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CN103515668A - Complete-set device for recycling metal in waste lithium battery - Google Patents

Complete-set device for recycling metal in waste lithium battery Download PDF

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Publication number
CN103515668A
CN103515668A CN201310513175.8A CN201310513175A CN103515668A CN 103515668 A CN103515668 A CN 103515668A CN 201310513175 A CN201310513175 A CN 201310513175A CN 103515668 A CN103515668 A CN 103515668A
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flue gas
waste
waste lithium
heat
recycling
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刘麟
张锁龙
廖昆
吴霄婷
李明杰
潘�清
任旭明
魏凡佳
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Changzhou University
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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
    • H01M10/54Reclaiming serviceable parts of waste accumulators
    • 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
    • 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
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/84Recycling of batteries or fuel cells

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  • Environmental & Geological Engineering (AREA)
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  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Treating Waste Gases (AREA)

Abstract

一种用于废旧锂电池中金属回收的成套装置属于环保技术领域。废旧锂离子电池能提取出锂、钴、铜、镍、轻稀土等材料,锂电池的回收具有巨大的潜在商业价值,其回收利用前景广阔。本设计首先对废旧锂电池进行破碎预处理,进料,随后进入烘焙室进行一次烘焙,再进入回转焚烧炉进行二次燃烧,然后连续进行三次降温,并进行尾气净化,最后烟气达标排入大气。在排出烟气的过程中,使用急冷装置迅速使尾气降温以防止二恶英的产生。通过板式换热器的热量进行回收,达到资源化利用的目的。A complete device for recycling metals from waste lithium batteries belongs to the technical field of environmental protection. Lithium, cobalt, copper, nickel, light rare earth and other materials can be extracted from waste lithium-ion batteries. The recycling of lithium batteries has huge potential commercial value, and its recycling prospects are broad. In this design, the waste lithium battery is first crushed and pretreated, fed, and then enters the baking room for a baking, and then enters the rotary incinerator for secondary combustion, and then continuously cools down three times, and performs exhaust gas purification, and finally the flue gas reaches the standard and is discharged into the atmosphere. In the process of exhausting the flue gas, a quenching device is used to quickly cool down the exhaust gas to prevent the generation of dioxins. The heat of the plate heat exchanger is recovered to achieve the purpose of resource utilization.

Description

一种用于废旧锂电池中金属回收的成套装置A complete device for recycling metals from waste lithium batteries

所属技术领域Technical field

本发明涉及一种用于废旧锂电池中金属回收的成套装置。属于环保技术领域。The invention relates to a complete set of equipment for recycling metals in waste lithium batteries. It belongs to the field of environmental protection technology.

背景技术Background technique

2011年,我国的锂离子电池产量约为12.5亿只,成为世界上最大的锂离子电池的生产和消费国家。锂离子电池一般可以使用大约3年时间,2012年全球废弃的锂离子电池达到了10亿只。In 2011, my country's lithium-ion battery output was about 1.25 billion, becoming the world's largest producer and consumer of lithium-ion batteries. Lithium-ion batteries can generally be used for about 3 years. In 2012, the number of lithium-ion batteries discarded worldwide reached 1 billion.

废旧锂离子电池能提取出锂、钴、铜、镍、轻稀土等材料,锂电池的回收具有巨大的潜在商业价值,其回收利用前景广阔。此外,废旧锂电池产生污染的成分如氯氟碳化物、卤素阻燃剂、汞、硒、镍、铅、铬等,如不能妥善处理而直接填埋或焚烧,将对空气、土壤和水体产生严重的污染。Lithium, cobalt, copper, nickel, light rare earth and other materials can be extracted from waste lithium-ion batteries. The recycling of lithium batteries has huge potential commercial value, and its recycling prospects are broad. In addition, the polluting components of waste lithium batteries, such as chlorofluorocarbons, halogen flame retardants, mercury, selenium, nickel, lead, chromium, etc., if not properly disposed of and directly landfilled or incinerated, will cause pollution to the air, soil and water. severe pollution.

