CN201060900Y - Non-water blocking pipeline device of fuel cell pack - Google Patents
Non-water blocking pipeline device of fuel cell pack Download PDFInfo
- Publication number
- CN201060900Y CN201060900Y CNU200720071684XU CN200720071684U CN201060900Y CN 201060900 Y CN201060900 Y CN 201060900Y CN U200720071684X U CNU200720071684X U CN U200720071684XU CN 200720071684 U CN200720071684 U CN 200720071684U CN 201060900 Y CN201060900 Y CN 201060900Y
- Authority
- CN
- China
- Prior art keywords
- pipeline
- fuel cell
- fluid
- cell pack
- fluid distributing
- 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.)
- Expired - Fee Related
Links
- 239000000446 fuel Substances 0.000 title claims abstract description 76
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 21
- 230000000903 blocking effect Effects 0.000 title 1
- 239000012530 fluid Substances 0.000 claims abstract description 58
- 239000001257 hydrogen Substances 0.000 claims abstract description 44
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 44
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 41
- 239000012809 cooling fluid Substances 0.000 claims abstract description 39
- 238000009434 installation Methods 0.000 claims description 8
- 238000009428 plumbing Methods 0.000 claims description 8
- 230000007306 turnover Effects 0.000 claims description 5
- 230000002349 favourable effect Effects 0.000 abstract 1
- 239000012528 membrane Substances 0.000 description 32
- 239000007800 oxidant agent Substances 0.000 description 17
- 230000001590 oxidative effect Effects 0.000 description 17
- 238000006243 chemical reaction Methods 0.000 description 11
- 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
- 239000003054 catalyst Substances 0.000 description 5
- 238000003487 electrochemical reaction Methods 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
- 229910052799 carbon Inorganic materials 0.000 description 4
- 150000001450 anions Chemical class 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 150000001768 cations Chemical class 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000010586 diagram 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
- 239000000047 product Substances 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 239000003570 air Substances 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 230000017525 heat dissipation Effects 0.000 description 2
- 238000001764 infiltration Methods 0.000 description 2
- 230000008595 infiltration Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000005012 migration Effects 0.000 description 2
- 238000013508 migration Methods 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000004020 conductor Substances 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
- 230000005518 electrochemistry Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 239000003502 gasoline Substances 0.000 description 1
- 239000007770 graphite material Substances 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 238000002407 reforming Methods 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 pipeline device of a fuel cell stack being uneasy to shut off water, which comprises a single cell stack or an integrated type cell stack, a fluid distributing plate, and a 3-in 3-out pipeline of a hydrogen inlet and outlet pipeline, an air inlet and outlet pipeline, and a cooling fluid inlet and outlet pipeline, wherein the fluid distributing plate comprises a central flow collecting plate, and a front/rear end fluid distributing plate, the 3-in 3-out pipeline is arranged on the fluid distributing plate of the fuel cell stack, wherein the hydrogen outlet pipeline, the air outlet pipeline, and the cooling fluid outlet pipeline are arranged at the lower end of the fluid distributing plate. Compared with the prior art, the utility model has the advantages that the utility model is favorable for the discharge of the fluid, and water shut off is uneasy to happen.
Description
Technical field
The utility model relates to fuel cell, relates in particular to a kind of plumbing installation that is difficult for the fuel cell pack of water blockoff.
Background technology
Electrochemical fuel cell is a kind of device that hydrogen fuel 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 electronics that the membrane electrode both sides can will take place to generate in the electrochemical reaction process with conductive body is drawn 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 block of flow guiding electrode plate contacts with membrane electrode, and formation is the guiding gutter of one or more at least.These flow guiding electrode plates can be the pole plates of metal material, also can be the pole plates of graphite material.Water conservancy diversion duct on these flow guiding electrode 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 the current collector motherboard, 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 (as hydrogen, methyl alcohol or the hydrogen-rich gas that obtained by 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, the heat absorption that hydrogen in the fuel cell, the exothermic reaction of oxygen electrochemistry are generated and take battery pack out of after dispel 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 can be used as the dynamical system of delivery vehicles such as all cars, ship, can make portable, portable, fixed Blast Furnace Top Gas Recovery Turbine Unit (TRT) again.The Proton Exchange Membrane Fuel Cells electricity generation system must comprise fuel cell pack, fuel hydrogen supply, air supply, cooling heat dissipation, various piece such as control and electric energy output automatically.Stable and the reliability of Proton Exchange Membrane Fuel Cells operation is very important to the application as car, ship power system or movable Blast Furnace Top Gas Recovery Turbine Unit (TRT).Stable and the reliability that wherein improves fuel cell pack is crucial.
