Copper Recycling Technique Using Electrochemical Processes

Copper Recycling Technique Using Electrochemical Processes

FEATURED TOPIC Copper Recycling Technique Using Electrochemical Processes Mitsuyasu OGAWA*, Masahiro KATO, Masatoshi MAJIMA, Tomoyuki AWAZU, Hitoshi YATA and Masaharu OOE ---------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------- The recent growing awareness of the environment and interest in resource saving have raised the importance of metal recycling. As an electric wire maker that handles a large quantity of copper, we strive to promote copper recycling proactively and have developed a copper recycling technique using electrochemical processes for small-scale operations. We made the process as eco-friendly as possible and succeeded in continuously recycling electric wire scrap into high-purity copper. ---------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------- Keywords: electrical wire scrap, copper, recycling, electrochemical, closed system 1. Introduction ering copper from scraped electrical wires. We collect the With the rise in concern about the environment and wire scrap, separate the outer covering from the inner core upsurge of resource nationalism in recent years, metal recy- with a stripping machine, and recycle the copper as a raw cling has become increasingly important. Copper is a material for electrical wires. Thin wires, which cannot be common material we use in everyday life. The Japanese processed by the stripping machine, are fed to a process, 10-yen coin and various types of cables are made of generally called a “nugget process,” which cuts the wires copper. However, the reserves-to-production ratio of into small pieces and sorts them into covering and copper copper is estimated to be 40 years. Therefore, copper is a metal by a physical method (e.g. gravity separation).(5) natural resource of which there are concerns about deple- However, separation is not perfect and a small amount of tion. In addition, the quality of copper concentrate mixed resin and copper pieces is left. It is thought that such extracted from copper mines has been declining over the sludge, which we call a “crushed sample” here, is also used years, which has boosted the load on the extraction and as a recycling material at non-electrochemical refineries. smelting processes.(1) Since the crushed sample, the target of this research, has a Scrapped electronic devices, such as printed wiring simple composition mainly consisting of resin covering boards (PWBs), contain a large amount of useful elements and copper metal, we thought they can be processed with a including precious metals, which are mostly recycled at straightforward electrochemical method. As a model case copper refineries using the non-electrochemical method.*1 of distributed recycling, we have developed an electro- However, it takes much energy and cost to transport chemical recycling technology that is suitable for crushed copper scraps from cities, where they are collected, to samples. refineries, which are often far from cities. And some components in the scrap can produce toxic gases in the recycling process.(2),(3) As mentioned above, the load on 2. Concept of Recycling non-electrochemical refineries has been increasing. And, based on the principle of local production for local The crushed sample, which is the target of this consumption, the need for distributed recycling has been research, is a mixture of small pieces of covering resin and growing. However, as the name suggests, distributed recy- copper metal that cannot be sorted by a physical method. cling tends to be operated on a small scale, which often The concept of our recycling method is to dissolve only the restricts efficiency and cost reduction. On the other hand, copper metal in a solvent and remove the remaining resin, the electrochemical method*2 is suitable for small-scale then recover the copper. Specifically, copper metal is operations with relatively high efficiency, despite some dissolved chemically and recovered by electrodeposition, a problems including effluent treatment. process called “electrowinning.” Electrical wires, which have been our mainstay for a Waste liquid is a significant issue in the electrochem- long time, are often made of high-purity copper because of ical method. To cope with this, a closed system was its excellent electrical conductivity. An electrical wire designed that minimizes waste liquid. In electrowinning in consists of a copper core covered with resign to provide an aqueous solvent, an oxygen-generating reaction by elec- insulation and corrosion resistance. The life of an electrical trolysis of water generally occurs at