JP2019177361A - Component scrap processing method - Google Patents
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- JP2019177361A JP2019177361A JP2018069023A JP2018069023A JP2019177361A JP 2019177361 A JP2019177361 A JP 2019177361A JP 2018069023 A JP2018069023 A JP 2018069023A JP 2018069023 A JP2018069023 A JP 2018069023A JP 2019177361 A JP2019177361 A JP 2019177361A
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- 238000003672 processing method Methods 0.000 title claims abstract description 18
- 239000000463 material Substances 0.000 claims abstract description 57
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 56
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 56
- 239000000758 substrate Substances 0.000 claims abstract description 42
- 239000002699 waste material Substances 0.000 claims description 94
- 238000000034 method Methods 0.000 claims description 28
- 239000000696 magnetic material Substances 0.000 claims description 4
- 229910052751 metal Inorganic materials 0.000 abstract description 24
- 239000002184 metal Substances 0.000 abstract description 24
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 21
- 239000010949 copper Substances 0.000 description 19
- 229910052802 copper Inorganic materials 0.000 description 19
- 150000002739 metals Chemical class 0.000 description 18
- 238000003723 Smelting Methods 0.000 description 15
- 239000000126 substance Substances 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 8
- 238000004458 analytical method Methods 0.000 description 7
- 239000003990 capacitor Substances 0.000 description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 238000005192 partition Methods 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 4
- 239000010931 gold Substances 0.000 description 4
- 229910052737 gold Inorganic materials 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- 239000003112 inhibitor Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 238000007873 sieving Methods 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 229920003002 synthetic resin Polymers 0.000 description 2
- 239000000057 synthetic resin Substances 0.000 description 2
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000009191 jumping Effects 0.000 description 1
- 238000007885 magnetic separation Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000002940 repellent Effects 0.000 description 1
- 239000005871 repellent Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
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- Processing Of Solid Wastes (AREA)
Abstract
Description
本発明は、部品屑の処理方法に関し、特に、使用済み電子・電気機器部品屑、具体的には電線屑のリサイクル処理に好適な部品屑の処理方法に関する。 The present invention relates to a method for treating component waste, and more particularly to a method for treating component waste suitable for recycling used electronic / electric equipment component waste, specifically, wire waste.
近年、資源保護の観点から、廃家電製品・PCや携帯電話等の電子・電気機器部品屑から、有価金属を回収することがますます盛んになってきており、その効率的な回収方法が検討され、提案されている。 In recent years, from the viewpoint of resource protection, it has become more and more popular to recover valuable metals from scrapped household electrical appliances, scraps of electronic and electrical equipment parts such as PCs and mobile phones. Has been proposed.
例えば、特開平9−78151号公報(特許文献1)では、有価金属を含有するスクラップ類を銅鉱石溶錬用自溶炉へ装入し、有価金属を炉内に滞留するマットへ回収させる工程を含む有価金属のリサイクル方法が記載されている。このようなリサイクル方法によれば、銅溶錬自溶炉での銅製錬にスクラップ処理を組み合わせることができるため、有価金属含有率が低いスクラップ類からでも低コストで有価金属を回収することができる。 For example, in Japanese Patent Laid-Open No. 9-78151 (Patent Document 1), scraps containing valuable metals are charged into a flash melting furnace for copper ore smelting, and the valuable metals are collected in a mat that stays in the furnace. Recycling method for valuable metals including is described. According to such a recycling method, since scrap processing can be combined with copper smelting in a copper smelting flash furnace, valuable metals can be recovered at low cost even from scraps having a low content of valuable metals. .
しかしながら、特許文献1に記載されるような銅溶錬自溶炉を用いた処理においては、電子・電気機器部品屑の処理量が増えることにより、銅溶錬自溶炉でトラブルが発生することが懸念されている。 However, in the process using the copper smelting flash furnace as described in Patent Document 1, troubles occur in the copper smelting flash furnace due to an increase in the processing amount of electronic / electric equipment component waste. There are concerns.
銅溶錬自溶炉の過還元によるトラブルを発生する手法の一つとして、電子・電気機器部品屑を銅溶錬自溶炉で処理する前に電子・電気機器部品屑を粉砕処理し、容量を小さくすることが提案されている。例えば、特開2015−123418号公報(特許文献2)では、銅を含む電気・電子機器部品屑を焼却後、所定のサイズ以下に粉砕し、粉砕した電気・電子機器部品屑を銅の溶錬炉で処理することが記載されている。 As one of the methods for generating troubles due to over-reduction of copper smelting flash smelting furnace, electronic / electrical equipment part waste is pulverized and processed before it is processed in copper smelting flash smelting furnace. It has been proposed to reduce. For example, in Japanese Patent Application Laid-Open No. 2015-123418 (Patent Document 2), electrical / electronic device component waste containing copper is incinerated and then crushed to a predetermined size or less, and the crushed electrical / electronic device component waste is smelted into copper. Processing in a furnace is described.
一方で、電子・電気機器部品屑の処理量が増加することにより、電子・電気機器部品屑に含まれる物質の種類によっては、その後の銅製錬工程での処理に好ましくないアルミニウムなどの物質(製錬阻害物質)を含む不要物が従来よりも多量に投入される場合がある。そのため、電子・電気機器部品屑の中から不要物を適切に除去するとともに、銅製錬工程で回収可能な有価物を効率良く回収するためのこれらの分離技術の向上が望まれている。 On the other hand, due to an increase in the processing amount of electronic / electric equipment component waste, depending on the type of material contained in the electronic / electric equipment component waste, a material such as aluminum (manufactured unfavorable for processing in the subsequent copper smelting process) Unnecessary substances including smelting inhibitors may be introduced in a larger amount than before. Therefore, it is desired to improve these separation techniques for appropriately removing unnecessary materials from the electronic / electric equipment component waste and efficiently recovering valuable materials recoverable in the copper smelting process.
例えば、鉄等の磁性体とアルミ等の非磁性金属とを選別するための装置として渦電流選別機が知られている。渦電流選別機は、磁性体である鉄に加え、銅、アルミ、亜鉛などの非磁性金属、更には電気的導体ではないプラスチックやゴムなどを連続的かつ効率良く自動選別できる点で有利である。 For example, an eddy current sorter is known as a device for sorting a magnetic material such as iron and a non-magnetic metal such as aluminum. The eddy current sorter is advantageous in that it can automatically and efficiently sort nonmagnetic metals such as copper, aluminum, and zinc, as well as plastic and rubber that are not electrical conductors, in addition to iron, which is a magnetic material. .
しかしながら、電子・電気機器部品屑のようにアルミ含有物及び基板屑を含む被処理物を渦電流選別機で選別処理すると、基板屑に含有される銅線などの金属中に渦電流が生じ、アルミ含有物と基板屑とを上手く分離することが困難である。そのため、アルミ含有物の回収に際し、銅等の有価金属を含有する基板屑が多量に混入して有価金属のロスを生じさせる場合があった。 However, when the object to be processed containing aluminum-containing material and substrate waste, such as electronic / electric equipment component waste, is sorted by an eddy current sorter, eddy current is generated in the metal such as copper wire contained in the substrate waste, It is difficult to successfully separate the aluminum-containing material from the substrate waste. Therefore, when recovering the aluminum-containing material, a large amount of substrate scrap containing valuable metals such as copper may be mixed to cause loss of valuable metals.
上記課題を鑑み、本開示は、電子・電気機器部品屑に含まれるアルミ含有物と基板屑とを効率良く分離し、有価金属のロスを低減しながらアルミ含有物を回収することが可能な部品屑の処理方法を提供する。 In view of the above problems, the present disclosure is a component capable of efficiently separating aluminum-containing materials and substrate waste contained in electronic / electric equipment component waste and recovering aluminum-containing materials while reducing loss of valuable metals. Provide a waste disposal method.
上記課題を解決するために本発明者が鋭意検討した結果、偏芯型の渦電流選別機を用いることが有効であるとの知見を得た。 As a result of intensive studies by the present inventor in order to solve the above problems, it has been found that it is effective to use an eccentric eddy current sorter.
本発明の実施の形態に係る部品屑の処理方法は一側面において、偏芯型の渦電流選別機を用いて、電子・電気機器部品屑に含まれるアルミ含有物を反発物側に、基板屑を非反発物側へと選別する工程を含む部品屑の処理方法である。 In one aspect, the component waste processing method according to the embodiment of the present invention uses an eccentric type eddy current sorter to move the aluminum-containing material contained in the electronic / electric equipment component waste to the repulsion side, and the substrate waste. It is a processing method of the component waste including the process of classifying to the non-repellent side.
