JPH08937B2 - Method for recovering silver oxide and metal from used silver oxide button batteries - Google Patents
Method for recovering silver oxide and metal from used silver oxide button batteriesInfo
- Publication number
- JPH08937B2 JPH08937B2 JP7092992A JP7092992A JPH08937B2 JP H08937 B2 JPH08937 B2 JP H08937B2 JP 7092992 A JP7092992 A JP 7092992A JP 7092992 A JP7092992 A JP 7092992A JP H08937 B2 JPH08937 B2 JP H08937B2
- Authority
- JP
- Japan
- Prior art keywords
- silver oxide
- silver
- metal
- cold water
- battery
- Prior art date
- Legal status (The legal status 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 status listed.)
- Expired - Fee Related
Links
Classifications
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
-
- 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
- Manufacture And Refinement Of Metals (AREA)
- Primary Cells (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は使用済みの酸化銀ボタン
電池から酸化銀および金属を回収する方法に関し、特
に、電池外被とその内容物とを物理的に分離して酸化
銀,銀,亜鉛,鉄およびニッケルを回収する方法に関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for recovering silver oxide and metal from a used silver oxide button battery, and more particularly, by physically separating the battery casing and its contents, silver oxide, silver, It relates to a method for recovering zinc, iron and nickel.
【0002】[0002]
【従来の技術】一般に、ボタン電池は酸化銀電池,水銀
電池,リチウム電池,アルカリマンガン電池に分類され
る。このうち、酸化銀電池には酸化銀と銀金属が含ま
れ、電池外被部分は亜鉛,鉄,ニッケルから作られてい
る。このような酸化銀電池はその使用後において酸化
銀,銀その他の金属を回収して再利用することが望まれ
ている。2. Description of the Related Art Button batteries are generally classified into silver oxide batteries, mercury batteries, lithium batteries and alkaline manganese batteries. Among them, the silver oxide battery contains silver oxide and silver metal, and the battery outer covering part is made of zinc, iron and nickel. It is desired that such a silver oxide battery recovers and reuses silver oxide, silver and other metals after use.
【0003】しかしながら現在においては、図3に示す
ように、酸化銀と銀のみが回収されている。すなわち、
電池外被を化学的方法で溶解し(1)、分離して
(2)、固体相の酸化銀および銀を回収し(5)、これ
を乾式精錬(例えば、NaCO3 とCを加えて1000
°Cに加熱するソーダ法)により精錬して95%の粗銀
を得(6)る。その後、粗銀は従来の方法により更に精
錬されて99.99%の純度の銀インゴットにして再売
却されるようにしており(7、8)、液体相に含まれる
銀以外の金属成分は回収されずに捨てられている(3、
4)のが現状である。さらに、前記の銀回収の過程にお
いては、排気や排水が汚染されて深刻な環境問題を引き
起こす問題がある。すなわち、従来から銀回収に用いら
れている方法においては、濃縮された硝酸と塩酸とから
なる王水が電池の外被を溶解するために使用されており
(1)、酸化銀および銀が回収されたあとの排水は強酸
性で環境汚染物質を含み(3,4)、NOx などの排気
ガスを発生する。このように、銀回収における従来の方
法においては非常に環境汚染をともなうものであり、こ
れらの汚染物質を除去し、排水基準に合うように処理す
るのは複雑な技術と多くの費用を要するものとなってい
る。However, at present, as shown in FIG. 3, only silver oxide and silver are recovered. That is,
The cell envelope is chemically dissolved (1) and separated (2) to recover the solid phase silver oxide and silver (5), which is dry smelted (for example, by adding NaCO 3 and C to 1000
Refining by a soda method of heating to ° C) to obtain 95% of crude silver (6). After that, the crude silver is further refined by the conventional method to be re-sold as a silver ingot having a purity of 99.99% (7, 8), and metal components other than silver contained in the liquid phase are recovered. It is thrown away without being (3,
The current situation is 4). Further, in the above-mentioned silver recovery process, there is a problem that exhaust gas and waste water are contaminated and cause serious environmental problems. That is, in the method conventionally used for silver recovery, aqua regia consisting of concentrated nitric acid and hydrochloric acid is used to dissolve the outer coat of the battery (1), and silver oxide and silver are recovered. The wastewater after being treated is strongly acidic and contains environmental pollutants (3, 4), and produces exhaust gas such as NOx. Thus, conventional methods of silver recovery are very environmentally-friendly, and removing these contaminants and treating them to meet effluent standards requires complex techniques and high costs. Has become.
