CN201051522Y - A fuel battery compound body - Google Patents
A fuel battery compound body Download PDFInfo
- Publication number
- CN201051522Y CN201051522Y CNU2007200715762U CN200720071576U CN201051522Y CN 201051522 Y CN201051522 Y CN 201051522Y CN U2007200715762 U CNU2007200715762 U CN U2007200715762U CN 200720071576 U CN200720071576 U CN 200720071576U CN 201051522 Y CN201051522 Y CN 201051522Y
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- current collecting
- fuel cell
- shaped space
- concave shaped
- collecting master
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- 239000000446 fuel Substances 0.000 title claims abstract description 88
- 150000001875 compounds Chemical class 0.000 title description 13
- 238000007789 sealing Methods 0.000 claims abstract description 11
- 239000012530 fluid Substances 0.000 claims description 49
- 239000001257 hydrogen Substances 0.000 claims description 24
- 229910052739 hydrogen Inorganic materials 0.000 claims description 24
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 23
- 230000007306 turnover Effects 0.000 claims description 13
- 239000000853 adhesive Substances 0.000 claims description 7
- 230000001070 adhesive effect Effects 0.000 claims description 7
- 239000000498 cooling water Substances 0.000 claims description 7
- 239000010410 layer Substances 0.000 claims description 4
- 239000012945 sealing adhesive Substances 0.000 claims description 4
- 230000002093 peripheral effect Effects 0.000 claims description 2
- 238000005536 corrosion prevention Methods 0.000 abstract 1
- 239000012528 membrane Substances 0.000 description 31
- 239000007800 oxidant agent Substances 0.000 description 13
- 230000001590 oxidative effect Effects 0.000 description 13
- 238000006243 chemical reaction Methods 0.000 description 10
- 239000000463 material Substances 0.000 description 10
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 7
- 239000007789 gas Substances 0.000 description 7
- 239000001301 oxygen Substances 0.000 description 7
- 229910052760 oxygen Inorganic materials 0.000 description 7
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 5
- 239000003054 catalyst Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 230000008676 import Effects 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 4
- 238000004026 adhesive bonding Methods 0.000 description 4
- 239000012790 adhesive layer Substances 0.000 description 4
- 229910052782 aluminium Inorganic materials 0.000 description 4
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 239000012809 cooling fluid Substances 0.000 description 4
- 229910052802 copper Inorganic materials 0.000 description 4
- 239000010949 copper Substances 0.000 description 4
- 230000007797 corrosion Effects 0.000 description 4
- 238000005260 corrosion Methods 0.000 description 4
- 238000003487 electrochemical reaction Methods 0.000 description 4
- 229910052697 platinum Inorganic materials 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 239000004411 aluminium Substances 0.000 description 3
- 150000001450 anions Chemical class 0.000 description 3
- 150000001768 cations Chemical class 0.000 description 3
- 239000004020 conductor Substances 0.000 description 3
- 238000006056 electrooxidation reaction Methods 0.000 description 3
- 150000002431 hydrogen Chemical class 0.000 description 3
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 229910001220 stainless steel Inorganic materials 0.000 description 3
- 239000010935 stainless steel Substances 0.000 description 3
- 239000002131 composite material Substances 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
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- 238000009792 diffusion process Methods 0.000 description 2
- 230000005518 electrochemistry Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 2
- 239000010931 gold Substances 0.000 description 2
- 229910052737 gold Inorganic materials 0.000 description 2
- 230000008595 infiltration Effects 0.000 description 2
- 238000001764 infiltration Methods 0.000 description 2
- 210000001503 joint Anatomy 0.000 description 2
- 229910021645 metal ion Inorganic materials 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 230000005012 migration Effects 0.000 description 2
- 238000013508 migration Methods 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 241001124569 Lycaenidae Species 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 235000014987 copper Nutrition 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000004512 die casting Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000005183 dynamical system Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000008393 encapsulating agent Substances 0.000 description 1
- 229920006335 epoxy glue Polymers 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 239000003502 gasoline Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- -1 gold-plated Substances 0.000 description 1
- 239000007770 graphite material Substances 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
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- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Images
Classifications
-
- 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
- Fuel Cell (AREA)
Abstract
The utility model relates to a fuel battery complex, comprising a fluid-distributing board, a current collecting master blank and a flow guiding pole plate. One side or two sides of the fluid-distributing board are provided with a concave space which is provided inside with the current collecting master blank, the surface of the current collecting master blank is flush with the lateral face of the fluid-distributing board, and corresponding surfaces of the flow guiding pole plate in front of the current collecting master blank and adjacent to the current collecting master blank are adhered, sealed and connected with non-concave space on the fluid-distributing board to a complex. Compared with the prior art, the fuel battery complex of the utility model has the advantages of corrosion prevention, great sealing, small contact resistance, low cost, convenient disassembly and assembly, and the like.
