CN105811040A - Method for smashing, detaching and recycling lithium battery - Google Patents
Method for smashing, detaching and recycling lithium battery Download PDFInfo
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- CN105811040A CN105811040A CN201610322411.1A CN201610322411A CN105811040A CN 105811040 A CN105811040 A CN 105811040A CN 201610322411 A CN201610322411 A CN 201610322411A CN 105811040 A CN105811040 A CN 105811040A
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- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 title claims abstract description 52
- 229910052744 lithium Inorganic materials 0.000 title claims abstract description 52
- 238000000034 method Methods 0.000 title claims abstract description 31
- 238000004064 recycling Methods 0.000 title abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 30
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 26
- 239000000463 material Substances 0.000 claims abstract description 24
- 239000006148 magnetic separator Substances 0.000 claims abstract description 15
- 239000004033 plastic Substances 0.000 claims abstract description 15
- 229920003023 plastic Polymers 0.000 claims abstract description 15
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 14
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 14
- 229910002804 graphite Inorganic materials 0.000 claims abstract description 12
- 239000010439 graphite Substances 0.000 claims abstract description 12
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000011889 copper foil Substances 0.000 claims abstract description 8
- 239000007921 spray Substances 0.000 claims abstract description 8
- 239000002985 plastic film Substances 0.000 claims abstract description 6
- 229920006255 plastic film Polymers 0.000 claims abstract description 6
- 239000000126 substance Substances 0.000 claims abstract description 5
- 230000018044 dehydration Effects 0.000 claims description 14
- 238000006297 dehydration reaction Methods 0.000 claims description 14
- 239000010865 sewage Substances 0.000 claims description 10
- 238000012216 screening Methods 0.000 claims description 8
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 7
- 238000011084 recovery Methods 0.000 claims description 7
- 238000001914 filtration Methods 0.000 claims description 4
- 238000004062 sedimentation Methods 0.000 claims description 4
- 230000009182 swimming Effects 0.000 claims 10
- 238000007664 blowing Methods 0.000 claims 3
- 239000005030 aluminium foil Substances 0.000 claims 2
- 229910000831 Steel Inorganic materials 0.000 claims 1
- 239000012736 aqueous medium Substances 0.000 claims 1
- 230000005611 electricity Effects 0.000 claims 1
- 238000000465 moulding Methods 0.000 claims 1
- 230000001376 precipitating effect Effects 0.000 claims 1
- 239000010959 steel Substances 0.000 claims 1
- 239000010926 waste battery Substances 0.000 abstract description 14
- 239000003344 environmental pollutant Substances 0.000 abstract description 7
- 231100000719 pollutant Toxicity 0.000 abstract description 7
- 239000011888 foil Substances 0.000 abstract description 6
- 229910001220 stainless steel Inorganic materials 0.000 abstract description 6
- 239000010935 stainless steel Substances 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- -1 diaphragm Substances 0.000 abstract description 2
- 239000007789 gas Substances 0.000 abstract description 2
- 239000000428 dust Substances 0.000 description 9
- 239000002699 waste material Substances 0.000 description 9
- 239000007774 positive electrode material Substances 0.000 description 6
- 238000000926 separation method Methods 0.000 description 6
- 239000002341 toxic gas Substances 0.000 description 5
- 238000003912 environmental pollution Methods 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 238000004806 packaging method and process Methods 0.000 description 3
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 229910001416 lithium ion Inorganic materials 0.000 description 1
- 238000007885 magnetic separation Methods 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
Classifications
