JP2002194448A - Method for recovering metal from electronic or electric parts with resin - Google Patents

Method for recovering metal from electronic or electric parts with resin

Info

Publication number
JP2002194448A
JP2002194448A JP2000400699A JP2000400699A JP2002194448A JP 2002194448 A JP2002194448 A JP 2002194448A JP 2000400699 A JP2000400699 A JP 2000400699A JP 2000400699 A JP2000400699 A JP 2000400699A JP 2002194448 A JP2002194448 A JP 2002194448A
Authority
JP
Japan
Prior art keywords
magnetic
magnetic force
less
force sorting
electronic
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.)
Granted
Application number
JP2000400699A
Other languages
Japanese (ja)
Other versions
JP4554068B2 (en
Inventor
Yusaku Masuda
雄策 益田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Mining Holdings Inc
Eneos Corp
Original Assignee
Nippon Mining and Metals Co Ltd
Nippon Mining Co Ltd
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 Nippon Mining and Metals Co Ltd, Nippon Mining Co Ltd filed Critical Nippon Mining and Metals Co Ltd
Priority to JP2000400699A priority Critical patent/JP4554068B2/en
Publication of JP2002194448A publication Critical patent/JP2002194448A/en
Application granted granted Critical
Publication of JP4554068B2 publication Critical patent/JP4554068B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B11/00Obtaining noble metals
    • C22B11/02Obtaining noble metals by dry processes
    • C22B11/021Recovery of noble metals from waste materials
    • C22B11/025Recovery of noble metals from waste materials from manufactured products, e.g. from printed circuit boards, from photographic films, paper, or baths
    • 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
    • C22B7/005Separation by a physical processing technique only, e.g. by mechanical breaking
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Abstract

PROBLEM TO BE SOLVED: To provide a method for recovering metal from electronic or electric parts with resin in which values metal such as gold, silver and copper can be sorted, and efficiently recovered. SOLUTION: This recovering method comprises a crushing step for crushing the electronic or electric parts with resin into pieces having the size of <=10 mm, a dust-collecting step for collecting the dust generated in the crushing step, a first magnetic force sorting step for sorting the crushed stuff generated in the crushing step into magnetic stuff and non-magnetic stuff with the magnetic force of 100-2,000 Gauss by a magnetic sorting machine, a second magnetic force sorting step for sorting the dust collected in the dust-collecting step into magnetic stuff and non-magnetic stuff with the magnetic force of 100-2,000 Gauss by a magnetic force sorting machine, and a second screening step for screening the non-magnetic stuff obtained in the second magnetic force sorting step. The magnetic stuff obtained in the first and second magnetic force sorting steps and the undersized stuff obtained in the second screening step are mixed to be briquetted, and treated by a copper refining furnace to obtain valued metal.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、家電製品やOA機
器等の樹脂付電子・電気部品から有価金属を回収する樹
脂付電子・電気部品からの金属の回収方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for recovering valuable metals from electronic and electrical parts with resin, such as home electric appliances and OA equipment.

【0002】[0002]

【従来の技術】従来、家電製品やOA機器等の廃棄物
は、そのまま埋め立てたり焼却後に埋め立てたりしてお
り、それらに含まれる有価金属はほとんど利用されてい
ないのが現状であった。OA機器については、コネクタ
に使用されている貴金属を回収することが一部で事業化
されているが、専ら手作業によるものでシステム化され
たものではなかった。
2. Description of the Related Art Conventionally, wastes such as home electric appliances and OA equipment have been buried as they are or buried after incineration, and at present, valuable metals contained therein are hardly used. Regarding OA equipment, the recovery of precious metals used for connectors has been partially commercialized, but it has been done manually and not systematized.

【0003】[0003]

【発明が解決しようとする課題】2001年に施行され
る家電リサイクル法では、家電4品目についての廃品の
リサイクルがメーカに義務付けられており、さらに、将
来にはその他の電気・電子機器類も追加される動きがあ
る。このように、家電製品やOA機器のリサイクルに対
して強い要請があるが、リサイクルを効率良く行う方法
は未だ提供されていないのが現状である。よって、本発
明は、上記事情に鑑みてなされたもので、金、銀、銅お
よびニッケルといった有価金属を選別して効率良く回収
することができる樹脂付電子・電気部品からの金属の回
収方法を提供することを目的としている。
According to the Home Appliance Recycling Law enforced in 2001, manufacturers are obliged to recycle waste items for four types of home appliances, and other electric and electronic devices will be added in the future. There is a movement to be done. As described above, there is a strong demand for recycling of home electric appliances and OA equipment, but at present, a method for efficiently recycling has not yet been provided. Accordingly, the present invention has been made in view of the above circumstances, and provides a method for collecting metals from resin-attached electronic / electric parts that can efficiently collect valuable metals such as gold, silver, copper and nickel. It is intended to provide.

