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CN108360022A - A kind of method that melten salt electriochemistry method recycles cobalt element in anode material of lithium battery - Google Patents

A kind of method that melten salt electriochemistry method recycles cobalt element in anode material of lithium battery Download PDF

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CN108360022A
CN108360022A CN201810410276.5A CN201810410276A CN108360022A CN 108360022 A CN108360022 A CN 108360022A CN 201810410276 A CN201810410276 A CN 201810410276A CN 108360022 A CN108360022 A CN 108360022A
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lithium battery
cathode
cobalt
anode material
salt
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尹华意
曲鑫
宁志强
宋秋实
谢宏伟
周先波
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Northeastern University China
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C3/00Electrolytic production, recovery or refining of metals by electrolysis of melts
    • C25C3/34Electrolytic production, recovery or refining of metals by electrolysis of melts of metals not provided for in groups C25C3/02 - C25C3/32
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B23/00Obtaining nickel or cobalt
    • C22B23/04Obtaining nickel or cobalt by wet processes
    • C22B23/0407Leaching processes
    • C22B23/0415Leaching processes with acids or salt solutions except ammonium salts solutions
    • C22B23/043Sulfurated acids or salts thereof
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B7/00Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
    • C22B7/006Wet processes
    • C22B7/007Wet processes by acid leaching
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C7/00Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells
    • C25C7/02Electrodes; Connections thereof
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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Abstract

一种熔盐电化学法回收锂电池正极材料中钴元素的方法,属于过渡金属元素回收与再利用技术领域。该方法为:1)将锂电池进行放电拆解,将正极材料粉碎,加入浸出液,50~80℃搅拌10~60min,过滤;2)向滤液中滴加NaOH水溶液,pH为4.7~8时,过滤;向一次滤液中滴加NaOH水溶液,pH为9.2~10.0时,抽滤,得到沉淀,干燥、研磨,压片,灼烧,得到电极压片;3)用泡沫镍包裹氧化钴电极压片与钼丝连接为阴极,石墨棒与不锈钢丝连接为阳极;4)将熔盐原料加热至熔化温度,阴极和阳极插入熔盐中,施加电压,电解后,阴极取出,冷却,超声波振荡清洗,得到钴。采用本方法回收废旧锂电池正极材料中的钴元素具有低成本、高效,操作简单的优点。The invention discloses a method for recovering cobalt element in lithium battery cathode material by molten salt electrochemical method, which belongs to the technical field of transition metal element recovery and reuse. The method is as follows: 1) disassemble the lithium battery after discharge, crush the positive electrode material, add the leachate, stir at 50-80°C for 10-60 minutes, and filter; 2) add NaOH aqueous solution dropwise to the filtrate, when the pH is 4.7-8, Filtration; add NaOH aqueous solution dropwise to the primary filtrate, when the pH is 9.2 to 10.0, filter with suction to obtain a precipitate, dry, grind, press, and burn to obtain an electrode tablet; 3) Wrap the cobalt oxide electrode tablet with foamed nickel The cathode is connected with the molybdenum wire, and the anode is connected with the graphite rod and the stainless steel wire; 4) The molten salt raw material is heated to the melting temperature, the cathode and the anode are inserted into the molten salt, a voltage is applied, and after electrolysis, the cathode is taken out, cooled, and cleaned by ultrasonic oscillation. Get cobalt. The method for recovering the cobalt element in the positive electrode material of the waste lithium battery has the advantages of low cost, high efficiency and simple operation.

Description

一种熔盐电化学法回收锂电池正极材料中钴元素的方法A method for recovering cobalt element in lithium battery positive electrode material by molten salt electrochemical method

技术领域technical field

本发明涉及废旧锂电池中正极材料中过渡金属元素回收与再利用技术领域,具体涉及一种熔盐电化学法回收锂电池正极材料中钴元素的方法。The invention relates to the technical field of recovery and reuse of transition metal elements in positive electrode materials in waste lithium batteries, in particular to a method for recovering cobalt elements in lithium battery positive electrode materials by a molten salt electrochemical method.

背景技术Background technique

与传统电池技术相比,锂电池充电更快,使用更持久,因此,锂离子电池的应用前景十分广阔。根据相关统计,移动电话使用的电池中锂离子电池至少占70%以上,2015年全球手机用户已经超过52亿,今后的用户数量还将继续扩大,而且随着平板电脑等高科技产品的问世和普及,锂离子电池的应用还将具有更大的潜在市场。另外电动汽车的保有量不断增加,对锂电池的需求还会持续增长。随着锂电池的大量使用,电池的回收刻不容缓。钴是构成锂电池正极材料的一种重要稀缺元素,对其进行高效回收利用不但可以避免资源的浪费,同时可以减少其对环境的污染及危害,符合可持续发展的要求。结合全球钴资源的储存情况,充分利用钴资源是电池可持续发展的必需。现有的在溶液中通过电解回收电池正极材料中的镍、锰、钴等金属元素的工艺方法,在实际操作时会产生大量含有重金属离子的废水,对环境造成污染,而在熔盐环境中实现电解则对环境更加友好。Compared with traditional battery technology, lithium batteries charge faster and last longer, so lithium-ion batteries have a bright future. According to relevant statistics, lithium-ion batteries account for at least 70% of the batteries used in mobile phones. In 2015, the global mobile phone users have exceeded 5.2 billion, and the number of users will continue to expand in the future. With the advent of high-tech products such as tablet computers and Popularity, the application of lithium-ion batteries will also have a larger potential market. In addition, the number of electric vehicles continues to increase, and the demand for lithium batteries will continue to grow. With the extensive use of lithium batteries, the recycling of batteries is urgent. Cobalt is an important scarce element that constitutes the cathode material of lithium batteries. Efficient recycling of cobalt can not only avoid the waste of resources, but also reduce its pollution and harm to the environment, which meets the requirements of sustainable development. Combined with the storage situation of global cobalt resources, making full use of cobalt resources is necessary for the sustainable development of batteries. The existing process of recovering metal elements such as nickel, manganese, and cobalt in the positive electrode material of the battery through electrolysis in the solution will produce a large amount of waste water containing heavy metal ions during actual operation, which will pollute the environment. The realization of electrolysis is more friendly to the environment.