在国内,报废锂电池的回收处理方式与其余大多电子废弃物一样,和城镇生活垃圾一起填埋、焚烧、堆肥,这种简单的锂电池处理方法对自然环境产生了严重的影响。由于锂电池中含有大量六氟磷酸锂(LiPF6)有机碳酸酯电解液,LiPF6具有很强的腐蚀性,且极易和水反应生成HF有毒气体,而锂电池中其他难降解的如DME(甲氧基乙烷)、甲醇、甲酸等有毒有害物质直接与大气、土壤和水接触会对其产生污染,进而危害人类的生态系统环境。In China, the recycling method of scrap lithium batteries is the same as that of most other electronic wastes, which are landfilled, incinerated, and composted together with urban domestic waste. This simple lithium battery treatment method has had a serious impact on the natural environment. Since lithium batteries contain a large amount of lithium hexafluorophosphate (LiPF 6 ) organic carbonate electrolyte, LiPF 6 is highly corrosive and easily reacts with water to generate HF poisonous gas, while other refractory lithium batteries such as DME (methoxy Ethane), methanol, formic acid and other toxic and harmful substances will pollute the atmosphere, soil and water in direct contact with them, thereby endangering the human ecosystem and environment.

锂离子电池正极材料主要成分是LiCoO2,我国属于贫钴国家,自然界存储量较低,金属钴主要依靠进口来满足需求,并且钴属于重金属元素,锂电池的简单处理方式将会使其含有的钴等重金属元素在自然环境中累积,最终会危害人类自身。此外,废旧锂电池的各种金属材料都有较高的回收价值,因此,如果能从废旧锂离子电池中回收锂、钴、铜、镍、铁、铝等金属,不仅具有显著经济效益,而且可以避免其对环境的污染,具有良好的社会效益。The main component of the positive electrode material of lithium-ion batteries is LiCoO 2 . China is a cobalt-poor country, and the natural storage capacity is low. Metal cobalt mainly depends on imports to meet the demand, and cobalt is a heavy metal element. Heavy metal elements such as cobalt accumulate in the natural environment and will eventually harm humans. In addition, various metal materials of waste lithium-ion batteries have high recycling value. Therefore, if metals such as lithium, cobalt, copper, nickel, iron, and aluminum can be recovered from waste lithium-ion batteries, it will not only have significant economic benefits, but also It can avoid its pollution to the environment and has good social benefits.

发明内容Contents of the invention

本发明涉及一种用于回收废旧锂电池中贵重金属的成套装置。整套废旧锂电池资源化再利用系统应能在实现回收贵重金属资源的基础上,通过一系列工艺流程,消除尾气和残渣的排放所造成的环境污染问题。为满足上述要求,整套锂电池资源化回收处理焚烧炉装置包含以下设备:烘焙室、废旧锂电池焚烧炉本体、翅片管换热器、急冷塔、尾气余热回收板式换热器、进料及管路系统、电控系统、烟气净化装置、引风机、独立烟囱。The invention relates to a complete set of devices for recycling precious metals in waste lithium batteries. The whole set of waste lithium battery resource recycling system should be able to eliminate the environmental pollution caused by exhaust gas and residue discharge through a series of technological processes on the basis of realizing the recovery of precious metal resources. In order to meet the above requirements, the complete set of lithium battery resource recovery and treatment incinerator device includes the following equipment: baking chamber, waste lithium battery incinerator body, finned tube heat exchanger, quenching tower, exhaust waste heat recovery plate heat exchanger, feed and Pipeline system, electric control system, flue gas purification device, induced draft fan, independent chimney.

本发明是采取以下技术方法来实现的。The present invention is realized by adopting the following technical methods.

(1)预处理(1) Pretreatment

废旧锂电池再进入回转焚烧炉之前采用破碎机进行破碎预处理,破碎后得到尺寸均匀的物料可以显著提高燃烧效率;并且还能够降低尾气中CO的含量。破碎后的废物进入预处理区进行暂时存坑,在预处理区进行配料掺混,整个预处理区也设置为密闭微负压状态,空气经炉引风机引入炉内,这样可以确保有害气体不外溢。Before the waste lithium battery enters the rotary incinerator, it is crushed and pretreated by a crusher. After crushing, the material with uniform size can significantly improve the combustion efficiency; and it can also reduce the content of CO in the exhaust gas. The crushed waste enters the pretreatment area for temporary storage, and mixes ingredients in the pretreatment area. The entire pretreatment area is also set in a closed micro-negative pressure state, and the air is introduced into the furnace through the furnace induced draft fan, so as to ensure that harmful gases are not released. Spill.

