CN110993944B - A kind of aqueous ion battery and its application - Google Patents

A kind of aqueous ion battery and its application Download PDF

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CN110993944B
CN110993944B CN201911087091.6A CN201911087091A CN110993944B CN 110993944 B CN110993944 B CN 110993944B CN 201911087091 A CN201911087091 A CN 201911087091A CN 110993944 B CN110993944 B CN 110993944B
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ion battery
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CN110993944A (en
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王晓东
李忆非
任江涛
王耀国
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Ningbo Fengcheng Advanced Energy Materials Research Institute Co ltd
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/60Selection of substances as active materials, active masses, active liquids of organic compounds
    • H01M4/602Polymers
    • H01M4/606Polymers containing aromatic main chain polymers
    • H01M4/608Polymers containing aromatic main chain polymers containing heterocyclic rings
    • 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
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M2004/026Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/027Negative electrodes
    • 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
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    • Y02E60/10Energy storage using batteries

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Abstract

The application discloses water system ion battery includes: an electrolyte, wherein the electrolyte is an aqueous solution containing electrolyte; a negative electrode containing a negative electrode active material; the negative electrode active material includes polyimide containing naphthalene ring; and a positive electrode containing a positive electrode active material; the positive electrode active material includes a sodium intercalation material. The method solves the problems: the existing negative electrode material and the positive electrode sodium intercalation material have the problem of poor matching (such as mass ratio of the positive electrode material to the negative electrode material, technological parameters of electrode preparation, potential voltage window and the like), so that the cycle life of the battery is low and the specific capacity is low; because the electrode preparation of the existing negative electrode material and the process of battery assembly are complex, the requirements on the conditions of an operation workshop are high, and the material preparation cost is high, so that the production and manufacturing cost of the whole battery is increased.

Description

一种水系离子电池及其应用A kind of aqueous ion battery and its application

技术领域technical field

本申请涉及一种水系离子电池,属于电池领域。The application relates to an aqueous ion battery, which belongs to the field of batteries.

背景技术Background technique

水系离子电池是以水为电解质的电池体系。与其它非水系离子电池相比,水系离子电池有着安全性能好,离子电导率高,价格低廉易得等优点。且水系电池无需无水无氧的环境,就可以完成电池生产、组装、密封等操作,大大降低了电池的生产及制造成本,因而逐渐受到重视,非常适合大规模储能市场。目前商业化使用的储能电池主要是铅酸电池,磷酸铁锂或三元动力电池。其中,铅酸电池寿命短,高污染。其负极使用金属铅(Pb),反应过程中生成硫酸铅(PbSO4)钝化层导致容量衰减,循环寿命只有几百圈。磷酸铁锂或三元动力电池均使用有机电解液,易燃爆炸安全性低。同时,因其使用镍钴锰铁等金属,成本上不具有优势。这几种电池均满足不了储能领域特殊的需求(如高度安全、超长循环寿命、低成本等)。Aqueous ion batteries are battery systems that use water as the electrolyte. Compared with other non-aqueous ion batteries, aqueous ion batteries have the advantages of good safety performance, high ion conductivity, low price and easy availability. In addition, water-based batteries can complete battery production, assembly, sealing and other operations without an anhydrous and oxygen-free environment, which greatly reduces the production and manufacturing costs of batteries. Therefore, it has gradually attracted attention and is very suitable for the large-scale energy storage market. Currently commercially used energy storage batteries are mainly lead-acid batteries, lithium iron phosphate or ternary power batteries. Among them, lead-acid batteries have short service life and high pollution. Its negative electrode uses metallic lead (Pb), and a lead sulfate (PbSO 4 ) passivation layer is formed during the reaction process, resulting in capacity fading, and the cycle life is only a few hundred cycles. Both lithium iron phosphate and ternary power batteries use organic electrolytes, which are flammable and explosive with low safety. At the same time, because of the use of metals such as nickel-cobalt-manganese-ferro, there is no advantage in cost. None of these types of batteries can meet the special needs in the field of energy storage (such as high safety, long cycle life, low cost, etc.).

在水系离子电池的进展中,水系锂离子电池得到了一定的发展。但是,地球上的锂资源是难以支撑大型储能系统的应用需求的。全球锂资源基础储量约为58M吨(以碳酸锂计),而且大多数锂资源集中于海拔4000米以上高原盐湖,开发利用困难。现在已知的可开采储量约为25M吨。目前全球碳酸锂年消耗量约为7至8万吨,预计可开采时间不过50多年。相比之下,钠与锂的化学性能类似,因而被认为能够替代锂适用于水系离子电池体系。钠在地壳中储量丰富,钠盐的价格也只有锂盐的十分之一。因此,结合水系电池的诸多优点,水系钠离子电池在发电侧和用户侧储能领域均有着广阔的应用前景。In the progress of aqueous ion batteries, aqueous lithium ion batteries have been developed to a certain extent. However, the lithium resources on the earth are difficult to support the application requirements of large-scale energy storage systems. The basic reserves of lithium resources in the world are about 58M tons (calculated as lithium carbonate), and most of the lithium resources are concentrated in plateau salt lakes above 4,000 meters above sea level, making it difficult to develop and utilize them. The known recoverable reserves are about 25M tons. At present, the annual consumption of lithium carbonate in the world is about 70,000 to 80,000 tons, and the expected mining time is only more than 50 years. In contrast, sodium has similar chemical properties to lithium, so it is considered to be suitable for aqueous ion battery systems as a substitute for lithium. Sodium is abundant in the earth's crust, and the price of sodium salt is only one tenth of that of lithium salt. Therefore, combined with many advantages of aqueous batteries, aqueous sodium-ion batteries have broad application prospects in the fields of power generation and user-side energy storage.

但是,目前已开发的水系二次电池也存在诸多问题。如循环寿命较低,材料难以放大,同时不能实现大规模应用等问题。水系钠离子电池循环寿命低的主要瓶颈在于负极材料。到目前为止,国内外已经研发了使用磷酸钛钠和普鲁士蓝作为负极材料用于水系钠离子电池,但这种材料在水溶液中,放电时会发生析氢副反应导致电池循环寿命低;且该类负极材料的电化学容量低,难以发挥出全电池的容量。However, the currently developed aqueous secondary batteries also have many problems. For example, the cycle life is low, the materials are difficult to scale up, and large-scale applications cannot be realized at the same time. The main bottleneck of the low cycle life of aqueous sodium-ion batteries lies in the anode materials. So far, sodium titanium phosphate and Prussian blue have been developed at home and abroad as negative electrode materials for aqueous sodium-ion batteries. However, when this material is in an aqueous solution, hydrogen evolution side reactions will occur during discharge, resulting in low battery cycle life; and the electrochemical capacity of this type of negative electrode material is low, and it is difficult to exert the capacity of the full battery.

针对上述问题,本申请提供了一种新的水系离子电池。In view of the above problems, the present application provides a new aqueous ion battery.

发明内容Contents of the invention

根据本申请的一个方面,提供了一种水系离子电池,解决了现有负极电极材料在水系电解液中稳定性差,放电时会发生析氢副反应,导致水系钠离子电池的循环寿命低,比容量低;现有负极电极材料的电极制备以及电池组装的工艺复杂,对操作车间的条件要求高,材料制备成本高,导致整个电池生产制造的成本增加;现有负极材料与正极嵌钠材料存在着匹配性差(如正、负极电极材料的质量配比、电极制备的工艺参数以及电位电压窗口等)的问题,导致电池的循环寿命低,比容量低。According to one aspect of the present application, a water-based ion battery is provided, which solves the problem that the existing negative electrode material has poor stability in the water-based electrolyte, and hydrogen evolution side reactions occur during discharge, resulting in low cycle life and low specific capacity of the water-based sodium-ion battery; the electrode preparation of the existing negative electrode material and the battery assembly process are complicated, the requirements for the operating workshop are high, and the cost of material preparation is high, resulting in an increase in the cost of the entire battery production; Preparation process parameters and potential voltage window, etc.) lead to low cycle life and low specific capacity of the battery.

所述水系离子电池,其特征在于,包括:The aqueous ion battery is characterized in that it comprises:

电解液,所述电解液为含有电解质的水溶液;An electrolytic solution, which is an aqueous solution containing an electrolyte;

负极,所述负极含有负极活性物质;所述负极活性物质包括含有萘环的聚酰亚胺;和Negative electrode, the negative electrode contains negative electrode active material; the negative electrode active material includes polyimide containing naphthalene ring; and

正极,所述正极含有正极活性物质;所述正极活性物质包括嵌钠系材料,所述嵌钠系材料选自NaMnO2、NaxMnO2、NaFeFe(CN)6、Na2CoFe(CN)6、Na2NiFe(CN)6中的至少一种。A positive electrode, the positive electrode contains a positive electrode active material; the positive electrode active material includes a sodium-intercalating material, and the sodium-intercalating material is at least one selected from NaMnO 2 , Na x MnO 2 , NaFeFe(CN) 6 , Na 2 CoFe(CN) 6 , and Na 2 NiFe(CN) 6 .

其中,NaMnO2为嵌入了钠离子的λ-MnO2;x为0.44~0.95;Among them, NaMnO 2 is λ-MnO 2 embedded with sodium ions; x is 0.44-0.95;

NaMnO2为嵌入了钠离子的λ-MnO2,按文献(1-2)方法制备;NaMnO 2 is λ-MnO 2 intercalated with sodium ions, prepared according to the method in literature (1-2);

文献1:Whitacre J F,Wiley T,Shanbhag S,et al.An aqueous electrolyte,sodium ion functional,large format energy storage device for stationaryapplications.J.Power Sources 2012,213:255-264.Document 1: Whitacre J F, Wiley T, Shanbhag S, et al. An aqueous electrolyte, sodium ion functional, large format energy storage device for stationary applications. J. Power Sources 2012, 213: 255-264.

文献2:Komaba S,Ogata A,Tsuchikawa T.Enhanced supercapacitivebehaviors of birnessite.Electrochem.Commun.,2008,10(10):1435-1437.Document 2: Komaba S, Ogata A, Tsuchikawa T. Enhanced supercapacitive behaviors of birthite. Electrochem. Commun., 2008, 10(10): 1435-1437.

NaFeFe(CN)6、Na2CoFe(CN)6、Na2NiFe(CN)6按文献(3-7)方法制备;NaFeFe(CN) 6 , Na 2 CoFe(CN) 6 , Na 2 NiFe(CN) 6 were prepared according to the method in literature (3-7);

文献3:C.D.Wessells,S.V.Peddada,R.A.Huggins and Y.Cui:‘Nickelhexacyanoferrate nanoparticle electrodes for aqueous sodium and potassium ionbatteries’,Nano Lett.,2011,11,5421–5425.Document 3: C.D. Wessells, S.V.Peddada, R.A. Huggins and Y.Cui: ‘Nickelhexacyanoferrate nanoparticles electrodes for aqueous sodium and potassium ionbatteries’, Nano Lett., 2011, 11, 5421–5425.

文献4:Yang You,Zhongsheng Sang&Jinping Liu.Recent developments onaqueous sodiumion batteries.Materials Technology:Advanced PerformanceMaterials 2016VOL.31NO.9.501-509.Document 4: Yang You, Zhongsheng Sang&Jinping Liu.Recent developments onaqueous sodium ion batteries.Materials Technology:Advanced PerformanceMaterials 2016VOL.31NO.9.501-509.

文献5:QIAN J,ZHOU M,CAO Y,et al.NaxMyFe(CN)6(M=Fe,Co,Ni):A new classof cathode materials for sodium ion batteries[J].J.Electrochem.,2012,18(2):108-112.Document 5: QIAN J, ZHOU M, CAO Y, et al. NaxMyFe(CN) 6 (M=Fe, Co, Ni): A new class of cathode materials for sodium ion batteries[J].J.Electrochem., 2012, 18(2): 108-112.

文献6:Pasta M,Wessells C D,Huggins R A,et al.A high-rate and longcycle life aqueous electrolyte battery for grid-scale energy storage.NatureCommun.,2012,3:1149.Document 6: Pasta M, Wessells C D, Huggins R A, et al. A high-rate and longcycle life aqueous electrolyte battery for grid-scale energy storage. Nature Commun., 2012, 3: 1149.

文献7:Wu X,Cao Y,Ai X,et al.A low-cost and environmentally benignaqueous rechargeable sodium-ion battery based on NaTi2(PO4)3-Na2NiFe(CN)6intercalation chemistry.Electrochem.Commun.,2013,31(0):145-148.Literature 7: WU X, Cao Y, AI X, ET Al. Et Al.Al. Cost and Environmentally Benignaqueous Rechargeable Sodium-ION BATTERY BASED on Nati 2 (PO 4 ) 3 - NIFE (CN) 6 Internet Ion Chemistry.electrochem.commun., 2013,31 (0): 145-148.

NaxMnO2按文献(8-10)方法制备;NaxMnO 2 is prepared according to the method of literature (8-10);

文献8:Whitacre J,Tevar A,Sharma S.Na4Mn9O18 as a positiveelectrodematerial for an aqueous electrolyte sodium-ion energy storagedevice.Electrochem.Commun.,2010,12(3):463-466.Literature 8: Whitacre J, Tevar A, Sharma S. Na 4 Mn 9 O 18 as a positive electrode material for an aqueous electrolyte sodium-ion energy storage device. Electrochem. Commun., 2010,12(3):463-466.

文献9:J.F.Whitacre,Electrochemistry Communication,12(2010)463-466.Document 9: J.F.Whitacre, Electrochemistry Communication, 12(2010) 463-466.

文献10:B.Zhang,Y.Liu,X.Wu,Y.Yang,Z.Chang,Z.Wen and Y.Wu:‘An aqueousrechargeable battery based on zinc anode and Na0.95MnO2’,Chem.Commun.,2014,50,1209–1211.Document 10: B. Zhang, Y. Liu, X. Wu, Y. Yang, Z. Chang, Z. Wen and Y. Wu: 'An aqueous rechargeable battery based on zinc anode and Na 0.95 MnO 2 ', Chem. Commun., 2014, 50, 1209–1211.

可选地,所述正极活性物质与负极活性物质的质量比为1~4;Optionally, the mass ratio of the positive active material to the negative active material is 1-4;

其中,负极活性物质的质量以其含有的含有萘环的聚酰亚胺的质量计,正极活性物质的质量以其含有的锰酸锂的质量计。Wherein, the mass of the negative electrode active material is calculated by the mass of the polyimide containing naphthalene ring contained therein, and the mass of the positive electrode active material is calculated by the mass of the lithium manganate contained therein.

可选地,所述含有萘环的聚酰亚胺的化学式如式I所示:Optionally, the chemical formula of the polyimide containing naphthalene ring is as shown in formula I:

其中,n=1000~10000。Among them, n=1000~10000.

可选地,所述电解质选自硫酸钠、硝酸钠、磷酸钠、碳酸钠、高锰酸钠、氯化钠、溴化钠、碘化钠中的至少一种。Optionally, the electrolyte is at least one selected from sodium sulfate, sodium nitrate, sodium phosphate, sodium carbonate, sodium permanganate, sodium chloride, sodium bromide, and sodium iodide.

可选地,所述电解液中电解质的浓度为1.5M~2.5M。Optionally, the electrolyte concentration in the electrolyte is 1.5M-2.5M.

可选地,所述水系离子电池还包括隔膜,所述隔膜将所述正极和所述负极分隔开,并通过电解质离子。Optionally, the aqueous ion battery further includes a separator, which separates the positive electrode from the negative electrode and passes electrolyte ions.

可选地,所述隔膜选自玻璃纤维滤纸、吸附式玻璃纤维膜、无纺布中的至少一种。Optionally, the separator is selected from at least one of glass fiber filter paper, absorbent glass fiber membrane, and non-woven fabric.

可选地,所述负极的制备方法包括以下步骤:Optionally, the preparation method of the negative electrode comprises the following steps:

将含有负极活性物质、导电剂、粘结剂的原料,与溶剂混合,得到浆料,将所述浆料涂覆到集流体上,干燥,得到所述负极。The raw materials containing the negative electrode active material, the conductive agent, and the binder are mixed with a solvent to obtain a slurry, and the slurry is coated on a current collector and dried to obtain the negative electrode.

可选地,所述负极活性物质、导电剂、粘结剂的质量比为5.5~9.6:0.25~3:0.25~1.25。Optionally, the mass ratio of the negative electrode active material, conductive agent, and binder is 5.5-9.6:0.25-3:0.25-1.25.

可选地,所述负极活性物质、导电剂、粘结剂的质量比为6:3:1。Optionally, the mass ratio of the negative electrode active material, conductive agent, and binder is 6:3:1.

可选地,所述溶剂选自无水乙醇、N-甲基吡咯烷酮、N-二甲基甲酰胺中的至少一种;Optionally, the solvent is selected from at least one of absolute ethanol, N-methylpyrrolidone, and N-dimethylformamide;

可选地,所述粘结剂选自聚偏氟乙烯、羧甲基纤维素、聚四氟乙烯、丁苯橡胶中的至少一种;Optionally, the binder is selected from at least one of polyvinylidene fluoride, carboxymethyl cellulose, polytetrafluoroethylene, and styrene-butadiene rubber;

可选地,所述导电剂选自导电炭黑、乙炔黑、碳纳米管、超导炭黑、碳纤维、导电石墨中的至少一种;Optionally, the conductive agent is selected from at least one of conductive carbon black, acetylene black, carbon nanotubes, superconducting carbon black, carbon fiber, and conductive graphite;

可选地,所述集流体选自不锈钢片、不锈钢网、不锈钢箔中的至少一种。Optionally, the current collector is selected from at least one of stainless steel sheet, stainless steel mesh, and stainless steel foil.

可选地,所述负极活性物质在所述集流体的面密度为2~5mg/cm2Optionally, the areal density of the negative electrode active material in the current collector is 2-5 mg/cm 2 .

可选地,所述正极的制备方法包括以下步骤:Optionally, the preparation method of the positive electrode comprises the following steps:

将含有正极活性物质、导电剂、粘结剂的原料,与溶剂混合,得到浆料,将所述浆料涂覆到集流体上,干燥,得到所述正极。The raw materials containing the positive electrode active material, conductive agent, and binder are mixed with a solvent to obtain a slurry, and the slurry is coated on a current collector and dried to obtain the positive electrode.

可选地,所述正极活性物质、导电剂、粘结剂的质量比为7.5~9.6:0.25~2.25:0.25~2.25。Optionally, the mass ratio of the positive active material, conductive agent and binder is 7.5-9.6:0.25-2.25:0.25-2.25.

可选地,所述正极活性物质、导电剂、粘结剂的质量比为8:1:1。Optionally, the mass ratio of the positive electrode active material, the conductive agent, and the binder is 8:1:1.

可选地,所述溶剂选自无水乙醇、N-甲基吡咯烷酮、N-二甲基甲酰胺中的至少一种;Optionally, the solvent is selected from at least one of absolute ethanol, N-methylpyrrolidone, and N-dimethylformamide;

所述粘结剂选自聚偏氟乙烯、羧甲基纤维素、聚四氟乙烯、丁苯橡胶中的至少一种;The binder is selected from at least one of polyvinylidene fluoride, carboxymethyl cellulose, polytetrafluoroethylene, and styrene-butadiene rubber;

所述导电剂选自导电炭黑、乙炔黑、碳纳米管、超导炭黑、碳纤维、导电石墨中的至少一种;The conductive agent is selected from at least one of conductive carbon black, acetylene black, carbon nanotubes, superconducting carbon black, carbon fiber, and conductive graphite;

所述集流体选自不锈钢片、不锈钢网、不锈钢箔中的至少一种。The current collector is selected from at least one of stainless steel sheet, stainless steel mesh, and stainless steel foil.

可选地,所述正极活性物质在所述集流体的面密度为3~8mg/cm2Optionally, the areal density of the positive electrode active material in the current collector is 3-8 mg/cm 2 .

可选地,所述负极活性物质的制备方法包括以下步骤:Optionally, the preparation method of the negative electrode active material comprises the following steps:

将含有1,4,5,8-萘四甲酸酐和乙二胺的溶液,在非活性气氛下,在120~180℃下反应4~18小时,经分离、洗涤干燥后,得到干粉;React the solution containing 1,4,5,8-naphthalene tetracarboxylic anhydride and ethylenediamine at 120-180°C for 4-18 hours in an inert atmosphere, and obtain a dry powder after separation, washing and drying;

将所述干粉在非活性气氛下烧结,得到所述负极活性物质。The dry powder is sintered in an inert atmosphere to obtain the negative electrode active material.

可选地,所述非活性气氛选自氮气、氦气、氩气中的至少一种。Optionally, the inert atmosphere is at least one selected from nitrogen, helium, and argon.

可选地,所述含有1,4,5,8-萘四甲酸酐和乙二胺的溶液的溶剂选自N-甲基吡咯烷酮、N-二甲基甲酰胺中的至少一种。Optionally, the solvent of the solution containing 1,4,5,8-naphthalene tetracarboxylic anhydride and ethylenediamine is at least one selected from N-methylpyrrolidone and N-dimethylformamide.

可选地,1,4,5,8-萘四甲酸酐和乙二胺的摩尔比为1:1~2。Optionally, the molar ratio of 1,4,5,8-naphthalene tetracarboxylic anhydride to ethylenediamine is 1:1-2.

可选地,所述烧结的温度为200~350℃。Optionally, the sintering temperature is 200-350°C.

可选地,所述烧结的时间为3~8小时。Optionally, the sintering time is 3-8 hours.

具体地,所述负极活性物质的制备方法包括以下步骤:Specifically, the preparation method of the negative electrode active material includes the following steps:

步骤A:在N-二甲基甲酰胺(DMF)的溶液中按照摩尔比1:1加入1,4,5,8-萘四甲酸酐粉末与乙二胺溶液,保持磁力搅拌。反应容器为玻璃烧瓶。对烧瓶进行氩气保护。将烧瓶转移到50℃油浴中,并逐步升温至150℃。在该温度下保持反应4到18小时。Step A: Add 1,4,5,8-naphthalene tetracarboxylic anhydride powder and ethylenediamine solution in N-dimethylformamide (DMF) solution at a molar ratio of 1:1, and keep magnetic stirring. The reaction vessel is a glass flask. The flask was protected with argon. The flask was transferred to a 50°C oil bath, and the temperature was gradually raised to 150°C. The reaction is maintained at this temperature for 4 to 18 hours.

步骤B:将生成物收集,离心,去除上清液。对于下方离心沉淀物用N-二甲基甲酰胺稀释清洗,进行第二次离心。再用乙醇进行清洗离心。最终物质在真空烘箱中烘干,得到干粉。Step B: Collect the product, centrifuge, and remove the supernatant. For the centrifuged sediment below, it was diluted and washed with N-dimethylformamide, and a second centrifugation was performed. Wash and centrifuge with ethanol. The final material was dried in a vacuum oven to obtain a dry powder.

步骤C:将上述干粉在管式炉中进行烧结,氩气气氛保护。烧结时间为3小时。Step C: sintering the above dry powder in a tube furnace under the protection of argon atmosphere. The sintering time was 3 hours.

具体地,所述水系离子电池包括:Specifically, the aqueous ion battery includes:

电解液,1.5~2.5M硫酸钠(Na2SO4)水溶液;Electrolyte, 1.5-2.5M sodium sulfate (Na 2 SO 4 ) aqueous solution;

隔膜,玻璃纤维滤纸(孔隙率1微米以下,厚度260微米左右);Diaphragm, glass fiber filter paper (porosity below 1 micron, thickness about 260 microns);

负极,含有萘环的聚酰亚胺电极;和negative electrode, a polyimide electrode containing naphthalene rings; and

正极,钠系材料电极(NaMnO2、NaxMnO2、NaFeFe(CN)6、Na2CoFe(CN)6、Na2NiFe(CN)6;其中:x为0.44~0.95)。Positive electrode, sodium-based material electrode (NaMnO 2 , Na x MnO 2 , NaFeFe(CN) 6 , Na 2 CoFe(CN) 6 , Na 2 NiFe(CN) 6 ; wherein: x is 0.44-0.95).

具体地,所述负极包括:Specifically, the negative electrode includes:

负极活性物质,含有萘环的聚酰亚胺有机材料;Negative electrode active material, polyimide organic material containing naphthalene ring;

导电剂,导电炭黑(Super P carbon);Conductive agent, conductive carbon black (Super P carbon);

粘结剂,聚四氟乙烯(PTFE)乳液;和Binder, polytetrafluoroethylene (PTFE) emulsion; and

集流体,不锈钢网。Collector, stainless steel mesh.

具体地,所述负极的制备方法包括以下步骤:Specifically, the preparation method of the negative electrode comprises the following steps:

将负极活性物质、导电炭黑、粘结剂按照质量比例为6:3:1,在乙醇溶液中混合搅拌形成泥浆状,涂覆到不锈钢网上,然后真空烘干。电极面积约为1.5cm2,活性物质的面密度为2~5mg·cm-2The negative electrode active material, conductive carbon black, and binder are mixed and stirred in an ethanol solution according to the mass ratio of 6:3:1 to form a slurry, coated on a stainless steel mesh, and then vacuum-dried. The electrode area is about 1.5 cm 2 , and the surface density of the active material is 2-5 mg·cm -2 .

具体地,所述正极包括:Specifically, the positive electrode includes:

正极活性物质,锰酸钠(NaMnO2,即嵌入了钠离子的λ-MnO2);Positive active material, sodium manganate (NaMnO 2 , that is, λ-MnO 2 embedded with sodium ions);

导电剂,导电炭黑(Super P carbon);Conductive agent, conductive carbon black (Super P carbon);

粘结剂,聚四氟乙烯(PTFE)乳液;和Binder, polytetrafluoroethylene (PTFE) emulsion; and

集流体,不锈钢网。Collector, stainless steel mesh.

具体地,所述正极的制备方法包括以下步骤:Specifically, the preparation method of the positive electrode includes the following steps:

将正极活性物质、导电炭黑、粘结剂按照质量比例为8:1:1,在乙醇中混合搅拌形成泥浆状,涂覆到不锈钢网上,然后真空烘干。电极面积约为1.5cm2,活性物质的面密度为3~8mg·cm-2The positive electrode active material, conductive carbon black, and binder are mixed and stirred in ethanol to form a slurry according to the mass ratio of 8:1:1, coated on the stainless steel mesh, and then vacuum-dried. The electrode area is about 1.5 cm 2 , and the surface density of the active material is 3-8 mg·cm -2 .

所述水系离子电池的工作原理为:The working principle of the water system ion battery is:

充电时:正极锰酸钠脱钠,钠离子在电解液中传导到负极聚酰亚胺羰基表面,被羰基官能团吸附,同时羰基得到外电路的电子被还原;When charging: the sodium manganate of the positive electrode is desodiumized, and the sodium ions are conducted to the surface of the polyimide carbonyl group of the negative electrode in the electrolyte, and are absorbed by the carbonyl functional group, and at the same time, the electrons obtained by the carbonyl group from the external circuit are reduced;

放电时:负极材料表面羰基脱钠离子,同时羰基失去电子被氧化,钠离子在电解液中传导到正极锰酸钠,并嵌入锰酸钠结构中。During discharge: the carbonyl group on the surface of the negative electrode material is free of sodium ions, and at the same time the carbonyl group loses electrons and is oxidized, and the sodium ions are conducted to the positive electrode sodium manganate in the electrolyte and embedded in the structure of sodium manganate.

水系钠离子电池采用含有钠离子的水溶液作为电解质,正极由不同离子嵌入化合物组成。充电时,钠离子从正极脱出,并通过电解液扩散至负极,在负极发生吸附或嵌入反应,电子则由正极转移至负极。放电过程与充电过程相反。Aqueous sodium-ion batteries use an aqueous solution containing sodium ions as the electrolyte, and the positive electrode is composed of different ion intercalation compounds. When charging, sodium ions come out of the positive electrode and diffuse to the negative electrode through the electrolyte, where adsorption or intercalation reactions occur at the negative electrode, and electrons are transferred from the positive electrode to the negative electrode. The discharge process is the opposite of the charge process.

根据本申请的另一个方面,提供一种所述的水系离子电池在储能中的应用。According to another aspect of the present application, an application of the aqueous ion battery in energy storage is provided.

根据本申请的另一个方面,提供一种所述的水系离子电池在水系储能电池中的应用。According to another aspect of the present application, an application of the aqueous ion battery in an aqueous energy storage battery is provided.

本申请能产生的有益效果包括:The beneficial effect that this application can produce comprises:

1)含有萘环的聚酰亚胺类有机材料,已被证明可以在非水系(传统)离子电池、水系液流电池和水系锂离子电池中工作。本工作将该类物质首次用于水系钠离子二次电池中,通过优化正负电极的配方和N/P配比,得到了优异的电化学性能。含有萘环的聚酰亚胺类有机材料,其重复单元中具有一个萘环,和两个酰亚胺结构与四个羰基官能团。其中羰基官能团具有电化学活性,可吸附和脱附锂离子从而贡献容量。同时,它具有高的机械强度和热稳定性,在充放电过程中能发生化学和结构上高度可逆的离子配位反应,反应速率快、对离子选择广泛,并与成熟的电极材料搭配,组成稳定的水系电池。与现有使用的水系电池电极材料相比,该类电池电极材料的能量和功率指标都毫不逊色,甚至在成本、低温性能、过充性能等方面更胜一筹,在水系电池发展中将会是一个大的突破。此外,其价格廉价、原料资源近乎无限,而借助更优化的分子结构设计和正极材料搭配,电池比能量可以取得超过成倍的提高;1) Polyimide-based organic materials containing naphthalene rings have been shown to work in non-aqueous (conventional) ion batteries, aqueous flow batteries, and aqueous lithium-ion batteries. In this work, this kind of material was used in aqueous sodium-ion secondary batteries for the first time, and excellent electrochemical performance was obtained by optimizing the formulation of positive and negative electrodes and the ratio of N/P. A polyimide organic material containing a naphthalene ring has a naphthalene ring in its repeating unit, two imide structures and four carbonyl functional groups. Among them, the carbonyl functional group is electrochemically active and can absorb and desorb lithium ions to contribute to the capacity. At the same time, it has high mechanical strength and thermal stability, and can undergo chemically and structurally highly reversible ion coordination reactions during charge and discharge. Compared with the currently used aqueous battery electrode materials, the energy and power indicators of this type of battery electrode materials are not inferior, and even better in terms of cost, low temperature performance, and overcharge performance. It will be a big breakthrough in the development of aqueous batteries. In addition, its price is cheap, and its raw material resources are almost unlimited. With the help of more optimized molecular structure design and cathode material matching, the specific energy of the battery can be more than doubled;

2)本申请所提供的水系离子电池,这类有机负极材料的电极制备工艺简单;对电池组装的车间要求低(无需密封,干燥环境等);电极材料能够在水系电池中稳定存在,可最大程度地抑制电池在充放过程中水分子的副反应,从而提高电池的容量和循环稳定性,循环次数可达1000次以上,高于铅酸电池(400次)和有机系锂/钠离子电池(500-1000次),可满足储能电站生命周期需求;2) For the water-based ion battery provided by this application, the electrode preparation process of this type of organic negative electrode material is simple; the workshop requirements for battery assembly are low (no need for sealing, dry environment, etc.); the electrode material can exist stably in the water-based battery, and can suppress the side reaction of water molecules during the charging and discharging process of the battery to the greatest extent, thereby improving the capacity and cycle stability of the battery. life cycle requirements;

3)本申请所提供的水系离子电池,含有萘环的聚酰亚胺类有机电极材料,作为负极用于水系钠离子电池,正极使用嵌钠体系的金属氧化物材料。该水系电池具有绝对安全(不起火不爆炸),具有高循环寿命(>1000次),无贵金属环境友好,成本可控,快充(水系中钠离子传导好),和大的温度使用范围等优点(盐水下可低温,上可高温)。非常适合大规模储能的应用;3) The aqueous ion battery provided by the present application, the polyimide organic electrode material containing naphthalene ring is used as the negative electrode for the aqueous sodium ion battery, and the positive electrode uses the metal oxide material of the sodium intercalation system. The water-based battery is absolutely safe (no fire or explosion), high cycle life (>1000 times), no precious metals, environmentally friendly, cost controllable, fast charging (good sodium ion conduction in the water system), and a large temperature range (low temperature under salt water, high temperature above). Very suitable for large-scale energy storage applications;

4)该水系电池的大的温度使用范围(-35℃到40℃),可以满足极端环境下的储能电站使用需求。其快充性能可以满足储能系统中的调频需求。此外,也可满足再生能源并网和辅助服务领域等应用场景。在削峰填谷、调峰调频、改善电能质量为主要需求的发电侧和用户侧储能领域,水系储能电池也拥有很好的应用前景。4) The large temperature range of the aqueous battery (-35°C to 40°C) can meet the needs of energy storage power stations in extreme environments. Its fast charging performance can meet the frequency regulation requirements in the energy storage system. In addition, it can also meet application scenarios such as renewable energy grid connection and ancillary services. Aqueous energy storage batteries also have good application prospects in the field of energy storage on the power generation side and the user side where peak-shaving and valley-filling, peak-shaving and frequency modulation, and improvement of power quality are the main demands.

附图说明Description of drawings

图1为本申请实施例4基于聚酰亚胺负极和锰酸钠正极的水系全电池的充放电曲线图;Fig. 1 is the charge-discharge curve diagram of the aqueous full battery based on polyimide negative electrode and sodium manganate positive electrode in embodiment 4 of the present application;

图2为本申请实施例4基于聚酰亚胺负极和锰酸钠正极的水系全电池的循环性能曲线图。FIG. 2 is a graph showing the cycle performance of an aqueous full battery based on a polyimide negative electrode and a sodium manganate positive electrode in Example 4 of the present application.

具体实施方式Detailed ways

下面结合实施例详述本申请,但本申请并不局限于这些实施例。The present application is described in detail below in conjunction with the examples, but the present application is not limited to these examples.

如无特别说明,本申请的实施例中的原料均通过商业途径购买。Unless otherwise specified, the raw materials in the examples of the present application were purchased through commercial channels.

本申请的实施例中分析方法如下:Analytic method is as follows in the embodiment of the application:

利用新威电池测试仪(型号:CT-4008-5V20mA-164,深圳市新威尔电子有限公司)进行电化学性能测试。在测试仪器上,设置以下程序:搁置1min时间;以1.0C电流恒流充电至1.9V;再搁置1min;然后以1.0C电流恒流放电至0.7V;重复上述充放电步骤800次。The electrochemical performance test was carried out by Xinwei battery tester (model: CT-4008-5V20mA-164, Shenzhen Xinwei Electronics Co., Ltd.). On the test instrument, set the following program: put it aside for 1min; charge to 1.9V with a constant current of 1.0C; rest for 1min; then discharge to 0.7V with a constant current of 1.0C; repeat the above charging and discharging steps 800 times.

实施例1合成负极活性物质Embodiment 1 synthesis of negative electrode active material

步骤A:在400mL N-二甲基甲酰胺(DMF)的溶液中按照摩尔比1:1.01加入52.08g1,4,5,8-萘四甲酸酐粉末与2.54mL一水合乙二胺溶液,保持磁力搅拌。反应容器为玻璃烧瓶。对烧瓶进行氩气保护。将烧瓶转移到50℃油浴中,并逐步升温至150℃。在该温度下保持反应4小时。Step A: Add 52.08g of 1,4,5,8-naphthalenetetracarboxylic anhydride powder and 2.54mL of ethylenediamine monohydrate solution in 400mL of N-dimethylformamide (DMF) solution at a molar ratio of 1:1.01, and keep magnetic stirring. The reaction vessel is a glass flask. The flask was protected with argon. The flask was transferred to a 50°C oil bath, and the temperature was gradually raised to 150°C. The reaction was maintained at this temperature for 4 hours.

步骤B:将生成物收集,离心,去除上清液。对于下方离心沉淀物用N-二甲基甲酰胺稀释清洗,进行第二次离心。再用乙醇进行清洗离心。最终物质在真空烘箱中烘干,得到干粉。Step B: Collect the product, centrifuge, and remove the supernatant. For the centrifuged sediment below, it was diluted and washed with N-dimethylformamide, and a second centrifugation was performed. Wash and centrifuge with ethanol. The final material was dried in a vacuum oven to obtain a dry powder.

步骤C:将上述干粉在管式炉中进行烧结,氩气气氛保护。烧结的温度为350℃,烧结时间为3小时,得到样品1。Step C: sintering the above dry powder in a tube furnace under the protection of argon atmosphere. The sintering temperature was 350° C. and the sintering time was 3 hours to obtain Sample 1 .

实施例2电极的制备The preparation of embodiment 2 electrodes

负极negative electrode

活性物质:含有萘环的聚酰亚胺有机材料样品1Active material: polyimide organic material sample 1 containing naphthalene ring

导电剂:导电炭黑(Super P carbon)Conductive agent: conductive carbon black (Super P carbon)

粘结剂:聚四氟乙烯(PTFE)乳液Binder: polytetrafluoroethylene (PTFE) emulsion

集流体:不锈钢网Current collector: stainless steel mesh

制备流程:将活性物质、导电炭黑、粘结剂按照质量比例为6:3:1,在乙醇溶液中混合搅拌形成泥浆状,涂覆到不锈钢网上,然后真空烘干。电极面积约为1.5cm2,活性物质的单面面密度为2mg·cm-2Preparation process: The active material, conductive carbon black, and binder are mixed and stirred in an ethanol solution according to the mass ratio of 6:3:1 to form a slurry, coated on a stainless steel mesh, and then vacuum-dried. The electrode area is about 1.5 cm 2 , and the density of one side of the active material is 2 mg·cm -2 .

实施例3电极的制备The preparation of embodiment 3 electrodes

正极:positive electrode:

活性物质:锰酸钠(NaMnO2,即嵌入了钠离子的λ-MnO2)Active substance: Sodium manganate (NaMnO 2 , i.e. λ-MnO 2 intercalated with sodium ions)

导电剂:导电炭黑(Super P carbon)Conductive agent: conductive carbon black (Super P carbon)

粘结剂:聚四氟乙烯(PTFE)乳液Binder: polytetrafluoroethylene (PTFE) emulsion

集流体:不锈钢网Current collector: stainless steel mesh

流程:将活性物质、导电炭黑、粘结剂按照质量比例为8:1:1,在乙醇中混合搅拌形成泥浆状,涂覆到不锈钢网上,然后真空烘干。电极面积约为1.5cm2,活性物质的单面面密度为5mg·cm-2Process: The active material, conductive carbon black, and binder are mixed in ethanol at a mass ratio of 8:1:1 to form a slurry, coated on a stainless steel mesh, and then vacuum-dried. The electrode area is about 1.5 cm 2 , and the density of one side of the active material is 5 mg·cm -2 .

实施例4电池的组装The assembly of embodiment 4 battery

结构组成Structure and composition

电解液:2.5M硫酸钠(Na2SO4)水溶液Electrolyte: 2.5M sodium sulfate (Na 2 SO 4 ) aqueous solution

隔膜:玻璃纤维滤纸(孔隙率1微米以下,厚度260微米左右)Diaphragm: glass fiber filter paper (porosity below 1 micron, thickness about 260 microns)

负极:含有萘环的聚酰亚胺电极Negative electrode: polyimide electrode containing naphthalene ring

正极:锰酸钠电极Positive electrode: sodium manganate electrode

组装过程:将负极壳放于绝缘平台面上,将负极极片置于负极壳中心;然后,将隔膜平放于负极极片上层,用移液器取适量电解液滴加入隔膜表面,让电解液充分浸润隔膜和极片;随后,用绝缘镊子将正极极片、垫片、弹簧片和正极壳依次置于隔膜上层;其中,涂覆有电极材料的正负极极片一面朝向并贴近隔膜;最后,用绝缘镊子将电池置于电池封口机模具上,调整压力为850Pa,保压时间为5秒;至此,就完成了整个电池的组装。Assembly process: place the negative electrode shell on the insulating platform, and place the negative electrode piece in the center of the negative electrode shell; then, place the diaphragm flat on the upper layer of the negative electrode plate, and use a pipette to take an appropriate amount of electrolyte and add it to the surface of the diaphragm to allow the electrolyte to fully infiltrate the diaphragm and the pole piece; then, use insulating tweezers to place the positive electrode piece, gasket, spring piece, and positive electrode case on the upper layer of the diaphragm in sequence; among them, the positive and negative pole pieces coated with electrode materials are facing and close to the diaphragm; finally, using insulating tweezers Place the battery on the mold of the battery sealing machine, adjust the pressure to 850Pa, and hold the pressure for 5 seconds; so far, the assembly of the entire battery is completed.

实施例5电池的组装The assembly of embodiment 5 batteries

结构组成与实施例4相似,区别在于,电解质为2M硫酸钠(Na2SO4)水溶液。The structural composition is similar to that of Example 4, except that the electrolyte is a 2M sodium sulfate (Na 2 SO 4 ) aqueous solution.

实施例6电池的组装The assembly of embodiment 6 batteries

结构组成与实施例4相似,区别在于,电解质为1.5M硫酸钠(Na2SO4)水溶液。The structural composition is similar to that of Example 4, except that the electrolyte is a 1.5M sodium sulfate (Na 2 SO 4 ) aqueous solution.

实施例7电池的组装The assembly of embodiment 7 batteries

结构组成与实施例4相似,区别在于,正极为Na2CoFe(CN)6The structural composition is similar to that of Example 4, except that the positive electrode is Na 2 CoFe(CN) 6 .

实施例8电池的组装The assembly of embodiment 8 batteries

结构组成与实施例4相似,区别在于,正极为Na2NiFe(CN)6The structural composition is similar to that of Example 4, except that the positive electrode is Na 2 NiFe(CN) 6 .

实施例9电池的组装The assembly of embodiment 9 batteries

结构组成与实施例4相似,区别在于,正极为Na0.44MnO2The structural composition is similar to that of Example 4, except that the positive electrode is Na 0.44 MnO 2 .

实施例10电池的组装The assembly of embodiment 10 battery

结构组成与实施例4相似,区别在于,正极为NaFeFe(CN)6The structural composition is similar to that of Example 4, except that the positive electrode is NaFeFe(CN) 6 .

实施例11电池的组装The assembly of embodiment 11 batteries

结构组成与实施例4相似,区别在于,正极为Na0.95MnO2The structural composition is similar to that of Example 4, except that the positive electrode is Na 0.95 MnO 2 .

实施例12电池性能测试Embodiment 12 battery performance test

测试条件:使用时先充电,之后进行放电和充电循环往复。充放电电流:1C=100mA/g。Test conditions: charge first when using, then discharge and charge repeatedly. Charge and discharge current: 1C=100mA/g.

基于聚酰亚胺负极和锰酸钠正极的水系全电池的充放电曲线,如图1所示,对应实施例4中的组装的电池。图1中显示,第一圈的可逆充放电比容量有117mAh/g。The charge-discharge curve of the aqueous full battery based on the polyimide negative electrode and the sodium manganate positive electrode is shown in FIG. 1 , which corresponds to the battery assembled in Example 4. As shown in Figure 1, the reversible charge-discharge specific capacity of the first cycle is 117mAh/g.

基于聚酰亚胺负极和锰酸钠正极的水系全电池的循环性能曲线图,如图2所示,对应实施例4中的组装的电池。充放电电流:1C=100mA/g。图2显示,在第3圈以后,充放电库伦效率可达98%以上,并一直保持。说明放电容量和充电容量都充分利用,几乎无副反应。在循环了800圈以后,容量依然有112mAh/g,容量保持率高达96%以上。The cycle performance curve of the aqueous full battery based on the polyimide negative electrode and the sodium manganate positive electrode is shown in FIG. 2 , which corresponds to the battery assembled in Example 4. Charge and discharge current: 1C=100mA/g. Figure 2 shows that after the third cycle, the charging and discharging Coulombic efficiency can reach more than 98%, and has been maintained. It shows that the discharge capacity and charge capacity are fully utilized, and there is almost no side reaction. After 800 cycles, the capacity is still 112mAh/g, and the capacity retention rate is as high as 96%.

正负极活性质量比(P/N)对全电池循环稳定性的影响。研究发现,当P/N=1.5时候,也就是正极锰酸钠质量小于负极有机物活性质量2倍时,电池容量衰减较快,800圈以后充放电容量衰减到第1圈的83%;当P/N=2.5时候,也就是正极锰酸钠质量大过量于负极有机物活性质量2倍时,电池容量保持较高的稳定性,800圈以后充放电比容量保持率高达96%以上,实验数据如表1所示。The effect of positive and negative active mass ratio (P/N) on the cycle stability of full battery. The study found that when P/N=1.5, that is, when the mass of positive sodium manganate is less than twice the active mass of the negative organic matter, the battery capacity decays rapidly, and the charge and discharge capacity decays to 83% of the first cycle after 800 cycles;

表1Table 1

实施例5-11组装的电池的性能与实施例4组装电池性能相似。The performance of the battery assembled in Examples 5-11 is similar to that of the battery assembled in Example 4.

以上所述,仅是本申请的几个实施例,并非对本申请做任何形式的限制,虽然本申请以较佳实施例揭示如上,然而并非用以限制本申请,任何熟悉本专业的技术人员,在不脱离本申请技术方案的范围内,利用上述揭示的技术内容做出些许的变动或修饰均等同于等效实施案例,均属于技术方案范围内。The above are only a few embodiments of the present application, and do not limit the present application in any form. Although the present application discloses the above with preferred embodiments, it is not intended to limit the present application. Any skilled person who is familiar with this profession, without departing from the scope of the technical solution of the present application, making some changes or modifications using the technical content disclosed above are equivalent to equivalent implementation cases, and all belong to the scope of the technical solution.

Claims (23)

1. An aqueous ion battery comprising:
an electrolyte, wherein the electrolyte is an aqueous solution containing an electrolyte;
a negative electrode containing a negative electrode active material; the negative electrode active material contains polyimide having naphthalene rings; and
a positive electrode containing a positive electrode active material; the positive electrode active material is embedded with sodium material, and the sodium material is Na x MnO 2
Wherein:
NaMnO 2 lambda-MnO for intercalation of sodium ions 2
x is 0.44-0.95;
the mass ratio of the positive electrode active material to the negative electrode active material is 2-4; wherein the mass of the negative electrode active material is calculated by the mass of polyimide containing naphthalene ring, and the mass of the positive electrode active material is calculated by the mass of sodium intercalation material.
2. The aqueous ion battery of claim 1, wherein the polyimide containing a naphthalene ring has a chemical formula as shown in formula I:
i is a kind of
Wherein n=1000 to 10000.
3. The aqueous ion battery according to claim 1, wherein the electrolyte is at least one selected from the group consisting of sodium sulfate, sodium nitrate, sodium phosphate, sodium carbonate, sodium permanganate, sodium chloride, sodium bromide, and sodium iodide.
4. The aqueous ion battery according to claim 1, wherein the concentration of the electrolyte in the electrolyte solution is 1.5m to 2.5m.
5. The aqueous ionic cell of claim 1, further comprising a separator separating the positive electrode and the negative electrode and passing electrolyte ions.
6. The aqueous ion battery according to claim 5, wherein the separator is at least one member selected from the group consisting of glass fiber filter paper, an adsorption type glass fiber film and a nonwoven fabric.
7. The aqueous ion battery according to claim 1, wherein the method for producing the negative electrode comprises the steps of:
mixing raw materials containing a negative electrode active material, a conductive agent and a binder with a solvent to obtain slurry, coating the slurry on a current collector, and drying to obtain the negative electrode.
8. The aqueous ion battery according to claim 7, wherein the mass ratio of the negative electrode active material, the conductive agent, and the binder is 5.5 to 9.6: 0.25-3: 0.25 to 1.25.
9. The aqueous ion battery according to claim 7, wherein the solvent is at least one selected from the group consisting of absolute ethyl alcohol, N-methylpyrrolidone, and N-dimethylformamide.
10. The aqueous ion battery according to claim 7, wherein the binder is at least one selected from polyvinylidene fluoride, carboxymethyl cellulose, polytetrafluoroethylene, and styrene-butadiene rubber.
11. The aqueous ion battery according to claim 7, wherein the conductive agent is at least one selected from the group consisting of conductive carbon black, acetylene black, carbon nanotubes, superconducting carbon black, carbon fibers, and conductive graphite.
12. The aqueous ion battery according to claim 7, wherein the current collector is at least one selected from the group consisting of a stainless steel sheet, a stainless steel mesh, and a stainless steel foil.
13. The aqueous ion battery according to claim 7, wherein the surface density of the negative electrode active material in the current collector is 2 to 5mg/cm 2
14. The aqueous ion battery according to claim 1, wherein the method for producing the positive electrode comprises the steps of:
mixing raw materials containing positive electrode active substances, a conductive agent and a binder with a solvent to obtain slurry, coating the slurry on a current collector, and drying to obtain the positive electrode.
15. The aqueous ion battery according to claim 14, wherein the mass ratio of the positive electrode active material, the conductive agent, and the binder is 7.5 to 9.6: 0.25-2.25: 0.25 to 2.25.
16. The aqueous ion battery according to claim 14, wherein the solvent is at least one selected from the group consisting of absolute ethyl alcohol, N-methylpyrrolidone, and N-dimethylformamide.
17. The aqueous ion battery according to claim 14, wherein the binder is at least one selected from polyvinylidene fluoride, carboxymethyl cellulose, polytetrafluoroethylene, and styrene-butadiene rubber.
18. The aqueous ion battery of claim 14, wherein the conductive agent is at least one selected from the group consisting of conductive carbon black, acetylene black, carbon nanotubes, superconducting carbon black, carbon fibers, and conductive graphite.
19. The aqueous ion battery of claim 14 wherein the current collector is selected from at least one of stainless steel sheet, stainless steel mesh, stainless steel foil.
20. The aqueous ion battery according to claim 14, wherein the positive electrode active material has an areal density of 3 to 8mg/cm in the current collector 2
21. The aqueous ion battery according to claim 1, wherein the method for producing the negative electrode active material comprises the steps of:
reacting a solution containing 1,4,5, 8-naphthalene tetracarboxylic anhydride and ethylenediamine for 4-18 hours at 120-180 ℃ in an inactive atmosphere, separating, washing and drying to obtain dry powder;
sintering the dry powder in an inactive atmosphere to obtain the anode active material;
the inactive atmosphere is at least one selected from nitrogen, helium and argon.
22. Use of the aqueous ion battery of any one of claims 1 to 21 for energy storage.
23. Use of the aqueous ion battery of any one of claims 1 to 21 in an aqueous energy storage battery.
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Publication number Priority date Publication date Assignee Title
CN111477853B (en) * 2020-04-17 2022-06-10 北京恩力动力科技有限公司 Aqueous sodium-based mixed ion secondary battery
CN111584867B (en) * 2020-05-15 2021-07-13 宁波锋成纳米科技有限公司 Electrode and preparation method and application thereof
CN111900387B (en) * 2020-07-28 2022-05-17 宁波锋成先进能源材料研究院 Water-based battery pole piece material, water-based battery pole piece, preparation method and application thereof
CN113381097B (en) * 2021-06-03 2022-07-15 中国科学技术大学 Aqueous prussian blue derivative-hydrogen secondary battery
CN114927686A (en) * 2022-05-27 2022-08-19 哈尔滨工程大学 Preparation method and application of novel aqueous magnesium-sodium mixed ion battery cathode material
CN115051046A (en) * 2022-06-22 2022-09-13 松山湖材料实验室 Aqueous manganese ion battery and preparation process thereof
CN115275208B (en) * 2022-09-27 2023-02-07 宇恒电池股份有限公司 High-specific-energy aqueous lithium ion battery and preparation method thereof

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20050030763A (en) * 2003-09-26 2005-03-31 삼성에스디아이 주식회사 Rechargeable lithium ion battery
CN103219551A (en) * 2013-03-27 2013-07-24 恩力能源科技(南通)有限公司 Water-system alkali metal ion power storage device
CN104779394A (en) * 2015-04-17 2015-07-15 复旦大学 Aqueous lithium (sodium) ion battery mixed negative material
CN105960724A (en) * 2014-02-04 2016-09-21 三井化学株式会社 Negative electrode for lithium ion secondary cell, lithium-ion secondary cell, mixture paste for negative electrode for lithium-ion secondary cell, and method for manufacturing negative electrode for lithium-ion secondary cell
CN107768670A (en) * 2017-10-23 2018-03-06 东莞理工学院 Positive electrode material, preparation method and application, positive electrode preparation method
CN109888411A (en) * 2019-04-09 2019-06-14 南开大学 A high-rate, long-cycle, wide-temperature water-based sodium-ion full battery

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20050030763A (en) * 2003-09-26 2005-03-31 삼성에스디아이 주식회사 Rechargeable lithium ion battery
CN103219551A (en) * 2013-03-27 2013-07-24 恩力能源科技(南通)有限公司 Water-system alkali metal ion power storage device
CN105960724A (en) * 2014-02-04 2016-09-21 三井化学株式会社 Negative electrode for lithium ion secondary cell, lithium-ion secondary cell, mixture paste for negative electrode for lithium-ion secondary cell, and method for manufacturing negative electrode for lithium-ion secondary cell
CN104779394A (en) * 2015-04-17 2015-07-15 复旦大学 Aqueous lithium (sodium) ion battery mixed negative material
CN107768670A (en) * 2017-10-23 2018-03-06 东莞理工学院 Positive electrode material, preparation method and application, positive electrode preparation method
CN109888411A (en) * 2019-04-09 2019-06-14 南开大学 A high-rate, long-cycle, wide-temperature water-based sodium-ion full battery

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
Long Chen等."Polyimide as anode electrode material for rechargeable sodium batteries".《The Royal Society of Chemistry》.2014,25369-25373. *

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