【0004】[0004]

【課題を解決するための手段】本発明の樹脂付電子・電
気部品からの金属の回収方法は、樹脂付電子・電気部品
を10mm以下の大きさに破砕する破砕工程と、この破
砕工程で発生する粉塵を集塵する集塵工程と、破砕工程
で生成された破砕物を磁力選別機により100〜200
0ガウスで磁性物と非磁性物とに選別する第1磁力選別
工程と、集塵工程で捕集されたダストを磁力選別機によ
り100〜2000ガウスで磁性物と非磁性物とに選別
する第2磁力選別工程と、第2磁力選別工程で得られた
非磁性物を篩い分ける第2篩別工程とを備え、第1、第
2磁力選別工程で得られた磁性物と第2篩別工程で得ら
れた網下品とを混合して団鉱し、これを錬銅炉にて処理
することで有価金属を得ることを特徴としている。
SUMMARY OF THE INVENTION According to the present invention, there is provided a method for recovering a metal from an electronic / electric part with resin according to the present invention, comprising the steps of: crushing an electronic / electric part with resin to a size of 10 mm or less; And a crushed material generated in the crushing step by a magnetic separator.
A first magnetic separation step for separating magnetic and non-magnetic substances at 0 Gauss; and a magnetic separation apparatus for separating dust collected in the dust collection step into magnetic and non-magnetic substances at 100 to 2000 Gauss. A magnetic material obtained in the first and second magnetic force sorting steps, and a second sieving step for sieving the non-magnetic material obtained in the second magnetic force sorting step. It is characterized in that valuable metals are obtained by mixing and briquetting with the undergarment obtained in (1) and treating it in a wrought copper furnace.

【0005】樹脂付電子・電気部品から金属を回収する
システムにおいて最もネックとなるのが樹脂の分離であ
り、これが不充分であると錬銅炉で溶解する際に黒煙状
の排ガスが発生して環境上の問題となる。この黒煙状の
排ガスの発生を防止するためには、錬銅炉に投入する原
料中の樹脂分の含有量を最大でも15重量%程度にする
必要があることが判明している。本発明の樹脂付電子・
電気部品からの金属の回収方法(以下、単に金属の回収
方法と称する)にあっては、破砕工程と集塵工程によっ
て破砕後の原料を破砕物とダストとに選別し、第1、第
2磁力選別工程を行うから、樹脂を効率良く分離するこ
とができる。さらに、本発明では、ダスト中の非磁性物
を篩い分ける第2篩別工程を備えている。ダストのうち
でも小さなものに金属の含有量が多いため、これを網下
品として選別して団鉱に用いるから、金属の品位を高め
ることができる。これにより、錬銅炉での処理効率を向
上させることができ、また、黒煙状の排ガスの発生を未
然に防止することができる。
[0005] In the system for recovering metals from electronic and electric parts with resin, the most bottleneck is the separation of resin. If this is insufficient, black smoke-like exhaust gas is generated when melting in a wrought copper furnace. Environmental problems. It has been found that in order to prevent the generation of black smoke-like exhaust gas, the content of the resin component in the raw material to be charged into the wrought copper furnace needs to be at most about 15% by weight. Electronic with resin of the present invention
In a method for recovering metal from electrical components (hereinafter simply referred to as a method for recovering metal), the crushed raw material is separated into crushed materials and dust by a crushing step and a dust collecting step, and the first and second materials are separated. Since the magnetic separation step is performed, the resin can be efficiently separated. Furthermore, the present invention includes a second sieving step of sieving non-magnetic substances in dust. Among the dusts, small ones have a high metal content, so that they are selected as net products and used for briquetting, so that the quality of the metal can be improved. Thereby, the processing efficiency in the wrought copper furnace can be improved, and the generation of black smoke-like exhaust gas can be prevented beforehand.

【0006】ここで、本発明では、第1、第2磁力選別
工程における磁束密度は100〜2000ガウスとして
いる。これは、磁束密度が100ガウス未満では、金、
銀、および銅といった貴金属の回収効率が低下し、20
00ガウスを超えても回収効率はさほど向上しなくなる
からである。
Here, in the present invention, the magnetic flux density in the first and second magnetic force separation steps is 100 to 2000 Gauss. This means that for magnetic flux densities less than 100 Gauss, gold,
Recovery efficiency of precious metals such as silver and copper decreases,
This is because the recovery efficiency does not improve so much even when it exceeds 00 Gauss.

