WO2010081422A1 - Pre-charging method for lithium-ion battery - Google Patents

Pre-charging method for lithium-ion battery Download PDF

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WO2010081422A1
WO2010081422A1 PCT/CN2010/070202 CN2010070202W WO2010081422A1 WO 2010081422 A1 WO2010081422 A1 WO 2010081422A1 CN 2010070202 W CN2010070202 W CN 2010070202W WO 2010081422 A1 WO2010081422 A1 WO 2010081422A1
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charging
ion battery
lithium ion
lithium
precharging
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PCT/CN2010/070202
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French (fr)
Chinese (zh)
Inventor
滕鑫
何伟
何名
饶汝宇
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深圳市比克电池有限公司
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Priority claimed from CN200910105012A external-priority patent/CN101783426A/en
Priority claimed from CN200910105010A external-priority patent/CN101783424A/en
Priority claimed from CN200910105011A external-priority patent/CN101783425A/en
Application filed by 深圳市比克电池有限公司 filed Critical 深圳市比克电池有限公司
Publication of WO2010081422A1 publication Critical patent/WO2010081422A1/en

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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/42Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
    • H01M10/44Methods for charging or discharging
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • 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
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/50Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
    • H01M4/505Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy
    • 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
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/52Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron
    • H01M4/525Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
    • 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

A pre-charging method for lithium-ion battery which includes at least two charging steps, charging current of the first charging step is higher than that of the second step, and the total pre-charging electric quantity of the two charging steps is 10%-45% of total charge capacity.

Description

锂离子电池预充方法 技术领域  Lithium ion battery pre-filling method
本发明涉及锂离子电池技术领域, 特别是涉及一种锂离子电池的预充 方法。  The present invention relates to the field of lithium ion battery technology, and in particular to a method for precharging a lithium ion battery.
背景技术 Background technique
目前锂离子电池的应用日趋广说泛, 电池需求量不断增加, 对电池制作 商而言, 一方面要提高生产效率来满足市场需要, 另一方面要求改进和完 善工艺, 在提高产品质量的同时提高生产书效率。 随着锂电行业的生产机械 化, 预充工序已经成为目前制约生产速率及产品质量的关键环节。  At present, the application of lithium-ion batteries is becoming more and more widespread, and the demand for batteries is increasing. For battery manufacturers, on the one hand, it is necessary to improve production efficiency to meet market needs, on the other hand, it is required to improve and improve processes, while improving product quality. Improve the efficiency of production books. With the mechanization of production in the lithium battery industry, the pre-filling process has become a key link that restricts production rates and product quality.
对锂离子电池来说, 预充即初次充电时, 由于电化学反应, 不可避免 地在碳负极与电解液的相界面上形成覆盖在碳电极表面的钝化薄层, 此薄 层即为固体电解质界面 ( sol id e lectrolyte interface )或称 SEI月莫。 对 锂离子电池进行首次充电的过程也称为化成。 在电池化成过程中, 在负极 表面生成 SEI膜的同时, 会发生副反应产生气体产物。 产生的气体需及时 排出电芯, 否则这些气体在电池内部积聚会造成电池膨胀, 外壳发鼓、 变 形, 甚至会导致电池发生爆炸。 而如果化成过程中气体产生不完全, 在电 芯后期的电循环过程中会持续放出, 严重影响电芯的电性能及安全性能。 因此锂离子二次充电电池的化成步骤是制造电池的重要阶段, 关系到电池 的容量高低、 循环寿命长短、 安全性能等多方面的品质。  For a lithium-ion battery, when the pre-charge is the first charge, due to the electrochemical reaction, a passivation thin layer covering the surface of the carbon electrode is inevitably formed at the interface between the carbon negative electrode and the electrolyte, and the thin layer is solid. The electrolyte interface (sol id e lectrolyte interface) or SEI month Mo. The process of charging a lithium-ion battery for the first time is also called chemical conversion. In the battery formation process, a SEI film is formed on the surface of the negative electrode, and a side reaction generates a gas product. The generated gas needs to be discharged out of the battery in time. Otherwise, the gas will accumulate inside the battery and cause the battery to expand. The outer casing will be drummed, deformed, and even cause the battery to explode. However, if the gas is incomplete during the formation process, it will continue to be released during the electrical cycle of the battery, which will seriously affect the electrical performance and safety performance of the battery. Therefore, the formation step of the lithium ion secondary rechargeable battery is an important stage in the manufacture of the battery, and is related to the quality of the battery, the cycle life, and the safety performance.
而现阶段的化成过程,通常是釆用小电流进行长达几十个小时的充电, 以期望获得理想的 SEI膜, 保持电池性能稳定。 但是, 长时间的化成步骤 导致生产效率低下。  At this stage, the formation process is usually carried out with a small current for several tens of hours of charging, in order to obtain an ideal SEI film to maintain stable battery performance. However, long-term chemical conversion steps result in inefficient production.
发明内容 Summary of the invention
本发明的目的是针对现有技术的不足, 提供一种能提高电芯性能并极 大缩短充电时间提高生产效率的锂离子电池预充方法。  SUMMARY OF THE INVENTION An object of the present invention is to provide a lithium ion battery prefilling method which can improve the performance of a battery core and greatly shorten the charging time and improve the production efficiency in view of the deficiencies of the prior art.
本发明公开了一种锂离子电池预充方法, 所述锂离子电池的预充方法 是釆用阶段式充电, 所述阶段式充电包括至少两个充电步骤, 第二充电步 骤的充电电流大于第一充电步骤的充电电流, 并且第一充电步骤与第二充 电步骤的总的预充电量为所述锂离子电池总电量的 10% ~ 45%。 在本发明一组具体的实施方式中, 所述锂离子电池的正极活性物质为 钴酸锂, 并且第一充电步骤与第二充电步骤的总的预充电量为所述锂离子 电池总电量的 10%~35%, 优选为 10%~30%。 所述第一充电步骤的充电 电流优选小于 0.1C ,充电时间为 5 ~ 30min。所述第一充电步骤的充电电流 进一步优选为 0.05C~0.1C, 充电时间为 5~ 15min。 所述第二充电步骤的 充电电流优选为 0.3C -0.6C, 充电时间为 10 ~ 60min。 更优选的, 所述第 一充电步骤的充电电流为 0.05C,充电时间为 lOmin,第二充电步骤的充电 电流为 0.5C, 充电时间为 12min。 优选的, 所述阶段式充电前的电解液注 液量为 80% ~ 85%, 阶段式充电后再补注液 10% ~ 15%。 The invention discloses a method for pre-charging a lithium ion battery, wherein the pre-charging method of the lithium ion battery is a stage charging, the stage charging comprises at least two charging steps, and the charging current of the second charging step is greater than the first a charging current of a charging step, and the first charging step and the second charging The total pre-charge amount of the electrical step is 10% to 45% of the total amount of the lithium ion battery. In a specific embodiment of the present invention, the positive active material of the lithium ion battery is lithium cobaltate, and the total precharge amount of the first charging step and the second charging step is the total amount of the lithium ion battery. 10% to 35%, preferably 10% to 30%. The charging current of the first charging step is preferably less than 0.1 C, and the charging time is 5 to 30 min. The charging current of the first charging step is further preferably 0.05 C to 0.1 C, and the charging time is 5 to 15 min. The charging current of the second charging step is preferably 0.3C - 0.6C, and the charging time is 10 ~ 60min. More preferably, the charging current of the first charging step is 0.05 C, the charging time is 10 min, the charging current of the second charging step is 0.5 C, and the charging time is 12 min. Preferably, the electrolyte injection amount before the staged charging is 80% to 85%, and the refilling liquid is 10% to 15% after the stage charging.
在本发明另一组具体的实施方式中, 所述锂离子电池的正极活性物质 为钴酸锂与镍钴锰酸锂的混合材料, 并且第一充电步骤与第二充电步骤的 总的预充电量为所述锂离子电池总电量的 15% ~ 35%,优选为 15%~30%。 优选的, 所述锂离子电池的正极活性物质中, 钴酸锂占 60% ~ 80%, 镍钴 锰酸锂占 20% ~ 40%, 更优选钴酸锂占 80%, 镍钴锰酸锂占 20%, 所述为 重量百分比。 优选的, 所述第一充电步骤的充电电流为小于 0.1C, 充电时 间为 5~30min。进一步优选的, 第一充电步骤的充电电流为 0.05C~0.1C, 充电时间为 5 ~ 15min。 或者优选的, 所述第二充电步骤的充电电流为 0.3C-0.6C, 充电时间为 10~60min。 进一步优选的, 所述第一充电步骤 的充电电流为 0.05C ,充电时间为 1 Omin,第二充电步骤的充电电流为 0.4C , 充电时间为 22min。 优选的, 所述阶段式充电前的电解液注液量为 80% ~ 85%, 阶段式充电后再注入电解液 15% ~ 10%。  In another specific embodiment of the present invention, the positive active material of the lithium ion battery is a mixed material of lithium cobaltate and lithium nickel cobalt manganese oxide, and the total pre-charging of the first charging step and the second charging step The amount is 15% to 35%, preferably 15% to 30%, of the total amount of the lithium ion battery. Preferably, among the positive electrode active materials of the lithium ion battery, lithium cobaltate accounts for 60% to 80%, lithium nickel cobalt manganese oxide accounts for 20% to 40%, and more preferably, lithium cobalt oxide accounts for 80%, lithium nickel cobalt manganese oxide. 20%, said weight percentage. Preferably, the charging current in the first charging step is less than 0.1 C, and the charging time is 5 to 30 min. Further preferably, the charging current in the first charging step is 0.05 C to 0.1 C, and the charging time is 5 to 15 min. Or preferably, the charging current of the second charging step is 0.3C-0.6C, and the charging time is 10~60min. Further preferably, the charging current of the first charging step is 0.05 C, the charging time is 1 Omin, the charging current of the second charging step is 0.4 C, and the charging time is 22 min. Preferably, the electrolyte injection amount before the staged charging is 80% to 85%, and the electrolyte is injected 15% to 10% after the stage charging.
