CN103515657A - Battery - Google Patents

Battery Download PDF

Info

Publication number
CN103515657A
CN103515657A CN201210208943.4A CN201210208943A CN103515657A CN 103515657 A CN103515657 A CN 103515657A CN 201210208943 A CN201210208943 A CN 201210208943A CN 103515657 A CN103515657 A CN 103515657A
Authority
CN
China
Prior art keywords
electrolyte
ion
battery
battery according
micelle
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.)
Granted
Application number
CN201210208943.4A
Other languages
Chinese (zh)
Other versions
CN103515657B (en
Inventor
陈璞
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Positec Power Tools Suzhou Co Ltd
Original Assignee
Positec Power Tools Suzhou Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Positec Power Tools Suzhou Co Ltd filed Critical Positec Power Tools Suzhou Co Ltd
Priority to CN201710381889.6A priority Critical patent/CN107331905B/en
Priority to CN201210208943.4A priority patent/CN103515657B/en
Publication of CN103515657A publication Critical patent/CN103515657A/en
Application granted granted Critical
Publication of CN103515657B publication Critical patent/CN103515657B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/36Accumulators not provided for in groups H01M10/05-H01M10/34
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0085Immobilising or gelification of electrolyte
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Abstract

The invention discloses a battery comprising a positive electrode, a negative electrode and an electrolyte solution. The electrolyte solution comprises an electrolyte and at least one of an aqueous solution or an alcoholic solution which can dissolve the electrolyte and make the electrolyte ionize; the electrolyte solution also comprises silicon dioxide which can make the electrolyte solution gelate. Silicon dioxide can make the electrolyte solution become gelatinous, therefore, the solution does not leak no matter how the battery is placed, so that the battery is safe and reliable, longer in service life, and convenient to transport and store.

Description

Battery
Technical field
The invention belongs to electrochemical energy storage field, be specifically related to a kind of battery.
Background technology
The extensive utilization of the mankind to new forms of energy, has caused the expansion rapidly in secondary cell market.In current new forms of energy system to secondary cell require ubiquitous.No matter be electric automobile, wind energy, solar grid-connected or peak load regulation network, is all badly in need of a kind of cheapness, reliable, the secondary cell that safety and life-span are long.The secondary cell developing at present mainly concentrates on lithium ion battery, high temperature sodium-sulphur battery, sodium nickel chlorine battery and vanadium flow battery.These batteries all have advantages of separately, and such as lithium ion battery with high-temperature sodium sulphur battery life is long and energy density is high, vanadium flow battery possesses the unlimited life-span etc. especially in theory.But which kind of battery no matter, all cannot meet simultaneously cheap, reliable, the requirement that safety and life-span are long.Traditional lithium ion battery is too expensive, and has potential safety hazard; High-temperature sodium sulphur battery manufacture technical threshold is high, fetch long price; The multinomial technical bottleneck of vanadium flow battery all fails to obtain breakthrough etc. at present.
Many researchers is all devoted to the research of aquo-lithium ion battery for this reason, hope significantly reduces the cost of lithium ion battery with this, and proposed some and take LiMn2O4 as anodal, the oxide of vanadium such as LiV3O8 etc. are the battery that negative pole, water are electrolyte, but the easy leakage of this type of battery, in the time of safe not, also reduce the capacity of battery, thereby made the life-span shorter.In addition, be also inconvenient to carry and store.
Summary of the invention
The present invention aim to provide a kind of safe and reliable, the life-span is longer, and the battery of convenient carrying and storage.
The invention provides a kind of battery, comprise positive pole, negative pole and electrolyte, described electrolyte comprises electrolyte and can dissolve described electrolyte and make the aqueous solution of described electrolyte ionization or at least one in alcoholic solution; Described electrolyte also comprises the silicon dioxide that makes electrolyte gel.
Beneficial effect of the present invention: silicon dioxide makes electrolyte gel.Like this, in any case place not can leakage for battery, thereby make that cell safety is reliable, the life-span is longer, convenient carrying and storage.
Preferably, the aerosil of described silicon dioxide for being prepared by vapor phase method by silicon tetrachloride.
Preferably, described silicon dioxide is prepared by silicate.
Preferably, described silicate is selected from a kind of in alumina silicate, sodium metasilicate, potassium silicate, calcium silicates, silicic acid phosphorus, Magnesiumaluminumsilicate, lithium magnesium silicate.
Preferably, after described electrolyte gel, have silica particle, the particle diameter of described micelle is not more than 20nm.
Preferably, the particle diameter of described micelle is between 10~20nm.
Preferably, the particle diameter of described micelle is between 5~7nm.
Preferably, described micelle have particle diameter at first group between 10~20nm and particle diameter second group between 5~7nm.
Preferably, the particle diameter of described micelle is less than 5nm.
Preferably, the weight accounting of described silicon dioxide in described electrolyte is 0.2%~20%.
Preferably, described electrolyte also comprises deflocculant, and described deflocculant is selected from least one in polyvinyl alcohol, dextrin, glycerine, polyethylene glycol, polyacrylamide and AEO.
Preferably, described positive pole comprises plus plate current-collecting body and participates in the positive active material of electrochemical reaction, described positive active material can be reversible deviate from-embedded ion; Described negative pole at least comprises negative current collector; Described electrolyte can ionize out at least one charge and discharge process and reduce-deposit and be oxidized at described negative pole-active ion that dissolves, described active ion comprises metal ion, and described metal is selected from least one in Zn, Fe, Cr, Cu, Mn, Ni, Sn.
Preferably, described metal ion is present in described electrolyte with the form of the mixture of sulfate, acetate or sulfate and acetate.
Preferably, lithium ion, sodium ion, zinc ion or magnesium ion can reversiblely be deviate from-embed to described positive active material.
Embodiment
Battery provided by the invention is not only safe and reliable and have the longer life-span, and very convenient carrying and storage, as portable type electronic products such as mobile phone, notebook computers, and electric automobile, electric bicycle, the fields such as electric tool have considerable application prospect.
The present invention has disclosed a kind of battery, and battery comprises positive pole, negative pole and electrolyte, and electrolyte comprises electrolyte and can dissolve electrolyte and make the aqueous solution of electrolyte ionization or at least one in alcoholic solution; Wherein, electrolyte also comprises the silicon dioxide that makes electrolyte gel.Like this, make electrolyte in gel state, battery can not produce leakage, thereby makes battery not only safe and reliable and have longer life, and very convenient carrying and storage.
After electrolyte gel, form silica particle.The particle diameter of micelle is different, and its specific area differs greatly.And the particle diameter of micelle depends primarily on preparation technology.
As shown in table 1, particle diameter is less, and the specific area of micelle is larger.Accordingly, the specific area of micelle is larger, and the surface of micelle can be just larger, and the reactivity of micelle is corresponding increase also.
Table 1
Particle diameter D (nm) Specific area (m 2/g)
<3 >1000
3~4 750~900
7~8 350~400
11~13 190~270
16~20 130~170
When particle diameter hour, between micelle, be easy to the formation chemical bond that reacts.When micelle near time, between micelle, by silanol condensation, form silicon oxygen bond, the skeleton that gel mainly relies on silicon oxygen bond to build is supporting.In skeleton, can wrap up water or alcohol, thereby form gel.And the process that forms silicon oxygen bond is irreversible, make the skeleton that relies on silicon oxygen bond to form be difficult to be broken.Therefore, hour, its gelation rate is very fast for particle diameter, forms that gel is fine and close, hard, intensity is large.
And along with the increase of particle diameter, the surface activity of micelle reduces, micelle centre-to-centre spacing also strengthens gradually, and the chance that forms silicon oxygen bond that reacts to each other between particle reduces.A small amount of less micelle is coupled to after larger micelle, and in system, the aggregation rate of particle will reduce.Now, between micelle, can not form three-dimensional framework by forming silicon oxygen bond.
Silica particle surface has a lot of hydroxyls, now can pass through Hydrogenbond, with hydrogen bond form, forms three-dimensional framework.And hydrogen bond is intermolecular a kind of weak binding, easily destroyed.Therefore.The skeleton forming by hydrogen bond is easily broken, and needs only shearing force a little, and skeleton is just destroyed, and the water or the alcohol that are wrapped in skeleton just can discharge.Once but remove shearing force, and skeleton structure is set up again, and water or alcohol are wrapped again.In sum, the formation of skeleton and to break be reversible completely, gels-soft is and flexible, and thixotropy is better.
Preferably, the particle diameter of micelle is not more than 20nm.If particle size analysis is excessive, fine although gel is cut rare property, three-dimensional framework forms very slow, be not enough to good gelation, and hydration phenomena is also comparatively serious.
Preferably, the particle diameter of micelle is between 10~20nm.
Preferably, the particle diameter of micelle is not more than 10nm.
Preferably, the particle diameter of micelle is between 5~7nm.
Preferably, the particle diameter of micelle is between 3~5nm.
Preferably, micelle have particle diameter at first group between 10~20nm and particle diameter second group between 5~7nm.So thickness micelle is reasonably combined, makes gel soft and flexible, and moderate strength, and solidifying property is good again.Thereby when guaranteeing that gel has certain toughness, intensity is also moderate.
In addition, wish obtains the gel electrolyte of superior performance, not only will change the size of silica particle, controls particle surface hydroxyl condensation level, but also will adjust the content of silicon dioxide.
In electrolyte, the weight accounting of silicon dioxide in electrolyte is 0.2%~20%, thereby guarantees that electrolyte has good gelling performance.
Preferably, the weight accounting of silicon dioxide in electrolyte is 0.2~0.5%, further improved the gelling performance of electrolyte.
Preferably, the weight accounting of silicon dioxide in electrolyte is 1.0~20%, further improved the gelling performance of electrolyte.
Preferably, the weight accounting of silicon dioxide in electrolyte is 1.0~3.2%.
Preferably, the weight accounting of silicon dioxide in electrolyte is 4.0~4.5%.
Preferably, the weight accounting of silicon dioxide in electrolyte is 5.0~20%.
Preferably, the aerosil of silicon dioxide for being prepared by vapor phase method by silicon tetrachloride.
Vapor phase method is again pyrolysismethod, dry method or combustion method.Its raw material is silicon tetrachloride, oxygen and hydrogen, and under high temperature, reaction forms.Reaction equation is: SiCl4+2H2+O2-> SiO2+4HCl.Air and hydrogen are sent into the synthetic stove that is hydrolyzed respectively after pressurization, separated, cooled dehydrated, dry, dust removal and filtration.Silicon tetrachloride raw material is delivered to after rectifying column rectifying, heating evaporation in evaporator, and the air of take after being dried, filtering is carrier, delivers to synthetic hydrolysis stove.After silicon tetrachloride at high temperature gasifies, under the high temperature of 1800 ℃ of left and right, carry out vapor phase hydrolysis with a certain amount of hydrogen and oxygen; The aerosil now generating is unbodied ultra-fine grain, is circulus, and gel force is strong, surface activity is high, can form the good silica gel of thixotropy.
In addition, silicon dioxide also can be prepared by silicate.In the world, the reserves of silicate are more, easily obtain, and cost compare is low.
Silicate can be selected from a kind of in sodium metasilicate, alumina silicate, potassium silicate, calcium silicates, silicic acid phosphorus, Magnesiumaluminumsilicate, lithium magnesium silicate.Certainly, also can be selected from and take montmorillonite, the smectite that alumina silicate is main component.
In addition, cheap because of water glass solution, the water glass solution that contains sodium metasilicate of often take is prepared silicon dioxide as raw material.Simple process flow is: concentrated → ultrafiltration that water glass solution → acid neutralization → anion-cation exchange resin is processed (stirring) → reduction vaporization.After ultrafiltration, the purity of silicon dioxide is higher, has reduced the impact of other metal impurities ion pair battery performance, and has improved the gelling performance of electrolyte.
In addition, electrolyte also comprises deflocculant, to change the configuration of surface of micelle, stops the effect of micelle gathering and delay gelatinizing process, can effectively change the performance of colloid.
Optional at least one in polyvinyl alcohol, dextrin, glycerine, polyethylene glycol, polyacrylamide and AEO of deflocculant.
Preferably, deflocculant is polyacrylamide.Polyacrylamide can effectively be alleviated the aquation layering of gel electrolyte.In addition, polyacrylamide also can play the effect that absorbs moisture, increases system viscosity, thereby as a kind of viscosity modifier.
Positive pole comprises plus plate current-collecting body and participates in the positive active material of electrochemical reaction, positive active material can be reversible deviate from-embedded ion; The material of plus plate current-collecting body is selected from a kind of in carbon-based material, metal or alloy; Negative pole at least comprises negative current collector; Electrolyte can ionize out at least one charge and discharge process and reduce at negative pole-deposit and be oxidized-active ion that dissolves.
Plus plate current-collecting body is only as the carrier of electrical conductivity and collection, do not participate in electrochemical reaction, in battery operated voltage range, plus plate current-collecting body can be stable is present in electrolyte and occurs without any side reaction, thereby guarantees that battery has stable cycle performance.
In the present invention, positive active material participates in anodal reaction, and can be reversible deviates from-embedded ion or functional group.Preferably, lithium ion, sodium ion, zinc ion or magnesium ion can reversiblely be deviate from-embed to positive active material.
Positive active material is to meet general formula Li 1+xmn ym zo kcan the reversible compound of deviating from-embed the spinel structure of lithium ion, wherein ,-1≤x≤0.5,1≤y≤2.5,0≤z≤0.5,3≤k≤6, M is selected from least one in Na, Li, Co, Mg, Ti, Cr, V, Zn, Zr, Si, Al.Preferably, positive active material contains LiMn 2o 4.Preferred, positive active material contains the LiMn through overdoping or coated modification 2o 4.
Positive active material is to meet general formula Li 1+xm ym ' zm " co 2+ncan the reversible compound of deviating from-embed the layer structure of lithium ion, wherein,-1 < x≤0.5,0≤y≤1,0≤z≤1,0≤c≤1,-0.2≤n≤0.2, M, M ', M " be selected from respectively Ni, Mn, Co, Mg, Ti, Cr, V, Zn, Zr, Si or Al at least one.Preferably, positive active material contains LiCoO 2.
Positive active material is to meet general formula Li xm 1-ym ' y(XO 4) ncan the reversible compound of deviating from-embed the olivine structural of lithium ion, wherein, 0 < x≤2,0≤y≤0.6,1≤n≤1.5, M is selected from Fe, Mn, V or Co, M ' be selected from Mg, Ti, Cr, V or Al at least one, X is selected from least one in S, P or Si.Preferably, positive active material contains LiFePO 4.
In current Lithium Battery Industry, nearly all positive active material all can be through overdoping, the modification such as coated.But doping, it is complicated that the means such as coated modification cause the chemical general formula of material to express, as LiMn 2o 4can not represent the general formula of now widely used " LiMn2O4 ", and should be with general formula Li 1+xmn ym zo kbe as the criterion, comprise widely the LiMn through various modifications 2o 4positive active material.Same, LiFePO 4and LiCoO 2also should be interpreted as widely to comprise through various doping, the modification such as coated, general formula meets respectively Li xm 1-ym ' y(XO 4) nand Li 1+xm ym ' zm " co 2+npositive active material.
Positive active material of the present invention is reversible while deviating from-embedding lithium ion compound, can select as LiMn 2o 4, LiFePO 4, LiCoO 2, LiM xpO 4, LiM xsiO ycompounds such as (wherein M are a kind of variable valency metal).In addition the compound that, can deviate from-embed sodium ion is as NaVPO 4f, can deviate from-embed the compound of zinc ion as γ-MnO 2, can deviate from-embed the compound of magnesium ion as MgM xo y(wherein M is a kind of metal, 0.5 < x < 3,2 < y < 6) and have similar functions, the compound of can deviate from-embedded ion or functional group can be as the positive active material of battery of the present invention.
In concrete execution mode, while preparing anode sizing agent, except positive active material, also need to add conductive agent and binding agent.
Conductive agent is selected from one or more in conducting polymer, activated carbon, Graphene, carbon black, carbon fiber, metallic fiber, metal dust and sheet metal.
Binding agent is selected from polyethylene oxide, polypropylene oxide, mixture and the derivative of a kind of or above-mentioned polymer in polyacrylonitrile, polyimides, polyester, polyethers, fluorinated polymer, poly-divinyl polyethylene glycol, polyethyleneglycol diacrylate, polyethylene glycol dimethacrylate.In embodiment, binding agent is selected from polytetrafluoroethylene (PTFE) or Kynoar (PVDF).
Negative pole at least comprises negative current collector, and in this execution mode, negative pole only comprises negative current collector, and negative current collector is only as the carrier of electrical conductivity and collection, does not participate in electrochemical reaction.The material of negative current collector is selected from least one in metal Ni, Cu, Ag, Pb, Mn, Sn, Fe, Al, Zn or the process above-mentioned metal of Passivation Treatment, or elemental silicon, or carbon-based material, wherein, carbon-based material comprises graphite material, such as the paper tinsel of business-like graphite compacting, wherein the shared part by weight scope of graphite is 90-100%.The material of negative current collector can also be selected from stainless steel or through the stainless steel of Passivation Treatment.Stainless steel includes but are not limited to stainless (steel) wire and stainless steel foil, same, and stainless model can be the stainless steel of 300 series, as stainless steel 304 or Stainless steel 316 or Stainless steel 316 L.
In addition, negative current collector can also be selected from the metal that contains plating/coating that hydrogen-evolution overpotential is high, thereby reduces the generation of negative pole side reaction.Plating/coating is selected from the simple substance that contains C, Sn, In, Ag, Pb, Co, Zn, alloy, or in oxide at least one.The thickness range of plating/coating is 1-1000nm.For example: tin on the negative current collector plated surface of Copper Foil or graphite foil, plumbous or silver-colored.
In addition, alcoholic solution includes but are not limited to ethanol or methyl alcohol.
Electrolyte can ionize out at least one charge and discharge process and reduce at negative pole-deposit and be oxidized-active ion that dissolves.
Active ion comprises metal ion, and metal is selected from least one in Zn, Fe, Cr, Cu, Mn, Ni, Sn.
Metal ion is present in electrolyte with forms such as chlorate, sulfate, nitrate, acetate, formates, phosphate.Preferably, metal ion is present in electrolyte with the form of the mixture of sulfate, acetate or sulfate and acetate.
Preferably, in electrolyte, also comprise a kind of electrolyte, electrolyte can ionize out at least one charge and discharge process can the reversible ion of deviating from-embedding at positive pole, thereby improve the ion-exchange speed in positive active material and electrolyte, thereby improve the high rate charge-discharge performance of the battery in the present invention.Concrete, positive active material is for can the reversible compound of deviating from-embed lithium ion, and what electrolyte was corresponding can also ionize out lithium ion.The reversible ion of deviating from-embedding comprises lithium ion or sodium ion or magnesium ion or zinc ion.
The charge-discharge principle of battery is: during charging, in positive active material, deviates from the reversible ion of deviating from-embedding, follows the interior variable valency metal of positive active material oxidized simultaneously, and ejected electron; Electronics arrives battery cathode via external circuit, and the active ion in while electrolyte obtains electronics at negative current collector and is reduced, and is deposited on negative current collector.Discharge process is the inverse process for charging.
Although inventor has done more detailed elaboration and has enumerated technical scheme of the present invention, be to be understood that, to those skilled in the art, above-described embodiment is modified and/or flexible or to adopt the replacement scheme being equal to be obvious, all can not depart from the essence of spirit of the present invention, the term occurring in the present invention, for to the elaboration of technical solution of the present invention and understanding, can not be construed as limiting the invention.

Claims (13)

1. a battery, comprises positive pole, negative pole and electrolyte, and described electrolyte comprises electrolyte and can dissolve described electrolyte and make the aqueous solution of described electrolyte ionization or at least one in alcoholic solution; It is characterized in that: described electrolyte also comprises the silicon dioxide that makes electrolyte gel.
2. battery according to claim 1, is characterized in that: the aerosil of described silicon dioxide for being prepared by vapor phase method by silicon tetrachloride.
3. battery according to claim 1, is characterized in that: described silicon dioxide is prepared by silicate.
4. battery according to claim 3, is characterized in that: described silicate is selected from a kind of in alumina silicate, sodium metasilicate, potassium silicate, calcium silicates, silicic acid phosphorus, Magnesiumaluminumsilicate, lithium magnesium silicate.
5. battery according to claim 1, is characterized in that: after described electrolyte gel, have silica particle, the particle diameter of described micelle is not more than 20nm.
6. battery according to claim 5, is characterized in that: the particle diameter of described micelle is between 10~20nm.
7. battery according to claim 5, is characterized in that: the particle diameter of described micelle is between 5~7nm.
8. battery according to claim 5, is characterized in that: described micelle have particle diameter at first group between 10~20nm and particle diameter second group between 5~7nm.
9. battery according to claim 1, is characterized in that: the weight accounting of described silicon dioxide in described electrolyte is 0.2%~20%.
10. battery according to claim 1, is characterized in that: described electrolyte also comprises deflocculant, and described deflocculant is selected from least one in polyvinyl alcohol, dextrin, glycerine, polyethylene glycol, polyacrylamide and AEO.
11. according to the battery of claim 1, and described positive pole comprises plus plate current-collecting body and participate in the positive active material of electrochemical reaction, described positive active material can be reversible deviate from-embedded ion; Described negative pole at least comprises negative current collector; Described electrolyte can ionize out at least one charge and discharge process and reduce-deposit and be oxidized at described negative pole-active ion that dissolves, described active ion comprises metal ion, and described metal is selected from least one in Zn, Fe, Cr, Cu, Mn, Ni, Sn.
12. batteries according to claim 11, is characterized in that: described metal ion is present in described electrolyte with the form of the mixture of sulfate, acetate or sulfate and acetate.
13. batteries according to claim 11, is characterized in that: lithium ion, sodium ion, zinc ion or magnesium ion can reversiblely be deviate from-embed to described positive active material.
CN201210208943.4A 2012-06-25 2012-06-25 Battery Active CN103515657B (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CN201710381889.6A CN107331905B (en) 2012-06-25 2012-06-25 Battery with a battery cell
CN201210208943.4A CN103515657B (en) 2012-06-25 2012-06-25 Battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201210208943.4A CN103515657B (en) 2012-06-25 2012-06-25 Battery

Related Child Applications (1)

Application Number Title Priority Date Filing Date
CN201710381889.6A Division CN107331905B (en) 2012-06-25 2012-06-25 Battery with a battery cell

Publications (2)

Publication Number Publication Date
CN103515657A true CN103515657A (en) 2014-01-15
CN103515657B CN103515657B (en) 2017-06-27

Family

ID=49898003

Family Applications (2)

Application Number Title Priority Date Filing Date
CN201210208943.4A Active CN103515657B (en) 2012-06-25 2012-06-25 Battery
CN201710381889.6A Active CN107331905B (en) 2012-06-25 2012-06-25 Battery with a battery cell

Family Applications After (1)

Application Number Title Priority Date Filing Date
CN201710381889.6A Active CN107331905B (en) 2012-06-25 2012-06-25 Battery with a battery cell

Country Status (1)

Country Link
CN (2) CN103515657B (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104505533A (en) * 2015-01-23 2015-04-08 杭州金色能源科技有限公司 Gel electrolyte, lithium ion battery and preparation method for lithium ion battery
CN105336956A (en) * 2014-06-06 2016-02-17 苏州宝时得电动工具有限公司 Battery
CN105932333A (en) * 2016-06-30 2016-09-07 普定县银丰农业科技发展有限公司 Lithium-ion battery electrolyte formula and preparation method
CN106374145A (en) * 2015-07-21 2017-02-01 苏州宝时得电动工具有限公司 Colloidal electrolyte and battery containing colloidal electrolyte
CN108270031A (en) * 2016-12-30 2018-07-10 财团法人工业技术研究院 colloidal electrolyte and application thereof
CN108461832A (en) * 2017-02-22 2018-08-28 中国科学院上海硅酸盐研究所 A kind of water-system alkali metal ion battery and preparation method thereof based on colloid or gel electrolyte
CN110010982A (en) * 2018-01-05 2019-07-12 苏州宝时得电动工具有限公司 Battery
CN111211360A (en) * 2018-11-22 2020-05-29 浙江浙能中科储能科技有限公司 Additive modified aqueous zinc ion colloidal electrolyte and preparation method thereof
CN111403829B (en) * 2020-04-24 2021-10-01 中国科学院上海硅酸盐研究所 Water system gel state electrolyte with low-temperature working characteristic, pole piece additive and solid sodium ion battery
CN114520375A (en) * 2022-02-16 2022-05-20 常州优特科新能源科技有限公司 Gel electrolyte with liquid retention function for air separator
WO2023138528A1 (en) * 2022-01-21 2023-07-27 戴文韬 Silicon negative electrode material and high-capacity fast-charging battery using same

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109585929B (en) * 2018-10-10 2022-03-01 湖南立方新能源科技有限责任公司 Preparation method of silicon cathode lithium ion battery

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1978507A (en) * 2006-11-24 2007-06-13 江苏鑫华富能源有限公司 High-molecular nano polymer electrolyte for lead-acid battery and its compounding method
CN102110839A (en) * 2009-12-29 2011-06-29 万向电动汽车有限公司 Battery
CN102315413A (en) * 2011-07-22 2012-01-11 浙江天能电池(江苏)有限公司 Explosion-proof valve controlled sealed lead-acid storage battery

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2178943Y (en) * 1993-12-18 1994-10-05 周连财 High discharge colloid storage battery
EP1020944B1 (en) * 1999-01-14 2011-12-07 Hitachi Chemical Company, Ltd. Lithium secondary battery, and process for producing the same
CN100508269C (en) * 2004-12-23 2009-07-01 钟发平 Colloid lead-cloth batteries in high energy, and preparation method
CN101136491A (en) * 2006-11-28 2008-03-05 创新能源技术(深圳)有限公司 Colloidal electrolyte formula and its confecting technique for lead acid accumulator
CN102208680B (en) * 2011-05-05 2014-07-02 中国东方电气集团有限公司 Gel electrolyte and preparation method thereof and corresponding anode and lithium sulfur battery
CN102263295B (en) * 2011-06-27 2014-03-26 扬州大学 Composite electrolyte for gel lead acid storage battery
CN102394319B (en) * 2011-11-03 2013-04-17 广西天鹅蓄电池有限责任公司 Colloidal electrolyte of storage battery

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1978507A (en) * 2006-11-24 2007-06-13 江苏鑫华富能源有限公司 High-molecular nano polymer electrolyte for lead-acid battery and its compounding method
CN102110839A (en) * 2009-12-29 2011-06-29 万向电动汽车有限公司 Battery
CN102315413A (en) * 2011-07-22 2012-01-11 浙江天能电池(江苏)有限公司 Explosion-proof valve controlled sealed lead-acid storage battery

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105336956A (en) * 2014-06-06 2016-02-17 苏州宝时得电动工具有限公司 Battery
CN104505533A (en) * 2015-01-23 2015-04-08 杭州金色能源科技有限公司 Gel electrolyte, lithium ion battery and preparation method for lithium ion battery
CN106374145A (en) * 2015-07-21 2017-02-01 苏州宝时得电动工具有限公司 Colloidal electrolyte and battery containing colloidal electrolyte
CN105932333B (en) * 2016-06-30 2018-09-25 普定县银丰农业科技发展有限公司 A kind of lithium-ion battery electrolytes formula and preparation method
CN105932333A (en) * 2016-06-30 2016-09-07 普定县银丰农业科技发展有限公司 Lithium-ion battery electrolyte formula and preparation method
CN108270031A (en) * 2016-12-30 2018-07-10 财团法人工业技术研究院 colloidal electrolyte and application thereof
CN108461832A (en) * 2017-02-22 2018-08-28 中国科学院上海硅酸盐研究所 A kind of water-system alkali metal ion battery and preparation method thereof based on colloid or gel electrolyte
CN110010982A (en) * 2018-01-05 2019-07-12 苏州宝时得电动工具有限公司 Battery
CN111211360A (en) * 2018-11-22 2020-05-29 浙江浙能中科储能科技有限公司 Additive modified aqueous zinc ion colloidal electrolyte and preparation method thereof
CN111211360B (en) * 2018-11-22 2021-07-06 浙江浙能中科储能科技有限公司 Additive modified aqueous zinc ion colloidal electrolyte and preparation method thereof
CN111403829B (en) * 2020-04-24 2021-10-01 中国科学院上海硅酸盐研究所 Water system gel state electrolyte with low-temperature working characteristic, pole piece additive and solid sodium ion battery
WO2023138528A1 (en) * 2022-01-21 2023-07-27 戴文韬 Silicon negative electrode material and high-capacity fast-charging battery using same
CN114520375A (en) * 2022-02-16 2022-05-20 常州优特科新能源科技有限公司 Gel electrolyte with liquid retention function for air separator

Also Published As

Publication number Publication date
CN107331905B (en) 2020-01-14
CN103515657B (en) 2017-06-27
CN107331905A (en) 2017-11-07

Similar Documents

Publication Publication Date Title
CN103515657B (en) Battery
Lai et al. A promising energy storage system: rechargeable Ni–Zn battery
CN102299326B (en) Graphene modified lithium iron phosphate/carbon composite material and its application
CN108539171B (en) Preparation method of zinc sulfide and graphene oxide compound and application of compound in positive electrode material of lithium-sulfur battery
CN102255078B (en) Coordinated method for preparing nanometer spherical iron phosphate and then using carbon fusion method to prepare nanometer spherical lithium iron phosphate
CN102324494B (en) Lithium iron phosphate / nano-powder tube oxide composite cathode material and preparation method thereof
CN108183039B (en) Preparation method of carbon-modified titanium niobate material, lithium ion capacitor and negative electrode slurry thereof
CN106654221A (en) Three-dimensional porous carbon-coated zinc selenide material for lithium ion battery anodes and preparation method of material
CN114050246A (en) Micron-sized porous sodium ferrous sulfate/carbon composite cathode material and sodium ion battery or sodium battery prepared from same
CN108658119B (en) Method for preparing copper sulfide nanosheet and compound thereof by low-temperature vulcanization technology and application
CN101764258A (en) Secondary aluminium cell and preparation method thereof
CN110323073B (en) Preparation method and application of oxygen-doped cobalt nickel phosphide-reduced graphene oxide composite material
CN105702958B (en) Preparation method and application of tin dioxide quantum dot solution and composite material thereof
CN103515595A (en) Sulfur/polypyrrole-graphene composite material, preparation method thereof, battery positive electrode and lithium-sulfur battery
Xiao et al. Research progress of nano-silicon-based materials and silicon-carbon composite anode materials for lithium-ion batteries
CN108899499B (en) Sb/Sn phosphate-based negative electrode material, preparation method thereof and application thereof in sodium ion battery
WO2024011862A1 (en) Iron-based sodium ion full battery and preparation method therefor
CN111646459A (en) Preparation method and application of boron-doped graphene material
CN110993923B (en) Carbon-coated auxiliary sodium-titanium double-doped lithium iron silicate positive electrode material and preparation method and application thereof
CN104681814B (en) A kind of anode material for lithium-ion batteries LiFePO with porous star pattern4And preparation method thereof
CN114023948B (en) Silicon-carbon negative electrode material, preparation method thereof and lithium ion battery
Sui et al. Highly dispersive CoSe 2 nanoparticles encapsulated in carbon nanotube-grafted multichannel carbon fibers as advanced anodes for sodium-ion half/full batteries
Muchuweni et al. Lithium-ion batteries: Recent progress in improving the cycling and rate performances of transition metal oxide anodes by incorporating graphene-based materials
CN104638248A (en) Method for preparing graphene/lead compound composite material
CN109399600B (en) Preparation method of three-dimensional ordered macroporous sodium ferrous fluorophosphate material

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant