CN1405917A - Proton-exchange film-fuel cell heat analog apparatus for heat management system test - Google Patents
Proton-exchange film-fuel cell heat analog apparatus for heat management system test Download PDFInfo
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- CN1405917A CN1405917A CN02148652A CN02148652A CN1405917A CN 1405917 A CN1405917 A CN 1405917A CN 02148652 A CN02148652 A CN 02148652A CN 02148652 A CN02148652 A CN 02148652A CN 1405917 A CN1405917 A CN 1405917A
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- fuel cell
- heat
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- thermal
- bipolar plates
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- 239000000446 fuel Substances 0.000 title claims abstract description 32
- 238000012360 testing method Methods 0.000 title claims abstract description 5
- 238000004088 simulation Methods 0.000 claims abstract description 21
- 239000012528 membrane Substances 0.000 claims abstract description 6
- 239000000498 cooling water Substances 0.000 abstract description 6
- 238000011160 research Methods 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 238000000605 extraction Methods 0.000 description 10
- 238000005183 dynamical system Methods 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000003487 electrochemical reaction Methods 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical group [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 241000276425 Xiphophorus maculatus Species 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 125000004430 oxygen atom Chemical group O* 0.000 description 1
- 239000012495 reaction gas Substances 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
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- Fuel Cell (AREA)
Abstract
一种用于热管理系统试验的质子交换膜燃料电池堆热模拟装置，属车用燃料电池动力系统热管理技术领域。本热模拟装置由多个单元板叠合在一起组成，每个单元板由一个模拟电极，两个双极板，两个排热板组成。在模拟电极及双极板上贴有热电阻片，通电后模拟燃料电池堆的产热情况，在排热板上开有冷却水通道。两块双极板分别与模拟电极的两侧面相贴合，两块排热板分别与两块双极板相贴合。采用本热模拟装置可开展燃料电池动力系统热管理试验研究。
The invention relates to a proton exchange membrane fuel cell stack thermal simulation device used for thermal management system test, which belongs to the technical field of thermal management of vehicle fuel cell power system. The thermal simulation device is composed of multiple unit plates stacked together, and each unit plate is composed of a simulated electrode, two bipolar plates, and two heat exhaust plates. Thermal resistance sheets are pasted on the simulated electrodes and bipolar plates to simulate the heat production of the fuel cell stack after power-on, and a cooling water channel is opened on the heat exhaust plate. The two bipolar plates are respectively attached to the two sides of the simulated electrode, and the two heat exhaust plates are respectively attached to the two bipolar plates. The thermal simulation device can be used to carry out experimental research on the thermal management of fuel cell power systems.
Description
Technical field
The present invention relates to Proton Exchange Membrane Fuel Cells (PEMFC) heap thermal cycle simulation, belong to vehicle fuel battery dynamical system thermal management technology field.
Background technology
Fuel-cell vehicle is to have substituted traditional combustion engine powered system by fuel cell power system with respect to the main distinction of orthodox car.The 2.5-3 that PEMFC dynamical system waste heat is about the traditional combustion engine dynamical system doubly, reactor behavior is to responsive to temperature, and coolant temperature and circumstance of temperature difference are little, have bigger heat management difficulty.Heat management not only influences highly significant to the PEMFC power system performance, what is more important, and can will directly influence it operate as normal.Therefore, the heat management of PEMFC dynamical system becomes the key issue in the fuel cell car research and development.
Fuel cell pack is the main thermal source of dynamical system, fuel chemical energy respectively accounts for 50% approximately by electric energy and the heat energy that fuel cell pack transforms, as a fuel cell pack that is output as 75KW, the heat of taking out of by heat management is about 75KW, is 2.5～3 times of traditional combustion engine.For drying and the overheating operation that prevents film, need corresponding heat transfer mechanism and remove the huge heat that electrochemical reaction produces.In addition, because the temperature difference is less between fuel cell and running environment, the heat extraction of reactor becomes one and has challenging problem.The heat balance of PEMFC inside plays key effect to fuel cell performance, life-span and security of operation.Therefore, study the heat extraction performance and the thermal uniformity of fuel cell, control inside battery fluid flows and conducts heat, and guarantees the heat balance and the water balance of reactor.
The experimental study of fuel cell power system heat management comprises the research of fuel cell pack heat management, the research of system integration heat management, the content of aspects such as the special equipment of heat management (as heat exchanger, cooling fan etc.) research and waste heat utilization technology research.
Use true fuel cell pack to carry out the experimental study of dynamical system heat management, there are problems such as the hydrogen potential safety hazard is big, the hydrogen consumption is big, and auxiliary system complexity such as supply of fuel, it is bigger and costly to cause testing difficulty, is not suitable for effectively carrying out flexibly of the special experimental study of heat management.
Summary of the invention
The thermal cycle simulation that the purpose of this invention is to provide a kind of pem fuel cell stack substitutes true fuel cell pack, uses for the experimental study of dynamical system heat management.
The structure that fuel cell pack is described is as follows: the single-cell structure of true fuel cell pack as shown in Figure 1, its core is made up of proton exchange membrane 3, anode catalyst layer 4a, cathode catalysis layer 4b, diffusion layer 5, bipolar plates 8 and heat extraction plates 9 etc.Catalytic Layer 4a, 4b are the places that electrochemical reaction takes place.The effect of diffusion layer 5 is to support Catalytic Layer 4a, 4b, collected current, and provide electron channel, gas passage and drainage channel for electrochemical reaction.Proton exchange membrane 3, Catalytic Layer 4a, 4b and diffusion layer 5 are formed electrode altogether.Bipolar plates 8 provides reaction gas passage and the effect of collected current is arranged.Hydrogen and oxygen (perhaps air) flow through the runner 6 of bipolar plates 8 respectively and diffused into electrode at 7 o'clock.In the anode-side of electrode, hydrogen atom is hydrogen ion and electronics by ionization under catalyst action, and wherein hydrogen ion passes proton exchange membrane 3 and transfers to cathode side, electronics then through the external circuit load flow to negative electrode; At cathode side, catalyst makes the oxygen atom of hydrogen ion and negative electrode and the electronics that returns from the external circuit be combined into hydrone again, and the while release heat.On heat extraction plates 9, the outer loop cooling water flows through path 10, takes away big quantitative response heat production, keeps the stable of battery operated temperature.
Pem fuel cell stack thermal cycle simulation of the present invention is superimposed together by a plurality of cell boards and forms.Each cell board is by a simulation electrode, two bipolar plates, and two heat extraction plates are formed.Post the thermal resistance sheet on simulation electrode and bipolar plates, the heat production situation of energising back analog fuel battery pile has cooling-water duct on heat extraction plates.Two bipolar plates fit with the two sides of simulation electrode respectively, and two heat extraction plates fit with two bipolar plates respectively.
Adopt thermal cycle simulation of the present invention can come the different operating situation of analog fuel battery pile, for experimental study by the caloric value of controlling every thermal resistance.
Description of drawings
Fig. 1 is the sectional view of proton exchanging film fuel cell unit plate
Fig. 2 is the sectional view of thermal cycle simulation cell board of the present invention
Fig. 3 is the end view of thermal cycle simulation cell board of the present invention
Fig. 4 is a thermal cycle simulation schematic diagram of the present invention
Embodiment
Fig. 4 is the schematic diagram of thermal cycle simulation, and wherein 17 is cell board
Fig. 2 is the sectional view of thermal cycle simulation cell board.Wherein 12 is simulation electrode, is a platy structure, is made by carbon cloth or carbon paper, and also available other material is made, as long as guarantee that the thermal resistance of simulation electrode is identical with the thermal resistance of electrode part in the true fuel cell.13 is bipolar plates, and 14 is heat extraction plates, and its structure is identical with true fuel cell with material, is generally atresia graphite.Two bipolar plates 13 are attached to the both sides of analog electrical pole plate 12, all are equipped with 11, two heat extraction plates 14 of thermal resistance sheet at the runner wall that reaches bipolar plates 13 between bipolar plates 13 and the analog electrical pole plate 12 and are attached to respectively on two bipolar plates 13.Every thermal resistance can be controlled its caloric value separately, to obtain reaching various heat distribution on the bipolar plates 13 on the simulation electrode 12, is convenient to carrying out of experimental study.
Fig. 3 is the end view of thermal cycle simulation cell board.Cooling water runner 16 on the heat extraction plates 14 is straight channel, and cooling water enters from inlet channel 15a, leaves by convergeing to water outlet 15b again after each branch's cooling water runner 16.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021486522A CN1173427C (en) | 2002-11-15 | 2002-11-15 | Proton exchange membrane fuel cell stack thermal simulator for thermal management system test |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021486522A CN1173427C (en) | 2002-11-15 | 2002-11-15 | Proton exchange membrane fuel cell stack thermal simulator for thermal management system test |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1405917A true CN1405917A (en) | 2003-03-26 |
| CN1173427C CN1173427C (en) | 2004-10-27 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB021486522A Expired - Fee Related CN1173427C (en) | 2002-11-15 | 2002-11-15 | Proton exchange membrane fuel cell stack thermal simulator for thermal management system test |
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| Country | Link |
|---|---|
| CN (1) | CN1173427C (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102956905A (en) * | 2012-09-21 | 2013-03-06 | 同济大学 | Thermal management simulation system for fuel cell stacks |
| CN103620844A (en) * | 2011-05-26 | 2014-03-05 | 原子能和替代能源委员会 | Fuel cell with improved thermal management |
| CN104733757A (en) * | 2014-12-24 | 2015-06-24 | 同济大学 | Rapid prototyping device for automobile fuel cell cooling auxiliary system |
| CN108417867A (en) * | 2017-10-30 | 2018-08-17 | 同济大学 | A stack simulation device for the development of high-power fuel cell thermal management system |
| CN114447391A (en) * | 2020-11-05 | 2022-05-06 | 未势能源科技有限公司 | Fuel cell stack |
-
2002
- 2002-11-15 CN CNB021486522A patent/CN1173427C/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103620844A (en) * | 2011-05-26 | 2014-03-05 | 原子能和替代能源委员会 | Fuel cell with improved thermal management |
| US9337500B2 (en) | 2011-05-26 | 2016-05-10 | Commissariat à l'énergie atomique et aux énergies alternatives | Fuel cell with improved thermal management |
| CN102956905A (en) * | 2012-09-21 | 2013-03-06 | 同济大学 | Thermal management simulation system for fuel cell stacks |
| CN102956905B (en) * | 2012-09-21 | 2014-10-22 | 同济大学 | Thermal management simulation system for fuel cell stacks |
| CN104733757A (en) * | 2014-12-24 | 2015-06-24 | 同济大学 | Rapid prototyping device for automobile fuel cell cooling auxiliary system |
| CN104733757B (en) * | 2014-12-24 | 2017-05-17 | 同济大学 | Rapid prototyping device for automobile fuel cell cooling auxiliary system |
| CN108417867A (en) * | 2017-10-30 | 2018-08-17 | 同济大学 | A stack simulation device for the development of high-power fuel cell thermal management system |
| CN114447391A (en) * | 2020-11-05 | 2022-05-06 | 未势能源科技有限公司 | Fuel cell stack |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1173427C (en) | 2004-10-27 |
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