【0004】[0004]
【発明が解決しようとする課題】本発明は前記のような
問題点に鑑みて創案されたものであり、その目的とする
ところは、環境汚染につながる有害物質を生じないよう
にして使用済み酸化銀ボタン電池から酸化銀や銀および
その他の金属を回収し、また、従来は捨てられていた有
価金属を回収することができるようにした、使用済酸化
銀ボタン電池からの酸化銀および金属回収方法を提供す
ることにある。SUMMARY OF THE INVENTION The present invention was made in view of the above-mentioned problems, and its purpose is to prevent the generation of harmful substances that may lead to environmental pollution, and to improve the quality of spent oxidation. A method for recovering silver oxide and metal from used silver oxide button batteries, which enables recovery of silver oxide, silver and other metals from silver button batteries, and recovery of valuable metals that were previously discarded. To provide.
【0005】[0005]
【課題を解決するための手段】本発明は前記の目的を達
成するために、使用済の酸化銀ボタン電池を破壊して破
片とし、前記破片を100°C以上の温度に加熱し乾燥
させ、加熱,乾燥した前記破片を激しく攪拌されている
30°C以下の冷水に移して電池の外被から内容物を剥
離し、剥離された外被と内容物とを含む前記冷水をさら
に固体相と液体相とに分離し、分離された前記固体相か
ら磁気手段により磁性体の鉄およびニッケルと、非磁性
体の酸化銀,銀および亜鉛とを分離して回収する方法に
よるものである。In order to achieve the above-mentioned object, the present invention destroys a used silver oxide button battery into pieces, and heats the pieces to a temperature of 100 ° C or more to dry them.
Is allowed, heating, dry and transferred to the debris to a vigorously stirred 30 ° C below the cold water are stripped jacket from the contents of the cell, the cold water and a stripped jacket and the contents further solid Phase and liquid phase, and from the separated solid phase, magnetic materials such as iron and nickel and non-magnetic materials such as silver oxide, silver and zinc are separated and recovered.
【0006】[0006]
【作 用】先ず、使用済みの電池を機械的な手段で粉砕
して破片とする。次にこの破片を高温に加熱し、直ちに
この加熱された破片を、激しく攪拌されている冷水に移
す。このように、加熱作用と冷却作用を連続させること
により物理的に電池外被からその内容物を簡単に剥離さ
せることができる。ついで、酸化銀,銀,鉄,亜鉛およ
びニッケル等の固体と、それ以外の液体とを分離し、さ
らに、分離された固体から磁気手段により磁性体の鉄お
よびニッケルと非磁性体の酸化銀,銀,亜鉛とを分離す
る。[Operation] First, a used battery is crushed into pieces by mechanical means. The debris is then heated to a high temperature and immediately the heated debris is transferred to vigorously stirred cold water. In this way, by continuing the heating action and the cooling action, the contents can be physically peeled off from the battery casing. Then, solids such as silver oxide, silver, iron, zinc and nickel are separated from other liquids, and further, iron and nickel as magnetic materials and silver oxide as non-magnetic material are separated from the separated solids by magnetic means. Separate from silver and zinc.
【0007】[0007]
【実施例】本発明の一実施例を図1に基づいて説明す
る。先ず、使用済みの酸化銀ボタン電池を例えばボール
ミル等の機械的手段により粉砕して破片とする(9)。
この破片を加熱炉で100°C以上の温度に加熱して
(10)乾燥させ、この破片を、直ちに30°以下の温
度に保たれて激しく攪拌されている冷水に移して急冷す
る(11)。このように、破壊された電池破片を加熱状
態から直ちに冷却状態に移すと、誇張,収縮に基づく物
理作用により、電池外被(鉄,亜鉛,ニッケル)とその
内容物(酸化銀,銀)を簡単に分離させることができ
る。ついで、篩分等の手段により固体相と液体相に分離
したあと(12,13,15)、液体相は廃棄され(1
4)、固体相はさらに磁気分離手段により、磁性体の
鉄,ニッケルと、非磁性体の酸化銀,銀,亜鉛とに磁性
分離する(16,17,19)。鉄とニッケルは精製せ
ずにそのまま売却されて再利用されるが(18)、非磁
性物質のうち亜鉛金属は乾式精錬法により蒸留分離さ
れ、濃縮されて回収され(20,23,24)、残った
酸化銀および銀は従来の方法により精製されて、銀イン
ゴットとして(19〜24)再売却される(22)。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT An embodiment of the present invention will be described with reference to FIG. First, a used silver oxide button battery is crushed into pieces by mechanical means such as a ball mill (9).
This shard is heated in a heating furnace to a temperature of 100 ° C. or higher (10) to be dried, and immediately transferred to chilled water which is kept at a temperature of 30 ° or lower and is vigorously stirred (11). . In this way, when the destroyed battery fragments are immediately transferred from the heated state to the cooled state, the physical action based on exaggeration and contraction causes the battery jacket (iron, zinc, nickel) and its contents (silver oxide, silver) to be removed. It can be easily separated. Then, after separating into a solid phase and a liquid phase by means such as sieving (12, 13, 15), the liquid phase is discarded (1
4), the solid phase is magnetically separated by magnetic separation means into iron and nickel which are magnetic substances and silver oxide, silver and zinc which are non-magnetic substances (16, 17, 19). Iron and nickel are sold and reused as they are without refining (18), but zinc metal among non-magnetic substances is separated by distillation by the dry refining method, concentrated and recovered (20, 23, 24), The remaining silver oxide and silver are purified by conventional methods and resold as silver ingots (19-24) (22).
【0008】次に100グラムの使用済み酸化銀ボタン
電池を実際に処理した例について、図2に基づき説明す
る。すなわち、使用済み酸化銀ボタン電池100グラム
をボールミルで破壊し(25)、この破壊された電池破
片を400°Cの加熱炉で30分間加熱した(26)。
次に、この加熱した電池の破片を直ちに10°Cの冷水
に移すとともにこの冷水を10分間にわたり激しく攪拌
して冷却した(27)。これにより電池外被とその内容
物が分離した。ついで、この電池外被とその内容物が分
離している冷水をメッシュ20の篩によって篩分けし、
82グラムの固体相を得ることができた(28,3
0)。残りの冷水をさらにフィルターにより濾過して1
8グラムの固体相を取り出し、濾液としての冷水は0.
1ppm 以下の銀含有率で、そのまま廃棄した(29,3
1,33,34,35)。このようにして回収された1
00グラムの固体(篩からの82グラムとフィルターか
らの18グラム)を磁気手段を利用して磁性物質と非磁
性物質とに磁性分離し、磁性体の鉄およびニッケル5
9.2グラムと、非磁性体の酸化銀と銀および亜鉛4
0.8グラムを得た。このようにして回収された酸化
銀,銀,その他の金属は従来の方法により精製され、あ
るいはそのまま売却され、再利用されるようにした。上
記のように、電池破片の加熱を、特に、400°Cで3
0分間とし、亜鉛を溶融することなく高い温度に保持す
ることにより、また、加熱破片の冷却を、特に、10°
C以下の冷水で10分間の攪拌条件で行うことにより、
急冷による誇張収縮に基づく物理的効果を利用して効率
的に外被から内容物を剥離できるものである。最後に本
発明の利点を、外被を溶融する従来の化学的方法と比較
した表を掲げる。Next, an example in which a 100-gram used silver oxide button battery is actually processed will be described with reference to FIG. That is, 100 grams of a used silver oxide button battery was broken by a ball mill (25), and the broken battery fragments were heated in a heating furnace at 400 ° C for 30 minutes (26).
The heated cell fragments were then immediately transferred to 10 ° C. cold water and the cold water was vigorously stirred and cooled for 10 minutes (27). This separated the battery envelope and its contents. Then, the cold water in which the battery casing and its contents are separated is sieved by a sieve of mesh 20,
82 g of solid phase could be obtained (28,3
0). Filter the remaining cold water through a filter and
8 grams of solid phase was removed and the cold water as filtrate was 0.
With a silver content of less than 1 ppm, it was discarded as it was (29,3
1, 33, 34, 35). 1 collected in this way
00 grams of solids (82 grams from the sieve and 18 grams from the filter) were magnetically separated into magnetic and non-magnetic materials using magnetic means, and magnetic materials iron and nickel 5
9.2 grams, non-magnetic silver oxide and silver and zinc 4
I got 0.8 grams. The silver oxide, silver, and other metals thus recovered were refined by a conventional method, or sold as they were for reuse. As mentioned above, heating the cell debris, especially at 400 ° C.
By keeping the zinc at a high temperature for 0 minutes without melting it, the cooling of the heating debris is also increased, especially at 10 °
By performing the stirring condition with cold water of C or lower for 10 minutes,
The contents can be efficiently peeled from the outer cover by utilizing the physical effect based on the exaggerated shrinkage caused by the rapid cooling. Finally, a table is provided which compares the advantages of the present invention with conventional chemical methods of melting jackets.
【0009】[0009]
【表1】 [Table 1]
【0010】[0010]
【発明の効果】以上説明のように、本発明によれば、使
用済み酸化銀ボタン電池を機械的に破壊して破片とし、
この破片を加熱したのち激しく攪拌されている冷水に移
して外被からその内容物を剥離して固体相を回収し、さ
らに磁気手段により磁性体金属と非磁性体金属とに分離
するようにしたので、従来のような科学的な処理を行う
場合のような汚染された排水や排気ガス等の有害物質を
排出せず、したがって環境汚染の問題が生ぜず、また、
従来においては捨てられていた有価金属を回収して再利
用することを可能とする、使用済酸化銀ボタン電池から
の酸化銀および金属回収方法とすることができる。ま
た、機械的に破壊されて加熱された破片は、激しく攪拌
されている冷水に移されるが、このように、加熱された
破片を単に冷水に投入して急冷するにとどまらず、当該
冷水を予め激しく攪拌しておくことにより、加熱した破
片の投入によって冷水の温度が一時的あるいは局所的に
上昇するのを避けることができる。したがって、破片の
冷却を速やかに行うことができて急冷による前記剥離を
確実かつ効率的に行うことができる。さらに、冷水を激
しく攪拌することによって、前記温度差による剥離とは
別に、あるいは、前記温度差による剥離と相まって、冷
水中における破片どうしの接触,衝突が発生することか
ら、前記剥離をより一層確実かつ効率的に行うことがで
きるようになる。As described above, according to the present invention, a used silver oxide button battery is mechanically broken into pieces,
The solid phase was recovered by stripping its contents from the outside and transferred to cold water being vigorously stirred After heating the pieces, it was to separate into a non-magnetic metal and a magnetic metal by further magnetic means Therefore, it does not emit polluted wastewater and harmful substances such as exhaust gas as in the case of performing conventional scientific treatment, and therefore does not cause a problem of environmental pollution, and
A method of recovering silver oxide and a metal from a used silver oxide button battery, which makes it possible to recover and reuse a valuable metal that has been conventionally discarded. Well
In addition, mechanically destroyed and heated debris is stirred vigorously.
Is transferred to cold water, but is thus heated
In addition to simply putting the debris into cold water to quench it,
If cold water is stirred vigorously in advance, the
The temperature of cold water is temporarily or locally increased by adding one piece.
You can avoid rising. Therefore, of debris
Cooling can be done quickly and the peeling caused by rapid cooling
It can be performed reliably and efficiently. In addition, cold water
What is the peeling due to the temperature difference by stirring vigorously
Separately, or in combination with the peeling due to the temperature difference,
Whether debris will come into contact or collide in water
Therefore, the peeling can be performed more reliably and efficiently.
Will be able to
【図1】本発明の一実施例の工程を示すフローチャート
である。FIG. 1 is a flowchart showing steps of an embodiment of the present invention.
【図2】100グラムの使用済み酸化銀ボタン電池を実
際に処理した例についての工程を示すフローチャートで
ある。FIG. 2 is a flow chart showing steps for an example of actual processing of 100 grams of used silver oxide button battery.
