JPS61488A - Apparatus for treating waste dry battery - Google Patents
Apparatus for treating waste dry batteryInfo
- Publication number
- JPS61488A JPS61488A JP59120943A JP12094384A JPS61488A JP S61488 A JPS61488 A JP S61488A JP 59120943 A JP59120943 A JP 59120943A JP 12094384 A JP12094384 A JP 12094384A JP S61488 A JPS61488 A JP S61488A
- Authority
- JP
- Japan
- Prior art keywords
- chute
- recovered
- nonferrous
- waste dry
- dry batteries
- 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.)
- Pending
Links
- 239000002699 waste material Substances 0.000 title claims abstract description 16
- 239000000463 material Substances 0.000 claims abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000003570 air Substances 0.000 claims 1
- 238000004064 recycling Methods 0.000 claims 1
- 239000002689 soil Substances 0.000 claims 1
- 229910052751 metal Inorganic materials 0.000 abstract description 20
- 239000002184 metal Substances 0.000 abstract description 20
- 239000000843 powder Substances 0.000 abstract description 7
- 239000000126 substance Substances 0.000 abstract description 5
- 239000000696 magnetic material Substances 0.000 abstract description 3
- 239000006148 magnetic separator Substances 0.000 abstract description 3
- 150000002739 metals Chemical class 0.000 abstract description 3
- 229920003023 plastic Polymers 0.000 abstract description 3
- 239000004033 plastic Substances 0.000 abstract description 3
- 238000001556 precipitation Methods 0.000 abstract 3
- 230000002265 prevention Effects 0.000 abstract 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 6
- 239000007864 aqueous solution Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 2
- 229920002554 vinyl polymer Polymers 0.000 description 2
- 239000010926 waste battery Substances 0.000 description 2
- -1 ferrous metals Chemical class 0.000 description 1
- 229910052755 nonmetal Inorganic materials 0.000 description 1
- 150000002843 nonmetals Chemical class 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
Description
【発明の詳細な説明】
廃乾電池の処理については、各自治体に於いてゴミ処理
上特に問題になるのは、エレクトニクス機器の向りに依
り年々乾電池の生産は急上昇し、それに伴い廃乾電池も
増収集されるため、その処理を誤れば公害問題が発生し
てくる。そのため、この解決はこれまで緊急とされてい
る。[Detailed Description of the Invention] Disposal of waste dry batteries is a particular problem in each local government when it comes to waste disposal.The production of dry batteries is rapidly increasing year by year due to the direction of electronics equipment, and as a result, the number of waste dry batteries is also increasing. As more and more waste is collected, if it is mishandled, pollution problems will occur. Therefore, this solution has been considered urgent.
本発明は、この解決法の−・つとしての提唱であって、
廃乾電池より採集出来る資源の再利用であり、さらには
公害の発生を防止するものである。此の様な意味で、本
発明は廃乾電池の処理技術としての、生産応用面での大
きな利点を発揮しうる。The present invention proposes one of these solutions,
This is a reuse of resources that can be collected from waste dry batteries, and it also prevents pollution from occurring. In this sense, the present invention can exhibit great advantages in production applications as a technology for processing waste dry batteries.
本発明を実施する上で、廃乾電池の種類によっては分離
する上で薬水溶液を替える事や通過時間等を変更する必
要を/j=じる場合がある。In carrying out the present invention, depending on the type of waste dry battery, it may be necessary to change the chemical aqueous solution or change the passage time etc. upon separation.
第1図は説明の為の装置の立面図の一例を示したもので
ある(1)は廃乾電池の貯蔵ホッパーでさらには廃乾電
池を供給する為のホッパー、(2)は定員フィーダーで
廃乾電池を(3)のシュートに一定基供給する。(4)
は破砕機で金属、非鉄金属、非金属を一定の大きさ、も
しくは粉末上に破砕、粉砕を行う。破砕、粉砕された廃
乾電池は(5)のシュートを通り(6)の磁選機を通過
さし磁性物(金属)を選別しく7)のコンベヤーとり8
)のシュー1〜で案内され(9)の貯金属バットに回収
へれる非磁性物は(10)のシュートを通り(11)の
分級機で、非鉄金属の塊と粉体の一部は(12)のメツ
シュコンベヤーへ送り非鉄金属の塊は(j9)の配管に
依る循環水で洗浄され(]3)の貯非鉄金属バットに回
収される。その他の非鉄金属粉は(16)の沈降槽No
2に入り沈降させ回収する。又大半の非鉄金属粉プラス
チック、ビニール等は(14)のオーバーフローダクト
で案内され(15)の沈降槽Nolに入り、プラスチッ
ク、ビニール、紙類は、水面上に浮」−する、これを臣
1収する。その他の非鉄金属粉は水面以下に沈降したも
のを回収する。Figure 1 shows an example of an elevation view of the device for explanation. (1) is a storage hopper for waste dry batteries and a hopper for supplying waste dry batteries, and (2) is a capacity feeder for discarding waste batteries. Supply a certain number of dry batteries to the chute (3). (4)
A crusher is used to crush and crush metals, non-ferrous metals, and non-metals into a certain size or into powder. The crushed and pulverized waste dry batteries pass through the chute in (5) and the magnetic separator in (6) to sort out magnetic substances (metals) and are transferred to the conveyor tray in 7).
