CN1601796A - Structure of flow field board for proton exchange film fuel cell - Google Patents
Structure of flow field board for proton exchange film fuel cell Download PDFInfo
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- CN1601796A CN1601796A CNA2004100674706A CN200410067470A CN1601796A CN 1601796 A CN1601796 A CN 1601796A CN A2004100674706 A CNA2004100674706 A CN A2004100674706A CN 200410067470 A CN200410067470 A CN 200410067470A CN 1601796 A CN1601796 A CN 1601796A
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- 239000000446 fuel Substances 0.000 title claims description 39
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 96
- 239000001257 hydrogen Substances 0.000 claims abstract description 93
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 93
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 239000012528 membrane Substances 0.000 claims description 16
- 239000007789 gas Substances 0.000 claims description 12
- 239000000463 material Substances 0.000 abstract description 5
- 229910021382 natural graphite Inorganic materials 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 10
- 239000001301 oxygen Substances 0.000 description 10
- 229910052760 oxygen Inorganic materials 0.000 description 10
- 239000003054 catalyst Substances 0.000 description 5
- 238000003411 electrode reaction Methods 0.000 description 5
- 239000003792 electrolyte Substances 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 230000009471 action Effects 0.000 description 4
- 239000002131 composite material Substances 0.000 description 4
- 238000013461 design Methods 0.000 description 4
- -1 hydrogen ions Chemical class 0.000 description 4
- 229910002804 graphite Inorganic materials 0.000 description 3
- 239000010439 graphite Substances 0.000 description 3
- 150000002431 hydrogen Chemical class 0.000 description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- QXYJCZRRLLQGCR-UHFFFAOYSA-N dioxomolybdenum Chemical compound O=[Mo]=O QXYJCZRRLLQGCR-UHFFFAOYSA-N 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000007800 oxidant agent Substances 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 239000002861 polymer material Substances 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000012827 research and development Methods 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 241000282412 Homo Species 0.000 description 1
- 229910002848 Pt–Ru Inorganic materials 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 210000000476 body water Anatomy 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000002860 competitive effect Effects 0.000 description 1
- 238000000748 compression moulding Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000007723 die pressing method Methods 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000010411 electrocatalyst Substances 0.000 description 1
- 238000003487 electrochemical reaction Methods 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- UQSQSQZYBQSBJZ-UHFFFAOYSA-N fluorosulfonic acid Chemical group OS(F)(=O)=O UQSQSQZYBQSBJZ-UHFFFAOYSA-N 0.000 description 1
- 239000003502 gasoline Substances 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 239000012495 reaction gas Substances 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Images
Classifications
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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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- Fuel Cell (AREA)
Abstract
Body of flow field board is made from material composed of processed natural graphite and high molecular material, and mold pressed at one time under high temp. There are hydrogen inlet, hydrogen outlet, air inlet and air outlet, circulating trough for water, water inlet and outlet, and diversion groove of connecting to air inlet and air outlet in flow field board. In the disclosed flow field board, there is each pair of air inlets and outlets, and hydrogen inlets and outlets in threadlike rectangle. Diversion groove for connecting to a pair of inlet and outlet is in streamline type parallel mode distribution structure in flow field. Width of groove is 1.0-3.5mm, depth is 0.3-0.6mm, and width of ridge is 1.0-5.0 mm. Features are: even air flow distribution, unobstructed for air flow, high use ratio of cross section, and steady operation.
Description
Technical Field
The invention relates to a fuel cell technology, in particular to a structure of a flow field plate for a proton exchange membrane fuel cell.
Background
Today, the rapid development of human society, such as traditional energy sources like coal, oil, natural gas, etc., has become increasingly unable to meet the needs of industrial society that has progressed through the twenty-first century. Energy resources on which humans live are being consumed in the last decades, and the serious environmental pollution caused by these traditional energy resources has become an obstacle to the survival and development of human society. In view of this, countries in the world have no obvious and full search for future alternative energy sources, so that the future alternative energy sources can comprehensively replace the current traditional energy sources; until now, the scientific community consistently considers that hydrogen energy is one of effective clean energy for replacing power energy such as gasoline, diesel oil and the like in twenty-first century; a proton exchange membrane FUEL CELL (FUEL CELL) is a device that directly converts chemical energy of hydrogen and oxygen into electrical energy through electrode reaction; because the battery has no combustion reaction, the battery is widely advocated by the scientific community and promoted to market.
