CN105336967B - A fuel cell bipolar plate structure - Google Patents
A fuel cell bipolar plate structure Download PDFInfo
- Publication number
- CN105336967B CN105336967B CN201510820686.3A CN201510820686A CN105336967B CN 105336967 B CN105336967 B CN 105336967B CN 201510820686 A CN201510820686 A CN 201510820686A CN 105336967 B CN105336967 B CN 105336967B
- Authority
- CN
- China
- Prior art keywords
- water conservancy
- conservancy diversion
- reducing agent
- oxidant
- runner
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 239000000446 fuel Substances 0.000 title claims abstract description 35
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 297
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 230
- 239000007800 oxidant agent Substances 0.000 claims abstract description 210
- 230000001590 oxidative effect Effects 0.000 claims abstract description 205
- 239000002826 coolant Substances 0.000 claims abstract description 86
- 238000006243 chemical reaction Methods 0.000 claims description 34
- 239000003795 chemical substances by application Substances 0.000 claims description 32
- 230000008676 import Effects 0.000 claims description 24
- 239000003963 antioxidant agent Substances 0.000 claims description 15
- 230000003078 antioxidant effect Effects 0.000 claims description 15
- 235000006708 antioxidants Nutrition 0.000 claims description 15
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 13
- 239000001301 oxygen Substances 0.000 claims description 13
- 229910052760 oxygen Inorganic materials 0.000 claims description 13
- 239000012528 membrane Substances 0.000 claims description 9
- 239000000203 mixture Substances 0.000 claims description 4
- 230000003647 oxidation Effects 0.000 claims description 4
- 238000007254 oxidation reaction Methods 0.000 claims description 4
- 230000009467 reduction Effects 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 2
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 239000000758 substrate Substances 0.000 abstract description 3
- 239000002184 metal Substances 0.000 description 7
- 239000000306 component Substances 0.000 description 5
- 239000000498 cooling water Substances 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 238000009826 distribution Methods 0.000 description 4
- 239000007769 metal material Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 241000790917 Dioxys <bee> Species 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 229910002804 graphite Inorganic materials 0.000 description 3
- 239000010439 graphite Substances 0.000 description 3
- 239000007770 graphite material Substances 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000008859 change Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 239000008358 core component Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 239000012495 reaction gas Substances 0.000 description 1
- 239000000126 substance 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
- H01M8/02—Details
-
- 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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
-
- 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
-
- 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)
- Fuel Cell (AREA)
Abstract
The invention discloses a kind of fuel cell bipolar plate structures, form above-mentioned fuel cell bipolar plate structure using multiple reducing agent pole plates, multiple oxidant pole plates and Multilayer Film Electrode component.The cavity that the bipolar plate structure that the present invention designs can reasonably utilize reducing agent pole plate, oxidant pole plate to be formed, provides flowing flow field for coolant, can be realized coolant in two substrate in combination and enter active region；Coolant is dexterously introduced into water conservancy diversion region runner by coolant water conservancy diversion runner simultaneously.And it can largely reduce flow resistance of the coolant in bipolar plates, reduce system energy consumption.Fuel cell bipolar plate structure provided by the invention can reduce bipolar plates weight, volume, the energy force density of the raising fuel cell.
Description
Technical field
The present invention relates to energy battery fields, and in particular to a kind of fuel cell bipolar plate structure.
Background technique
Proton Exchange Membrane Fuel Cells (PEMFC) is that a kind of chemical energy in fuel by chemical reaction is converted into electric energy
Power generator, have many advantages, such as high power density, low environment pollution, fixed power source, electric vehicle, military special type power pack can
It has broad application prospects in terms of with dynamic power supply, causes the attention of more and more national and enterprise.Currently, having become both at home and abroad
PEMFC is applied on manned bus and car to function.
Although the basis at present in relation to PEMFC has made significant progress with application study, still have quite from commercialization
Distance, cost and service life are key restriction factors.Bipolar plates are one of core components of fuel cell, account for entire battery weight
70% ~ 80% and cost 45% or more, play very important effect in terms of the cost and weight for controlling entire battery.Cause
This, exploitation be easily achieved the light-duty of large-scale production, thin layer bipolar plates for improve pile specific power, reduce pile cost, into
And PEMFC commercialization tool is pushed to have very important significance.
Bipolar plates have the function of to be isolated and evenly distribute reaction gas, collect simultaneously derived current, each monocell of series connection etc..
Its material mainly includes metal material, graphite material and composite material.Since graphite type material has good electric conductivity and change
Stability is learned, is the plate material that current PEMFC is widely used.But graphite material is crisp, poor air-tightness, mechanical strength is low and adds
Expenses of labour with it is high the disadvantages of be not easy to be mass produced, limit its industrial applications.Compared with graphite material, metal material has machine
Tool intensity height, good conductive and heating conduction, while being easy to be processed to thin plate, the specific energy of pile can be increased substantially,
Make the bipolar plate material of great competitiveness.
Bipolar plates are also not quite similar due to plate material difference, design.Graphite bi-polar plate is usually by hydrogen plate and oxygen plate
Composition, the flow field of cooling water is to be combined to be formed by the flow field of hydrogen plate and oxygen backboard portion.Flow field depth of cooling water etc. can basis
It is required that processing to obtain by the way of machine milling or pressing mold.Thus, the flow resistance of cooling water can control in lesser range.
When using other corrosion resistant thin metal materials, pole plate processing is carried out using the mechanical technology of punching press.In order to reduce pile weight
Amount, identical as graphite plate, metal double polar plates can be formed using two, three or more metal plates combines.Two metal plates
The flow field of cooling water be composed of the back side of hydrogen plate and oxygen plate, and the bipolar plates of three or more metal plates combines are then
There is individual coolant pole plate.But three or more metal double polar plates combinations are since quantity of polar plate is more, thus pole plate
Weight and volume it is larger, than two pole plate combinations of gravimetric specific power of pile are low by 25% or more, volumetric specific power low 40%
Left and right.Two pole plate combinations are compared with three and the above quantity pole plate combination is complicated in structure, and difficulty of processing is larger.
Since metal plate is process using Sheet Metal Forming Technology, thus the pole plate back side cannot pass through the flow field that secondary operation forms cooling water,
The flow field and water conservancy diversion field of coolant are made of the back side runner of two pole plates.Due to the limitation of metal material itself, polar plate flow field
Groove depth generally will not too deep (< 0.75mm), especially lead flow field portion.The flow field for causing each medium of fuel cell is deep
Spend shallower, resistance of the medium in each flow field increases, and increases distribution difficulty and system energy consumption of the medium in flow field.
Summary of the invention
The purpose of the present invention is to provide a kind of fuel cell bipolar plate structures, using multiple reducing agent pole plates, multiple oxygen
Agent pole plate and Multilayer Film Electrode component form above-mentioned fuel cell bipolar plate structure.The bipolar plate structure that the present invention designs can
The cavity reasonably formed using reducing agent pole plate, oxidant pole plate, is provided flowing flow field for coolant, can be realized two
Coolant enters active region in substrate in combination；Coolant is dexterously introduced into water conservancy diversion region by coolant water conservancy diversion runner simultaneously
Runner.And it can largely reduce flow resistance of the coolant in bipolar plates, reduce system energy consumption.The present invention mentions
The fuel cell bipolar plate structure of confession can reduce bipolar plates weight, volume, the energy force density of the raising fuel cell.
In order to achieve the above object, the invention is realized by the following technical scheme:
A kind of fuel cell bipolar plate structure, which includes: multiple reducing agent pole plates, multiple oxygen
Agent pole plate and Multilayer Film Electrode component；
Multiple oxidant pole plates and multiple reducing agent polar plate intervals are symmetrical arranged；Wherein, each oxidation
Agent pole plate symmetrically matches setting with the corresponding one reducing agent pole plate and forms a pair of of bipolar plate structure；
The oxidant pole plate and another pair institute of a pair of bipolar plate structure is arranged in every layer of membrane electrode assembly
It states between the reducing agent pole plate of bipolar plate structure.
Form coolant flow field between each pair of bipolar plate structure, each reducing agent pole plate and the corresponding film
Reducing agent runner is formed between electrode assembly, forms oxygen between each oxidant pole plate and the corresponding membrane electrode assembly
Agent runner.
Each reducing agent pole plate includes:
Reducing agent import, reducing agent are entered in the reducing agent pole plate by the reducing agent import；
The one end in the first reducing agent water conservancy diversion region, the first reducing agent water conservancy diversion region is connect with the reducing agent import；
Reducing agent active reaction region, the other end in the first reducing agent water conservancy diversion region and the reducing agent active reaction
The one end in region connects；
Second reducing agent water conservancy diversion region, described second reducing agent water conservancy diversion region one end and reducing agent active reaction region
The other end connection；
Reducing agent outlet, connect with the second reducing agent water conservancy diversion region other end.
Include in the first reducing agent water conservancy diversion region:
Multiple first reducing agent water conservancy diversion runners, one end of each first reducing agent water conservancy diversion runner and the reducing agent into
Mouth connection；
Multiple first reducing agent water conservancy diversion runner ridges, multiple first reducing agent water conservancy diversion runner ridges are gone back with multiple described first
Former agent water conservancy diversion runner is alternatively arranged setting, and one end of each first reducing agent water conservancy diversion runner ridge and the reducing agent import connect
It connects；
The reducing agent active reaction includes in region:
Multiple second reducing agent water conservancy diversion runners, one end of each second reducing agent water conservancy diversion runner and corresponding described
The other end of one reducing agent water conservancy diversion runner connects；
Multiple third reducing agent water conservancy diversion runners, multiple third reducing agent water conservancy diversion runners and multiple second reducing agent water conservancy diversion
Runner is alternatively arranged, one end of each third reducing agent water conservancy diversion runner and the corresponding first reducing agent water conservancy diversion runner ridge
The other end connection；
Include in the second reducing agent water conservancy diversion region:
Multiple 4th reducing agent water conservancy diversion runners, one end of each 4th reducing agent water conservancy diversion runner and corresponding described
The other end of two reducing agent water conservancy diversion runners connects；The other end of each 4th reducing agent water conservancy diversion runner goes out with the reducing agent
Mouth connection；
Multiple second reducing agent water conservancy diversion runner ridges, multiple second reducing agent water conservancy diversion runner ridges are gone back with multiple described four
Former agent water conservancy diversion runner is alternatively arranged setting, and one end of each second reducing agent water conservancy diversion runner ridge and the corresponding third are also
The other end of former agent water conservancy diversion runner connects, and the other end and the reducing agent of each second reducing agent water conservancy diversion runner ridge export
Connection.