At present, pem fuel cell stack in the design of each fluid passage, usually adopt sacrifice pole plate effectively utilize area, offer fluid bore in the same position of each membrane electrode and pole plate, and with each piece membrane electrode and pole plate through each fluid passage of superimposed composition.That is to say, be equipped with the fluid bore that fuel advances, fuel goes out, oxidant advances, oxidant goes out, cooling fluid advances, cooling fluid goes out on every membrane electrode and the pole plate, these membrane electrodes and guide plate are just formed fuel battery through vertical after superimposed, and the fuel that these fluid bore have just been formed fuel battery inside into and out of; Oxidant into and out of; Cooling fluid into and out of each fluid flow guiding passage, and these fluid passages be integrated into before or after the fuel battery form fuel inlet, fuel outlet on the end plate, oxidant inlet, oxidant outlet, cooling fluid import, cooling fluid outlet.
At present, hydrogen supply in the Proton Exchange Membrane Fuel Cells electricity generation system, air supply, three of cooling heat dissipation advances three and goes out the fluid distributing board 7 that pipeline all is arranged on fuel cell pack, 8 rear and front end, as shown in Figure 1, hydrogen inlet pipeline 1, air intlet pipeline 3, cooling fluid inlet ductwork 5 is arranged on the rear and front end of the front end-plate 7 of fuel cell pack, hydrogen outlet pipeline 2, air outlet slit pipeline 4, cooling fluid export pipeline 6 is arranged on the rear and front end of the end plate 8 of fuel cell pack, after fluid enters pile from the front and back end of fluid distributing board, after flowing through the baffler reaction, after compiling, flow out the climb front and back end of fluid distributing board, the fluid that will inevitably need bigger fluid pressure will flow to the baffler lower end is pressed onto certain altitude, could flow out from the fluid issuing that is arranged on the fluid distributing board front and back end, this design fluid discharge difficulty is bigger, easily causes water blockoff.
The utility model content
The purpose of this utility model is exactly a kind of plumbing installation that helps the fluid discharge, is difficult for the fuel cell pack that is difficult for water blockoff of water blockoff that provides in order to address the above problem.
The purpose of this utility model is achieved in that a kind of plumbing installation that is difficult for the fuel cell pack of water blockoff, comprise monocell heap or integrated form battery heap, fluid distributing board, hydrogen turnover pipeline, air turnover pipeline, three of cooling fluid turnover pipeline advances three settings that go out pipeline, it is characterized in that, described fluid distributing board comprises central collector plate, front/rear end fluid distributing board, described three advance three goes out on the fluid distributing board that pipeline is arranged on fuel cell pack, wherein the hydrogen outlet pipeline, the air outlet slit pipeline, the cooling fluid export pipeline is arranged on the lower end of fluid distributing board.
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.
Described fuel cell pack is the monocell heap, the fluid distributing board of this monocell heap is the front/rear end fluid distributing board of fuel cell pack, described hydrogen inlet pipeline, air intlet pipeline, cooling fluid inlet ductwork are arranged on the front/rear end fluid distributing board, and described hydrogen outlet pipeline, air outlet slit pipeline, cooling fluid export pipeline are arranged on the lower end of front/rear end fluid distributing board.
Described fuel cell pack is integrated form battery heap, the fluid distributing board of this integrated form battery heap comprises two rear end fluid distributing boards of central collector plate and corresponding two ends with it, described hydrogen inlet pipeline, air intlet pipeline, cooling fluid inlet ductwork are arranged on central collector plate or the two rear end fluid distributing boards, and described hydrogen outlet pipeline, air outlet slit pipeline, cooling fluid export pipeline are arranged on the lower end of central collector plate or two rear end fluid distributing boards.
Compared with prior art, the utility model is arranged on hydrogen outlet pipeline, air outlet slit pipeline, cooling fluid export pipeline the lower end of the fluid distributing board of fuel cell pack, make the reacted fluid of fuel cell pack under action of gravity, flow out pile naturally, it is unimpeded to have guaranteed that fluid flows, and is difficult for water blockoff.
Description of drawings
Fig. 1 is that three of prior art fuel cell advances three and goes out the pipeline schematic diagram;
Fig. 2 is three the advancing three and go out the pipeline schematic diagram of fuel cell of the utility model embodiment 1;
Fig. 3 is three the advancing three and go out the pipeline schematic diagram of fuel cell of the utility model embodiment 2.
Embodiment
Embodiment 1:
As shown in Figure 2, a kind of monocell fuel cell pack, comprise hydrogen inlet pipeline 1, hydrogen outlet pipeline 2, air intlet pipeline 3, air outlet slit pipeline 4, cooling fluid inlet ductwork 5, cooling fluid export pipeline 6, front end-plate 7, end plate 8, described hydrogen inlet pipeline 1, air intlet pipeline 3, cooling fluid inlet ductwork 5 are arranged on the rear and front end of the front end-plate 7 of fuel cell pack, and described hydrogen outlet pipeline 2, air outlet slit pipeline 4, cooling fluid export pipeline 6 are arranged on the lower end of the end plate 8 of fuel cell pack.Hydrogen, air, cooling fluid enter battery pile from front end-plate 7 rear and front ends respectively, after the reaction, flow out pile from end plate 8 lower ends.
Described hydrogen inlet pipeline 1, hydrogen outlet pipeline 2, air intlet pipeline 3, air outlet slit pipeline 4, cooling fluid inlet ductwork 5, cooling fluid export pipeline 6 can be separately positioned on the front and back end or the lower end of front end-plate 7, end plate 8 as required.