发明内容Contents of the invention

本发明的目的是提供一种熔盐电化学法回收锂电池正极材料中钴元素的方法,将通过回收电池制取的氧化钴与泡沫镍集流体包裹与钼丝连接制成阴极、石墨棒与不锈钢丝集流体连接制成阳极电解得到金属钴,在氯化物或者碳酸熔盐中,高温下(具体温度根据熔盐组成而定),施加电压电解一段时间使氧化钴被还原得到金属钴,将构件提离熔盐冷却、水中超声波震荡清洗除去盐、吹干,实现在熔盐环境中电解、回收钴。采用本发明的方法回收废旧锂电池正极材料中的钴元素具有低成本、高效,操作简单的优点。The purpose of the present invention is to provide a method for recycling the cobalt element in the positive electrode material of the lithium battery by the molten salt electrochemical method. The cobalt oxide produced by recycling the battery is wrapped with the foamed nickel current collector and connected with the molybdenum wire to form a cathode, a graphite rod and a molybdenum wire. The stainless steel wire current collector is connected to make anode electrolysis to obtain metal cobalt. In chloride or carbonate molten salt, at high temperature (the specific temperature depends on the composition of the molten salt), apply voltage for electrolysis for a period of time to reduce cobalt oxide to obtain metal cobalt. The component is lifted from the molten salt for cooling, ultrasonically oscillated in water to remove the salt, and dried to realize electrolysis and recovery of cobalt in the molten salt environment. Adopting the method of the invention to recover the cobalt element in the positive electrode material of the waste lithium battery has the advantages of low cost, high efficiency and simple operation.

本发明的一种熔盐电化学法回收锂电池正极材料中钴元素的方法,按以下步骤进行:A kind of molten salt electrochemical method of the present invention reclaims the method for cobalt element in lithium battery cathode material, carries out according to the following steps:

步骤1:锂电池正极材料的溶解Step 1: Dissolution of Lithium Battery Cathode Material

(1)将锂电池进行放电处理后,进行拆解,分离得到锂电池正极材料和负极材料;(1) After the lithium battery is discharged, it is disassembled and separated to obtain the positive electrode material and the negative electrode material of the lithium battery;

(2)将锂电池正极材料粉碎后,加入浸出液,在50~80℃恒温加热10~60min,同时伴随搅拌,得到浸出混合液;(2) After pulverizing the positive electrode material of the lithium battery, add the leaching solution, and heat at a constant temperature of 50-80°C for 10-60 minutes while stirring to obtain a leaching mixture;

其中,按固液比,锂电池正极材料:浸出液=(0.5~1)g:(5~20)mL;Among them, according to the solid-liquid ratio, lithium battery positive electrode material: leachate = (0.5 ~ 1) g: (5 ~ 20) mL;

浸出液为摩尔浓度为2~6mol/L的H2SO4和体积百分数为20~40%的H2O2的混合水溶液,按体积比,摩尔浓度为2~6mol/L H2SO4:体积百分数为20~40%的H2O2=(3~5):1;The leaching solution is a mixed aqueous solution of H2SO4 with a molar concentration of 2-6mol /L and H2O2 with a volume percentage of 20-40%. According to the volume ratio, the molar concentration is 2-6mol / LH2SO4 : volume percentage 20-40% H 2 O 2 =(3-5):1;

(3)将浸出混合液进行过滤,得到滤液;(3) filtering the leaching mixture to obtain a filtrate;

步骤2:氧化钴电极压片的制备Step 2: Preparation of cobalt oxide electrode pellets

(1)向滤液中滴加摩尔浓度为1~3mol/L的NaOH水溶液,当pH值为4.7~8时,有Fe、Al形成的沉淀析出,过滤,去除Fe、Al形成的沉淀,得到一次滤液;(1) Add dropwise an aqueous NaOH solution with a molar concentration of 1 to 3 mol/L in the filtrate. When the pH value is 4.7 to 8, precipitates formed by Fe and Al will precipitate out. Filter to remove the precipitates formed by Fe and Al to obtain a filtrate;

(2)向一次滤液中继续滴加摩尔浓度为1~3mol/L的NaOH水溶液,当pH值为9.2~10.0时,Co形成的沉淀析出,进行抽滤,得到Co(OH)2沉淀;(2) In the primary filtrate, continue to dropwise add the NaOH aqueous solution whose molar concentration is 1~3mol/L, when the pH value is 9.2~10.0, the precipitate formed by Co is separated out, and suction filtration is carried out to obtain Co(OH) Precipitate ;

