• Title/Summary/Keyword: copper leaching

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Study on Recovery of Precious Metal (Ag, Au) from Anode Slime Produced by Electro-refining Process of Anode Copper (양극동의 전해정련시 발생된 양극슬라임으로부터 귀금속(Ag, Au) 회수에 대한 연구)

  • Kim, Young-Am;Park, Bo-Gun;Park, Jae-Hun;Hwang, Su-Hyun
    • Resources Recycling
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    • v.27 no.6
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    • pp.23-29
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    • 2018
  • Recently rapid economic growth and technological development have led to an increase in the generation of waste electrical and electronic equipment (WEEE). As the amount of electric and electronic waste generated increases, the importance of processing waste printed circuit boards (PCB) is also increasing. Various studies have been conducted to recycle various valuable metals contained in a waste PCB in an environmentally friendly and economical manner. To get anode slime containing Ag and Au, Anode copper prepared from PCB scraps was used by means of electro-refining. Ag and Au recovery was conducted by leaching, direct reduction, and ion exchange method. In the case of silver, the anode slime was leached at 3 M $HNO_3$, 100 g/L, $70^{\circ}C$, and Ag was recovered by precipitation, alkali dissolution, and reduction method. In the case of gold, the nitrate leaching residues of the anode slime was leached at 25% aqua regia, 200 g/L, $70^{\circ}C$, and Au was recovered by pH adjustment, ion exchange resin adsorption, desorption and reduction method. The purity of the obtained Au and Ag were confirmed to be 99.99%.

Decay of Populus cathay Treated with Paraffin Wax Emulsion and Copper Azole Compound

  • Liu, Jie;Liu, Min;Hou, Bingyi;Ma, Erni
    • Journal of the Korean Wood Science and Technology
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    • v.47 no.1
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    • pp.21-32
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    • 2019
  • In order to investigate the decay process of wood treated with preservative, waterproofing agent and their compound systems, a full-cell process was applied to impregnate the sapwood of poplar (Populus cathay) at paraffin wax emulsion concentrations of 0.5% and 2.0%, Copper Azole (CA) concentrations of 0.3% and 0.5%, and their four compound systems, respectively. Leaching tests and laboratory decay resistance against the white-rot fungus Corious versicolor (L.) Murrill for treated wood were carried out according to the America Standard E11-06 and China Standard GB/T 13942.1-2009. At certain time intervals during the decay test, samples were characterized by Fourier transform infrared spectroscopy (FTIR) and X-ray diffraction technique (XRD) to investigate the time-dependent changes of chemical components and crystalline structure, thus clarifying the decay mechanisms. The results suggested that white-rot fungi degrade hemicellulose and lignin in the wood cell wall first, followed by a simultaneous degradation of polysaccharides and lignin. Besides, CA could not only slower the decomposition of both hemicellulose and lignin, but also reduce the degradation amount of hemicellulose. However, paraffin wax emulsion at high concentration had a negative effect on the impregnation of CA for the compound system treated wood.

Recovery of Copper from Synthetic Leaching Solution of Manganese Nodule Matte by Solvent Extraction-electrowinning Process (망간단괴 매트상 모의 침출용액으로부터 용매추출-전해채취 공정에 의한 구리의 회수)

  • Kim, Hyun-Ho;Park, Kyung-Ho;Nam, Chul-Woo;Yoon, Ho-Sung;Kim, Min-Seuk;Kim, Chul-Joo;Park, Sang-Woon
    • Resources Recycling
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    • v.25 no.1
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    • pp.60-67
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    • 2016
  • A scale-up test with a continuous solvent extraction and electro-winning system was carried out to separate and recover copper from a synthetic sulfuric acid solution (Cu 10.5 g/L, Co 2.0 g/L, Ni 15.0 g/L, Fe 0.2 g/L). The solution was introduced into mixer-settlers with four stages of extraction and two stages of stripping for continuous countercurrent solvent extraction to separate copper from nickel and cobalt. The loading was carried out using 40% LIX 84-I(v/v) as extractant with a phase ratio of A : O = 1 : 1. Meanwhile, the stripping was undertaken at a phase ratio of A : O = 1 : 1.5 using depleted electrolyte containing 35.0 g/L Cu and 180 g/L $H_2SO_4$ as stripping solution. The extraction and stripping efficiencies were found to be 96.7% and 91.0%, respectively. The copper composition of the stripped solution (pregnant electrolyte) was 50.0 g/L Cu with impurities of 25 ppm nickel, 5 ppm cobalt and 3 ppm iron. In the electro-winning process, copper metal of 99.833 purity was yielded with current efficiency of 98.9% and current density of $1.50A/dm^2$.

Microstructural Analysis of the Solidified Arsenic-containing Heavy Metal Sludge (비소를 함유한 중금속슬러지 고화체의 미세구조적 분석)

  • Kim, Yeong-Kwan;Jeong, Myoung-Sun
    • Journal of Industrial Technology
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    • v.16
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    • pp.169-174
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    • 1996
  • Microstructural analyses of synthetic arsenic-containing heavy metal sludges solidified with Portland cement were performed. Heavy metal sludges containing 0.04M of cadmium, chromium, copper, lead, and arsenic were prepared by sodium hydroxide precipitation and successive vacuum filtration. The sludges mixed with cement were cured for 14 days. The solidified sample was characterized by 1) leaching test, 2) scanning electron microscopy and 3) X-ray diffractometry. Of the metals tested, only Pb concentration in the leachate exceeded the Korean regulatory limit. The level of lead in the leachate was as high as 10 times the regulatory limit. X-ray analysis suggested that the metal hydroxides might be present in complex or impure crystalline phases.

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EAF Dust Treatment at Miike Smelting CO., LTD.

  • Noda, Shinji;Tatehana, Yoshikazu
    • Proceedings of the IEEK Conference
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    • 2001.10a
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    • pp.375-380
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    • 2001
  • MF is a half shaft blast furnace which has been developed at Mitsui Miike Smelter in the 1960’s to treat vertical retort residue. The MF has also been tested for treatment of various recycling materials and wastes. Now various secondaries and wastes (EAF dust, zinc leaching residue, Cu sludge, etc ) are mainly treated. Powder materials are briquetted with reductant before being fed to the furnace. Products are crude zinc oxide, matte, non-hazardous slag and steam. Zinc and lead are recovered in oxide dust, and copper and silver are recovered in matte. The MF can be widely applied to many kinds of materials which contain such non-ferrous metal-valuables. In addition, the improvement in operation and technology has effectively made the unit capacity much larger. The MF now has many advantages for these treatment processes.

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A Study on Removal of Heavy Metal from Contaminated Sediment via Bioleaching (연안어장 준설 퇴적물내 함유된 중금속 처리에 관한 연구)

  • Ko Seong-Jung;Yun Jong-Hwui;Song Young-Chae;Kim Dong-Geun;Chung Ho-Soon
    • Proceedings of KOSOMES biannual meeting
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    • 2005.05a
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    • pp.119-122
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    • 2005
  • As it is known that the korean coastal fishing areas are getting contaminated by heavy metals from the sediment, the authors conducted the experiments to treat the heavy metals with bioleaching process. As a result, it is found that (1) acidification for the leaching of heavy metals is effectively processed when adding more than $0.3\%$ of sulfur and $0.1\%$ of ferrous sulfate. and (2) copper is rapidly solubilized irrespective of addition of sulfur, while solubilization is not processed even of FeS is added., and (3) bioleaching with sulfur and FeSO4 is possible method to effectively treat the heavy metals form the contaminated sediments.

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Leaching of copper using electro-generated chlorine in hydrochloric acid solution (전해생성된 염소에 의한 구리 침출 연구)

  • Kim, Eun-Young;Kim, Min-Seuk;Lee, Jae-Chun;Jung, Jin-Ki
    • Proceedings of the Korean Institute of Resources Recycling Conference
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    • 2006.05a
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    • pp.86-89
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    • 2006
  • 전해 생성된 염소를 이용하여 구리를 침출하는 연구를 수행하였다. 염산농도 $1molL^{-1}$, 반응온도 $25^{\circ}C$, 교반속도 400rpm 조건에서 전류밀도 $10mA/cm^{2}$의 경우 반응온도에 상관없이 구리의 침출속도가 동일하였으나 $Cl_{2}$ 생성량이 충분한 $40mA/cm^{2}$의 경우 온도가 높을수록 구리의 침출속도가 증가하였다. 침출된 구리농도가 6g/L 부근에 도달하면 염소의 공급속도에 상관없이 구리의 침출이 둔화되었다. 이는 구리-염소 착화물의 형성과 관련된 것으로 생각된다.

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Depth Profiles of Heavy Metals in the Surface Sediments of $H^{o}edong$ Reservoir

  • Moon Byung-Chul;Park Kwang-Jae;Jung Eui-Han;Jeong Gi Ho
    • Environmental Sciences Bulletin of The Korean Environmental Sciences Society
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    • v.1 no.1
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    • pp.1-9
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    • 1997
  • We investigated the depth profiles of heavy metals in the surface sediments at Heedong reservoir in Pusan. Sampling was done at the intervals of 50 m of drift along the water channel into the reservoir. All samples were analyzed with an ICP-AES. We determined the content of Zn, Pb, Cd, Mn, Cu, Cr, and Fe. The overall mean content of these heavy metals were observed to $(2.9\pm1.2){\times}10^{-3},\;(1.3\pm0.7){\times}10^{-3},$ $(1.9\pm2.1){\times}10^{-4},$ $(2.3\pm1.1){\times}10^{-2},\;(1.6\pm1.0){\times}10^{-3},\;and\;(4.5\pm2.6){\times}10^{-4}$ ppm/ppmFe, respectively excluding iron data. Mean contents of Cu show an increasing trend toward the surface of sediments, while those of Cd show a decreasing trend, and those of Pb and Cr are relatively stable. Comparing with the contents of heavy metals in soils at two sites of Kumjeong mountain, enrichment factors of heavy metals in the surface sediments were determined. Among heavy metals we investigated, copper showed the largest value of enrichment factor. Considering the maximum content of heavy metals in the surface sediment, the values of enrichment factors of Cu, Cd and Cr were significant, which were 22, 8.1 and 4.0, respectively. In leaching experiment, it appeared that Pb, Cd, Cr, and Fe in sediments were hardly leached out into water, We also examined the effect of pH on the content of heavy metals.

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Depth Profiles of Heavy Metals in the Surface Sediments of Haedong Reservoir

  • Byung-Chul Moon;Kwa
    • Journal of Environmental Science International
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    • v.1 no.1
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    • pp.1.2-9
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    • 1992
  • We investigated the depth profiles of heavy metals in the surface sediments at Haedong reservoir in Pusan. Sampling was done at the intervals of 50 m of drift along the water channel into the reservoir. All samples were analyzed with an ICP-AES. We determined the content of Zn, Pb, Cd, Mn, Cu, Cr, and Fe. The overall mean content of these heavy metals were observed to $(2.9{\pm}1.2){\times}10^{-3}$, $(1.3{\pm}0.7){\times}10^{-3}$, $(1.9{\pm}2.1){\times}10^{-4}$ $(2.3{\pm}1.1){\times}10^{-2}$ $(1.6{\pm}1.0){\times}10{-3}$, and $(4.5{\pm}2.6){\times}10^{-4}$ ppm/ppm Fe, recpectively excluding iron data. Mean contents of Cu show an increasing trend toward the surface of sediments, while those of U show a decreasing trend, and those of Pb and Cr are relatively stable. Comparing with the contents of heavy metals in soils at two sites of Kumjeong mountain, enrichment factors of heavy metals in the surface sediments were determined. Among heavy metals we investigated, copper showed the largest value of enrichment factor. Considering the maximum content of heavy metals in the surface sediment, the values of enrichment factors of Cu, Cd and Cr were significant which were n, 8.1 and 4.0, respectively. In leaching experiment, it appeared that Pb, Cd, Cr, and Fe in sediments were hardly leached out into water. We also examined the effect of pH on the content of heavy metals.

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A Modified Process for the Separation of Fe(III) and Cu(II) from the Sulfuric Acid Leaching Solution of Metallic Alloys of Reduction Smelted Spent Lithium-ion Batteries (폐리튬이온전지의 용융환원된 금속합금상의 황산침출액에서 철(III)과 구리(II)의 분리를 위한 공정 개선)

  • Nguyen, Thi Thu Huong;Tran, Thanh Tuan;Lee, Man Seung
    • Resources Recycling
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    • v.31 no.1
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    • pp.12-20
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    • 2022
  • The smelting reduction of spent lithium-ion batteries results in metallic alloys containing Co, Cu, Fe, Mn, Ni, and Si. A process to separate metal ions from the sulfuric acid leaching solution of these metallic alloys has been reported. In this process, ionic liquids are employed to separate Fe(III) and Cu(II). In this study, D2EHPA and Cyanex 301 were employed to replace these ionic liquids. Fe(III) and Cu(II) from the sulfate solution were sequentially extracted using 0.5 M D2EHPA with three stages of cross-current and 0.3 M Cyanex 301. The stripping of Fe(III) and Cu(II) from the loaded phases was performed using 50% (v/v) and 60% (v/v) aqua regia solutions, respectively. The mass balance results from this process indicated that the recovery and purity percentages of the metals were greater than 99%.