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JP7689540B2 - Cu recovery method - Google Patents
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JP7689540B2 - Cu recovery method - Google Patents

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JP7689540B2
JP7689540B2 JP2023028048A JP2023028048A JP7689540B2 JP 7689540 B2 JP7689540 B2 JP 7689540B2 JP 2023028048 A JP2023028048 A JP 2023028048A JP 2023028048 A JP2023028048 A JP 2023028048A JP 7689540 B2 JP7689540 B2 JP 7689540B2
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molten metal
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based molten
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salt
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JP2024121129A (en
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琢真 箕浦
盾 八百川
加瑞馬 日比
伸彦 松本
理恵 荒川
航 高野
亮作 筒井
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Toyota Tsusho Corp
Toyota Central R&D Labs Inc
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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B1/00Preliminary treatment of ores or scrap
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B15/00Obtaining copper
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B21/00Obtaining aluminium
    • 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
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B9/00General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals
    • C22B9/10General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals with refining or fluxing agents; Use of materials therefor, e.g. slagging or scorifying agents
    • 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

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Description

本発明は、再生原料から銅(Cu)を回収する方法等に関する。 The present invention relates to a method for recovering copper (Cu) from recycled raw materials.

環境意識の高揚に伴い、循環型社会の構築が図られている。その一環として金属資源の再生利用(リサイクル)が進められている。その一例として、Cuの回収方法に関連する記載が下記の文献にある。 As environmental awareness grows, efforts are being made to build a recycling-oriented society. As part of this, the reuse (recycling) of metal resources is being promoted. As an example, the following document contains a description of a method for recovering Cu.

特開2021-110026Patent Publication No. 2021-110026

特許文献1は、Al基溶湯(Al-0.7%Mg)とその上に設けた溶融塩層(NaCl+KCl+MgCl)とそれらの接触界面を架橋する黒鉛棒(電極)とを用いて、溶融塩層へ添加した酸化銅(CuO)からCuを黒鉛棒に析出させて回収している。 In Patent Document 1, an Al-based molten metal (Al-0.7% Mg) is used, a molten salt layer (NaCl+KCl+MgCl 2 ) is placed on the Al-based molten metal, and a graphite rod (electrode) bridges the contact interface between the two. Cu is recovered by precipitating it onto the graphite rod from copper oxide (CuO) added to the molten salt layer.

ちなみに、その酸化銅に替えて(純)銅片を溶融塩層へ添加すると、銅片は、その形態に応じて、溶融塩層に浮遊分散したり、Al基溶湯の底部に沈降したり、溶融塩とAl基溶湯の界面付近に析出したりする。このような場合、Cuの効率的な回収は困難である。 Incidentally, if (pure) copper pieces are added to the molten salt layer instead of the copper oxide, the copper pieces will, depending on their form, either float or disperse in the molten salt layer, sink to the bottom of the Al-based molten metal, or precipitate near the interface between the molten salt and the Al-based molten metal. In such cases, it is difficult to efficiently recover Cu.

本発明はこのような事情に鑑みて為されたものであり、再生原料から銅を回収する新たな方法等を提供することを目的とする。 The present invention was made in consideration of these circumstances, and aims to provide a new method for recovering copper from recycled raw materials.

本発明者はこの課題を解決すべく鋭意研究した結果、Al基溶湯のCa濃度によりCuの回収効率が大きく変化することを新たに見出した。この成果を発展させることにより、以降に述べる本発明を完成するに至った。 The inventors conducted extensive research to solve this problem and discovered that the efficiency of Cu recovery varies greatly depending on the Ca concentration in the Al-based molten metal. By expanding on this finding, they were able to complete the present invention, which is described below.

《Cu回収方法》
本発明は、Al基材とCu基材が混在した再生原料を、Al基溶湯上に形成した溶融塩へ入れる処理工程を備え、該Al基溶湯全体に対してCaを0.3質量%以下にして、Cuを該Al基溶湯に溶け込ませて回収するCu回収方法である。
<Cu recovery method>
The present invention provides a Cu recovery method that includes a process of placing a recycled raw material containing a mixture of an Al base and a Cu base into a molten salt formed on an Al-based molten metal, reducing Ca to 0.3 mass% or less with respect to the entire Al-based molten metal, and dissolving Cu into the Al-based molten metal to recover it.