【図3】従来例における化学的処理工程を示すフローチ
ャートである。FIG. 3 is a flowchart showing a chemical treatment process in a conventional example.
9・・粉砕 10・加熱(100°C以上) 11・冷却(激しく攪拌。30°C以下) 12・分離 16・磁性分離 9 ・ ・ Pulverization 10 ・ Heating (100 ° C or higher) 11 ・ Cooling (vigorous stirring; 30 ° C or lower) 12 ・ Separation 16 ・ Magnetic separation
───────────────────────────────────────────────────── フロントページの続き (72)発明者 李 伯興 中華民国(台湾) 新竹県竹東鎮中興路4 段195号64館 (56)参考文献 特開 昭63−24560(JP,A) 特開 昭51−69261(JP,A) 特開 昭57−152433(JP,A) 特開 平2−209433(JP,A) 特開 平2−290928(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Lee Haoxing, Republic of China (Taiwan) Zhongxing Road, Zhongxing Town, Hsinchu County, No. 195, 64th Building, No. 64 (56) References JP-A-63-24560 (JP, A) Kai 51-69261 (JP, A) JP 57-152433 (JP, A) JP 2-209433 (JP, A) JP 2-290928 (JP, A)
Claims (1)
片とし、 前記破片を100°C以上の温度に加熱し乾燥させ、 加熱,乾燥した前記破片を激しく攪拌されている30°
C以下の冷水に移して電池の外被から内容物を剥離し、 剥離された外被と内容物とを含む前記冷水をさらに固体
相と液体相とに分離し、 分離された前記固体相から磁気手段により磁性体の鉄お
よびニッケルと、非磁性体の酸化銀,銀および亜鉛とを
分離して回収することを特徴とする使用済酸化銀ボタン
電池からの酸化銀および金属回収方法。1. A used silver oxide button battery is broken into pieces, and the pieces are heated to a temperature of 100 ° C. or higher and dried, and the heated and dried pieces are vigorously stirred at 30 °.
The contents are peeled from the battery casing by transferring to cold water of C or lower, and the cold water containing the peeled casing and contents is further separated into a solid phase and a liquid phase, A method for recovering silver oxide and metal from a used silver oxide button battery, characterized in that magnetic materials such as iron and nickel are separated from non-magnetic materials such as silver oxide, silver and zinc.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7092992A JPH08937B2 (en) | 1992-03-27 | 1992-03-27 | Method for recovering silver oxide and metal from used silver oxide button batteries |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7092992A JPH08937B2 (en) | 1992-03-27 | 1992-03-27 | Method for recovering silver oxide and metal from used silver oxide button batteries |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH05287393A JPH05287393A (en) | 1993-11-02 |
| JPH08937B2 true JPH08937B2 (en) | 1996-01-10 |
Family
ID=13445698
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7092992A Expired - Fee Related JPH08937B2 (en) | 1992-03-27 | 1992-03-27 | Method for recovering silver oxide and metal from used silver oxide button batteries |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH08937B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012038572A (en) * | 2010-08-06 | 2012-02-23 | Sumitomo Metal Mining Co Ltd | Method of peeling positive electrode active material and method of recovering valuable metal from a lithium ion battery |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5169261A (en) * | 1974-11-11 | 1976-06-15 | Japan Metals & Chem Co Ltd | Jukabutsuno kaishuhoho |
| JPS57152433A (en) * | 1981-03-17 | 1982-09-20 | Daido Metal Kogyo Kk | Separating and recovering method for layered material from multilayered material |
| AT386512B (en) * | 1986-01-08 | 1988-09-12 | Hartjes Rudolf | SHOE, ESPECIALLY SPORTSHOE |
| JPH02209433A (en) * | 1989-02-09 | 1990-08-20 | Tanaka Kikinzoku Kogyo Kk | Method for recovering plantinum group metal from metallic carrier catalyst |
| JPH02290928A (en) * | 1989-04-27 | 1990-11-30 | Toshiba Corp | Method for disjointing mold apparatus |
-
1992
- 1992-03-27 JP JP7092992A patent/JPH08937B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH05287393A (en) | 1993-11-02 |
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