Reducing agent enters multiple first reducing agents in the first reducing agent water conservancy diversion region by the reducing agent import
Water conservancy diversion runner, and pass through multiple second reducing agent water conservancy diversion runners in reducing agent active reaction region, described second respectively
Multiple 4th reducing agent water conservancy diversion runners in reducing agent water conservancy diversion region flow out to the reducing agent outlet.
Each oxidant pole plate includes:
Oxidant inlet, oxidant are entered in the oxidant pole plate by the oxidant inlet；The oxidant inlet
The same side of fuel cell bipolar plate structure is in the reducing agent import；
The one end in the first oxidant water conservancy diversion region, the first oxidant water conservancy diversion region is connect with the oxidant inlet；
Anti-oxidant active conversion zone, one end and first oxidant guiding region of the anti-oxidant active conversion zone
The other end in domain connects；
Second oxidant water conservancy diversion region, described second oxidant water conservancy diversion region one end and the anti-oxidant active conversion zone
The other end connection；
Oxidant outlet is connect with the second oxidant water conservancy diversion region other end.
Include in the first oxidant water conservancy diversion region:
Multiple first oxidant water conservancy diversion runners, one end of each first oxidant water conservancy diversion runner and the oxidant into
Mouth connection；
Multiple first oxidant water conservancy diversion runner ridges, multiple first oxidant water conservancy diversion runner ridges and multiple first oxygen
Agent water conservancy diversion runner is alternatively arranged setting, and one end of each first oxidant water conservancy diversion runner ridge and the oxidant inlet connect
It connects；Multiple first oxidant water conservancy diversion runner ridges intersect composition third with multiple first reducing agent water conservancy diversion runner ridges respectively
Cross-point region；
Include in the anti-oxidant active conversion zone:
Multiple second oxidant water conservancy diversion runners, one end of each second oxidant water conservancy diversion runner and corresponding described
The other end of one oxidant water conservancy diversion runner connects；
Multiple third oxidant water conservancy diversion runners, multiple third oxidant water conservancy diversion runners and multiple second oxidant water conservancy diversion
Runner is alternatively arranged, one end of each third oxidant water conservancy diversion runner and the corresponding first oxidant water conservancy diversion runner ridge
The other end connection；
Include in the second oxidant water conservancy diversion region:
Multiple 4th oxidant water conservancy diversion runners, one end of each 4th oxidant water conservancy diversion runner and corresponding described
The other end of dioxy agent water conservancy diversion runner connects；The other end of each 4th oxidant water conservancy diversion runner goes out with the oxidant
Mouth connection；
Multiple second oxidant water conservancy diversion runner ridges, multiple second oxidant water conservancy diversion runner ridges and multiple 4th oxygen
Agent water conservancy diversion runner is alternatively arranged setting, one end of each second oxidant water conservancy diversion runner ridge and the corresponding third oxygen
The other end of agent water conservancy diversion runner connects, the other end and the oxidant outlet of each second oxidant water conservancy diversion runner ridge
Connection.
Oxidant enters multiple first oxidants in the first oxidant water conservancy diversion region by the oxidant inlet
Water conservancy diversion runner, and pass through multiple second oxidant water conservancy diversion runners in the anti-oxidant active conversion zone, described second respectively
Multiple 4th oxidant water conservancy diversion runners in oxidant water conservancy diversion region flow out to the oxidant outlet.
Oxidant inlet, the reducing agent of the coolant inlet of each pair of bipolar plate structure and the oxidant pole plate
The reducing agent import of pole plate is in the same side, the oxygen of the coolant outlet to the bipolar plate structure and the oxidant pole plate
Agent outlet, the reducing agent outlet of the reducing agent pole plate are in the same side；
It include multiple coolant water conservancy diversion runners in each pair of bipolar plate structure；
Multiple coolant water conservancy diversion runners respectively with multiple first reducing agent water conservancy diversion runner ridge combined crosswises, and
Infall forms the first cross-point region；
Multiple coolant water conservancy diversion runners respectively with multiple first oxidant water conservancy diversion runner ridge combined crosswises, and
Infall forms the second cross-point region.
After coolant is from each coolant inlet into multiple coolant water conservancy diversion runners, coolant is respectively enterd
The reducing agent pole plate, the oxidant pole plate；
When coolant enters multiple first cross-point regions along multiple coolant water conservancy diversion runners, coolant meeting
Enter multiple first reducing agent water conservancy diversion runner ridges by multiple first cross-point regions；
When coolant enters multiple second cross-point regions along multiple coolant water conservancy diversion runners, coolant meeting
Enter multiple first oxidant water conservancy diversion runner ridges by multiple second cross-point regions.
When coolant respectively enters multiple first reducing agent water conservancy diversion runner ridges, multiple first oxidant water conservancy diversion streams
After road ridge；At multiple third cross-point regions, coolant is redistributed, and enables coolant again uniform
Multiple first reducing agent water conservancy diversion runner ridges, multiple first oxidant water conservancy diversion runner ridges are assigned to, and are entered described cold
But agent flow field.