本発明によれば、Al基材とCu基材が混在した再生原料から、CuをAl基溶湯に取り込んで効率的に回収することができる。 According to the present invention, Cu can be efficiently recovered by incorporating it into an Al-based molten metal from recycled raw materials that contain a mixture of Al and Cu base materials.

《Al合金/その製造方法》
本発明は、Cuを含むAl合金(溶湯を含む)またはその製造方法としても把握される。Al基溶湯に取り込まれたCuは、例えば、電解析出等により金属銅(単体)等として分離可能である。もっとも、CuはAl合金の代表的な合金元素でもある。このためCuを取り込んだAl基溶湯(処理工程後のAl基溶湯)は、(再生)Al合金(インゴット、溶湯など)またはその原料として利用されてもよい。
<<Aluminum alloy/its manufacturing method>>
The present invention can also be understood as an Al alloy (including molten metal) containing Cu or a manufacturing method thereof. Cu incorporated in the Al-based molten metal can be separated as metallic copper (single element) by, for example, electrolytic deposition. However, Cu is also a representative alloying element of Al alloys. Therefore, the Al-based molten metal containing Cu (Al-based molten metal after the treatment process) may be used as a (recycled) Al alloy (ingot, molten metal, etc.) or a raw material thereof.

《その他》
(1)本明細書でいう濃度や組成は、特に断らない限り、対象物(溶湯、基材等)の全体に対する質量割合(適宜「%」で示す。)である。
"others"
(1) Unless otherwise specified, concentrations and compositions in this specification are mass percentages (denoted as "%" as appropriate) relative to the entire object (molten metal, base material, etc.).

(2)本明細書でいうAl基溶湯は、Alが主成分(50%超)であれば、Ca以外の具体的な組成を問わない。Al基溶湯は実質的に純Al溶湯(Al:98%以上さらには99%以上)でもよい。なお、Al基溶湯は固液共存状態(半溶融状態)でもよい。 (2) As used herein, the Al-based molten metal may have any specific composition other than Ca, so long as it is mainly composed of Al (more than 50%). The Al-based molten metal may be substantially pure Al molten metal (Al: 98% or more, or even 99% or more). The Al-based molten metal may be in a solid-liquid coexistence state (semi-molten state).

(3)特に断らない限り本明細書でいう「x~y」は下限値xおよび上限値yを含む。本明細書に記載した種々の数値または数値範囲に含まれる任意の数値を新たな下限値または上限値として「a~b」のような範囲を新設し得る。 (3) Unless otherwise specified, "x to y" in this specification includes a lower limit of x and an upper limit of y. Any number included in the various numerical values or numerical ranges described in this specification may be used as a new lower limit or upper limit to create a new range such as "a to b."

再生原料からCuを回収する各工程を示す模式図である。FIG. 2 is a schematic diagram showing each step of recovering Cu from recycled raw materials. Al基溶湯中のCa濃度とそのAl基溶湯に回収されたCu濃度との関係を示すグラフである。1 is a graph showing the relationship between the Ca concentration in an Al-based molten metal and the Cu concentration recovered in the Al-based molten metal.

上述した本発明の構成要素に、本明細書中から任意に選択した一つまたは二つ以上の構成要素を付加し得る。本明細書で説明する内容は、方法的な構成要素であっても物(例えば、再生Al合金(溶湯))に関する構成要素ともなり得る。 One or more components selected from this specification may be added to the components of the present invention described above. The contents described in this specification may be components related to a method or to an object (e.g., recycled Al alloy (molten metal)).

《再生原料》
再生原料は、少なくともAl基材とCu基材が混在してなる。再生原料は、例えば、裁断等された片材(シュレッダー片等)からなる。片材の形態(形状、大きさ)は問わないが、その一片の最大長は、例えば0.1~30mm、1~15mm程度である。
《Recycled raw materials》
The recycled raw material is a mixture of at least an Al base material and a Cu base material. The recycled raw material is, for example, a piece of material that has been cut (such as shredder pieces). The form (shape and size) of the piece of material does not matter, but the maximum length of the piece is, for example, about 0.1 to 30 mm, or 1 to 15 mm.

