JP2019037945A - Method of recovering valuable metal from printed circuit board scrap - Google Patents

Method of recovering valuable metal from printed circuit board scrap Download PDF

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JP2019037945A
JP2019037945A JP2017162787A JP2017162787A JP2019037945A JP 2019037945 A JP2019037945 A JP 2019037945A JP 2017162787 A JP2017162787 A JP 2017162787A JP 2017162787 A JP2017162787 A JP 2017162787A JP 2019037945 A JP2019037945 A JP 2019037945A
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printed circuit
circuit board
pulverizer
board waste
valuable metals
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JP7171173B2 (en
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秀行 森明
Hideyuki Moriaki
秀行 森明
敬幸 木寺
Atsuyuki Kidera
敬幸 木寺
野村 和弘
Kazuhiro Nomura
和弘 野村
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JX Nippon Mining and Metals Corp
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JX Nippon Mining and Metals Corp
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    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/82Recycling of waste of electrical or electronic equipment [WEEE]

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  • Crushing And Pulverization Processes (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Processing Of Solid Wastes (AREA)
  • Combined Means For Separation Of Solids (AREA)

Abstract

To provide a method of recovering valuable metal from printed circuit board scrap that can improve the recovery rate of valuable metal from the printed circuit board scrap and its quality.SOLUTION: The method has a first step for crushing printed circuit board scrap with an impact crusher (10A, 10B) by one stage or two stages, a second step for crushing the crushed matter that is obtained by crushing the printed circuit board scrap, with a final crusher (10C), and a third step for separating the powder matter that results from crushing with the final crusher, with a pneumatic separator (70), into powder matter mainly composed of valuable metal, and other parts, to recover the valuable metal from the powder matter. The first, second and third steps are continuously performed.SELECTED DRAWING: Figure 3

Description

本発明は、プリント基板屑からの有価金属の回収方法に関する。   The present invention relates to a method for recovering valuable metals from printed circuit board waste.

プリント基板、部品を搭載したプリント基板及びこれらの製造工程で発生する成形残から銅滓などの有価金属を回収する方法が提案されている。   Methods have been proposed for recovering valuable metals such as copper troughs from printed circuit boards, printed circuit boards on which components are mounted, and molding residues generated in these manufacturing processes.

例えば、特許文献1には、処理対象物を粗粉砕し、続けて圧縮力やせん断力などの外力を加えて微粉砕し、微粉砕物を金属分などの比重の大きな物質を多く含む部分及び樹脂などの比重の小さな物質を多く含む部分の比重差を使用して分離し、さらに導電体を多く含む部分と、絶縁体を多く含む部分とに静電分離することにより、有価金属を回収する方法が開示されている。   For example, Patent Document 1 discloses that a processing object is roughly pulverized, and then finely pulverized by applying an external force such as a compressive force or a shearing force. Separation is performed using the specific gravity difference of a part containing a large amount of a material having a small specific gravity such as a resin, and further valuable metal is recovered by electrostatic separation into a part containing a large amount of conductor and a part containing a large amount of an insulator. A method is disclosed.

特開平07−251154号公報Japanese Patent Application Laid-Open No. 07-251154

プリント基板等から銅滓などの有価金属を回収する場合、回収率を高くでき、かつ品位を高くできることが好ましい。   When recovering valuable metals such as copper trough from a printed circuit board or the like, it is preferable that the recovery rate can be increased and the quality can be increased.

本発明は上記の課題に鑑み、プリント基板屑からの有価金属の回収率及び品位を向上させるプリント基板屑からの有価金属の回収方法を提供すること目的とする。   In view of the above problems, an object of the present invention is to provide a method for recovering valuable metals from printed circuit board waste that improves the recovery rate and quality of valuable metals from printed circuit board waste.

本発明に係るプリント基板屑からの有価金属の回収方法は、プリント基板屑を衝撃式粉砕機により1段階又は2段階で粉砕する第1工程と、前記プリント基板屑を粉砕した後の粉砕物を最終粉砕機により粉砕する第2工程と、前記最終粉砕機により粉砕され生成された粉体物を、風力選別機により有価金属を主成分とする粉状物とそれ以外とに分離し、前記粉体物から有価金属を回収する第3工程と、を含んでおり、前記第1工程、前記第2工程及び前記第3工程が、連続的に実施される。   The method for recovering valuable metals from printed circuit board waste according to the present invention includes a first step of pulverizing printed circuit board waste in one or two stages by an impact pulverizer, and a pulverized product after the printed circuit board waste is crushed. A second step of pulverizing by a final pulverizer, and a powdered material pulverized and generated by the final pulverizer separated into a powdery material mainly composed of valuable metals and the other by a wind power sorter; A third step of recovering the valuable metal from the body, and the first step, the second step, and the third step are continuously performed.

本発明に係るプリント基板屑からの有価金属の回収方法によれば、プリント基板屑からの有価金属の回収率及び品位を向上させることができる。   According to the method for recovering valuable metals from printed circuit board waste according to the present invention, the recovery rate and quality of valuable metals from printed circuit board waste can be improved.

廃プリント基板の処理工程を表す工程図である。It is process drawing showing the process of a waste printed circuit board. 廃プリント基板の処理設備を示す図(その1)である。It is FIG. (1) which shows the processing facility of a waste printed board. 廃プリント基板の処理設備を示す図(その2)である。It is FIG. (2) which shows the processing facility of a waste printed board.

図1は、廃プリント基板の処理工程を表す工程図である。図1で例示するように、出発原料は廃プリント基板である。本実施形態において、廃プリント基板とは、電子部品等が実装されていないプリント基板を意味し、電子部品を実装する前のプリント基板(以後、ベタ基板と称する)、電子部品が実装された回路基板の製造工程において、打ち抜きにより発生するプリント基板の成形残(以後、枠基板と称する)、及び切断により発生するプリント基板の切れ端(以後、長尺基板と称する)を含む。   FIG. 1 is a process diagram illustrating a process of processing a waste printed board. As illustrated in FIG. 1, the starting material is a waste printed board. In the present embodiment, the waste printed circuit board means a printed circuit board on which electronic components or the like are not mounted, a printed circuit board before mounting the electronic component (hereinafter referred to as a solid substrate), and a circuit on which the electronic component is mounted. In the substrate manufacturing process, a printed circuit board forming residue (hereinafter referred to as a frame substrate) generated by punching and a printed circuit board cut end (hereinafter referred to as a long substrate) generated by cutting are included.

(予備粉砕)
予備粉砕では、例えば、スクリーン径50mmの一軸粉砕機を用いて、廃プリント基板を1次粉砕で使用する衝撃式粉砕機に投入可能なサイズ(例えば、縦及び横の長さが50mm以下)にする。廃プリント基板のうち、そのサイズが既に1次粉砕で使用する衝撃式粉砕機に投入可能なサイズとなっているもの(例えば、長尺基板)については、予備粉砕は行われない。以後、1次粉砕で使用する衝撃式粉砕機に投入可能なサイズとなっている廃プリント基板をプリント基板屑と称する。
(Preliminary grinding)
In the preliminary pulverization, for example, using a uniaxial pulverizer with a screen diameter of 50 mm, the size of the waste printed circuit board can be put into an impact pulverizer used for primary pulverization (for example, the vertical and horizontal lengths are 50 mm or less). To do. Of the waste printed circuit boards, those whose sizes are already large enough to be put into an impact pulverizer used for primary pulverization (for example, long substrates) are not preliminarily pulverized. Hereinafter, a waste printed circuit board having a size that can be charged into an impact pulverizer used in primary pulverization is referred to as printed circuit board waste.

