TW201732088A - Method for recovering metal from printed circuit boards by using hydrochloride acid - Google Patents

Abstract

The invention provides a method for recovering metal from printed circuit boards by using hydrochloride acid which adopts a hydrometallurgical process to recover precious metals from waste printed circuit boards. To simplify the metal leaching process, large pieces of PCBs were used instead of a pulverized sample. The chemical coating present on the PCBs was removed by sodium hydroxide treatment prior to the hydrometallurgical treatment. Among the leaching reagents, hydrochloric acid showed great potential for the recovery of metals. Increasing the acid concentration decreased the time required for complete metal recovery. The shaking speed showed a positive effect on metal recovery. The results showed that 1 M HCl dissolved and then recovered all of the metals from 4*4 cm PCBs at 25 DEG C and 150 rpm shaking speed lasting for 22 h.

Description

Method for recovering metal in printed circuit board by using hydrochloric acid

The present invention relates to a wet metallurgy process for recovering metals, and more particularly to a method for recovering metals in a printed circuit board using hydrochloric acid.

Due to the development of information technology, the products of electric and electronic equipment (EEE) have increased rapidly, and printed circuit boards (PCBs) are almost the necessary originals for all discarded equipment. EEE's rapid technological development has shortened its life cycle, which in turn has resulted in a large number of discarded PCBs being manufactured, thus creating new environmental problems. The metal content of discarded PCBs can be as high as 40%, which basically includes copper, tin, lead, cadmium, chromium, zinc, nickel and manganese. Therefore, a special purpose for recycling waste EEE is to recover PCBs, which can be the second source of valuable metals. Recycling waste PCBs not only helps to reuse resources, but also protects the environment.

In recent years, a variety of high temperature metallurgy and wet metallurgy methods have been used to recover metals from discarded PCBs. Among them, pyrometallurgical method must heat the discarded PCBs to high temperature, but these treatments lead to the generation of harmful gases. The reason is that halogen-resistant materials are widely used in EEE, and the production of dioxin and furan in the high temperature environment is unavoidable. Environmental problems are caused, so exhaust gas treatment is a prerequisite, and these cleaning methods are not only energy-intensive but also costly. In addition, pyrometallurgy has high quality requirements for PCBs (ie, wastes rich in copper and precious metals). Compared to higher temperature metallurgy, wet metallurgy offers lower capital costs, reduced environmental impact and high metal recovery, and is relatively suitable for small-scale applications, making wet metallurgy a potential option. Used to dispose of discarded EEE.

Wet metallurgy involves the dissolution of metals in alkaline or acidic media. Many studies have indicated that nitric acid, hydrochloric acid, sulfuric acid and aqua regia can be used to recover metals from waste PCBs. Reagents such as halides, thioides, and the like are also commonly used to recover precious metals. Most of the above studies reported the use of powdered/pulverized waste PCBs for metal recovery, but fewer people use large-scale PCBs because of the poor metal recovery of large sheet PCBs by wet metallurgy. In the wet metallurgy recovery method, it has also been reported that the above-mentioned leaching agent is used for the sheet PCBs. If the metal can be completely recovered from the large-sized PCBs, the remaining substrate (the metal-free portion) can be easily recovered, whereas the pulverized PCBs are not easily recovered. There is therefore a need for a simplified method of recovering metals and the complete recovery of valuable metals from PCBs.

The invention provides a method for recovering metal in a printed circuit board by using hydrochloric acid, which belongs to the wet metallurgy method, is for pre-processing to remove the chemical coating on the PCBs for the large-sized PCBs, and then performing acid leaching treatment. Dissolve the metal in the PCBs and mix air during the leaching process. In the present invention, a plurality of process parameters for metal recovery are also optimized.

The invention provides a method for recovering metal in a printed circuit board by using hydrochloric acid, comprising: a cutting step of cutting a printed circuit board into a predetermined size; and a pre-processing step of removing one of the predetermined size of the printed circuit board a chemical coating; a leaching step of immersing the printed circuit board of the chemical coating in a hydrochloric acid, and mixing oxygen to generate chlorine gas, so that the hydrochloric acid dissolves one of the metals in the printed circuit board to form a metal compound a leaching solution; a separating step of separating the printed circuit board to obtain the leaching solution; and a purification step of purifying the leaching solution to obtain the metal, wherein the metal comprises copper, lead, silver, platinum, and gold At least one of them.

In one embodiment, the pre-treating step comprises immersing the printed circuit board in a sodium hydroxide solution to remove a chemical coating on the printed circuit board.