このような再生原料は、例えば、廃棄される熱交換器や電子・電気機器等が供給源となる。具体的にいうと、Al基材(片)は、例えば、チューブとフィンからなる熱交換器本体、電子基板や放熱板(ヒートシンク)等から得られる。またCu基材(片)は、例えば、熱交換器の配管、基板に設けられる膜状またはワイヤ状の配線(導線)等が供給源となる。 These recycled raw materials are supplied, for example, from discarded heat exchangers and electronic/electrical equipment. Specifically, Al substrates (pieces) are obtained, for example, from heat exchanger bodies consisting of tubes and fins, electronic circuit boards and heat sinks. Cu substrates (pieces) are supplied, for example, from heat exchanger piping and film- or wire-like wiring (conductors) provided on circuit boards.

Al基材やCu基材片の組成は問わない。Al基材は、純Al材でもAl合金材でもよい。またCu基材も純Cu材でもCu合金材でもよい。但し、再生原料は、その全体に対するCa含有量が0.3質量%(単に「%」という。)以下、0.2%以下さらには0.1%以下であると、Cuの回収が安定して効率的になされ得る。 The composition of the Al substrate and Cu substrate pieces does not matter. The Al substrate may be pure Al material or Al alloy material. The Cu substrate may be pure Cu material or Cu alloy material. However, if the Ca content of the recycled raw material is 0.3 mass% or less (simply referred to as "%)", 0.2% or less, or even 0.1% or less, Cu recovery can be performed stably and efficiently.

《Al基溶湯》
Al基溶湯は、少なくとも処理工程前(再生原料を添加・投入等する前)に、Ca濃度が0.3%以下、0.3%未満、0.25%以下、0.2%以下、0.15%以下、0.1%以下、0.05%以下、0.03%以下であるとよい。Ca濃度の下限値は問わないが、敢えていうならCaは0.005%以上、0.01%以上でもよい。本明細書では、適宜、処理工程の開始前(再生原料の添加前)のAl基溶湯を「処理前溶湯」という。
《Al-based molten metal》
The Al-based molten metal may have a Ca concentration of 0.3% or less, less than 0.3%, 0.25% or less, 0.2% or less, 0.15% or less, 0.1% or less, 0.05% or less, or 0.03% or less at least before the treatment process (before the recycled raw material is added or charged). There is no lower limit for the Ca concentration, but if necessary, the Ca concentration may be 0.005% or more, or 0.01% or more. In this specification, the Al-based molten metal before the start of the treatment process (before the recycled raw material is added) is appropriately referred to as the "molten metal before treatment".

処理前溶湯は、純Al溶湯(不可避不純物は含まれ得る。)でもよいし、Cuの回収(溶湯への取り込み)を阻害しない合金元素(Ca以外)を1種以上含んでもよい。 The molten metal before treatment may be pure Al molten metal (which may contain unavoidable impurities), or it may contain one or more alloying elements (other than Ca) that do not inhibit the recovery of Cu (incorporation into the molten metal).

Al基溶湯の成分組成は、処理工程中に加えられる再生原料の種類や量、処理工程の時間等に応じて変動し得るが、Ca濃度が上述した範囲に維持管理されると好ましい。もっとも、再生原料中のCa含有量(特にAl基材中のCa濃度)が十分に小さければ(例えば、0.3%以下、0.2%以下さらには0.1%以下であれば)、Al基溶湯のCa濃度は処理工程中も低く維持され、Al基溶湯によるCuの回収が安定して効率的になされ得る。 The component composition of the Al-based molten metal may vary depending on the type and amount of recycled raw material added during the treatment process, the treatment time, etc., but it is preferable that the Ca concentration be maintained within the above-mentioned range. However, if the Ca content in the recycled raw material (particularly the Ca concentration in the Al base material) is sufficiently small (for example, 0.3% or less, 0.2% or less, or even 0.1% or less), the Ca concentration of the Al-based molten metal will be maintained low during the treatment process, and Cu recovery using the Al-based molten metal will be stable and efficient.

《溶融塩》
溶融塩は、例えば、安定な金属ハロゲン化物(特に塩化物および/または臭化物)を原料とすればよい。ハロゲン化物を構成する金属元素は、例えば、Ca、Na、Li、Sr、K、Mg、Cs、Ba等の一種以上である。Naおよび/またはKのハロゲン化物は、安価で安定しており溶融塩に好適である。
Molten Salt
The molten salt may be prepared, for example, from a stable metal halide (particularly, chloride and/or bromide). The metal element constituting the halide may be, for example, one or more of Ca, Na, Li, Sr, K, Mg, Cs, Ba, etc. Halides of Na and/or K are inexpensive and stable, and are suitable for the molten salt.

溶融塩は、複数種の金属ハロゲン化物が混在した混合塩でもよい。その代表例としてNaClとKClの混合塩がある。溶融塩の配合(成分調整)により、溶融温度、密度等の調整が可能となる。少なくとも溶融塩は、Al基溶湯よりも低密度(比重)であるとよい。なお、溶融塩は、単層に限らず複層でもよい。 The molten salt may be a mixed salt containing multiple types of metal halides. A typical example is a mixed salt of NaCl and KCl. The melting temperature, density, etc. can be adjusted by blending the molten salt (adjusting the components). It is preferable that the molten salt has at least a lower density (specific gravity) than the Al-based molten metal. The molten salt is not limited to a single layer, and may be a multi-layer.

溶融塩の温度は、少なくともAl基材(片)の溶融温度以上(超)であるとよい。溶融塩は、少なくとも再生原料を浸漬させ得る十分な厚さ(例えば層厚が3mm以上さらには10mm以上)があるよい。 The temperature of the molten salt should be at least equal to or higher than the melting temperature of the Al substrate (piece). The molten salt should be thick enough to immerse the recycled raw material (for example, a layer thickness of 3 mm or more, or even 10 mm or more).

《処理工程》
処理工程は、Al基溶湯(処理前溶湯)の湯面を覆う溶融塩(層)へ、再生原料を添加または投入してなされる。再生原料は、連続的に加えられても、断続的に加えられてもよい。処理工程は、Al基溶湯および/または溶融塩を撹拌しつつなされてもよいし、静置した状態でなされてもよい。処理時間(再生原料を添加してからAl基溶湯を取り出すまでの時間)は、例えば、1~180分間さらには10~90分間である。
Processing Steps
The treatment step is performed by adding or pouring the recycled raw material into the molten salt (layer) covering the surface of the Al-based molten metal (molten metal before treatment). The recycled raw material may be added continuously or intermittently. The treatment step may be performed while stirring the Al-based molten metal and/or the molten salt, or may be performed in a stationary state. The treatment time (the time from adding the recycled raw material to removing the Al-based molten metal) is, for example, 1 to 180 minutes, or further 10 to 90 minutes.

処理工程後のAl基溶湯(適宜「処理後溶湯」という。)の取り出しは、断続的でも連続的でもよい。処理後溶湯は、そのまま利用されてもよいし、成分調整がなされて利用されてもよいし、凝固させて利用されてもよい。 The removal of the Al-based molten metal after the treatment process (referred to as the "treated molten metal") may be intermittent or continuous. The treated molten metal may be used as is, may have its composition adjusted, or may be solidified and used.

本発明の一具体例として、純Alからなるフィンやチューブと純Cuからなる配管とを備える熱交換器のシュレッダー片からCuを回収するような場合を想定して、以下の実験を行なった。これにより、Al基溶湯中のCa濃度とそのAl基溶湯に回収されるCu濃度との関係を明らかにした。このような具体例に基づいて、本発明をより詳しく説明する。 As a specific example of the present invention, the following experiment was conducted, assuming a case in which Cu was recovered from shredded pieces of a heat exchanger equipped with fins and tubes made of pure Al and piping made of pure Cu. This clarified the relationship between the Ca concentration in the Al-based molten metal and the Cu concentration recovered in the Al-based molten metal. The present invention will be explained in more detail based on this specific example.

《実験》
(1)Al基溶湯
Ca濃度が異なる7種類のAl基溶湯(処理前溶湯)を調製した。各溶湯の具体的な組成は、純Al(Ca0%)、Al-0.05%Ca、Al-0.08%Ca、Al-0.1%Ca、Al-0.2%Ca、Al-0.3%Ca、Al-0.5%Caとした。Ca濃度は溶湯全体に対するCaの質量割合である。溶湯の原料には、市販の純Alと純Ca(試薬)を用いた。秤量した各原料を黒鉛坩堝(株式会社TYK製)に入れ、720℃(溶解温度)まで炉加熱して完全に溶解させた。こうしてCa濃度が異なるAl基溶湯を50gずつ用意した。
"experiment"
(1) Al-based molten metal Seven types of Al-based molten metal (molten metal before treatment) with different Ca concentrations were prepared. The specific compositions of the molten metals were pure Al (Ca 0%), Al-0.05%Ca, Al-0.08%Ca, Al-0.1%Ca, Al-0.2%Ca, Al-0.3%Ca, and Al-0.5%Ca. The Ca concentration is the mass ratio of Ca to the entire molten metal. Commercially available pure Al and pure Ca (reagent) were used as the raw materials for the molten metal. Each weighed raw material was placed in a graphite crucible (manufactured by TYK Corporation) and heated in a furnace to 720°C (melting temperature) to completely melt it. In this way, 50g of Al-based molten metal with different Ca concentrations was prepared.

(2)溶融塩
ナトリウム塩化物(44g)とカリウム塩化物(56g)との混合塩(100g)をアルミナ坩堝(株式会社ニッカトー製B3)に入れ、720℃(溶解温度)まで炉加熱して完全に溶解させた。こうして混合塩からなる溶融塩(100g)を用意した。溶融塩中のNaClとKClのモル比率は略1となる。
(2) Molten salt A mixed salt (100 g) of sodium chloride (44 g) and potassium chloride (56 g) was placed in an alumina crucible (Nikkato Corporation, B3) and heated to 720°C (melting temperature) in a furnace to completely melt the salt. Thus, a molten salt (100 g) made of the mixed salt was prepared. The molar ratio of NaCl to KCl in the molten salt was approximately 1.

(3)処理浴
黒鉛坩堝内のAl基溶湯をアルミナ坩堝の溶融塩へ静かに注いだ。両者の比重差により、Al基溶湯(下層)上に溶融塩(上層)が形成された二層構造の処理浴がアルミナ坩堝に形成された。
(3) Treatment bath The Al-based molten metal in the graphite crucible was gently poured into the molten salt in the alumina crucible. Due to the difference in specific gravity between the two, a two-layer treatment bath was formed in the alumina crucible, with the molten salt (upper layer) formed on the Al-based molten metal (lower layer).

(4)再生原料
純Al片(Al基材/略1~10mm角)と純Cu片(Cu基材/略1~10mm角)が混在したシュレッダー片(片材)を10g用意した。このシュレッダー片は、実際の廃棄物の裁断片であり、Cu片の混在率(質量割合)はおおよそ9~12%である。
(4) Recycled raw material 10 g of shredded pieces (piece material) containing a mixture of pure Al pieces (Al base material/approximately 1 to 10 mm square) and pure Cu pieces (Cu base material/approximately 1 to 10 mm square) were prepared. These shredded pieces were actual waste fragments, and the Cu piece mixture ratio (mass ratio) was approximately 9 to 12%.

(5)処理工程
図1に示すように、先ず、720℃に保持した処理浴上へ、再生原料を少しずつ静かに添加した。撹拌をせず、そのまま30分間静置した。
(5) Treatment Step As shown in Fig. 1, first, the recycled raw material was slowly and gradually added to the treatment bath maintained at 720°C. The mixture was left to stand for 30 minutes without stirring.

その処理浴を観察すると、再生原料の一部は溶融塩中に微細分散し、残部はAl基溶湯中に溶解した。 When the treatment bath was observed, a portion of the recycled raw material was finely dispersed in the molten salt, while the remainder was dissolved in the Al-based molten metal.

次に、微細な分散粒子を含む溶融塩だけを処理浴から取り除いた(溶融塩の除去工程)。具体的には、アルミナ坩堝を静かに傾動することで上層の溶融塩のみを流し出して行なった。 Next, only the molten salt containing fine dispersed particles was removed from the treatment bath (molten salt removal process). Specifically, this was done by gently tilting the alumina crucible to pour out only the upper layer of molten salt.

