9
 Preparation of shape-controlled copper oxide powders from copper -contai ning solution Younghee Ko Kim * , Doh-Hyung Riu, Soo-Ryong Kim, Byung-Ik Kim  Enviro nmental Resource Laborato ry, Korea Institute of Ceramic Engineeri ng and T echnology , 233-5 Gasan-Dong, Guemcheon- Gu, Seoul 153-801, South Korea Received 11 May 2001; received in revised form 6 August 2001; accepted 4 September 2001 Abstract Shape-controlled copper oxides have been recovered from copper-containing waste etchant by neutralization with alkali hydroxide. Large amounts of copper-containing waste etchant composed of copper chloride, hydrochloric acid and water are generated from the printed circuit board (PCB) industry. In an environmental and economic point of view, the retrieval of the valuable natural resource from waste is important. In the recycling process of copper oxide from the waste etchant, reaction temperature controls the shapes and sizes of the products. Copper oxide recovered below the reaction temperature of 40  C was of the needle shape, while copper oxide comes in a platy shape above 40  C. As a result of the experiments, more than 99% of the copper in the waste etchant was recovered as copper oxide, and its by-products are only sodium chloride and water. Physical  properties of the samples have been characterized using scanning electron microscopy (SEM), X-ray powder diffraction (XRD), thermal gravimetric analysis (TGA) and atomic absorption spectroscopy. The particle size scatters in the range of 0.5–10  Am. Shape-controlled copper oxides are expected to be promising precursors for synthesizing copper powder by reduction. D 2002 Elsevier Science B.V. All rights reserved.  Keywor ds: Copper oxide; Copper-containing waste etchant; PCB industry; Sodium hydroxide; Neutralization 1. Introduction Pri nted cir cuit boards (PCB) are widely used in many elec tronic compute r devi ces [1] . A chemical milling process is commonly utilized in manufactur- ing printed circuit boa rds. In a typical chemical milling process, an etchant solution etches the cop-  per-plated printed circuit board. One of the most common etchants in the electr oni c and comput er indust rie s is the acidic et chant which consis ts of hydrochloric acid (HCl) and copper chloride (CuCl 2 ). The disposal of the etchant without proper treatment has pos ed an envir onment al problem because the acidic etchant contains a significant amount of cop-  per (10 15 wt.%). In addition, the disposal of the acidic etchant wit hout treatment resul ts in a gr eat economic loss. Recently, in an attempt to solve this  problem, there have been several approaches to re- cover copper from the etchant [2–4]. For example, the copper oxychloride being used as an agricultural ingredient is recovered by mixing the acidic etchant with the alkali etchant that is also a waste from the PCB industry. 0167-577X/02/$ - see front matter  D 2002 Elsevier Science B.V. All rights reserved. PII: S0167-577X(01)00568-7 * Corres pondi ng author . Te l.: +82-2-3 282-2472; fax: +82-2- 3282-2430.  E-mail addr ess:  [email protected] (Y.K. Kim). www.elsevier.com/locate/matlet May 2002 Materials Letters 54 (2002) 229–237

Preparation of shape-controlled copper oxide powders from copper-containing solution

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  • Preparation of shape-controlled copper oxide powders from

    copper-containing solution

    Younghee Ko Kim*, Doh-Hyung Riu, Soo-Ryong Kim, Byung-Ik Kim

    Environmental Resource Laboratory, Korea Institute of Ceramic Engineering and Technology, 233-5 Gasan-Dong, Guemcheon-Gu,

    Seoul 153-801, South Korea

    Received 11 May 2001; received in revised form 6 August 2001; accepted 4 September 2001