the anode, which wire is mainly determined by the life of the outer consumes relatively a large amount of electricity. covering(4) and the core can be recycled to copper material. Therefore, a reaction with minimum electric power cost Scrapped electrical wires are collected and the outer was used. In addition, with consideration given to the cost, covering and inner cores are separated, which are recycled ease of handling, and reusability of the chemical liquid, a or disposed of Sumitomo Electric Industries, Ltd. and its trivalent iron ion (Fe3+) was used for dissolving copper group companies have been actively committed to recov- metal (Cu), which was regenerated at the opposite elec- SEI TECHNICAL REVIEW · NUMBER 84 · APRIL 2017 · 93 trode during electrodeposition (Fig. 1). This technique several hours. requires a two-liquid electrolytic bath with a diaphragm A reaction, which is essentially the same as the above that prevents re-dissolution of the recovered copper into equation, is sometimes used to etch copper on PWBs. This the liquid flown from the opposite electrode where it has suggests that developing and applying this process might been regenerated. Sulfuric acid was added to the liquid to make it possible to recover copper from waste etching maintain stability. liquid. 3-2 Resin removal process The copper solution contained covering resin in powder form, which was removed by passing the solution Crushed sample through a general-purpose filter. (copper + resin) 3-3 Electrowinning and liquid regeneration process Diaphragm The solution with the resin removed was poured into a vessel with two sections separated by a diaphragm, such as an ion-exchange membrane, and the positive and negative (1) Feeding the sample electrodes were plunged into the solution in each section. Fe3+ Fe2+ When the electrodes were connected to a power source, copper metal was deposited on the negative electrode, the cathode according to the electroplating principle. At the positive electrode, the anode, an oxidation of iron ions Recovering from bivalent to trivalent occurred, which results in regen- the resin erating the solution so it can dissolve copper again. These reactions are expressed in the following equations: Cu2+ Right- and left-side 2+ - 0 .. (2) Copper dissolution Cathode: Cu + 2e → Cu E = 0.340 V (2) Cu liquids swapped and Fe2+ and resin removal Fe3+ process repeated Anode: Fe2+ → Fe3+ + e- E0 = 0.771 V .. (3) Fe2+ where, e- indicates an electron and E0 the standard electrode potential.(6) At the cathode, if the potential is lower than E0, Power - + the reaction in Eq. (2) moves from left to right. If the supply potential of the anode is higher than E0, the reaction in Base Electrode material Eq. (3) moves from left to right. Since an aqueous solvent H+ (3) Copper is being used, electrolysis of water occurs as a side 2+ recovery and Cu 4 Fe3+ solvent reaction,* which is represented in the following equations: Cu regeneration 2+ Fe + - 0 2 .. Fe2+ Cathode: 2H + 2e → H E = 0.000 V (4) + - 0 Anode: 2H2O → 4H + O2 + 4e E = 1.229 V .. (5) Fig. 1. Concept of this process E0 in Eq. (2) is higher than that in Eq. (4), and E0 in Eq. (3) is lower than that in Eq. (5). This follows that the standard electrode potentials of the reactions of this copper 3. Element Experiment recovery process are inside the standard electrode poten- To evaluate the feasibility of this concept, we built a tials of the electrolysis of water at both the cathode and mini plant with 80 L of liquid per electrode, and conducted anode. Therefore, in principle, it is possible to promote the experimental recovery of copper metal from a crushed copper recovery reaction without involving electrolysis of sample, which is illustrated in Fig. 1. water. 3-1 Copper dissolving process As a result of the experiment, a high current effi- Copper metal is dissolved with a trivalent iron ion ciency*5 of 95% or more was obtained. The oxidation of according to reaction Eq. (1). iron ions, represented in Eq. (3), occurred at near 100% efficiency, which indicates that electrowinning with 2Fe3+ + Cu → 2Fe2+ + Cu2+ .................................... (1) minimal side reaction was achieved. In this reaction, the standard free energy change*3 is negative. Therefore, the reaction should progress spontane- 4. Purity of Recovered Copper ously according to thermodynamics. However, the speed of the reaction is affected by various parameters including the Since high-quality copper is required as a raw mate- surface area of the copper to be dissolved, the concentra- rial of electrical wires, the purity of the recovered copper tion, and the

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