There are five types of fuel cells developed at present, namely alkaline fuel cells, phosphoric acid fuel cells, solid oxide fuel cells, molten carbonate fuel cells and proton exchange membrane fuel cells, and proton exchange membrane fuel cells are one of the most competitive energy projects. The main working principle of the proton exchange membrane fuel cell is as follows: the proton exchange membrane fuel cell mainly utilizes hydrogen and oxygen to generate water through electrochemical reaction and release electric energy, can be regarded as a reverse device of water electrolysis, and mainly comprises four conductive structures of an anode, a cathode, an electrolyte and an external circuit.
(1) Introducing hydrogen gas into the anode;
(2) under the action of an anode catalyst, carrying out an anodic oxidation reaction, wherein the electrode reaction equation is as follows:
(3) at the other end of the cell, oxygen (or air) is introduced into the cathode;
(4) the hydrogen ions at the anode pass through the electrolyte to the cathode, and the electrons at the anode also pass through an external circuit to the cathode;
(5) the hydrogen ions and the oxygen undergo a cathode reduction reaction under the action of a cathode catalyst to generate water, and the electrode reaction formula is as follows:
the Proton Exchange Membrane Fuel Cell (PEMFC) takes a perfluorosulfonic acid proton exchange membrane as an electrolyte, Pt/C, Pt-Ru/C or nano molybdenum dioxide as an electrocatalyst, hydrogen or purified reformed gas as a fuel, air or pure oxygen as an oxidant, and a high-purity graphite plate with a gas flow channel, a high-molecular composite material graphite plate or a surface-modified corrosion-resistant metal plate as a bipolar plate. The electrode reactions in PEMFCs are analogous to other acid electrolyte fuel cells. The hydrogen in the anode catalyst layer is subjected to electrode reaction under the action of the catalyst to generate electrons which reach the cathode through an external circuit, and hydrogen ions reach the cathode through the proton exchange membrane. The oxygen, the hydrogen ions and the electrons react under the action of the cathode catalyst to generate water, and the generated water does not dilute the electrolyte but is discharged along with reaction tail gas through the electrode.
Proton Exchange Membrane Fuel Cells (PEMFC) are considered to be the best candidate power source for future electric automobiles and submarines, and have wide application prospects in the aspects of mobile power sources, household power stations, underwater robots, aerospace vehicles and the like. PEMFC technology is becoming more mature, and bipolar plates (bipolar plates) are one of the major factors affecting its cost. The bipolar plate has its unique role: firstly, separating the oxidant and the reducing agent; secondly, the function of collecting current is completed; flow fields for uniformly distributing reaction gases are arranged on two sides of the bipolar plate; fourthly, the temperature of the cell stack is ensured to be uniformly distributed, and a good heat dissipation effect is achieved. The cost of PEMFCs is even 60-70%. Therefore, in recent years, different types of bipolar plates have been researched and developed in various countries around the world, and the molded polymer composite bipolar plate is a hot point of research and development. At present, the technology has many technical difficulties to be studied deeply, including the flow field structure of the bipolar plate in the battery stack, different polymer material formulas, processing technology, product cost and the like. The present invention is designed to solve the above problems of the flow field structure of the bipolar plate.
At present, a great deal of research and development work is carried out on bipolar plate materials and flow field design in the United states, Canada, Germany, Japan and China, and great progress is made in the aspect of marketization promotion. Such as: bipolar plate patents of fuel cells (patent numbers 01124227.0 and 01124228.0) applied by the athetian fuel cell science and technology corporation of taiwan; united states united signal company applies for (patent number: 00814108.8) fuel cells and bipolar plate patents for fuel cells in our country. However, these patents have more or less disadvantages: for example, the gas flow distribution of the bipolar plate is not sufficiently uniform; the water generated by the reaction is easy to accumulate and is difficult to discharge, the flow field structure design is easy to cause reaction dead zones, the voltage is unstable and the like, which influence the normal operation performance of the battery.
Disclosure of Invention
The invention aims to overcome the defects in the prior art, and provides a flow field plate structure for a proton exchange membrane fuel cell, which has the characteristics of smooth air guide, uniform air flow distribution, high space utilization rate, improvement on the energy utilization rate of reaction gas and the like; the flow field plate structure is also used for preventing the flow guide groove from being blocked in the reaction process, so that the operation stability of the fuel cell is improved.