(1次粉砕:第1工程の一部)
1次粉砕では、プリント基板屑を、例えば、スクリーン径15mmの衝撃式粉砕機を用いて粉砕する。なお、衝撃式粉砕機は、ハンマーミルであることが好ましい。また、1次粉砕を省略してもよい。
(Primary grinding: part of the first step)
In the primary pulverization, the printed circuit board waste is pulverized using, for example, an impact pulverizer having a screen diameter of 15 mm. The impact pulverizer is preferably a hammer mill. Further, primary grinding may be omitted.

(2次粉砕:第1工程の一部)
2次粉砕では、1次粉砕で粉砕したプリント基板屑を、例えば、スクリーン径9mmの衝撃式粉砕機を用いて粉砕する。なお、衝撃式粉砕機は、ハンマーミルであることが好ましい。
(Secondary grinding: part of the first step)
In the secondary pulverization, the printed circuit board waste pulverized by the primary pulverization is pulverized using, for example, an impact pulverizer having a screen diameter of 9 mm. The impact pulverizer is preferably a hammer mill.

(3次粉砕:第2工程)
3次粉砕では、最終粉砕機を用いて、2次粉砕により得られた粉砕物を粉砕し、平均粒径(D50)が200μm〜360μmの粉体物にする。最終粉砕機は、衝撃粉砕機であることが好ましく、ハンマーミル又は高速ハンマーミルであることがより好ましい。なお、高速ハンマーミルは、周速100m/s以上のハンマーミルである。この場合、例えばスクリーン径2mmのスクリーン、又は気流分級により平均粒径(D50)が200μm〜360μmの粉体物を得ることができる。
(Third grinding: second step)
In the tertiary pulverization, the pulverized product obtained by the secondary pulverization is pulverized using a final pulverizer to obtain a powder having an average particle size (D50) of 200 μm to 360 μm. The final pulverizer is preferably an impact pulverizer, and more preferably a hammer mill or a high-speed hammer mill. The high-speed hammer mill is a hammer mill having a peripheral speed of 100 m / s or more. In this case, for example, a screen having a screen diameter of 2 mm, or a powder product having an average particle diameter (D50) of 200 μm to 360 μm can be obtained by airflow classification.

(分離工程:第3工程)
分離工程では、粉体物を、風力選別機により銅滓とそれ以外とに分離し、銅滓を回収する。風力選別機は、二種類以上の成分をそれらの比重差に基づいて分離するもので、バリアブルインパクタ、サイクロン、ミクロンセパレータ(商品名)等が挙げられる。
(Separation process: 3rd process)
In the separation step, the powder material is separated into a copper slag and the other by a wind sorter, and the copper slag is collected. The wind sorter separates two or more types of components based on the difference in specific gravity between them, and examples thereof include a variable impactor, a cyclone, and a micron separator (trade name).

(回収工程)
回収工程では、分離工程において排出された樹脂を含む成分から、バグフィルタなどの集塵装置を用いて樹脂を分離、回収する。このようにして得られた樹脂は、産業廃棄物の焼却炉等で処理することができる。
(Recovery process)
In the recovery process, the resin is separated and recovered from the component containing the resin discharged in the separation process using a dust collector such as a bag filter. The resin thus obtained can be treated in an industrial waste incinerator or the like.

図2には、プリント基板屑の処理設備(基板粉砕設備)100の一例が示されている。図2の基板粉砕設備100は、1次粉砕から3次粉砕までを連続的に実施するための設備である。   FIG. 2 shows an example of a printed board scrap processing facility (substrate grinding facility) 100. The substrate crushing facility 100 in FIG. 2 is a facility for continuously performing from primary crushing to tertiary crushing.

図2に示すように、基板粉砕設備100は、1次粉砕及び2次粉砕に用いられる衝撃式粉砕機として、ハンマーミル10A、10Bを有するとともに、3次粉砕に用いられる最終粉砕機として、ハンマーミル10Cを有する。また、基板粉砕設備100は、分離工程で用いるミクロンセパレータ等の風力選別機70を有する。なお、図示は省略しているが、風力選別機70の後段には、バグフィルタやファン、排気ダクト等が設けられている。   As shown in FIG. 2, the substrate crushing equipment 100 has hammer mills 10A and 10B as impact pulverizers used for primary pulverization and secondary pulverization, and a hammer as a final pulverizer used for tertiary pulverization. It has a mill 10C. In addition, the substrate crushing equipment 100 has a wind sorter 70 such as a micron separator used in the separation process. Although not shown, a bag filter, a fan, an exhaust duct, and the like are provided at the subsequent stage of the wind power sorter 70.

ハンマーミル10Aには、プリント基板屑が投入される。ハンマーミル10Aでプリント基板屑が粉砕されると、下部の排出口から排出され、垂直搬送コンベア20Aによって上方に搬送される。そして、垂直搬送コンベア20Aによって搬送されたプリント基板屑は、ホッパ30Aに投入され、ホッパ30A下方に設けられたスクリューフィーダ40Aにより、次のハンマーミル10Bに投入される。   Printed circuit board waste is put into the hammer mill 10A. When the printed circuit board waste is pulverized by the hammer mill 10A, it is discharged from the lower discharge port and conveyed upward by the vertical conveyor 20A. Then, the printed circuit board waste conveyed by the vertical conveyor 20A is put into the hopper 30A, and is put into the next hammer mill 10B by the screw feeder 40A provided below the hopper 30A.

ハンマーミル10Bに対して1次粉砕されたプリント基板屑が投入されると、さらに粉砕され、粉砕により得られた粉砕物は、下部の排出口から排出され、垂直搬送コンベア20Bによって上方に搬送される。そして、垂直搬送コンベア20Bによって搬送された粉砕物は、ホッパ30Bに投入され、ホッパ30B下方に設けられたスクリューフィーダ40Bにより、次のハンマーミル10Cに投入される。   When the printed circuit board waste that has been primarily pulverized is input to the hammer mill 10B, it is further pulverized, and the pulverized material obtained by the pulverization is discharged from the lower discharge port and conveyed upward by the vertical conveyor 20B. The Then, the crushed material conveyed by the vertical conveyor 20B is put into the hopper 30B, and is put into the next hammer mill 10C by the screw feeder 40B provided below the hopper 30B.

ハンマーミル10Cに対して2次粉砕により得られた粉砕物が投入されると、さらに粉砕され、粉砕により得られた粉体物は、下部の排出口から排出される。この下部の排出口には、風力選別機70に直結された、経路を形成する輸送ダクト(空気輸送管)60が接続されている。このため、風力選別機70が動作を開始すると、輸送ダクト60内に吸引力が生じる。これにより、ハンマーミル10Cから排出された粉体物が吸引され、輸送ダクト60内を通って、風力選別機70内に輸送されるようになっている。   When the pulverized material obtained by the secondary pulverization is input to the hammer mill 10C, the pulverized material is further pulverized, and the powdered material obtained by the pulverization is discharged from the lower discharge port. A transport duct (pneumatic transport pipe) 60 that is directly connected to the wind power sorter 70 and forms a path is connected to the lower discharge port. For this reason, when the wind power sorter 70 starts operation, a suction force is generated in the transport duct 60. As a result, the powder discharged from the hammer mill 10 </ b> C is sucked and transported into the wind power sorter 70 through the transport duct 60.

本実施形態では、ハンマーミル10Cの下部の排出口と風力選別機70とを輸送ダクト60で連結し、ハンマーミル10Cから排出された粉体物を風力選別機70の吸引力で風力選別機70まで搬送することができ、風力選別機70において、銅滓を分離することができる。   In the present embodiment, the discharge port at the lower part of the hammer mill 10 </ b> C and the wind sorter 70 are connected by the transport duct 60, and the powder material discharged from the hammer mill 10 </ b> C is sucked by the wind sorter 70 with the suction force of the wind sorter 70. In the wind power sorter 70, the copper slag can be separated.

また、本実施形態では、1次粉砕から3次粉砕までを連続的に実施することで、ハンマーミル間において作業者が粉砕物や粉体物を搬送等する必要がなくなるため、作業者の作業負担を減らすことができる。   Further, in this embodiment, since the primary pulverization to the tertiary pulverization are continuously performed, it is not necessary for the operator to transport the pulverized material or the powder material between the hammer mills. The burden can be reduced.

ここで、図2の基板粉砕設備100を用いて、1次粉砕〜3次粉砕を連続的に実行した場合には、3つのハンマーミル10A〜10Cを単独で運転して1次粉砕〜3次粉砕を実行した場合と比べて、回収率は同等であるにもかかわらず、銅滓中の銅の品位が20〜30%程度低下することが分かった。   Here, when the primary pulverization to the tertiary pulverization are continuously executed using the substrate pulverization equipment 100 of FIG. 2, the three hammer mills 10A to 10C are operated independently to perform the primary pulverization to the tertiary pulverization. It was found that the quality of copper in the copper slag was reduced by about 20 to 30%, even though the recovery rate was the same as compared with the case where pulverization was performed.

本発明者は、この結果について鋭意検討したところ、ハンマーミル10Cの下部の排出口と風力選別機70とを輸送ダクト60で接続した場合、吸引力が強いため、3次粉砕が十分に行われていない粉砕物が吸引、搬送されている可能性があることに気づいた。そして、本発明者は、このような知見に基づき、図3のような基板粉砕設備100’を開発した。   The present inventor has intensively studied this result, and when the discharge port at the lower part of the hammer mill 10C and the wind sorter 70 are connected by the transport duct 60, since the suction force is strong, the third pulverization is sufficiently performed. I noticed that there was a possibility that the crushed material was not sucked and transported. The inventor has developed a substrate crushing equipment 100 ′ as shown in FIG. 3 based on such knowledge.

基板粉砕設備100’は、図3に示すように、ハンマーミル10Cの下部の排出口と輸送ダクト60との間に上部が開放されたホッパ50が設けられている点が基板粉砕設備100(図2)と異なっている。   As shown in FIG. 3, the substrate crushing equipment 100 ′ is provided with a substrate crushing equipment 100 (FIG. 3) in which a hopper 50 having an open top is provided between the lower outlet of the hammer mill 10C and the transport duct 60. It is different from 2).

図3の基板粉砕設備100’では、下部の排出口から排出される粉体物がホッパ50に投入され、ホッパ50内に投入された粉体物が、風力選別機70が発生する吸引力により輸送ダクト60内を搬送される。図3の例では、この吸引の際に、ホッパ50の上部開口から外気(フリーエア)を取り入れることができるため、吸引力が適度に調整され、粉体物の搬送速度が適度に調整されるようになっている。これにより、ハンマーミル10C内で行われる3次粉砕に対して吸引力が与える影響を抑制することができる。このようにすることで、回収率と銅滓中の銅の品位とを、3つのハンマーミル10A〜10Cを単独で運転して1次粉砕〜3次粉砕を実行した場合と同等にすることができる。   In the substrate crushing equipment 100 ′ of FIG. 3, the powder material discharged from the lower discharge port is put into the hopper 50, and the powder material put into the hopper 50 is sucked by the suction force generated by the wind power sorter 70. It is transported in the transport duct 60. In the example of FIG. 3, since the outside air (free air) can be taken in from the upper opening of the hopper 50 at the time of this suction, the suction force is adjusted appropriately, and the conveying speed of the powder material is adjusted appropriately. It is like that. Thereby, the influence which a suction force has with respect to the 3rd grinding | pulverization performed within the hammer mill 10C can be suppressed. By doing in this way, it is possible to make the recovery rate and the quality of the copper in the copper basket equivalent to the case where the three hammer mills 10A to 10C are operated independently and the primary grinding to the tertiary grinding are executed. it can.

