TWM603622U - Battery recycling equipment - Google Patents

Battery recycling equipment Download PDF

Info

Publication number
TWM603622U
TWM603622U TW109203945U TW109203945U TWM603622U TW M603622 U TWM603622 U TW M603622U TW 109203945 U TW109203945 U TW 109203945U TW 109203945 U TW109203945 U TW 109203945U TW M603622 U TWM603622 U TW M603622U
Authority
TW
Taiwan
Prior art keywords
battery
battery recycling
tank
grinding wheel
crusher
Prior art date
Application number
TW109203945U
Other languages
Chinese (zh)
Inventor
李駿恒
Original Assignee
李駿恒
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 李駿恒 filed Critical 李駿恒
Priority to TW109203945U priority Critical patent/TWM603622U/en
Publication of TWM603622U publication Critical patent/TWM603622U/en

Links

Images

Classifications

    • 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

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Primary Cells (AREA)

Abstract

本新型之電池回收設備,用於分解多個電池,該電池回收設備包括一馬達、一槽體、一低溫材料、一壓碎機及一研磨砂輪。電池被投入槽體內。低溫材料用以急速冷凍該電池。壓碎機用以擠壓急速冷凍後的電池。研磨砂輪是連結該馬達,研磨砂輪用以研磨急速冷凍後的該電池。其中,低溫材料的溫度不高於-40°C。The battery recycling equipment of the present invention is used to decompose multiple batteries. The battery recycling equipment includes a motor, a tank, a low temperature material, a crusher and a grinding wheel. The battery is put into the tank. The low temperature material is used to rapidly freeze the battery. The crusher is used to squeeze the rapidly frozen battery. The grinding wheel is connected to the motor, and the grinding wheel is used to grind the rapidly frozen battery. Among them, the temperature of low-temperature materials is not higher than -40°C.

Description

電池回收設備Battery recycling equipment

本新型是關於一種電池回收設備,特別是一種具有低溫材料的電池回收設備。The new model relates to a battery recycling equipment, especially a battery recycling equipment with low-temperature materials.

現今鋰電池回收技術分為乾式處理(乾式冶金法)與濕式處理(濕法冶金法)兩大類,主要對正極極板中的鋰、鈷、鎳、錳等金屬元素進行萃取提煉。 請參閱圖1A,圖1A所繪示為乾式冶金法的方塊示意圖,乾式冶金法是將廢鋰電池從回收站收集回來後,先依照電池組或電池芯的大小以及種類先行分組,再以高溫的方式進行熔融燒結後回收。尚未放電完全的鋰電池則先行放電程序,並先使用人工拆除電池金屬結構及去除外殼,直到剩下電池芯。之後,才會再進行切割電池芯的程序,該放電程序能夠避免在焚燒處理時因為熱解而燃燒或爆炸的危險性。經過放電去殼及切割處理後的電池芯則被導入焚化爐中,進行高溫約700~800℃處理。在處理過程中,藉由熔點及比重的差異,分別將Co、Ni、Fe、Al等金屬回收。而鋰金屬則是以氧化鋰(Li2O)的形式逸出,然後再與水(H2O)、碳酸鈉(Na2CO3)反應形成碳酸鋰(Li2CO3)予以回收。然而,由於電池芯本身的硬度頗高,所以在切割的程序中需消耗極大的能量,每平方公分施以200~300焦耳的能量。並且,使用火源加熱的方式會降低有用物質的回收率,也容易形成爆炸起火的情況及產生有毒的氣體。 請參閱圖1B,圖1B所繪示為濕式冶金法的方塊示意圖,濕式冶金法主要是以無機酸溶液作為處理液,將廢電池中欲回收之成分進行萃取後再予以純化回收。濕式冶金法與乾式冶金法一樣需先將鋰電池組經過放電處理、去殼及切割程序。之後,將電池芯碎片放進吸收室再以無機酸溶液噴灑。之後,將鋰電池所含之電解液和鋰金屬成分(鋰鹽溶液)予以萃取吸收,而其餘的殘渣則依照各種金屬之特性不同進行分離,純化後供再生使用。然而,在濕法冶金法的作業之前,需要大量人工將電池芯本體與其他附屬組件分拆開來,且濕法冶金法也會消耗大量化學藥劑。並且,由於鋰電池經由大量無機酸溶液的噴灑,所以其所產生的廢棄物屬於高汙染物,需再進行處理後才能丟棄。 因此,如何設計一種能改善上述的問題,便是本領域具有通常知識者值得去思量地。 Nowadays, lithium battery recycling technologies are divided into two categories: dry treatment (dry metallurgy) and wet treatment (hydrometallurgy). They mainly extract and refine metal elements such as lithium, cobalt, nickel, and manganese in the positive electrode plate. Please refer to Figure 1A. Figure 1A shows a schematic block diagram of dry metallurgy. After the dry metallurgy is collected from the recycling station, the waste lithium batteries are first grouped according to the size and type of the battery pack or battery cell, and then the high temperature It is recycled after melting and sintering. Lithium batteries that have not been fully discharged are discharged first, and the metal structure of the battery and the outer casing are manually removed until the battery core is left. After that, the battery cell cutting procedure will be carried out. This discharge procedure can avoid the danger of burning or explosion due to pyrolysis during incineration. The battery core after discharge shelling and cutting is introduced into the incinerator and processed at a high temperature of about 700~800℃. During the treatment process, metals such as Co, Ni, Fe, Al, etc. are respectively recovered by the difference in melting point and specific gravity. The lithium metal escapes in the form of lithium oxide (Li2O), and then reacts with water (H2O) and sodium carbonate (Na2CO3) to form lithium carbonate (Li2CO3) for recovery. However, due to the high hardness of the battery cell itself, it consumes a lot of energy during the cutting process, applying 200-300 joules of energy per square centimeter. In addition, the use of a fire source for heating will reduce the recovery rate of useful substances, and it is also easy to cause explosions and fires and produce toxic gases. Please refer to Fig. 1B. Fig. 1B shows a schematic block diagram of the hydrometallurgical method. The hydrometallurgical method mainly uses an inorganic acid solution as a treatment liquid, and extracts the components to be recovered in the waste battery before purifying and recycling. The wet metallurgy method and the dry metallurgy method require the discharge treatment, shelling and cutting procedures of the lithium battery. After that, put the battery core fragments into the absorption chamber and spray with inorganic acid solution. After that, the electrolyte and lithium metal components (lithium salt solution) contained in the lithium battery are extracted and absorbed, and the remaining residues are separated according to the characteristics of various metals, and purified for regeneration. However, before the operation of the hydrometallurgical method, a large amount of manual labor is required to separate the battery core body from other auxiliary components, and the hydrometallurgical method also consumes a lot of chemicals. In addition, because lithium batteries are sprayed with a large amount of inorganic acid solutions, the waste generated by them is highly pollutant and needs to be processed before being discarded. Therefore, how to design a solution that can improve the above-mentioned problems is worth considering for those with ordinary knowledge in this field.

本新型之目的在於提供一電池回收設備,該電池回收設備能降低能量的消耗,提高有用物質的回收率,也不會產生高汙染物危害生態環境。 本新型之電池回收設備是用於分解多個電池,電池回收設備包括一馬達、一槽體、一低溫材料、一壓碎機及一研磨砂輪。其中,電池被投入該槽體內。低溫材料是用以急速冷凍該電池。壓碎機是用以擠壓急速冷凍後的該電池。研磨砂輪是連結該馬達,研磨砂輪用以研磨急速冷凍後的該電池。其中,低溫材料的溫度不高於-40°C。 在上述之電池回收設備,其中低溫材料可為氮氣、氦氣或乾冰。 在上述之電池回收設備,其中,該壓碎機以大於每平方公分4~6焦耳的能量擠壓該電池。 在上述之電池回收設備,還包括一推移機構,當壓碎機擠壓該電池後,該推移機構用以推移該電池。 為讓本之上述特徵和優點能更明顯易懂,下文特舉較佳實施例,並配合所附圖式,作詳細說明如下。 The purpose of the present invention is to provide a battery recycling device, which can reduce energy consumption, increase the recovery rate of useful substances, and will not produce high pollutants to harm the ecological environment. The battery recycling equipment of the present invention is used to decompose multiple batteries. The battery recycling equipment includes a motor, a tank, a low temperature material, a crusher and a grinding wheel. Among them, the battery is put into the tank. Low temperature materials are used to quickly freeze the battery. The crusher is used to squeeze the rapidly frozen battery. The grinding wheel is connected to the motor, and the grinding wheel is used to grind the rapidly frozen battery. Among them, the temperature of low-temperature materials is not higher than -40°C. In the above battery recycling equipment, the low temperature material can be nitrogen, helium or dry ice. In the above battery recycling equipment, wherein the crusher squeezes the battery with an energy greater than 4-6 joules per square centimeter. The aforementioned battery recycling equipment further includes a pushing mechanism. After the battery is squeezed by the crusher, the pushing mechanism is used to push the battery. In order to make the above-mentioned features and advantages of the present invention more obvious and understandable, a detailed description is given below of preferred embodiments in conjunction with the accompanying drawings.

請參閱圖2A及圖2B,圖2A所繪示為本實施例之電池回收方法20的流程圖,圖2B所繪示為本實施例之電池回收設備10的示意圖。本實施例之電池回收方法20及電池回收設備10 是用於分解及回收多個電池8,電池8的種類例如為磷酸鐵鋰電池、錳酸鋰電池或三元鋰電池。上述中,本案回收方法是以回收電池8為主。然而,本領域通常知識者能得知,本案回收方法也能用於分解及回收多個電池組(該電池組包括電芯、電路板及保護板)或多個電芯。 請再參閱圖2B,本實施例之電池回收設備10包括一馬達13、一槽體12、一低溫材料16、一壓碎機15、一研磨砂輪14及一推移機構17,馬達13是連結研磨砂輪,推移機構17是設置在槽體12的其中一側,而研磨砂輪14是設置於槽體12內,槽體12包括一導入孔120,低溫材料16是經由導入孔120灌入槽體12內,低溫材料16的溫度不高於-40°C,低溫材料16例如為氮氣、氦氣或乾冰。 值得注意的是,本實施例之電池回收方法20是配合本實施例之電池回收設備10而運行,電池回收方法20包括下列步驟。 首先,請參閱步驟S21,提供多個電池8,這些電池8都是要廢棄回收的電池、電池組或電芯。 之後,請參閱步驟S21,依照電池8的體積大小及種類進行分組。具體來說,體積較大的電池8會被分成一組,而體積較小的電池8會被分成另一組。並且,在依據不同的種類進行分組,例如:磷酸鐵鋰電池屬於第一組、錳酸鋰電池屬於第二組及三元鋰電池屬於第三組。如此一來,有利於後續的篩選或回收出相接近的物質材料。 之後,請參閱步驟S23,將分組後的電池8投入電池回收設備10的槽體12內。舉例來說,先將第三組的三元鋰電池投入於槽體12。 之後,請參閱步驟S24,將低溫材料16投入槽體12以急速冷凍電池8。詳細來說,使用未回溫或正在回溫中的工業氮氣、氦氣或乾冰從導入孔120灌入槽體12內,靜置半小時後,低溫材料16會慢慢回溫(從-192°C上升至-40°C),以讓槽體12內的低溫擴散到電池8內部的電芯。如此一來,電池8的電芯無法輸出電力(在-40°C~-60°C之間,電芯可輸出的電量為零),所以能在後續的步驟中安全的破壞電池8。 之後,請參閱步驟S25,將急速冷凍後的電池8進行擠壓及研磨。詳細來說,當電池8的溫度低于Tk(韌脆臨界轉變溫度)時,其組成材料可接收沖擊與吸收能量的韌性明顯下降,電池8由韌性狀態變為脆性狀態。因此,相較於傳統的切割程序中需消耗極大的能量(200~300焦耳),本實施例的壓碎機15只需大於每平方公分4~6焦耳的能量去擠壓電池8,便能破壞電池8的結構。之後,推移機構用以推移被破壞結構的電池8,以使被破壞結構的電池8移動至研磨砂輪14的表面上。之後,在馬達13快速轉動下,研磨砂輪14會研磨被破壞結構的電池8。這樣一來,電池8將碎裂成多個碎塊,且該碎塊的長度約為2~3mm或大於3mm 。 之後,當電池8碎裂成多個小碎塊後,便能進行篩選材料的程序或研磨成更小的材料粉末讓冶金工廠進行後續的處理。 綜上,由於電池回收方法20沒有加化學藥劑,所以其產生的廢料只需簡單篩選和分離即可。 此外,電池回收方法20也沒有使用火源加熱,所以能提高電池8內的有用物質的回收率。並且,在沒有使用火源加熱的情況下,電池8也不會產生爆炸起火的情形,便不會產生有毒氣體,更不會減損材料(部分材料可能被高溫燒掉,比如塑料)。 請參閱圖3,圖3所繪示為另一實施例之電池回收方法30的流程圖。電池回收方法30與電池回收方法20的差異在於:電池回收方法30還包括一加水回溫的程序,請參閱步驟S36,當電池8進行擠壓及研磨後,將一水溶液加入槽體12內。這樣一來,槽體12內會回溫到0°C或室內溫度以使電池8的碎塊增加材料的破碎程度,而『水』於收集後,可以針對電解液再施以回收處理。並且,該水溶液能大幅降低電解液在回收料當中的Ph值並帶走殘留材料的酸性溶液,降低環境的危害。值得注意的是,步驟S36非絕對必要程序,其唯一好處是加速回到室溫,然後接續下一個工作程序。 綜上所述,本實施例之電池回收方法20配合電池回收設備10能降低能量的消耗,提高有用物質的回收率,也不會產生高汙染物危害生態環境。此外,由於電池回收方法20是採急冷的方法,所以處理的時程非常的短,能達到大幅減少人力投入、提高分解電池的安全度,擁有高的投入、產出率以及材料回收率。 雖然本新型已以較佳實施例揭露如上,然其並非用以限定本新型,任何所屬技術領域中具有通常知識者,在不脫離本新型之精神和範圍內,當可作些許之更動與潤飾,因此本新型之保護範圍當視後附之申請專利範圍所界定者為準。 Please refer to FIGS. 2A and 2B. FIG. 2A shows a flowchart of the battery recycling method 20 of this embodiment, and FIG. 2B shows a schematic diagram of the battery recycling device 10 of this embodiment. The battery recycling method 20 and the battery recycling device 10 of this embodiment are used for decomposing and recycling a plurality of batteries 8. The types of the batteries 8 are, for example, lithium iron phosphate batteries, lithium manganese oxide batteries, or ternary lithium batteries. Among the above, the recovery method in this case is mainly to recover the battery 8. However, those skilled in the art can know that the recycling method of this case can also be used to decompose and recycle multiple battery packs (the battery pack includes battery cells, circuit boards, and protective boards) or multiple battery cells. Please refer to FIG. 2B again. The battery recycling device 10 of this embodiment includes a motor 13, a tank 12, a low-temperature material 16, a crusher 15, a grinding wheel 14 and a pushing mechanism 17. The motor 13 is connected to grinding The grinding wheel, the pushing mechanism 17 is arranged on one side of the tank body 12, and the grinding wheel 14 is arranged in the tank body 12. The tank body 12 includes an introduction hole 120, and the low temperature material 16 is poured into the tank body 12 through the introduction hole 120 In addition, the temperature of the low-temperature material 16 is not higher than -40°C, and the low-temperature material 16 is, for example, nitrogen, helium, or dry ice. It is worth noting that the battery recycling method 20 of this embodiment runs in conjunction with the battery recycling device 10 of this embodiment, and the battery recycling method 20 includes the following steps. First, referring to step S21, a plurality of batteries 8 are provided, and these batteries 8 are all batteries, battery packs or batteries to be discarded and recycled. After that, referring to step S21, the batteries 8 are grouped according to their size and type. Specifically, the battery 8 with a larger volume is divided into one group, and the battery 8 with a smaller volume is divided into another group. In addition, they are grouped according to different types. For example, lithium iron phosphate batteries belong to the first group, lithium manganate batteries belong to the second group, and ternary lithium batteries belong to the third group. In this way, it is beneficial to subsequent screening or recovery of similar materials. After that, referring to step S23, put the grouped batteries 8 into the tank 12 of the battery recovery device 10. For example, first put the third group of ternary lithium batteries into the tank 12. After that, referring to step S24, the low-temperature material 16 is put into the tank 12 to rapidly freeze the battery 8. In detail, use industrial nitrogen, helium or dry ice that has not been warmed up or is being warmed up into the tank 12 from the inlet 120. After standing for half an hour, the low-temperature material 16 will slowly warm up (from -192 °C to -40°C) to allow the low temperature in the tank 12 to diffuse to the cells inside the battery 8. As a result, the cells of the battery 8 cannot output power (between -40°C and -60°C, the power that the cells can output is zero), so the battery 8 can be safely destroyed in the subsequent steps. After that, referring to step S25, the rapidly frozen battery 8 is squeezed and ground. In detail, when the temperature of the battery 8 is lower than Tk (the critical transition temperature between toughness and brittleness), the toughness of its constituent materials that can receive impact and absorb energy is significantly reduced, and the battery 8 changes from a tough state to a brittle state. Therefore, compared to the traditional cutting procedure that consumes a lot of energy (200~300 joules), the crusher 15 of this embodiment only needs more than 4~6 joules per square centimeter to squeeze the battery 8, and it can The structure of the battery 8 is destroyed. After that, the pushing mechanism is used to push the battery 8 of the destroyed structure, so that the battery 8 of the destroyed structure is moved to the surface of the grinding wheel 14. After that, under the rapid rotation of the motor 13, the grinding wheel 14 will grind the battery 8 with the damaged structure. In this way, the battery 8 will be broken into a plurality of fragments, and the length of the fragments is about 2 to 3 mm or greater than 3 mm. After that, when the battery 8 is broken into a plurality of small pieces, the material can be screened or ground into smaller material powder for subsequent processing by the metallurgical factory. In summary, since the battery recycling method 20 does not add chemicals, the waste generated by it only needs to be simply screened and separated. In addition, the battery recovery method 20 does not use fire source heating, so the recovery rate of useful substances in the battery 8 can be improved. In addition, without using a fire source for heating, the battery 8 will not explode or catch fire, will not generate toxic gases, and will not degrade materials (some materials may be burned at high temperatures, such as plastic). Please refer to FIG. 3, which shows a flowchart of a battery recycling method 30 according to another embodiment. The difference between the battery recycling method 30 and the battery recycling method 20 is that the battery recycling method 30 also includes a process of adding water to warm up. Please refer to step S36. After the battery 8 is squeezed and ground, an aqueous solution is added to the tank 12. In this way, the inside of the tank body 12 will be warmed to 0°C or room temperature to make the fragments of the battery 8 increase the degree of material fragmentation, and the "water" can be recycled for the electrolyte after being collected. Moreover, the aqueous solution can greatly reduce the Ph value of the electrolyte in the recovered material and take away the acidic solution of the residual material, reducing environmental hazards. It is worth noting that step S36 is not an absolutely necessary procedure, and its only advantage is to accelerate the return to room temperature, and then continue the next working procedure. In summary, the battery recycling method 20 of this embodiment and the battery recycling device 10 can reduce energy consumption, increase the recovery rate of useful substances, and will not produce high pollutants that harm the ecological environment. In addition, since the battery recovery method 20 is a rapid cooling method, the processing time is very short, which can greatly reduce manpower input, improve the safety of disassembling batteries, and have high input, output and material recovery rates. Although the present invention has been disclosed in the preferred embodiments as above, it is not intended to limit the present invention. Anyone with ordinary knowledge in the relevant technical field can make some changes and modifications without departing from the spirit and scope of the present invention. Therefore, the scope of protection of this new model shall be subject to the scope of the attached patent application.

8:電池 10:電池回收設備 12:槽體 120:導入孔 13:馬達 14:研磨砂輪 15:壓碎機 16:低溫材料 17:推移機構 20、30:電池回收方法 S21~S25:步驟 S36:步驟 8: battery 10: Battery recycling equipment 12: tank 120: lead-in hole 13: Motor 14: Grinding wheel 15: Crusher 16: Low temperature materials 17: Moving agency 20, 30: Battery recycling method S21~S25: steps S36: Step

圖1A所繪示為乾式冶金法的方塊示意圖。 圖1B所繪示為濕式冶金法的方塊示意圖。 圖2A所繪示為本實施例之電池回收方法20的流程圖。 圖2B所繪示為本實施例之電池回收設備10的示意圖。 圖3所繪示為另一實施例之電池回收方法30的流程圖。 Figure 1A shows a block diagram of the dry metallurgy method. Figure 1B shows a block diagram of the hydrometallurgical method. FIG. 2A shows a flowchart of the battery recycling method 20 of this embodiment. FIG. 2B shows a schematic diagram of the battery recycling device 10 of this embodiment. FIG. 3 shows a flowchart of a battery recycling method 30 according to another embodiment.

8:電池 8: battery

10:電池回收設備 10: Battery recycling equipment

12:槽體 12: tank

120:導入孔 120: lead-in hole

13:馬達 13: Motor

14:研磨砂輪 14: Grinding wheel

15:壓碎機 15: Crusher

16:低溫材料 16: Low temperature materials

17:推移機構 17: Moving agency

Claims (4)

一種電池回收設備,用於分解多個電池,該電池回收設備包括: 一馬達; 一槽體,該電池被投入該槽體內; 一低溫材料,用以急速冷凍該電池; 一壓碎機,用以擠壓急速冷凍後的該電池;及 一研磨砂輪,連結該馬達,該研磨砂輪用以研磨急速冷凍後的該電池; 其中,該低溫材料的溫度不高於-40°C。 A battery recycling device is used to decompose multiple batteries. The battery recycling device includes: A motor A tank, the battery is put into the tank; A low-temperature material to quickly freeze the battery; A crusher for squeezing the rapidly frozen battery; and A grinding wheel connected to the motor, the grinding wheel is used to grind the battery after the rapid freezing; Among them, the temperature of the low-temperature material is not higher than -40°C. 如申請專利範圍第1項所述之電池回收設備,其中該低溫材料為氮氣、氦氣或乾冰。In the battery recycling equipment described in item 1 of the scope of patent application, the low-temperature material is nitrogen, helium or dry ice. 如申請專利範圍第1項所述之電池回收設備,其中,該壓碎機以大於每平方公分4~6焦耳的能量擠壓該電池。The battery recycling device described in item 1 of the scope of patent application, wherein the crusher squeezes the battery with an energy greater than 4-6 joules per square centimeter. 如申請專利範圍第1項所述之電池回收設備,還包括一推移機構,當該壓碎機擠壓該電池後,該推移機構用以推移該電池。The battery recycling device described in item 1 of the scope of the patent application further includes a pushing mechanism. After the crusher squeezes the battery, the pushing mechanism is used to push the battery.
TW109203945U 2020-04-06 2020-04-06 Battery recycling equipment TWM603622U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
TW109203945U TWM603622U (en) 2020-04-06 2020-04-06 Battery recycling equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
TW109203945U TWM603622U (en) 2020-04-06 2020-04-06 Battery recycling equipment

Publications (1)

Publication Number Publication Date
TWM603622U true TWM603622U (en) 2020-11-01

Family

ID=74203191

Family Applications (1)

Application Number Title Priority Date Filing Date
TW109203945U TWM603622U (en) 2020-04-06 2020-04-06 Battery recycling equipment

Country Status (1)

Country Link
TW (1) TWM603622U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2022224264A1 (en) * 2021-04-23 2022-10-27 Batx Energies Pvt Ltd A method for recycling of used scrap lithium battery

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2022224264A1 (en) * 2021-04-23 2022-10-27 Batx Energies Pvt Ltd A method for recycling of used scrap lithium battery

Similar Documents

Publication Publication Date Title
Zhong et al. Pretreatment for the recovery of spent lithium ion batteries: theoretical and practical aspects
CN111495925B (en) Method for pyrolyzing and defluorinating chlorine of waste lithium battery
CN102017276A (en) Reutilization method of a waste LiFeP04 power battery
Yi et al. Technology for recycling and regenerating graphite from spent lithium-ion batteries
CN110061320A (en) A method of utilizing active powder material in cracking process recycling waste power lithium battery
CN107623152B (en) Applying waste lithium ionic power battery resource recycle method
KR102447931B1 (en) Eco-friendly recycling method for wasted battery
CN108933307A (en) A kind of method of low temperature comprehensive reutilization waste lithium ion
CN107275700A (en) A kind of waste and old lithium ion battery recovery and treatment method crushed based on wet type
CA2311792A1 (en) Method for crushing cell
CN111029677A (en) Inactivation treatment method before crushing of waste charged soft package lithium ion battery
CN108808156B (en) Method for recovering electrolyte in waste lithium ion battery
KR20110046938A (en) Recycling apparatus and method of the waste lithium battery
CN107069134A (en) A kind of method that waste lithium cell positive electrode is separated with collector
WO2023005430A1 (en) Waste lithium battery recycling pyrolysis temperature control method and application
CN107240732A (en) A kind of stripping means of positive material of waste lithium iron phosphate and collector
JP2016207648A (en) Processing method of lithium ion battery
CN105895854A (en) Recovery method of positive electrode leftover material of lithium-ion battery
CN112909370A (en) Method for repairing ternary cathode material in waste lithium battery
KR100860972B1 (en) Safe method for dismantling spent lithium-ion secondary batteries
CN113067028A (en) Recycling method of lithium iron phosphate retired lithium ion battery
CN114151802A (en) Method for recycling all components of waste lithium battery
TWM603622U (en) Battery recycling equipment
CN112934373A (en) Machine is retrieved to smokeless environment-friendly lithium cell
CN112201872B (en) Safe discharge method and wet physical sorting method for retired batteries

Legal Events

Date Code Title Description
MM4K Annulment or lapse of a utility model due to non-payment of fees