The invention can be implemented by the following technical scheme: a structure of flow field plate of proton exchange membrane fuel cell, wherein, the flow field plate body is formed by the material that the natural high-purity graphite and macromolecular material that is processed are compounded and are formed by high-temperature one-time die pressing; the flow fieldplate comprises a hydrogen inlet, a hydrogen outlet, an air inlet, an air outlet, a water circulation groove, a water inlet, a water outlet, a flow guide groove communicated with the gas inlet and the gas outlet, and the like; the flow field plate is provided with a pair of air inlet and outlet and a pair of hydrogen inlet and outlet, which are in a slender rectangle, and the flow guide grooves communicated with the pair of inlet and outlet adopt a streamline parallel flow field distribution structure.
The flow field plate body is a hydrogen guiding flow field plate or an air guiding flow field plate or a flow field plate with one surface used for guiding hydrogen and the other surface used for guiding air; the flow field plate for guiding hydrogen is provided with a pair of hydrogen inlet and hydrogen outlet which are positioned at the same side of the flow field plate (namely, positioned at the same edge of the flow field plate), as shown in fig. 3 and 4, and the flow field plate for guiding air is provided with a pair of air inlet and air outlet which are positioned at the same side of the flow field plate (namely, positioned at the same edge of the flow field plate), as shown in fig. 5 and 6; the flow guide grooves communicated with the air inlets and the air outlets adopt a flow field plate distribution structure which is in a streamline parallel type and is processed by a curved surface type at a right-angle turning point.
The hydrogen inlet and the hydrogen outlet of the hydrogen guiding flow field plate are equal in size and shape, are in a slender rectangle and have the width of 2-5 mm; the size and the shape of an air inlet and an air outlet of the air-guiding flow field plate are equal, the flow field plate is in a slender rectangle shape, and the width of the flow field plate is 4-10 mm; the length of an air inlet of the air guide flow field plate is basically equal to that of a hydrogen inlet, the length of an air outlet is basically equal to that of a hydrogen outlet, and the length of the air outlet is 30-38 mm; the actual use width of the air inlet of the flow field plate is twice that of the hydrogen inlet; the actual use width of the air outlet of the flow field plate is twice as wide as that of the hydrogen outlet.
The flow field plate for guiding hydrogen is provided with a pair of hydrogen inlet and outlet ports, wherein the hydrogen inlet port is divided into a plurality of hydrogen guiding flow grooves, the plurality of hydrogen guiding flow grooves adopt a flow field plate distribution structure which is in a streamline parallel type, has a plurality of right-angle turning points and is processed in a curved type, and finally converge at the hydrogen outlet port, and the total length of each hydrogen guiding flow groove from the hydrogen inlet port to the hydrogen outlet port is basically equal; the air guiding flow field plate is provided with a pair of air inlet and air outlet ports, wherein the air inlet port is divided into a plurality of air guiding flow grooves, the air guiding flow grooves adopt a flow field plate distribution structure which is in a streamline parallel type, has a plurality of right-angle turning points and is processed in a curved type, and finally are collected at the air outlet port of the air, and the total length from the air inlet port to the air outlet port of each air guiding flow groove is basically equal.
The hydrogen inlet of the hydrogen flow field plate is divided into a plurality of hydrogen flow guiding grooves in claim 4, and is also divided into two hydrogen flow guiding grooves, the total length of the two hydrogen flow guiding grooves is four fifths of the total length of the hydrogen flow guiding grooves in claim 4, the number of the right-angle turning flows is less than that of the right-angle turning flows of the hydrogen flow guiding grooves in claim 4, the two hydrogen flow guiding grooves arerespectively positioned at two sides of the hydrogen inlet and are finally connected to the hydrogen outlet; the air inlet of the air-guiding flow field plate is divided into a plurality of air-guiding grooves in claim 4, and is also divided into two air-guiding grooves, the total length of the two air-guiding grooves is four fifths of the total length of the air-guiding grooves in claim 4, the number of the right-angle bends is less than that of the right-angle bends of the air-guiding grooves in claim 4, the two air-guiding grooves are respectively positioned at two sides of the air inlet and are finally connected with an air outlet, and the air-guiding grooves are used for preventing the battery from generating a 'dead halt' phenomenon when the long-range grooves are blocked in the reaction process.
The width of the air flow guiding groove communicated with the air inlet and the air outlet of the air guiding flow field plate is larger than that of the hydrogen flow guiding groove communicated with the hydrogen inlet and the hydrogen outlet of the hydrogen guiding flow field plate.