なお、図3の例では、ハンマーミル10Cの下部の排出口と輸送ダクト60との間にホッパ50を設けることで、フリーエアを取り入れる場合について説明したが、これに限られるものではない。例えば、輸送ダクト60とハンマーミル10Cの下部の排出口を直結し、輸送ダクト60又はハンマーミル10Cの下部の排出口の一部にフリーエアを取り入れるための取り込み口を設けることとしてもよい。このようにしても、吸引力を調整し、粉体物の搬送速度を調整することができるため、図3と同様の作用効果を得ることができる。   In the example of FIG. 3, the case has been described in which free air is introduced by providing the hopper 50 between the lower outlet of the hammer mill 10 </ b> C and the transport duct 60, but is not limited thereto. For example, the transport duct 60 and the lower discharge port of the hammer mill 10C may be directly connected, and an intake port for taking in free air may be provided in a part of the lower discharge port of the transport duct 60 or the hammer mill 10C. Even in this case, since the suction force can be adjusted and the conveying speed of the powder can be adjusted, the same effect as that of FIG. 3 can be obtained.

また、図2、図3のように、ハンマーミル10Cで粉砕された粉体物を風力選別機70の吸引力を利用して、風力選別機70まで搬送するため、粉体物を搬送するための装置(コンベヤ等)を用意しなくてもよくなる。これにより、コストを削減することができる。   Further, as shown in FIGS. 2 and 3, the powder material crushed by the hammer mill 10C is transported to the wind power sorter 70 using the suction force of the wind power sorter 70, so that the powder material is transported. It is not necessary to prepare a device (such as a conveyor). Thereby, cost can be reduced.

また、本実施形態によれば、プリント基板屑を衝撃式粉砕機により1段階又は2段階で粉砕し、プリント基板屑を粉砕した後の粉砕物を最終粉砕機により粉砕し、平均粒径(D50)が200μm〜360μmの粉体物にすることで、有価金属と基板層とを十分に剥離することができる。これにより、基板層に付着したままの有価金属の量が低減されるので、有価金属の回収効率を向上させることができる。なお、衝撃式粉砕機はハンマーミルであることが好ましい。この場合、最終粉砕機前のハンマーミルのスクリーン径が8mm以上9mm以下であることが好ましい。また、最終粉砕機は衝撃式粉砕機であることが好ましく、ハンマーミル又は高速ハンマーミル(周速100m/s以上のハンマーミル)であることがより好ましい。   Further, according to the present embodiment, the printed circuit board waste is pulverized in one or two stages by an impact pulverizer, and the pulverized product after pulverizing the printed circuit board waste is pulverized by the final pulverizer to obtain an average particle diameter (D50 ) Can be sufficiently separated from the valuable metal and the substrate layer. As a result, the amount of valuable metal remaining attached to the substrate layer is reduced, so that the recovery efficiency of valuable metal can be improved. The impact pulverizer is preferably a hammer mill. In this case, it is preferable that the screen diameter of the hammer mill before the final pulverizer is 8 mm or more and 9 mm or less. The final pulverizer is preferably an impact pulverizer, more preferably a hammer mill or a high-speed hammer mill (a hammer mill having a peripheral speed of 100 m / s or more).

また、本実施形態によれば、プリント基板屑を衝撃式粉砕機により1段階又は2段階で粉砕し、プリント基板屑を粉砕した後の粉砕物を最終粉砕機により平均粒径(D50)が200μm〜360μmとなるよう粉砕し、最終粉砕機による粉砕によって得られた粉体物を、風力選別機により有価金属を主成分とする粉状物とそれ以外とに分離し、有価金属を回収することで、有価金属の回収効率を向上させることができる。なお、有価金属は銅滓であることが好ましい。   In addition, according to the present embodiment, the printed circuit board waste is pulverized in one or two stages by an impact pulverizer, and the pulverized product after the printed circuit board crushed powder is crushed by the final pulverizer has an average particle diameter (D50) of 200 μm. Crushing to ~ 360 μm, separating the powder obtained by pulverization by the final pulverizer into a powdery substance mainly composed of valuable metals and the other by wind power sorter, and recovering valuable metals Thus, the recovery efficiency of valuable metals can be improved. In addition, it is preferable that a valuable metal is a copper cocoon.