本開示によれば、電子・電気機器部品屑に含まれるアルミ含有物と基板屑とを効率良く分離し、有価金属のロスを低減しながらアルミ含有物を回収することが可能な部品屑の処理方法が提供できる。 According to the present disclosure, it is possible to efficiently separate the aluminum-containing material and the substrate waste contained in the electronic / electric equipment component waste, and to process the component waste capable of recovering the aluminum-containing material while reducing the loss of valuable metals. A method can be provided.
以下、図面を参照しながら本発明の実施の形態に係る部品屑の処理方法について説明する。なお、以下に示す実施の形態はこの発明の技術的思想を具体化するための装置や方法を例示するものであって、この発明の技術的思想は、各構成部品の構造、配置及び手順等を下記のものに特定するものではない。 Hereinafter, a method for treating component waste according to an embodiment of the present invention will be described with reference to the drawings. The following embodiments exemplify apparatuses and methods for embodying the technical idea of the present invention, and the technical idea of the present invention is the structure, arrangement, procedure, etc. of each component. Is not specified as follows.
本発明の実施の形態に係る部品屑の処理方法は、図1に示すように、偏芯型の渦電流選別機1を用いて、電子・電気機器部品屑10に含まれるアルミ含有物10aを反発物側に、基板屑10bを非反発物側に選別処理し、電子・電気機器部品屑10のアルミニウムを反発物側へと分離させる工程を含む。 As shown in FIG. 1, the component waste processing method according to the embodiment of the present invention uses an eccentric eddy current sorter 1 to remove the aluminum-containing material 10 a contained in the electronic / electric equipment component waste 10. The step of sorting the substrate waste 10b to the non-repulsive material side and separating the aluminum of the electronic / electric equipment component waste 10 to the repulsive material side is included on the repulsive material side.
なお、本実施形態に係る「電子・電気機器部品屑」は、廃家電製品・PCや携帯電話等の電子・電気機器を破砕した屑であり、回収された後、適当な大きさに破砕されたものを指す。この電子・電気機器部品屑は、基板屑、コンデンサ等のパーツ、筐体などに使われる合成樹脂類(プラスチック)、SUS、鉄、アルミ等のメタル類、フィルム状部品屑、破砕や粉砕によって生じる粉状物、その他からなる部品屑を含んでいる。 The “electronic / electrical device parts waste” according to the present embodiment is a waste product obtained by crushing waste electrical appliances / electronic / electrical devices such as PCs and mobile phones, and after being collected, it is crushed to an appropriate size. Refers to things. This electronic / electric equipment component waste is generated by substrate waste, parts such as capacitors, synthetic resins (plastics) used in housings, metals such as SUS, iron and aluminum, film-like component waste, crushing and crushing It contains scraps of powder and other parts.
以下に限定されるものではないが、本実施形態では、粒度100mm以下、より具体的には粒度80mm以下に破砕され、且つ部品屑として単体分離されている割合が重量比で70%以上の電子・電気機器部品屑を好適に処理することができる。 Although not limited to the following, in the present embodiment, an electron having a particle size of 100 mm or less, more specifically, a particle size of 80 mm or less, and a single component separated as a component waste is 70% or more by weight. -Electrical equipment component waste can be treated appropriately.
本発明の実施の形態に係る部品屑の処理方法に特に適した原料としては、種々の部品屑を含む電子・電気機器部品屑10の中でも、アルミ含有物10aを1〜50質量%、基板屑10bを1〜50質量%、より具体的にはアルミ含有物10aを1〜20質量%、基板屑10bを1〜30質量%、更にはアルミ含有物10aを1〜10質量%、基板屑10bを1〜15質量%含有する電子・電気機器部品屑10を使用することができる。アルミ含有物10aとしては、板状又はシート状のアルミ片、コンデンサなどが含まれる。 The raw material particularly suitable for the component waste processing method according to the embodiment of the present invention includes 1 to 50% by mass of the aluminum-containing material 10a among the electronic / electric equipment component scraps 10 including various component scraps, and substrate scraps. 10b is 1 to 50% by mass, more specifically 1 to 20% by mass of aluminum-containing material 10a, 1 to 30% by mass of substrate waste 10b, and further 1 to 10% by mass of aluminum-containing material 10a and 10b of substrate waste It is possible to use electronic / electric equipment component waste 10 containing 1 to 15% by mass. The aluminum-containing material 10a includes a plate-shaped or sheet-shaped aluminum piece, a capacitor, and the like.
このような処理対象物を得るためには、廃家電製品・PCや携帯電話等の電子・電気機器を破砕した後の原料を、風力選別した後の重量物を用いることが好ましく、更にはこの風力選別による重量物に対してスリット状のスリット状の篩を有する篩別機で選別し、篩別機で選別された篩上物を更に風力選別し、風力選別による重量物を磁力選別機で磁力選別した後の非磁性物が好適に利用できる。 In order to obtain such an object to be treated, it is preferable to use a heavy material after wind sorting the raw material after crushing waste home appliances, electronic and electrical equipment such as PCs and mobile phones. Sorting with a sieving machine having a slit-like slit-shaped sieve against heavy objects by wind sorting, further sorting the objects on the sieve selected by the sieving machine with wind, and using heavy objects by magnetic sorting. A non-magnetic material after magnetic separation is preferably used.
このような手順で処理された原料を利用することにより、本実施形態に係る渦電流選別機1によって反発物側への基板屑10bの混入を抑制しながらアルミ含有物10aを反発物側に濃縮させることができるため、アルミ含有物10aを銅製錬処理工程の処理系外へと出すことができる。 By using the raw material treated in such a procedure, the eddy current sorter 1 according to the present embodiment concentrates the aluminum-containing material 10a on the repulsive material side while suppressing the mixing of the substrate waste 10b on the repulsive material side. Therefore, the aluminum-containing material 10a can be taken out of the treatment system of the copper smelting treatment process.
更には、電子・電気機器部品屑10を風力選別する前に、電子・電気機器部品屑10に含まれるネジ及び針金を含むステンレス片を選別する工程を行うことが好ましい。選別は機械を用いた選別でも手選別でも構わない。電子・電気機器部品屑10に含まれるネジ及び針金を含むステンレス片を選別することにより、渦電流選別機1の故障を防いで長期間処理を行うことができる。 Furthermore, it is preferable to perform a step of sorting out the stainless steel pieces including screws and wires contained in the electronic / electric equipment component waste 10 before sorting the electronic / electric equipment component waste 10 by wind power. Sorting may be performed using a machine or by hand. By sorting out the stainless steel pieces including the screws and wires contained in the electronic / electric equipment component waste 10, it is possible to prevent the eddy current sorter 1 from being broken and perform the treatment for a long time.
図1は、本発明の実施の形態に渦電流選別機1を用いて電子・電気機器部品屑10に含まれるアルミ含有物10a、基板屑10b及びその他の合成樹脂類、磁性金属などを含むその他部品屑10cを選別する工程を示している。 FIG. 1 shows an embodiment of the present invention that uses an eddy current sorter 1 to contain aluminum-containing material 10a, substrate waste 10b and other synthetic resins, magnetic metal, etc. contained in electronic / electric equipment component waste 10 The process which sorts out part waste 10c is shown.
渦電流選別機1は、例えば、電子・電気機器部品屑10を搬送する回転ベルト2と、回転ベルト2を回転させるコンベヤヘッドプーリ3と、コンベヤヘッドプーリ3内に配置され、回転ベルト2上の搬送面に磁界を発生させる磁石ドラム4と、回転ベルト2の下方に設けられ、磁石ドラム4が発生させる磁界と反発作用を示すアルミ含有物10aを主として含む反発物を収容するための容器5と、反発物側に収容されない基板屑10b、その他部品屑10cを主として含む非反発物を収容するための容器6と、反発物と非反発物との分離効率向上のために容器5と容器6との間に配置され、傾斜角度及び長さ(高さ)が調整可能な仕切板7とを備える。 The eddy current sorter 1 is, for example, disposed in a rotating belt 2 that conveys electronic / electrical equipment component waste 10, a conveyor head pulley 3 that rotates the rotating belt 2, and the conveyor head pulley 3. A magnetic drum 4 that generates a magnetic field on the conveying surface; and a container 5 that is provided below the rotating belt 2 and that contains a repulsive material mainly including an aluminum-containing material 10a that exhibits a magnetic field and a repulsive action generated by the magnetic drum 4. , A container 6 for containing non-repulsive material mainly containing substrate waste 10b and other component waste 10c that are not accommodated on the repulsive material side, and containers 5 and 6 for improving the separation efficiency between the repulsive material and the non-repulsive material And a partition plate 7 that can be adjusted in inclination angle and length (height).
本実施形態では、磁石ドラム4の直径はコンベヤヘッドプーリ3の直径より小さく、磁石ドラム4の軸芯4aとコンベヤヘッドプーリ3の軸芯3aの位置が異なる偏芯型の渦電流選別機1を用いるのが好ましい。 In this embodiment, the eccentric drum type eddy current sorter 1 in which the diameter of the magnetic drum 4 is smaller than the diameter of the conveyor head pulley 3 and the positions of the axial core 4a of the magnetic drum 4 and the axial core 3a of the conveyor head pulley 3 are different. It is preferable to use it.
渦電流選別機1としては、コンベヤヘッドプーリ3内に配置される磁石ドラム4の軸芯4aが、コンベヤヘッドプーリ3の軸芯3aに対して、コンベヤヘッドプーリ3の回転方向に偏芯角θが0°〜45°で偏芯して配置された偏芯型の渦電流選別機1を用いるのが好ましい。 In the eddy current sorter 1, the shaft core 4 a of the magnetic drum 4 disposed in the conveyor head pulley 3 is offset in the rotational direction of the conveyor head pulley 3 with respect to the shaft core 3 a of the conveyor head pulley 3. It is preferable to use the eccentric type eddy current sorter 1 arranged eccentrically at 0 ° to 45 °.
偏芯型の渦電流選別機1を用いることにより、同心型の渦電流選別機に比べて、回転ベルト2上の飛び出しに最適な位置において、強い磁界を集中的に電子・電気機器部品屑10に与えることができる。これにより、アルミ含有物10aにより強い反発力を生じさせてアルミ含有物10aの飛距離を向上させることができる。 By using the eccentric type eddy current sorter 1, compared with the concentric type eddy current sorter 1, a strong magnetic field is intensively applied to the electronic / electric equipment component waste 10 at a position optimal for jumping on the rotating belt 2. Can be given to. Thereby, the strong repulsive force can be produced by the aluminum containing material 10a, and the flight distance of the aluminum containing material 10a can be improved.
よって、偏芯型の渦電流選別機1を用いることにより、アルミ含有物10aをより選択的に回収することができ、アルミ含有物10a側に混入し得る銅線等を含む基板屑10bとの分離効率を向上させることができる。 Therefore, by using the eccentric type eddy current sorter 1, the aluminum-containing material 10a can be more selectively collected, and the substrate waste 10b including copper wire or the like that can be mixed into the aluminum-containing material 10a side. Separation efficiency can be improved.
なお、ドラム4の軸芯4aは、図1に示すように、コンベヤヘッドプーリ3の軸芯3aに比べて距離dだけ偏芯しており、コンベヤヘッドプーリ3の軸芯3aを通る垂線方向を0°とし、コンベヤヘッドプーリ3の回転方向に正の偏芯角θを有するように偏芯している。偏芯角θは0°〜30°がより好ましく、更に好ましくは0°〜20°である。 As shown in FIG. 1, the shaft core 4 a of the drum 4 is eccentric by a distance d compared to the shaft core 3 a of the conveyor head pulley 3, and the perpendicular direction passing through the shaft core 3 a of the conveyor head pulley 3 is It is set to 0 ° and is eccentric so as to have a positive eccentric angle θ in the rotation direction of the conveyor head pulley 3. The eccentric angle θ is more preferably 0 ° to 30 °, and still more preferably 0 ° to 20 °.
回転ベルト2の速度(ベルト速度)は、遅すぎると処理効率が低下し、速くしすぎると部品の転がりが発生して分離精度が悪化するという場合がある。回転ベルト2の速度は50〜120m/minとすることが好ましく、より好ましくは80〜120m/min、更に好ましくは100〜120m/minである。 If the speed of the rotating belt 2 (belt speed) is too slow, the processing efficiency may decrease, and if it is too fast, parts may roll and the separation accuracy may deteriorate. The speed of the rotating belt 2 is preferably 50 to 120 m / min, more preferably 80 to 120 m / min, and still more preferably 100 to 120 m / min.
磁石ドラム4の回転数は、速くするとアルミニウム含有物の回収効率が向上する一方で、金、銅等の有価金属を含む基板屑10bやこれら有価金属を含むメタル類が非反発物側に混入して有価金属ロスを生じさせる場合がある。磁石ドラム4の回転数は1000〜3000rpmとして処理することが好ましい。回転数はより好ましくは1000〜2500rpmであり、より好ましくは1000〜2000rpmである。 Increasing the rotational speed of the magnet drum 4 improves the recovery efficiency of the aluminum-containing material, while the substrate scrap 10b containing valuable metals such as gold and copper and metals containing these valuable metals are mixed into the non-repulsive material side. May cause valuable metal loss. It is preferable to process the rotational speed of the magnet drum 4 as 1000 to 3000 rpm. The number of rotations is more preferably 1000 to 2500 rpm, and more preferably 1000 to 2000 rpm.