Description
Technical field
The utility model relates to fuel cell, relates in particular to a kind of fuel cell complex.
Background technology
Electrochemical fuel cell is a kind of device that hydrogen and oxidant can be changed into electric energy and product.The internal core parts of this device are membrane electrode (Membrane Electrode Assembly are called for short MEA), and membrane electrode (MEA) is made up of as carbon paper a proton exchange membrane, two porous conductive materials of film two sides folder.The catalyst that contains the initiation electrochemical reaction of even tiny dispersion on two boundary faces of film and carbon paper is as the metal platinum catalyst.The membrane electrode both sides can electrochemistry will take place with conductive body to be sent out and answers the electronics that generates in the process, draws by external circuit, constitutes current circuit.
At the anode tap of membrane electrode, fuel can pass porousness diffusion material (carbon paper) by infiltration, and electrochemical reaction takes place on catalyst surface, lose electronics, form cation, cation can pass proton exchange membrane by migration, arrives the other end cathode terminal of membrane electrode.At the cathode terminal of membrane electrode, contain the gas of oxidant (as oxygen), as air, pass porousness diffusion material (carbon paper), and the generation electrochemical reaction obtains electronics on catalyst surface, forms anion by infiltration.The cation of coming in the anion and the anode tap migration of cathode terminal formation reacts, and forms product.
Adopting hydrogen is fuel, and the air that contains oxygen is in the Proton Exchange Membrane Fuel Cells of oxidant (or pure oxygen is an oxidant), and fuel hydrogen has just produced hydrogen cation (or being proton) in the catalytic electrochemical reaction of anode region.Proton exchange membrane helps the hydrogen cation to move to the cathodic region from the anode region.In addition, proton exchange membrane is separated the air-flow and the oxygen containing air-flow of hydrogen fuel, they can not mixed mutually and produces explosion type reaction.
In the cathodic region, oxygen obtains electronics on catalyst surface, forms anion, and moves the hydrogen cation reaction of coming, reaction of formation product water with the anode region.In the Proton Exchange Membrane Fuel Cells that adopts hydrogen, air (oxygen), anode reaction and cathode reaction can be expressed in order to following equation:
Anode reaction: H
2→ 2H
++ 2e
Cathode reaction: 1/2O
2+ 2H
++ 2e → H
2O
In typical Proton Exchange Membrane Fuel Cells, membrane electrode (MEA) generally all is placed in the middle of the pole plate of two conductions, and quarter is milled by die casting, punching press or machinery in the surface that every guide plate contacts with membrane electrode, and formation is the guiding gutter of one or more at least.These guide plates can above metal material pole plate, also can be the pole plate of graphite material.Fluid duct on these guide plates and guiding gutter import fuel and oxidant the anode region and the cathodic region on membrane electrode both sides respectively.In the structure of a Proton Exchange Membrane Fuel Cells monocell, only there is a membrane electrode, the membrane electrode both sides are respectively the guide plate of anode fuel and the guide plate of cathode oxidant.These guide plates are both as current collector plate, also as the mechanical support on membrane electrode both sides, guiding gutter on the guide plate acts as a fuel again and enters the passage of anode, cathode surface with oxidant, and as the passage of taking away the water that generates in the fuel cell operation process.