The width of the groove is 1.0-3.5 mm, the depth is 0.3-0.6 mm, and the width of the stem strip is 1.0-5.0 mm.
The width 1 of the groove for guiding the hydrogen flow is smaller than the width of the stalk strip 2 on the flow field plate for guiding the hydrogen flow; the width 1 of the air flow guiding groove is smaller than the width 2 of the stalk strip on the air flow guiding plate.
The number of the hydrogen flow guiding grooves is 5-10; the number of the air guiding flow grooves is 5-10.
Compared with the prior art, the invention has the characteristics that: the inlet and outlet of the gas on the flow field plate are in an elongated rectangular shape instead of a common semicircular shape or a quarter-circular shape; the length of the air inlet and outlet is the same as that of the hydrogen inlet and outlet, and the width of the air inlet and outlet is larger than that of the hydrogen inlet and outlet. Namely: the total area of the hydrogen inlet and outlet is half of the total area of the air inlet and outlet. As shown in fig. two and three, 3 and 4 in fig. two are respectively an inlet and an outlet of hydrogen, and 5 and 6 in fig. two are respectively an inlet and an outlet of air. The inlet and outlet of fluid on the flow field plate are positioned on the same side of the flow field plate, so that the overall distribution of the grooves for connecting the fluid inlet and outlet is different from the conventional distribution. The width of the air guiding flow groove communicated with the air inlet and the air outlet of the air guiding flow field plate is larger than that of the hydrogen guiding flow groove communicated with the hydrogen inlet and the hydrogen outlet of the hydrogen guiding flow field plate. The inlets of the hydrogen guide flow and the air guide flow of the flow field plate are divided into two edge guide grooves 7 and 8 respectively besides a plurality of guide grooves, and are finally connected with the outlets of the flow field. 7. The length of 8 two diversion grooves is four fifths of the total length of the diversion groove body 9, and the number of the right-angle turns is less than that of the diversion groove body.
The advantages of the design of the air inlet and outlet and the flow guide groove of the flow field plate of the proton exchange membrane fuel cell are as follows: the flow guide opening of the same flow field plate is formed by a slender rectangle, so that a large-area flow guide opening is avoided, and the effective utilization area of the flow field plate body is increased; the area of the air inlet of the air is larger than that of the hydrogen, and meanwhile, the flow guide groove of the air is wider than that of the hydrogen, so that the ventilation volume of the air in the reaction is larger than that of the hydrogen due to the design structure, the concentration of cheap reactant (air) is increased, and the reaction rate of the system can be accelerated; the distribution characteristics of the grooves on the same side of the inlet and the outlet and for connecting the inlet and the outlet enable the reaction path of the gas to be longer than that of a common plate, and therefore the utilization rate of the energy gas is improved. In addition, this utility model can prevent effectively that the water blocking water conservancy diversion recess that reaction generated from causing the condition of whole reaction interrupt to take place through the hydrophobic nature processing to flow field plate surface.
Description of the drawings:
FIG. 1 is a schematic structural view of a cross section of a composite bipolar plate according to the present invention
FIG. 2 is a schematic structural view of a hydrogen-conducting flow field plate of a fuel cell
FIG. 3 is a schematic structural view of an air or oxygen flow field plate for a fuel cell
Wherein: in the attached drawings, the number 1 is a flow field plate groove section, the number 2 is a flow field plate stem section, the number 3 is a hydrogen guiding flow field plate air inlet, the number 4 is a hydrogen guiding flow field plate air outlet, the number 5 is an air guiding or oxygen flow field plate air inlet, the number 6 is an air guiding or oxygen flow field plate air outlet, the numbers 7 and 8 are two edge flow guiding grooves, and the number 9 is a body flow guiding groove.
The specific implementation modeis as follows:
the present invention will be described in detail below by way of specific embodiments with reference to the accompanying drawings.
Examples
Mixing natural high-purity graphite powder, a high polymer material, an auxiliary agent and the like according to a certain proportion, putting the mixture into a mold, putting the mold into a flat vulcanizing machine, and carrying out one-step compression molding at 10-100 MPa and 100-300 ℃ to form a composite bipolar plate product containing a flow field.