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/54—Reclaiming serviceable parts of waste accumulators
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/84—Recycling of batteries or fuel cells
Landscapes
- Secondary Cells (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
本发明涉及一种锂电池破碎拆解回收方法,通过水式吸风破机、磁选机、卧式风选机、水式摩擦机、第一涡分机、第二涡分机等设备将废旧锂电池分选出如塑料、隔膜、不锈钢、铝塑膜、铝、塑料、铜箔、铝箔、石墨等物料,分选纯度可达到94%‑99%之间。生产过程中锂电池中的各种有害气体经过喷淋塔、活性炭塔处理进行达标排放,生产过程中所需的水全部进行循环利用,无外排水源,并且水在循环过程中经过沉淀、过滤和添加化学药剂进行水处理。本发明无需对废弃电池进行预处理,可直接进入破碎、拆解、回收;能够显著地提高废弃电池的处理质量和处理效率,且可有效地控制处理过程中的污染物排放。
The invention relates to a lithium battery crushing, dismantling and recycling method, which uses equipment such as a water suction wind breaker, a magnetic separator, a horizontal winnowing machine, a water friction machine, a first vortex separator, a second vortex separator, etc. Materials such as plastic, diaphragm, stainless steel, aluminum-plastic film, aluminum, plastic, copper foil, aluminum foil, graphite, etc. are sorted out of batteries, and the sorting purity can reach between 94%‑99%. During the production process, various harmful gases in the lithium battery are treated by spray towers and activated carbon towers to meet the discharge standards. All the water required in the production process is recycled. There is no external drainage source, and the water is precipitated and filtered during the circulation process. and adding chemicals for water treatment. The invention does not require pretreatment of waste batteries, and can be directly crushed, disassembled, and recycled; can significantly improve the treatment quality and efficiency of waste batteries, and can effectively control the discharge of pollutants during the treatment process.
Description
技术领域technical field
本发明涉及废弃电池拆解回收技术领域,具体涉及一种锂电池破碎拆解回收方法。The invention relates to the technical field of dismantling and recycling of waste batteries, in particular to a method for crushing, dismantling and recycling of lithium batteries.
背景技术Background technique
随着国家对电动汽车的大力推广,未来将有大量电池面临报废的问题,根据中国汽车技术研究中心的预计,我国废弃电池的回收率不足2%,大量废弃的电池造成了资源能源的浪费和环境污染,废旧锂离子电池中含有大量可利用的资源,例如铝、铜等有价金属以及石墨、炭基材料等;如果这些废旧锂电池处置不当,将会造成很大的资源浪费和环境污染。With the country's vigorous promotion of electric vehicles, a large number of batteries will face the problem of being scrapped in the future. According to the prediction of China Automotive Technology Research Center, the recycling rate of waste batteries in my country is less than 2%. A large number of waste batteries cause waste of resources and energy. Environmental pollution, waste lithium-ion batteries contain a lot of available resources, such as valuable metals such as aluminum and copper, graphite, carbon-based materials, etc.; if these waste lithium batteries are not disposed of properly, it will cause a lot of waste of resources and environmental pollution .
然而现有技术中锂电池的回收刚刚起步,且现有的分离方法通常具有较大的局限性,不能一次性将废弃电池的可再利用资源进行有效分离,且分离过程中会产生较大的粉尘及有害物,不仅影响废旧电池的处理质量和处理效率,而且会对环境造成严重的破坏,因此,需要本领域的技术人员对此作出改善。However, the recycling of lithium batteries in the prior art has just started, and the existing separation methods usually have relatively large limitations. They cannot effectively separate the reusable resources of waste batteries at one time, and a large amount of energy will be generated during the separation process. Dust and harmful substances not only affect the treatment quality and efficiency of waste batteries, but also cause serious damage to the environment. Therefore, it is necessary for those skilled in the art to improve this.
发明内容Contents of the invention
本发明的一个目的是为了克服上述现有技术的不足,进而提供一种锂电池破碎拆解回收方法,本发明无需对废弃电池进行预处理,可直接进入破碎、拆解、回收;能够显著地提高废弃电池的处理质量和处理效率,且可有效地控制处理过程中的污染物排放。An object of the present invention is to overcome the above-mentioned deficiencies in the prior art, and then provide a lithium battery crushing and dismantling recycling method, the present invention does not need to carry out pretreatment to waste batteries, can directly enter crushing, dismantling, recycling; can significantly Improve the treatment quality and efficiency of waste batteries, and effectively control the discharge of pollutants in the treatment process.
本发明的技术方案:Technical scheme of the present invention:
一种锂电池破碎拆解回收方法,包括以下步骤:A method for crushing, dismantling, and recovering lithium batteries, comprising the following steps:
第一步,将带电或不带电的锂电池整体投入水式吸风破机中;The first step is to put the charged or uncharged lithium battery into the water type suction crusher as a whole;
第二步,所述水式吸风破机对锂电池进行破碎处理,通过水介质对破碎过程中的锂电池进行安全保护,污水沉淀后可过滤获得锂电池中的正极材料与石墨的混合物;集料关风机与所述水式吸风破机连接,通过集料关风机可获得锂电池中的塑膜;In the second step, the water-type suction crusher crushes the lithium battery, and protects the lithium battery in the crushing process through the water medium. After the sewage is precipitated, it can be filtered to obtain a mixture of the positive electrode material and graphite in the lithium battery; The aggregate shut-off fan is connected to the water-type suction breaker, and the plastic film in the lithium battery can be obtained through the aggregate shut-off fan;
第三步,将破碎后的锂电池输送至磁选机,通过磁选机可分离获得锂电池中的铁;The third step is to transport the crushed lithium battery to the magnetic separator, and the iron in the lithium battery can be separated by the magnetic separator;
第四步,将破碎后的物料输送至卧式风选机,卧式风选机分选出较轻物质与较重物质,卧式风选机分别与第一涡分机和水式摩擦机连接,较重物质通过第一涡分机处理后可获得塑壳、不锈钢和铝,水式摩擦机依次与筛选机、第二涡分机连接,较轻物质经过水式摩擦机,筛选机可分离获得铝塑包装物,经过第二涡分机处理后可分离获得塑料杂物、铝箔、铜箔,污水经过脱水装置回到沉淀池,进行沉淀得到正极材料与石墨的混合物。The fourth step is to convey the crushed materials to the horizontal winnowing machine. The horizontal winnowing machine separates the lighter material and the heavier material. The horizontal winnowing machine is connected with the first vortex separator and the water friction machine respectively. After the heavy material is processed by the first vortex separator, plastic shell, stainless steel and aluminum can be obtained. The water friction machine is connected with the screening machine and the second vortex separator in turn. The lighter material can be separated by the water friction machine, and the screening machine can be separated to obtain aluminum. The plastic packaging can be separated to obtain plastic debris, aluminum foil, and copper foil after being treated by the second vortex separator. The sewage is returned to the sedimentation tank through the dehydration device, and the mixture of positive electrode material and graphite is obtained by precipitation.
进一步地,所述磁选机与所述水式吸风破机之间设置有脱水上料机,还包括至少一个供水池,所述供水池分别对所述水式吸风破机、脱水上料机、水式摩擦机供水。Further, a dehydration feeder is provided between the magnetic separator and the water-type air suction crusher, and at least one water supply pool is provided, and the water supply pool is respectively used for the water-type air suction crusher and the dehydration upper machine. feeder, water friction machine water supply.
进一步地,所述集料关风机依次与引风机、喷淋塔、活性炭塔连接。Further, the aggregate shut-off fan is sequentially connected with the induced draft fan, the spray tower, and the activated carbon tower.
进一步地,在所述磁选机与所述卧式风选机之间依次设置有提升机、S形振动风选机、上料机,所述S形振动风选机与所述集料关风机连接。Further, a hoist, an S-shaped vibrating air separator, and a feeder are sequentially arranged between the magnetic separator and the horizontal air separator, and the S-shaped vibrating air separator is connected to the aggregate. Fan connection.
进一步地,所述第二步中所述水式吸风破机排出的污水沉淀后,还需要依次通过过滤、脱水步骤获得所述正极材料与石墨的混合物。Furthermore, after the sewage discharged from the water-type air suction breaker in the second step settles, it is necessary to successively pass through the steps of filtration and dehydration to obtain the mixture of the positive electrode material and graphite.
进一步地,所述第二涡分机与所述重介分选机连接,所述重介分选机能够将所述铝箔与所述铜箔分离。Further, the second vortex separator is connected to the dense medium separator, and the dense medium separator can separate the aluminum foil from the copper foil.
本发明相对于现有技术具有以下有益效果:本发明公开的锂电池破碎拆解回收方法,具体包括如下四个步骤,第一步,将带电或不带电的锂电池整体投入水式吸风破机,通过水式吸风破机可以对废弃的锂电池整体进行破碎处理,无需对锂电池进行预拆解处理等程序,可以有效地提高处理效率,且采用水式破碎,可以通过水对破碎过程中丰润锂电池物料进行安全保护,可防止过程中粉尘污染物的产生;第二步,上述步骤融合后的污水沉淀后可分离获得锂电池中正极材料与石墨混合体,并将集料关风机与水式吸风破机连接,可利用集料关风机将锂电池中的塑膜分离;第三步,通过磁选机,对锂电池中的铁材质进行分离;第四步,将破碎后的物料输送至卧式风选机,卧式风选机分选出较轻物质与较重物质。卧式风选机分别与第一涡分机和水式摩擦机连接,较重物质通过第一涡分机处理后可获得塑壳、不锈钢和铝,水式摩擦机依次与筛选机、第二涡分机连接,较轻物质经过水式摩擦机,筛选机可分离获得铝塑包装物,经过第二涡分机处理后可分离获得塑料杂物、铝箔、铜箔,污水经过脱水装置回到沉淀池,进行沉淀得到正极材料与石墨的混合体。Compared with the prior art, the present invention has the following beneficial effects: The lithium battery crushing, dismantling and recycling method disclosed in the present invention specifically includes the following four steps. Machine, the waste lithium battery can be crushed as a whole through the water-type suction crusher, without pre-dismantling the lithium battery and other procedures, which can effectively improve the processing efficiency, and the water-type crushing can be crushed by water During the process, Fengrun lithium battery materials are protected safely to prevent the generation of dust pollutants in the process; in the second step, the sewage after the fusion of the above steps can be separated to obtain the positive electrode material and graphite mixture in the lithium battery, and the aggregate is closed. The fan is connected to the water-type suction crusher, and the plastic film in the lithium battery can be separated by using the aggregate shut-off fan; the third step is to separate the iron material in the lithium battery through a magnetic separator; the fourth step is to crush the The final material is transported to the horizontal winnowing machine, and the horizontal winnowing machine separates the lighter material and the heavier material. The horizontal winnowing machine is respectively connected with the first vortex separator and the water type friction machine. After the heavy material is processed by the first vortex separator, plastic shell, stainless steel and aluminum can be obtained. The water type friction machine is connected with the screening machine and the second vortex separator in turn. Connected, the lighter matter passes through the water friction machine, the screening machine can separate to obtain aluminum-plastic packaging, and after the second vortex separator can separate and obtain plastic debris, aluminum foil, copper foil, the sewage returns to the sedimentation tank through the dehydration device, and is processed Precipitate to obtain a mixture of positive electrode material and graphite.
如此设置,可通过上述流水线式的分离过程,将废弃电池中的有价资源分离回收,能够显著地提高废弃电池的处理质量和处理效率,且可有效地控制处理过程中的污染物排放。With such an arrangement, the valuable resources in waste batteries can be separated and recovered through the above-mentioned pipeline-type separation process, which can significantly improve the treatment quality and efficiency of waste batteries, and can effectively control the discharge of pollutants during the treatment process.
本发明的附加方面和优点将在下面的描述中部分给出,部分将从下面的描述中变得明显,或通过发明的实践了解到。Additional aspects and advantages of the invention will be set forth in part in the description which follows, and in part will be obvious from the description, or may be learned by practice of the invention.
附图说明Description of drawings
图1是本发明实施例的处理流程示意图;Fig. 1 is a schematic diagram of the processing flow of an embodiment of the present invention;
具体实施方式detailed description
以下将结合附图对本发明进行详细说明。The present invention will be described in detail below in conjunction with the accompanying drawings.
结合图1所示,本实施例公开的锂电池破碎拆解回收方法,包括如下步骤:As shown in Figure 1, the lithium battery crushing, dismantling and recycling method disclosed in this embodiment includes the following steps:
第一步,将带电或不带电的锂电池整体投入水式吸风破机中,通过水式吸风破机可以对废弃的锂电池整体进行破碎处理,无需对锂电池进行预拆解处理等程序,相对于现有技术需要对废弃锂电池进行放电和破拆预处理,可以有效地提高处理效率,且采用水式破碎,可以通过水将破碎后的锂电池物料进行融合,可防止过程中粉尘污染物的产生;The first step is to put the charged or uncharged lithium battery into the water-type suction crusher, and the waste lithium battery can be crushed through the water-type suction crusher without pre-dismantling the lithium battery. Compared with the existing technology, it is necessary to discharge and dismantle the waste lithium battery, which can effectively improve the treatment efficiency, and adopts water crushing, which can fuse the crushed lithium battery materials through water, which can prevent the process of generation of dust pollutants;
第二步,水式吸风破机对锂电池进行破碎处理,通过水介质对破碎过程中的锂电池进行安全保护,污水沉淀后,优选地,通过过滤获得下沉物,并对下沉物进行脱水后可获得锂电池中的正极材料与石墨杂物;集料关风机与水式吸风破机连接,通过集料关风机可获得锂电池中的塑膜;优选地,集料关风机还需要依次与引风机、喷淋塔、活性炭塔连接,通过引风机可以将集料关风机中吸入的粉尘等颗粒状污染物及有毒气体排入喷淋塔,喷淋塔可对粉尘等颗粒状污染物进行除尘处理,后续的活性炭塔可以对有毒气体等进行有效地吸附,如此设置,可防止废弃锂电池拆解处理过程中产生的粉尘及有毒气体排放入大气,可避免环境污染;In the second step, the water-type suction crusher crushes the lithium battery, and protects the lithium battery during the crushing process through the water medium. After the sewage is precipitated, preferably, the sinking is obtained by filtration, and the sinking After dehydration, the positive electrode material and graphite impurities in the lithium battery can be obtained; the aggregate shut-off fan is connected to the water-type suction breaker, and the plastic film in the lithium battery can be obtained through the aggregate shut-off fan; preferably, the aggregate shut-off fan It also needs to be connected with the induced draft fan, spray tower, and activated carbon tower in turn. Through the induced draft fan, the dust and other particulate pollutants and toxic gases inhaled by the aggregate fan can be discharged into the spray tower, and the spray tower can treat dust and other particles. The following activated carbon tower can effectively adsorb toxic gases, etc., so that the dust and toxic gases generated during the dismantling process of waste lithium batteries can be prevented from being discharged into the atmosphere, and environmental pollution can be avoided;
第三步,经上述第二步处理后的锂电池碎料输送至磁选机,优选地,在磁选机和水式吸风破机之间还设置有脱水上料机,通过脱水上料机可方便将水式吸风破机处理后的碎料进一步地脱水和上料处理,有助于后序的磁选,通过磁选机可将碎料中的铁分离;In the third step, the lithium battery scraps processed in the second step above are transported to the magnetic separator. Preferably, a dehydration feeding machine is also provided between the magnetic separator and the water-type suction crusher, and the dehydration feeding The machine can facilitate the further dehydration and feeding treatment of the crushed materials processed by the water suction air crusher, which is helpful for the subsequent magnetic separation, and the iron in the crushed materials can be separated through the magnetic separator;
第四步,经上述磁选机处理后的锂电池碎料输送至卧式风选机,优选地,在磁选机与卧式风选机之间还依次设置有提升机、S形振动风选机、上料机,其中S形振动风选机与集料关风机连接,如此设置,可以通过S形振动风选机将锂电池碎料中残留及振动后产生的粉尘和有毒气体经集料关风机后序的引风机、喷淋塔、活性炭塔进行除尘和吸附处理,可进一步地防止粉尘及有毒气体对环境造成污染;卧式风选机分别与第一涡分机和水式摩擦机连接,通过第一涡分机可以将电池碎料中的塑料、不锈钢、铝分离,优选地,通过风选或感应分选机可以将塑料和不锈钢分离;水式摩擦机依次与筛选机、第二涡分机连接,筛选机可以将铝塑包装物进行分离,第二涡分机可以将铜箔、铝箔分离,优选地,通过重介分选机可以将铝箔与铜箔分离,从而实现了有价金属及基质材料的分离回收。