在本发明再一组具体的实施方式中, 所述锂离子电池的正极活性物质 为钴酸锂与镍钴酸锂的混合材料, 并且第一充电步骤与第二充电步骤的总 的预充电量为所述锂离子电池总电量的 25%~45%, 优选为 25%~40%。 优选的, 所述锂离子电池的正极活性物质中, 镍钴酸锂的分子式为 LiNixCo1-x02, x=0.75 ~0.85。 所述锂离子电池的正极活性物质中, 优选钴 酸锂占 75% ~ 85%, 镍钴酸锂占 15% ~ 25%, 更优选钴酸锂占 80%, 镍钴 酸锂占 20%, 所述为重量百分比。 优选的, 所述第一充电步骤的充电电流 为小于 0.1C, 充电时间为 5~30min。 进一步优选的, 第一充电步骤的充电 电流为 0.05C~0.1C, 充电时间为 5~ 15min。 或者优选的, 所述第二充电 步骤的充电电流为 0.3C ~ 0.6C , 充电时间为 25 ~ 80min。 最优选第一充电 步骤的充电电流为 0.05C,充电时间为 lOmin,第二充电步骤的充电电流为 0.4C,充电时间为 38min。优选的,阶段式充电前的电解液注液量为 80% ~ 85%, 阶段式充电后再注入电解液 15% ~ 10%。 In still another specific embodiment of the present invention, the positive active material of the lithium ion battery is a mixed material of lithium cobaltate and lithium nickel cobaltate, and the total precharge amount of the first charging step and the second charging step It is 25%~45% of the total amount of the lithium ion battery, preferably 25%~40%. Preferably, in the positive electrode active material of the lithium ion battery, the lithium nickel cobaltate has a molecular formula of LiNi x Co 1-x 0 2 and x=0.75 to 0.85. Among the positive electrode active materials of the lithium ion battery, lithium cobaltate accounts for 75% to 85%, lithium nickel cobaltate accounts for 15% to 25%, more preferably, lithium cobaltate accounts for 80%, and lithium nickel cobaltate accounts for 20%. The percentage is by weight. Preferably, the charging current of the first charging step is less than 0.1 C, and the charging time is 5 to 30 min. Further preferably, the charging current of the first charging step is 0.05 C~0.1 C, and the charging time is 5-15 min. Or preferably, the second charging The charging current of the step is 0.3C ~ 0.6C, and the charging time is 25 ~ 80min. Most preferably, the charging current of the first charging step is 0.05 C, the charging time is 10 min, the charging current of the second charging step is 0.4 C, and the charging time is 38 min. Preferably, the electrolyte injection amount before the staged charging is 80% to 85%, and the electrolyte is injected 15% to 10% after the stage charging.
釆用本发明的预充方法对锂离子电池进行预充电, 能够使电芯达到与 釆用传统小电流长时间预充工艺的电芯相当甚至更优的电学性能, 同时极 大地缩短了预充时间, 同时也能缩短电芯的陈化时间, 大大地提高了生产 效率。 节约了生产成本。  The pre-charging of the lithium ion battery by the pre-charging method of the present invention enables the battery core to achieve comparable or even better electrical performance than the battery core of the conventional small current long-time pre-charging process, and greatly shortens the pre-charging. Time, at the same time, can shorten the aging time of the battery core and greatly improve production efficiency. Save on production costs.
附图说明 DRAWINGS
图 1是正极活性物质为钴酸锂的锂离子电池釆用电流为 0.1 C的充电曲 线图。  Fig. 1 is a charging graph showing a current of 0.1 C for a lithium ion battery in which a positive electrode active material is lithium cobaltate.
图 2是正极活性物质为钴酸锂与镍钴锰酸锂按 8:2的重量比例混合的锂 离子电池, 其釆用电流为 0.1C的充电曲线图, 横坐标为时间 (min ) , 纵坐 标为电压值。  2 is a lithium ion battery in which a positive electrode active material is a mixture of lithium cobaltate and lithium nickel cobalt manganate in a weight ratio of 8:2, and a charging current of 0.1 C is used, and the abscissa is time (min), vertical. The coordinates are voltage values.
图 3是正极活性物质为钴酸锂 ( LiCo02 ) 与镍钴酸锂 ( LiNixCo1-x02, x=0.75 ~ 0.85 )按 8:2的重量比例混合的锂离子电池, 其釆用电流为 0.1C的充 电曲线图, 横坐标为时间 (min ) , 纵坐标为电压值(V ) 。 3 is a lithium ion battery in which a positive electrode active material is lithium cobaltate (LiCo0 2 ) and lithium nickel cobaltate (LiNi x Co 1-x 0 2 , x=0.75 to 0.85) in a weight ratio of 8:2, and the like. Using a charging curve with a current of 0.1 C, the abscissa is time (min) and the ordinate is voltage value (V).
具体实施方式 detailed description
目前锂离子电池的应用日趋广泛, 电池需求量不断增加, 对电池制作 商而言, 一方面要提高生产效率来满足市场需要, 另一方面要求改进和完 善工艺, 在提高产品质量的同时提高生产效率。 随着锂电行业的生产机械 化, 预充工序已经成为目前制约生产速率及产品质量的关键环节, 本发明 提供了一种锂离子电池的预充方法, 能在电芯性能得到提升的前提下极大 的提高生产效率。  At present, the application of lithium-ion batteries is becoming more and more extensive, and the demand for batteries is increasing. For battery manufacturers, on the one hand, it is necessary to improve production efficiency to meet market needs, on the other hand, it is required to improve and improve processes, and improve production while improving product quality. effectiveness. With the mechanization of production in the lithium battery industry, the pre-filling process has become a key link that restricts the production rate and product quality. The present invention provides a pre-charging method for a lithium ion battery, which can greatly improve the performance of the battery core. Improve production efficiency.
本发明通过引入大电流的预充工步,加速了 SEI膜形成过程中副反应 的进行, 从而能在较短的时间达到预充目的。 本发明首先通过实验确定预 充电量与预充电压的关系, 然后通过成膜时的电压确定预充的合适电量, 最后再通过一系列实施例, 通过大电流预充工步的引入, 在较短的时间完 成成膜的副反应, 并得到综合性能提高的产品。 减少电芯的陈化时间。 陈化的目的是为了使电解液充分浸润到极片里面, 从而保证避免预充时的极化现象和电解液的损失、 保证封口电芯剩余电解 液的电解液量等, 因为传统工艺釆用一次性 100 %注液, 而且预充时间长, 因此陈化时间相对长, 通常需要十几个小时; 调整为本发明的新的预充工 艺后, 注液是分两次, 先注液 80% ~ 85%, 预充后再补注液 10% ~ 15%, 虽然第二步电流比较大,但时间短, 因此在这个基础上将陈化时间也缩短, 可缩短至 1 ~ 2h。 The invention accelerates the progress of the side reaction in the formation process of the SEI film by introducing a pre-charging step of a large current, so that the pre-charging can be achieved in a shorter time. The invention firstly determines the relationship between the pre-charging amount and the pre-charging pressure through experiments, and then determines the appropriate amount of pre-charging by the voltage at the time of film formation, and finally through a series of embodiments, through the introduction of the large current pre-charging step, The side reaction of the film formation is completed in a short time, and a product with improved overall performance is obtained. Reduce the aging time of the battery. The purpose of aging is to fully infiltrate the electrolyte into the pole piece, thus ensuring avoidance of polarization and electrolyte loss during pre-charging, and ensuring residual electrolysis of the sealed cell. The amount of electrolyte in the liquid, etc., because the conventional process uses a one-time 100% injection, and the pre-filling time is long, so the aging time is relatively long, usually takes more than ten hours; after adjustment to the new pre-filling process of the present invention The injection is divided into two parts. The first injection is 80% ~ 85%. After pre-filling, the refilling liquid is 10% ~ 15%. Although the second step current is relatively large, but the time is short, it will be aged on this basis. The time is also shortened and can be shortened to 1 ~ 2h.
一、 正极活性物质为钴酸锂  1. The positive active material is lithium cobaltate
首先, 考察正极活性物质为钴酸锂预充电流为 0.1C的充电曲线图, 如图 1所示。  First, a charging profile in which the positive active material is a lithium cobaltate precharge flow of 0.1 C is examined, as shown in FIG.
根据 0.1C 充电时间 -电压值曲线图, 分别考察充电量在 10 % ( 60min )、 20 % ( 120min )和 30 % ( 180min ) (电压值对应为 3.74V、 3.82V 和 3.84V )之间的成品电芯性能。 由于 SEI膜的成膜电压为 3.60V, 在预充 (化成)过程中, 虽然负极表面形成 SEI膜的主要反应会因化成电压不同 而不同, 但在充电电压达到成膜电压 3.60V时, SEI膜开始形成, 并在其 后的充电过程中随着反应的进行逐渐地改变其结构和性能。 也就是说, 由 图 1可知, 当充电电量为 10%时, 由于电压以达 3.74V超过 3.60V, SEI 膜就已经足够形成。 由此本发明釆用不同的预充电流及时间组合, 获得预 充电量在大约 10 % - 30 %之间的不同下拒电压值, 考察电芯的容量(容量 发挥)、 内阻、 尺寸及其循环性能, 均符合要求。  According to the 0.1C charging time-voltage value graph, the charge is between 10% (60min), 20% (120min) and 30% (180min) (corresponding to 3.74V, 3.82V and 3.84V). Finished battery performance. Since the film formation voltage of the SEI film is 3.60 V, the main reaction of forming the SEI film on the surface of the negative electrode may differ depending on the formation voltage during the precharge process, but when the charge voltage reaches the film formation voltage of 3.60 V, the SEI The film begins to form and gradually changes its structure and properties as the reaction progresses during subsequent charging. That is to say, as can be seen from Fig. 1, when the charge amount is 10%, since the voltage exceeds 3.60 V by 3.74 V, the SEI film is sufficiently formed. Therefore, the present invention uses different precharge currents and time combinations to obtain different reverse voltage values of precharge amounts between about 10% and 30%, and inspects the capacity (capacity), internal resistance, size, and Its cycle performance meets the requirements.
本发明釆用阶段式充电方式, 包括第一充电步骤与第二充电步骤。 第 一步釆用小电流对 SEI膜的形成有积极作用, 有利于提高电芯容量, 但长 时间的小电流充电会导致形成的 SEI膜阻抗增大, 从而影响成品电芯的倍 率放电性能, 时间过程长也影响生产效率, 因此第一步小电流(0.1C以内) 短时间(30min以内), 其对阶段式的预充方式而言, 对电芯成品性能的影 响几乎是可以忽略不计的。通过图 1的充电曲线可知, 0.1C充电 5分钟时, 电压为 3.22V, 而在此之前电压值的变化(上升)很快而且是不稳定的, 由此, 对于第一步小电流充电时间的下限值, 若以 0.1C 充电则优选为 5 分钟, 若以 0.05C充电则优选为 10分钟。 第二步引入大电流, 大电流的充 电方式能够加速副反应的进行, 提高化成效率, 但容易破坏 SEI膜的形成 并导致电芯性能的恶化, 同时预充拒使用大电流稳定性和误差均较大, 因 此应选择合适的充电电流及充电时间。 本发明的预充方法中大电流选择在 0.3C - 0.6C之间, 充电时间根据电流的大小进行调整, 通常在 10 ~ 60min 以内。 对于本发明的阶段式预充工艺而言, 由于第一步电流小而且充电时 间较短, 因此, 第一步所达到的电量可以忽略不计, 而第二步大电流预充 后所要达到的电量应为总电量的 10% ~ 30%左右。 The invention adopts a stage charging method, which comprises a first charging step and a second charging step. In the first step, a small current has a positive effect on the formation of the SEI film, which is beneficial to increase the cell capacity, but a long time of small current charging may cause an increase in the impedance of the formed SEI film, thereby affecting the rate discharge performance of the finished cell. The long time process also affects the production efficiency. Therefore, the first step of small current (within 0.1C) is short (within 30min). For the stage precharge method, the impact on the performance of the battery core is almost negligible. . According to the charging curve of Fig. 1, when the voltage is charged for 5 minutes at 0.1 C, the voltage is 3.22 V, and before this time, the change (rise) of the voltage value is fast and unstable, thereby, for the first step, the small current charging time The lower limit value is preferably 5 minutes when charged at 0.1 C, and preferably 10 minutes when charged at 0.05 C. The second step introduces a large current, and the charging method of the large current can accelerate the progress of the side reaction and improve the formation efficiency, but it is easy to damage the formation of the SEI film and cause deterioration of the performance of the battery core, and at the same time, the high current stability and error are pre-filled. Larger, so you should choose the right charging current and charging time. In the pre-charging method of the present invention, the large current is selected between 0.3C and 0.6C, and the charging time is adjusted according to the magnitude of the current, usually within 10 to 60 minutes. For the stage pre-filling process of the present invention, since the first step current is small and charging The short distance, therefore, the amount of electricity achieved in the first step can be neglected, and the amount of electricity to be reached after the second step of high current precharge should be about 10% ~ 30% of the total electricity.
下面通过具体实施例进一步详细描述。 上述部分及下面实施例 1-18 中所用到的电芯均是同一批次生产的 053450Al-900mAh 电芯, 正极活性 物质为钴酸锂, 实施例 1-18电芯具有一致的正负极敷料量, 电极密度, 釆 用相同的电解液注液, 注液量, 保持同样的注液预充及封口, 清洗等实验 条件。  The details are described in further detail below by way of specific examples. The above-mentioned parts and the batteries used in the following Examples 1-18 are all 053450Al-900mAh batteries produced in the same batch, the positive active material is lithium cobaltate, and the electrolytes of Examples 1-18 have consistent positive and negative dressings. The amount of the electrode, the density of the electrode, the same electrolyte injection, the amount of liquid injection, and the same conditions for pre-filling and sealing, cleaning, etc.
实施例 1  Example 1
具体过程步骤如下: 将样品电芯进行首次注液, 注液量为工艺要求 85 % , 再将电芯陈化 1 ~ 2h后上预充拒按 0.05C、 lOmin; 0.3C、 20min的预充 方法进行预充, 然后下拒测量电压, 再次补注液 15 %后对电芯进行挤压并 完成封口, 以上工序步骤均在相同的温湿度环境下进行, 温度≤26°C ; 湿度 ≤2 % 。 在室温环境下, 对已封口的电芯清洗后测量尺寸, 老化 6天后对电芯 进行检测分容, 分容制度按表 2中所示参数进行。 考察其容量、 内阻、 3.92V 尺寸和循环性能测试, 结果见表 3所示。  The specific process steps are as follows: The first sample is injected into the sample cell, the amount of liquid injection is 85% of the process requirement, and the cell is aged for 1 ~ 2 hours, then pre-filled and refused to be 0.05C, lOmin; 0.3C, 20min precharge The method pre-charges, then refuses to measure the voltage, and re-fills the liquid 15%, then squeezes the battery and completes the sealing. The above steps are all carried out under the same temperature and humidity environment, the temperature is ≤26°C; the humidity is ≤2 %. In the room temperature environment, the sealed cell is cleaned and measured, and after 6 days of aging, the cell is tested and divided. The capacity system is based on the parameters shown in Table 2. The capacity, internal resistance, 3.92V size and cycle performance test were examined. The results are shown in Table 3.
其中, 测试电压目的是为了考察预充过程有无异常, 比如电流大小和 充电时间的设置、充电过程拒点电流的稳定性等,对比 0.1C充电曲线图判 定, 在相同充电电量下电压值大小应该是相同的, 误差在 ±0.01V, 排除对 后面成品电芯性能考察的干扰因素。  Among them, the purpose of the test voltage is to investigate whether there is abnormality in the precharge process, such as the setting of current magnitude and charging time, the stability of the reject current in the charging process, etc., compared with the 0.1C charging curve, the voltage value under the same charging power. It should be the same, with an error of ±0.01V, excluding the interference factors for the performance of the finished battery.
预充过程是一个 SEI膜及其副反应发生的过程, 如果预充电量不够或 预充没达到预期效果, 比如说如果有气体未完全排出的话, 清洗后的电芯 就会有鼓壳的现象,因此测量清洗后尺寸可以在一定程度上反映预充效果。 在相同预充条件下, 清洗尺寸小的相对来说其预充效果比较好。  The pre-charging process is a process in which the SEI film and its side reactions occur. If the pre-charging amount is insufficient or the pre-charging does not achieve the desired effect, for example, if the gas is not completely discharged, the cleaned cell will have a drum shell phenomenon. Therefore, measuring the size after cleaning can reflect the pre-filling effect to some extent. Under the same pre-filling conditions, the pre-filling effect is relatively good when the cleaning size is small.
考察电芯内阻是因为内阻小说明界面性能好, SEI膜形成的性能好。 电芯内阻的影响因素比较多, 比如说正负极耳焊接有无虚焊、不同的材料、 材料配比、 预充方法等。 由于我们所选用的电芯是同一批次生产的电芯进 行不同预充方法实验, 因此能够尽量排除预充方法外其余工序所带来的干 扰。 就是说选用相同的材料、 相同的电极密度、 厚度, 确定极耳焊接正常 的卷芯来进行预充方法实验。如果预充方法不合理,造成极片有局部过充、 析锂等状况, 此时内阻就相应的要比较高, 因此本发明的实施例中电阻可 作为侧面反应充电效果的一个指标。  The internal resistance of the cell is investigated because the small internal resistance indicates good interface performance and the SEI film has good performance. There are many factors affecting the internal resistance of the battery, such as the welding of the positive and negative ear solder joints, different materials, material ratio, pre-filling method. Since the batteries we selected are those of the same batch of batteries that are subjected to different pre-filling methods, the interference from the rest of the pre-filling process can be eliminated as much as possible. That is to say, using the same material, the same electrode density, and thickness, the normal core of the tab is welded to perform the pre-filling method experiment. If the pre-filling method is unreasonable, the pole piece has a local overcharge, lithium deposition, etc., and the internal resistance is relatively high at this time. Therefore, the resistor in the embodiment of the present invention can be used as an indicator of the side reaction charging effect.
而将电芯充电至 3.92V, 然后考察其尺寸变化状况是电池行业对电芯 成品性能考察的一个惯常指标。 And charging the battery to 3.92V, and then examining its dimensional change is the battery industry battery A customary indicator of the performance of finished products.
同样, 其他实施例及对比例 1釆用相同的步骤, 只是预充方法釆用的 时间和电流不一样。 本发明中, 注液是分两次, 先注液 80% - 85%, 预充 后再补注液 10% ~ 15%。 对比例 2为传统工艺, 除注液釆用一次性 100 % 注液、 预充方法为表 1中所示以及陈化时间 12 ~ 16h不一样外, 其他步骤 与以上实施例相同。  Similarly, the other examples and the comparative example 1 use the same steps except that the time and current used in the pre-filling method are different. In the present invention, the injection is divided into two parts, the first injection is 80% - 85%, and after the pre-filling, the refilling liquid is 10% ~ 15%. Comparative Example 2 is a conventional process, except that the one-time 100% injection, the prefilling method is shown in Table 1 and the aging time is 12 to 16 hours, and the other steps are the same as the above embodiment.
所有实施例及对比例的预充方法见表 1所示,其技术效果数据见表 3。  The prefilling methods of all the examples and comparative examples are shown in Table 1, and the technical effect data are shown in Table 3.
表 1. 各实施例及对比例的预充方法  Table 1. Prefilling methods of various examples and comparative examples
Figure imgf000008_0001
Figure imgf000008_0001
表 2. 分容制度  Table 2. Capacity-sharing system
Figure imgf000008_0002
Figure imgf000008_0002
锂电芯在这里化成得到容量, 并知道容量的大小, 就是分容。 通过 容, 确定了电芯的等级。 表 3. 各实施例及对比例技术效果 The lithium battery is here to get the capacity, and know the size of the capacity, that is, the volume. Through the capacity, the level of the battery cell is determined. Table 3. Technical effects of various examples and comparative examples
Figure imgf000009_0001
各实施例与对比例 2的数据表明, 通过选用本发明的预充方法, 能够 够极大地缩减预充时间, 提高生产效率。 而各实施例与对比例 1的数据表 明了第一小电流充电的必要性, 若不进行第一步小电流预充的话其成品电 芯尺寸、 容量发挥以及循环性能等效果都要更差。
Figure imgf000009_0001
The data of the respective examples and Comparative Example 2 show that by selecting the pre-filling method of the present invention, the pre-filling time can be greatly reduced, and the production efficiency can be improved. The data of the respective examples and Comparative Example 1 indicate the necessity of the first small current charging. If the first step of the small current precharging is not performed, the effects of the size, capacity, and cycle performance of the finished battery are worse.
本发明通过引入大电流预充, 能够缩短电芯的预充时间, 进一步优化 正极活性物质为钴酸锂的锂离子预充方法为 0.05C、 lOmin; 0.5C、 12min。 该优化的预充方法是由以上各实施例横向、 纵向的对比, 最能体现预充方 法优劣的数据是正极克容量和循环性能以及预充时间, 再考察其内阻和尺 寸等综合性能, 从而对比得出最优化的预充方法。  The invention can shorten the pre-charging time of the battery core by introducing a large current pre-charging, and further optimize the lithium ion pre-charging method of the positive electrode active material to be lithium cobaltate to be 0.05 C, lOmin; 0.5 C, 12 min. The optimized pre-filling method is a horizontal and vertical comparison of the above embodiments, and the data which best reflects the advantages and disadvantages of the pre-filling method are the positive gram capacity and the cycle performance and the pre-charge time, and then the comprehensive performances such as internal resistance and size are examined. , thus comparing the optimized pre-filling method.
本发明以上具体实施方式中所选用的是 900mAh的电芯, 对于其它容 量大小的电芯, 只需满足正极活性物质为钴酸锂, 本发明的预充方法对其 同样适合。 但是, 考虑到如果锂离子电池电芯的标称容量过大, 大于In the above specific embodiment of the present invention, a battery of 900 mAh is selected. For other capacity batteries, it is only necessary to satisfy the positive electrode active material as lithium cobaltate, and the precharge method of the present invention The same is true. However, considering that if the nominal capacity of the lithium-ion battery cell is too large, it is greater than
1500mAh时, 由于相应的预充方法第二步的充电电流比较大, 对此预充拒 的电流误差比较大,或是稳定性比较差, 由此对电芯性能会造成一定影响。 因此, 本发明的预充方法所适合的电芯容量范围最好是小于 1500mAh, 优 选小于 1200mAh。但若能克服预充拒大电流充电所造成的误差或保证其稳 定性, 则本发明的预充方法所适用的电芯容量无限制。 二、 正极活性物质为钴酸锂和镍钴锰酸锂 At 1500 mAh, the charging current of the second step of the corresponding pre-charging method is relatively large, and the current error of the pre-charging is relatively large, or the stability is relatively poor, thereby having a certain influence on the performance of the battery. Therefore, the cell capacity range suitable for the prefilling method of the present invention is preferably less than 1500 mAh, preferably less than 1200 mAh. However, if the error caused by the pre-filling of the large current charging is overcome or the stability is ensured, the capacity of the battery to which the precharging method of the present invention is applied is not limited. 2. The positive active materials are lithium cobalt oxide and lithium nickel cobalt manganese oxide.
考察正极活性物质为钴酸锂和镍钴锰酸锂按比例 8:2 混合,预充电流 为 0.1C的充电曲线图, 如图 2所示。  The charge activity chart of the positive electrode active material was lithium cobaltate and lithium nickel cobalt manganate mixed in a ratio of 8:2, and the precharge current was 0.1 C, as shown in Fig. 2.
根据 0.1C 充电时间 -电压值曲线图, 分别考察充电量在 10 % According to the 0.1C charging time-voltage value graph, the charge is 10% respectively.
( 60min )、 20 % ( 120min )和 30 % ( 180min ) (电压值对应为 3.61V、 3.72V 和 3.81 V )之间的成品电芯性能。 由于 SEI膜的成膜电压为 3.60V, 在预充Finished cell performance between (60min), 20% (120min) and 30% (180min) (voltage values corresponding to 3.61V, 3.72V and 3.81V). Since the film formation voltage of the SEI film is 3.60V, it is precharged.
(化成)过程中, 虽然负极表面形成 SEI膜的主要反应会因化成电压不同 而不同, 但在充电电压达到成膜电压 3.60V时, SEI膜开始形成, 并在其 后的充电过程中随着反应的进行逐渐地改变其结构和性能。 也就是说, 由 图(2 )可知, 当充电电量为 10%时, 由于电压以达 3.61V超过 3.60V, SEI 膜就已经开始形成。 为进一步验证成膜及其副反应是否充分完成, 本专利 先将电芯用 0.1C分别充电 60min、 90min、 120min和 180min, 使电芯预充 电量在 10 %、 15 %、 20 %和 30 % , 分别考察其容量、 尺寸、 内阻等性能, 通过考察结果, 预充电量在 10 %时, 因成膜副反应排气不充分, 电芯有尺 寸超厚和析锂等不良现象。 因此本专利釆用不同的预充电流及时间组合, 使得预充电量在 15 % - 35 % ,优选 15 % - 30 %之间的不同下拒电压值,考 察电芯的容量(容量发挥)、 内阻、 尺寸及其循环性能。 During the formation process, although the main reaction of forming the SEI film on the surface of the negative electrode may be different depending on the formation voltage, when the charging voltage reaches the film formation voltage of 3.60 V, the SEI film starts to form and is subsequently charged during the subsequent charging process. The progress of the reaction gradually changes its structure and properties. That is to say, as shown in Fig. (2), when the charge amount is 10%, since the voltage exceeds 3.60 V by 3.61 V, the SEI film has begun to form. In order to further verify whether the film formation and its side reactions are fully completed, this patent first charges the cells with 0.1C for 60min, 90min, 120min and 180min respectively, so that the pre-charge amount of the cells is 10%, 15%, 20% and 30%. The properties of the capacity, size, and internal resistance were examined separately. According to the results, when the pre-charge amount was 10%, the exhaust gas due to the film formation side reaction was insufficient, and the battery core had excessive thickness and lithium deposition. Therefore, this patent uses different pre-charge currents and time combinations, so that the pre-charge amount is between 15% - 35%, preferably 15% - 30%, and the voltage capacity (capacity play) is investigated. Internal resistance, size and cycle performance.
本发明釆用阶段式充电方式, 包括第一充电步骤与第二充电步骤。 第 一步釆用小电流对 SEI膜的形成有积极作用, 有利于提高电芯容量, 但长 时间的小电流充电会导致形成的 SEI膜阻抗增大, 从而影响成品电芯的倍 率放电性能, 时间过程长也影响生产效率, 因此第一步小电流(0.1C以内) 短时间(30min以内), 其对阶段式的预充方式而言, 对电芯成品性能的影 响几乎是可以忽略不计的。 通过图 (2 ) 的充电曲线可知, 0.1C充电 5分 钟时, 电压为 2.89V, 而在此之前电压值的变化(上升)很快而且是不稳 定的, 由此, 对于第一步小电流充电时间的下限值, 若以 0.1C充电则优选 为 5分钟, 若以 0.05C充电则优选为 10分钟。 第二步引入大电流, 大电流 的充电方式能够加速副反应的进行, 提高化成效率, 但容易破坏 SEI膜的 形成并导致电芯性能的恶化,同时预充拒使用大电流稳定性和误差均较大, 因此应选择合适的充电电流及充电时间。 本发明的预充方法中大电流选择 在 0.3C - 0.6C之间,充电时间根据电流的大小进行调整,通常在 10 ~ 60min 以内。 对于本发明的阶段式预充工艺而言, 由于第一步电流小而且充电时 间较短, 因此, 第一步所达到的电量可以忽略不计, 而第二步大电流预充 后所要达到的电量应为总电量的 15% ~ 35%优选 15% ~ 30%左右。 The invention adopts a stage charging method, which comprises a first charging step and a second charging step. In the first step, a small current has a positive effect on the formation of the SEI film, which is beneficial to increase the cell capacity, but a long time of small current charging may cause an increase in the impedance of the formed SEI film, thereby affecting the rate discharge performance of the finished cell. The long time process also affects the production efficiency. Therefore, the first step of small current (within 0.1C) is short (within 30min). For the stage precharge method, the impact on the performance of the battery core is almost negligible. . According to the charging curve of (2), when the voltage is charged for 0.1 minutes at 0.1C, the voltage is 2.89V, and before that, the voltage value changes (rises) quickly and is unstable, thus, the first step is small current. The lower limit of the charging time, if charging at 0.1C, it is preferable It is 5 minutes, and if it is charged at 0.05 C, it is preferably 10 minutes. The second step introduces a large current. The charging method of high current can accelerate the side reaction and improve the formation efficiency, but it is easy to damage the formation of the SEI film and cause deterioration of the performance of the cell. At the same time, the pre-filling uses large current stability and error. Larger, so you should choose the right charging current and charging time. In the pre-charging method of the present invention, the large current is selected between 0.3C and 0.6C, and the charging time is adjusted according to the magnitude of the current, usually within 10 to 60 minutes. For the stage pre-filling process of the present invention, since the first step current is small and the charging time is short, the amount of electricity reached in the first step is negligible, and the amount of electricity to be reached after the second step of high current pre-charging is It should be 15% ~ 35% of the total electricity, preferably 15% ~ 30%.
下面通过具体实施例进一步详细描述。 上述部分及以下实施例 19 ~ 34、对比例 3、 4中所用到的电芯均是同一批次生产的 613048AM-1000mAh 电芯, 正极活性物质为钴酸锂和镍钴锰酸锂按 8:2的重量比例混合而成; 实施例 35 ~ 39 及对比例 5、 6 中所用到的电芯均是另一批次生产的 613048AM-1000mAh电芯 , 正极活性物质为钴酸锂和镍钴锰酸锂按 6:4的 重量比例混合而成。 同一批次所有实施例电芯具有一致的正负极敷料量, 电极密度, 釆用相同的电解液注液, 注液量, 保持同样的注液预充及封口, 清洗等实验条件。  The details are described in further detail below by way of specific examples. The above-mentioned parts and the batteries used in the following Examples 19 to 34 and Comparative Examples 3 and 4 were all 613048AM-1000mAh batteries produced in the same batch, and the positive electrode active materials were lithium cobaltate and lithium nickel cobalt manganate according to 8: The weight ratio of 2 is mixed; the batteries used in Examples 35 to 39 and Comparative Examples 5 and 6 are 613048AM-1000mAh batteries produced in another batch, and the positive active materials are lithium cobalt oxide and nickel cobalt manganese. Lithium acid is mixed in a weight ratio of 6:4. All the cells in the same batch have the same positive and negative dressing amount, electrode density, the same electrolyte injection, the amount of liquid injection, and the same pre-filling and sealing, cleaning and other experimental conditions.
实施例 19  Example 19
具体过程步骤如下: 将样品电芯进行首次注液, 注液量为工艺要求 85 % , 再将电芯陈化 1 ~ 2h后上预充拒按 0.05C、 lOmin; 0.3C、 29min的预充 方法进行预充, 然后下拒测量电压, 再次补注液 10 %后对电芯进行挤压并 完成封口, 以上工序步骤均在相同的温湿度环境下进行, 温度≤26°C ; 湿度 ≤2 % 。 在室温环境下, 对已封口的电芯清洗后测量尺寸, 老化 6天后对电芯 进行检测分容, 分容制度按表 5中所示参数进行。 考察其容量、 内阻、 3.92V 尺寸和循环性能测试, 结果见表 6所示。  The specific process steps are as follows: The first sample is injected into the sample cell, the amount of liquid injection is 85% of the process requirement, and the cell is aged for 1 ~ 2 hours, then pre-filled and refused to press 0.05C, lOmin; 0.3C, 29min pre-charge The method pre-charges, then refuses to measure the voltage, and re-fills the liquid 10%, then squeezes the battery and completes the sealing. The above steps are all carried out under the same temperature and humidity environment, the temperature is ≤26°C; the humidity is ≤2 %. In the room temperature environment, the sealed cell is cleaned and measured, and after 6 days of aging, the cell is tested and divided. The capacity system is based on the parameters shown in Table 5. The capacity, internal resistance, 3.92V size and cycle performance test were examined. The results are shown in Table 6.
同样, 其他实施例及对比例 3、 5釆用相同的步骤, 只是预充方法釆用 的时间和电流不一样。  Similarly, the other examples and Comparative Examples 3, 5 use the same steps except that the precharge method uses different times and currents.
对比例 4、 6为传统工艺, 除注液釆用一次性 100 %注液、 预充方法为 表 4中所示以及陈化时间 12 ~ 16h不一样夕卜,其他步骤与以上实施例相同。  Comparative Examples 4 and 6 are conventional processes, except for the one-time 100% injection, the prefilling method is shown in Table 4 and the aging time is 12 to 16 hours, and the other steps are the same as the above embodiment.
所有实施例及对比例的预充方法见表 4所示,其技术效果数据见表 6。 表 4. 各实施例及对比例的预充方法 The prefilling methods of all the examples and comparative examples are shown in Table 4, and the technical effect data thereof is shown in Table 6. Table 4. Prefilling methods for each of the examples and comparative examples
Figure imgf000012_0001
表 5. 分容制度
Figure imgf000012_0001
Table 5. Capacity sharing system
Figure imgf000012_0002
Figure imgf000012_0002
锂电芯在这里化成得到容量, 并知道容量的大小, 就是分容。 通过 容, 确定了电芯的等级。 表 6. 各实施例及对比例技术效果 The lithium battery is here to get the capacity, and know the size of the capacity, that is, the volume. Through the capacity, the level of the battery cell is determined. Table 6. Technical effects of various examples and comparative examples
Figure imgf000013_0001
实施例 19 ~ 34与对比例 4以及实施例 35 ~ 39与对比例 6的数据表明, 通过选用本发明的预充方法, 能够使电芯达到与釆用传统预充工艺的电芯 相当甚至更优的电学性能, 同时能够极大地缩减预充时间,提高生产效率。 而实施例 19 ~ 34与对比例 3以及实施例 35 ~ 39与对比例 5的数据表明了 第一小电流充电的必要性, 若不进行第一步小电流预充的话其成品电芯尺 寸、 容量发挥以及循环性能等效果都要更差。 本发明通过引入大电流预充, 能够缩短电芯的预充时间, 进一步优化 正极活性物质为钴酸锂和镍钴锰酸锂混合的锂离子电池预充方法为
Figure imgf000013_0001
The data of Examples 19 to 34 and Comparative Example 4 and Examples 35 to 39 and Comparative Example 6 show that by selecting the prefilling method of the present invention, it is possible to make the cell reach or even more than that of the conventional prefilling process. Excellent electrical performance, while greatly reducing pre-filling time and improving production efficiency. The data of Examples 19 to 34 and Comparative Example 3 and Examples 35 to 39 and Comparative Example 5 indicate the necessity of the first small current charging, and if the first step of the small current precharging is not performed, the finished cell size, The effects of capacity and loop performance are even worse. The invention can shorten the pre-charging time of the electric core by introducing a large current pre-charging, and further optimize the pre-charging method of the lithium ion battery in which the positive active material is a mixture of lithium cobaltate and lithium nickel cobalt manganate.
0.05C、 lOmin; 0.4C、 22min。 该优化的预充方法是由以上各实施例横向、 纵向的对比, 最能体现预充方法优劣的数据是正极克容量和循环性能以及 预充时间, 再考察其内阻和尺寸等综合性能, 从而对比得出最优化的预充 方法。 0.05C, lOmin; 0.4C, 22min. The optimized pre-filling method is a horizontal and vertical comparison of the above embodiments, and the data which best reflects the advantages and disadvantages of the pre-filling method are the positive gram capacity and the cycle performance and the pre-charge time, and then the comprehensive performances such as internal resistance and size are examined. , thus comparing the optimized pre-filling method.
在锂离子电池的预充过程中, 随着正极活性物质中三元镍钴锰酸锂比 例的增加,预充 SEI膜形成过程副反应产气、排气过程其时间会相应增加, 因此, 本发明的锂离子电池预充方法所适用的锂离子电池, 其对正极活性 物质中钴酸锂和镍钴锰酸锂混合的比例有一定范围要求, 即钴酸锂所占的 重量百分含量应为 60% ~ 80%, 镍钴锰酸锂所占应为 20% ~ 40%。  During the pre-charging process of the lithium ion battery, as the proportion of the ternary nickel-cobalt-manganese oxide in the positive electrode active material increases, the time during the production of the pre-charged SEI film by the side reaction gas production and the exhaust process will increase accordingly. The lithium ion battery to which the lithium ion battery pre-filling method is applied has a certain range of requirements for the mixing ratio of lithium cobaltate and lithium nickel cobalt manganese oxide in the positive electrode active material, that is, the weight percentage of lithium cobalt oxide should be For 60% ~ 80%, lithium nickel cobalt manganese oxide should account for 20% ~ 40%.
本发明以上具体实施方式中所选用的是 lOOOmAh的电芯,对于其它容 量大小的电芯, 只需满足正极活性物质为钴酸锂和镍钴锰酸锂的混合, 混 合比例范围在钴酸锂占 60% ~ 80% , 镍钴锰酸锂占 20% ~ 40% , 则本发明 的预充方法对其同样适合。 但是, 考虑到如果锂离子电池电芯的标称容量 过大, 大于 1500mAh时, 由于相应的预充方法第二步的充电电流比较大, 对此预充拒的电流误差比较大, 或是稳定性比较差, 由此对电芯性能会造 成一定影响。 同时考虑三元镍钴锰酸锂正极材料相对于钴酸锂来说还未大 范围商业化, 再者其混合的比例所限制, 若容量过大其预充过程其副反应 产气排气要比理论上的复杂, 时间也会长很多, 因此, 本发明的预充方法 所适合的电芯容量范围是小于 1500mAh, 优选小于 1200mAh。  In the above specific embodiment of the present invention, a battery of 1000 mAh is selected. For other capacity batteries, only the positive active material is required to be a mixture of lithium cobaltate and lithium nickel cobalt manganate, and the mixing ratio ranges from lithium cobaltate. The pre-filling method of the present invention is equally suitable for 60% to 80% and lithium nickel cobalt manganese oxide for 20% to 40%. However, considering that if the nominal capacity of the lithium ion battery cell is too large, greater than 1500 mAh, the current error of the second step is relatively large due to the corresponding precharge method, and the current error is relatively large or stable. Poor sex, which will have a certain impact on the performance of the battery. At the same time, considering the ternary nickel-cobalt-manganese hydride cathode material has not been widely commercialized with respect to lithium cobaltate, and the proportion of its mixing is limited. If the capacity is too large, its side-by-side reaction gas is required to be exhausted. More time-consuming than theoretical, the time will be much longer. Therefore, the cell capacity range suitable for the pre-filling method of the present invention is less than 1500 mAh, preferably less than 1200 mAh.
本发明的预充方法所适用的锂离子电池, 其正极活性物质中的镍钴锰 酸锂优选元素比满足 Ni:Co:Mn = 1/3: 1/3: 1/3的镍钴锰酸锂, 并且在本发 明具体实施方式以及所有实施例、 对比例中所用的镍钴锰酸锂, 其分子式 均为 LiNi^Co^Mn^C^  In the lithium ion battery to which the pre-filling method of the present invention is applied, the nickel-cobalt-manganese oxide in the positive electrode active material preferably has an element ratio of Ni:Co:Mn = 1/3: 1/3: 1/3 of nickel-cobalt-manganic acid. Lithium, and lithium nickel cobalt manganese oxide used in the specific embodiments of the present invention and all the examples and comparative examples, the molecular formula is LiNi^Co^Mn^C^
本发明预充方法的实施必将使镍钴锰酸锂三元材料更广泛的运用打 好坚实的基础。  The implementation of the pre-filling method of the present invention will surely lay a solid foundation for the wider application of lithium nickel cobalt manganate ternary materials.
三、 正极活性物质为钴酸锂和镍钴酸锂  3. The positive active materials are lithium cobaltate and lithium nickel cobaltate.
考察正极活性物质为钴酸锂 ( LiCo02 )和镍钴酸锂 ( LiNixCo1-x02, x=0.75-0.85 )按重量比例 8:2混合,预充电流为 0.1C的充电曲线图, 如图 3 所示。 The charge activity of the positive electrode active material was lithium cobaltate (LiCo0 2 ) and lithium nickel cobaltate (LiNi x Co 1-x 0 2 , x=0.75-0.85) mixed at a weight ratio of 8:2, and the precharge current was 0.1C. Figure, as shown in Figure 3.
根据 0.1C 充电时间 -电压值曲线图, 分别考察充电量在 10 % ( 60min )、 20 % ( 120min )和 30 % ( 180min ) (电压值对应为 3.63V、 3.68V 和 3.80V )之间的成品电芯性能。 由于 SEI膜的成膜电压为 3.60V, 在预充According to the 0.1C charging time-voltage value graph, the charge is 10% respectively. Finished cell performance between (60min), 20% (120min) and 30% (180min) (voltage values corresponding to 3.63V, 3.68V and 3.80V). Since the film formation voltage of the SEI film is 3.60V, it is precharged.
(化成)过程中, 虽然负极表面形成 SEI膜的主要反应会因化成电压不同 而不同, 但在充电电压达到成膜电压 3.60V时, SEI膜开始形成, 并在其 后的充电过程中随着反应的进行逐渐地改变其结构和性能。 也就是说, 由 图(3 )可知, 当充电电量为 10%时, 由于电压以达 3.63V超过 3.60V, SEI 膜就已经开始形成。 但由于该体系混合了二元材料和该二元材料中镍的含 量比较高, 为进一步验证成膜及其副反应是否充分完成, 本发明先将电芯 用 0.1C分别充电 60min、 90min、 120min和 150min, 使电芯预充电量在 10 %、 15 %、 20 %和 25 % , 分别考察其容量、 尺寸、 内阻等性能, 通过考 察结果, 预充电量在 10 %、 15 %和 20 %时, 因成膜副反应排气不充分, 电 芯有尺寸超厚和析锂等不良现象。 本发明釆用的是先小电流后大电流阶段 式的预充方法, 分别考察小电流和大电流预充对该材料体系的影响, 结果 是小电流充电时间在 30min 内对电芯性能的影响不是一个关键因子,而充 电电流过大, 大于 0.6C电芯有析锂现象。 因此本发明釆用不同的预充电流 及时间组合, 使得预充电量在 25 % - 45 %之间的不同下拒电压值, 考察电 芯的容量(容量发挥)、 内阻、 尺寸及其循环性能。 During the formation process, although the main reaction of forming the SEI film on the surface of the negative electrode may be different depending on the formation voltage, when the charging voltage reaches the film formation voltage of 3.60 V, the SEI film starts to form and is subsequently charged during the subsequent charging process. The progress of the reaction gradually changes its structure and properties. That is to say, as shown in Fig. (3), when the charge amount is 10%, since the voltage exceeds 3.60 V by 3.63 V, the SEI film has begun to form. However, since the binary material is mixed in the system and the content of nickel in the binary material is relatively high, in order to further verify whether the film formation and its side reactions are fully completed, the present invention first charges the cells with 0.1 C for 60 min, 90 min, and 120 min, respectively. And 150min, the cell pre-charge amount is 10%, 15%, 20% and 25%, respectively, the capacity, size, internal resistance and other properties are examined. By examining the results, the pre-charge amounts are 10%, 15% and 20%. At the time of the film formation side reaction, the exhaust gas is insufficient, and the battery core has a problem of excessive size and lithium deposition. The invention uses a pre-charging method of a small current and a large current stage, respectively, to investigate the influence of the small current and the large current pre-charging on the material system, and the result is the influence of the small current charging time on the performance of the battery in 30 minutes. It is not a key factor, and the charging current is too large, and the lithium core is more than 0.6C. Therefore, the present invention uses different pre-charge currents and time combinations, so that the pre-charge amount is between 25% and 45%, and the voltage capacity (capacity play), internal resistance, size, and cycle thereof are investigated. performance.
本发明釆用阶段式充电方式, 包括第一充电步骤与第二充电步骤。 第 一步釆用小电流对 SEI膜的形成有积极作用, 有利于提高电芯容量, 但长 时间的小电流充电会导致形成的 SEI膜阻抗增大, 从而影响成品电芯的倍 率放电性能, 时间过程长也影响生产效率, 因此第一步小电流(0.1C以内) 短时间(30min以内), 其对阶段式的预充方式而言, 对电芯成品性能的影 响几乎是可以忽略不计的。 通过图 (3 ) 的充电曲线可知, 0.1C充电 5分 钟时, 电压为 2.89V, 而在此之前电压值的变化(上升)很快而且是不稳 定的, 由此, 对于第一步小电流充电时间的下限值, 若以 0.1C充电则优选 为 5分钟, 若以 0.05C充电则优选为 10分钟。 第二步引入大电流, 大电流 的充电方式能够加速副反应的进行, 提高化成效率, 但容易破坏 SEI膜的 形成并导致电芯性能的恶化,同时预充拒使用大电流稳定性和误差均较大, 因此应选择合适的充电电流及充电时间。 本发明的预充方法中大电流选择 在 0.3C - 0.6C之间,充电时间根据电流的大小进行调整,通常在 25 ~ 80min 以内。 对于本发明的阶段式预充工艺而言, 由于第一步电流小而且充电时 间较短, 因此, 第一步所达到的电量可以忽略不计, 而第二步大电流预充 后所要达到的电量应为总电量的 25% ~ 45%, 优选 25% ~ 40%, 更优选 25% ~ 35%左右。 The invention adopts a stage charging method, which comprises a first charging step and a second charging step. In the first step, a small current has a positive effect on the formation of the SEI film, which is beneficial to increase the cell capacity, but a long time of small current charging may cause an increase in the impedance of the formed SEI film, thereby affecting the rate discharge performance of the finished cell. The long time process also affects the production efficiency. Therefore, the first step of small current (within 0.1C) is short (within 30min). For the stage precharge method, the impact on the performance of the battery core is almost negligible. . According to the charging curve of (3), when the voltage is charged for 0.1 minutes at 0.1C, the voltage is 2.89V, and before that, the voltage value changes (rises) quickly and is unstable, thus, the first step is small current. The lower limit of the charging time is preferably 5 minutes when charged at 0.1 C, and preferably 10 minutes when charged at 0.05 C. The second step introduces a large current. The charging method of high current can accelerate the side reaction and improve the formation efficiency, but it is easy to damage the formation of the SEI film and cause deterioration of the performance of the cell. At the same time, the pre-filling uses large current stability and error. Larger, so you should choose the right charging current and charging time. In the pre-charging method of the present invention, the large current is selected between 0.3C and 0.6C, and the charging time is adjusted according to the magnitude of the current, usually within 25 to 80 minutes. For the stage pre-charging process of the present invention, since the first step current is small and the charging time is short, the amount of electricity achieved in the first step is negligible, and the second step is pre-charging the large current. The amount of electricity to be reached afterwards should be 25% to 45% of the total amount of electricity, preferably 25% to 40%, more preferably 25% to 35%.
下面通过具体实施例进一步详细描述。 上述部分、 实施例 40-53及对 比例 7-8中所用到的电芯均是同一批次生产的 043855A-950mAh电芯, 正 极活性物质为 LiCo02和 LiNixCo1-x02 (x=0.75 - 0.85) 按 LiCo02 : LiNixCoi-x02 = 8:2的比例混合而成。 同一批次所有实施例电芯具有一致的 正负极敷料量, 电极密度, 釆用相同的电解液注液, 注液量, 保持同样的 注液预充及封口, 清洗等实验条件。 The details are described in further detail below by way of specific examples. The batteries used in the above sections, Examples 40-53 and Comparative Examples 7-8 were all 043855A-950mAh cells produced in the same batch, and the positive active materials were LiCo0 2 and LiNi x Co 1-x 0 2 (x =0.75 - 0.85) Mixed in a ratio of LiCo0 2 : LiNi x Coi -x 0 2 = 8:2. All the cells in the same batch have the same positive and negative dressing amount, electrode density, the same electrolyte injection, the amount of liquid injection, and the same pre-filling and sealing, cleaning and other experimental conditions.
实施例 40  Example 40
具体过程步骤如下: 将样品电芯进行首次注液, 注液量为工艺要求 85 % , 再将电芯陈化 1 ~ 2h后上预充拒按 0.05C、 lOmin; 0.3C、 50min的预充 方法进行预充, 然后下拒测量电压, 再次补注液 10 %后对电芯进行挤压并 完成封口, 以上工序步骤均在相同的温湿度环境下进行, 温度≤26°C ; 湿度 ≤2 % 。 在室温环境下, 对已封口的电芯清洗后测量尺寸, 老化 6天后对电芯 进行检测分容, 分容制度按表 8中所示参数进行。 考察其容量、 内阻、 3.92V 尺寸和循环性能测试, 结果见表 9所示。  The specific process steps are as follows: The sample cell is firstly injected, the amount of liquid injection is 85% of the process requirement, and the cell is aged for 1 to 2 hours, and then pre-filled to 0.05 C, lOmin; 0.3 C, 50 min precharge The method pre-charges, then refuses to measure the voltage, and re-fills the liquid 10%, then squeezes the battery and completes the sealing. The above steps are all carried out under the same temperature and humidity environment, the temperature is ≤26°C; the humidity is ≤2 %. At room temperature, the sealed cells are cleaned and measured. After 6 days of aging, the cells are tested and divided. The volumetric system is based on the parameters shown in Table 8. The capacity, internal resistance, 3.92V size and cycle performance test were examined. The results are shown in Table 9.
同样, 其他实施例及对比例 7釆用相同的步骤, 只是预充方法釆用的 时间和电流不一样。 对比例 8为传统工艺, 除注液釆用一次性 100 %注液、 预充方法为表 7中所示以及陈化时间 12 ~ 16h不一样外, 其他步骤与以上 实施例相同。 所有实施例及对比例的预充方法见表 7所示, 其技术效果数 据见表 9。  Similarly, the other steps and the same procedure were used for the other examples, except that the time and current used in the pre-filling method were different. Comparative Example 8 is a conventional process, except that the one-time 100% injection, the prefilling method is the same as shown in Table 7 and the aging time is 12 to 16 hours, and the other steps are the same as the above embodiment. The prefilling methods of all the examples and comparative examples are shown in Table 7, and the technical effect data thereof is shown in Table 9.
表 7. 各实施例及对比例的预充方法  Table 7. Prefilling methods for each of the examples and comparative examples
Figure imgf000016_0001
实施例 50 0.05C 12min 0.4C 38 min 26.3 % 实施例 51 0.05C 20min 0.4C 38 min 27.0 % 实施例 52 0.05C 30min 0.4C 38 min 27.8 % 实施例 53 0.05C 5min 0.4C 38 min 25.8 % 对比例 7 0 0 0.4C 38 min 25.3 % 对比例 8 0.1C 360min 0 0 60.0 % 表 8. 分容制度
Figure imgf000016_0001
Example 50 0.05 C 12 min 0.4 C 38 min 26.3 % Example 51 0.05 C 20 min 0.4 C 38 min 27.0 % Example 52 0.05 C 30 min 0.4 C 38 min 27.8 % Example 53 0.05 C 5 min 0.4 C 38 min 25.8 % Comparative Example 7 0 0 0.4C 38 min 25.3 % Comparative Example 8 0.1C 360min 0 0 60.0 % Table 8. Capacity-sharing system
Figure imgf000017_0001
Figure imgf000017_0001
锂电芯在这里化成得到容量, 并知道容量的大小, 就是分容。 通过 容, 确定了电芯的等级。  The lithium battery is here to get the capacity, and know the size of the capacity, that is, the volume. Through the capacity, the level of the battery cell is determined.
表 9. 各实施例及对比例技术效果  Table 9. Technical effects of various examples and comparative examples
Figure imgf000017_0002
实施例 40 ~ 53与对比例 8的数据表明, 通过选用本发明的预充方法, 时能够极大地缩减预充时间, 提高生产效率。 而实施例 40 ~ 53与对比例 7 的数据表明了第一小电流充电的必要性, 若不进行第一步小电流预充的话 其成品电芯尺寸、 容量发挥以及循环性能等效果都要更差。
Figure imgf000017_0002
The data of Examples 40 to 53 and Comparative Example 8 show that by selecting the prefilling method of the present invention, the precharge time can be greatly reduced, and the production efficiency can be improved. The data of Examples 40 ~ 53 and Comparative Example 7 indicate the necessity of the first small current charging. If the first step of small current precharging is not carried out, the effect of the finished cell size, capacity and cycle performance will be more effective. difference.
本发明通过引入大电流预充, 能够缩短电芯的预充时间, 进一步优化 的预充方法为 0.05C、 lOmin; 0.4C、 38min。 该优化的预充方法是由以上 各实施例横向、 纵向的对比, 最能体现预充方法优劣的数据是正极克容量 和循环性能以及预充时间, 再考察其内阻和尺寸等综合性能, 从而对比得 出最优化的预充方法。  The invention can shorten the pre-charging time of the battery core by introducing large current pre-charging, and the further optimized pre-charging method is 0.05C, lOmin; 0.4C, 38min. The optimized pre-filling method is a horizontal and vertical comparison of the above embodiments, and the data which best reflects the advantages and disadvantages of the pre-filling method are the positive gram capacity and the cycle performance and the pre-charge time, and then the comprehensive performances such as internal resistance and size are examined. , thus comparing the optimized pre-filling method.
通过进一步的实验证实, 对于正极活性物质为钴酸锂 ( LiCo02 )与镍 钴酸锂(LiNixCo1-x02, x=0.75 ~ 0.85 )的混合材料的锂离子电池, 当钴酸 锂与镍钴酸锂的重量比满足钴酸锂占 75% ~ 85% , 镍钴酸锂占 15% ~ 25% 时, 利用本发明的预充方法, 使预充电量达到所述锂离子电池总电量的 25% ~ 45%, 优选达到 25% ~ 40%, 即釆用阶段式充电方式, 包括第一充 电步骤与第二充电步骤,第一充电步骤的充电电流为小于 0.1 C ,优选 0.05 ~ 0.1C, 充电时间为 5 ~ 30min, 优选 5 ~ 15min; 第二充电步骤的充电电流 为 0.3 ~ 0.6C, 充电时间 25 ~ 80分钟, 则均能达到优化电芯性能的同时提 高预充效率的目的, 达到生产要求。 It was confirmed by further experiments that the lithium ion battery with a positive electrode active material of a mixed material of lithium cobaltate (LiCo0 2 ) and lithium nickel cobaltate (LiNi x Co 1-x 0 2 , x=0.75 ~ 0.85 ), when cobalt acid When the weight ratio of lithium to lithium nickel cobaltate satisfies 75% to 85% of lithium cobaltate and 15% to 25% of lithium nickel cobaltate, the precharge amount of the lithium ion battery is achieved by the precharge method of the present invention. 25% ~ 45% of the total amount of electricity, preferably 25% ~ 40%, that is, using the stage charging method, including the first charging step and the second charging step, the charging current of the first charging step is less than 0.1 C, preferably 0.05 ~ 0.1C, charging time is 5 ~ 30min, preferably 5 ~ 15min; charging current of the second charging step is 0.3 ~ 0.6C, charging time is 25 ~ 80 minutes, both can optimize the performance of the battery while improving the pre-charging efficiency The purpose is to meet production requirements.
本发明以上具体实施方式中所选用的是 950mAh的电芯, 对于其它容 量大小的电芯, 只需满足正极活性物质为钴酸锂和镍钴酸锂的混合, 且优 选混合比例钴酸锂占 75% ~ 85%, 镍钴酸锂占 15% ~ 25%, 则本发明的预 充方法对其同样适合。但是,考虑到如果锂离子电池电芯的标称容量过大, 大于 1200mAh时, 由于相应的预充方法第二步的充电电流比较大,对此预 充拒的电流误差比较大, 或是稳定性比较差, 由此对电芯性能会造成一定 影响; 同时考虑二元镍钴酸锂正极材料相对于钴酸锂来说还未大范围商业 化, 再者二元材料中镍含量比例较高 (在 0.75 - 0.85之间)所限制, 若容 量过大预充过程其副反应产气排气要比理论上的复杂, 时间也会长很多, 因此, 本发明的预充方法所适合的电芯容量范围优选是≤1200mAh。 本发 明预充方法的实施必将使镍钴酸锂等二元材料更广泛的运用打好坚实的基 础。  In the above specific embodiment of the present invention, a 950 mAh battery cell is selected. For other capacity batteries, it is only necessary to satisfy the mixture of the positive electrode active material as lithium cobaltate and lithium nickel cobaltate, and preferably the mixed proportion of lithium cobaltate. 75% to 85%, lithium nickel cobaltate accounts for 15% to 25%, and the prefilling method of the present invention is equally suitable. However, considering that if the nominal capacity of the lithium ion battery cell is too large, greater than 1200 mAh, the current error of the pre-filling is relatively large or stable due to the relatively large charging current of the second step of the corresponding pre-charging method. Poor sex, which will have a certain impact on the performance of the battery; at the same time consider that the binary lithium nickel cobalt oxide cathode material has not been widely commercialized relative to lithium cobalt oxide, and the proportion of nickel in the binary material is higher. (Limited between 0.75 and 0.85), if the capacity is too large, the secondary reaction gas is exhausted in the precharge process, which is more complicated than the theoretical one, and the time is much longer. Therefore, the precharge method of the present invention is suitable for electricity. The core capacity range is preferably ≤ 1200 mAh. The implementation of the pre-filling method of the present invention will surely lay a solid foundation for the wider application of binary materials such as lithium nickel cobaltate.

Claims

权 利 要 求 书 Claim
1、 一种锂离子电池预充方法, 其特征在于: 所述锂离子电池的预充方 法是釆用阶段式充电, 所述阶段式充电包括至少两个充电步骤, 第二充电 步骤的充电电流大于第一充电步骤的充电电流, 并且第一充电步骤与第二 充电步骤的总的预充电量为所述锂离子电池总电量的 10% ~ 45%。 A method for pre-charging a lithium ion battery, characterized in that: the pre-charging method of the lithium ion battery is a stage charging, the stage charging comprises at least two charging steps, and the charging current of the second charging step The charging current is greater than the charging current of the first charging step, and the total pre-charging amount of the first charging step and the second charging step is 10% to 45% of the total amount of the lithium ion battery.
2、根据权利要求 1所述的一种锂离子电池预充方法, 其特征在于: 所 述锂离子电池的正极活性物质为钴酸锂, 并且第一充电步骤与第二充电步 骤的总的预充电量为所述锂离子电池总电量的 10% ~ 35%。  2 . The method of precharging a lithium ion battery according to claim 1 , wherein: the positive active material of the lithium ion battery is lithium cobaltate, and the total pre-step of the first charging step and the second charging step The amount of charge is 10% to 35% of the total amount of the lithium ion battery.
3、根据权利要求 2所述的一种锂离子电池预充方法, 其特征在于: 第 一充电步骤与第二充电步骤的总的预充电量为所述锂离子电池总电量的 10% ~ 30%。  The method for precharging a lithium ion battery according to claim 2, wherein: the total precharge amount of the first charging step and the second charging step is 10% to 30 of the total amount of the lithium ion battery. %.
4、根据权利要求 2或 3所述的一种锂离子电池预充方法,其特征在于: 所述第一充电步骤的充电电流为小于 0.1C, 充电时间为 5 ~ 30min。  The method for precharging a lithium ion battery according to claim 2 or 3, wherein: the charging current in the first charging step is less than 0.1 C, and the charging time is 5 to 30 min.
5、根据权利要求 4所述的一种锂离子电池预充方法, 其特征在于: 所 述第一充电步骤的充电电流为 0.05C - 0.1C, 充电时间为 5 ~ 15min。  The method for precharging a lithium ion battery according to claim 4, wherein the charging current in the first charging step is 0.05 C - 0.1 C, and the charging time is 5 ~ 15 min.
6、根据权利要求 2或 3所述的一种锂离子电池预充方法,其特征在于: 所述第二充电步骤的充电电流为 0.3C ~ 0.6C, 充电时间为 10 ~ 60min。  The method for precharging a lithium ion battery according to claim 2 or 3, wherein the charging current in the second charging step is 0.3 C to 0.6 C, and the charging time is 10 to 60 min.
7、根据权利要求 4所述的一种锂离子电池预充方法, 其特征在于: 所 述第二充电步骤的充电电流为 0.3C ~ 0.6C , 充电时间为 10 ~ 60min。  The method for precharging a lithium ion battery according to claim 4, wherein the charging current in the second charging step is 0.3 C to 0.6 C, and the charging time is 10 to 60 min.
8、根据权利要求 7所述的一种锂离子电池预充方法, 其特征在于: 所 述第一充电步骤的充电电流为 0.05C,充电时间为 lOmin,第二充电步骤的 充电电流为 0.5C, 充电时间为 12min。  The method for precharging a lithium ion battery according to claim 7, wherein: the charging current in the first charging step is 0.05 C, the charging time is 10 min, and the charging current in the second charging step is 0.5 C. , charging time is 12min.
9、根据权利要求 1所述的一种锂离子电池预充方法, 其特征在于: 所 述锂离子电池的正极活性物质为钴酸锂与镍钴锰酸锂的混合材料, 并且第 一充电步骤与第二充电步骤的总的预充电量为所述锂离子电池总电量的 15% ~ 35%。  9. The method of precharging a lithium ion battery according to claim 1, wherein: the positive active material of the lithium ion battery is a mixed material of lithium cobaltate and lithium nickel cobalt manganese oxide, and the first charging step The total pre-charge amount with the second charging step is 15% to 35% of the total amount of the lithium ion battery.
10、 根据权利要求 9所述的一种锂离子电池预充方法, 其特征在于: 第一充电步骤与第二充电步骤的总的预充电量为所述锂离子电池总电量的 15% ~ 30%。  10 . The method of precharging a lithium ion battery according to claim 9 , wherein: the total pre-charging amount of the first charging step and the second charging step is 15% to 30 of the total amount of the lithium ion battery %.
11、根据权利要求 9或 10所述的一种锂离子电池预充方法,其特征在  A method for precharging a lithium ion battery according to claim 9 or 10, characterized in that
1 于: 所述锂离子电池的正极活性物质中, 钴酸锂占 60% ~ 80%, 镍钴锰酸 锂占 20% ~ 40%, 所述为重量百分比。 1 In the positive electrode active material of the lithium ion battery, lithium cobaltate accounts for 60% to 80%, and lithium nickel cobalt manganese oxide accounts for 20% to 40%, which is a weight percentage.
12、 根据权利要求 11所述的一种锂离子电池预充方法, 其特征在于: 所述第一充电步骤的充电电流为小于 0.1C, 充电时间为 5 ~ 30min。  12. The method of precharging a lithium ion battery according to claim 11, wherein: the charging current in the first charging step is less than 0.1 C, and the charging time is 5 to 30 min.
13、 根据权利要求 12所述的一种锂离子电池预充方法, 其特征在于: 所述第一充电步骤的充电电流为 0.05C ~ 0.1C, 充电时间为 5 ~ 15min。  13. The method of precharging a lithium ion battery according to claim 12, wherein: the charging current in the first charging step is 0.05 C to 0.1 C, and the charging time is 5 to 15 min.
14、 根据权利要求 11所述的一种锂离子电池预充方法, 其特征在于: 所述第二充电步骤的充电电流为 0.3C ~ 0.6C , 充电时间为 10 ~ 60min。  14. The method of precharging a lithium ion battery according to claim 11, wherein: the charging current in the second charging step is 0.3 C to 0.6 C, and the charging time is 10 to 60 min.
15、 根据权利要求 12所述的一种锂离子电池预充方法, 其特征在于: 所述第二充电步骤的充电电流为 0.3C ~ 0.6C , 充电时间为 10 ~ 60min。  15. The method of precharging a lithium ion battery according to claim 12, wherein: the charging current in the second charging step is 0.3 C to 0.6 C, and the charging time is 10 to 60 min.
16、 根据权利要求 15所述的一种锂离子电池预充方法, 其特征在于: 所述第一充电步骤的充电电流为 0.05C,充电时间为 lOmin,第二充电步骤 的充电电流为 0.4C , 充电时间为 22min。  The method for precharging a lithium ion battery according to claim 15, wherein: the charging current of the first charging step is 0.05 C, the charging time is 10 min, and the charging current of the second charging step is 0.4 C. , charging time is 22min.
17、 根据权利要求 1所述的一种锂离子电池预充方法, 其特征在于: 所述锂离子电池的正极活性物质为钴酸锂与镍钴酸锂的混合材料, 并且第 一充电步骤与第二充电步骤的总的预充电量为所述锂离子电池总电量的 25% ~ 45%。  17. The method of precharging a lithium ion battery according to claim 1, wherein: the positive active material of the lithium ion battery is a mixed material of lithium cobaltate and lithium nickel cobaltate, and the first charging step is The total pre-charge amount of the second charging step is 25% to 45% of the total amount of the lithium ion battery.
18、 根据权利要求 17所述的一种锂离子电池预充方法, 其特征在于: 第一充电步骤与第二充电步骤的总的预充电量为所述锂离子电池总电量的 25% ~ 40%。  18. The method of precharging a lithium ion battery according to claim 17, wherein: the total precharge amount of the first charging step and the second charging step is 25% to 40% of the total amount of the lithium ion battery. %.
19、 根据权利要求 17或 18所述的一种锂离子电池预充方法, 其特征 在于: 所述锂离子电池的正极活性物质中, 镍钴酸锂的分子式为 LiNixCo1-x02, x=0.75 ~ 0.85。 The method for precharging a lithium ion battery according to claim 17 or 18, wherein: in the positive electrode active material of the lithium ion battery, the molecular formula of lithium nickel cobaltate is LiNi x Co 1-x 0 2 , x=0.75 ~ 0.85.
20、 根据权利要求 19所述的一种锂离子电池预充方法, 其特征在于: 所述锂离子电池的正极活性物质中, 钴酸锂占 75% ~ 85% , 镍钴酸锂占 15% ~ 25%, 所述为重量百分比。  The method for precharging a lithium ion battery according to claim 19, wherein: among the positive active materials of the lithium ion battery, lithium cobaltate accounts for 75% to 85%, and lithium nickel cobaltate accounts for 15%. ~ 25%, the percentage is by weight.
21、 根据权利要求 20所述的一种锂离子电池预充方法, 其特征在于: 所述锂离子电池的正极活性物质中, 钴酸锂占 80%, 镍钴酸锂占 20%, 所 述为重量百分比。  The method for precharging a lithium ion battery according to claim 20, wherein: in the positive active material of the lithium ion battery, lithium cobaltate accounts for 80%, and lithium nickel cobaltate accounts for 20%. As a percentage by weight.
22、 根据权利要求 17、 18、 20、 21中任意一项所述的一种锂离子电池 预充方法, 其特征在于: 所述第一充电步骤的充电电流为小于 0.1C, 充电 时间为 5 ~ 30min。 22. A lithium ion battery according to any one of claims 17, 18, 20, The precharging method is characterized in that: the charging current of the first charging step is less than 0.1 C, and the charging time is 5 to 30 min.
23、 根据权利要求 17、 18、 20、 21中任意一项所述的一种锂离子电池 预充方法, 其特征在于: 所述第二充电步骤的充电电流为 0.3C ~ 0.6C, 充 电时间为 25 ~ 80min。  The method for precharging a lithium ion battery according to any one of claims 17, 18, 20, 21, wherein: the charging current of the second charging step is 0.3 C ~ 0.6 C, charging time It is 25 ~ 80min.
24、 根据权利要求 22所述的一种锂离子电池预充方法, 其特征在于: 所述第二充电步骤的充电电流为 0.3C ~ 0.6C , 充电时间为 25 ~ 80min。  The method for precharging a lithium ion battery according to claim 22, wherein: the charging current in the second charging step is 0.3 C to 0.6 C, and the charging time is 25 to 80 min.
25、 根据权利要求 24所述的一种锂离子电池预充方法, 其特征在于: 所述第一充电步骤的充电电流为 0.05C,充电时间为 lOmin,第二充电步骤 的充电电流为 0.4C , 充电时间为 38min。  The method for precharging a lithium ion battery according to claim 24, wherein: the charging current of the first charging step is 0.05 C, the charging time is 10 min, and the charging current of the second charging step is 0.4 C. , charging time is 38min.
26、根据权利要求 2、 9、 17中任意一项所述的一种锂离子电池预充方 法, 其特征在于: 所述阶段式充电前的电解液注液量为 80% ~ 85%, 阶段 式充电后再注入电解液 15% ~ 10%。  The method for precharging a lithium ion battery according to any one of claims 2, 9 and 17, wherein: the electrolyte injection amount before the staged charging is 80% to 85%, the stage After charging, inject 15% ~ 10% of electrolyte.
3  3
PCT/CN2010/070202 2009-01-15 2010-01-15 Pre-charging method for lithium-ion battery WO2010081422A1 (en)

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