A flow field plate structure for proton exchange membrane fuel cell includes a flow field plate body. The flow field plate body is a flow guide bipolar plate, one surface of the flow field plate body is a hydrogen guide flow field plate, and the other surface of the flow field plate body is an air guide flow field plate; fig. two shows the hydrogen conducting gas flow field plate. It is provided with a pair of flow guide ports 3 and 4 for hydrogen to enter and exit, and the flow guide ports are distributed on the same side of the flow field plate. The hydrogen inlet and the hydrogen outlet are equal in size and shape, are in a slender rectangle, and are 3mm in width and 33mm in length; there are 8 water conservancy diversion recesses, and its width is 1.5mm, and the degree of depth is 0.5mm, and two marginal water conservancy diversion recesses 7, 8 are shorter than body water conservancy diversion recess 9, and the length of 7, 8 two water conservancy diversion recesses is four fifths of the total length of water conservancy diversion body recess, and the number of right angle turn is less than the number of right angle turn of water conservancy diversion recess body. The width of the stem strips is 3 mm.
Fig. three shows the described air or oxygen flow field plate. It is provided with a pair of flow guide ports 5 and 6 for air or oxygen to enter and exit, and the flow guide ports are distributed on the same side of the flow field plate. The air inlet and the air outlet are equal in size and shape, are in a slender rectangle, and are 6mm in width and 32mm in length; the width of the 7 flow guide grooves is 2.0mm, the depth of the 7 flow guide grooves is 0.5mm, the two edge flow guide grooves 7 and 8 are shorter than the body flow guide groove 9, the lengths of the 7 flow guide grooves and the 8 flow guide grooves are four fifths of the total length of the flow guide body grooves, and the number of the right-angle turns is less than that of the flow guide groove bodies. The width of the main stem strip is 3mm, and the width of the rest 6 stem strips is 4 mm.
Claims (9)
1. A structure of flow field plate for proton exchange membrane fuel cell, including hydrogen inlet, hydrogen outlet, air inlet, air outlet, circulation groove and water inlet and outlet, diversion trench communicating gas inlet and outlet on the flow field plate; the flow field plate is characterized in that a pair of air inlets and air outlets for air and hydrogen are respectively arranged on the flow field plate and are in a slender rectangle shape, and a streamline parallel flow field distribution structure is adopted by a flow guide groove for communicating the pair of air inlets and air outlets.
2. The structure of a flow field plate of a fuel cell according to claim 1, wherein the flow field plate body is a hydrogen-conducting flow field plate or an air-conducting flow field plate or a flow field plate with one surface for conducting hydrogen and the other surface for conducting air; the flow field plate for guiding hydrogen is provided with a pair of hydrogen inlet and hydrogen outlet which are positioned at the same side of the flow field plate, and the flow field plate for guiding air is provided with a pair of air inlet and air outlet which are positioned at the same side of the flow field plate; the flow guide grooves communicated with the air inlets and the air outlets adopt a flow field plate distribution structure which is in a streamline parallel type and is processed by a curved surface type at a right-angle turning point.
3. The structure of the flow field plate of the fuel cell according to claim 2, wherein the hydrogen inlet and the hydrogen outlet of the flow field plate for guiding hydrogen are equal in size and shape, are in a slender rectangle shape, and have a width of 2-5 mm; the size and the shape of an air inlet and an air outlet of the air-guiding flow field plate are equal, the flow field plate is in a slender rectangle shape, and the width of the flow field plate is 4-10 mm; the length of an air inlet of the air guide flow field plate is basically equal to that of a hydrogen inlet, the length of an air outlet is basically equal to that of a hydrogen outlet, and the length of the air outlet is 30-38 mm; the actual use width of the air inlet of the flow field plate is twice that of the hydrogen inlet; the actual use width of the air outlet of the flow field plate is twice as wide as that of the hydrogen outlet.
4. The structure of a flow field plate for a fuel cell according to claim 3, wherein the flow field plate for guiding hydrogen gas is provided with a pair of hydrogen gas inlet and outlet ports, wherein the hydrogen gas inlet port is divided into a plurality of hydrogen gas flow grooves, the plurality of hydrogen gas flow grooves adopt a flow field plate distribution structure which is in a streamline parallel type, has a plurality of right-angle turning points and is processed in a curved type, and finally converge at the hydrogen gas outlet port, and the total length of the plurality of hydrogen gas flow grooves from the hydrogen gas inlet port to the hydrogen gas outlet port is substantially equal; the air guiding flow field plate is provided with a pair of air inlet and air outlet ports, wherein the air inlet port is divided into a plurality of air guiding flow grooves, the air guiding flow grooves adopt a flow field plate distribution structure which is in a streamline parallel type, has a plurality of right-angle turning points and is processed in a curved type, and finally are collected at the air outlet port of the air, and the total length from the air inlet port to the air outlet port of each air guiding flow groove is basically equal.