Compared with the prior art, the present invention has the following advantages:
A kind of fuel cell bipolar plate structure disclosed by the invention, using multiple reducing agent pole plates, multiple oxidant pole plates
And Multilayer Film Electrode component forms above-mentioned fuel cell bipolar plate structure.The bipolar plate structure that the present invention designs being capable of reasonable land productivity
The cavity formed with reducing agent pole plate, oxidant pole plate, provides flowing flow field for coolant, can be realized two substrate in combination
Middle coolant enters active region；Coolant is dexterously introduced into water conservancy diversion region runner by coolant water conservancy diversion runner simultaneously, and
It is introduced using the intersection region of the oxidant water conservancy diversion runner ridge of the reducing agent water conservancy diversion runner ridge and oxidant pole plate of reducing agent pole plate
The cooling reaction zone of activity.And it can largely reduce flow resistance of the coolant in bipolar plates, reduce system energy
Consumption.Fuel cell bipolar plate structure provided by the invention can reduce bipolar plates weight, volume, the ability of the raising fuel cell
Density.
Detailed description of the invention
Fig. 1 is a kind of overall structure cross-sectional view of fuel cell bipolar plate structure of the present invention.
Fig. 2 is a kind of reducing agent pole plate schematic diagram of fuel cell bipolar plate structure of the present invention.
Fig. 3 is a kind of oxidant pole plate schematic diagram of fuel cell bipolar plate structure of the present invention.
Fig. 4 is that a kind of coolant water conservancy diversion runner of fuel cell bipolar plate structure of the present invention intersects with reducing agent water conservancy diversion runner
Area schematic.
Fig. 5 is that a kind of coolant water conservancy diversion runner of fuel cell bipolar plate structure of the present invention intersects with oxidant water conservancy diversion runner
Area schematic.
Fig. 6 is that a kind of reducing agent water conservancy diversion runner of fuel cell bipolar plate structure of the present invention intersects with oxidant water conservancy diversion runner
Area schematic.
Specific embodiment
The present invention is further elaborated by the way that a preferable specific embodiment is described in detail below in conjunction with attached drawing.
As shown in Figure 1, a kind of fuel cell bipolar plate structure 100, which includes: multiple
Reducing agent pole plate 2, multiple oxidant pole plates 1 and Multilayer Film Electrode component 3.
Multiple oxidant pole plates 1 are symmetrical arranged with multiple reducing agent pole plates 2 interval.Wherein, each oxidant pole plate 1 with it is right
Symmetrically matching setting forms a pair of of bipolar plate structure 100 to the reducing agent pole plate 2 answered.Every layer membrane electrode component 3 is arranged one
Oxidant pole plate 1 to bipolar plate structure 100 and between the reducing agent pole plate 2 of another pair bipolar plate structure 100.
Coolant flow field 4, each reducing agent pole plate 2 and corresponding membrane electrode assembly are formed between each pair of bipolar plate structure 100
Reducing agent runner 21 is formed between part 3, forms oxidant flow channel between each oxidant pole plate 1 and corresponding membrane electrode assembly 3
11。
As shown in Fig. 2, each reducing agent pole plate 2 includes: reducing agent import 201, is gone back first reducing agent water conservancy diversion region 202
Former agent active reaction region 203, the second reducing agent water conservancy diversion region 204 and reducing agent outlet 205.
Wherein, reducing agent is entered in reducing agent pole plate 2 by reducing agent import 201；First reducing agent water conservancy diversion region 202
One end is connect with reducing agent import 201, the other end in the first reducing agent water conservancy diversion region 202 and reducing agent active reaction region 203
One end connection；Second reducing agent water conservancy diversion region, 204 one end is connect with the other end in reducing agent active reaction region 203, reduction
Agent outlet 205 is connect with 204 other end of the second reducing agent water conservancy diversion region.
As shown in Fig. 2, including in the first reducing agent water conservancy diversion region 202: multiple first reducing agent water conservancy diversion runners 2021, multiple
First reducing agent water conservancy diversion runner ridge 2022.
Wherein, one end of each first reducing agent water conservancy diversion runner 2021 is connect with reducing agent import 201；Multiple first reduction
Agent water conservancy diversion runner ridge 2022 and multiple first reducing agent water conservancy diversion runners 2021 are alternatively arranged setting, each first reducing agent water conservancy diversion stream
One end of road ridge 2022 is connect with reducing agent import 201.
As shown in Fig. 2, including in reducing agent active reaction region 203: multiple second reducing agent water conservancy diversion runners 2031, multiple
Third reducing agent water conservancy diversion runner 2032.
Wherein, one end of each second reducing agent water conservancy diversion runner 2031 and corresponding first reducing agent water conservancy diversion runner 2021
Other end connection；Multiple third reducing agent water conservancy diversion runners 2032 are alternatively arranged with multiple second reducing agent water conservancy diversion runners 2031, often
One end of a third reducing agent water conservancy diversion runner 2032 is connected with the other end of corresponding first reducing agent water conservancy diversion runner ridge 2022.
As shown in Fig. 2, including in the second reducing agent water conservancy diversion region 204: multiple 4th reducing agent water conservancy diversion runners 2041, multiple
Second reducing agent water conservancy diversion runner ridge 2042.