(3)将Co(OH)2沉淀干燥,研磨成粉末,压片,在空气中灼烧,得到氧化钴电极压片;(3) Co(OH) 2 is precipitated and dried, ground into powder, pressed into tablets, and burned in air to obtain cobalt oxide electrode tablets;

步骤3:电化学准备Step 3: Electrochemical Preparation

用泡沫镍集流体包裹氧化钴电极压片,然后与钼丝连接作为阴极,石墨棒与不锈钢丝集流体连接作为阳极;Wrap the cobalt oxide electrode sheet with a nickel foam current collector, and then connect it with a molybdenum wire as a cathode, and connect a graphite rod with a stainless steel wire collector as an anode;

将熔盐原料烘干去除水分,置于坩埚中,再将坩埚放入反应器中,阴极和阳极悬吊在熔盐原料上方,封闭反应器,向反应器中持续通入氩气,形成氩气气氛;Dry the molten salt raw material to remove moisture, place it in a crucible, then put the crucible into the reactor, hang the cathode and anode above the molten salt raw material, close the reactor, and continuously feed argon gas into the reactor to form argon gas atmosphere;

步骤4:电解Step 4: Electrolysis

(1)将熔盐原料加热至熔化温度形成熔盐,阴极和阳极插入熔盐中,构成两电极体系,在两电极中施加电压,进行电解,电解完成后,将电解后的阴极取出,冷却,并插入另一个阴极施加电压继续进行电解;其中,阴极和阳极的水平间距为15±5mm,施加电压为2.0~2.1V,电解时间为8~12h;(1) Heat the molten salt raw material to the melting temperature to form a molten salt. Insert the cathode and anode into the molten salt to form a two-electrode system. Apply voltage to the two electrodes to perform electrolysis. After the electrolysis is completed, take out the electrolyzed cathode and cool it down. , and insert another cathode to apply voltage to continue electrolysis; wherein, the horizontal distance between cathode and anode is 15±5mm, the applied voltage is 2.0-2.1V, and the electrolysis time is 8-12h;

(2)将冷却的电解后的阴极,放入水中,超声波振荡清洗,去除阴极表面附着的盐,得到的阴极即为钴。(2) Put the cooled cathode after electrolysis into water, and clean it with ultrasonic vibration to remove the salt attached to the surface of the cathode, and the obtained cathode is cobalt.

所述的步骤1的(1)中,所述的放电处理,具体为:使用充放电仪进行放电处理,恒流放电3A,放电时间≥30min。In (1) of the above-mentioned step 1, the discharge treatment specifically includes: using a charge-discharge instrument to perform discharge treatment, discharge at a constant current of 3A, and discharge time ≥ 30min.

所述的步骤1的(2)中,所述的锂电池正极材料粉碎,粉碎后,锂电池正极材料的粒度为D97。In (2) of the step 1, the lithium battery cathode material is pulverized, and after pulverization, the particle size of the lithium battery cathode material is D97.

所述的步骤2的(3)中,所述的干燥为在90~100℃下,在空气中干燥500~600min。In (3) of the step 2, the drying is at 90-100° C. for 500-600 minutes in air.

所述的步骤2的(3)中,所述的研磨为,得到粒径为0.10~0.20mm的Co(OH)2粉末。In (3) of the step 2, the grinding is to obtain Co(OH) 2 powder with a particle size of 0.10-0.20 mm.

所述的步骤2的(3)中,所述的压片为称量2.0g Co(OH)2粉末进行压制。In (3) of the step 2, the tableting is carried out by weighing 2.0g Co(OH) powder .

所述的步骤2的(3)中,所述的灼烧为在900~1000℃下在空气中灼烧1~24h。In (3) of step 2, the burning is burning in air at 900-1000° C. for 1-24 hours.

所述的步骤3中,所述的石墨棒还可以为SnO2陶瓷或Ni基合金。In the step 3, the graphite rods can also be SnO 2 ceramics or Ni-based alloys.

所述的步骤3中,所述的熔盐原料为氯化物熔盐原料、碳酸物熔盐原料、氢氧化物熔盐原料中的一种或几种混合;In the step 3, the molten salt raw material is one or a mixture of chloride molten salt raw materials, carbonate molten salt raw materials, and hydroxide molten salt raw materials;

当为氯化物熔盐原料时,具体为CaCl2,LiCl,NaCl,KCl,MgCl2,BaCl2中的一种或几种的混合熔盐;When it is a chloride molten salt raw material, it is specifically a mixed molten salt of one or more of CaCl 2 , LiCl, NaCl, KCl, MgCl 2 , and BaCl 2 ;

当为碳酸物熔盐原料时,具体为Li2CO3,Na2CO3,K2CO3,CaCO3中的一种或几种的混合熔盐;When it is a carbonate molten salt raw material, it is specifically a mixed molten salt of one or more of Li 2 CO 3 , Na 2 CO 3 , K 2 CO 3 , and CaCO 3 ;

当为氢氧化物熔盐原料时,具体为LiOH,NaOH,KOH中的一种或几种的混合熔盐。When it is a hydroxide molten salt raw material, it is specifically one or more mixed molten salts of LiOH, NaOH, and KOH.

所述的步骤3中,所述的氩气由反应器进气口通入,由反应器出气口排出,排出时,将熔盐产生的湿气带走。In the step 3, the argon gas is introduced through the inlet of the reactor and discharged from the gas outlet of the reactor. When discharged, the moisture generated by the molten salt is taken away.