The non-magnetic materials guided by the shoes 1 to (9) and collected in the metal storage vat (9) pass through the chute (10) and are passed through the classifier (11), where some of the non-ferrous metal lumps and powder are collected in the metal storage vat (9). The nonferrous metal lumps sent to the mesh conveyor (12) are washed with circulating water through the pipe (j9) and collected in the nonferrous metal storage vat (]3). For other non-ferrous metal powders, settle tank No. (16)
2, settle and collect. Also, most of the non-ferrous metal powder plastics, vinyl, etc. are guided through the overflow duct (14) and enter the sedimentation tank No. (15), where the plastics, vinyl, and paper float on the water surface. collect. Other non-ferrous metal powders that settle below the water surface are collected.
(11)の分級機には薬水溶液を入れ(15) (16
)の沈降槽Nol、 No2にオーバーフローさせ、薬
水溶液の−にずみ液を(]7)の配管に通しく18)の
循環ポンプで(19)の配管を通しく12)メツシュコ
ンベヤー」二の非鉄金属塊の洗浄と(11)の分級機へ
の循環を行う。此の様に金属含有の薬水溶液は外部に流
失させないため、公害の発生を防止する。 以」二のよ
うに1本発明は資源の材料別回収を連続的に行う為、杆
費の節減と作業効率向上ができる。Put the medicinal solution into the classifier (11) (15) (16
) overflow into sedimentation tanks No. 1 and No. 2, and pass the medicinal aqueous solution through the piping of (7). The non-ferrous metal lump is washed and circulated to the classifier (11). In this way, the metal-containing chemical aqueous solution is not leaked to the outside, thereby preventing the occurrence of pollution. As described above, the present invention continuously recovers resources by material, thereby reducing rod costs and improving work efficiency.
第1図は装置の立面図で、
(1)は廃乾電池の貯蔵、供給用ホッパー、(2)は定
量フィーダー。
(3)はシュート、(4)は破砕機、(5)はシュート
、(6)は磁選機。
(7)はコンベヤー、(8)はシュート、(9)は貯金
属バット。
(10)はシュート、 (I+)は分級機、 (12)
はメツシュコンベヤー。
(13)はIl’i非鉄金属バット、 (1,4)はオ
ーバーフローダクト。
(15)(16)は沈降槽Nol、 No2. (17
)は給水配管、 (18)は循環ポンプ、 (19)は
送水配管。Figure 1 is an elevational view of the device; (1) is a hopper for storing and supplying waste batteries, and (2) is a quantitative feeder. (3) is a chute, (4) is a crusher, (5) is a chute, and (6) is a magnetic separator. (7) is a conveyor, (8) is a chute, and (9) is a metal storage vat. (10) is a chute, (I+) is a classifier, (12)
is a mesh conveyor. (13) is the Il'i non-ferrous metal bat, (1,4) is the overflow duct. (15) (16) are settling tanks No. 1 and No. 2. (17
) is the water supply pipe, (18) is the circulation pump, and (19) is the water supply pipe.
Claims (1)
分するものと、資源材料として再利用するものとにそれ
ぞれ連続的に分離し、再利用出来る資源材料は、材料別
に分離する。又、この廃乾電池は、自然廃棄や焼却処理
をすると、水質、土壌、空気等が汚染され公害問題の発
生も考えられる。従って、資源の再利用と、公害の発生
を防止することを目的とする装置。Waste dry batteries are mechanically crushed, and the materials inside the batteries are continuously separated into those to be disposed of and those to be reused as resource materials, and the resource materials that can be recycled are separated by material. In addition, if these waste dry batteries are disposed of naturally or incinerated, they may contaminate water, soil, air, etc. and cause a pollution problem. Therefore, devices aimed at recycling resources and preventing the occurrence of pollution.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59120943A JPS61488A (en) | 1984-06-11 | 1984-06-11 | Apparatus for treating waste dry battery |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59120943A JPS61488A (en) | 1984-06-11 | 1984-06-11 | Apparatus for treating waste dry battery |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61488A true JPS61488A (en) | 1986-01-06 |
Family
ID=14798805
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59120943A Pending JPS61488A (en) | 1984-06-11 | 1984-06-11 | Apparatus for treating waste dry battery |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61488A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5498360A (en) * | 1993-06-30 | 1996-03-12 | Nomura Kohsan Co., Ltd. | Process for recycling used-up dry cells, and ferrite production process |
KR100637680B1 (en) | 2005-04-01 | 2006-10-24 | 메탈화학(주) | Apparatus and method for recovering cobalt powder from used lithium ion secondary battery |
KR100716199B1 (en) | 2006-06-23 | 2007-05-10 | 한국지질자원연구원 | Recycling apparatus of the waste lithium first battery and its method |
-
1984
- 1984-06-11 JP JP59120943A patent/JPS61488A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5498360A (en) * | 1993-06-30 | 1996-03-12 | Nomura Kohsan Co., Ltd. | Process for recycling used-up dry cells, and ferrite production process |
KR100637680B1 (en) | 2005-04-01 | 2006-10-24 | 메탈화학(주) | Apparatus and method for recovering cobalt powder from used lithium ion secondary battery |
KR100716199B1 (en) | 2006-06-23 | 2007-05-10 | 한국지질자원연구원 | Recycling apparatus of the waste lithium first battery and its method |
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