磁石ドラム4の磁力は1000〜5000G、より好ましくは1500〜3500G、更に好ましくは1500〜3000Gとして処理することが好ましい。これにより、基板屑の随伴をより低減した状態でアルミニウム含有物をより多く非反発物側の容器5へと搬送することができる。 The magnetic force of the magnetic drum 4 is preferably 1000 to 5000 G, more preferably 1500 to 3500 G, and still more preferably 1500 to 3000 G. Thereby, more aluminum-containing materials can be conveyed to the container 5 on the non-repulsive material side in a state where the accompanying of the substrate waste is further reduced.
本発明の実施の形態に係る部品屑の処理方法によれば、偏芯型の渦電流選別機1を用いて選別処理を行うことにより、電子・電気機器部品屑に含まれる銅等を含む基板屑10bを反発物側に随伴させることを抑制しながら、アルミ含有物10aを反発物側に濃縮させ、基板屑10bとアルミ含有物10aとを効率良く分離することができる。以下に限定されるものではないが、本発明の実施の形態に係る部品屑の処理方法によれば、被処理物(電子・電気機器部品屑)中のアルミニウムを化学分析値で30質量%以上、より好ましい態様では50質量%、更に好ましい態様では80質量%以上分離することができる。その結果、基板屑10b等に含まれる有価金属のロスを低減しつつ、その後の製錬工程において製錬処理の阻害物質となり得るアルミニウムを選択的に処理系外へと排出することができる。 According to the component waste processing method according to the embodiment of the present invention, the substrate containing copper or the like contained in the electronic / electric equipment component waste by performing the sorting process using the eccentric type eddy current sorter 1. The aluminum containing material 10a can be concentrated on the repulsive material side and the substrate waste 10b and the aluminum containing material 10a can be efficiently separated while suppressing the accompanying of the waste 10b to the repulsive material side. Although not limited to the following, according to the component waste processing method according to the embodiment of the present invention, aluminum in the object to be processed (electronic / electrical device component waste) has a chemical analysis value of 30% by mass or more. In a more preferred embodiment, it can be separated by 50 mass%, and in a more preferred embodiment, it can be separated by 80 mass% or more. As a result, while reducing the loss of valuable metals contained in the substrate scrap 10b and the like, aluminum that can be an inhibitor of the smelting process in the subsequent smelting process can be selectively discharged out of the processing system.
本発明は上記の実施形態に限定されるものではなく、その要旨を逸脱しない範囲で構成要素を変形して具体化できる。また、上記実施形態に開示されている複数の構成要素の適宜な組み合わせにより、種々の発明を形成できる。例えば、実施形態に示される全構成要素からいくつかの構成要素を削除してもよい。更に、異なる実施形態の構成要素を適宜組み合わせてもよい。 The present invention is not limited to the above-described embodiment, and can be embodied by modifying the components without departing from the scope of the invention. In addition, various inventions can be formed by appropriately combining a plurality of components disclosed in the embodiment. For example, some components may be deleted from all the components shown in the embodiment. Furthermore, you may combine the component of different embodiment suitably.
以下に本発明の実施例を比較例と共に示すが、これらの実施例は本発明及びその利点をよりよく理解するために提供するものであり、発明が限定されることを意図するものではない。 Examples of the present invention will be described below together with comparative examples, but these examples are provided for better understanding of the present invention and its advantages, and are not intended to limit the invention.
(実施例1)
廃家電製品・PCや携帯電話等の電子・電気機器を破砕した後の原料を20m/分で風力選別した後のアルミニウム含有物を質量比で5%、基板屑を質量比で2.5%含有する重量物を、日本磁力選鉱製偏芯型渦電流選別機を用いて、ベルト速度を100m/分、磁石ドラムの回転数を1400rpm、磁石ドラムの磁力を3000G、偏芯角θを0°として選別処理した。反発物の外観と化学分析結果を図2に示す。
Example 1
Waste materials, PCs, mobile phones, and other electronic / electrical equipment after crushing raw materials at 20 m / min, the aluminum content is 5% by mass, and substrate scrap is 2.5% by mass. Using an eccentric type eddy current sorter made by Nippon Magnetic Sorting, the heavy weight contained in the belt is 100 m / min, the rotational speed of the magnetic drum is 1400 rpm, the magnetic force of the magnetic drum is 3000 G, and the eccentric angle θ is 0 °. As a sorting process. The appearance and chemical analysis results of the repulsion are shown in FIG.
図2及び以下に示す図2〜6において、表中の「分配」とは、各物質(反発物、基板屑、アルミ片、コンデンサ)に関し、投入した重量(g)に対する反発した重量物(g)の割合(=反発物重量/投入物重量)を示す。 In FIG. 2 and FIGS. 2 to 6 shown below, “distribution” in the table refers to a repulsive heavy object (g) with respect to the input weight (g) with respect to each substance (repulsive object, substrate waste, aluminum piece, capacitor). ) Ratio (= rebound weight / input weight).
図2に示すように、実施例1では、反発物側には外観上は基板の分配がなく、アルミ片の約2割、コンデンサの約4割を反発物側に分離することができた。化学分析の結果、被処理物に対し、約55質量%ものアルミニウムを反発物側に分離できていた。化学分析の結果、金のロス2質量%、銅のロス3質量%と良好な結果が得られた。 As shown in FIG. 2, in Example 1, there was no substrate distribution on the side of the repulsion, and about 20% of the aluminum pieces and about 40% of the capacitor could be separated on the repulsion side. As a result of chemical analysis, about 55% by mass of aluminum was separated on the repulsion side with respect to the object to be treated. As a result of chemical analysis, good results were obtained with a gold loss of 2 mass% and a copper loss of 3 mass%.
(実施例2)
実施例1と同様の重量物に対し、実施例1と同様の偏芯型渦電流選別機を用いて磁石ドラムの回転数を2700rpmとし、その他の条件は実施例1と同様にして選別処理を行った。反発物の外観を図3に示す。
(Example 2)
For the same heavy load as in Example 1, the rotational speed of the magnetic drum was set to 2700 rpm using the eccentric eddy current sorter similar to that in Example 1, and the other conditions were the same as in Example 1. went. The appearance of the resilience is shown in FIG.
実施例2では、アルミ片の約3割、コンデンサの約7割を反発物側に分離でき、化学分析の結果、被処理物に対し、約88質量%ものアルミニウムを反発物側に分離できていた。また、実施例2では基板屑を非反発物側に約8割移行させることができたが、反発物側にも基板屑が約2割分配された。金のロス8質量%、銅のロス7質量%という有価金属のロスも発生した。 In Example 2, about 30% of the aluminum piece and about 70% of the capacitor can be separated on the repulsion side. As a result of chemical analysis, about 88% by mass of aluminum can be separated on the repulsion side. It was. In Example 2, about 80% of the substrate waste could be transferred to the non-repulsive material side, but about 20% of the substrate waste was also distributed to the repulsive material side. Loss of valuable metals, such as gold loss of 8% by mass and copper loss of 7% by mass, also occurred.
実施例2では重量物中のアルミニウムを高効率で回収でき、基板の随伴を抑制してアルミニウム含有物と基板との分離選別も十分行えているが、実施例1と比較すると基板屑の選別効果及び有価金属ロス低減の面ではやや劣っていた。偏芯型の渦電流選別機を用いた場合においても、基板屑に反発力を生じさせない程度の条件にして基板屑の選別効果を更に向上させるためには、回転数をより小さくする方がより好ましいことが分かる。 In Example 2, aluminum in heavy objects can be recovered with high efficiency, and the accompanying of the substrate is suppressed, and the separation and sorting of the aluminum-containing material and the substrate can be sufficiently performed. And it was somewhat inferior in terms of reducing valuable metal loss. Even in the case of using an eccentric type eddy current sorter, in order to further improve the sorting effect of substrate waste under conditions that do not cause repulsive force on the substrate waste, it is better to reduce the rotation speed. It turns out that it is preferable.
(実施例3)
実施例1と同様の重量物に対し、カネテック製偏芯型渦電流選別機を用いて、ベルト速度を60m/分、磁石ドラムの回転数を2500rpm、磁石ドラムの磁力を2800G、偏芯角θを12°として選別処理した。反発物の外観を図4に示す。
(Example 3)
Using the eccentric type eddy current sorter manufactured by Kanetec, the belt speed is 60 m / min, the rotational speed of the magnetic drum is 2500 rpm, the magnetic force of the magnetic drum is 2800 G, and the eccentric angle θ. Was selected as 12 °. The appearance of the resilience is shown in FIG.