また、本実施形態によれば、風力選別機により分類された樹脂分を主成分とする粉状物をバグフィルタにて回収することで、樹脂分を効率よく回収することができる。   In addition, according to the present embodiment, the resin content can be efficiently recovered by recovering the powdery material mainly composed of the resin content classified by the wind power sorter with the bag filter.

なお、図2、図3の基板粉砕設備100、100’においては、ハンマーミル10A、10Bのいずれか一方を省略し、衝撃式粉砕機による粉砕を1段階としてもよい。   In the substrate crushing equipment 100 and 100 'shown in FIGS. 2 and 3, either one of the hammer mills 10A and 10B may be omitted, and crushing by an impact crusher may be performed in one stage.

以下、本発明の実施例を示すが、本発明は実施例に限定されるものではない。
(実施例1〜6)
表1に示した廃プリント基板を原料とし、それぞれ示された条件により廃プリント基板の粉砕処理を行った。表2に、得られた粉体物の平均粒径(D50)を示す。比較のため、長尺基板を原料とし、予備粉砕を行わず、1次粉砕及び2次粉砕をせん断式の粉砕機で行った。しかしながら、比較例では、2次粉砕の終了時点において、目視の状態でも十分な粉砕物を得ることが出来ず、また、有価金属と基板層とが十分に剥離できていなかったため、2次粉砕の終了時点で粉砕を中止した。
Examples of the present invention will be described below, but the present invention is not limited to the examples.
(Examples 1-6)
The waste printed circuit board shown in Table 1 was used as a raw material, and the waste printed circuit board was pulverized under the indicated conditions. Table 2 shows the average particle diameter (D50) of the obtained powder. For comparison, a long substrate was used as a raw material, and primary pulverization and secondary pulverization were performed with a shearing pulverizer without preliminary pulverization. However, in the comparative example, at the end of the secondary pulverization, a sufficient pulverized product could not be obtained even visually, and the valuable metal and the substrate layer were not sufficiently peeled off. Grinding was stopped at the end.

Figure 2019037945
Figure 2019037945
Figure 2019037945
Figure 2019037945

表2に示すように、実施例1〜6において、得られた粉体物の平均粒径(D50)は、200〜360μmとなり、プリント基板屑を粉状に粉砕することができた。また、目視にて、プリント基板屑が良好に粉砕され、かつ、有価金属と基板層とが十分に剥離されていることが確認された。   As shown in Table 2, in Examples 1-6, the average particle diameter (D50) of the obtained powder was 200-360 μm, and the printed circuit board waste could be pulverized into powder. Moreover, it was confirmed by visual observation that the printed circuit board waste was pulverized well and that the valuable metal and the substrate layer were sufficiently separated.

風力選別機を用いて、上記の粉砕処理により得られた粉体物から銅滓及び樹脂の回収を行った。なお、粉体物に含まれる銅品位、銅量はICP法にて測定して評価した。   Using a wind power sorter, copper slag and resin were collected from the powder obtained by the above pulverization treatment. Note that the copper quality and the amount of copper contained in the powder were measured and evaluated by the ICP method.

実施例1から実施例6で得られた合計の粉体物184kgには、50kgのCuが含まれていたが、56kgの銅滓と128kgの樹脂に分離された。
回収された樹脂成分の銅品位は5%未満であり、銅滓と樹脂とを有効に分離でき、また、高い回収率で銅滓成分が得られることが明らかとなった。
The total amount of powder 184 kg obtained in Examples 1 to 6 contained 50 kg of Cu, but was separated into 56 kg of copper cake and 128 kg of resin.
The copper grade of the recovered resin component was less than 5%, and it was revealed that the copper cocoon and the resin can be effectively separated, and that the copper cocoon component can be obtained with a high recovery rate.

以上、本発明の実施例について詳述したが、本発明は係る特定の実施例に限定されるものではなく、特許請求の範囲に記載された本発明の要旨の範囲内において、種々の変形・変更が可能である。   Although the embodiments of the present invention have been described in detail above, the present invention is not limited to such specific embodiments, and various modifications and changes can be made within the scope of the gist of the present invention described in the claims. It can be changed.

