• Resources Recycling
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• v.14 no.5 s.67
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• pp.24-31
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• 2005

In order to recover valuable metals from fine-grained electronic waste, bioleaching of Cu, Zn, Al, Co, Ni, Fe, Sn and Pb were carried out using Aspergillus niger as a leaching microorganism in a shaking flask. Aspergillus niger was able to grow in the presence of electronic scrap. The formation of organic acids(citric and oxalic acid) from Aspergillus niger caused the mobilization of metals from waste electronic scrap. In a preliminary study, in order to obtain the data on the leaching of Cu, Zn, Al, Fe, Co and Ni from electronic scrap, chemical leaching using organic acid(Citric acid and Oxalic acid) was accomplished. At the electronic scrap concentration of 50 g/L, Aspergillus niger were able to leach more than 95% of the available Cu, Co. But Al, Zn, Pb and Sn were leached about 15-35%. Ni and Fe were detected in the leachate less than 10%.

• Resources Recycling
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• v.28 no.4
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• pp.51-58
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• 2019

Dismantlement of lithium primary batteries without explosion is required to recycle the lithium primary batteries which could be exploded by heating too much or crushing. In the present study, the optimum discharging condition was investigated to dismantle the batteries without explosion. When the batteries were discharged with $0.5kmol{\cdot}m^{-3}$ sulfuric acid, the reactivity of the batteries decreased after 4 days at $35^{\circ}C$ and after 1 day at $50^{\circ}C$, respectively. This result shows that higher temperature removed the high reactivity of the batteries. Because loss of metals recycled increases when the batteries are discharged only with the sulfuric acid, discharging process using acid solution and water was newly proposed. When the batteries were discharged with water during 24 hours after discharging with $0.5kmol{\cdot}m^{-3}$ sulfuric acid during 6 hours, the batteries discharged were dismantled without explosion. Because decrease in loss of metals was accomplished by new process, the recycling process of the batteries could become economic by the 2-step discharging process.

• Resources Recycling
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• v.28 no.5
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• pp.19-29
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• 2019

Recently, it is increasing a amount of installized solar-cell rapidly, and waste Solar cell module are generated in according to the reduction of efficiency largely. Therefore, it is concerned at the environmental problems and recycling of valuable materials, greatly. The treatment processes of end-of-life photovoltaic modules are composed the disassembly of Aluminum frames, separation of Tempered glass, removal of Ethylene Vinyl Acetate and recovery of valuable Metals. For the efficient recycling, we are considered to the treatment technology seriously. And we are proposed on the general opinions according to the developing technology, EPR (Extended Producer Responsibility) problems and promotion plans for the activation of recycling industry.

• Economic and Environmental Geology
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• v.37 no.1
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• pp.113-119
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• 2004

Mineral wastes are generated by the minerals, mining, and metal industries. These are generally inorganic waste streams of mainly waste rock or residues from refining during extraction of metals or minerals from the ore. There are many plants where minerals are recovered in secondany circuits, treating tailings, where the feed grades are much lower than would be economic on a mined ore. The world is now becoming aware of the finite nature of its resources at a price, and of the ever-increasing development costs of large new mines. Reprocessing of old tailings on a large scale must be worth examining very seriously by those with access to sufficient material of this type. In the present paper, mineral separation techniques to recover valuable metals and resources from the old tailings are reviewed, and new trends for future developments are also discussed.

• Proceedings of the KAIS Fall Conference
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• 2012.05a
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• pp.423-425
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• 2012

레드머드(Red mud)란 Bauxite 광물을 Bayer process 공정을 거쳐 알루미나를 정제하는 과정에서 발생하는 슬러리 형태의 산업폐기물이다. 레드머드는 pH 10-12.5 범위의 높은 알칼리성을 나타내며, 14-21 가지의 광물상을 함유하고 있다. 하지만 유가성 물질이 함유되어 있음에도 불구하고 적절한 처리 방법이 없어 폐기물로써 처리되어지고 있다. 레드머드의 처리 및 보관 부분에서 강우로 인한 지하수 오염, 처리 토지 면적 등과 같은 문제점이 다소 발생하여 효율적인 처리가 시급한 실정이다. 이로 인해 환경, 토목, 건설 등 다양한 분야에서 레드머드를 재활용하기 위해 활발히 연구가 진행되어 지고 있지만 재활용양이 발생량에 비해 극히 적다. 따라서 본 연구에서는 최종 처리되는 레드머드의 부피를 줄여 최종 처리 비용을 감소시키고자 레드머드에 함유되어 있는 유가성 금속 성분 중 $TiO_2$ 성분의 회수 방법 중 초음파를 방사하여 회수하는 방법을 알아보았다.

• Proceedings of the Korean Institute of Resources Recycling Conference
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• 2002.05a
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• pp.66-73
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• 2002

전기로제강분진을 적절한 공정을 통하여 처리하여 유가금속을 회수하고 처리잔사를 철원으로 재활용한다면 환경오염방지 및 폐자원의 재자원화 효과가 기대된다. 본 연구에서는 고온환원과 전해공정을 조합한 새로운 전기로제강분진 처리공정을 제안하고, 각 공정에 대한 기초실험을 수행하여 그 가능성을 조사, 검토 하였다. 전기로제강분진의 고온환원실험과 환원과정에서 분위기와 증기압의 차이를 이용한 Zn및 Pb 성분의 분리, 휘발실험의 결과들이 분석되었으며, 아울러 환원처리잔사 중의 Fe성분함량을 증가시켜 철원으로 재활용할 수 있는 가능성을 확인하기 위하여 전기로제강분진과 millscale을 혼합, 환원하는 실험을 수행하였다. 또한 환원과정의 휘발산물인 조산화아연의 침출 및 전해에 관한 기초실험을 수행하여 고순도금속아연회수의 가능성도 조사, 검토하였다.

• Resources Recycling
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• v.10 no.2
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• pp.20-26
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• 2001

Sulfuric acid leaching of Mn, Co and Fe from spent petrochemical catalyst was performed using hydrogen peroxide as a reducing agent. Low extraction of Mn, Co and Fe was obtained by only sulfuric acid. When hydrogen peroxide were added as a reducing agent, the high extraction of these metals could be obtained. Different from ordinary leaching, the extraction per-centages of metal components decreased with elevating leaching temperature in this process. Under the optimum condition, the extraction percentages of Mn, Co and Fe were 93.0% , 87.0% and 100% respectively.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.14 no.11
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• pp.6015-6022
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• 2013

It has been known that there are large amount of nitric acid and valuable metals, copper in the plating waste solution of automobile wheel. As nitric acid and valuable metals are high price and toxic, they should be recovered for economics and environment. Plating waste was extracted with TBP diluted with kerosene. The concentration of nitric acid in aqueous phase was analyzed by titration method by NaOH solution (0.1~1.0N) and the amount of metals by ICP-MS and ICP-AES. The concentration of copper in plating waste were 76,850 mg/L. The concentration of nitric acid in plating waste was 1.02 M. After three step extraction was performed with 50% TBP, each organic phase was stripped three times with distilled water to obtain 48.1% of nitric acid. Purity of final nitric acid was over 99.9% by ICP analysis. After recovery of nitric acid, copper was extracted with various solvent extractors like PC 88A, D2EPHA, LIX 84 and ISE 106. Among these extractors, 92% of copper was recovered by ISE 106 after 1st extraction and 30% $H_2SO_4$ stripping. Copper ion was reduced with $N_2H_4$ to make metal powders, respectively.

• Journal of Powder Materials
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• v.20 no.1
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• pp.60-67
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• 2013

• Proceedings of the Korean Institute of Resources Recycling Conference
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• 2004.05a
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• pp.40-44
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• 2004