Wherein, one end of each 4th reducing agent water conservancy diversion runner 2041 and corresponding second reducing agent water conservancy diversion runner 2031
Other end connection；The other end of each 4th reducing agent water conservancy diversion runner 2041 is connect with reducing agent outlet 205.Multiple second reduction
Agent water conservancy diversion runner ridge 2042 and multiple 4th reducing agent water conservancy diversion runners 2041 are alternatively arranged setting, each second reducing agent water conservancy diversion stream
One end of road ridge 2042 is connected with the other end of corresponding third reducing agent water conservancy diversion runner 2032, each second reducing agent water conservancy diversion stream
The other end of road ridge 2042 is connect with reducing agent outlet 205.
In the present invention, reducing agent enters multiple first in the first reducing agent water conservancy diversion region 202 by reducing agent import 201
Reducing agent water conservancy diversion runner 2021, and pass through multiple second reducing agent water conservancy diversion runners in reducing agent active reaction region 203 respectively
2031, multiple 4th reducing agent water conservancy diversion runners 2041 in the second reducing agent water conservancy diversion region 204 flow out to reducing agent outlet 205.
As shown in figure 3, each oxidant pole plate 1 includes: oxidant inlet 101, the first oxidant water conservancy diversion region 102, oxygen
Agent active reaction region 103, the second oxidant water conservancy diversion region 104 and oxidant outlet 105.
Wherein, oxidant is entered in oxidant pole plate 1 by oxidant inlet 101；The oxidant inlet 101 and reducing agent
Import 201 is in the same side of fuel cell bipolar plate structure 100.The one end in the first oxidant water conservancy diversion region 102 and oxidant
Import 101 connects, and one end of anti-oxidant active conversion zone 103 is connect with the other end in the first oxidant water conservancy diversion region 102；The
104 one end of dioxy agent guiding region domain is connect with the other end of anti-oxidant active conversion zone 103；Oxidant outlet 105 and
The connection of 104 other end of dioxy agent guiding region domain.
As shown in figure 3, including in the first oxidant water conservancy diversion region 102: multiple first oxidant water conservancy diversion runners 1021, multiple
First oxidant water conservancy diversion runner ridge 1022.
Wherein, one end of each first oxidant water conservancy diversion runner 1021 is connect with oxidant inlet 101.Multiple first oxidations
Agent water conservancy diversion runner ridge 1022 and multiple first oxidant water conservancy diversion runners 1021 are alternatively arranged setting, each first oxidant water conservancy diversion stream
One end of road ridge 1022 is connect with oxidant inlet 101；Multiple first oxidant water conservancy diversion runner ridges 1022 are respectively with multiple first
Reducing agent water conservancy diversion runner ridge 2022 intersects composition third cross-point region 150.
As shown in figure 3, including in anti-oxidant active conversion zone 103: multiple second oxidant water conservancy diversion runners 1031, multiple
Third oxidant water conservancy diversion runner 1032.
Wherein, one end of each second oxidant water conservancy diversion runner 1031 and corresponding first oxidant water conservancy diversion runner 1021
Other end connection；Multiple third oxidant water conservancy diversion runners 1032 are alternatively arranged with multiple second oxidant water conservancy diversion runners 1031, often
One end of a third oxidant water conservancy diversion runner 1032 is connected with the other end of corresponding first oxidant water conservancy diversion runner ridge 1022.
As shown in figure 3, including in the second oxidant water conservancy diversion region 104: multiple 4th oxidant water conservancy diversion runners 1041, multiple
Second oxidant water conservancy diversion runner ridge 1042.
Wherein, one end of each 4th oxidant water conservancy diversion runner 1041 and corresponding second oxidant water conservancy diversion runner 1031
Other end connection, the other end of each 4th oxidant water conservancy diversion runner 1041 are connect with oxidant outlet 105.Multiple second oxidations
Agent water conservancy diversion runner ridge 1042 and multiple 4th oxidant water conservancy diversion runners 1041 are alternatively arranged setting, each second oxidant water conservancy diversion stream
One end of road ridge 1042 is connected with the other end of corresponding third oxidant water conservancy diversion runner 1032, each second oxidant water conservancy diversion stream
The other end of road ridge 1042 is connect with oxidant outlet 105.
Oxidant is led by multiple first oxidants that oxidant inlet 101 enters in the first oxidant water conservancy diversion region 102
Runner 1021 is flowed, and passes through multiple second oxidant water conservancy diversion runners 1031, second in anti-oxidant active conversion zone 103 respectively
Multiple 4th oxidant water conservancy diversion runners 1041 in oxidant water conservancy diversion region 104 flow out to oxidant outlet 105.
As shown in Figure 2 and Figure 3, the oxidant of the coolant inlet 401 of each pair of bipolar plate structure 100 and oxidant pole plate 1 into
Mouthfuls 101, the reducing agent import 201 of reducing agent pole plate 2 be in the same side, the coolant outlet 402 to bipolar plate structure 100 and
The reducing agent outlet 205 of the oxidant outlet 105, reducing agent pole plate 2 of oxidant pole plate 1 is in the same side.
It as shown in Figure 4, Figure 5, include multiple coolant water conservancy diversion runners 110 in each pair of bipolar plate structure 100.Multiple coolants
Water conservancy diversion runner 110 respectively with multiple first reducing agent water conservancy diversion runner ridge, 2022 combined crosswises, and infall formed first intersect
Point region 130.Multiple coolant water conservancy diversion runners 110 respectively with multiple first oxidant water conservancy diversion runner ridge, 1022 combined crosswises, and
The second cross-point region 140 is formed in infall.
As shown in Figure 4-Figure 6, the specific working principle is as follows for a kind of fuel cell bipolar plate structure disclosed by the invention:
Flow process of the reducing agent in reducing agent pole plate 2 are as follows: reducing agent is through more in the first reducing agent water conservancy diversion region 202
A first reducing agent water conservancy diversion runner 2021 enters multiple second reducing agent water conservancy diversion runners in reducing agent active reaction region 203
2031, and multiple 4th reducing agent water conservancy diversion runners 2041 through the second reducing agent water conservancy diversion region 204 pass through 205 stream of reducing agent outlet
Out.Flow process of the oxidant in oxidant pole plate 1 are as follows: oxidant is through multiple in the first oxidant water conservancy diversion region 102
One oxidant water conservancy diversion runner 1021 enters multiple second oxidant water conservancy diversion runners 1031 in anti-oxidant active conversion zone 103,
And it is flowed out through multiple 4th oxidant water conservancy diversion runners 1041 in the second oxidant water conservancy diversion region 104 by oxidant outlet 105.
After coolant is from each coolant inlet 401 into multiple coolant water conservancy diversion runners 110, coolant is respectively enterd also
Former agent pole plate 2, oxidant pole plate 1.
When coolant along multiple coolant water conservancy diversion runners 110 enter multiple first reducing agent water conservancy diversion runner ridges 2022 with it is multiple
When multiple first cross-point regions 130 that coolant water conservancy diversion runner 110 is formed, portion cooling agent can pass through multiple first crosspoints
Region 130 enters multiple first reducing agent water conservancy diversion runner ridges 2022, and remainder coolant branches to multiple coolant water conservancy diversion streams
Road 110.When coolant along multiple coolant water conservancy diversion runners 110 enter multiple first oxidant water conservancy diversion runner ridges 1022 with it is multiple cold
When multiple second cross-point regions 140 that but agent water conservancy diversion runner 110 is formed, portion cooling agent can pass through multiple second cross-point regions
Domain 140 enters multiple first oxidant water conservancy diversion runner ridges 1022, and remainder coolant branches to multiple coolant water conservancy diversion runners
110。
When coolant respectively enters multiple first reducing agent water conservancy diversion runner ridges 2022, multiple first oxidant water conservancy diversion runner ridges
After 1022；At multiple third cross-point regions 150, coolant is redistributed, and enables coolant again uniform
After distribution, portion cooling agent is diverted to multiple first reducing agent water conservancy diversion runner ridges 2022, remaining coolant is diverted to multiple first
Oxidant water conservancy diversion runner ridge 1022, so that distribution of the coolant in each distribution runner is more uniform.Finally, coolant enters
Coolant flow field 4.
It is discussed in detail although the contents of the present invention have passed through above preferred embodiment, but it should be appreciated that above-mentioned
Description is not considered as limitation of the present invention.After those skilled in the art have read above content, for of the invention
A variety of modifications and substitutions all will be apparent.Therefore, protection scope of the present invention should be limited to the appended claims.
Claims (3)
1. a kind of fuel cell bipolar plate structure, which is characterized in that the fuel cell bipolar plate structure includes: multiple reducing agent poles
Plate, multiple oxidant pole plates and Multilayer Film Electrode component；
Multiple oxidant pole plates and multiple reducing agent polar plate intervals are symmetrical arranged；Wherein, each oxidizing agent pole
Plate symmetrically matches setting with the corresponding one reducing agent pole plate and forms a pair of of bipolar plate structure；
Every layer of membrane electrode assembly be arranged in a pair of bipolar plate structure the oxidant pole plate and another pair described in it is double
Between the reducing agent pole plate of electrode plate structure；
Form coolant flow field between each pair of bipolar plate structure, each reducing agent pole plate and the corresponding membrane electrode
Reducing agent runner is formed between component, forms oxidant between each oxidant pole plate and the corresponding membrane electrode assembly
Runner；
Each reducing agent pole plate includes:
Reducing agent import, reducing agent are entered in the reducing agent pole plate by the reducing agent import；
The one end in the first reducing agent water conservancy diversion region, the first reducing agent water conservancy diversion region is connect with the reducing agent import；
Reducing agent active reaction region, the other end in the first reducing agent water conservancy diversion region and reducing agent active reaction region
One end connection；
Second reducing agent water conservancy diversion region, described second reducing agent water conservancy diversion region one end are another with reducing agent active reaction region
One end connection；
Reducing agent outlet, connect with the second reducing agent water conservancy diversion region other end；
Include in the first reducing agent water conservancy diversion region:
Multiple first reducing agent water conservancy diversion runners, one end of each first reducing agent water conservancy diversion runner and the reducing agent import connect
It connects；
Multiple first reducing agent water conservancy diversion runner ridges, multiple first reducing agent water conservancy diversion runner ridges and multiple first reducing agents
Water conservancy diversion runner is alternatively arranged setting, and one end of each first reducing agent water conservancy diversion runner ridge is connect with the reducing agent import；
The reducing agent active reaction includes in region:
Multiple second reducing agent water conservancy diversion runners, one end of each second reducing agent water conservancy diversion runner are gone back with corresponding described first
The other end of former agent water conservancy diversion runner connects；
Multiple third reducing agent water conservancy diversion runners, multiple third reducing agent water conservancy diversion runners and multiple second reducing agent water conservancy diversion runners
It is alternatively arranged, one end of each third reducing agent water conservancy diversion runner is another with the corresponding first reducing agent water conservancy diversion runner ridge