【0007】[0007]

【発明の実施の形態】以下、本発明の好適な実施の形態
について図1を参照しながら説明する。 破砕工程 廃OA機器や家電製品からプリント基板を取り外し、こ
れを破砕装置に投入して10mm以下に破砕する。破砕
装置としては、装置の上部で原料を衝撃破砕し、装置の
下部で摺動破砕して破砕物を細かく分断するするような
構造のものが好ましく、樹脂付電子・電気部品を3〜
0.2mm程度に破砕するのが良い。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A preferred embodiment of the present invention will be described below with reference to FIG. Crushing process The printed circuit board is removed from the waste OA equipment and the home electric appliances, and is put into a crushing device and crushed to 10 mm or less. The crushing device preferably has a structure in which the raw material is subjected to impact crushing at the upper portion of the device and slidingly crushed at the lower portion of the device to finely divide the crushed material.
It is better to crush to about 0.2 mm.

【0008】集塵工程 プリント基板を上記のように細かく破砕するため、多く
のダストが発生する。このダストにも有価金属が含まれ
ているので、破砕装置の内部をダクトを介して吸引し、
たとえばサイクロン、バグフィルタなどの集塵装置でダ
ストを回収する。
Dust Collection Step Since the printed circuit board is finely crushed as described above, a large amount of dust is generated. Since valuable metal is also contained in this dust, the inside of the crusher is sucked through a duct,
For example, dust is collected by a dust collector such as a cyclone or a bag filter.

【0009】第1磁力選別工程 破砕装置に残された原料に対して磁力選別を行う。第1
磁力選別工程の磁力選別機は、図5に示すような構造の
ものが好適に用いられる。この図に示す磁力選別機は、
ケーシング70の内部に、周囲に沿って永久磁石を配置
した回転ドラム71を配置し、回転ドラム71の下方に
仕切72を配置したもので、ケーシング70の上方から
ベルトコンベア73で搬送されて落下させられる原料M
のうち非磁性物M1を仕切72の手前側に、磁性物Aを
仕切の向こう側へ落下させるようになっている。
First magnetic separation step Magnetic separation is performed on the raw material left in the crushing apparatus. First
As the magnetic force sorting machine in the magnetic force sorting step, one having a structure as shown in FIG. 5 is suitably used. The magnetic separator shown in this figure is
A rotating drum 71 having permanent magnets disposed around the periphery of the casing 70 and a partition 72 disposed below the rotating drum 71 are conveyed from above the casing 70 by a belt conveyor 73 and dropped. Raw material M
Among them, the non-magnetic substance M1 is dropped to the front side of the partition 72, and the magnetic substance A is dropped to the other side of the partition.

【0010】第2磁力選別工程 集塵工程で集塵されたダストに対して磁力選別を行う。
ダストに対して行う第2磁力選別工程は、第1磁力選別
工程よりも高い精度で行われることが望ましい。この場
合の磁力選別機は、下側のベルトコンベアで材料を搬送
するとともに上側のベルトコンベアのベルトに交互に配
置した永久磁石のS極とN極により磁力選別するものが
適している。そして、この第2磁力選別工程により、磁
性物Bが選別される。なお、第2磁力選別工程では、S
極とN極とを交互に配置したドラム式の磁力選別機を使
用することも可能である。
Second magnetic separation step The magnetic separation is performed on the dust collected in the dust collection step.
It is desirable that the second magnetic force sorting step performed on dust be performed with higher accuracy than the first magnetic force sorting step. In this case, a magnetic force sorter that conveys a material by a lower belt conveyor and sorts magnetic force by S and N poles of permanent magnets alternately arranged on a belt of an upper belt conveyor is suitable. Then, the magnetic substance B is sorted by the second magnetic force sorting step. In the second magnetic force sorting step, S
It is also possible to use a drum type magnetic separator in which poles and N poles are alternately arranged.

【0011】第1篩別工程 第1磁力選別工程で得られた非磁性物を篩別機により篩
い分ける第1篩別工程を行うことが望ましい。具体的に
は、第1篩別工程では、2mm未満品、2mm以上3m
m未満品、3mm以上5mm未満品、および5mm以上
10mm未満品に篩い分ける。破砕物のうち小さいもの
と大きいものに金属が多く含まれることが経験的に判明
している。したがって、第1篩別工程で得られた2mm
未満品Cおよび5mm以上10mm未満品Dを団鉱の材
料に混合するのが望ましい。
First sieving step It is desirable to carry out a first sieving step of sieving the non-magnetic material obtained in the first magnetic separation step with a sieving machine. Specifically, in the first sieving step, a product of less than 2 mm, 2 mm or more and 3 m
The product is sieved into a product of less than m, a product of 3 mm or more and less than 5 mm, and a product of 5 mm or more and less than 10 mm. It has been empirically found that small and large pieces of crushed material contain a large amount of metal. Therefore, 2 mm obtained in the first sieving process
It is desirable to mix less than product C and less than 5 mm and less than 10 mm product D into briquette material.

