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CN102709587B - A kind of lithium ion battery and cathode current collector thereof - Google Patents

A kind of lithium ion battery and cathode current collector thereof Download PDF

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CN102709587B
CN102709587B CN201210005082.XA CN201210005082A CN102709587B CN 102709587 B CN102709587 B CN 102709587B CN 201210005082 A CN201210005082 A CN 201210005082A CN 102709587 B CN102709587 B CN 102709587B
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current collector
lithium ion
ion battery
cathode current
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CN102709587A (en
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许国成
袁庆丰
赵丰刚
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Ningde Amperex Technology Ltd
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Abstract

本发明属于锂离子电池技术领域,特别涉及一种改善锂离子电池安全性能的阴极集流体及包含该阴极集流体的锂离子电池。包括阴极集流体本体,所述阴极集流体本体表面还覆盖有处理层,按重量百分比计,所述处理层由70~80wt%的共轭大π键导电高分子、19.4~29.8wt%的粘结剂和0.2~0.6wt%的草酸组成。相对于现有技术,本发明利用导电高分子的电化学活性特点,将其用在阴极集流体的处理层中,从而改善锂离子电池的防过充过放特性,起到改善电池安全性能的作用。此外,本发明实施简单,便于工业化。此外,本发明还公开了一种包含该阴极集流体的锂离子电池。The invention belongs to the technical field of lithium ion batteries, and in particular relates to a cathode current collector for improving the safety performance of the lithium ion battery and a lithium ion battery comprising the cathode current collector. Including the cathode current collector body, the surface of the cathode current collector body is also covered with a treatment layer, and the treatment layer is composed of 70-80 wt% of a conjugated large π bond conductive polymer, 19.4-29.8 wt% of a viscous Binder and 0.2-0.6wt% oxalic acid. Compared with the prior art, the present invention utilizes the electrochemically active characteristics of conductive polymers and uses them in the treatment layer of the cathode current collector, thereby improving the anti-overcharge and overdischarge characteristics of lithium-ion batteries and improving the safety performance of the batteries. effect. In addition, the present invention is simple to implement and convenient for industrialization. In addition, the invention also discloses a lithium ion battery comprising the cathode current collector.

Description

一种锂离子电池及其阴极集流体A kind of lithium ion battery and cathode current collector thereof

技术领域technical field

本发明属于锂离子电池技术领域,特别涉及一种改善锂离子电池安全性能的阴极集流体及包含该阴极集流体的锂离子电池。The invention belongs to the technical field of lithium ion batteries, and in particular relates to a cathode current collector for improving the safety performance of the lithium ion battery and a lithium ion battery comprising the cathode current collector.

背景技术Background technique

1991年,日本索尼(Sony)公司率先将锂离子电池商业化以来,由于其具有高能量密度、高电压、低自放电率和重量轻等优点,在各种领域得到了广泛应用。随着全球能源危机的加剧及对环保的重视,锂离子电池作为一种绿色环保能源备受关注,近年来,锂离子电池已逐渐应用在风力发电储能系统和电动汽车(EV,HEV,PHEV)中。在这些应用中,人们对电池的安全性能特别关注。In 1991, Japan's Sony (Sony) took the lead in commercializing lithium-ion batteries. Due to its advantages of high energy density, high voltage, low self-discharge rate and light weight, it has been widely used in various fields. With the intensification of the global energy crisis and the emphasis on environmental protection, lithium-ion batteries have attracted much attention as a green energy source. In recent years, lithium-ion batteries have been gradually used in wind power storage systems and electric vehicles (EV, HEV, PHEV )middle. In these applications, people pay special attention to the safety performance of the battery.

对锂离子电池而言,不论是单体电池还是将单体电池组装成电池组,在使用过程中都会存在过充过放等问题。这些问题对电池的循环寿命及安全性能是个极大的考验。因为在充电过程中,电能在阳极是以LiC6的形式储存起来,随着充电的不断进行,该体系的安全性能不断降低。For lithium-ion batteries, whether it is a single battery or assembled into a battery pack, there will be problems such as overcharging and over-discharging during use. These problems are a great test for the cycle life and safety performance of the battery. Because the electrical energy is stored in the form of LiC 6 at the anode during the charging process, the safety performance of the system continues to decrease as the charging continues.

当过充发生时,很容易使得电解液被分解,电池产生大量热量,从而导致电池起火甚至引起爆炸,给电池/电池组的使用带来严重的安全隐患。目前防护电池过充的措施包括在保护板上增加正温度系数热敏电阻(PTC)或对隔离膜进行特殊处理,当电池过充发热导致温度超过一定值时,保护装置开始工作。这两种措施可以有效的改善过充安全,但它们的作用机理略有差异:PTC的作用机理是该保护模块的电阻随温度上升而急剧增大,但它发挥作用的温度较高,此时的高温对电池产生了恶劣的负面影响;而处理隔离膜防过充的机理是电池发热产生的高温使隔膜发生闭孔,使得过充不能继续进行,从而起到保护作用。但此时隔膜已经发生闭孔,对电池造成永久性破坏,使得电池后续的充放电难以进行。When overcharging occurs, it is easy to cause the electrolyte to be decomposed, and the battery generates a lot of heat, causing the battery to catch fire or even explode, which brings serious safety hazards to the use of the battery/battery pack. The current measures to protect the battery from overcharging include adding a positive temperature coefficient thermistor (PTC) on the protective plate or performing special treatment on the isolation film. When the battery is overcharged and the temperature exceeds a certain value due to overcharging, the protective device will start to work. These two measures can effectively improve overcharge safety, but their mechanism of action is slightly different: the mechanism of PTC is that the resistance of the protection module increases sharply with the rise of temperature, but the temperature at which it works is relatively high. The high temperature has a bad negative impact on the battery; and the mechanism of dealing with the anti-overcharge of the separator is that the high temperature generated by the heating of the battery causes the diaphragm to close the pores, so that the overcharge cannot continue, thus playing a protective role. But at this time, the diaphragm has closed pores, causing permanent damage to the battery, making subsequent charging and discharging of the battery difficult.

另一方面,当电池过放时,阳极电位升高,当电位高于一定值时,阳极集流体发生氧化溶解,导致电池性能恶化,严重影响电池后续的电化学性能。目前防过放的手段主要是通过外部电子电路进行监控,这对单体电池起到很好的保护作用,但如果在电池组中要开发电路模块监控每个电池,不但会大大的增加电池组的成本,而且并不能十分有效的改善电池组中每个电池的防过放性能。On the other hand, when the battery is over-discharged, the potential of the anode rises. When the potential is higher than a certain value, the anode current collector oxidizes and dissolves, resulting in deterioration of battery performance and seriously affecting the subsequent electrochemical performance of the battery. At present, the means of preventing over-discharge is mainly through external electronic circuit monitoring, which plays a very good role in protecting the single battery, but if a circuit module is to be developed in the battery pack to monitor each battery, it will not only greatly increase the battery life. cost, and it cannot effectively improve the over-discharge prevention performance of each battery in the battery pack.

有鉴于此,确有必要提供一种在不影响锂离子电池正常电化学性能的前提下,能够显著的改善锂离子电池体系防过充过放特性,从而有效的改善电池的安全性能的锂离子电池阴极集流体及包含该阴极集流体的锂离子电池。In view of this, it is necessary to provide a lithium-ion battery that can significantly improve the anti-overcharge and over-discharge characteristics of the lithium-ion battery system without affecting the normal electrochemical performance of the lithium-ion battery, thereby effectively improving the safety performance of the battery. A battery cathode collector and a lithium ion battery comprising the cathode collector.

发明内容Contents of the invention

本发明的目的之一在于:针对现有技术的不足,而提供一种在不影响锂离子电池正常电化学性能的前提下,能够显著的改善锂离子电池体系防过充过放特性,从而有效的改善电池的安全性能的锂离子电池阴极集流体。One of the purposes of the present invention is to: address the deficiencies of the prior art, and provide a lithium-ion battery system that can significantly improve the anti-overcharge and over-discharge characteristics of the lithium-ion battery system without affecting the normal electrochemical performance of the lithium-ion battery, thereby effectively A lithium-ion battery cathode current collector for improving battery safety performance.

为了达到上述目的,本发明采用如下技术方案:In order to achieve the above object, the present invention adopts following technical scheme:

一种锂离子电池阴极集流体,包括阴极集流体本体,所述阴极集流体本体表面还覆盖有处理层,按重量百分比计,所述处理层由70~80wt%的共轭大π键导电高分子、19.4~29.8wt%的粘结剂和0.2~0.6wt%的草酸组成。A lithium ion battery cathode current collector, comprising a cathode current collector body, the surface of the cathode current collector body is also covered with a treatment layer, and the treatment layer is composed of 70 to 80 wt% of conjugated large π bonds with high conductivity Molecules, 19.4-29.8 wt% binder and 0.2-0.6 wt% oxalic acid.

采用该处理层处理的阴极集流体,少量的草酸在处理过程中对阴极集流体本体进行刻蚀,增加阴极集流体表面的粗糙度,有利于提高处理层与阴极集流体本体的粘结能力,草酸的重量百分比选择为0.2~0.6wt%,是因为若草酸含量太小,则对阴极集流体本体的腐蚀作用不够,导致阴极集流体本体的粗糙度不够,不利于阴极集流体本体和处理层的粘接,而如果草酸含量太大,则可能将阴极集流体本体腐蚀穿,不利于电池的制备;粘接剂则将处理层中的草酸和共轭大π键导电高分子颗粒粘接在一起,并将整个处理层粘接在阴极集流体的表面,粘接剂的重量百分比选择为19.4~29.8wt%是因为:若粘接剂的含量太低,则颗粒间粘接作用不强,容易产生掉粉等问题,而如果粘接剂的含量太大,则由于粘接剂本身不导电,会造成电池性能的劣化;共轭大π键导电高分子只能在某些特定电化学窗口起电子导通作用,当阴极电位过高(或过低),超出该特定电化学窗口时,该处理层电阻急剧增大起到电子绝缘作用,电池回路在阴极内部被断开,很好的起到防止过充过放特性,对电池起到很好的保护作用,当电位降低(或者升高)回到其电化学活性窗口时,该处理层又能导通电子,电池恢复正常工作。本发明正是利用导电高分子的电化学活性特点,将其用在阴极集流体的处理层中,从而改善锂离子电池的防过充过放特性,起到改善电池安全性能的作用。此外,本发明实施简单,便于工业化,而且对电池起保护作用的同时不会破坏电池体系和损害电池性能,解决了在不损坏电池的前提下改善电池/电池组安全性能的技术难题。The cathode current collector treated with this treatment layer, a small amount of oxalic acid etches the cathode current collector body during the treatment process, increasing the surface roughness of the cathode current collector, which is conducive to improving the bonding ability between the treatment layer and the cathode current collector body, The weight percentage of oxalic acid is selected as 0.2-0.6wt%, because if the oxalic acid content is too small, the corrosion effect on the cathode current collector body is not enough, resulting in insufficient roughness of the cathode current collector body, which is not conducive to the cathode current collector body and the treatment layer. If the oxalic acid content is too large, the body of the cathode current collector may be corroded, which is not conducive to the preparation of the battery; the adhesive will bond the oxalic acid in the treatment layer and the conjugated large π bond conductive polymer particles to the together, and the whole treatment layer is bonded on the surface of the cathode current collector, the weight percentage of the binder is selected as 19.4~29.8wt% because: if the content of the binder is too low, the bonding effect between the particles is not strong, It is easy to cause problems such as powder falling, and if the content of the binder is too large, the battery performance will be deteriorated because the binder itself is not conductive; the conjugated large π bond conductive polymer can only be used in certain specific electrochemical windows. It plays the role of electronic conduction. When the cathode potential is too high (or too low) and exceeds the specific electrochemical window, the resistance of the treatment layer increases sharply to play the role of electronic insulation, and the battery circuit is disconnected inside the cathode, which is very good It has the characteristics of preventing overcharge and overdischarge, and plays a very good role in protecting the battery. When the potential decreases (or increases) and returns to its electrochemical active window, the treatment layer can conduct electrons again, and the battery resumes normal operation. The present invention utilizes the electrochemical activity characteristics of the conductive polymer and uses it in the treatment layer of the cathode current collector, thereby improving the anti-overcharge and overdischarge characteristics of the lithium-ion battery and improving the safety performance of the battery. In addition, the invention is easy to implement, easy to industrialize, and protects the battery without damaging the battery system and battery performance, and solves the technical problem of improving the safety performance of the battery/battery pack without damaging the battery.

作为本发明锂离子电池阴极集流体的一种改进,所述的共轭大π键导电高分子为聚苯胺、聚-2,5-二甲氧基苯胺、聚间甲氧基苯胺和聚邻甲苯胺中的至少一种,这些导电高分子相对于Li+/Li电极的电化学活性电位是2.9V~3.8V,当电位在2.9V~3.8V之间时该处理层是电子良导体,而当电位低于2.9V或者高于3.8V时该处理层是绝缘体。As an improvement of the lithium ion battery cathode current collector of the present invention, the conjugated large π bond conductive polymer is polyaniline, poly-2,5-dimethoxyaniline, poly-m-methoxyaniline and poly-o- At least one of toluidine, the electrochemical active potential of these conductive polymers relative to the Li + /Li electrode is 2.9V ~ 3.8V, when the potential is between 2.9V ~ 3.8V, the treatment layer is a good electronic conductor, The handle layer is an insulator when the potential is lower than 2.9V or higher than 3.8V.

作为本发明锂离子电池阴极集流体的一种改进,所述的粘结剂为聚偏氟乙烯和聚四氟乙烯中的至少一种。As an improvement of the lithium ion battery cathode current collector of the present invention, the binder is at least one of polyvinylidene fluoride and polytetrafluoroethylene.

作为本发明锂离子电池阴极集流体的一种改进,所述的处理层通过挤压涂布方式覆盖在所述阴极集流体本体表面。As an improvement of the lithium ion battery cathode collector of the present invention, the treatment layer is covered on the surface of the cathode collector body by extrusion coating.

作为本发明锂离子电池阴极集流体的一种改进,所述的处理层通过静电印刷方式覆盖在所述阴极集流体本体表面。As an improvement of the lithium ion battery cathode collector of the present invention, the treatment layer is covered on the surface of the cathode collector body by electrostatic printing.

作为本发明锂离子电池阴极集流体的一种改进,所述的处理层厚度小于5um。若处理层的厚度太大,则会导致电池整体厚度的增大,从而影响电池的能量密度。As an improvement of the lithium ion battery cathode current collector of the present invention, the thickness of the treatment layer is less than 5um. If the thickness of the treatment layer is too large, the overall thickness of the battery will increase, thereby affecting the energy density of the battery.

作为本发明锂离子电池阴极集流体的一种改进,所述的处理层厚度为3um。As an improvement of the lithium ion battery cathode current collector of the present invention, the thickness of the treatment layer is 3um.

作为本发明锂离子电池阴极集流体的一种改进,所述的阴极集流体本体为铝箔或不锈钢片。As an improvement of the lithium ion battery cathode collector of the present invention, the cathode collector body is aluminum foil or stainless steel sheet.

本发明的另一个目的在于提供一种包含上述阴极集流体的锂离子电池,一种锂离子电池,包括阴极集流体和涂覆在所述阴极集流体上的阴极活性物质层,阳极集流体和涂覆在所述阳极集流体上的阳极活性物质层,隔离膜,以及电解液,所述阴极集流体为上述段落所述的锂离子电池阴极集流体。Another object of the present invention is to provide a lithium ion battery comprising the above-mentioned cathode collector, a lithium ion battery comprising a cathode collector and a cathode active material layer coated on the cathode collector, an anode collector and An anode active material layer, a separator, and an electrolyte coated on the anode current collector, and the cathode current collector is the lithium ion battery cathode current collector described in the above paragraph.

作为本发明锂离子电池的一种改进,所述阴极活性物质层包括磷酸铁锂(LiFePO4),这是因为磷酸铁锂的可逆脱嵌锂电位是3.45V,正好在聚苯胺及其衍生物的电化学活性窗口(2.9V~3.8V)内。As an improvement of the lithium ion battery of the present invention, the cathode active material layer includes lithium iron phosphate (LiFePO 4 ), because the reversible lithium iron phosphate lithium deintercalation potential is 3.45V, just in the polyaniline and its derivatives. Within the electrochemical activity window (2.9V ~ 3.8V).

相对于现有技术,本发明锂离子电池由于其阴极集流体的处理层中引入了共轭大π键导电高分子,使其在保持电池性能的前提下,具有良好的安全特性。Compared with the prior art, the lithium-ion battery of the present invention has good safety characteristics under the premise of maintaining battery performance due to the introduction of conjugated large π-bond conductive polymers into the treatment layer of the cathode current collector.

附图说明Description of drawings

图1为本发明实施例1至6和对比例1的电池在常温时不同电压及内阻的曲线;Fig. 1 is the curves of different voltages and internal resistances of the batteries of Examples 1 to 6 of the present invention and Comparative Example 1 at normal temperature;

图2为本发明实施例1至6和对比例1的电池在常温时不同电压及内阻取对数后的曲线。Fig. 2 is the logarithmic curves of different voltages and internal resistances of the batteries of Examples 1 to 6 of the present invention and Comparative Example 1 at room temperature.

具体实施方式detailed description

下面结合具体实施方式和说明书附图,对本发明做进一步的说明。The present invention will be further described below in conjunction with specific implementation methods and accompanying drawings.

实施例1Example 1

阴极集流体处理层浆料的制备:Preparation of cathode current collector treatment layer slurry:

将草酸(C2H2O4)、导电聚苯胺(PANI)和粘结剂聚偏氟乙烯(PVDF)按照重量比0.2∶70∶29.8依次加入N-甲基吡咯烷酮(NMP)中搅拌均匀,NMP占浆料总重量的80wt%。搅拌均匀的浆料用200目不锈钢筛网过滤,即制得所需的阴极集流体处理层浆料。Add oxalic acid (C 2 H 2 O 4 ), conductive polyaniline (PANI) and binder polyvinylidene fluoride (PVDF) into N-methylpyrrolidone (NMP) in a weight ratio of 0.2:70:29.8 and stir evenly. NMP accounts for 80wt% of the total weight of the slurry. The uniformly stirred slurry is filtered with a 200-mesh stainless steel screen to obtain the required cathode collector treatment layer slurry.

阴极集流体的制备:Preparation of cathode current collector:

采用12um铝箔作为阴极集流体本体,将上述阴极集流体处理层浆料用凹版印刷机均匀地印刷在铝箔两面,印刷速度是2m/min,烘干温度为55℃,得到单面印刷层厚度为3um的处理集流体。Using 12um aluminum foil as the cathode current collector body, the above-mentioned cathode current collector treatment layer slurry was evenly printed on both sides of the aluminum foil with a gravure printing machine, the printing speed was 2m/min, and the drying temperature was 55°C. The thickness of the printed layer on one side was obtained. 3um processing current collector.

阴极极片的制备:Preparation of the cathode sheet:

将磷酸铁锂(LiFePO4)、超导碳(Super-P)和聚偏氟乙烯(PVDF)按重量比93∶2∶5加入N-甲基吡咯烷酮(NMP)中搅拌均匀,得到具有一定流动性的阴极浆料;然后,将阴极浆料涂布在上述处理好的阴极集流体上,鼓风干燥,随后利用辊压机进行冷压处理,裁剪等工序得到阴极极片。Add lithium iron phosphate (LiFePO 4 ), superconducting carbon (Super-P) and polyvinylidene fluoride (PVDF) into N-methylpyrrolidone (NMP) in a weight ratio of 93:2:5 and stir evenly to obtain a certain flow Then, the cathode slurry is coated on the above-mentioned treated cathode current collector, blown and dried, and then cold-pressed with a roller press, cut and other processes to obtain the cathode sheet.

阳极极片的制备:Preparation of the anode sheet:

将石墨、超导碳(Super-P)、聚偏氟乙烯(PVDF)按重量比96∶1∶3加入NMP中混合搅拌均匀,得到具有一定流动性的阳极浆料;然后,将阳极浆料涂布在9um的铜箔集流体上,鼓风干燥,随后利用辊压机进行冷压处理,裁剪等工序得到阳极极片。Add graphite, superconducting carbon (Super-P), and polyvinylidene fluoride (PVDF) into NMP in a weight ratio of 96:1:3 and mix and stir evenly to obtain an anode slurry with certain fluidity; then, the anode slurry Coated on a 9um copper foil current collector, air-dried, and then cold-pressed with a roller press, cut and other processes to obtain the anode sheet.

电池的组装:Assembly of the battery:

在阴极和阳极极片上焊接导电极耳,并按照正极极片、隔离膜和负极极片的顺序叠放整齐,其中的隔离膜为厚度为20um的聚丙烯(PP)/聚乙烯(PE)复合隔离膜。叠放整齐后将其卷绕成四方状,再用铝塑膜包装,注入非水电解液,电池的电解液为1mol/L的LiPF6溶液,溶剂为碳酸乙烯酯(EC)、碳酸丙烯酯(PC)和碳酸二甲酯(DMC)的混合物,三者的体积比为40∶20∶20。对铝塑膜进行封装后对电池进行化成和老化测试,得到长宽厚为109mm×101mm×3mm的方形软包装电池。Weld conductive lugs on the cathode and anode pole pieces, and stack them neatly in the order of the positive pole piece, the separator and the negative pole piece, and the separator is a polypropylene (PP)/polyethylene (PE) composite with a thickness of 20um isolation film. After stacking neatly, wind it into a square shape, then pack it with aluminum-plastic film, and inject non-aqueous electrolyte. The electrolyte of the battery is 1mol/L LiPF 6 solution, and the solvent is ethylene carbonate (EC), propylene carbonate (PC) and dimethyl carbonate (DMC), the volume ratio of the three is 40:20:20. After packaging the aluminum-plastic film, the formation and aging tests of the battery were carried out to obtain a square soft-packed battery with a length, width, and thickness of 109mm×101mm×3mm.

实施例2Example 2

与实施例1不同之处在于:阴极集流体处理层浆料中,草酸(C2H2O4)、导电聚苯胺(PANI)和粘结剂聚四氟乙烯(PTFE)的重量比为0.3∶72∶27.7,溶剂N-甲基吡咯烷酮(NMP)占浆料总重量的90wt%。The difference from Example 1 is that in the cathode collector treatment layer slurry, the weight ratio of oxalic acid (C 2 H 2 O 4 ), conductive polyaniline (PANI) and binder polytetrafluoroethylene (PTFE) is 0.3 :72:27.7, the solvent N-methylpyrrolidone (NMP) accounts for 90wt% of the total weight of the slurry.

阴极集流体本体为不锈钢片,厚度为10μm,且阴极集流体处理层浆料是通过挤压涂布的方式涂布在不锈钢片的两面,烘干后得到的处理层单面厚度为1um。The body of the cathode current collector is a stainless steel sheet with a thickness of 10 μm, and the cathode current collector treatment layer slurry is coated on both sides of the stainless steel sheet by extrusion coating, and the thickness of one side of the treatment layer obtained after drying is 1 μm.

其余同实施例1,这里不再赘述。The rest are the same as in Embodiment 1, and will not be repeated here.

实施例3Example 3

与实施例1不同之处在于:阴极集流体处理层浆料中,草酸(C2H2O4)、聚-2,5-二甲氧基苯胺和粘结剂聚四氟乙烯(PTFE)及聚偏氟乙烯(PVDF)的重量比为0.4∶74∶20∶5.6,溶剂N-甲基吡咯烷酮(NMP)占浆料总重量的70wt%。The difference from Example 1 is that in the cathode current collector treatment layer slurry, oxalic acid (C 2 H 2 O 4 ), poly-2,5-dimethoxyaniline and binder polytetrafluoroethylene (PTFE) The weight ratio of polyvinylidene fluoride (PVDF) is 0.4:74:20:5.6, and the solvent N-methylpyrrolidone (NMP) accounts for 70wt% of the total weight of the slurry.

阴极集流体本体为不锈钢片,厚度为12μm,且阴极集流体处理层浆料是通过挤压涂布的方式涂布在不锈钢片的两面,烘干后得到的处理层单面厚度为5um。The body of the cathode current collector is a stainless steel sheet with a thickness of 12 μm, and the cathode current collector treatment layer slurry is coated on both sides of the stainless steel sheet by extrusion coating, and the thickness of one side of the treatment layer obtained after drying is 5um.

其余同实施例1,这里不再赘述。The rest are the same as in Embodiment 1, and will not be repeated here.

实施例4Example 4

与实施例1不同之处在于:阴极集流体处理层浆料中,草酸(C2H2O4)、聚间甲氧基苯胺和粘结剂聚偏氟乙烯(PVDF)的重量比为0.5∶76∶23.5,溶剂N-甲基吡咯烷酮(NMP)占浆料总重量的75wt%。The difference from Example 1 is that in the cathode collector treatment layer slurry, the weight ratio of oxalic acid (C 2 H 2 O 4 ), poly-m-methoxyaniline and binder polyvinylidene fluoride (PVDF) is 0.5 :76:23.5, the solvent N-methylpyrrolidone (NMP) accounts for 75wt% of the total weight of the slurry.

将浆料通过凹版印刷机涂覆在厚度为12μm的铝箔上,烘干后得到的处理层单面厚度为4um。The slurry was coated on an aluminum foil with a thickness of 12 μm by a gravure printing machine, and the thickness of one side of the treatment layer obtained after drying was 4 μm.

其余同实施例1,这里不再赘述。The rest are the same as in Embodiment 1, and will not be repeated here.

实施例5Example 5

与实施例1不同之处在于:阴极集流体处理层浆料中,草酸(C2H2O4)、聚邻甲苯胺和粘结剂聚四氟乙烯(PTFE)及聚偏氟乙烯(PVDF)的重量比为0.55∶78∶21.45,溶剂N-甲基吡咯烷酮(NMP)占浆料总重量的85wt%。The difference from Example 1 is that in the cathode current collector treatment layer slurry, oxalic acid (C 2 H 2 O 4 ), poly-o-toluidine and binders polytetrafluoroethylene (PTFE) and polyvinylidene fluoride (PVDF ) in a weight ratio of 0.55:78:21.45, and the solvent N-methylpyrrolidone (NMP) accounts for 85wt% of the total weight of the slurry.

阴极集流体本体为不锈钢片,厚度为12μm,且阴极集流体处理层浆料是通过挤压涂布的方式涂布在不锈钢片的两面,烘干后得到的处理层单面厚度为2um。The body of the cathode current collector is a stainless steel sheet with a thickness of 12 μm, and the cathode current collector treatment layer slurry is coated on both sides of the stainless steel sheet by extrusion coating, and the thickness of one side of the treatment layer obtained after drying is 2um.

其余同实施例1,这里不再赘述。The rest are the same as in Embodiment 1, and will not be repeated here.

实施例6Example 6

与实施例1不同之处在于:阴极集流体处理层浆料中,草酸(C2H2O4)、聚间甲氧基苯胺、导电聚苯胺(PANI)和粘结剂聚偏氟乙烯(PVDF)的重量比为0.6∶10∶70∶19.4,溶剂N-甲基吡咯烷酮(NMP)占浆料总重量的87wt%。The difference from Example 1 is that in the cathode current collector treatment layer slurry, oxalic acid (C 2 H 2 O 4 ), poly-m-methoxyaniline, conductive polyaniline (PANI) and binder polyvinylidene fluoride ( The weight ratio of PVDF) is 0.6:10:70:19.4, and the solvent N-methylpyrrolidone (NMP) accounts for 87wt% of the total weight of the slurry.

将浆料通过凹版印刷机涂覆在厚度为12μm的铝箔上,烘干后得到的处理层单面厚度为2.5um。The slurry was coated on an aluminum foil with a thickness of 12 μm by a gravure printing machine, and the thickness of one side of the treatment layer obtained after drying was 2.5 μm.

其余同实施例1,这里不再赘述。The rest are the same as in Embodiment 1, and will not be repeated here.

对比例1Comparative example 1

与实施例1不同之处在于:阴极集流体采用没有经过本发明处理过的铝箔集流体,也就是仅使用集流体本体作为阴极集流体,其余同实施例1,这里不再赘述。The difference from Example 1 is that the cathode current collector adopts an aluminum foil current collector that has not been processed by the present invention, that is, only the current collector body is used as the cathode current collector, and the rest is the same as that of Embodiment 1, and will not be repeated here.

将上述实施例1至6及对比例1所制得的阴极极片进行粘接性能测试及电阻测试,结果见下表:The cathode pole piece that above-mentioned embodiment 1 to 6 and comparative example 1 are made carry out bonding performance test and resistance test, and the results are shown in the following table:

表1不同集流体阴极极片粘接性能及电阻测试数据Table 1 Adhesive performance and resistance test data of different current collector cathode electrodes

由表1可知,在阴极集流体本体上覆盖处理层后,阴极极片本身具有更强的粘接力和更小的膜片内阻。这是因为与不做表面处理的阴极集流体相比,本发明的集流体的处理层上包含粘接剂,可以与活性物质层起到较好的粘接作用,同时,处理层中包含草酸,草酸能够对集流体本身起到一定的腐蚀作用,可以增强集流体本体的粗糙度,从而增强集流体和处理层的粘接作用。另外,由于聚苯胺及其衍生物本身具有较好的导电性,因此可以减少阴极极片的内阻。It can be seen from Table 1 that after the cathode current collector body is covered with a treatment layer, the cathode sheet itself has stronger adhesion and smaller internal resistance of the diaphragm. This is because compared with the cathode current collector without surface treatment, the treatment layer of the current collector of the present invention contains an adhesive, which can play a better bonding effect with the active material layer. At the same time, the treatment layer contains oxalic acid , oxalic acid can have a certain corrosion effect on the current collector itself, and can enhance the roughness of the current collector body, thereby enhancing the adhesion between the current collector and the treatment layer. In addition, since polyaniline and its derivatives have good electrical conductivity, the internal resistance of the cathode sheet can be reduced.

将上述实施例1至6及对比例1所制得的电池在室温下进行充放电测试,计算电池的首次容量、并记录电池的容量降至首次容量的80%时的充放电循环次数。循环寿命测试对比,结果见表2:The batteries prepared in the above Examples 1 to 6 and Comparative Example 1 were charged and discharged at room temperature, the initial capacity of the battery was calculated, and the number of charge and discharge cycles when the capacity of the battery dropped to 80% of the initial capacity was recorded. Cycle life test comparison, the results are shown in Table 2:

表2电池容量、循环寿命测试数据Table 2 battery capacity, cycle life test data

由表2可知,本发明的锂离子电池的容量和循环寿命并没有受到影响。It can be seen from Table 2 that the capacity and cycle life of the lithium ion battery of the present invention are not affected.

此外,将上述实施例1至6及对比例1所制得的电池在室温下进行充放电测试,并记录其在不同电压下对应的内阻值,所得结果示于图1和图2。In addition, the batteries prepared in Examples 1 to 6 and Comparative Example 1 were subjected to charge and discharge tests at room temperature, and their corresponding internal resistance values at different voltages were recorded. The results are shown in FIGS. 1 and 2 .

从图1和图2可以得知,电池在不同电压下的内阻值是不同的。实施例1至6与对比例1相比,当电压高于3.8V时,电池内阻急剧增大,这是因为集流体上的导电高分子在高电位下被氧化,导致其失去导电子能力而变成了不导电层,从而使得电池内阻急剧增大,使得电池不会出现过充现象,提高了电池的防过充特性。当电压低于2.4V时,此时实施例1至6中的导电高分子在低电位下被还原使其失去电化学活性而变成不导电层,从而使得电池内阻急剧增大,使得电池不会出现过放现象,提高了电池的防过放特性。因此本发明阴极集流体能够同时解决电池的防过充过放的问题。It can be seen from Figure 1 and Figure 2 that the internal resistance of the battery is different at different voltages. Compared with Comparative Example 1 in Examples 1 to 6, when the voltage is higher than 3.8V, the internal resistance of the battery increases sharply, because the conductive polymer on the current collector is oxidized at a high potential, causing it to lose its ability to conduct electrons And it becomes a non-conductive layer, so that the internal resistance of the battery increases sharply, so that the battery will not be overcharged, and the overcharge prevention characteristics of the battery are improved. When the voltage is lower than 2.4V, the conductive macromolecules in Examples 1 to 6 are reduced at a low potential to lose electrochemical activity and become a non-conductive layer, so that the internal resistance of the battery increases sharply, making the battery There will be no over-discharge phenomenon, which improves the anti-over-discharge characteristics of the battery. Therefore, the cathode current collector of the present invention can simultaneously solve the problem of preventing overcharge and overdischarge of the battery.

综上所述,本发明锂离子电池阴极集流体在不影响锂离子电池正常电化学性能的前提下,能够显著的改善锂离子电池体系防过充过放特性,从而有效的改善电池的安全性能。In summary, the lithium ion battery cathode current collector of the present invention can significantly improve the anti-overcharge and overdischarge characteristics of the lithium ion battery system without affecting the normal electrochemical performance of the lithium ion battery, thereby effectively improving the safety performance of the battery .

根据上述说明书的揭示和教导,本发明所属领域的技术人员还可以对上述实施方式进行适当的变更和修改。例如,本发明所属领域的技术人员还可以将实施例中的单个锂离子电池按照现有技术组装成电池组。因此,本发明并不局限于上面揭示和描述的具体实施方式,对本发明的一些修改和变更(如将本发明的单个电池组装成电池组)也应当落入本发明的权利要求的保护范围内。此外,尽管本说明书中使用了一些特定的术语,但这些术语只是为了方便说明,并不对本发明构成任何限制。According to the disclosure and teaching of the above specification, those skilled in the art to which the present invention pertains can also make appropriate changes and modifications to the above embodiment. For example, those skilled in the art to which the present invention belongs can also assemble the single lithium ion battery in the embodiment into a battery pack according to the prior art. Therefore, the present invention is not limited to the specific embodiments disclosed and described above, and some modifications and changes to the present invention (such as assembling a single battery of the present invention into a battery pack) should also fall within the protection scope of the claims of the present invention . In addition, although some specific terms are used in this specification, these terms are only for convenience of description and do not constitute any limitation to the present invention.

Claims (9)

1. a lithium ion battery cathode collector, including cathode current collector body, it is characterised in that: described cathode current collector is originally Surface is also covered with processing layer, and by weight percentage, described process layer is conducted electricity high by the conjugation big π key of 70~80wt% The binding agent of molecule, 19.4~29.8wt% and the oxalic acid composition of 0.2~0.6wt%;Described conjugation big π key conduction height Molecule is poly-2, at least one in 5-dimethoxyaniline, poly-m-anisidine.
2. according to the lithium ion battery cathode collector described in claim 1, it is characterised in that: described binding agent is for poly-inclined At least one in PVF and polytetrafluoroethylene (PTFE).
3. according to the lithium ion battery cathode collector described in claim 1, it is characterised in that: described process layer is by squeezing Extrusion mode for cloth covers at described cathode current collector body surface.
4. according to the lithium ion battery cathode collector described in claim 1, it is characterised in that: described process layer is by quiet Electricity mode of printing covers at described cathode current collector body surface.
5. according to the lithium ion battery cathode collector described in claim 1, it is characterised in that: described process layer thickness is little In 5 m.
6. according to the lithium ion battery cathode collector described in claim 5, it is characterised in that: described process layer thickness is 3 µm。
7. according to the lithium ion battery cathode collector described in claim 1, it is characterised in that: described cathode current collector is originally Body is aluminium foil or stainless steel substrates.
8. a lithium ion battery, including cathode current collector and the cathode active material layer being coated on described cathode current collector, Anode collector and the anode active material layer being coated in described anode collector, barrier film, and electrolyte, its feature exists In: described cathode current collector is the lithium ion battery cathode collector described in any one of claim 1 to 7.
Lithium ion battery the most described, it is characterised in that: described cathode active material layer includes ferric phosphate Lithium (LiFePO4)。
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