実施例3では、アルミ片の約4割、コンデンサの約1割を反発物側に分離でき、化学分析の結果、被処理物に対し、約38質量%のアルミニウムを反発物側に分離できていた。また、実施例3では、基板屑を非反発物側に約8割移行させることができたが、反発物側にも基板屑が約2割分配された。金のロス3質量%銅の5質量%という有価金属のロスも発生した。 In Example 3, about 40% of the aluminum piece and about 10% of the capacitor can be separated on the repulsion side. As a result of chemical analysis, about 38% by mass of aluminum can be separated on the repulsion side. It was. In Example 3, about 80% of the substrate waste could be transferred to the non-repulsive material side, but about 20% of the substrate waste was also distributed to the repulsive material side. The loss of valuable metals, 3% by weight of gold and 5% by weight of copper, also occurred.
(比較例1)
アルミニウム含有物を50質量%、基板屑を50質量%含有する重量物を、同心型の渦電流選別機を用いてベルト速度90m/分、磁石ドラムの回転数1500rpm、磁石ドラムの磁力3000Gで選別処理し、実施例2と同様にアルミニウム分離ができるように仕切板の長さ及び角度を調整した場合の反発物の外観を図5に示す。比較例1では、実施例1と同程度の条件で処理した結果、アルミ片を90質量%除去できたものの、反発物側にも基板屑が50質量%と多量に随伴し、アルミ含有物と基板屑とを効率良く分離できなかった。
(Comparative Example 1)
A heavy material containing 50% by mass of aluminum-containing material and 50% by mass of substrate waste is sorted using a concentric eddy current sorter at a belt speed of 90 m / min, a magnetic drum rotation speed of 1500 rpm, and a magnetic drum magnetic force of 3000 G. FIG. 5 shows the appearance of the resilience when the length and angle of the partition plate are adjusted so that aluminum can be separated in the same manner as in Example 2. In Comparative Example 1, the aluminum piece was removed by 90% by mass as a result of the treatment under the same conditions as in Example 1, but the substrate scrap was accompanied by a large amount of 50% by mass on the repulsion side. The substrate waste could not be separated efficiently.
(比較例2)
実施例1と同様の重量物に対し、同心型の渦電流選別機を用いてベルト速度90m/分、磁石ドラムの回転数1500rpm、磁石ドラムの磁力3000Gで選別処理し、仕切板を調整した場合の反発物の外観と化学分析結果を図6に示す。比較例2では、実施例1と同程度の条件で処理したものの、反発物側に収容された物質の量自体が非常に少なく被処理物が殆ど非反発物側に収容されてしまい、実施例1同程度の処理条件で同心型の渦電流選別を用いた基板屑とアルミニウム含有物との選別は困難であった。また、比較例2では、仕切板を調整して基板屑の混入を防ぐことはできたものの、アルミ片は4質量%、コンデンサも2%質量程度しか回収できず、反発物側に分離されたアルミニウム含有物はかなり少なくなった。
(Comparative Example 2)
When a heavy object similar to that of Example 1 is subjected to a sorting process using a concentric eddy current sorter at a belt speed of 90 m / min, a magnet drum rotation speed of 1500 rpm, and a magnet drum magnetic force of 3000 G, and the partition plate is adjusted. The appearance and chemical analysis results of the repulsion product are shown in FIG. In Comparative Example 2, the treatment was performed under the same conditions as in Example 1, but the amount of the substance accommodated on the side of the repulsion was very small, and the object to be treated was almost contained on the non-repulsion side. It was difficult to sort substrate waste and aluminum-containing material using concentric eddy current sorting under the same processing conditions. Further, in Comparative Example 2, although the partition plate was adjusted to prevent the mixing of the substrate scrap, only about 4% by mass of the aluminum piece and about 2% by mass of the capacitor could be recovered and separated on the repulsion side. The aluminum content was considerably less.
1…渦電流選別機
2…回転ベルト
3…コンベヤヘッドプーリ
3a…軸芯
4…磁石ドラム
4a…軸芯
5…容器
6…容器
7…仕切板
10…電気機器部品屑
10a…アルミ含有物
10b…基板屑
10c…その他他部品屑
DESCRIPTION OF SYMBOLS 1 ... Eddy current sorter 2 ... Rotating belt 3 ... Conveyor head pulley 3a ... Shaft core 4 ... Magnet drum 4a ... Shaft core 5 ... Container 6 ... Container 7 ... Partition plate 10 ... Electrical equipment component waste 10a ... Aluminum content 10b ... Substrate waste 10c ... Other parts waste
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