the air supply unit, is linked to the side away from this hydrophobic breathable layer in this battery unit.
4. fuel cell system as claimed in claim 1, wherein this mea comprises anode gas diffusion layer, anode catalyst layer, electrolytic thin-membrane, cathode catalysts layer and the cathode gas diffusion layer that piles up formation in regular turn.
5. fuel cell system as claimed in claim 2, wherein this fuel supply unit comprises the bog of liquid fuel and this liquid fuel.
6. fuel cell system as claimed in claim 5, wherein this bog is to be formed by this liquid fuel direct boiling.
7. fuel cell system as claimed in claim 1, wherein this hydrophilic gas barrier layer is a wetting film, passes through this hydrophilic gas barrier layer to block the generation gas that is produced by this mea.
8. fuel cell system as claimed in claim 7, wherein the material of this hydrophilic gas barrier layer comprise as weave cotton cloth, hydrophilic porous material such as adhesive-bonded fabric, stationery, bubble silk floss, polyurathamc.
9. fuel cell system as claimed in claim 7, wherein the aperture of this hydrophilic gas barrier layer must be less than the twice of thickness.
10. fuel cell system as claimed in claim 6, wherein this hydrophobic breathable layer stops that moisture in this battery unit leaves this battery unit and controlled the speed that this bog feeds this battery unit.
11. fuel cell system as claimed in claim 10, wherein the material of this hydrophobic breathable layer comprises polytetrafluoroethylene.
12. fuel cell system as claimed in claim 11, wherein this hydrophobic breathable layer has the above pressure that blocks water of 10kPa.
13. fuel cell system as claimed in claim 5 also comprises the gas-liquid separation film, is arranged in this fuel supply unit, to separate this bog that this liquid fuel and this liquid fuel is generated.
14. fuel cell system as claimed in claim 2 also comprises porous plate, is arranged between the end face and this battery unit of this fuel supply unit.
15. fuel cell system as claimed in claim 14, wherein this porous plate has the percent opening between 0.1～20%.
16. a fuel cell system comprises:
Battery unit comprises:
The anode current collection layer;
The negative electrode current collection layer;
Mea is folded between this anode current collection layer and this negative electrode current collection layer;
Framework is around this mea, this anode current collection layer and this negative electrode current collection layer;
Hydrophilic gas barrier layer is arranged at the below of this mea and this framework;
Hydrophobic breathable layer is arranged at the below of this hydrophilic gas barrier layer; And
At least one gaseous emission raceway groove is embedded in this framework, exposes the environment of an one of this hydrophilic gas barrier layer and contiguous this battery unit of contact, with arrange logical by generation gas that this mea was produced to this battery unit;
Fuel supply unit is linked to a side of being close to this hydrophobic breathable layer in this battery unit, to supply fuel gas to this battery unit; And
The air supply unit is linked to the side away from this hydrophobic breathable layer in this battery unit, to supply oxygen-containing gas to this battery unit.
17. fuel cell system as claimed in claim 16, wherein this mea comprises anode gas diffusion layer, anode catalyst layer, electrolytic thin-membrane, cathode catalysts layer and the cathode gas diffusion layer that piles up formation in regular turn.
18. fuel cell system as claimed in claim 16, wherein this fuel supply unit comprises the bog of liquid fuel and this liquid fuel.
19. fuel cell system as claimed in claim 18, wherein this bog is to be formed by this liquid fuel direct boiling.
20. fuel cell system as claimed in claim 16, wherein this hydrophilic gas barrier layer is a wetting film, passes through this hydrophilic gas barrier layer to block the generation gas that is produced by this mea.
21. fuel cell system as claimed in claim 20, wherein the material of this hydrophilic gas barrier layer comprise as weave cotton cloth, hydrophilic porous material such as adhesive-bonded fabric, stationery, bubble silk floss, polyurathamc.
22. fuel cell system as claimed in claim 20, wherein the aperture of this hydrophilic gas barrier layer must be less than the twice of thickness.
23. fuel cell system as claimed in claim 16, wherein this hydrophobic breathable layer stops that moisture in this battery unit leaves this battery unit and controlled the speed that this bog feeds this battery unit.
24. fuel cell system as claimed in claim 23, wherein the material of this hydrophobic breathable layer comprises polytetrafluoroethylene.
25. fuel cell system as claimed in claim 16, wherein this hydrophobic breathable layer has the above pressure that blocks water of 10kPa.
26. fuel cell system as claimed in claim 16 also comprises the gas-liquid separation film, is arranged in this fuel supply unit, to separate this bog that this liquid fuel and this liquid fuel is generated.
