JP4147246B2 - Method for recovering metallic copper from waste liquid containing copper chloride - Google Patents
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Description
本発明は、塩化銅を含有する工場廃液等から、金属銅を回収する方法に関し、より詳しくは、プリント配線基板等の製造過程で使用されたエッチング廃液から金属銅を回収する方法に関する。 The present invention relates to a method for recovering metallic copper from a factory waste liquid containing copper chloride, and more particularly to a method for recovering metallic copper from an etching waste liquid used in the manufacturing process of a printed wiring board or the like.
プリント配線基板等のエッチング工程で使用されたエッチング溶剤の廃液中には銅成分が塩化銅の形で含有されていることから、回収されたエッチング溶剤の廃液から塩化銅を金属銅として回収するとともにエッチング液を再生する技術が従来からいくつか提案されている。
Since the copper component is contained in the form of copper chloride in the waste liquid of the etching solvent used in the etching process of the printed wiring board, etc., the copper chloride is recovered as metallic copper from the recovered waste liquid of the etching solvent. Several techniques for regenerating an etching solution have been proposed.
回収されたエッチング溶剤の廃液から金属銅を回収するものの1つとして、従来、例えば塩化銅溶液に硫酸溶液を加えて濃縮し、希塩酸を回収し、希塩酸を回収した後の硫酸銅結晶と硫酸銅水溶液の混合物を水で希釈し、希釈工程で結晶を溶解した後の水溶液を電解して金属銅を回収する技術である。(特許文献1参照) As one of the methods for recovering metallic copper from the recovered etching solvent waste liquid, conventionally, for example, a sulfuric acid solution is added to a copper chloride solution and concentrated to recover dilute hydrochloric acid. After recovering dilute hydrochloric acid, copper sulfate crystals and copper sulfate are recovered. In this technique, a mixture of aqueous solutions is diluted with water and the aqueous solution after the crystals are dissolved in the dilution step is electrolyzed to recover metallic copper. (See Patent Document 1)
また、塩化銅含有エッチング廃液をpH9以上のアルカリ液と混合し、この混合液に酸化剤を添加して溶存銅イオンを沈殿させて銅を回収するようにしたものも提案されている。(特許文献2参照) Also proposed is a solution in which copper chloride-containing etching waste liquid is mixed with an alkaline liquid having a pH of 9 or more, and an oxidizing agent is added to the liquid mixture to precipitate dissolved copper ions to recover copper. (See Patent Document 2)
さらに、ニッケル及び銅を多く含む塩化第二鉄のエッチング廃液に、小片状又は塊状の金属鉄を添加して残存塩化第二鉄を塩化第1鉄に還元するとともに、廃液中の銅イオン濃度を10ppm以下になるように銅を析出し、前記還元された液に鉄粉を添加してニッケルを析出除去し、脱ニッケルされた液を酸化して塩化第二鉄に再生するようにする技術も提案されている。(特許文献3)
ところが、前記従来のものでは、いずれも、大型の設備と機械器具を備えなければならず、設備費用が高額になるとともに、必要な工数が多く、金属銅回収のためのコストが高くなるという問題があった。 However, each of the conventional devices has to be equipped with large-scale equipment and machinery, which increases the equipment cost, requires a large number of man-hours, and increases the cost for recovering copper metal. was there.
本発明はこのような点に着目し、簡潔な工程で純度の高い金属銅を回収する方法を提供することを目的とする。 This invention pays attention to such a point, and it aims at providing the method of collect | recovering metallic copper with high purity by a simple process.
上述の目的を達成するために、本発明は鉄粉を粉砕機でより微粉末化し、この微粉末化した鉄粉と水とを混練して泥状鉄水混合物を形成する泥状鉄水混合物作成工程と、塩化銅を含有した塩化第二鉄液の廃液を回収して得られた塩化銅含有廃液に前記泥状鉄水混合物を投入し、攪拌して反応させる攪拌反応工程と、攪拌反応で生成された塩化第一鉄溶液を排出するとともに、底部に沈殿している沈殿物を粉砕機に取出す排出工程と、粉砕機に投入した沈殿物を、pH4以下の塩酸溶液内で粉砕して金属銅を分離させる金属銅分離工程と、取出した金属銅を水洗するすすぎ工程とで構成したことを特徴としている。 In order to achieve the above-mentioned object, the present invention is a muddy iron-water mixture in which iron powder is further pulverized by a pulverizer and the pulverized iron powder and water are kneaded to form a muddy iron-water mixture. A stirring reaction step in which the muddy iron-water mixture is added to the copper chloride-containing waste liquid obtained by recovering the waste liquid of the ferric chloride solution containing copper chloride, and stirred to react; In addition to discharging the ferrous chloride solution produced in step 1, the discharge step of taking out the precipitate precipitated at the bottom to the pulverizer, and pulverizing the precipitate charged in the pulverizer in a hydrochloric acid solution having a pH of 4 or less It is characterized by comprising a metallic copper separation step for separating metallic copper and a rinsing step for washing out the extracted metallic copper.