    Abstract

    Shape-controlled copper oxides have been recovered from copper-containing waste etchant by neutralization with alkali

    hydroxide. Large amounts of copper-containing waste etchant composed of copper chloride, hydrochloric acid and water are

    generated from the printed circuit board (PCB) industry. In an environmental and economic point of view, the retrieval of the

    valuable natural resource from waste is important. In the recycling process of copper oxide from the waste etchant, reaction

    temperature controls the shapes and sizes of the products. Copper oxide recovered below the reaction temperature of 40 jC wasof the needle shape, while copper oxide comes in a platy shape above 40 jC. As a result of the experiments, more than 99% ofthe copper in the waste etchant was recovered as copper oxide, and its by-products are only sodium chloride and water. Physical

    properties of the samples have been characterized using scanning electron microscopy (SEM), X-ray powder diffraction (XRD),

    thermal gravimetric analysis (TGA) and atomic absorption spectroscopy. The particle size scatters in the range of 0.510 Am.Shape-controlled copper oxides are expected to be promising precursors for synthesizing copper powder by reduction. D 2002

    Elsevier Science B.V. All rights reserved.

    Keywords: Copper oxide; Copper-containing waste etchant; PCB industry; Sodium hydroxide; Neutralization

    1. Introduction

    Printed circuit boards (PCB) are widely used in

    many electronic computer devices [1]. A chemical

    milling process is commonly utilized in manufactur-

    ing printed circuit boards. In a typical chemical

    milling process, an etchant solution etches the cop-

    per-plated printed circuit board. One of the most

    common etchants in the electronic and computer

    industries is the acidic etchant which consists of

    hydrochloric acid (HCl) and copper chloride (CuCl2).

    The disposal of the etchant without proper treatment

    has posed an environmental problem because the

    acidic etchant contains a significant amount of cop-

    per (1015 wt.%). In addition, the disposal of the

    acidic etchant without treatment results in a great

    economic loss. Recently, in an attempt to solve this

    problem, there have been several approaches to re-

    cover copper from the etchant [24]. For example,

    the copper oxychloride being used as an agricultural

    ingredient is recovered by mixing the acidic etchant

    with the alkali etchant that is also a waste from the

    PCB industry.

    0167-577X/02/$ - see front matter D 2002 Elsevier Science B.V. All rights reserved.

    PII: S0167 -577X(01 )00568 -7

    * Corresponding author. Tel.: +82-2-3282-2472; fax: +82-2-

    3282-2430.

    E-mail address: [email protected] (Y.K. Kim).

    www.elsevier.com/locate/matlet

    May 2002

    Materials Letters 54 (2002) 229237

  • We attempted to develop a new process of recy-

    cling copper from an acidic etching solution such as

    copper oxide. Copper oxide powder has been widely

    utilized in many different fields such as a sintering

    aid for ferrite compounds in the electronic industry,

    an active constituent of fungicidal composition, a

    catalyst and a pigment, etc. [5]. Various methods

    are reported for the preparation of copper oxide [5].

    Generally, copper oxide is produced by following

    two processes. First, in pyrometallurgical process,

    elemental copper is oxidized to copper oxide at 800

    jC under oxygen atmosphere or air. Another com-mon process for synthesizing copper oxide is the

    neutralization process. Soluble salt of copper like

    copper chloride, nitrate and carbonate is neutralized

    with alkali hydroxide to produce copper oxide. The

    waste etchant from the PCB industry contains quite a

    large amount of copper chloride and is a good source

    of soluble copper salt.

    In this study, we report the preparation of highly

    pure copper oxide from the acidic waste of the PCB

    industry by neutralization with alkali hydroxide. This

    process is a very environmentally benign process

    where it generates only sodium chloride and water

    as by-products. The recycled copper oxide has been

    characterized using SEM, XRD, TGA and atomic

    absorption spectroscopy.

    2. Experiments

    When the PCB is fabricated, waste etchant con-

    taining a large quantity of copper is produced during

    the chemical milling process. The waste etchant can

    be classified into two types: acidic waste etchant

    (copper chloride waste etchant) and basic waste

    etchant (alpine copper waste etchant). The physical

    properties of the etching solution from the PCB

    industry are given in Table 1. As shown in Table

    1, the copper-containing etching solution that was

    discharged in the PCB industry contains copper of

    about 1015 wt.% concentration.

    For this study, the commercial etching solution,

    waste etchant provided from the PCB factory, has

    been used as a starting material for synthesizing

    copper oxide. The process of copper oxide prepara-

    tion from the acidic etching solution is available in

    Fig. 1 as a block diagram. Sodium hydroxide sol-

    ution of 3350 wt.% is slowly added to the acidic

    etching solution by maintaining the reaction tempera-

    ture between 30 and 60 jC and then heated at 5080jC for aging. After several hours, the slurry is fil-tered and washed with water several times and sin-

    tered at 100400 jC for 13 h.It is recommended that 8201100 g of 33 wt.%

    sodium hydroxide solution is added to 1 l of the

    acidic ething solution. If the sodium hydroxide added

    is less than 820 g, the reaction is not complete, so its

    product contains an excess of chlorine impurity.

    Meanwhile, if the sodium hydroxide added is more

    than 1100 g, an excess of sodium hydroxide is

    unnecessarily consumed.

    Table 1

    Physical properties of acidic and alkali etching solution from the

    PCB industry

    Components Acidic etching

    solution

    Alkali etching

    solution

    Chemical CuCl2+HCl+

    H2O

    Cu(NH3)4Cl2+

    NH4OH

    Specific gravity

    (25 jC)1.211.22 1.211.23

    Cu content

    (wt.%)

    1015 1015

    Color Green Blue

    pH 14

    Fig. 1. Block diagram of copper oxide synthesis.

    Y.K. Kim et al. / Materials Letters 54 (2002) 229237230

  • The dried copper oxide is calcined at the prefer-

    able temperature of 100400 jC. If the temperatureis lower than 100 jC, the calcination is not complete-ly achieved. The dried copper oxide may be calcined

    at a temperature of more than 400 jC, however, forthe sake of economical energy consumption, the

    temperature of 400 jC at the maximum is mostdesirable.

    A Rigaku D/max-RINT 2500 diffractometer with

    Cu Ka radiation was used for the XRD analysis of thesamples. Chemical analyses were performed by a

    Jarrell-Ash Poliscan 61E inductively coupled plasma

    (ICP) spectrometer and by a Perkin-Elmer 5000 atomic

    absorption spectrophotometer. HITACHI S-4100 scan-

    ning electron microscope was used for the morphology

    observation of the copper oxide precipitation. Particle

    size distribution was measured using a particle size

    analyzer (Beckman Coulter, Model LS 230). Thermo-

    gravimetric analyses were done using a Cahn TG

    system 121 thermogravimetric analyzer. All samples

    were heated to 700 jC at a rate of 10 jC/min undernitrogen atmosphere.

    3. Results and discussion

    3.1. Neutralization of the acidic etchant with alkali

    hydroxide

    In the neutralization process, either sodium hy-

    droxide or potassium hydroxide can be used as the

    alkali aqueous solution. However, considering the

    easiness of obtaining a material and a unit cost of

    production of the copper oxide, it is preferred to use

    sodium hydroxide.

    By addition of the sodium hydroxide into the

    acidic etchant below 40 jC, precipitation occurs.Copper oxychloride (CuCl23Cu(OH)2) was formedin the range of pH 58, and copper hydroxide

    (Cu(OH)2) above pH 9. Fig. 2 shows the neutraliza-

    tion curve below 40 jC of the acidic etchant while itneutralizes the sodium hydroxide solution. However,

    with the addition of the sodium hydroxide into the

    acidic etching solution above 40 jC, copper oxidewas formed in all pH ranges. Fig. 3 presents the X-ray

    powder diffraction (XRD) patterns of copper oxides

    Fig. 2. Neutralization curve of the acidic etchant.

    Y.K. Kim et al. / Materials Letters 54 (2002) 229237 231

  • recovered from the copper-containing waste etchant.

    The sample was prepared at 30 jC to produce a cop-per hydroxide precursor and aged at 80 jC to getcopper oxide and dried at 100 jC. X-ray powder dif-fraction pattern is well matched with JCPDS No. 48-

    1548 without any impurities. However, the X-ray

    powder diffraction pattern is quite broad. It is as-

    cribed that the sample is not fully crystallized, a sin-

    tering process is required to get a highly crystallized

    sample.

    3.2. Effect of reaction temperature

    Acidic etchants in the electronic and computer in-

    dustries are composed of hydrochloric acid (HCl, 7

    10%), copper chloride (CuCl2, 1925.5%) and water

    (H2O, 64.574%). The addition of NaOH to the

    waste etchant generates large amounts of heat by

    acidbase titration since the waste etchant contains

    a large amount of HCl. It leads to the instant increase

    of reaction temperature of up to 80 jC. Copper oxide

    Fig. 3. X-ray powder diffraction patterns of copper oxides recovered from the copper-containing waste etchant.

    Y.K. Kim et al. / Materials Letters 54 (2002) 229237232

  • was formed at the beginning of the reaction. Prepared

    copper oxide by this process shows a platy shape by

    SEM analysis (Fig. 4a). On the other hand, the

    addition of NaOH to the waste etchant while main-

    taining the reaction temperature under 40 jC leads tothe copper hydroxide slurry having a bright blue

    Fig. 4. Scanning electron microscopy analysis of copper oxides. (a) Reaction temperature: 60 jC. (b) Reaction temperature: 30 jC.

    Fig. 5. Particle size distribution of copper oxides. (a) Aging temperature: 50 jC. (b) Aging temperature: 80 jC.

    Y.K. Kim et al. / Materials Letters 54 (2002) 229237 233

  • color. Aging of the copper hydroxide precursor at

    5080 jC for 13 h produces to black precipitationof copper oxide. By SEM analysis, it can be seen that

    the copper oxide prepared through the copper hydrox-

    ide precursor has a needle shape (Fig. 4b). The

    process of needle shape formation of copper oxide

    during the aging period was observed by scanning

    electron microscopy (SEM). The SEM analysis shows

    that the copper hydroxide precursor was of the junky

    shape below 40 jC of reaction temperature. However,needle-shaped copper oxides were grown from the

    junky shape of the copper hydroxide 1 h after raising

    the aging temperature to 80 jC, and for 3 h more, thesample was completely turned into the needle-shaped

    copper oxide. It is believed that copper oxide of the

    needle shape was formed during the dehydration

    stage of copper hydroxide. The high purity of fine

    powder and the controllability of particle shape and

    size are of importance for its practical use. It is

    noted that the synthesis process plays an important

    role in determining the shape and size of the

    particles.

    3.3. Effect of aging temperature

    Aging of copper hydroxide precursor was per-

    formed at 5080 jC for 13 h to increase the cry-stallinity of the final product of copper oxide. Particle

    Fig. 6. Scanning electron microscopy analysis of copper oxides calcined at different temperatures (a) 100 jC, (b) 300 jC, (c) 400 jC and (d)500 jC. The samples were prepared at 30 jC and aged at 80 jC.

    Y.K. Kim et al. / Materials Letters 54 (2002) 229237234

  • size distribution at different aging temperatures was

    measured using the particle size analyzer. The average

    particle size of copper oxides aged at 50 and 80 jC for

    2 h was about 10 Am (Fig. 5). The aging temperaturesdo not significantly affect the average particle size of

    the copper oxide.

    Fig. 7. Thermal gravimetric analysis data of copper oxides.

    Fig. 8. X-ray powder diffraction patterns of copper oxides prepared at different conditions.

    Y.K. Kim et al. / Materials Letters 54 (2002) 229237 235

  • Table 2

    Chemical analysis data of the recovered copper oxides

    Sample Reaction Aging Calcination Chemical analysis data

    number temperature

    (jC)temperature

    (jC)temperature

    (jC)Cu2+

    (wt.%)

    Cu+

    (wt.%)

    Cl

    (wt.%)

    Na

    (ppm)

    Zn

    (ppm)

    Pb

    (ppm)

    Cd

    (ppm)

    Fe

    (ppm)

    Purity

    as CuO

    M 22 30 80 300 78.3 2.28 Tr Tr 98.0

    400 78.6 2.3 Tr Tr 98.4

    500 78.1 2.16 Tr Tr 28.24 40.94

  • 3.4. Effect of calcination temperature

    SEM analyses of calcinated copper oxide at differ-

    ent temperatures show different morphologies with

    different calcination temperatures (Fig. 6). Sample

    dried at 100 jC appears to have a long needle shapehaving inhomogeneous particle size distribution.

    However, the samples calcined at 400 or 500 jChave spherical shapes and homogeneous size distri-

    butions. It is ascribed that recrystallization occurs at

    the surface of the sample during the calcination

    process.

    3.5. Effect of reaction pH

    The pH value (10.512) was controlled by the

    amount of NaOH added while maintaining the reac-

    tion temperature under 30 jC. Each sample dried at100 jC was analyzed using thermal gravimetricanalysis (TGA) (Fig. 7). Sample prepared at pH

    10.5 shows weight loss at 300 jC. This weight losscan be explained by the sublimation of chloride

    impurity in the sample. However, the sample prepared

    at pH 12 does not show significant weight loss at the

    same temperature. TGA data confirm that the entire

    chloride ions of the starting material are replaced by

    hydroxyl ions only above pH 12. The above results

    were also confirmed by X-ray powder diffraction

    data. X-ray powder diffraction data of the sample

    prepared at pH 12 show only copper oxide peaks.

    However, X-ray powder diffraction data of the sample

    prepared at pH 10.5 show copper oxychloride peaks

    accounted for an impurity besides copper oxide peaks

    (Fig. 8).

    3.6. Chemical analysis and yield

    The chemical analysis data of copper oxide pre-

    pared from waste etchant are shown in Table 2. The

    purity and yield of copper oxide prepared from waste

    etchant of the PCB industry are higher than 99%. It

    contains impurities of Zn, Pb and Fe in ppm level.

    Yield of recovered copper oxide was calculated

    based on the copper concentration of the starting

    material which is the commercial acidic etching

    solution.

    4. Conclusion

    Highly pure copper oxides have been recovered

    from copper-containing waste etchant of the PCB

    industry. In recycling copper oxide from the waste

    etchant by neutralization process using alkali hydrox-

    ide solution, the reaction temperature controls the

    shapes and sizes of the copper oxides. The results

    are summarized in Table 3. The copper oxide recov-

    ered below the reaction temperature of 40 jC was ofthe needle shape, while copper oxide comes in a platy

    shape above 40 jC. As a result of the study, more than99% of the copper in the waste etchant was recovered

    as copper oxide and its by-products are only sodium

    chloride and water. Shape-controlled copper oxides

    are expected to be promising precursors for synthesiz-

    ing copper powder by reduction [6,7].

    References

    [1] G.R. Allardyce, A.J. Davies, D.J. Wayness, A. Singh, US Patent

    5,106,454 (1992).

    [2] M.A. Rabah, Hydrometallurgy 56 (2000) 75.

    [3] B. Greenberg, US Patent 5,188,703 (1993).

    [4] K.S. Doh, N.Y. Kim, D.K. Kim, J. Korea Solid Wastes Eng.

    Soc. 14 (7) (1997) 667.

    [5] H.W. Richardson, Hand Book of Copper Compounds and Ap-

    plications, Marcel Dekker, New York, USA, 1997.

    [6] L. Liu, T.J. Zhang, K. Cui, Y.D. Dong, J. Mater. Res. 14 (10)

    (1999) 4062.

    [7] J. Durisin, M. Orolinova, K. Durisinova, V. Katana, J. Mater.

    Sci. Lett. 13 (1994) 688.

    Table 3

    The result of shape-controlled copper oxide preparation

    Sample

    number

    Reaction

    temperature (jC)Aging

    temperature

    (jC)

    Shape of final

    products

    M 22 30 80 Needle shape

    M 20 40 80 Needle shape

    M 23 50 80 Platy shape

    M 19 60 60 Platy shape

    Y.K. Kim et al. / Materials Letters 54 (2002) 229237 237

    Preparation of shape-controlled copper oxide powders from copper-containing solutionIntroductionExperimentsResults and discussionNeutralization of the acidic etchant with alkali hydroxideEffect of reaction temperatureEffect of aging temperatureEffect of calcination temperatureEffect of reaction pHChemical analysis and yield

    ConclusionReferences