さらに、アルミナ坩堝の底部に残ったAl基溶湯(処理後溶湯)を、鋳型(ステンレス製分析型)へ注湯し、大気中で自然冷却して凝固させた。こうして、処理工程後のAl基溶湯が凝固した鋳塊を得た。 The Al-based molten metal (post-treatment molten metal) remaining at the bottom of the alumina crucible was then poured into a mold (stainless steel analytical mold) and allowed to cool naturally in the air and solidify. In this way, an ingot was obtained in which the Al-based molten metal after the treatment process had solidified.

《分析》
各鋳塊中に含まれるCu濃度を蛍光X線分光法(XRF)により分析した。処理前溶湯に含有させたCa濃度と、処理後溶湯が凝固した鋳塊に含まれていたCu濃度との関係を図2に示した。
"analysis"
The Cu concentration in each ingot was analyzed by X-ray fluorescence spectroscopy (XRF). The relationship between the Ca concentration in the molten metal before the treatment and the Cu concentration in the ingot solidified from the molten metal after the treatment is shown in Figure 2.

《評価》
図2から明らかなように、処理前のAl基溶湯のCa濃度が低いほど、再生原料から取り込むCu濃度が高くなることが明らかとなった。この傾向は、そのCa濃度が0.3質量%以下(未満)さらには0.25%以下のときに顕著であった。
"evaluation"
As is clear from Fig. 2, the lower the Ca concentration of the Al-based molten metal before treatment, the higher the Cu concentration taken in from the recycled raw material. This tendency was remarkable when the Ca concentration was 0.3 mass% or less (less than 0.3 mass%) and further 0.25% or less.

以上から、本発明により、再生原料に含まれるCuがAl基溶湯に取り込んで効率的に回収されることが確認された。 From the above, it has been confirmed that the present invention allows the Cu contained in the recycled raw material to be incorporated into the Al-based molten metal and efficiently recovered.

Claims (5)

Al基材とCu基材が混在した再生原料を、Al基溶湯上に形成した溶融塩へ入れる処理工程を備え、
該Al基溶湯全体に対してCaを0.3質量%以下にして、Cuを該Al基溶湯に溶け込ませて回収するCu回収方法。
The method includes a process of inserting a mixed recycled raw material containing an Al base material and a Cu base material into a molten salt formed on an Al-based molten metal,
The Cu recovery method comprises adjusting the Ca content to 0.3 mass % or less relative to the entire Al-based molten metal, and dissolving Cu in the Al-based molten metal to recover it.
前記再生原料は、その全体に対するCa含有量が0.3質量%以下である請求項1に記載のCu回収方法。 The Cu recovery method according to claim 1, wherein the recycled raw material has a Ca content of 0.3 mass% or less relative to the total amount. 前記再生原料は、裁断された片材からなる請求項1に記載のCu回収方法。 The Cu recovery method according to claim 1, wherein the recycled raw material consists of cut pieces of material. 前記溶融塩は、混合塩からなる請求項1に記載のCu回収方法。 The Cu recovery method according to claim 1, wherein the molten salt is a mixed salt. 前記処理工程後のAl基溶湯を再生Al合金として利用する請求項1~4のいずれかに記載のCu回収方法。 A Cu recovery method according to any one of claims 1 to 4, in which the Al-based molten metal after the treatment process is used as recycled Al alloy.
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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016121383A (en) 2014-12-25 2016-07-07 株式会社シンコーフレックス Aluminum / copper alloy production method from lithium ion secondary battery
JP2021110025A (en) 2020-01-15 2021-08-02 株式会社豊田中央研究所 Metal remover
JP2021110026A (en) 2020-01-15 2021-08-02 株式会社豊田中央研究所 Metal removal method and metal recovery method

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016121383A (en) 2014-12-25 2016-07-07 株式会社シンコーフレックス Aluminum / copper alloy production method from lithium ion secondary battery
JP2021110025A (en) 2020-01-15 2021-08-02 株式会社豊田中央研究所 Metal remover
JP2021110026A (en) 2020-01-15 2021-08-02 株式会社豊田中央研究所 Metal removal method and metal recovery method

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