One end connection；
Include in the second reducing agent water conservancy diversion region:
Multiple 4th reducing agent water conservancy diversion runners, one end of each 4th reducing agent water conservancy diversion runner are gone back with corresponding described second
The other end of former agent water conservancy diversion runner connects；The other end of each 4th reducing agent water conservancy diversion runner and reducing agent outlet connect
It connects；
Multiple second reducing agent water conservancy diversion runner ridges, multiple second reducing agent water conservancy diversion runner ridges and multiple 4th reducing agents
Water conservancy diversion runner is alternatively arranged setting, one end of each second reducing agent water conservancy diversion runner ridge and the corresponding third reducing agent
The other end of water conservancy diversion runner connects, and the other end of each second reducing agent water conservancy diversion runner ridge and reducing agent outlet connect
It connects,
Reducing agent enters multiple first reducing agent water conservancy diversion in the first reducing agent water conservancy diversion region by the reducing agent import
Runner, and pass through multiple second reducing agent water conservancy diversion runners in reducing agent active reaction region, second reduction respectively
Multiple 4th reducing agent water conservancy diversion runners in agent water conservancy diversion region flow out to the reducing agent outlet；
Each oxidant pole plate includes:
Oxidant inlet, oxidant are entered in the oxidant pole plate by the oxidant inlet；The oxidant inlet and institute
State the same side that reducing agent import is in fuel cell bipolar plate structure；
The one end in the first oxidant water conservancy diversion region, the first oxidant water conservancy diversion region is connect with the oxidant inlet；
Anti-oxidant active conversion zone, one end of the anti-oxidant active conversion zone and the first oxidant water conservancy diversion region
Other end connection；
Second oxidant water conservancy diversion region, described second oxidant water conservancy diversion region one end are another with the anti-oxidant active conversion zone
One end connection；
Oxidant outlet is connect with the second oxidant water conservancy diversion region other end；
Include in the first oxidant water conservancy diversion region:
Multiple first oxidant water conservancy diversion runners, one end of each first oxidant water conservancy diversion runner and the oxidant inlet connect
It connects；
Multiple first oxidant water conservancy diversion runner ridges, multiple first oxidant water conservancy diversion runner ridges and multiple first oxidants
Water conservancy diversion runner is alternatively arranged setting, and one end of each first oxidant water conservancy diversion runner ridge is connect with the oxidant inlet；
Multiple first oxidant water conservancy diversion runner ridges intersect composition third with multiple first reducing agent water conservancy diversion runner ridges respectively to be handed over
Crunode region；
Include in the anti-oxidant active conversion zone:
Multiple second oxidant water conservancy diversion runners, one end of each second oxidant water conservancy diversion runner and corresponding first oxygen
The other end of agent water conservancy diversion runner connects；
Multiple third oxidant water conservancy diversion runners, multiple third oxidant water conservancy diversion runners and multiple second oxidant water conservancy diversion runners
It is alternatively arranged, one end of each third oxidant water conservancy diversion runner is another with the corresponding first oxidant water conservancy diversion runner ridge
One end connection；
Include in the second oxidant water conservancy diversion region:
Multiple 4th oxidant water conservancy diversion runners, one end of each 4th oxidant water conservancy diversion runner and corresponding second oxygen
The other end of agent water conservancy diversion runner connects；The other end and the oxidant outlet of each 4th oxidant water conservancy diversion runner connect
It connects；
Multiple second oxidant water conservancy diversion runner ridges, multiple second oxidant water conservancy diversion runner ridges and multiple 4th oxidants
Water conservancy diversion runner is alternatively arranged setting, one end of each second oxidant water conservancy diversion runner ridge and the corresponding third oxidant
The other end of water conservancy diversion runner connects, and the other end and the oxidant outlet of each second oxidant water conservancy diversion runner ridge connect
It connects,
Oxidant enters multiple first oxidant water conservancy diversion in the first oxidant water conservancy diversion region by the oxidant inlet
Runner, and pass through multiple second oxidant water conservancy diversion runners in the anti-oxidant active conversion zone, second oxidation respectively
Multiple 4th oxidant water conservancy diversion runners in agent water conservancy diversion region flow out to the oxidant outlet；
Oxidant inlet, the reducing agent pole plate of the coolant inlet of each pair of bipolar plate structure and the oxidant pole plate
Reducing agent import be in the same side, the oxidant of the coolant outlet to the bipolar plate structure and the oxidant pole plate
Outlet, the reducing agent outlet of the reducing agent pole plate are in the same side；
It include multiple coolant water conservancy diversion runners in each pair of bipolar plate structure；
Multiple coolant water conservancy diversion runners with multiple first reducing agent water conservancy diversion runner ridge combined crosswises, and are intersecting respectively
Place forms the first cross-point region；
Multiple coolant water conservancy diversion runners with multiple first oxidant water conservancy diversion runner ridge combined crosswises, and are intersecting respectively
Place forms the second cross-point region.
2. such as claim 1 fuel cell bipolar plate structure, which is characterized in that
After coolant is from each coolant inlet into multiple coolant water conservancy diversion runners, coolant respectively enters described
Reducing agent pole plate, the oxidant pole plate；
When coolant enters multiple first cross-point regions along multiple coolant water conservancy diversion runners, coolant can pass through
Multiple first cross-point regions enter multiple first reducing agent water conservancy diversion runner ridges；
When coolant enters multiple second cross-point regions along multiple coolant water conservancy diversion runners, coolant can pass through
Multiple second cross-point regions enter multiple first oxidant water conservancy diversion runner ridges.