In the fourth step, the lithium battery scraps processed by the above-mentioned magnetic separator are transported to the horizontal air separator. Preferably, a hoist, an S-shaped vibrating air separator, and an elevator are arranged in sequence between the magnetic separator and the horizontal air separator. Selecting machine and feeding machine, in which the S-shaped vibrating air separator is connected with the aggregate closing fan, so that the S-shaped vibrating air separator can collect the dust and toxic gas remaining in the lithium battery fragments and generated after vibration. The induced draft fan, spray tower, and activated carbon tower after the material shutdown fan are used for dust removal and adsorption treatment, which can further prevent dust and toxic gases from polluting the environment; Connection, through the first vortex separator, the plastic, stainless steel, and aluminum in the battery scrap can be separated, preferably, the plastic and stainless steel can be separated by air separation or induction sorting machine; the water friction machine is sequentially connected with the screening machine, the second The vortex separator is connected, the screening machine can separate the aluminum-plastic packaging, and the second vortex separator can separate the copper foil and the aluminum foil. And the separation and recovery of matrix materials.
优选地,还包括至少一个供水池,通过供水池可以对水式吸风破机、脱水上料机、水式摩擦机进行供水,同时污水经沉淀过滤后可返还至供水池,实现循环利用。Preferably, at least one water supply pool is also included, through which water can be supplied to the water-type suction breaker, dehydration feeder, and water-type friction machine, and at the same time, the sewage can be returned to the water supply pool after sedimentation and filtration to realize recycling.
本发明对废弃电池在不进行预处理放电情况下整体破碎,然后逐一、梯级自选出相应材料。该流程通过水式吸风破机、磁选机、卧式风选机、水式摩擦机、第一涡分机、第二涡分机等设备将废旧锂电池分选出如塑料、隔膜、不锈钢、铝塑膜、铝、塑料、铜箔、铝箔、石墨等物料,分选纯度可达到94%-99%之间。生产过程中锂电池中的各种有害气体经过喷淋塔、活性炭塔处理进行达标排放,生产过程中所需的水全部进行循环利用,无外排水源,并且水在循环过程中经过沉淀、过滤和添加化学药剂进行水处理。本发明可以拆解各类锂电池,不受形状与电池结构影响,具有拆解效率高,成本低等优点。In the invention, waste batteries are completely broken without pretreatment and discharge, and then corresponding materials are self-selected one by one and step by step. In this process, waste lithium batteries such as plastic, diaphragm, stainless steel, Aluminum-plastic film, aluminum, plastic, copper foil, aluminum foil, graphite and other materials, the separation purity can reach between 94% and 99%. During the production process, various harmful gases in lithium batteries are treated by spray towers and activated carbon towers to meet the discharge standards. All the water required in the production process is recycled. There is no external drainage source, and the water is precipitated and filtered during the circulation process. and adding chemicals for water treatment. The invention can dismantle various lithium batteries without being affected by the shape and structure of the battery, and has the advantages of high dismantling efficiency and low cost.
本发明无需对废弃电池进行预处理,可直接进入破碎、拆解、回收;能够显著地提高废弃电池的处理质量和处理效率,且可有效地控制处理过程中的污染物排放。The invention does not require pretreatment of waste batteries, and can be directly crushed, disassembled, and recycled; can significantly improve the treatment quality and efficiency of waste batteries, and can effectively control the discharge of pollutants during the treatment process.
以上实施例只是对本专利的示例性说明,并不限定它的保护范围,本领域技术人员还可以对其局部进行改变,只要没有超出本专利的精神实质,都在本专利的保护范围内。The above embodiments are only exemplary illustrations of this patent, and do not limit its protection scope. Those skilled in the art can also make partial changes to it, as long as they do not exceed the spirit and essence of this patent, they are all within the protection scope of this patent.
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