【0012】図2および図3は、第1篩別工程に用いて
好適な篩別機の例を示すものである。これらの図に示す
篩別機は、振動機10の上に篩別容器20を取り付けた
ものである。篩別容器20の内部には、図3に示すよう
に、下部枠体30、中間下部枠体40、中間上部枠体5
0および上部枠体60が収容され、それらの間に下部網
体35、中間網体45および上部網体55がそれぞれ介
装されている。図3に示すものは、3種類の網体35,
45,55によって原料を大、中、小、微小の4種類の
大きさに篩い分けるものである。
FIGS. 2 and 3 show an example of a sieving machine suitable for the first sieving step. The sieving machine shown in these figures has a sieving container 20 mounted on a vibrator 10. As shown in FIG. 3, a lower frame 30, an intermediate lower frame 40, and an intermediate upper frame 5 are provided inside the sieving container 20.
The lower net 35, the intermediate net 45, and the upper net 55 are interposed therebetween. FIG. 3 shows three types of nets 35,
According to 45 and 55, the raw material is sieved into four types of sizes, large, medium, small and minute.

【0013】第2篩別工程 ダストから分離された非磁性物のうち小さいものにも有
価金属が含まれているので、第2篩別工程により金属を
選別する。この場合の篩別機は、30〜100メッシュ
の網を備えたものが好適であり、その網下品Eを団鉱の
原料として使用する。
Second sieving step Since non-magnetic substances separated from the dust contain valuable metals, metals are sorted in the second sieving step. The sieving machine in this case is preferably provided with a mesh of 30 to 100 mesh, and the net product E is used as a raw material for briquetting.

【0014】第1、第2風力選別工程 第1篩別工程で得られる2mm以上3mm未満品および
3mm以上5mm未満品にも有価金属が含まれているの
で、それぞれの大きさの原料毎に風力選別を行って重量
物と軽量物とに選別し、得られた重量物Fを団鉱の材料
に混合して団鉱とするのが望ましい。図4はこれら第
1、第2風力選別工程に好適に用いられる風力選別装置
の概略を示す縦断面図である。図中符号1は塔体であ
り、塔体1の内部には、上下方向に向けてジグザグに屈
曲する流路2が設けられている。流路2の上端部には原
料投入口3が設けられ、流路2の下端部には空気流入口
4が設けられている。また、塔体1の上端部には、サイ
クロン、バグフィルタおよびファンがこの順に接続され
ている。この風力分離装置では、ファンで空気を吸引す
ることにより空気流入口4から空気を流入させ、原料投
入口から破砕物の非磁性物のうち2mm以上3mm未
満、または3mm以上5mm未満のものを投入する。こ
れにより、重量物が流路2に沿って落下する一方、軽量
物が上方へ吸い上げられる。また、吸い上げられた軽量
物は、サイクロンとバグフィルタにより回収される。そ
して、第1風力分離工程により、3mm以上5mm未満
品のうち金属が濃縮された重量物が塔体1の下部に選別
され、また、第2風力分離工程により、2mm以上3m
m未満品のうち金属が濃縮された重量物が塔体1の下部
に選別される。なお、サイクロンおよびバグフィルタに
は、樹脂が濃縮されたものが分離される。
First and Second Wind Separation Steps Since valuable metals are contained in the products of 2 mm or more and less than 3 mm and in the products of 3 mm or more and less than 5 mm obtained in the first sieving step, the wind power is separated for each raw material of each size. It is preferable that the material is separated into a heavy material and a light material by performing sorting, and the obtained heavy material F is mixed with the material of the briquette to form a briquette. FIG. 4 is a vertical cross-sectional view schematically showing a wind power sorting device suitably used in the first and second wind power sorting processes. In the figure, reference numeral 1 denotes a tower body, and inside the tower body 1, there is provided a flow path 2 which is bent in a zigzag manner in a vertical direction. A raw material inlet 3 is provided at an upper end of the flow path 2, and an air inlet 4 is provided at a lower end of the flow path 2. A cyclone, a bag filter, and a fan are connected to the upper end of the tower 1 in this order. In this wind separation apparatus, air is introduced from the air inlet 4 by sucking air with a fan, and non-magnetic material of crushed material of 2 mm or more and less than 3 mm or 3 mm or more and less than 5 mm is introduced from the material inlet. I do. Thereby, while the heavy object falls along the flow path 2, the light object is sucked up. In addition, the sucked lightweight material is collected by a cyclone and a bag filter. In the first wind separation step, heavy objects in which the metal is concentrated are selected from the lower part of the tower 1 among the products of 3 mm or more and less than 5 mm, and in the second wind separation step, 2 mm or more and 3 m
Among the products of less than m, heavy materials in which the metal is concentrated are sorted at the lower part of the tower 1. The cyclone and the bag filter are separated from the resin in which the resin is concentrated.