Claims (8)

プリント基板屑を衝撃式粉砕機により1段階又は2段階で粉砕する第1工程と、
前記プリント基板屑を粉砕した後の粉砕物を最終粉砕機により粉砕する第2工程と、
前記最終粉砕機により粉砕され生成された粉体物を、風力選別機により有価金属を主成分とする粉状物とそれ以外とに分離し、前記粉体物から有価金属を回収する第3工程と、を含み、
前記第1工程、前記第2工程及び前記第3工程が、連続的に実施されることを特徴とする、プリント基板屑からの有価金属の回収方法。
A first step of crushing printed circuit board waste in one or two stages with an impact crusher;
A second step of pulverizing the pulverized product after pulverizing the printed circuit board waste with a final pulverizer;
A third step of separating the powdered material pulverized and generated by the final pulverizer into a powdery material mainly composed of valuable metals and the other by a wind power sorter and recovering the valuable metals from the powdered materials. And including
The said 1st process, the said 2nd process, and the said 3rd process are implemented continuously, The collection | recovery method of the valuable metal from printed circuit board waste characterized by the above-mentioned.
前記最終粉砕機で得られる粉体物を風力選別機の吸引力を利用して、該風力選別機に搬送することを特徴とする請求項1に記載のプリント基板屑からの有価金属の回収方法。   The method for recovering valuable metals from printed circuit board waste according to claim 1, wherein the powder obtained by the final pulverizer is conveyed to the wind power sorter by using the suction force of the wind power sorter. . 前記最終粉砕機と前記風力選別機を繋ぐ経路中に外気を取り込む取り込み口を設け、前記最終粉砕機で得られる前記粉体物の搬送速度を調整することを特徴とする請求項2に記載のプリント基板屑からの有価金属の回収方法。   The intake port for taking in outside air is provided in a path connecting the final pulverizer and the wind power sorter, and the conveyance speed of the powder material obtained by the final pulverizer is adjusted. A method for recovering valuable metals from printed circuit board waste. 1段階又は2段階の前記衝撃式粉砕機と前記最終粉砕機とをコンベアで連結し、前記粉砕物及び前記粉体物を連続的に搬送することを特徴とする請求項1〜3のいずれか一項に記載のプリント基板屑からの有価金属の回収方法。   The one-stage or two-stage impact pulverizer and the final pulverizer are connected by a conveyor, and the pulverized material and the powdered material are continuously conveyed. A method for recovering valuable metals from printed circuit board waste according to one item. 前記最終粉砕機により平均粒径(D50)が200μm〜360μmの粉体物が生成されることを特徴とする請求項1〜4のいずれか一項に記載のプリント基板屑からの有価金属の回収方法。   The recovery of valuable metals from printed circuit board waste according to any one of claims 1 to 4, wherein the final pulverizer generates a powder having an average particle size (D50) of 200 µm to 360 µm. Method. 前記衝撃式粉砕機はハンマーミルであることを特徴とする請求項1〜5のいずれか一項に記載のプリント基板屑からの有価金属の回収方法。   The method for recovering valuable metals from printed circuit board waste according to any one of claims 1 to 5, wherein the impact pulverizer is a hammer mill. 前記最終粉砕機が衝撃式粉砕機であることを特徴とする請求項1〜6のいずれか一項に記載のプリント基板屑からの有価金属の回収方法。   The method for recovering valuable metals from printed circuit board waste according to any one of claims 1 to 6, wherein the final pulverizer is an impact pulverizer. 前記衝撃式粉砕機はハンマーミル又は高速ハンマーミルであることを特徴とする請求項7に記載のプリント基板屑からの有価金属の回収方法。   8. The method for recovering valuable metals from printed circuit board waste according to claim 7, wherein the impact pulverizer is a hammer mill or a high-speed hammer mill.
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