Embodiment 2:
As shown in Figure 3, a kind of integrated fuel cell pile of four piles, comprise hydrogen inlet pipeline 1, hydrogen outlet pipeline 2, air intlet pipeline 3, air outlet slit pipeline 4, cooling fluid inlet ductwork 5, cooling fluid export pipeline 6, central authorities' collector plate 9, end plate 10, described hydrogen inlet pipeline 1, air intlet pipeline 3, cooling fluid inlet ductwork 5 is arranged on the preceding two ends of the central collector plate 9 of fuel cell pack, described air outlet slit 4 is arranged on the lower end of central collector plate 9, described hydrogen outlet pipeline 2, cooling fluid export pipeline 6 is arranged on the lower end of end plate 10.Hydrogen, air, cooling fluid enter battery pile from central collector plate 9 front ends respectively, after the reaction, flow out pile from the lower end of central collector plate 9 or end plate 10.
Can be as required, hydrogen inlet pipeline 1, hydrogen outlet pipeline 2, air intlet pipeline 3, air outlet slit pipeline 4, cooling fluid inlet ductwork 5, cooling fluid export pipeline 6 are arranged on the front and back or the lower end of central collector plate 9 or end plate 10, guarantee that each fluid issuing gets final product in the lower end of central collector plate 9 or end plate 10.Utilize action of gravity, each fluid is discharged naturally, it is unimpeded to have guaranteed that fluid flows, and is difficult for water blockoff.
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 all around and/or upper and lower settings, hydrogen, air enter battery pile from the fluid distributing board rear and front end of fuel cell pack respectively, flow through in the fuel cell pack by after the air outlet slit of all guide plates and electrode, the air outlet passage and hydrogen outlet passage that hydrogen outlet is formed, through fluid distributing board and directly discharge from the fluid distributing board lower end.
Claims (4)
1. plumbing installation that is difficult for the fuel cell pack of water blockoff, comprise that monocell heap or integrated form battery heap, fluid distributing board, hydrogen turnover pipeline, air turnover pipeline, cooling fluid pass in and out three of pipeline and advance three settings that go out pipeline, it is characterized in that, described fluid distributing board comprises central collector plate, front/rear end fluid distributing board, described three advance three goes out on the fluid distributing board that pipeline is arranged on fuel cell pack, and wherein hydrogen outlet pipeline, air outlet slit pipeline, cooling fluid export pipeline are arranged on the lower end of fluid distributing board.
2. a kind of plumbing installation that is difficult for the fuel cell pack of water blockoff according to claim 1, it is characterized in that, 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 plumbing installation that is difficult for the fuel cell pack of water blockoff 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 the front/rear end fluid distributing board of fuel cell pack, described hydrogen inlet pipeline, air intlet pipeline, cooling fluid inlet ductwork are arranged on the front/rear end fluid distributing board, and described hydrogen outlet pipeline, air outlet slit pipeline, cooling fluid export pipeline are arranged on the lower end of front/rear end fluid distributing board.
4. a kind of plumbing installation that is difficult for the fuel cell pack of water blockoff 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 comprises two rear end fluid distributing boards of central collector plate and corresponding two ends with it, described hydrogen inlet pipeline, the air intlet pipeline, the cooling fluid inlet ductwork is arranged on central collector plate or the two rear end fluid distributing boards, described hydrogen outlet pipeline, the air outlet slit pipeline, the cooling fluid export pipeline is arranged on the lower end of central collector plate or two rear end fluid distributing boards.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU200720071684XU CN201060900Y (en) | 2007-06-26 | 2007-06-26 | Non-water blocking pipeline device of fuel cell pack |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU200720071684XU CN201060900Y (en) | 2007-06-26 | 2007-06-26 | Non-water blocking pipeline device of fuel cell pack |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201060900Y true CN201060900Y (en) | 2008-05-14 |
Family
ID=39409389
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU200720071684XU Expired - Fee Related CN201060900Y (en) | 2007-06-26 | 2007-06-26 | Non-water blocking pipeline device of fuel cell pack |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201060900Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113629283A (en) * | 2021-07-28 | 2021-11-09 | 江苏江淮动力有限公司 | Liquid tank assembly for connecting several groups of batteries to feed and discharge liquid |
| CN114122476A (en) * | 2021-11-29 | 2022-03-01 | 苏州市华昌能源科技有限公司 | End plate assembly, electric pile control system and fuel cell |
-
2007
- 2007-06-26 CN CNU200720071684XU patent/CN201060900Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113629283A (en) * | 2021-07-28 | 2021-11-09 | 江苏江淮动力有限公司 | Liquid tank assembly for connecting several groups of batteries to feed and discharge liquid |
| CN114122476A (en) * | 2021-11-29 | 2022-03-01 | 苏州市华昌能源科技有限公司 | End plate assembly, electric pile control system and fuel cell |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080514 Termination date: 20150626 |
|
| EXPY | Termination of patent right or utility model |