5. The structure of a flow field plate for a fuel cell according to claim 3, wherein the hydrogen inlet of the hydrogen-guiding flow field plate is divided into two hydrogen-guiding flow grooves, which have a total length of four fifths of the total length of the hydrogen-guiding flow grooves in claim 4 and a smaller number of right-angled turns than the number of right-angled turns of the hydrogen-guiding flow grooves in claim 4, in addition to the plurality of hydrogen-guiding flow grooves in claim 4, and the two hydrogen-guiding flow grooves are respectively located at two sides of the hydrogen inlet and finally connected to the hydrogen outlet; the air inlet of the air-guiding flow field plate is divided into a plurality of air-guiding grooves in claim 4, and is also divided into two air-guiding grooves, the total length of the two air-guiding grooves is four fifths of the total length of the air-guiding grooves in claim 4, the number of the right-angle bends of the two air-guiding grooves is less than that of the right-angle bends of the air-guiding grooves in claim 4, the two air-guiding grooves are respectively positioned at two sides of the air inlet and are finally connected with the air outlet.
6. A structure of a flow field plate for a fuel cell according to claim 4 or 5, wherein a width of the air flow guiding groove communicating with the air inlet and outlet of the air flow field plate is larger than a width of the hydrogen flow guiding groove communicating with the hydrogen inlet and outlet of the hydrogen flow field plate.
7. The flow field plate structure of the fuel cell according to claim 4, 5 or 6, wherein the width of the groove is 1.0-3.5 mm, the depth is 0.3-0.6 mm, and the width of the stem strip is 1.0-5.0 mm.
8. A flow field plate structure for a fuel cell according to claims 4, 5, 6 and 7, wherein the grooves of the hydrogen-guiding flow field plate have a width smaller than the width of the stalk strips on the hydrogen-guiding flow field plate; the width of the air flow guiding groove is smaller than that of the stem strip on the air flow guiding plate.
9. The flow field plate structure of a fuel cell according to claim 6, 7 or 8, wherein the number of the hydrogen flow guiding grooves is 5-10; the number of the air guiding flow grooves is 5-10.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100674706A CN1300883C (en) | 2004-10-22 | 2004-10-22 | Structure of flow field board for proton exchange film fuel cell |
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| Application Number | Priority Date | Filing Date | Title |
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| CNB2004100674706A CN1300883C (en) | 2004-10-22 | 2004-10-22 | Structure of flow field board for proton exchange film fuel cell |
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| CN1601796A true CN1601796A (en) | 2005-03-30 |
| CN1300883C CN1300883C (en) | 2007-02-14 |
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| CNB2004100674706A Expired - Fee Related CN1300883C (en) | 2004-10-22 | 2004-10-22 | Structure of flow field board for proton exchange film fuel cell |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100442582C (en) * | 2005-04-12 | 2008-12-10 | 浙江大学 | Structure of double-swallow-tail shape flow field plate for proton exchange membrane fuel cell |
| CN101483244B (en) * | 2008-01-10 | 2011-09-28 | 株式会社神户制钢所 | Method for regenerating separator for fuel cell, regenerated separator for fuel cell, and fuel cell |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1121075C (en) * | 1998-07-22 | 2003-09-10 | 大连新源动力股份有限公司 | Double electrode plate of proton exchange film fuel cell |
| CN1198352C (en) * | 2001-04-13 | 2005-04-20 | 上海神力科技有限公司 | Fuel battery with higher output power |
| CN2643491Y (en) * | 2003-07-14 | 2004-09-22 | 亚太燃料电池科技股份有限公司 | Flow field structure for fuel cell |
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2004
- 2004-10-22 CN CNB2004100674706A patent/CN1300883C/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100442582C (en) * | 2005-04-12 | 2008-12-10 | 浙江大学 | Structure of double-swallow-tail shape flow field plate for proton exchange membrane fuel cell |
| CN101483244B (en) * | 2008-01-10 | 2011-09-28 | 株式会社神户制钢所 | Method for regenerating separator for fuel cell, regenerated separator for fuel cell, and fuel cell |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1300883C (en) | 2007-02-14 |
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