本発明では、粉砕機により微粉末化した鉄粉と水とを混練することにより得られた泥状鉄水混合物を塩化銅含有廃液に投入攪拌することで、廃液中の塩化第二鉄が鉄粉と発熱を伴って激しく反応して、塩化第一鉄になるとともに、廃液中の塩化第二銅は鉄粉と反応して塩素イオンを放出して金属銅となり、鉄粉が放出し塩素イオンと結合して塩化第一鉄となる。しかし、このとき金属銅は鉄粉の表面をコーティングする状態に付着していることから、金属銅での付着した鉄粉を粉砕機で塩酸存在下で粉砕することで、表面の金属銅に亀裂を生じさせて内部の鉄粉と塩酸とを作用させて鉄分を溶解することで金属銅を分離させ、この金属銅を水洗することで、高純度の金属銅を回収できる。 In the present invention, a slurry-like iron water mixture obtained by kneading iron powder finely pulverized by a pulverizer and water is charged into a copper chloride-containing waste liquid and stirred so that ferric chloride in the waste liquid is iron. It reacts violently with powder and heat generation to become ferrous chloride, and cupric chloride in the waste liquid reacts with iron powder to release chlorine ions to become metallic copper, and iron powder is released to chlorine ions. To ferrous chloride. At this time, however, the metallic copper adheres to the surface of the iron powder coating, so the iron powder adhering to the metallic copper is cracked in the metallic copper on the surface by grinding it in the presence of hydrochloric acid with a grinder The metal copper is separated by causing the internal iron powder and hydrochloric acid to act to dissolve the iron content, and the metal copper is washed with water, whereby high-purity metal copper can be recovered.
以下、本発明方法を一実施形態に基づいて説明する。図1は本発明方法の手順を示す流れ図である。
プリント配線基板等のエッチング工程等で使用されたエッチング溶剤の廃液中には、塩化第二鉄溶液及び塩化第一鉄溶液とともに塩化銅が含有されている。この塩化銅含有廃液を回収する(ステップS1)。
Hereinafter, the method of the present invention will be described based on one embodiment. FIG. 1 is a flowchart showing the procedure of the method of the present invention.
Copper chloride is contained together with the ferric chloride solution and the ferrous chloride solution in the waste liquid of the etching solvent used in the etching process of the printed wiring board and the like. The copper chloride-containing waste liquid is recovered (step S1).
一方、前処理段階として、鉄粉を回転ドラム式粉砕機に投入して、パウダー状の鉄粉となるまで微粉末にする(ステップS2)。この微粉末化した鉄粉を攪拌混合槽に投入し、水を加えて攪拌混合して、鉄粉と水とがスラリー状混合物(泥状鉄水混合物)となるように形成する。(ステップS3) ここで粉砕機により粉砕形成された微粉末は、60から350メッシュの篩を通過できる程度の粒径のものをいう。また、鉄粉をスラリー化して添加するのは反応むらを少なくするとともに、反応を早くするためであり、鉄粉と水とは体積比で、1:1から1:1.5程度の比率で攪拌混合している。 On the other hand, as a pre-treatment stage, iron powder is put into a rotating drum type pulverizer to make a fine powder until it becomes powdery iron powder (step S2). This finely powdered iron powder is put into a stirring and mixing tank, and water is added and stirred and mixed to form a slurry-like mixture (a mud-like iron-water mixture). (Step S3) Here, the fine powder pulverized and formed by the pulverizer has a particle size enough to pass through a sieve of 60 to 350 mesh. The addition of iron powder in a slurry is to reduce reaction unevenness and speed up the reaction, and the iron powder and water are in a volume ratio of about 1: 1 to 1: 1.5. Stir and mix.
前述の塩化銅含有廃液を攪拌槽に注入し、前記泥状鉄水混合物を順次に投入して、攪拌槽内温度を15℃程度に維持しながら攪拌混合する。この塩化銅含有廃液への泥状鉄水混合物投入攪拌により、塩化銅含有廃液中の塩化第二鉄と泥状鉄水混合物中の鉄粉とが発熱反応して、塩化第一鉄になるとともに、塩化銅含有廃液中の塩化銅と泥状鉄水混合物中の鉄粉とが置換反応して、塩化第一鉄と金属銅とに変化する。このとき、金属銅は泥状鉄水混合物中の鉄粉の表面をコーティングする状態に付着した状態で存在することになる。(ステップS4) The above-described copper chloride-containing waste liquid is poured into a stirring tank, the muddy iron water mixture is sequentially added, and stirring and mixing are performed while maintaining the temperature in the stirring tank at about 15 ° C. By adding and stirring the slurry-like iron water mixture into the copper chloride-containing waste liquid, ferric chloride in the copper chloride-containing waste liquid and iron powder in the slurry-like iron-water mixture react exothermically to become ferrous chloride. The copper chloride in the copper chloride-containing waste liquid and the iron powder in the muddy iron water mixture undergo a substitution reaction to change to ferrous chloride and metallic copper. At this time, metallic copper exists in the state which adhered to the state which coats the surface of the iron powder in a muddy iron-water mixture. (Step S4)
そして、塩化銅含有廃液中の反応に関与する塩素成分が消費されて鉄粉との反応が治まると、泥状鉄水混合物の投入を停止する。なお、泥状鉄水混合物の投入を停止した後も数分間(例えば10分間)攪拌を継続した後、攪拌を停止する。(ステップS5) Then, when the chlorine component involved in the reaction in the copper chloride-containing waste liquid is consumed and the reaction with the iron powder is stopped, the introduction of the mud iron water mixture is stopped. The stirring is stopped after the stirring is continued for several minutes (for example, 10 minutes) even after the introduction of the muddy iron-water mixture is stopped. (Step S5)
攪拌停止後、攪拌槽を所定時間(例えば1時間)静置する。(ステップS6)
この静置により、金属銅で表面がコーティングされている鉄粉は攪拌槽の底部に沈殿し、攪拌槽内の液体は塩化第一鉄溶液となる。この塩化第一鉄溶液をポンプで吸い出すとともに、攪拌槽底部に沈殿滞留している銅で被覆された鉄粉を粉砕機に取出す。(ステップS7)
After the stirring is stopped, the stirring tank is allowed to stand for a predetermined time (for example, 1 hour). (Step S6)
By this standing, the iron powder whose surface is coated with metallic copper precipitates at the bottom of the stirring tank, and the liquid in the stirring tank becomes a ferrous chloride solution. While sucking out this ferrous chloride solution with a pump, the iron powder coat | covered with the copper settled and accumulated in the bottom part of a stirring tank is taken out to a grinder. (Step S7)
粉砕機では、前述の銅で被覆された鉄粉に塩酸を投入し、粉砕機内の液の水素指数をpH4以下、好ましくはpH1〜3の範囲に保持しながら銅で被覆された鉄粉を破砕する。この破砕により、被覆している銅に亀裂が生じ、この亀裂から塩酸が被覆銅内に浸入して被覆銅内の鉄粉や他の金属と反応し、鉄や他の金属(不純物)を取り除き、金属銅を分離する。このとき、鉄粉等にととも取り込まれたカーボンは、破砕に伴う攪拌で粉砕機中の液面に浮揚してくる。(ステップS8) In the pulverizer, hydrochloric acid is added to the iron powder coated with copper, and the iron powder coated with copper is crushed while maintaining the hydrogen index of the liquid in the pulverizer at pH 4 or less, preferably in the range of pH 1 to 3. To do. This crushing causes cracks in the coated copper, and hydrochloric acid penetrates into the coated copper from this crack and reacts with iron powder and other metals in the coated copper to remove iron and other metals (impurities). , Isolate the copper metal. At this time, the carbon taken in along with the iron powder and the like floats on the liquid surface in the pulverizer by stirring accompanying crushing. (Step S8)
塩酸浴中で分離された金属銅は塩酸を排出した後、水道水の後に精製水で洗浄するすすぎ工程(ステップS9)を経た後、金属銅として取出す。(ステップS10)
ここで、先に水道水でのすすぎを行うのは、経済的事情によるものであり、最終段階として精製水ですすぎを行うのは、不純物の付着を防止するためである。
The metallic copper separated in the hydrochloric acid bath is taken out as metallic copper after passing through a rinsing step (step S9) in which the hydrochloric acid is discharged and then washed with purified water after tap water. (Step S10)
Here, the rinsing with tap water is for economic reasons, and the rinsing with purified water as a final step is to prevent the adhesion of impurities.
また、ステップS8の金属銅分離工程と、ステップS9のすすぎ工程とを数回繰り返し、上澄液が無色になるまで繰り返すことで、回収する金属銅の純度を98%以上の純度まで高めることができる。 In addition, the metal copper separation process in step S8 and the rinsing process in step S9 are repeated several times until the supernatant becomes colorless, thereby increasing the purity of the recovered metal copper to 98% or more. it can.
上述の実施手順で、前処理段階として鉄粉を粉砕して微粉末にしているが、この場合の鉄粉としては、ショットブラスト作業の結果得られた鉄粉を使用しているが、研磨作業や研削作業で得られたチップ状鉄粉を破砕したものであってもよい。また、鉄粉やチップ状鉄粉を界面活性剤と水とで洗浄して油分を除去した後に粉砕して微粉末にすることもある。 In the above implementation procedure, the iron powder is pulverized into a fine powder as the pretreatment stage, but as the iron powder in this case, the iron powder obtained as a result of the shot blasting work is used, but the polishing work Or the chip-like iron powder obtained by grinding operation may be crushed. In addition, iron powder or chip-like iron powder may be washed with a surfactant and water to remove oil and then pulverized into a fine powder.
また、すすぎ工程の終盤において、処理水の水素指数がpH7程度になった際に水道水あるいは精製水中に処理物(金属銅)を所定時間放置したのち排水するようにすると、その放置により、塩化第一鉄の残液が水酸化鉄溶液になって上澄液に溶け込むことから、取り出された金属銅の純度をさらに向上させることができる。 Also, at the end of the rinsing process, when the hydrogen index of the treated water reaches about pH 7, if the treated product (metal copper) is left in the tap water or purified water for a predetermined time and then discharged, Since the residual liquid of ferrous iron becomes an iron hydroxide solution and dissolves in the supernatant, the purity of the extracted metallic copper can be further improved.
本発明は、プリント基板のエッチングをはじめとする銅板のエッチングなどに使用した塩化第一鉄廃液から金属銅を回収するものに利用することができる。 INDUSTRIAL APPLICATION This invention can be utilized for what collect | recovers metallic copper from the ferrous chloride waste liquid used for the etching of copper plates including the etching of a printed circuit board.
Claims (2)
塩化銅を含有した塩化第二鉄液の廃液を回収して得られた塩化銅含有廃液に前記泥状鉄水混合物を投入し、攪拌して反応させる攪拌反応工程と、
攪拌反応で生成された塩化第一鉄溶液を排出するとともに、底部に沈殿している沈殿物を粉砕機に取出す排出工程と、
粉砕機に投入した沈殿物を、pH4以下の塩酸溶液内で粉砕して金属銅を分離させる金属銅分離工程と、
取出した金属銅を水洗するすすぎ工程、
とからなることを特徴とする塩化銅含有工場廃液からの金属銅回収方法。 A muddy iron water mixture creating step in which the iron powder is further finely pulverized by a pulverizer, and the fine powdered iron powder and water are kneaded to form a muddy iron water mixture
A stirring reaction step of adding the muddy iron-water mixture to the copper chloride-containing waste liquid obtained by recovering the waste liquid of ferric chloride liquid containing copper chloride, and stirring and reacting;
A discharge step of discharging the ferrous chloride solution generated by the stirring reaction and taking out the precipitate precipitated at the bottom to a pulverizer,
A metal copper separation step of separating the metal copper by pulverizing the precipitate charged in the pulverizer in a hydrochloric acid solution having a pH of 4 or less;
A rinsing step of washing out the extracted copper metal,
A method for recovering metallic copper from a waste liquid containing a copper chloride-containing factory.
The method for recovering metallic copper from a copper chloride-containing factory waste liquid according to claim 1, wherein the metallic copper separation step and the rinsing step are repeated.
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| CN106521166A (en) * | 2016-11-29 | 2017-03-22 | 湖南埃格环保科技有限公司 | Method for preparing copper powder and ferrous sulfate by using solution leached through sludge containing copper wet method |
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| JP5880931B2 (en) * | 2011-11-30 | 2016-03-09 | 住友重機械工業株式会社 | 64Cu separation and purification method and 64Cu separation and purification apparatus |
| JP7453002B2 (en) * | 2020-01-22 | 2024-03-19 | 大口電子株式会社 | How to collect silver |
| CN112777710B (en) * | 2021-01-13 | 2023-05-09 | 陕西高科环保科技有限公司 | Automatic recovery unit of copper-containing waste water |
| CN112919672A (en) * | 2021-01-25 | 2021-06-08 | 湖北林泰环境科技有限公司 | Method for preparing high-purity copper powder and ferrous chloride water purifying agent by using waste acidic etching solution |
| CN114734050B (en) * | 2022-04-01 | 2024-06-21 | 浙江旭德新材料有限公司 | Preparation machine and preparation method of superfine pure copper powder for thermal spraying technology |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN106521166A (en) * | 2016-11-29 | 2017-03-22 | 湖南埃格环保科技有限公司 | Method for preparing copper powder and ferrous sulfate by using solution leached through sludge containing copper wet method |
| CN106521166B (en) * | 2016-11-29 | 2018-09-18 | 湖南埃格环保科技有限公司 | A method of preparing copper powder and ferrous sulfate using copper-contained sludge wet-leaching solution |
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