【0015】上記のようにして第1磁力選別工程で得ら
れた磁性物A、第2磁力選別工程で得られた磁性物B、
第1篩別工程で得られた2mm未満品Cおよび5mm以
上10mm未満品D、第2篩別工程で得られた網下品
E、第1、第2風力選別工程で得られた重量物Fは、混
合して団鉱され、錬銅炉にて処理される。団鉱は、原料
に適当な水分と粘結剤を加えて圧縮成形し、所定の塊状
とする処理である。団鉱物を錬銅炉に投入して溶解する
ことによりスラグと粗銅が生成され、粗銅を電解精錬す
ることによって金、銀、銅、ニッケルといった有価金属
が精製される。なお、錬銅炉としては、銅製錬で用いら
れるPS転炉やMI法で用いられるC炉等がある。
As described above, the magnetic substance A obtained in the first magnetic separation step, the magnetic substance B obtained in the second magnetic separation step,
The product C of less than 2 mm and the product D of 5 mm or more and less than 10 mm obtained in the first sieving process, the under-net product E obtained in the second sieving process, the heavy material F obtained in the first and second wind screening processes are: , Mixed and aggregated and processed in a wrought copper furnace. Briquette is a process of adding a suitable water and binder to a raw material, compressing the raw material, and forming the raw material into a predetermined mass. Slag and blister copper are generated by putting the briquette mineral into a wrought copper furnace and melting it, and valuable metals such as gold, silver, copper, and nickel are refined by electrorefining the blister copper. The wrought copper furnace includes a PS converter used in copper smelting and a C furnace used in the MI method.

【0016】[0016]

【実施例】次に、図1を参照して本発明の実施例を詳細
に説明する。 破砕工程 破砕工程では、破砕装置に表1に示す金属成分からなる
プリント基板を20kg投入し破砕した。
Next, an embodiment of the present invention will be described in detail with reference to FIG. Crushing Step In the crushing step, 20 kg of a printed circuit board made of a metal component shown in Table 1 was charged into a crushing apparatus and crushed.

【0017】[0017]

【表1】 [Table 1]

【0018】集塵工程 上記破砕工程で発生したダストをサイクロンおよびバグ
フィルタにより集塵した。集塵されたダストの成分を表
2に、破砕装置内に残された破砕物の成分を表3に示
す。なお、表において分配率とは、破砕装置とサイクロ
ンおよびバグフィルタに分配された各成分の重量割合を
示す。
Dust Collection Step The dust generated in the crushing step was collected by a cyclone and a bag filter. Table 2 shows the components of the collected dust, and Table 3 shows the components of the crushed material left in the crusher. In the table, the distribution ratio indicates the weight ratio of each component distributed to the crusher, the cyclone, and the bag filter.

【0019】[0019]

【表2】 [Table 2]

【0020】[0020]

【表3】 [Table 3]

【0021】第1磁力選別工程 破砕装置に残された原料に対して磁力選別を行った。こ
の磁力選別には、ドラム式磁選機を用いた。その際の磁
力は1500ガウスに設定した。この第1磁力選別工程
で得られた磁性物の成分を表4に、非磁性物の成分を表
5に示す。
First Magnetic Separation Step Magnetic separation was performed on the raw material left in the crushing apparatus. For this magnetic force separation, a drum type magnetic separator was used. The magnetic force at that time was set to 1500 Gauss. Table 4 shows the components of the magnetic material obtained in the first magnetic force sorting step, and Table 5 shows the components of the non-magnetic material.

【0022】[0022]

【表4】 [Table 4]

【0023】[0023]

【表5】 [Table 5]

【0024】第2磁力選別工程 ダストに対して磁力選別を行った。この磁力選別には、
ベルトコンベア式乾式磁選機を用い、その際の磁力を5
00ガウスとした。この第2磁力選別工程で得られた磁
性物の成分を表6に、非磁性物の成分を表7に示す。
Second magnetic separation step Magnetic separation was performed on the dust. In this magnetic separation,
Use a belt conveyor type dry magnetic separator and set the magnetic force at that time to 5
00 Gauss. Table 6 shows the components of the magnetic substance obtained in the second magnetic force sorting step, and Table 7 shows the components of the non-magnetic substance.

【0025】[0025]

【表6】 [Table 6]

【0026】[0026]

【表7】 [Table 7]

【0027】第1篩別工程 第1磁力選別工程で得られた非磁性物を篩別機により篩
い分けた。この第1篩別工程では、2mm未満品、2m
m以上3mm未満品、3mm以上5mm未満品、および
5mm以上10mm未満品に篩い分けた。それらの成分
を表8〜11に示す。
First sieving step The non-magnetic material obtained in the first magnetic separation step was sieved by a sieving machine. In this first sieving step, a product of less than 2 mm, 2 m
The product was sieved into a product of m or more and less than 3 mm, a product of 3 mm or more and less than 5 mm, and a product of 5 mm or more and less than 10 mm. The components are shown in Tables 8-11.

【0028】[0028]

【表8】 [Table 8]

【0029】[0029]

【表9】 [Table 9]

【0030】[0030]

【表10】 [Table 10]

【0031】[0031]

【表11】 [Table 11]

【0032】第2篩別工程 ダストから分離された非磁性物に対して篩い分けを行っ
た。この第2篩別工程で使用した篩別機では、50メッ
シュの網を使用した。第2篩別工程後の網上品と網下品
の成分をそれぞれ表12および表13に示す。
Second sieving step The non-magnetic material separated from the dust was sieved. In the sieving machine used in the second sieving step, a 50-mesh net was used. Tables 12 and 13 show the components of the on-screen product and the under-screen product after the second sieving step, respectively.

【0033】[0033]

【表12】 [Table 12]

【0034】[0034]

【表13】 [Table 13]

【0035】第1風力選別工程 第1篩別工程で得られた3mm以上5mm未満品に対し
て図4に示す風力選別装置を用いて第1風力選別工程を
行った。風力選別後の金属が濃縮された塔下での重量物
の成分を表14に、樹脂分が濃縮されたサイクロンおよ
びバグフィルタ側での成分を表15に示した。
First Air Separation Step The first air separation step was performed on the product obtained in the first sieving step, which was 3 mm or more and less than 5 mm, using the air separation apparatus shown in FIG. Table 14 shows the components of the heavy materials under the tower where the metals were concentrated after the wind separation, and Table 15 shows the components on the cyclone and bag filter side where the resin components were concentrated.

【0036】[0036]

【表14】 [Table 14]

【0037】[0037]

【表15】 [Table 15]

【0038】第2風力選別工程 第1篩別工程で得られた2mm以上3mm未満品に対し
て図4に示す風力選別装置を用いて第2風力選別工程を
行った。風力選別後の金属が濃縮された塔下での重量物
の成分を表16に、樹脂分が濃縮されたサイクロンおよ
びバグフィルタ側での成分を表17に示した。
Second Wind Separation Step A second wind separation step was performed on the product obtained in the first sieving step and having a size of 2 mm or more and less than 3 mm using the wind separation apparatus shown in FIG. Table 16 shows the components of the heavy material under the tower where the metal was concentrated after the wind separation, and Table 17 shows the components on the cyclone and bag filter side where the resin component was concentrated.

【0039】[0039]

【表16】 [Table 16]

【0040】[0040]

【表17】 [Table 17]

【0041】上記の第1磁力選別工程で得られた磁性
物(No.1)、の第2磁力選別工程で得られた磁性
物(No.9)、の第1篩別工程で得られた2mm未
満品(No.8)および5mm以上10mm未満品(N
o.3)、の第2篩別工程で得られた網下品(No.
12)、の第1、第2風力選別工程で得られた重量物
(No.4,6)を混合して団鉱した。この団鉱に供し
た金属濃縮分の成分を表18に、分離された樹脂濃縮分
(No.5,7,11)の成分を表19に示す。
The magnetic substance (No. 1) obtained in the first magnetic force sorting step and the magnetic substance (No. 9) obtained in the second magnetic force sorting step were obtained in the first screening step. No more than 2mm (No. 8) and 5mm or more and less than 10mm (N
o. 3), the undergarment obtained in the second screening step (No.
12), the weights (Nos. 4, 6) obtained in the first and second wind separation processes were mixed and aggregated. Table 18 shows the components of the metal concentrate supplied to the briquette, and Table 19 shows the components of the separated resin concentrates (Nos. 5, 7, and 11).

【0042】[0042]

【表18】 [Table 18]

【0043】[0043]

【表19】 [Table 19]

【0044】表18及び表19から判るように、金属濃
縮分では極めて多くの有価金属が回収されており、ま
た、樹脂の品位も10.4重量%であった。この原料を
銅転炉に投入し溶解して粗銅を得たところ、何ら問題な
く操業することができた。
As can be seen from Tables 18 and 19, an extremely large amount of valuable metal was recovered from the metal concentrate, and the resin grade was 10.4% by weight. This raw material was put into a copper converter and melted to obtain blister copper, which could be operated without any problem.

【0045】[0045]

【発明の効果】以上説明したように本発明の金属の回収
方法においては、錬銅炉の操業に支障を来すことなく、
金、銀、銅といった有価金属を選別して効率良く回収す
ることができるという効果が得られる。
As described above, in the metal recovery method according to the present invention, the operation of the wrought copper furnace is not hindered.
An effect is obtained in that valuable metals such as gold, silver and copper can be sorted and efficiently collected.

【図面の簡単な説明】[Brief description of the drawings]

【図1】 本発明の実施形態および実施例における工程
を示す図である。
FIG. 1 is a diagram showing steps in embodiments and examples of the present invention.

【図2】 本発明に用いて好適な篩別機の全体を示す斜
視図である。
FIG. 2 is a perspective view showing an entire sieving machine suitable for use in the present invention.

【図3】 篩別機の網体等を示す斜視図である。FIG. 3 is a perspective view showing a mesh body and the like of the sieving machine.

【図4】 本発明の実施例で使用した風力選別装置を示
す縦断面図である。
FIG. 4 is a longitudinal sectional view showing a wind power sorting device used in an embodiment of the present invention.

【図5】 本発明に用いて好適なドラム式磁力選別機の
概略を示す縦断面図である。
FIG. 5 is a longitudinal sectional view schematically showing a drum type magnetic separator suitable for use in the present invention.

【符号の説明】[Explanation of symbols]

71 回転ドラム 72 仕切 73 ベルトコンベア A 磁性物 M 原料 M1 非磁性物 71 Rotary drum 72 Partition 73 Belt conveyor A Magnetic material M Raw material M1 Non-magnetic material

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B07B 4/02 B07B 4/02 9/00 9/00 A B09B 3/00 B09B 3/00 301Z 301 C22B 1/14 5/00 ZAB 1/248 C22B 1/14 7/00 A 1/248 11/00 7/00 15/00 // C22B 11/00 B09B 3/00 Z 15/00 5/00 ZABC Fターム(参考) 4D004 AA22 BA05 CA04 CA08 CA09 CA12 CA14 CA15 CA29 DA03 DA20 4D021 AA03 CA07 CB11 DA13 EA10 EB01 FA02 GA04 GA13 GB01 HA10 4K001 AA01 AA04 AA09 BA22 CA01 CA04 CA25 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) B07B 4/02 B07B 4/02 9/00 9/00 A B09B 3/00 B09B 3/00 301Z 301 C22B 1 / 14 5/00 ZAB 1/248 C22B 1/14 7/00 A 1/248 11/00 7/00 15/00 // C22B 11/00 B09B 3/00 Z 15/00 5/00 ZABC F-term ( Reference) 4D004 AA22 BA05 CA04 CA08 CA09 CA12 CA14 CA15 CA29 DA03 DA20 4D021 AA03 CA07 CB11 DA13 EA10 EB01 FA02 GA04 GA13 GB01 HA10 4K001 AA01 AA04 AA09 BA22 CA01 CA04 CA25

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 樹脂付電子・電気部品を10mm以下の
大きさに破砕する破砕工程と、この破砕工程で発生する
粉塵を集塵する集塵工程と、上記破砕工程で生成された
破砕物を磁力選別機により100〜2000ガウスで磁
性物と非磁性物とに選別する第1磁力選別工程と、上記
集塵工程で捕集されたダストを磁力選別機により100
〜2000ガウスで磁性物と非磁性物とに選別する第2
磁力選別工程と、上記第2磁力選別工程で得られた非磁
性物を篩い分ける第2篩別工程とを備え、 上記第1、第2磁力選別工程で得られた磁性物と上記第
2篩別工程で得られた網下品とを混合して団鉱し、これ
を錬銅炉にて処理することで有価金属を得ることを特徴
とする樹脂付電子・電気部品からの金属の回収方法。
1. A crushing step for crushing an electronic / electric part with resin into a size of 10 mm or less, a dust collecting step for collecting dust generated in the crushing step, and a crushed material generated in the crushing step. A first magnetic separation step of separating magnetic and non-magnetic substances at 100 to 2,000 gauss by a magnetic separator, and dust collected in the dust collection step by a magnetic separator.
The second to sort magnetic and non-magnetic materials at ~ 2000 Gauss
A magnetic force sorting step, and a second screening step of sieving the non-magnetic material obtained in the second magnetic force sorting step, wherein the magnetic material obtained in the first and second magnetic force sorting steps and the second sieve A method of recovering metal from electronic and electrical parts with resin, comprising mixing and briquetting products obtained in a separate process, briquetting the mixture, and treating it with a wrought copper furnace to obtain valuable metals.
【請求項2】 前記第1磁力選別工程で得られた非磁性
物を篩別機により2mm未満品、2mm以上3mm未満
品、3mm以上5mm未満品、および5mm以上10m
m未満品に篩い分ける第1篩別工程を備え、この第1篩
別工程で得られた2mm未満品および5mm以上10m
m未満品を前記団鉱の材料に混合して団鉱とすることを
特徴とする請求項1に記載の樹脂付電子・電気部品から
の金属の回収方法。
2. The non-magnetic material obtained in the first magnetic separation step is a product of less than 2 mm, a product of 2 mm or more and less than 3 mm, a product of 3 mm or more and less than 5 mm, and a product of 5 mm or more and less than 10 mm by a sieving machine.
a first sieving step of sieving into products having a size of less than 2 m
The method for recovering metal from an electronic / electric part with resin according to claim 1, wherein a product having a diameter of less than m is mixed with the material of the briquette to form briquette.
【請求項3】 前記第1篩別工程で得られる2mm以上
3mm未満品および3mm以上5mm未満品をそれぞれ
風力選別等の比重分離法により重量物と軽量物とに選別
する第1及び第2風力選別工程を備え、この第1、第2
風力選別工程により得られた重量物を前記団鉱の材料に
混合して団鉱とすることを特徴とする請求項2に記載の
樹脂付電子・電気部品からの金属の回収方法。
3. A first and second wind turbines each of which separates a product of 2 mm or more and less than 3 mm and a product of 3 mm or more and less than 5 mm obtained in the first sieving process into a heavy material and a light material by a specific gravity separation method such as a wind separation. A sorting step, and the first and second
The method for recovering metal from an electronic / electric component with resin according to claim 2, wherein a heavy material obtained by a wind separation process is mixed with the material of the briquette to form briquette.
【請求項4】 前記第1篩別工程の前に行われる前記第
1磁力選別工程の前記磁力選別機は、ドラムに配置した
永久磁石により磁力選別し、前記第2篩別工程の前に行
われる前記第2磁力選別工程の前記磁力選別機は、下側
のベルトコンベアで材料を搬送するとともに上側のベル
トコンベアのベルトに交互に配置した永久磁石のS極と
N極により磁力選別することを特徴とする請求項1〜3
のいずれかに記載の樹脂付電子・電気部品からの金属の
回収方法。
4. The magnetic separation machine of the first magnetic separation step, which is performed before the first screening step, performs a magnetic separation by a permanent magnet disposed on a drum, and performs a magnetic separation before the second screening step. In the second magnetic force sorting step, the magnetic force sorting machine conveys the material by the lower belt conveyor and performs magnetic force sorting by the S pole and the N pole of the permanent magnet alternately arranged on the belt of the upper belt conveyor. Claims 1-3
The method for recovering metal from electronic and electrical parts with resin according to any one of the above.
【請求項5】 前記第1篩別工程の前に行われる前記第
1磁力選別工程の前記磁力選別機は、ドラムに配置した
永久磁石により磁力選別し、前記第2篩別工程の前に行
われる前記第2磁力選別工程の前記磁力選別機は、ドラ
ムにS極とN極を交互に配置した永久磁石により磁力選
別することを特徴とする請求項1〜3のいずれかに記載
の樹脂付電子・電気部品からの金属の回収方法。
5. The magnetic force sorting machine of the first magnetic force sorting process, which is performed before the first screening process, performs a magnetic force sorting by a permanent magnet arranged on a drum, and performs a magnetic force sorting before the second screening process. The resin separator according to any one of claims 1 to 3, wherein the magnetic separator in the second magnetic separator is a magnetic separator using a permanent magnet in which S poles and N poles are alternately arranged on a drum. A method for recovering metals from electronic and electrical components.
JP2000400699A 2000-12-28 2000-12-28 Method of recovering metal from electronic / electric parts with resin Expired - Fee Related JP4554068B2 (en)

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