In one embodiment, the concentration of the hydrochloric acid in the leaching step is 0.1 to 12M.

In one embodiment, the concentration of the hydrochloric acid in the leaching step is 1 to 6 M.

In one embodiment, the method of mixing oxygen into the leaching step comprises a convolution.

In one embodiment, the speed of the convolution oscillation in the leaching step is 50 to 500 rpm.

In an embodiment, the speed of the gyro oscillation in the leaching step is 50 to 200 rpm.

In an embodiment, the metal further comprises at least one of zinc, tin, nickel, iron, and aluminum.

In one embodiment, the purification step comprises purifying the metal from the leach solution by solution extraction, activated carbon adsorption, ion exchange, precipitation, cementation, and electrowinning.

Based on the above, the present invention replaces the pulverized PCBs with sheet-like PCBs, and can easily separate the PCBs from the leaching solution, thereby effectively simplifying the process of recovering metals. In addition, the present invention utilizes hydrochloric acid as a leaching agent to completely dissolve the metal in the PCBs and shorten the leaching time, thus providing an economical choice for the method of recovering metals.

S11‧‧‧ cutting steps

S13‧‧‧Pretreatment steps

S15‧‧‧ leaching steps

S17‧‧‧Separation step

S19‧‧‧Purification step

1 is a flow chart showing a method for recovering metal in a printed circuit board using hydrochloric acid according to the present invention; and FIG. 2 is a view showing a relationship between a leaching agent and a leaching time in the embodiment and the comparative example of FIG. 1; 3b is a graph showing the relationship between the leaching agent and the metal removal rate in the embodiment of Fig. 1; Fig. 4 is a graph showing the relationship between the hydrochloric acid concentration and the leaching time in the embodiment of Fig. 1; A graph of the relationship between the rotational speed of the embodiment and the metal removal rate in the embodiment; and Fig. 6 is a graph showing the relationship between the PCBs size and the leaching time in the embodiment of Fig. 1.

Hereinafter, a method of recovering metal in a printed circuit board using hydrochloric acid according to an embodiment of the present invention will be described with reference to FIG. First, a cutting step (S11) is performed: PCBs containing various precious metals are collected from the waste recycling site, connecting elements on the PCBs and harmful substances are removed, and then the PCBs can be cut into predetermined sizes by conventional means. In the present invention, the predetermined size is exemplified by, but not limited to, a sheet shape cut into 2 × 2, 4 × 4, and 6 × 6 cm.

Next, a pretreatment step (S13) is performed: since the PCBs have a chemical coating (solderproof layer), which is usually made of an epoxy resin, the chemical coating covers the metal lines, so that the leaching agent cannot penetrate therein. The metal cannot be dissolved, so the cut and predetermined PCBs can be placed in a 10M sodium hydroxide solution and soaked overnight to remove the chemical coating such as the solder mask. After soaking, the PCBs can be cleaned with running tap water and then rinsed with distilled water to completely remove the sodium hydroxide from the PCBs.

Then proceed to the leaching step (S15): first dilute with deionized water as leaching The hydrochloric acid of the agent is prepared as a leach solution, and the concentration of hydrochloric acid in the leach solution may be 0.1 to 12M. When the concentration is close to the lower limit, the reaction between hydrochloric acid and metal is less severe and has better safety. When the concentration is close to the upper limit, the reaction speed is faster, and the process time can be shortened. Therefore, the safety and process can be considered. Balance in time. In the present embodiment, the concentration of hydrochloric acid is preferably from 1 to 6 M, more preferably from 1 to 3 M. The cleaned PCBs are then immersed in a vessel containing a predetermined concentration of the leachate. The vessel can be placed on a cyclotron, swirled at a constant temperature to mix oxygen, and reacted with hydrochloric acid to produce chlorine. The metal on the PCBs reacts with oxygen, chlorine, and hydrochloric acid to form a metal compound that is soluble in water, that is, the metal on the PCBs is leached by the leach solution to obtain a leach solution containing the metal compound. The rotational speed of the convolution may be 50-500 rpm, preferably 50-200 rpm; the constant temperature may be any temperature in the range of 25-60 °C.

Thereafter, a separation step (S17) is carried out, and the leached PCBs can be separated by a conventional separation and filtration means to obtain a leach solution containing a metal compound. For example, but not limited to, the separation can be accomplished by directly removing the PCBs from the container using a jig.

Purification step (S19), the leaching solution obtained in the above step is obtained by a conventional purification method, and the purification method is exemplified by, but not limited to, solution extraction, activated carbon adsorption, ion exchange, precipitation, cementation, and electrolysis. Metallurgical law.