3. such as claim 2 fuel cell bipolar plate structure, which is characterized in that when coolant respectively enters multiple described first also
After former agent water conservancy diversion runner ridge, multiple first oxidant water conservancy diversion runner ridges；It is cooling at multiple third cross-point regions
Agent is redistributed, and coolant is enabled to be evenly distributed to multiple first reducing agent water conservancy diversion runner ridges, more again
A first oxidant water conservancy diversion runner ridge, and enter the coolant flow field.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510820686.3A CN105336967B (en) | 2015-11-24 | 2015-11-24 | A fuel cell bipolar plate structure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510820686.3A CN105336967B (en) | 2015-11-24 | 2015-11-24 | A fuel cell bipolar plate structure |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105336967A CN105336967A (en) | 2016-02-17 |
| CN105336967B true CN105336967B (en) | 2019-02-05 |
Family
ID=55287366
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510820686.3A Active CN105336967B (en) | 2015-11-24 | 2015-11-24 | A fuel cell bipolar plate structure |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105336967B (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109687001A (en) * | 2017-10-18 | 2019-04-26 | 熵零技术逻辑工程院集团股份有限公司 | A kind of fuel cell |
| CN108767288B (en) * | 2018-06-11 | 2020-11-10 | 西安交通大学 | A variable-section tree-shaped fuel cell flow channel structure |
| CN110767919B (en) * | 2019-12-26 | 2020-04-10 | 武汉中极氢能产业创新中心有限公司 | Bipolar plate of fuel cell and fuel cell |
| CN111900429B (en) * | 2020-07-24 | 2021-11-05 | 浙江泓林新能源科技有限公司 | Metal bipolar plate of fuel cell and processing method thereof |
| CN114551922B (en) * | 2022-03-02 | 2024-02-20 | 重庆理工大学 | Fuel cell bipolar plate structure and fuel cell |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106134491B (en) * | 2004-04-07 | 2011-01-12 | 上海空间电源研究所 | Proton Exchange Membrane Fuel Cells novel metal bipolar plates |
| US7687175B2 (en) * | 2004-05-03 | 2010-03-30 | Gm Global Technology Operations, Inc. | Hybrid bipolar plate assembly and devices incorporating same |
| CN101420037B (en) * | 2008-12-10 | 2011-05-18 | 新源动力股份有限公司 | A metal bipolar plate for a proton exchange membrane fuel cell |
| CN101572318B (en) * | 2009-06-16 | 2010-12-08 | 新源动力股份有限公司 | Metal bipolar plate of proton exchange membrane fuel cell |
| CN203760565U (en) * | 2014-02-18 | 2014-08-06 | 武汉理工大学 | Metal bipolar plate of proton exchange membrane fuel battery |
-
2015
- 2015-11-24 CN CN201510820686.3A patent/CN105336967B/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| CN105336967A (en) | 2016-02-17 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105336967B (en) | A fuel cell bipolar plate structure | |
| CN210443621U (en) | Metal matrix bipolar plate | |
| CN100449836C (en) | A Hybrid Gradually Variable Flow Field Plate for Proton Exchange Membrane Fuel Cell | |
| CN101101993A (en) | Bipolar plates for proton exchange membrane fuel cells based on sheet stamping | |
| CN105762396B (en) | A kind of flat hot recycling ammonia battery using foam metal electrode | |
| CN109686995A (en) | A kind of interior bipolar plates with wedge-shaped protrusion of runner | |
| CN107634241B (en) | Flow frame for flow battery | |
| CN211743309U (en) | Bipolar plate for testing power generation performance of membrane electrode of hydrogen fuel cell | |
| CN102473928A (en) | Air-cooled metal separator for fuel cell and fuel cell stack using the same | |
| CN217973433U (en) | Monopolar plate, bipolar plate and water electrolysis device | |
| CN107634240A (en) | A kind of small fuel cell metal double polar plates | |
| CN110429296A (en) | A kind of fuel battery double plates | |
| CN102683718A (en) | Bipolar plate for fuel cell | |
| CN105529478A (en) | Fuel cell bipolar plate and electric pile constituted by same | |
| CN210224176U (en) | Proton exchange membrane fuel cell bipolar plate with improved common conduit and fluid channel | |
| CN202275888U (en) | Metal Bipolar Plates for Proton Exchange Membrane Fuel Cells Facilitating Improved Fluid Distribution | |
| CN209374562U (en) | A kind of interior bipolar plates with wedge-shaped protrusion of runner | |
| CN104701550B (en) | Metal bipolar plate of fuel battery | |
| CN101388465A (en) | Fuel cell polar plate and fuel cell using the same | |
| CN213583872U (en) | Bipolar plate of fuel cell | |
| CN100550500C (en) | A kind of fuel battery | |
| CN103579641B (en) | A kind of electric pile structure of flow battery | |
| CN203707257U (en) | Cathode structure of proton exchange membrane fuel cell | |
| CN101087026A (en) | A flow guiding polarized plate of fuel battery | |
| CN207504106U (en) | A kind of fuel battery double plates |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |