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CN1332475C - Production of LixCoO2 from recovering waste lithium ionic battery - Google Patents

Production of LixCoO2 from recovering waste lithium ionic battery Download PDF

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CN1332475C
CN1332475C CNB2005100150781A CN200510015078A CN1332475C CN 1332475 C CN1332475 C CN 1332475C CN B2005100150781 A CNB2005100150781 A CN B2005100150781A CN 200510015078 A CN200510015078 A CN 200510015078A CN 1332475 C CN1332475 C CN 1332475C
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CN1747224A (en
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梁辉
黄继承
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TIANJIN RECYCLABLE RESOURCES INSTITUTE OF ALL CHINA FEDERATION OF SUPPLY AND MARKETING COOPERATIVES
Tianjin University
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TIANJIN RECYCLABLE RESOURCES INSTITUTE OF ALL CHINA FEDERATION OF SUPPLY AND MARKETING COOPERATIVES
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Abstract

本发明公开了一种从报废的锂离子电池中回收制备LixCoO2的方法,属于液相包覆沉淀复合粉体制备工艺。该方法包括步骤:切割开电池,分离正极材料并将正极材料剪成小碎片;将剪成的碎片浸泡在N-甲基-2-吡咯烷酮液体中,加热分离活性物质LixCoO2,得到黑色粉末;黑色粉末分散硝酸溶液或盐酸溶液中,过滤得到含有Co2+、Li+离子的硝酸盐溶液或氯化物溶液;向含有Co2+、Li+离子的酸性浸取溶液加入NH3·H2O,形成蓝色沉淀,同时加表面活性剂,补加LiOH调整悬浮液中的Li+离子的浓度;将悬浮液中的沉淀物过滤并干燥,在600~900℃的温度下焙烧,即得到LixCoO2粉体。本发明从废旧的锂离子电池中能回收至少95%的钴和至少93%的锂,制得LixCoO2粉体,粒径为0.2~1.0μm、比表面积为2.0~6.0m2·g-1

Figure 200510015078

The invention discloses a method for recovering and preparing Li x CoO 2 from discarded lithium ion batteries, which belongs to the preparation process of liquid-phase coating precipitation composite powder. The method comprises the steps of: cutting the battery, separating the positive electrode material and cutting the positive electrode material into small pieces; soaking the cut pieces in N-methyl-2-pyrrolidone liquid, heating and separating the active material Li x CoO 2 to obtain black powder; black powder dispersed in nitric acid solution or hydrochloric acid solution, filtered to obtain nitrate solution or chloride solution containing Co 2+ , Li + ions; add NH 3 ·H to the acidic leaching solution containing Co 2+ , Li + ions 2 O to form a blue precipitate, and at the same time add a surfactant and LiOH to adjust the concentration of Li + ions in the suspension; filter and dry the precipitate in the suspension, and roast it at a temperature of 600-900°C, that is Li x CoO 2 powder is obtained. The present invention can recover at least 95% of cobalt and at least 93% of lithium from waste lithium-ion batteries to prepare Li x CoO 2 powder with a particle size of 0.2-1.0 μm and a specific surface area of 2.0-6.0 m 2 ·g -1 .

Figure 200510015078

Description

从废旧的锂离子电池中回收制备LixCoO2的方法 Reclaim and prepare LixCoO2 method from waste lithium-ion batteries

技术领域technical field

本发明涉及一种从报废的锂离子电池中回收制备LixCoO2的方法,属于化学分离和无机粉体的制备技术。特别是,该技术所涉及的工艺是一种液相包覆沉淀复合粉体制备工艺。The invention relates to a method for recovering and preparing LixCoO2 from discarded lithium ion batteries, which belongs to the technology of chemical separation and preparation of inorganic powder. In particular, the process involved in this technology is a liquid-phase coating precipitation composite powder preparation process.

背景技术Background technique

锂离子电池正极材料是由活性材料LiCoO2、碳黑和乙炔黑、粘结剂按一定的比例粘附在铝箔上的,正极材料各部分的含量如表1所示:The positive electrode material of lithium ion battery is made of active material LiCoO 2 , carbon black, acetylene black, and binder adhered to the aluminum foil in a certain proportion. The content of each part of the positive electrode material is shown in Table 1:

表1锂离子电池正极材料的成分Table 1 Composition of cathode materials for lithium-ion batteries

物质 substance LiCoO2 LiCoO2  碳黑、乙炔黑 carbon black, acetylene black  粘结剂 Binder  铝箔 aluminum foil 含量(wt.%) Content (wt.%) 76.80 76.80  9.03 9.03  4.52 4.52  9.65 9.65

报废的锂离子电池的处理通常面临以下问题:一是在报废的锂离子电池的正负极的表面通常会含有少量的单质锂,由于单质状态的金属锂具有很强的易燃易爆性,这是电池处理中需要特别注意的安全问题;另外,钴是重金属,如果处理不当就会对环境造成危害。因此报废的锂离子电池的合理处置,对于保护环境具有重要的意义。The disposal of scrapped lithium-ion batteries usually faces the following problems: First, the surface of the positive and negative electrodes of scrapped lithium-ion batteries usually contains a small amount of elemental lithium. Since metal lithium in the elemental state is highly flammable and explosive, This is a safety issue that requires special attention in battery disposal; in addition, cobalt is a heavy metal that can be harmful to the environment if not handled properly. Therefore, the reasonable disposal of scrap lithium-ion batteries is of great significance to protect the environment.

在国外关于锂离子二次电池回收的研究工作中,比较有代表性的技术是日本索尼公司已和住友金属矿山公司合作研究开发的从废旧锂离子二次电池中回收钴等的技术,其工艺为先将电池焚烧以除去有机物,再筛选,去铁和铜后,将残余粉加热并溶于酸中,用有机溶剂萃取便可提出氧化钴,该产品可作为原料用于颜料、涂料工业中。然而以上方法还存在一定不足:首先,采用焚烧除去有机物的方法、需配套烟气净化设备,否则易引起大气环境污染;另外,在加热的条件下,以盐酸溶解“残余粉”,对设备防腐要求很高、操作环境恶劣。In foreign research work on the recovery of lithium-ion secondary batteries, the more representative technology is the technology of recovering cobalt from waste lithium-ion secondary batteries, which has been jointly researched and developed by Sony Corporation of Japan and Sumitomo Metal Mining Corporation. Incinerate the battery first to remove organic matter, then screen, remove iron and copper, heat the residual powder and dissolve it in acid, and extract it with an organic solvent to extract cobalt oxide. This product can be used as a raw material for pigments and coatings industries. . However, the above methods still have certain deficiencies: First, the method of incineration to remove organic matter needs to be equipped with flue gas purification equipment, otherwise it will easily cause air pollution; in addition, under the condition of heating, the "residual powder" is dissolved with hydrochloric acid to prevent corrosion of the equipment The requirements are high and the operating environment is harsh.

采用化学浸取法回收处理废旧锂离子电池的方法还有:日本专利JP 11185834提出的方法,其特征为以盐酸溶蚀电池的正极材料,采用草酸根为沉淀剂,以所形成的草酸钴沉淀为回收产物;日本专利JP 11054159提出的方法是以硝酸溶蚀正极材料,以氢氧化锂调整酸碱值,以金属钴的氢氧化物为回收产物;中国专利CN 1402376A提出的方法是,以含有氯化钠的盐酸水溶液溶蚀废锂离子电池There are also methods for recycling waste lithium-ion batteries by chemical leaching: the method proposed by Japanese Patent JP 11185834, which is characterized in that the positive electrode material of the battery is eroded with hydrochloric acid, oxalate is used as a precipitant, and the formed cobalt oxalate precipitate is used as a recovery method. Product; the method proposed in Japanese Patent JP 11054159 is to corrode the positive electrode material with nitric acid, adjust the pH value with lithium hydroxide, and take the hydroxide of metal cobalt as the recovery product; the method proposed in Chinese Patent CN 1402376A is to contain sodium chloride Aqueous hydrochloric acid solution dissolves spent lithium-ion batteries

发明内容Contents of the invention

本发明目的在于提供一种从报废的锂离子电池中回收制备LixCoO2的方法。以该方法制备的LixCoO2粉体比表面积高,具有R3m空间群结构的六方晶系的层状结构晶体。The purpose of the present invention is to provide a method for recovering and preparing Li x CoO 2 from discarded lithium ion batteries. The Li x CoO 2 powder prepared by the method has a high specific surface area and a hexagonal layered structure crystal with an R3m space group structure.

本发明是通过以下技术方案加以实现的,一种从报废的锂离子电池中回收制备LixCoO2的方法(式中X=0.95~1.05),其特征在于包括以下步骤:The present invention is achieved through the following technical solutions, a method of reclaiming and preparing Li x CoO from discarded lithium ion batteries (X=0.95~1.05 in the formula), which is characterized in that it comprises the following steps:

(1)电池的切割(1) Cutting of battery

将电池在水中切割开,使正极材料和其它部件分离,并将正极材料剪成小碎片;Cut the battery in water to separate the positive electrode material from other components, and cut the positive electrode material into small pieces;

(2)将剪成的正极板碎片浸泡在N-甲基-2-吡咯烷酮(NMP)液体中,每1kg正极碎片需要NMP 1.5~2.0L,加热该液体到85~100℃,经过15~30分钟,即可以使粘附在铝箔上的正极活性物质LixCoO2和碳黑脱落到液体中,取出铝箔,过滤,并回收NMP循环利用,用清水清洗滤出的粉体,经过滤、干燥即可得到黑色粉末;(2) Soak the cut positive plate fragments in N-methyl-2-pyrrolidone (NMP) liquid, 1.5~2.0L of NMP is needed for every 1kg of positive electrode fragments, heat the liquid to 85~100℃, and after 15~30 Minutes, the positive electrode active material Li x CoO 2 and carbon black adhering to the aluminum foil can fall off into the liquid, take out the aluminum foil, filter, and recover NMP for recycling, wash the filtered powder with water, filter and dry A black powder can be obtained;

(3)把所得到的黑色粉末分散在质量浓度10~30%的硝酸溶液或质量浓度10~30%盐酸溶液中,每0.1~0.5kg粉末需要硝酸溶液或盐酸溶液1~1.5L,并向该溶液中滴加10~50ml质量浓度为1~5%的过氧化氢溶液,搅拌约40分钟,过滤得到含有Co2+、Li+离子的硝酸盐溶液或氯化物溶液;通过准确称量所得到的碳黑的量,可以计算出溶液中的Co2+、Li+离子的浓度,也可以通过EDTA滴定法测定出溶液中的Co2+离子的浓度,通过氟离子选择电极法测定溶液中的Li+离子的浓度;(3) Disperse the obtained black powder in nitric acid solution of mass concentration 10~30% or mass concentration 10~30% hydrochloric acid solution, every 0.1~0.5kg powder needs nitric acid solution or hydrochloric acid solution 1~1.5L, and add to Add 10-50ml of hydrogen peroxide solution with a mass concentration of 1-5% dropwise into the solution, stir for about 40 minutes, and filter to obtain a nitrate solution or chloride solution containing Co2 + and Li + ions; by accurately weighing the The amount of carbon black obtained can calculate the concentration of Co 2+ and Li + ions in the solution, and can also measure the concentration of Co 2+ ions in the solution by EDTA titration, and measure the concentration of Co 2+ ions in the solution by the fluoride ion selective electrode method. concentration of Li + ions;

(4)室温下,向步骤(3)制备的含有Co2+、Li+离子的酸性浸取溶液中缓慢加入NH3·H2O,调整并控制溶液的pH为8~11,形成蓝色沉淀,同时加入以下的表面活性剂之一:聚丙烯酸(PAA),聚乙二醇(PEG),聚甲基丙烯酸(PMAA),聚乙烯亚胺(PEI),加入量为原始黑色粉末的质量的1~5%,持续搅拌8~12小时;(4) At room temperature, slowly add NH 3 ·H 2 O to the acidic leaching solution containing Co 2+ and Li + ions prepared in step (3), adjust and control the pH of the solution to 8-11, and form a blue color Precipitation, while adding one of the following surfactants: polyacrylic acid (PAA), polyethylene glycol (PEG), polymethacrylic acid (PMAA), polyethyleneimine (PEI), the amount added is the quality of the original black powder 1% to 5% of the concentration, keep stirring for 8 to 12 hours;

(5)水浴加热步骤(4)溶液到80~95℃,通过补加LiOH调整悬浮液中的Li+离子的浓度,并使摩尔比Li∶Co=1~1.10∶1;在强力搅拌的同时,向该悬浮液中滴加浓度为2~5mol/L的NH4HCO3溶液,加入量为使NH4HCO3的摩尔数大于溶液中的Li+的摩尔数的1.6~2倍,持续搅拌2~4小时;(5) water bath heating step (4) solution to 80~95 ℃, adjust the concentration of Li + ions in the suspension by adding LiOH, and make the molar ratio Li: Co=1~1.10: 1; While vigorously stirring , add dropwise a NH 4 HCO 3 solution with a concentration of 2 to 5 mol/L in the suspension, the amount added is to make the molar number of NH 4 HCO 3 greater than 1.6 to 2 times the molar number of Li + in the solution, and keep stirring 2 to 4 hours;

(6)将步骤(5)的悬浮液中的沉淀物过滤并干燥,在600~900℃的温度下焙烧7~12小时,即得到LixCoO2粉体。(6) Filter and dry the precipitate in the suspension in step (5), and calcinate at a temperature of 600-900° C. for 7-12 hours to obtain Li x CoO 2 powder.

采用上述方法可以从废旧的锂离子电池中回收至少95%的钴和至少93%的锂;可以制备出粒径约0.2~1.0μm、比表面积为2.0~6.0m2·g-1的LixCoO2粉体。Using the above method, at least 95% of cobalt and at least 93% of lithium can be recovered from waste lithium-ion batteries; Li x with a particle size of about 0.2-1.0 μm and a specific surface area of 2.0-6.0 m 2 ·g -1 can be prepared CoO 2 powder.

附图说明Description of drawings

图1为本发明实施例1制得LixCoO2粉体的X射线衍射谱图。Fig. 1 is an X-ray diffraction spectrum of Li x CoO 2 powder prepared in Example 1 of the present invention.

图2为本发明实施例2制得LixCoO2粉体的X射线衍射谱图。Fig. 2 is an X-ray diffraction spectrum of Li x CoO 2 powder prepared in Example 2 of the present invention.

具体实施方式Detailed ways

例1.example 1.

取各种型号的锂离子电池,在水中把电池切开,使正极材料和其它部件分离,称取150g正极板,将正极板剪为小于2cm×2cm大小的碎片,在室温下,把这些碎片放入300ml的N-甲基-2-吡咯烷酮(NMP)液体中,加热该液体到85℃,经过30分钟,即可以使粘附在铝箔上的所有粉体物质(包括正极活性物质LixCoO2和碳黑)脱落到液体中,取出铝箔,过滤液体并回收NMP(可循环利用),用清水清洗滤出的粉体,干燥得到127g(理论值应为128.7g)黑色粉末;把所得到的黑色粉末放入1.4L浓度为15%(wt.)的硝酸溶液中,并在搅拌的同时向该溶液中滴加浓度为5%(wt.)的H2O2溶液0.18L,继续搅拌约40分钟,过滤得到含有Co2+、Li+离子的硝酸盐溶液,通过EDTA滴定法测定出溶液中的钴的质量为65.90g(理论值为69.36g),钴的浸取率为95.05%,通过氟离子选择电极法测定溶液中的锂的质量为7.76g(理论值为8.23g),锂的浸取率为94.34%,溶液中的金属离子的mol比为Li+∶Co2+=0.95∶1;在上述溶液中缓慢加入NH3·H2O,调整并控制pH为9,形成蓝色沉淀,同时加入分子量为1000的聚乙二醇2.5g,持续搅拌10小时,水浴加热上述悬浮液体至90℃,向该悬浮液中补加0.12molLiOH,在强力搅拌的同时,滴加370ml浓度为3mol/L的NH4HCO3溶液,持续搅拌3小时,将悬浮液中的沉淀物过滤并干燥,从而得到合成产物的前驱体粉体,将该前驱体在700℃的温度下焙烧8小时,即得到晶粒尺度小于1μm的LixCoO2粉体。所得粉体的晶相分析如图1的X射线衍射图所示,粉体的晶格参数如表2所示,表明所制备的LixCoO2粉体具有规则的六方晶系层状结构;采用氮气BET多层吸附法测定的样品1的粉体的比表面积为7.95m2·g-1;所制备的LixCoO2的一次放电容量为142mAh·g-1Take various types of lithium-ion batteries, cut the battery in water, separate the positive electrode material from other components, weigh 150g of the positive plate, cut the positive plate into pieces smaller than 2cm×2cm, and put these pieces at room temperature Put into 300ml of N-methyl-2-pyrrolidone (NMP) liquid, heat the liquid to 85°C, and after 30 minutes, all the powder substances (including the positive electrode active material Li x CoO) adhered on the aluminum foil can be made 2 and carbon black) fall off into the liquid, take out the aluminum foil, filter the liquid and reclaim NMP (recyclable), wash the filtered powder with clear water, dry to obtain 127g (theoretical value should be 128.7g) black powder; Put the black powder into 1.4L concentration of 15% (wt.) nitric acid solution, and while stirring, dropwise add concentration of 5% (wt.) H 2 O 2 solution 0.18L in this solution, continue to stir About 40 minutes, filter to obtain the nitrate solution containing Co2+ , Li + ions, the quality of the cobalt in the solution measured by EDTA titration is 65.90g (theoretical value is 69.36g), and the leaching rate of cobalt is 95.05% , the mass of lithium in the solution measured by the fluoride ion selective electrode method is 7.76g (theoretical value is 8.23g), the leaching rate of lithium is 94.34%, and the mol ratio of the metal ion in the solution is Li + : Co 2+ = 0.95:1; slowly add NH 3 ·H 2 O to the above solution, adjust and control the pH to 9, and form a blue precipitate, at the same time add 2.5 g of polyethylene glycol with a molecular weight of 1000, continue stirring for 10 hours, and heat the above solution in a water bath Suspend the liquid to 90°C, add 0.12mol LiOH to the suspension, add dropwise 370ml of NH 4 HCO 3 solution with a concentration of 3 mol/L while stirring vigorously, keep stirring for 3 hours, and filter the precipitate in the suspension and drying to obtain a precursor powder of the synthesized product, which is calcined at a temperature of 700° C. for 8 hours to obtain a Li x CoO 2 powder with a grain size of less than 1 μm. The crystal phase analysis of the obtained powder is shown in the X-ray diffraction diagram of Figure 1, and the lattice parameters of the powder are shown in Table 2, indicating that the prepared Li x CoO The powder has a regular hexagonal layered structure; The specific surface area of the powder of sample 1 measured by nitrogen BET multilayer adsorption method was 7.95m 2 ·g -1 ; the primary discharge capacity of the prepared Li x CoO 2 was 142mAh·g -1 .

表2不同样品LixCoO2的晶格参数,粉体的比表面积以及放电容量Table 2 The lattice parameters of different samples Li x CoO 2 , the specific surface area of the powder and the discharge capacity

样品sample a()a (A) c()c(A) c/ac/a I(003)/I(104) I (003) /I (104)   比表面积(m2·g-1)Specific surface area (m 2 ·g -1 )    放电容量(mAh·g-1)Discharge capacity (mAh·g -1 )     样品1 Sample 1   2.8158 2.8158   14.0484 14.0484   4.9904 4.9904   2.5316 2.5316   7.95 7.95     142 142     样品2 Sample 2   2.8167 2.8167   14.0783 14.0783   4.9989 4.9989   1.9081 1.9081   5.12 5.12     147 147

例2.Example 2.

采用与例1相同的工艺制备合成产物的前驱体,将该前驱体在800℃的温度下焙烧8小时,即得到晶粒尺度小于1μm的LixCoO2粉体。所得粉体的晶相分析如图2的X射线衍射图所示,粉体的晶格参数如表2所示,表明所制备的LixCoO2粉体具有规则的六方晶系层状结构;采用氮气BET多层吸附法测定的样品1的粉体的比表面积为5.12m2·g-1;所制备的LixCoO2的一次放电容量为147mAh·g-1The precursor of the synthesized product was prepared by the same process as in Example 1, and the precursor was calcined at a temperature of 800°C for 8 hours to obtain a Li x CoO 2 powder with a grain size of less than 1 μm. The crystal phase analysis of the obtained powder is shown in the X-ray diffraction diagram of Figure 2, and the lattice parameters of the powder are shown in Table 2, indicating that the prepared Li x CoO The powder has a regular hexagonal layered structure; The specific surface area of the powder of sample 1 measured by nitrogen BET multilayer adsorption method was 5.12m 2 ·g -1 ; the primary discharge capacity of the prepared Li x CoO 2 was 147mAh·g -1 .

Claims (1)

1.一种从报废的锂离子电池中回收制备LixCoO2的方法,式中x=0.95~1.05,其特征在于包括以下步骤:1. a kind of reclaims and prepares Li x CoO from discarded lithium ion battery The method, x=0.95~1.05 in the formula, it is characterized in that comprising the following steps: (1)将电池在水中切割开,使正极材料和其它部件分离,并将正极材料剪成小碎片;(1) Cut the battery in water to separate the positive electrode material from other components, and cut the positive electrode material into small pieces; (2)将剪成的正极板碎片浸泡在N-甲基-2-吡咯烷酮液体中,每1kg正极碎片需要N-甲基-2-吡咯烷酮1.5~2.0L,加热该液体到85~100℃,经过15~30分钟,即可以使粘附在铝箔上的正极活性物质LixCoO2和碳黑脱落到液体中,取出铝箔,过滤,并回收N-甲基-2-吡咯烷酮循环利用,用清水清洗滤出的粉体,经过滤、干燥即可得到黑色粉末;(2) Soak the cut positive plate fragments in N-methyl-2-pyrrolidone liquid, 1.5-2.0L of N-methyl-2-pyrrolidone is needed for each 1kg of positive electrode fragments, heat the liquid to 85-100°C, After 15 to 30 minutes, the positive electrode active material Li x CoO 2 and carbon black adhering to the aluminum foil can fall off into the liquid, take out the aluminum foil, filter, and recover N-methyl-2-pyrrolidone for recycling. Wash the filtered powder, filter and dry to obtain black powder; (3)把所得到的黑色粉末分散在质量浓度10~30%的硝酸溶液或质量浓度10~30%的盐酸溶液中,每0.1~0.5kg粉末需要硝酸溶液或盐酸溶液1~1.5L,并向该溶液中滴加10~50ml质量浓度为1~5%的过氧化氢溶液,搅拌40分钟,过滤得到含有Co2+、Li+离子的硝酸盐溶液或氯化物溶液;通过EDTA滴定法测定出溶液中的Co2+离子的浓度,通过氟离子选择电极法测定溶液中的Li+离子的浓度;(3) Disperse the obtained black powder in a nitric acid solution with a mass concentration of 10-30% or a hydrochloric acid solution with a mass concentration of 10-30%. Every 0.1-0.5kg of powder requires 1-1.5L of nitric acid solution or hydrochloric acid solution, and Add dropwise 10~50ml mass concentration of 1~5% hydrogen peroxide solution in this solution, stir for 40 minutes, filter to obtain nitrate solution or chloride solution containing Co 2+ , Li + ions; measure by EDTA titration The concentration of the Co ion in the solution is determined, and the concentration of the Li ion in the solution is measured by the fluoride ion selective electrode method; (4)室温下,向步骤(3)制备的含有Co2+、Li+离子的酸性浸取溶液中缓慢加入NH3·H2O,调整并控制溶液的pH为8~11,形成蓝色沉淀,同时加入以下的表面活性剂之一:(4) At room temperature, slowly add NH 3 ·H 2 O to the acidic leaching solution containing Co 2+ and Li + ions prepared in step (3), adjust and control the pH of the solution to 8-11, and form a blue color Precipitation, while adding one of the following surfactants: 聚丙烯酸,聚乙二醇,聚甲基丙烯酸或聚乙烯亚胺,加入量为原始黑色粉末的质量含量的1~5%,持续搅拌8~12小时;Polyacrylic acid, polyethylene glycol, polymethacrylic acid or polyethyleneimine, the addition amount is 1-5% of the mass content of the original black powder, and the stirring is continued for 8-12 hours; (5)水浴加热步骤(4)溶液到80~95℃,通过补加LiOH调整悬浮液中的Li+离子的浓度,并使摩尔比Li∶Co=(1~1.10)∶1;在强力搅拌的同时,向该悬浮液中滴加浓度为2~5mol/L的NH4HCO3溶液,加入量为使NH4HCO3的摩尔数大于溶液中的Li+的摩尔数的1.6~2倍,持续搅拌2~4小时;(5) water bath heating step (4) solution to 80~95 ℃, adjust the concentration of Li ion in the suspension by adding LiOH, and make molar ratio Li : Co=(1~1.10): 1; At the same time, in the suspension, dropwise add a concentration of 2 to 5 mol/L NH 4 HCO 3 solution, the amount added is to make the molar number of NH 4 HCO 3 greater than 1.6 to 2 times the molar number of Li + in the solution, Keep stirring for 2-4 hours; (6)将步骤(5)的悬浮液中的沉淀物过滤并干燥,在600~900℃的温度下焙烧7~12小时,即得到LixCoO2粉体。(6) Filter and dry the precipitate in the suspension in step (5), and calcinate at a temperature of 600-900° C. for 7-12 hours to obtain Li x CoO 2 powder.
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CN102412430B (en) * 2011-11-14 2014-02-26 佛山市邦普循环科技有限公司 Chemical separating method for aluminum foil in waste lithium ion battery positive plate
CN103224257A (en) * 2012-11-28 2013-07-31 江苏大学 A method for preparing Co3O4 from waste lithium-ion batteries
CN104953200B (en) * 2015-06-30 2017-06-23 哈尔滨工业大学 Battery-grade iron phosphate and the method that lithium iron phosphate positive material is prepared using waste lithium iron phosphate battery are reclaimed in ferric phosphate lithium cell
CN106058353B (en) * 2016-08-11 2018-05-25 荆门市格林美新材料有限公司 The reparative regeneration method of old and useless battery positive electrode
CN110144460A (en) * 2019-04-28 2019-08-20 北京点域科技有限公司 The leaching and recovery process of metal in a kind of lithium ion cell anode waste
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