CN205985277U - Chargeable zinc air fuel cell - Google Patents
Chargeable zinc air fuel cell Download PDFInfo
- Publication number
- CN205985277U CN205985277U CN201620737265.4U CN201620737265U CN205985277U CN 205985277 U CN205985277 U CN 205985277U CN 201620737265 U CN201620737265 U CN 201620737265U CN 205985277 U CN205985277 U CN 205985277U
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- China
- Prior art keywords
- zinc
- pipeline
- battery cell
- fuel cell
- electrode
- 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.)
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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
- Y02E60/10—Energy storage using batteries
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Abstract
The utility model relates to a chargeable zinc air fuel cell comprises battery monomer, sponge grease zinc, charge metal electrode and air electrode, inside two cavities from top to bottom that are divided into of battery monomer, sponge grease zinc is placed to lower cavity, and the battery monomer surface of these sponge grease zinc both sides sets up the metal electrode that charges, air electrode respectively. The utility model discloses beneficial effect does: electrolyte passes through the feed liquor orifice flow and goes into to the pipeline II in, flow in the electrolyte space through the outage, heat conduction that the metal electrode that charges produced is to the zinc metal sponge in, the biological chemistry reaction is sent out with zinc metal sponge to electrolyte, the oxygen accessible air electrode that chemical reaction produced absorbs, produce gaseously behind chemical reaction, in flowing in pipeline I through the inlet port, go into to the electrolyte space in through the exhaust orifice flow, exhaust, the circulated electrolyte that supplyes, has the convenience of application, it is safe energy -conserving, light weight, the environmental protection is nontoxic, there are not advantages such as emission.
Description
Technical field
This utility model is related to water battery technical field, more particularly, to a kind of chargeable zinc/air fuel cell.
Background technology
With people to the understanding of environmental protection and pursuit, global scientist is making substantial amounts of opening for eco-friendly power source
Send out and research.Supply of electric power source now, sends out including solar electrical energy generation, wind-power electricity generation, hydroelectric generation, tidal power generation, underground heat
Electricity, thermal power generation and nuclear energy power generation.At present, thermal power generation and nuclear energy power generation are mainly to provide society stable electric energy supply
Source;However, thermal power generation and nuclear energy power generation have serious environmental pollution and the low problem of conversion efficiency, and solar energy is sent out
The ability for stable power-supplying in technology and equipment such as electricity, wind-power electricity generation, hydroelectric generation, tidal power generation or geothermal power generation also
Need to break through.Therefore, be converted to the fuel cell of electric power with chemical energy, gradually show up prominently.
Fuel cell is a kind of electric supply installation that the chemical energy of fuel is directly converted to electric energy, is similar to a kind of small power generation
Stand, the assembly of composition fuel cell is minimum to need battery body, two electrodes (electrode), electrolyte, electrolytic thin-membranes
(electrolyte membrane) and/or current collector (current collector) etc..In simple terms, electrode is fuel oxygen
Change the place with the electrochemical reaction generation of oxidant reduction, or the diffusion media of anode chemical fuel, and electrode is general
Anode (Anode) electrode and negative electrode (Cathode) electrode two parts can be divided into;And the function of electrolyte is to separate oxidant and go back
Former dose and proton conducting simultaneously.Additionally, current collector is also referred to as bipolar plates (bipolar plate), it has collected current, dredges
The effect led reacting gas and separate oxidant and reducing agent.
For metal air fuel cell (abbreviation metal-air battery) with metal and oxygen as fuel, it is by metal
The diffusion oxygen being imported with air pole carries out oxidation reaction, and produce electric energy after generate simultaneously metal-oxide, hydrogen and/
Or water.The electrochemical reaction being oxygen and metal due to the operation principles of metal-air battery, it has high performance price ratio
Characteristic, so be subject to the suitable attention of personal electric consumption market.
The R&D direction of common metal air cell manufacturer is conceived to how quickly and easily to carry out battery recycling and profit again
With, therefore the design form of its product to carry out group to a plurality of metal-air batteries nothing more than the housing accessory being transmission complexity
Dress, and consumer also also needs to start or close the running of metal-air battery product by extra control computer.
Problem deserving of attention is, complicated housing accessory and extra control computer not only can make the life of metal-air battery product
Produce high cost, and can make metal-air battery product that consumer cannot be allowed to carry with.
Meanwhile, for the internal structure of metal-air battery, manufacturer in order to obtain preferably packaging effect and safety, because
And increased complexity packaging mechanism, result in battery volume increase and cannot rapid disassembling or recovery, and if contact or simultaneously
Join multiple fuel cells, or formed along with other fuel tanks hybrid power mechanism when, its device is packaged
Also lifted therewith with the difficulty of disassembly & recycling.If additionally, battery run out of gas in addition it is also necessary to be passed to battery design manufacturer or
It is the maintenance manufacturer of battery, more loaded down with trivial details step is dismantled and encapsulates with complexity again, more cause manpower and machine cost
Increase.
From the foregoing, it will be observed that the complicated packaging mechanism of metal-air battery makes to run out of gas, battery has economic worth reaction
Metal (oxidized metal) afterwards is not easy to remove, battery body or shell mechanism also cannot recycling, cause the pole of resource
Big waste.
Therefore, for the above, need prior art is reasonably improved.
Utility model content
For disadvantages described above, this utility model provides a kind of application convenience, energy-saving safe, lightweight, environment-protecting asepsis, no arranges
The chargeable zinc/air fuel cell put, to solve many deficiencies of prior art.
For achieving the above object, this utility model employs the following technical solutions:
A kind of chargeable zinc/air fuel cell, by battery cell, sponge grease zinc, charging metal electrode and air electricity
Pole forms, and is divided into upper and lower two chambers, upper chamber's side setting pipeline I, lower chambers side setting pipe inside described battery cell
Road II;Lower chambers between described pipeline I and pipeline II place sponge grease zinc, outside the battery cell of this sponge grease zinc both sides
Surface is respectively provided with charging metal electrode, air electrode;Steam vent is passed through with battery cell upper chamber even in described pipeline I upper end
Logical, pipeline I lower end is connected with battery cell lower chambers by air inlet, and inlet opening and battery cell are passed through in described pipeline II upper end
Lower chambers connect, and pipeline II lower end is connected with battery cell lower chambers by outage, thus the cyclic electrolysis liquid space being formed.
Correspondingly, described outage is in sponge grease zinc bottom;
Pipeline is carried, battery cell upper end is provided with vent valve inside described battery cell;Battery cell top carries adds
The hole of electrolyte.
The having the beneficial effect that of chargeable zinc/air fuel cell described in the utility model:Electrolyte is flowed into by inlet opening
To in pipeline II, it is flowed into electrolysis liquid space through outage, the heat that charging metal electrode produces is transmitted in zinc metal sponge,
There is chemical reaction with zinc metal sponge in electrolyte, the oxygen that chemical reaction produces can be absorbed by air electrode, through chemistry
Produce gas after reaction, be flowed in pipeline I by air inlet, be flowed in electrolysis liquid space by steam vent, be exhausted,
Capable of circulation carry out supplementing electrolyte, have the advantages that to apply convenience, energy-saving safe, lightweight, environment-protecting asepsis, no discharge.
Brief description
Below according to accompanying drawing, this utility model is described in further detail.
Fig. 1 is the structural representation of chargeable zinc/air fuel cell described in this utility model embodiment;
Fig. 2 is that the air inlet of chargeable zinc/air fuel cell described in this utility model embodiment is illustrated with steam vent arrangement
Figure;
Fig. 3 is the partial exploded view of chargeable zinc/air fuel cell described in this utility model embodiment.
In figure:
1st, battery cell;2nd, inlet opening;3rd, venthole;4th, steam vent;5th, outage;6th, pipeline I;7th, pipeline II;8th, sea
Continuous metallic zinc;9th, charging metal electrode;10th, air electrode.
Specific embodiment
Embodiment 1
As Figure 1-3, the chargeable zinc/air fuel cell described in this utility model embodiment, by battery cell 1, sea
Continuous metallic zinc 8, charging metal electrode 9 and air electrode 10 form, and are divided into upper and lower two chambers inside described battery cell 1,
Upper chamber's side setting pipeline I 6, lower chambers side arranges pipeline II 7;Battery compartment between described pipeline I 6 and pipeline II 7
Middle placement sponge grease zinc 8, battery cell 1 outer surface of this sponge grease zinc 8 both sides is respectively provided with charging metal electrode 9, uses
In the air electrode 10 absorbing oxygen;
Correspondingly, described pipeline I 6 upper end is connected with battery cell 1 upper chamber by steam vent 4, and pipeline I 6 lower end is passed through
Venthole 3 is connected with battery cell 1 lower chambers, and described pipeline II 7 upper end is connected with battery cell 1 lower chambers by inlet opening 2,
Pipeline II 7 lower end is connected with battery cell 1 lower chambers by outage 5 and this outage 5 is in sponge grease zinc 8 bottom,
By arranging the electrolysis liquid space that formed with corresponding pipeline of upper and lower two chambers in order to allow electrolyte recycling capable of circulation.
Correspondingly, described battery cell 1 is internal flows to lower section with pipeline in order to the electrolyte above making, and allows simultaneously
If gas produces when charging, the space of top can be discharged into;Described battery cell 1 upper end is provided with vent valve, and battery cell 1 pushes up
Portion carries the hole adding electrolyte.
Embodiment 2
As Figure 1-3, the chargeable zinc/air fuel cell described in this utility model embodiment, by battery cell 1, sea
Continuous metallic zinc 8, charging metal electrode 9 and air electrode 10 form, and place sponge grease in described battery cell 1 battery compartment
Zinc 8, battery cell 1 outer surface of this sponge grease zinc 8 both sides is respectively provided with charging metal electrode 9, the sky for absorbing oxygen
Pneumoelectric pole 10;
It is respectively provided with steam vent 4, venthole 3, described pipe between described pipeline I 6 upper/lower terminal and battery cell 1 inner chamber
It is respectively provided with inlet opening 2, outage 5 between road II 7 upper/lower terminal and battery cell 1 inner chamber and this outage 5 is in sponge
Metallic zinc 8 bottom.
Chargeable zinc/air fuel cell described in above this utility model embodiment, during work, electrolyte passes through feed liquor
Hole 2 is flowed in pipeline II 7, is flowed into electrolysis liquid space through outage 5, and the heat that charging metal electrode 9 produces is transmitted to sea
In continuous metallic zinc 8, there is chemical reaction with sponge grease zinc 8 in electrolyte, and the oxygen that chemical reaction produces can pass through air electrode
10 absorptions;Produce gas after after chemical reaction, be flowed in pipeline I 6 by air inlet 3, electrolysis is flowed into by steam vent 4
In liquid space, it is exhausted, capable of circulation carry out supplementing electrolyte.
The above-mentioned description to embodiment is for the ease of those skilled in the art it will be appreciated that and applying this
Case technology, person skilled in the art obviously can make various modifications to these examples easily, and described herein one
As principle be applied in other embodiments without through performing creative labour.Therefore, this case is not limited to above example, for
Improvement and modification that this case is made, for example, the structure design of the improvement of battery case shape, anode and battery cathode, if
No produce beyond the beneficial effect outside this case scope, then all should be in the protection domain of this case.
Claims (5)
1. a kind of chargeable zinc/air fuel cell is it is characterised in that by battery cell (1), sponge grease zinc (8), charge gold
Belong to electrode (9) and air electrode (10) composition, inside described battery cell (1), be divided into upper and lower two chambers, upper chamber side
Setting pipeline I (6), lower chambers side arranges pipeline II (7);Lower chambers between described pipeline I (6) and pipeline II (7) are placed
Sponge grease zinc (8), battery cell (1) outer surface of this sponge grease zinc (8) both sides be respectively provided with charging metal electrode (9),
Air electrode (10);Described pipeline I (6) upper end is connected with battery cell (1) upper chamber by steam vent (4), under pipeline I (6)
End is connected with battery cell (1) lower chambers by venthole (3), and inlet opening (2) and battery list are passed through in described pipeline II (7) upper end
Body (1) lower chambers connect, and pipeline II (7) lower end is connected with battery cell (1) lower chambers by outage (5), thus formed
Cyclic electrolysis liquid space.
2. chargeable zinc/air fuel cell according to claim 1 it is characterised in that:Described outage (5) is in sea
Continuous metallic zinc (8) bottom.
3. chargeable zinc/air fuel cell according to claim 1 it is characterised in that:Described battery cell (1) is internal
With pipeline.
4. chargeable zinc/air fuel cell according to claim 1 it is characterised in that:Described battery cell (1) upper end
It is provided with vent valve.
5. chargeable zinc/air fuel cell according to claim 1 it is characterised in that:Described battery cell (1) top
With the hole adding electrolyte.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620737265.4U CN205985277U (en) | 2016-07-13 | 2016-07-13 | Chargeable zinc air fuel cell |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620737265.4U CN205985277U (en) | 2016-07-13 | 2016-07-13 | Chargeable zinc air fuel cell |
Publications (1)
Publication Number | Publication Date |
---|---|
CN205985277U true CN205985277U (en) | 2017-02-22 |
Family
ID=58024141
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201620737265.4U Expired - Fee Related CN205985277U (en) | 2016-07-13 | 2016-07-13 | Chargeable zinc air fuel cell |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN205985277U (en) |
-
2016
- 2016-07-13 CN CN201620737265.4U patent/CN205985277U/en not_active Expired - Fee Related
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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: 20170222 |
|
CF01 | Termination of patent right due to non-payment of annual fee |