27. fuel cell system as claimed in claim 16 also comprises porous plate, is arranged between the end face and this battery unit of this fuel supply unit.
28. fuel cell system as claimed in claim 27, wherein this porous plate has the percent opening between 0.1～20%.
29. fuel cell system as claimed in claim 27, wherein the material of this porous plate comprises polyester or TPO material, for example: poly terephthalic acid second two fat, polypropylene cyanogen, polyethylene, polypropylene etc.
30. fuel cell system as claimed in claim 27 also comprises aqua storage tank, is used to store water, and this hydrophilic gas barrier layer protrudes in a side of this framework and partly is embedded in this aqua storage tank.
31. fuel cell system as claimed in claim 30 also comprises the layer that catchments, be arranged in this air supply unit, this layer and being linked in this aqua storage tank of catchmenting, with supply condensate gas to this aqua storage tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2007101018591A CN101295796B (en) | 2007-04-25 | 2007-04-25 | Fuel cell system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2007101018591A CN101295796B (en) | 2007-04-25 | 2007-04-25 | Fuel cell system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101295796A true CN101295796A (en) | 2008-10-29 |
| CN101295796B CN101295796B (en) | 2011-06-15 |
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ID=40065915
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2007101018591A Active CN101295796B (en) | 2007-04-25 | 2007-04-25 | Fuel cell system |
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| Country | Link |
|---|---|
| CN (1) | CN101295796B (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101771162A (en) * | 2008-12-30 | 2010-07-07 | 财团法人工业技术研究院 | Flat fuel cell assembly |
| CN102569847A (en) * | 2010-12-16 | 2012-07-11 | 财团法人工业技术研究院 | Fuel distribution structure and fuel cell |
| US9153829B2 (en) | 2008-12-22 | 2015-10-06 | Industrial Technology Research Institute | Passive fuel cell assembly |
| CN105470545A (en) * | 2016-01-12 | 2016-04-06 | 山东联星能源集团有限公司 | Methanol fuel cell |
| CN106505235A (en) * | 2016-11-14 | 2017-03-15 | 中国科学院上海高等研究院 | Anode moisture retention structure and the passive direct methanol fuel cell using which |
| CN109148920A (en) * | 2017-06-28 | 2019-01-04 | 中国科学院苏州纳米技术与纳米仿生研究所 | Fuel cell and preparation method thereof |
| CN111240376A (en) * | 2018-11-29 | 2020-06-05 | 中国科学院大连化学物理研究所 | Passive air pressure adjusting device |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8211592B2 (en) * | 2005-09-15 | 2012-07-03 | GM Global Technology Operations LLC | Hydrophilic layer on flowfield for water management in PEM fuel cell |
-
2007
- 2007-04-25 CN CN2007101018591A patent/CN101295796B/en active Active
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9153829B2 (en) | 2008-12-22 | 2015-10-06 | Industrial Technology Research Institute | Passive fuel cell assembly |
| CN101771162A (en) * | 2008-12-30 | 2010-07-07 | 财团法人工业技术研究院 | Flat fuel cell assembly |
| CN101771162B (en) * | 2008-12-30 | 2016-01-20 | 财团法人工业技术研究院 | Flat fuel cell group |
| CN102569847A (en) * | 2010-12-16 | 2012-07-11 | 财团法人工业技术研究院 | Fuel distribution structure and fuel cell |
| CN102569847B (en) * | 2010-12-16 | 2014-07-02 | 财团法人工业技术研究院 | Fuel distribution structure and fuel cell |
| CN105470545A (en) * | 2016-01-12 | 2016-04-06 | 山东联星能源集团有限公司 | Methanol fuel cell |
| CN105470545B (en) * | 2016-01-12 | 2018-05-04 | 山东联星能源集团有限公司 | A kind of methanol fuel cell |
| CN106505235A (en) * | 2016-11-14 | 2017-03-15 | 中国科学院上海高等研究院 | Anode moisture retention structure and the passive direct methanol fuel cell using which |
| CN109148920A (en) * | 2017-06-28 | 2019-01-04 | 中国科学院苏州纳米技术与纳米仿生研究所 | Fuel cell and preparation method thereof |
| CN111240376A (en) * | 2018-11-29 | 2020-06-05 | 中国科学院大连化学物理研究所 | Passive air pressure adjusting device |
| CN111240376B (en) * | 2018-11-29 | 2021-06-01 | 中国科学院大连化学物理研究所 | Passive air pressure adjusting device |
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| Publication number | Publication date |
|---|---|
| CN101295796B (en) | 2011-06-15 |
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