所述的步骤4中,所述的超声波振荡清洗,清洗用水为5≤pH≤7的弱酸性清水。In the step 4, in the ultrasonic vibration cleaning, the cleaning water is weakly acidic water with 5≤pH≤7.

所述的步骤4中,所述的超声波振荡清洗,超声波频率为0.5kHZ~100kHZ。In the step 4, the ultrasonic vibration cleaning has an ultrasonic frequency of 0.5kHZ-100kHZ.

本发明的一种熔盐电化学法回收锂电池正极材料中钴元素的方法,其有益效果在于:A kind of molten salt electrochemical method of the present invention reclaims the method for cobalt element in lithium battery cathode material, and its beneficial effect is:

1、锂电池回收主要是回收锂电池正极材料中的镍、锰、钴等金属元素。本发明通过在熔盐中采用电化学方法回收锂电池正极材料中的钴元素。首先将电池正极材料中的钴以氢氧化物的形式(Co(OH)2)提取出来,随后将Co(OH)2灼烧制备氧化钴并进行压片并与泡沫镍集流体连接制成阴极、石墨棒与不锈钢丝集流体连接制成阳极在熔盐中电解得到金属钴。1. Lithium battery recycling is mainly to recover metal elements such as nickel, manganese, and cobalt in the positive electrode material of lithium batteries. The invention recovers the cobalt element in the positive electrode material of the lithium battery by adopting an electrochemical method in molten salt. Firstly, the cobalt in the positive electrode material of the battery is extracted in the form of hydroxide (Co(OH) 2 ), and then the Co(OH) 2 is burned to prepare cobalt oxide, which is pressed into tablets and connected with the foamed nickel current collector to make a cathode 1. Graphite rods are connected with stainless steel wire collectors to make anodes, and the metal cobalt is obtained by electrolysis in molten salt.

2、本发明将回收制取的氧化钴与泡沫镍、钼丝作为阴极,石墨棒与不锈钢丝集流体连接制成阳极,在熔盐环境中电解,在电解时阴极生成金属钴,阳极制得氧气或者二氧化碳,不会对环境产生危害,将为我国的锂电池回收提供助力。2. In the present invention, the reclaimed cobalt oxide, nickel foam and molybdenum wire are used as the cathode, and the graphite rod and the stainless steel wire collector are connected to form an anode, which is electrolyzed in a molten salt environment, and the cathode generates metallic cobalt during electrolysis, and the anode is made Oxygen or carbon dioxide will not harm the environment and will provide assistance for the recycling of lithium batteries in our country.

3、本技术发明具有低成本,易操作,对环境友好,可高效回收手机锂电池中的钴元素。3. The technical invention has low cost, easy operation, and environmental friendliness, and can efficiently recover the cobalt element in the lithium battery of the mobile phone.

附图说明Description of drawings

图1为本发明电解装置示意图。Figure 1 is a schematic diagram of the electrolysis device of the present invention.

具体实施方式Detailed ways

下面结合实施例对本发明作进一步的详细说明。The present invention will be described in further detail below in conjunction with embodiment.

以下实施例中,除非特殊说明,采用的设备和原料均为市购,纯度为分析纯及以上。In the following examples, unless otherwise specified, the equipment and raw materials used are commercially available, and the purity is analytically pure or above.

实施例1Example 1

一种熔盐电化学法回收锂电池正极材料中钴元素的方法,按以下步骤进行:A kind of molten salt electrochemical method reclaims the method for cobalt element in lithium battery cathode material, carries out according to the following steps:

步骤1:锂电池正极材料的溶解Step 1: Dissolution of Lithium Battery Cathode Material

(1)将回收得到的锂电池使用充放电仪进行放电处理,恒流放电3A,放电时间为30min,随后进行人工拆解电池,分离得到锂电池正极材料和负极材料;(1) Discharge the recovered lithium battery using a charge-discharge instrument, discharge at a constant current of 3A, and discharge for 30 minutes, then manually disassemble the battery to separate and obtain the positive and negative materials of the lithium battery;

(2)将锂电池正极材料粉碎后,加入浸出液,在70℃恒温加热30min,同时伴随搅拌,得到浸出混合液;其中,按固液比,锂电池正极材料:浸出液=1g:10mL;浸出液为摩尔浓度为4mol/L,H2SO4和体积百分数为30%的H2O2的混合液,按体积比,摩尔浓度为4mol/LH2SO4:体积百分数为30%的H2O2=5:1;(2) After crushing the positive electrode material of the lithium battery, add the leaching solution, heat at a constant temperature of 70°C for 30 minutes, and at the same time stir to obtain the leaching mixture; wherein, according to the solid-to-liquid ratio, the positive electrode material of the lithium battery: leaching solution = 1g: 10mL; the leaching solution is The molar concentration is 4mol/L, the mixed solution of H 2 SO 4 and 30% H 2 O 2 by volume, according to the volume ratio, the molar concentration is 4 mol/L H 2 SO 4 : 30% H 2 O 2 by volume =5:1;

(3)将浸出混合液进行过滤,得到滤液;(3) filtering the leaching mixture to obtain a filtrate;

步骤2:氧化钴电极压片的制备Step 2: Preparation of cobalt oxide electrode pellets

(1)向滤液中滴加摩尔浓度为2mol/L的NaOH水溶液,当pH值为6.47时,有Fe、Al形成的沉淀析出,过滤,去除Fe、Al形成的沉淀,得到一次滤液;(1) dripping the NaOH aqueous solution that molar concentration is 2mol/L in the filtrate, when pH value is 6.47, the precipitation that has Fe, Al formation is separated out, filters, and removes the precipitation that Fe, Al formation, obtains primary filtrate;

(2)向一次滤液中继续滴加摩尔浓度为2mol/L的NaOH水溶液,当pH值为10时,Co形成的沉淀析出,进行抽滤,得到Co(OH)2沉淀;(2) continue dripping the NaOH aqueous solution that molar concentration is 2mol/L in primary filtrate, when pH value is 10, the precipitation that Co forms is separated out, carries out suction filtration, obtains Co(OH) Precipitate ;

(3)将Co(OH)2沉淀在90℃下干燥560min,研磨成粒径为0.1mm粉末,取2.0gCo(OH)2粉末压片,在空气中,于1000℃灼烧5h,得到氧化钴电极压片;(3) Dry the Co(OH) 2 precipitate at 90°C for 560 minutes, grind it into a powder with a particle size of 0.1mm, take 2.0g of Co(OH) 2 powder, press it into tablets, and burn it at 1000°C for 5 hours in the air to obtain the oxidized Cobalt electrode pellets;

步骤3:电化学准备Step 3: Electrochemical Preparation

用泡沫镍集流体包裹氧化钴电极压片,然后与钼丝连接作为阴极,石墨棒与不锈钢丝集流体连接作为阳极;Wrap the cobalt oxide electrode sheet with a nickel foam current collector, and then connect it with a molybdenum wire as a cathode, and connect a graphite rod with a stainless steel wire collector as an anode;

将熔盐原料CaCl2烘干去除水分,置于坩埚中,再将坩埚放入反应器中,阴极和阳极悬吊在熔盐原料上方,封闭反应器,通过反应器上的进气口向反应器中持续通入氩气,出气口排出,在反应器内形成氩气气氛,其电解装置示意图见图1;Dry the molten salt raw material CaCl2 to remove moisture, place it in a crucible, then put the crucible into the reactor, hang the cathode and anode above the molten salt raw material, close the reactor, and feed the reactor through the air inlet on the reactor. The argon gas is continuously fed into the reactor, and the gas outlet is discharged to form an argon atmosphere in the reactor. The schematic diagram of the electrolysis device is shown in Figure 1;

步骤4:电解Step 4: Electrolysis

(1)将熔盐原料CaCl2加热至熔化温度形成熔盐,加热过程中产生的湿气被氩气带走;阴极和阳极插入熔盐中,构成两电极体系,在两电极中施加电压,进行电解,电解完成后,将电解后的阴极取出,冷却,并插入另一个阴极施加电压继续进行电解;其中,阴极和阳极的水平间距为15mm,施加电压为2.0V,恒槽压电解时间为10h;(1) The molten salt raw material CaCl2 is heated to the melting temperature to form a molten salt, and the moisture generated during the heating process is taken away by the argon; the cathode and the anode are inserted into the molten salt to form a two-electrode system, and a voltage is applied to the two electrodes, Carry out electrolysis. After the electrolysis is completed, take out the electrolyzed cathode, cool it, and insert another cathode to apply voltage to continue electrolysis; wherein, the horizontal distance between the cathode and the anode is 15mm, the applied voltage is 2.0V, and the constant cell pressure electrolysis time for 10h;

(2)将冷却的电解后的阴极,放入pH值为6.5的弱酸性清水中,超声波频率为50kHZ超声波振荡清洗,去除阴极表面附着的盐,得到的阴极即为钴。(2) Put the cooled cathode after electrolysis into weakly acidic clear water with a pH value of 6.5, and clean it with an ultrasonic frequency of 50kHZ ultrasonic oscillation to remove the salt attached to the surface of the cathode, and the obtained cathode is cobalt.

实施例2Example 2

一种熔盐电化学法回收锂电池正极材料中钴元素的方法,按以下步骤进行:A kind of molten salt electrochemical method reclaims the method for cobalt element in lithium battery cathode material, carries out according to the following steps:

步骤1:锂电池正极材料的溶解Step 1: Dissolution of Lithium Battery Cathode Material

(1)将回收得到的锂电池使用充放电仪进行放电处理,恒流放电3A,放电时间为40min,随后进行人工拆解电池,分离得到锂电池正极材料和负极材料;(1) Discharge the recovered lithium battery using a charge-discharge instrument, discharge at a constant current of 3A, and discharge for 40 minutes, then manually disassemble the battery to separate and obtain the positive and negative materials of the lithium battery;

(2)将锂电池正极材料粉碎后,加入浸出液,在50℃恒温加热60min,同时伴随搅拌,得到浸出混合液;其中,按固液比,锂电池正极材料:浸出液=0.5g:5mL;浸出液为摩尔浓度为6mol/L,H2SO4和体积百分数为40%的H2O2的混合液,按体积比,摩尔浓度为6mol/LH2SO4:体积百分数为40%的H2O2=3:1;(2) After pulverizing the positive electrode material of lithium battery, add leachate, heat at 50°C for 60 minutes at a constant temperature, and at the same time stir to obtain the leach mixture; wherein, according to the solid-to-liquid ratio, lithium battery positive electrode material: leachate = 0.5g: 5mL; leachate It is a mixture of H 2 SO 4 and 40% H 2 O 2 with a molar concentration of 6 mol/L, and the molar concentration is 6 mol/L H 2 SO 4 : 40% H 2 O by volume 2 = 3:1;

(3)将浸出混合液进行过滤,得到滤液;(3) filtering the leaching mixture to obtain a filtrate;

步骤2:氧化钴电极压片的制备Step 2: Preparation of cobalt oxide electrode pellets

(1)向滤液中滴加摩尔浓度为1mol/L的NaOH水溶液,当pH值为4.7时,有Fe、Al形成的沉淀析出,过滤,去除Fe、Al形成的沉淀,得到一次滤液;(1) dripping the NaOH aqueous solution that molar concentration is 1mol/L in the filtrate, when pH value is 4.7, the precipitation that has Fe, Al formation is separated out, filters, and removes the precipitation that Fe, Al formation, obtains primary filtrate;

(2)向一次滤液中继续滴加摩尔浓度为1mol/L的NaOH水溶液,当pH值为9.2时,Co形成的沉淀析出,进行抽滤,得到Co(OH)2沉淀;(2) continue dripping the NaOH aqueous solution that molar concentration is 1mol/L in the primary filtrate, when the pH value is 9.2, the precipitation that Co forms is separated out, carries out suction filtration, obtains Co(OH) Precipitate ;

(3)将Co(OH)2沉淀在100℃下干燥500min,研磨成粒径为0.2mm粉末,取2.0gCo(OH)2粉末压片,在空气中,于900℃灼烧10h,得到氧化钴电极压片;(3) Dry the Co(OH) 2 precipitate at 100°C for 500min, grind it into a powder with a particle size of 0.2mm, take 2.0g of Co(OH) 2 powder, press it into tablets, and burn it at 900°C for 10h in the air to obtain the oxidized Cobalt electrode pellets;

步骤3:电化学准备Step 3: Electrochemical Preparation

同实施例1,不同点在于:With embodiment 1, difference is:

(1)步骤3中,SnO2陶瓷与不锈钢丝集流体连接作为阳极。(1) In step 3, the SnO2 ceramic is connected with the stainless steel wire current collector as the anode.

(2)步骤3中,熔盐原料为Li2CO3(2) In step 3, the molten salt raw material is Li 2 CO 3 .

步骤4:电解Step 4: Electrolysis

同实施例1,不同点在于:With embodiment 1, difference is:

(1)步骤4中,阴极和阳极的水平间距为16mm,施加电压为2.1V,恒槽压电解时间为8h;(1) In step 4, the horizontal distance between the cathode and the anode is 16mm, the applied voltage is 2.1V, and the constant cell voltage electrolysis time is 8h;

(2)步骤4中,超声波振荡清洗,清洗用水pH为7的弱酸性清水,超声波频率为10kHZ。(2) In step 4, ultrasonic vibration cleaning is performed, the cleaning water is weakly acidic water with a pH of 7, and the ultrasonic frequency is 10kHZ.

其他方式相同。Other methods are the same.

实施例3Example 3

一种熔盐电化学法回收锂电池正极材料中钴元素的方法,按以下步骤进行:A kind of molten salt electrochemical method reclaims the method for cobalt element in lithium battery cathode material, carries out according to the following steps:

步骤1:锂电池正极材料的溶解Step 1: Dissolution of Lithium Battery Cathode Material

(1)将回收得到的锂电池使用充放电仪进行放电处理,恒流放电3A,放电时间为60min,随后进行人工拆解电池,分离得到锂电池正极材料和负极材料;(1) Discharge the recovered lithium battery using a charge-discharge instrument, discharge at a constant current of 3A, and discharge for 60 minutes, then manually disassemble the battery to separate and obtain the positive and negative materials of the lithium battery;

(2)将锂电池正极材料粉碎后,加入浸出液,在80℃恒温加热10min,同时伴随搅拌,得到浸出混合液;其中,按固液比,锂电池正极材料:浸出液=1g:20mL;浸出液为摩尔浓度为2mol/L,H2SO4和体积百分数为20%的H2O2的混合液,按体积比,摩尔浓度为2mol/LH2SO4:体积百分数为20%的H2O2=4:1;(2) After crushing the positive electrode material of the lithium battery, add the leaching solution, heat at a constant temperature of 80°C for 10 minutes, and at the same time stir to obtain the leaching mixture; wherein, according to the solid-to-liquid ratio, the positive electrode material of the lithium battery: leaching solution = 1g: 20mL; the leaching solution is The molar concentration is 2mol/L, the mixed solution of H 2 SO 4 and 20% H 2 O 2 by volume, the molar concentration is 2 mol/L H 2 SO 4 : 20% H 2 O 2 by volume =4:1;

(3)将浸出混合液进行过滤,得到滤液;(3) filtering the leaching mixture to obtain a filtrate;

步骤2:氧化钴电极压片的制备Step 2: Preparation of cobalt oxide electrode pellets

(1)向滤液中滴加摩尔浓度为3mol/L的NaOH水溶液,当pH值为8时,有Fe、Al形成的沉淀析出,过滤,去除Fe、Al形成的沉淀,得到一次滤液;(1) dripping the NaOH aqueous solution that molar concentration is 3mol/L in the filtrate, when the pH value is 8, have the precipitation that Fe, Al form to separate out, filter, remove the precipitation that Fe, Al form, obtain primary filtrate;

(2)向一次滤液中继续滴加摩尔浓度为3mol/L的NaOH水溶液,当pH值为10时,Co形成的沉淀析出,进行抽滤,得到Co(OH)2沉淀;(2) continue dripping the NaOH aqueous solution that molar concentration is 3mol/L in the primary filtrate, when the pH value is 10, the precipitation that Co forms is separated out, carries out suction filtration, obtains Co(OH) Precipitate ;

(3)将Co(OH)2沉淀在100℃下干燥600min,研磨成粒径为0.1mm粉末,取2.0gCo(OH)2粉末压片,在空气中,于1000℃灼烧5h,得到氧化钴电极压片;(3) Dry the Co(OH) 2 precipitate at 100°C for 600 minutes, grind it into a powder with a particle size of 0.1mm, take 2.0g of Co(OH) 2 powder, press it into tablets, and burn it at 1000°C for 5 hours in the air to obtain the oxide Cobalt electrode pellets;

步骤3:电化学准备Step 3: Electrochemical Preparation

同实施例1,不同点在于:With embodiment 1, difference is:

(1)步骤3中,Ni基合金与不锈钢丝集流体连接作为阳极。(1) In step 3, the Ni-based alloy is connected to the stainless steel wire current collector as an anode.

(2)步骤3中,熔盐原料为NaOH。(2) In step 3, the molten salt raw material is NaOH.

步骤4:电解Step 4: Electrolysis

同实施例1,不同点在于:With embodiment 1, difference is:

(1)步骤4中,阴极和阳极的水平间距为20mm,施加电压为2.0V,恒槽压电解时间为12h;(1) In step 4, the horizontal distance between the cathode and the anode is 20mm, the applied voltage is 2.0V, and the constant cell voltage electrolysis time is 12h;

(2)步骤4中,超声波振荡清洗,清洗用水pH为5的弱酸性清水,超声波频率为5kHZ。(2) In step 4, ultrasonic vibration cleaning is performed, the cleaning water is weakly acidic water with a pH of 5, and the ultrasonic frequency is 5kHZ.

其他方式相同。Other methods are the same.

实施例4Example 4

一种熔盐电化学法回收锂电池正极材料中钴元素的方法,同实施例1,不同点在于:A method for recycling the cobalt element in the lithium battery positive electrode material by molten salt electrochemical method, the same as embodiment 1, the difference is:

步骤3:电解准备Step 3: Preparation for Electrolysis

(1)步骤3中,Ni基合金与不锈钢丝集流体连接作为阳极。(1) In step 3, the Ni-based alloy is connected to the stainless steel wire current collector as an anode.

(2)步骤3中,熔盐原料为Na2CO3和K2CO3,两者质量比为1:1。(2) In step 3, the molten salt raw materials are Na 2 CO 3 and K 2 CO 3 , and the mass ratio of the two is 1:1.

步骤4:电解Step 4: Electrolysis

同实施例1,不同点在于:With embodiment 1, difference is:

(1)步骤4中,阴极和阳极的水平间距为10mm,施加电压为2.0V,恒槽压电解时间为10h;(1) In step 4, the horizontal distance between the cathode and the anode is 10mm, the applied voltage is 2.0V, and the constant cell voltage electrolysis time is 10h;

(2)步骤4中,超声波振荡清洗,清洗用水pH为6的弱酸性清水,超声波频率为100kHZ。(2) In step 4, ultrasonic vibration cleaning is performed, the cleaning water is weakly acidic water with a pH of 6, and the ultrasonic frequency is 100kHZ.

其他方式相同。Other methods are the same.

实施例5Example 5

一种熔盐电化学法回收锂电池正极材料中钴元素的方法,同实施例1,不同点在于:A method for recycling the cobalt element in the lithium battery positive electrode material by molten salt electrochemical method, the same as embodiment 1, the difference is:

(1)步骤3中,熔盐原料为CaCl2和LiCl,两者原子个数比为Li:Ca=0.65:0.35。(1) In step 3, the molten salt raw materials are CaCl and LiCl, and the atomic number ratio of the two is Li: Ca=0.65:0.35.

其他方式相同。Other methods are the same.

实施例6Example 6

一种熔盐电化学法回收锂电池正极材料中钴元素的方法,同实施例1,不同点在于:A method for recycling the cobalt element in the lithium battery positive electrode material by molten salt electrochemical method, the same as embodiment 1, the difference is:

(1)步骤3中,熔盐原料为MgCl2和Na2CO3,两者质量比为1:1。(1) In step 3, the molten salt raw materials are MgCl 2 and Na 2 CO 3 , and the mass ratio of the two is 1:1.

其他方式相同。Other methods are the same.

Claims (10)

1. a kind of method of cobalt element in melten salt electriochemistry method recycling anode material of lithium battery, which is characterized in that according to the following steps It carries out:
Step 1:The dissolving of anode material of lithium battery
(1) it after lithium battery being carried out discharge treatment, is disassembled, isolated anode material of lithium battery and negative material;
(2) after crushing anode material of lithium battery, leachate is added, in 50~80 DEG C of 10~60min of heated at constant temperature, and meanwhile it is adjoint Stirring obtains leaching mixed liquor;
Wherein, by solid-to-liquid ratio, anode material of lithium battery:Leachate=(0.5~1) g:(5~20) mL;
Leachate is the H that molar concentration is 2~6mol/L2SO4The H for being 20~40% with percentage by volume2O2Mixed aqueous solution, By volume, molar concentration is 2~6mol/LH2SO4:The H that percentage by volume is 20~40%2O2=(3~5):1;
(3) mixed liquor will be leached to be filtered, obtains filtrate;
Step 2:The preparation of cobalt oxide electrode tabletting
(1) the NaOH aqueous solutions that molar concentration is 1~3mol/L are added dropwise into filtrate, when pH value is 4.7~8, there is Fe, Al shape At Precipitation, filtering, removal Fe, Al formed precipitation, obtain first-time filtrate;
(2) continue that the NaOH aqueous solutions that molar concentration is 1~3mol/L are added dropwise into first-time filtrate, when pH value is 9.2~10.0 When, the Precipitation that Co is formed is filtered, obtains Co (OH)2Precipitation;
(3) by Co (OH)2Precipitation drying, grind into powder, tabletting, in air calcination obtain cobalt oxide electrode tabletting;
Step 3:Electrochemistry prepares
Cobalt oxide electrode tabletting is wrapped up with foamed nickel current collector, cathode, graphite rod and stainless steel wire are then connected to molybdenum filament Collector is connected to anode;
Fused salt raw material stoving is removed into moisture removal, is placed in crucible, then crucible is put into reactor, cathode and anode are suspended in molten Above salt raw material, closed reactor is continually fed into argon gas into reactor, forms argon gas atmosphere;
Step 4:Electrolysis
(1) fused salt raw material being heated to fusion temperature and forms fused salt, cathode and anode are inserted into fused salt, constitute two electrode systems, Apply voltage in two electrodes, be electrolysed, after the completion of electrolysis, the cathode after electrolysis is taken out, it is cooling, and it is inserted into another the moon Pole applies voltage and continues to be electrolysed;Wherein, the level interval of cathode and anode be 15 ± 5mm, apply voltage be 2.0~ 2.1V, electrolysis time are 8~12h;
(2) by the cathode after cooling electrolysis, into the water, cleaned by ultrasonic vibration, the salt of removal cathode surface attachment obtains Cathode be cobalt.
2. the method for cobalt element, feature exist in melten salt electriochemistry method recycling anode material of lithium battery as described in claim 1 In, in (1) of the step 1, the discharge treatment, specially:Discharge treatment, constant-current discharge are carried out using charge and discharge instrument 3A, discharge time >=30min.
3. the method for cobalt element, feature exist in melten salt electriochemistry method recycling anode material of lithium battery as described in claim 1 In in (3) of the step 2, the drying is to dry 500~600min in air at 90~100 DEG C.
4. the method for cobalt element, feature exist in melten salt electriochemistry method recycling anode material of lithium battery as described in claim 1 In in (3) of the step 2, described is ground to, and obtains the Co (OH) that grain size is 0.10~0.20mm2Powder.
5. the method for cobalt element, feature exist in melten salt electriochemistry method recycling anode material of lithium battery as described in claim 1 In in (3) of the step 2, the calcination is the calcination 1~for 24 hours in air at 900~1000 DEG C.
6. the method for cobalt element, feature exist in melten salt electriochemistry method recycling anode material of lithium battery as described in claim 1 In in the step 3, the graphite rod can also be SnO2Ceramics or Ni based alloys.
7. the method for cobalt element, feature exist in melten salt electriochemistry method recycling anode material of lithium battery as described in claim 1 In in the step 3, the fused salt raw material is molten chloride raw material, carbonation fused salt raw material, hydroxide fused salt original The mixing of one or more of material.
8. the method for cobalt element, feature exist in melten salt electriochemistry method recycling anode material of lithium battery as claimed in claim 7 In, when for molten chloride raw material, specially CaCl2, LiCl, NaCl, KCl, MgCl2, BaCl2One or more of Fused salt mixt;
When for carbonation fused salt raw material, specially Li2CO3, Na2CO3, K2CO3, CaCO3One or more of mixing it is molten Salt;
When for hydroxide fused salt raw material, specially LiOH, NaOH, the fused salt mixt of one or more of KOH.
9. the method for cobalt element, feature exist in melten salt electriochemistry method recycling anode material of lithium battery as described in claim 1 In in the step 3, the argon gas is passed through by reactor air inlet, is discharged by reactor gas outlet, when discharge, will be melted The moisture that salt generates is taken away.
10. the method for cobalt element, feature exist in melten salt electriochemistry method recycling anode material of lithium battery as described in claim 1 In in the step 4, the cleaned by ultrasonic vibration, water for cleaning is the faintly acid clear water of 5≤pH≤7;Ultrasonic wave frequency Rate is 0.5kHZ~100kHZ.
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CN109706320A (en) * 2019-01-29 2019-05-03 东北大学 A method for wet recovery of Co and Li from waste lithium batteries with ethanol as reducing agent
CN109722538A (en) * 2019-01-29 2019-05-07 东北大学 Method for recovering cobalt and lithium in waste lithium cobalt oxide battery by molten salt electrolysis
CN110611136A (en) * 2019-09-09 2019-12-24 华北理工大学 A method for recovering and preparing cobalt element from waste lithium batteries by using molten salt method
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