(2)进料(2) Feed

焚烧系统由烘焙室、回转焚烧炉及控制系统组成。经过预处理破碎的待处理废旧锂电池废料按适当比例配比后先进入带加热式喂料机,废料由喂料机的传送装置送至焚烧炉进料口,完成进料。废料在喂料机中可以得到预热,由20℃升温到200℃,整个预热过程的热量由一次降温的翅片管式换热器出口的导热油提供,导热油通入夹套内,对废料完成预热后的导热油出口温度降至230℃,然后继续通入翅片管式换热器。The incineration system consists of a baking chamber, a rotary incinerator and a control system. After pretreatment and crushing, the waste lithium battery waste to be treated is proportioned in an appropriate proportion and then enters the heated feeder. The waste is sent to the incinerator feed port by the conveying device of the feeder to complete the feeding. The waste can be preheated in the feeder, from 20°C to 200°C, the heat of the whole preheating process is provided by the heat transfer oil at the outlet of the finned tube heat exchanger that has been cooled down once, and the heat transfer oil is passed into the jacket. After preheating the waste, the outlet temperature of the heat transfer oil drops to 230°C, and then continues to pass into the finned tube heat exchanger.

(3)一次烘焙(3) Baking once

在回转焚烧炉连续旋转作用下,废料在窑内不停翻动,首先进入烘焙室,进行废料电解液的分离,并完成干燥、气化和初步燃烧。经过一次烘焙,废料完成了进一步预热,这样也有利于提高燃烧效率,能够使燃烧更加彻底。Under the action of the continuous rotation of the rotary incinerator, the waste material is constantly turned in the kiln, and first enters the baking chamber to separate the waste material electrolyte, and complete drying, gasification and preliminary combustion. After one baking, the waste material is further preheated, which is also conducive to improving the combustion efficiency and making the combustion more thorough.

(4)二次燃烧(4) Secondary combustion

随着窑体的转动,废料会被移动到温度较高的中部,开始热解,低燃点的物质开始燃烧;接着移动到窑尾,温度进一步升高,危险废物裂解为一氧化碳等可燃气体和废渣。在回转焚烧炉内,通过对废料进行反复翻转与持续推进以及低燃点气体的燃烧,使危险废物基本完全分解为可燃气体和残渣。With the rotation of the kiln body, the waste will be moved to the middle part with higher temperature, pyrolysis will start, and the substances with low ignition point will start to burn; then move to the end of the kiln, the temperature will rise further, and the hazardous waste will be cracked into combustible gases such as carbon monoxide and waste residue . In the rotary incinerator, the hazardous waste is basically completely decomposed into combustible gas and residue through repeated turning and continuous propulsion of the waste and combustion of low ignition point gas.

(5)一次降温(5) Cool down once

回转焚烧炉出口烟气首先进入翅片管换热器(烟气降温至800℃)加热来自生产车间的230℃的导热油至260℃废料预热使用,废料预热系统出口导热油温度会被降至230℃,然后继续通入翅片管换热器中进行对烟气的一次降温,将高温烟气中的部分热能再次回收,整个过程实现了热量在同一个工艺流程中的有效循环利用。The flue gas at the outlet of the rotary incinerator first enters the finned tube heat exchanger (the flue gas is cooled to 800°C) to heat the heat transfer oil from the production workshop at 230°C to 260°C for waste preheating, and the temperature of the heat transfer oil at the outlet of the waste preheating system will be reduced It is lowered to 230°C, and then continues to pass through the finned tube heat exchanger to cool down the flue gas once, and recover part of the heat energy in the high-temperature flue gas again. The whole process realizes the effective recycling of heat in the same process flow .

(6)二次降温(6) Second cooling

当温度在250~500℃的温度区间时,废气中将很容易发生二恶英的再生成反应,因此为最大程度避免尾气降温过程中二恶英的再生成,应将要把翅片管换热器出口烟气迅速降到200℃以下,以便快速“跃过”二恶英的生成温度区。技术上采用烟气急冷塔,使烟气在1s左右极短时间内降到200℃。急冷塔采用喷水急冷,急冷塔内通过水喷雾方式与逆流而上的烟气混合,使得烟气温度迅速降低以避开了二恶英产生的旺盛区域;另外被烟气加热的冷却水可以供工厂循环使用。When the temperature is in the temperature range of 250-500°C, the regeneration reaction of dioxins will easily occur in the exhaust gas. Therefore, in order to avoid the regeneration of dioxins during the cooling process of the exhaust gas to the greatest extent, the heat exchange of finned tubes should be carried out. The flue gas at the outlet of the device quickly drops below 200°C in order to quickly "jump over" the formation temperature zone of dioxins. Technically, a flue gas quenching tower is used to reduce the flue gas to 200°C in a very short time of about 1 second. The quenching tower is quenched by spraying water, and the water spraying method in the quenching tower is mixed with the flue gas upstream, so that the temperature of the flue gas is rapidly reduced to avoid the strong area where dioxins are produced; in addition, the cooling water heated by the flue gas can For factory recycling.