In order to increase the gross power of whole Proton Exchange Membrane Fuel Cells, two or more monocells can be connected into battery pack or be unified into battery pack by the mode that tiles usually by straight folded mode.In straight folded, in-line battery pack, can there be guiding gutter on the two sides of a pole plate, and wherein one side can be used as the anode guide face of a membrane electrode, and another side can be used as the cathode diversion face of another adjacent membranes electrode, and this pole plate is called bipolar plates.A series of monocell connects together by certain way and forms a battery pack.Battery pack tightens together by front end-plate, end plate and pull bar usually and becomes one.
A typical battery stack generally includes: the water conservancy diversion import and the flow-guiding channel of (1) fuel and oxidant gas are distributed to fuel (hydrogen-rich gas that obtains as hydrogen, methyl alcohol or methyl alcohol, natural gas, gasoline) and oxidant (mainly being oxygen or air) in the guiding gutter of each anode, cathode plane equably after reforming; (2) import and export and the flow-guiding channel of cooling fluid (as water) are evenly distributed to cooling fluid in each battery pack inner cooling channel, and the heat absorption that hydrogen in the fuel cell, the exothermic reaction of oxygen electrochemistry are generated is also taken battery pack out of and dispelled the heat; (3) outlet of fuel and oxidant gas and corresponding flow-guiding channel, fuel gas and oxidant gas are when discharging, and portability goes out the liquid that generates in the fuel cell, the water of steam state.Usually, the import and export of all fuel, oxidant, cooling fluid are all opened on the end plate of fuel battery or on two end plates.
Proton Exchange Membrane Fuel Cells both can be used as the dynamical system of delivery vehicles such as car, ship, can be used as movable type or stationary power generation station again.
Proton Exchange Membrane Fuel Cells generally is made up of several monocells, these monocells are coupled together the formation pem fuel cell stack in the mode of serial or parallel connection, and pem fuel cell stack and other operation back-up systems are combined constitutes whole Proton Exchange Membrane Fuel Cells electricity generation system.
As Fig. 1 is the membrane electrode that has now in the Proton Exchange Membrane Fuel Cells monocell, and it comprises air inlet 1a, water inlet 2a, hydrogen inlet 3a, electrode activity zone 4a, air gas outlet 5a, delivery port 6a, hydrogen gas outlet 7a; As Fig. 2 is the guide plate that has now in the Proton Exchange Membrane Fuel Cells monocell, and it comprises air inlet 1a, water inlet 2a, hydrogen inlet 3a, runner 8a, air gas outlet 5a, delivery port 6a, hydrogen gas outlet 7a; As Fig. 3 is the fuel cell pack that a kind of several monocells connect with series system, and it comprises panel 9a, the first current collecting master board 10a, battery pile 11a, the second current collecting master board 12a, load 13a; Pem fuel cell stack can be made up of several monocell series systems, also can several monocell series connection constitute a unit, again several this unit are constituted fuel cell pack as Fig. 4 with parallel form, this fuel cell pack comprises the first current collecting master board 10a, battery pile 11a, the second current collecting master board 12a, insulation board 14a; The pem fuel cell stack of above Fig. 3, Fig. 4 indication all relates to two or polylith current collecting master board, is respectively the positive and negative or negative, positive current collecting master board in the fuel cell pack.These two current collecting master boards have following two kinds of effects:
1, the fuel-cell single-cell of several serial or parallel connections or the electric current of whole fuel cell pack are extracted, constitute the positive and negative electrode of conducting external current;
2, hole, various fluids road is also arranged on the current collecting master board, can allow the various fluids of fuel cell freely pass through, the same size with pod apertures on the guide plate of this fluid bore, current collecting master board size are identical with guide plate size in the fuel cell pack basically.
Current collecting master board in the present various fuel cell pack all adopts very special material in order to reach above two kinds of effects, for example, and metallic gold, metal platinum or adopt other metals such as the method for stainless steel, copper, aluminium, gold-plated, platinum.Adopt these materials, electric conductivity is very good, and at various fluids the electrochemical corrosion reaction can not take place during by current collecting master board and produces the metal ion that fuel cell is endangered.But these materials are very expensive as noble metals such as gold, platinum, electroplate on materials such as other metallic coppers, stainless steel, aluminium, and price is also more expensive, and inconvenient.
If directly adopt stainless steel, metallic copper, aluminum as current collecting master board, electrochemical corrosion can take place at various fluids during by current collecting master board, then can produce metal ion to fuel cell harm.
In order to overcome above-mentioned technological deficiency, the patent of Shanghai supernatural power scientific ﹠ technical corporation " a kind of compound current collecting master board of high-efficiency anticorrosive that is used for fuel cell " (China Patent No. is 02265853.X) has adopted a kind of inexpensive, corrosion resistant current collecting master board, this current collecting master board can be divided into a plurality of fundamental regions: the material on current collecting master board zone A and the zone C is corrosion-resistant non-conducting material, plastics for example, epoxy resin board, glass etc., and the material on the area B is good electric conducting material, aluminium for example, copper, zinc, titanium, zone A, zone C and area B bond together by certain mode, and can isolate mutually by encapsulant, can not leak into area B when making various fluids by regional A and zone C, area B can be isolated fully with media such as air and water like this, the electrochemical corrosion reaction does not take place in the afflux conduction, just in case corrode, the ion of generation can seepage not enter each fluid passage and the pollution feul battery yet.Each zone of this compound current collecting master board equates on thickness.
But the technology of the compound current collecting master board of this high-efficiency anticorrosive also has certain technological deficiency:
1. the compound current collecting master board of this high-efficiency anticorrosive is that the different materials by zones of different constitutes, and is relatively more inconvenient on making;
2. when fuel cell pack assembles, if when having fuel hydrogen, oxidant air, cooling fluid import and export on the front end-plate of fuel cell pack or end plate, just sealing device should be arranged between forward and backward end plate of fuel cell and the current collecting master board so, assurance allows three kinds into and out of fluid during by the pod apertures on current collecting master board and the end plate, fluid can not leak out between current collecting master board and end plate, and a kind of often rubber seal of this sealing device, trouble not only, and in the repeated disassembled and assembled process easy ageing failure.When fuel cell is integrated, also relate to the sealing of central collector plate and current collecting master board, guide plate, the process complexity, the sealing difficulty, and also contact resistance is very big.
The utility model content
The purpose of this utility model is exactly that a kind of compact conformation, anticorrosion, fuel cell complex that contact resistance is little are provided in order to overcome the defective that above-mentioned prior art exists.
The purpose of this utility model can be achieved through the following technical solutions: a kind of fuel cell complex, it is characterized in that, this complex comprises fluid distributing board, current collecting master board, guide plate, described fluid distributing board one or both sides are provided with a concave shaped space, in this concave shaped space, current collecting master board is set, and current collecting master board surface is concordant with the fluid distributing board side, before the described current collecting master board on the respective face of adjacent with it guide plate and the fluid distributing board non-concave shaped space position adhering and sealing connect into a complex.
Described fuel cell pack comprises monocell heap and integrated form battery heap, and described integrated form battery is piled and comprised that at least two groups are arranged at the forward and backward of central collector plate both sides or homonymy, the fuel cell pack of left and right or upper and lower position.
Described fuel cell pack is the monocell heap, the fluid distributing board of this monocell heap is an end plate before and after the fuel cell pack, this front and back end plate one side is provided with concave shaped space, in this concave shaped space, current collecting master board is set, and the current collecting master board surface is concordant with end plate side, front and back, the concave shaped space position periphery at end plate two ends is provided with hydrogen and passes in and out duct, air turnover duct, cooling water turnover duct before and after the described fuel cell pack, and on the side, duct of this concave shaped space position periphery the guide plate adhesive sealing adhesive layer that the front and back end plate is adjacent is set.
Described fuel cell pack is integrated form battery heap, the fluid distributing board of this integrated form battery heap is fuel cell pack central authorities collector plate, these central authorities collector plate both sides are provided with concave shaped space, in this concave shaped space, current collecting master board is set, and the current collecting master board surface is concordant with central collector plate two sides, the concave shaped space position periphery of described central collector plate both sides is provided with hydrogen turnover duct, air passes in and out duct, cooling water turnover duct, and at the other guide plate adhesive sealing adhesive layer that the front and back end plate is adjacent that is provided with in this periphery duct, concave shaped space position.
The close-connected with it guide plate in described central collector plate both sides, a side is an airflow guiding slot number plate, opposite side is a hydrogen flow guiding slot number plate.
Described current collecting master board be provided with at least one from top or from a left side and/or right electric current of drawing draw ear.
Described electric current is drawn ear and is provided with at least one connecting hole.
Described fluid distributing board one or both sides are provided with a concave shaped space by the geomery of current collecting master board, and described current collecting master board is embedded to be adhesively fixed with fluid distributing board in this concave shaped space and by adhesive and is connected.
Described current collecting master board is arranged on the concave shaped space position of fluid distributing board, and the guide plate adjacent with fluid distributing board is arranged on the concave shaped space peripheral position of fluid distributing board, becomes a complex.
The utility model is owing to adopted above technical scheme, being about to current collecting master board is embedded in the fluid distributing board, and guide plate and fluid distributing board that will be adjacent with fluid distributing board be gluing, guide plate and current collecting master board are fitted tightly, good sealing effect, fluid enters the respective streams body opening of guide plate from the fluid bore on the fluid distributing board, can not flow into current collecting master board, the corrosion current collecting master board, make current collecting master board keep bright and clean, thereby guide plate is little with the contact resistance that this current collecting master board contacts; When a plurality of piles are assembled, guide plate one side that current collecting master board is close to the collector plate both sides by central authorities is an airflow guiding slot number plate, opposite side must be hydrogen flow guiding slot number plate, make the both positive and negative polarity of central collector plate both sides pile not stride the pile projected current and do not need to be provided with in addition lead directly by central collector plate butt joint.Compared with prior art, the utlity model has anticorrosion, good seal, contact resistance is little, cost is low, advantages such as easy accessibility.
Description of drawings
Fig. 1 is the structural representation of membrane electrode in the existing fuel-cell single-cell;
Fig. 2 is the structural representation of guide plate in the existing fuel-cell single-cell;
Fig. 3 constitutes the structural representation of fuel cell pack for existing several monocells that connect with series system;
Fig. 4 constitutes the structural representation of fuel cell pack for existing several monocells that connect with parallel way;
Fig. 5 is the structural representation of the fuel cell pack of the utility model embodiment 1;
Fig. 6 is current collecting master board and fluid distributing board among Fig. 5, the guide plate structural representation before compound;
Fig. 7 is the structural representation after compound among Fig. 6;
Fig. 8 is the structural representation of the integrated fuel cell pile of the utility model embodiment 2;
Fig. 9 is current collecting master board and central collector plate among Fig. 8, the guide plate structural representation before compound;
Figure 10 is the structural representation after compound among Fig. 9.
Embodiment
The utility model is described in further detail below in conjunction with the accompanying drawings and the specific embodiments.
Shown in Fig. 5～7, a kind of fuel cell complex, this fuel cell pack comprises pile 1, fluid distributing board, this fluid distributing board comprises fuel cell pack front end-plate 21, end plate 22, front and back end plate 21,22 1 sides have concave shaped space 211, in this concave shaped space, inlay current collecting master board 31,32, with current collecting master board 31,32 are adhesive in front end-plate 21 respectively, the concave shaped space position of end plate 22, and the surface of the current collecting master board after embedding is concordant with end plate side, front and back, current collecting master board 31,32 are provided with an electric current of drawing from a left side draws ear 311,321, this electric current is drawn ear 311,321 are provided with connecting hole 312,322, the non-concave shaped space position 212 at end plate two ends is provided with hydrogen turnover duct 41 before and after the described fuel cell pack, 42, air turnover duct 43,44, cooling water turnover duct 45,46, and otherly in this duct adhesive layer 5 is set, the airflow guiding slot number plate 6 sticking sealings that front end-plate 21 is adjacent, the sticking sealing of the hydrogen flow guiding slot number plate that end plate 22 is adjacent.
Fig. 6 is the airflow guiding slot number plate that is adjacent before the front end-plate 21 of fuel cell and current collecting master board 31 and this current collecting master board 31 6 structural representations before compound, by adhesive layer is set between front end-plate 21 and current collecting master board 31 front end-plate 21 and current collecting master board 31 are glued together, and adhesive layer is set in the non-concave shaped space position at front end-plate 21 two ends airflow guiding slot number plate 6 is become a composite monolithic with front end-plate 21 and current collecting master board 31 are gluing, as shown in Figure 7.In like manner pass through the airflow guiding slot number plate 6 that is adjacent before end plate 22 current collecting master boards 32 and this current collecting master board 32 gluing compound in aggregates.
Embodiment 2
Shown in Fig. 8～10, a kind of fork truck is with the fuel cell of the integrated assembling of two piles, comprise two battery pile 1,1 ', fluid distributing board, this fluid distributing board comprises front end-plate 21, end plate 22, central collector plate 23, current collecting master board 31,32,33, the electric current that current collecting master board is provided with draw ear 311,321,331, electric current draw connecting hole 312,322,332, described central collector plate 23 both sides side mid portions that ear is provided with mill dig out one rectangular-shaped, about long 20cm, wide 10cm, the concave shaped space of dark 3mm; In this concave shaped space, inlay long 20cm, wide 10cm, approximately 2.9mm is thick, just can put the current collecting master board 33 of above-mentioned concave shaped space into, current collecting master board (red copper material) 33 is coated epoxy glue to be put above-mentioned concave shaped space into and polishes after 80 ℃ of curing of high temperature again, make central collector plate 23 be in same plane with current collecting master board 33, and be respectively equipped with two electric currents on two current collecting master boards 33 of central collector plate 23 both sides and draw ear 331, electric current is drawn the connecting hole 332 that ear is provided with, connect respective connecting 332 by conductive lever 8, make two battery pile 1,1 ' series connection, the non-concave shaped space position of described central collector plate both sides is provided with hydrogen and enters duct 41, air enters duct 43, cooling water goes out duct 46, described front end-plate 21, end plate 22 is provided with hydrogen and goes out duct 42, air goes out duct 44, cooling water enters duct 45, and in each duct the other adhesive layer 5 that is provided with, make the central collector plate 23 airflow guiding slot number plate 6 adjacent, hydrogen flow guiding slot number plate 7 formation one composite monolithics glued together with its both sides.As Fig. 9 is central collector plate and current collecting master board, the schematic diagram before guide plate is compound, and Figure 10 is central collector plate and current collecting master board, the schematic diagram after guide plate is compound.
In addition before front end-plate 21, end plate 22 and current collecting master board 31,32 and the end plate complex method of adjacent corresponding guide plate with last same.
Described current collecting master board is embedded in the fluid distributing board, and guide plate and fluid distributing board that will be adjacent with fluid distributing board be gluing, guide plate and current collecting master board are fitted tightly, good sealing effect, fluid enters the respective streams body opening of guide plate from the fluid bore on the fluid distributing board, can not flow into current collecting master board, the corrosion current collecting master board, make current collecting master board keep bright and clean, thereby guide plate is little with the contact resistance that this current collecting master board contacts; When a plurality of piles are assembled, guide plate one side that current collecting master board is close to the collector plate both sides by central authorities is an airflow guiding slot number plate, opposite side must be hydrogen flow guiding slot number plate, make the both positive and negative polarity of central collector plate both sides pile not stride the pile projected current and do not need to be provided with in addition lead directly by central collector plate butt joint.
Described fuel cell pack is that integrated form battery heap comprises the monocell heap, about two battery pile or upper and lower settings, four battery pile all around or upper and lower settings, and other a plurality of battery pile are all around and/or upper and lower settings.
Claims (9)
1. fuel cell complex, it is characterized in that, this complex comprises fluid distributing board, current collecting master board, guide plate, described fluid distributing board one or both sides are provided with a concave shaped space, in this concave shaped space, current collecting master board is set, and current collecting master board surface is concordant with the fluid distributing board side, before the described current collecting master board on the respective face of adjacent with it guide plate and the fluid distributing board non-concave shaped space position adhering and sealing connect into a complex.
2. a kind of fuel cell complex according to claim 1, it is characterized in that, described fuel cell pack comprises monocell heap and integrated form battery heap, described integrated form battery heap comprises that at least two groups are arranged at the forward and backward of central collector plate both sides or homonymy, the fuel cell pack of left and right or upper and lower position.
3. a kind of fuel cell complex according to claim 1, it is characterized in that, described fuel cell pack is the monocell heap, the fluid distributing board of this monocell heap is an end plate before and after the fuel cell pack, this front and back end plate one side is provided with concave shaped space, in this concave shaped space, current collecting master board is set, and the current collecting master board surface is concordant with end plate side, front and back, the concave shaped space position periphery at end plate two ends is provided with hydrogen turnover duct before and after the described fuel cell pack, air turnover duct, cooling water turnover duct, and the guide plate adhesive sealing adhesive layer that end plate is adjacent before and after the other setting in the duct of this concave shaped space position periphery makes.
4. a kind of fuel cell complex according to claim 1, it is characterized in that, described fuel cell pack is integrated form battery heap, the fluid distributing board of this integrated form battery heap is fuel cell pack central authorities collector plate, these central authorities collector plate both sides are provided with concave shaped space, in this concave shaped space, current collecting master board is set, and the current collecting master board surface is concordant with central collector plate two sides, the concave shaped space position periphery of described central collector plate both sides is provided with hydrogen turnover duct, air turnover duct, cooling water turnover duct, and at the other guide plate adhesive sealing adhesive layer that the front and back end plate is adjacent that is provided with in this periphery duct, concave shaped space position.
5. a kind of fuel cell complex according to claim 4 is characterized in that, the close-connected with it guide plate in described central collector plate both sides, and a side is an airflow guiding slot number plate, opposite side is a hydrogen flow guiding slot number plate.
6. a kind of fuel cell complex according to claim 1 is characterized in that, described current collecting master board be provided with at least one from top or from a left side and/or right electric current of drawing draw ear.
7. a kind of fuel cell complex according to claim 6 is characterized in that described electric current is drawn ear and is provided with at least one connecting hole.
8. a kind of fuel cell complex according to claim 1, it is characterized in that, described fluid distributing board one or both sides are provided with a concave shaped space by the geomery of current collecting master board, and described current collecting master board is embedded to be adhesively fixed with fluid distributing board in this concave shaped space and by adhesive and is connected.
9. a kind of fuel cell complex according to claim 1, it is characterized in that, described current collecting master board is arranged on the concave shaped space position of fluid distributing board, and the guide plate adjacent with fluid distributing board is arranged on the concave shaped space peripheral position of fluid distributing board, becomes a complex.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200715762U CN201051522Y (en) | 2007-06-25 | 2007-06-25 | A fuel battery compound body |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200715762U CN201051522Y (en) | 2007-06-25 | 2007-06-25 | A fuel battery compound body |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201051522Y true CN201051522Y (en) | 2008-04-23 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007200715762U Expired - Fee Related CN201051522Y (en) | 2007-06-25 | 2007-06-25 | A fuel battery compound body |
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| Country | Link |
|---|---|
| CN (1) | CN201051522Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108075163A (en) * | 2017-12-05 | 2018-05-25 | 新奥科技发展有限公司 | A kind of fuel cell pile and its assemble method |
| CN112687905A (en) * | 2020-12-26 | 2021-04-20 | 上海捷氢科技有限公司 | Fuel cell anode collector plate and fuel cell stack |
-
2007
- 2007-06-25 CN CNU2007200715762U patent/CN201051522Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108075163A (en) * | 2017-12-05 | 2018-05-25 | 新奥科技发展有限公司 | A kind of fuel cell pile and its assemble method |
| CN108075163B (en) * | 2017-12-05 | 2020-08-14 | 北京英博新能源有限公司 | Fuel cell stack and assembling method thereof |
| CN112687905A (en) * | 2020-12-26 | 2021-04-20 | 上海捷氢科技有限公司 | Fuel cell anode collector plate and fuel cell stack |
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