By recovering the metal in the printed circuit board by using hydrochloric acid in FIG. 1 , the metal in the PCBs can be completely dissolved, and the leachate containing the metal compound can be further purified from the metal, and the zinc, tin and nickel can be completely recovered from the PCBs. Iron, aluminum and aluminum can completely recover metals such as copper, lead, silver, platinum and gold.

Based on the above description, a method of recovering metal in a printed circuit board using hydrochloric acid in an embodiment of the present invention will be further described below with reference to FIG. 1 through an embodiment. However, the embodiments of the present invention are susceptible to those skilled in the art and are not intended to limit the implementation of the present invention. Any changes or modifications made by those skilled in the art will be covered by the spirit of the present invention. Within the scope of the patent application in this case.

Example 1

The collected PCBs are first cut into 4×4cm sheets (step S11), and the cut PCBs are placed in a 10M sodium hydroxide solution and soaked overnight to remove the chemical coating on the PCBs (solderproofing) Floor). Next, the PCBs are washed with running tap water and then washed with distilled water until the sodium hydroxide on the PCBs is completely removed (step S13). Pretreated PCBs and sodium hydroxide solution respectively The metal content was analyzed by an inductively coupled plasma mass spectrometer (ICP). Then, 37% (12M) concentrated hydrochloric acid was diluted with deionized water to 1M hydrochloric acid as a leach solution, 100 mL of the leachate was poured into a 500 mL beaker, and the cut PCBs (4×4 cm) were placed. Into the beaker. The beakers containing the PCBs were placed in a cyclotron, and the PCBs were leached at a return rotation speed of 150 rpm and room temperature (25 ° C) to completely dissolve the metal therein (step S15). Next, the PCBs are taken out from the beaker to obtain a metal-impregnated leach solution in the beaker (step S17). After obtaining the metal-dissolved leach solution, the extracted PCBs and the metal-impregnated leach solution can be analyzed by ICP for the metal content.

Then, the metal-dissolved leach solution obtained in the above step is purified to further completely recover the metal in the PCBs. The purification method may include a solution extraction method, an activated carbon adsorption method, an ion exchange method, a precipitation method, a cementation method, and an electrolytic metallurgy method (step S19).

Example 2~6

In the same operation procedure as in the first embodiment, the size of the fixed PCBs was 4×4 cm, the leaching time was 22 h, and the return rotation speed was 150 rpm, and only the hydrochloric acid concentration of the leachate was sequentially adjusted to 2M, 3M, 4M, 5M, and 6M. The effect of the hydrochloric acid concentration on the leaching time was compared with Example 1.

Example 7~10

In the same manner as in the operation of Example 1, the size of the fixed PCBs was 4 × 4 cm, the concentration of hydrochloric acid in the leaching solution was 1 M, and the return rotation speed was only sequentially adjusted to 0 rpm, 50 rpm, 100 rpm, and 200 rpm. The effect of the rotational speed on the leaching time was compared with Example 1.

Examples 11~12

In the same procedure as in the first embodiment, the hydrochloric acid concentration of the fixed leach solution was 1 M, and the rotational speed was 150 rpm. Only the dimensions of the PCBs were cut into 2 x 2 cm and 6 x 6 cm, respectively. The effect of PCB size on the leaching time was compared with Example 1.

Comparative example 1~4

As in the operation method of Example 1, the size of the fixed PCBs was 4 × 4 cm, and the rotational speed was 150 rpm, and only 1 M hydrochloric acid was sequentially replaced with the same concentration of nitric acid, sulfuric acid, acetic acid, and oxalic acid. The leaching solution in which the metal was dissolved in the step S17 was subjected to ICP to analyze the metal content therein, and the relationship between the leaching time and the recovery rate of the leaching agent was compared with Example 1.

Results and discussion

(metal content of sodium hydroxide solution)

In Example 1, the sodium hydroxide solution after the immersion treatment was analyzed by ICP as shown in Table 1. As shown, aluminum, zinc, tin, iron, lead, copper, and nickel were observed to be eluted in a small amount, while silver, platinum, and gold were not detected (thus not shown in Table 1).

(metal content in PCBs)

In Example 1, after the pretreatment of the sodium hydroxide solution, the PCBs before the leaching were analyzed by ICP, and the contents of the respective metals are shown in Table 2.

(effect of leaching agent)

Since the metal content in the leachate will affect the final metal recovery obtained in the purification step S19, the present invention will be directed to the dissolution effect of the leachate on the metal. Line discussion.

Fig. 2 is a view showing the influence of different acids as the leaching agent on the leaching time in Example 1 and Comparative Examples 1 to 4, and Figs. 3a and 3b show the leaching time shown in Fig. 2, The effect of the leachant on the metal removal rate.

Wherein, the metal removal rate is further obtained by the following formula after obtaining the metal content of the PCBs after leaching:

Under the leaching conditions of PCBs size, back rotation speed and concentration, it was found that hydrochloric acid and nitric acid could completely dissolve the metal content in the PCBs (the metal removal rate was 100%), but the time for the complete dissolution of the metal by hydrochloric acid only took 22 hours, while the nitric acid Need 96h. The use of sulfuric acid, acetic acid and citric acid as the leaching agent for the leaching time of more than 22h, followed by 96h, 96h and 364h, can not completely dissolve all the metals in the PCBs, in which copper, for example, the metal removal rate is only They are 8.8%, 9.89% and 19.57%.

According to the influence of the above leaching agent, the effect of using hydrochloric acid as a leaching agent to recover metal is not only 100% metal extraction rate but also economical leaching time, which is because the leaching time is higher than other acids. Chloride, nitrate and sulfate ions in hydrochloric acid, nitric acid and sulfuric acid are all believed to help remove metals from the component, especially chloride ions can form highly stable chlorinated complexes with metals (chloro-complex ), thus accelerating metal dissolution. In contrast, nitrate ions and sulfate ions have different chemical properties from chloride ions, and have a weaker ability to form a complex with metals, so the metal dissolution rate is slower. The use of an organic acid such as acetic acid or citric acid does not easily form a metal complex because of its anion, and it is impossible to accelerate the dissolution of the metal, and also exhibits poor metal solubility and dissolution rate.

In addition, when leaching with nitric acid, the process generates an unavoidable harmful gas, that is, nitrogen oxides. Therefore, after the leaching step, the leachate is further subjected to post-treatment to completely remove residual nitric acid, complicating the process and Increase costs.

When leaching with sulfuric acid, lead-insoluble lead sulfate (PbSO ₄ ) is precipitated with lead during the leaching process, which is not conducive to lead recovery.

Furthermore, the highest corrosion strength of the above acids is nitric acid, followed by sulfuric acid, hydrochloric acid, acetic acid, citric acid, wherein hydrochloric acid is less corrosive than nitric acid and sulfuric acid, industrial application It can reduce the erosion of equipment and also has the ability to dissolve metals from sulfides, oxides and metal compounds. Therefore, hydrochloric acid is a preferred leachant for recovering metals in PCBs.

(effect of hydrochloric acid concentration)

As shown in Fig. 4, comparing the relationship between the metal content of the leachate and the leaching time in step S17, it is known that the concentration of hydrochloric acid is in the range of 1 to 6 M, and the time required for completely dissolving the metal in the PCBs is from 22 h. Decrease, in which the concentration of hydrochloric acid is within 1~3M, the reaction rate increases with the increase of hydrochloric acid concentration, so the leaching time has a significant decreasing trend. When the concentration of hydrochloric acid is greater than 3 M, the degree of change in the leaching time decreases.

(the effect of the speed of return)

Fig. 5 is a view showing the metal removal rate of each metal eluted at different rotational speeds in Examples 1 and 7 to 10. When the conditions of PCBs size, hydrochloric acid concentration, and leaching time were fixed, the recovery rate of metal increased from 0 rpm to 150 rpm, and the metal recovery rate was 100% at 150 rpm.

Among them, copper must be dissolved and leached in an oxidizing environment, but hydrochloric acid is different from nitric acid, and is not an acid having oxidizing ability itself, and cannot directly react with copper to cause copper to be leached. Through the cyclotron oscillation of the cyclotron, especially the return rotation speed of 150 rpm, the oxygen in the air can be sufficiently mixed into the leachate and used as an oxidant, and the copper is further dissolved in combination with hydrochloric acid to form a water-soluble copper compound. Under this condition, the dissolution reaction of copper is as shown in formula (1): 4Cu _(S) +4HCl _(aq) + O _{2 (aq)} → 4CuCl _(aq) + 2H ₂ O ₍₁₎ Formula (1)

Platinum can be dissolved in hydrochloric acid in the presence of oxygen to extract a platinum-forming complex, and the dissolution reaction formula is as shown in the two-step reaction of formula (2) and formula (3): 2HCl _(aq) + O _{2 (g )} →Cl _2(aq) +2H ₂ O ₍₁₎ Formula (2)

Pd _(s) +2HCl _(aq) + Cl _{2 (aq)} → H ₂ PdCl _{4 (aq)} + 2H ₂ O ₍₁₎ Formula (3)

Similarly, gold can be dissolved and leached in the presence of oxidant (oxygen) and chlorine. The dissolution reaction formula can be summarized as shown in formula (4): Au _(S) + 2HCl _(aq) → AuCl _{2 (aq)} +H _2(g) formula (4)

In addition to the above three metals, metals such as zinc, tin, nickel, iron, aluminum, silver, and lead are also dissolved in the presence of hydrochloric acid, and the dissolution reaction sequence is as shown in the following formulas (5) to (11): Zn _(S) +2HCl _(aq) → ZnCl _{2 (aq)} + H _{2 (g)} Formula (5)

Sn _(S) +2HCl _(aq) → SnCl _{2 (aq)} + H _{2 (g)} Formula (6)

Ni _(S) +2HCl _(aq) → NiCl _{2 (aq)} + H _{2 (g)} Formula (7)

Fe _(S) +2HCl _(aq) → FeCl _{2 (aq)} + H _{2 (g)} Formula (8)

2Al _(S) +6HCl _(aq) → 2AlCl _3(aq) +3H _2(g) Formula (9)

2Ag _(S) +2HCl _(aq) → 2AgCl _(aq) + H _{2 (g)} Formula (10)

Pb _(S) +4HCl _(aq) → PbCl _4(aq) +2H _2(g) Formula (11)

(effect of PCBs size)

Fig. 6 is a graph showing the relationship between the PCBs size and the leaching time under the conditions of fixed hydrochloric acid concentration and reciprocating speed in Examples 1 and 11-12. When the PCBs are cut into 2×2cm, the time required for completely leaching the metal is 8h, and the required time when the PCBs are 4×4cm and 6×6cm is 22h and 25h. From this, it can be seen that, by the recycling method of the present invention, even if the size of the PCBS after cutting is enlarged, the recovery rate of the metal is not affected, and at the same time, the balance can be obtained at the leaching time.

In addition, the present invention also tests the effect of temperature on the leaching effect. Under the conditions of fixed PCBs size, hydrochloric acid concentration and oscillating oscillating speed, the leaching temperature was adjusted from 25 ° C to 60 ° C, and no significant change was observed in the leaching effect, so the temperature factor was leached in the present invention. There is no influence, so it is not further detailed and discussed in the present invention.

According to the invention, a method for recovering metal in a printed circuit board by using hydrochloric acid, using hydrochloric acid as a leaching agent, can effectively dissolve the metal completely in the leaching solution without precipitation, and helps to recover metal from the leaching solution. Reuse can also shorten the time required for leaching metal. Even for sheet PCBs, the metal can be completely dissolved for recycling, so it is an economical wet metallurgy method.

S11‧‧‧ cutting steps

S13‧‧‧Pretreatment steps

S15‧‧‧ leaching steps

S17‧‧‧Separation step

S19‧‧‧Purification step

Claims (9)

A method for recovering metal in a printed circuit board by using hydrochloric acid, comprising: a cutting step of cutting a printed circuit board to a predetermined size; and a pre-treating step of removing a chemical coating on the printed circuit board of the predetermined size a leaching step, immersing the chemically coated printed circuit board in a hydrochloric acid, and mixing oxygen to generate chlorine gas, so that the hydrochloric acid dissolves one of the metals in the printed circuit board to form a metal compound containing one of the leaching a separation step of separating the printed circuit board to obtain the leach solution; and a purification step of purifying the leachate to obtain the metal, wherein the metal comprises at least one of copper, lead, silver, platinum, and gold One. The method of claim 1, wherein the pretreating step comprises immersing the printed circuit board in a sodium hydroxide solution to remove a chemical coating on the printed circuit board. The method of claim 1, wherein the concentration of the hydrochloric acid in the leaching step is 0.1 to 12M. The method of claim 1, wherein the concentration of the hydrochloric acid in the leaching step is 1 to 6 M. The method of claim 1, wherein the method of mixing oxygen in the leaching step comprises a convolution. The method of claim 5, wherein the oscillating vibration speed in the leaching step is 50 to 500 rpm. The method of claim 5, wherein the oscillating vibration speed in the leaching step is 50 to 200 rpm. The method of claim 1, wherein the metal further comprises at least one of zinc, tin, nickel, iron, and aluminum. The method of claim 1, wherein the purifying step comprises purifying the metal from the leach solution by solution extraction, activated carbon adsorption, ion exchange, precipitation, cementation, and electrowinning. .