(7)第三次降温(7) The third cooling

由于急冷塔出口烟气温度为200℃,此时若将其排放至空气中不但浪费了能源,而且还会导致大气的热污染。故需要再进行第三次降温,该步骤由尾气余热回收板式换热器完成,经过第三次降温,板式换热器出口温度降为150℃,达到了烟气温度排放标准。Since the flue gas temperature at the exit of the quenching tower is 200°C, if it is discharged into the air at this time, it will not only waste energy, but also cause thermal pollution of the atmosphere. Therefore, a third cooling is required. This step is completed by the tail gas waste heat recovery plate heat exchanger. After the third cooling, the outlet temperature of the plate heat exchanger drops to 150°C, which meets the flue gas temperature emission standard.

(8)烟气净化及排放(8) Flue gas purification and emission

经板式换热器出口的烟气将进入半干式反应装置进行烟气净化,在干式反应装置中喷入活性炭及Ca(OH)2对烟气进一步脱酸,并对重金属及可能再生产的二恶英等物质进行吸附;携有大量粒状物的烟气从反应塔出来进入后续的袋式除尘器,部分未反应的石灰附在滤袋上与通过滤袋的酸气再次反应,使去除效率进一步提高;最后,烟气净化的最后一道工序是湿式脱酸,在湿式脱酸塔中喷入碱液脱除SO2、HCl、HF等酸性气体,达到严格的烟气排放标准。最后经过净化的烟气被加热以消去白烟后通过引风机的作用送入烟囱排入大气中。The flue gas at the outlet of the plate heat exchanger will enter the semi-dry reaction device for flue gas purification. Activated carbon and Ca(OH)2 are sprayed into the dry reaction device to further deacidify the flue gas, and to remove heavy metals and possibly reproduced Dioxin and other substances are adsorbed; the flue gas with a large amount of particulate matter comes out of the reaction tower and enters the subsequent bag filter, and part of the unreacted lime is attached to the filter bag and reacts again with the acid gas passing through the filter bag to remove The efficiency is further improved; finally, the last process of flue gas purification is wet deacidification, spraying lye into the wet deacidification tower to remove acid gases such as SO 2 , HCl, HF, etc., to meet strict flue gas emission standards. Finally, the purified flue gas is heated to eliminate white smoke, and then sent into the chimney through the action of the induced draft fan to be discharged into the atmosphere.

本发明专利的有益效果是:The beneficial effects of the patent of the present invention are:

本发明所设计的废旧锂电池金属回收成套装置设计原理和方法简单清晰,在保留了回转焚烧炉的适应能力强、运行稳定可靠的基础上,通过应用急冷塔及换热器对烟气进行处理,使排放烟气的热度、有机物的去除率和焚烧残渣的热灼减率可满足国标的要求,对热量进行换热回收,实现了资源再生利用;同时减少了二恶英和一氧化碳的排放,达到无害化处理的目的。The design principle and method of the waste lithium battery metal recycling complete set designed by the present invention are simple and clear. On the basis of retaining the strong adaptability and stable and reliable operation of the rotary incinerator, the flue gas is processed by using a quenching tower and a heat exchanger. , so that the heat of exhaust flue gas, the removal rate of organic matter and the thermal ignition loss rate of incineration residue can meet the requirements of the national standard, and the heat can be recovered by heat exchange to realize the recycling of resources; at the same time, the emission of dioxin and carbon monoxide can be reduced, reaching The purpose of harmless disposal.

附图说明Description of drawings

废旧锂电池中金属回收的成套装置的工艺流程图Process flow chart of a complete set of equipment for metal recovery from waste lithium batteries

具体实施方式Detailed ways

下面结合成套装置的工艺流程图对废旧锂电池中金属回收的成套装置进行描述。The complete set of equipment for metal recovery in waste lithium batteries is described below in conjunction with the process flow chart of the complete set of equipment.

本发明由烘焙室、废旧锂电池焚烧炉本体、翅片管换热器、急冷塔、尾气余热回收板式换热器、进料及管路系统、电控系统、烟气净化装置、引风机、独立烟囱组成。The present invention consists of a baking chamber, a waste lithium battery incinerator body, a finned tube heat exchanger, a quench tower, a plate heat exchanger for exhaust waste heat recovery, a feed and pipeline system, an electric control system, a flue gas purification device, an induced draft fan, independent chimney.

首先对废旧锂电池进行破碎预处理,进料;随后进入烘焙室进行一次烘焙,再进入回转焚烧炉进行二次燃烧,以实现锂电池的充分燃烧分解;然后由翅片管换热器对排出的烟气进行一次降温,降温用的导热油用于烘焙室的锂电池预加热;用急冷塔对翅片管换热器排出烟气进行二次急速降温,跃过烟气中二恶英的生成温度区间,避免二恶英的生成;使用板式换热器对烟气进行三次降温,使其达到向大气中排放的温度标准,节约能源并避免产生热污染;板式换热器出口烟气通过干式-除尘-湿式三段式烟气净化装置进行充分的脱酸除尘,最后将无害烟气由引风机将其通过烟囱排入大气。First, the waste lithium battery is crushed and pretreated, and the material is fed; then it enters the baking room for a baking, and then enters the rotary incinerator for secondary combustion to achieve full combustion and decomposition of the lithium battery; then it is discharged by the finned tube heat exchanger The flue gas is cooled once, and the heat-conducting oil used for cooling is used to preheat the lithium battery in the baking chamber; the flue gas discharged from the finned tube heat exchanger is rapidly cooled twice with a rapid cooling tower, skipping the dioxin in the flue gas Generate a temperature range to avoid the generation of dioxins; use a plate heat exchanger to cool the flue gas three times to make it reach the temperature standard for emission into the atmosphere, save energy and avoid thermal pollution; the flue gas at the outlet of the plate heat exchanger passes through The dry-dust removal-wet three-stage flue gas purification device performs sufficient deacidification and dust removal, and finally the harmless flue gas is discharged into the atmosphere through the chimney by the induced draft fan.

Claims (4)

1. this method is a kind of energy-conservation, innoxious, convenient and from waste lithium cell, reclaim efficiently the complete sets of equipment of metal.The present invention preheats and assembled set device that incineration system, tail gas waste heat recovering system and flue gas purification system form by curing, on the basis of adaptable, stable and reliable operation that has retained rotary incinerator, by application quench tower and heat exchanger, flue gas is processed, the hot burn decrement rate that makes to discharge the temperature of flue gas, organic clearance and incineration residue can meet the requirement of GB, heat is carried out to heat exchange recovery, realized resource regeneration; Reduce the discharge of dioxin and carbon monoxide simultaneously, reached the object of harmless treatment.
2. according to right 1, require the described the complete sets of equipment for waste lithium cell metal recovery, it is characterized in that preheating and incineration system, tail gas waste heat recovering system and flue gas purification system three parts form in order by curing.
3. according to right 1, require the described the complete sets of equipment for waste lithium cell metal recovery, it is characterized in that lithium battery was preheated by baking chamber before burning, its origin of heat flue gas heat that finned tube exchanger conduction oil reclaims in flue gas waste heat recovery system.
4. according to right 1, require the described the complete sets of equipment for waste lithium cell metal recovery, it is characterized in that flue gas purification system is by the equipment sequential combination mode of " dry type-dedusting-wet type " syllogic gas cleaning, can fully realize after burning lithium battery and produce deacidifying flue gas dedusting demand.
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CN104480311A (en) * 2014-11-21 2015-04-01 邱江波 Method for separating metal and organic matters
CN107441915A (en) * 2017-07-31 2017-12-08 合肥国轩高科动力能源有限公司 A treatment method for waste power battery pyrolysis waste gas
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CN107774698A (en) * 2017-10-31 2018-03-09 泰兴市开普蓝环保设备制造有限公司 A kind of old and useless battery anaerobic catalytic cracking system and method
CN107959076A (en) * 2017-11-13 2018-04-24 中国恩菲工程技术有限公司 The processing method of waste and old lithium ion battery
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CN108172923A (en) * 2017-11-13 2018-06-15 中国恩菲工程技术有限公司 The processing system of waste and old lithium ion battery
CN110719963A (en) * 2017-11-22 2020-01-21 住友金属矿山株式会社 Treatment method of lithium ion battery waste
CN110719963B (en) * 2017-11-22 2021-10-15 住友金属矿山株式会社 How to dispose of lithium-ion battery waste
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CN109273790A (en) * 2018-09-26 2019-01-25 贵州中伟资源循环产业发展有限公司 A kind of system for metal recovery in waste lithium cell
CN109713315A (en) * 2018-12-19 2019-05-03 天能电池(芜湖)有限公司 Grid smear byproduct for treatment reuse method
CN111939679A (en) * 2020-07-06 2020-11-17 浙江天能新材料有限公司 Flue gas dry purification treatment system and method in lithium battery recycling treatment process
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Application publication date: 20140115