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Recovery of High Purity Tin from Waste Solution of the Tin Plating by Ion-exchange and Cyclone-electrowinning (주석도금폐액으로부터 이온교환 및 사이클론 전해채취를 이용한 고순도 주석의 회수)

  • Kang, Yong-Ho;Shin, Gi-Wung;Ahn, Jae-Woo
    • Resources Recycling
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    • v.25 no.4
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    • pp.42-48
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    • 2016
  • A research for the recovery of the metal with high purity from the waste tin plating solution was carried out. First, tin plating waste solution was tested to remove the organic substances and metallic impurities such as Fe, Zn, Na etc. using ion exchange resin having iminodiacetic functional groups (Lewatit TP 207). Second, the tin solution was purified to obtain the high purity tin solution using ion exchange resin having ethylhexyl-phosphate functional groups (Lewatit VPOC 1026). Finally, 99.98% of the high purity of tin metal can be recovered from the purified solution by cyclone type electrowinning method.

A Study on the Recovery of Aluminum from Aluminum dross (알루미늄 드로스로부터 알루미늄의 회수에 관한 연구)

  • 김홍진;김용현;이병우;이광학
    • Resources Recycling
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    • v.6 no.1
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    • pp.5-10
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    • 1997
  • The aluminum was recovered from the middle size (Q1.0-12.0 mm) aluminum drosses using NaCl and KC1 mixuture as a basic salt flux. The maximum aluminum recovery was about 76.9% when 40% basic salt flux was added to aluminum dross at 850$^{\circ}$C for two hours. Also, aluminum remvery increased with increasing fluoride (1%-5%) addition to basic salt flux. But, there was no considerable effect due ta the increasing of viscosity when the fluorides were added over 5%, respectively. E s p d y , the most aluminum recovery was about 83.5% when 5% cryolite was added to 40% basic salt flux.

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Recovery of Tin from Tin Oxide Resulted from Glass Manufacturing Process by Pyrometallurgy (유리생산공정 폐주석산화물에서 건식제련에 의한 주석회수기술)

  • Lee, Sang-Ro;Kim, Sang-Yeol;Lee, Man-Seung;Park, Man-Bok
    • Resources Recycling
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    • v.24 no.2
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    • pp.23-28
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    • 2015
  • Most of the domestic need for tin rely on imports. In this work, a pyrometallurgical process was investigated to recover pure tin from the tin oxides in tin bath which results from the production of flat glass and LCD panel. From the results on the effect of reaction temperature, the highest recovery percentage of tin was obtained at $1350^{\circ}C$. The recovery percentage of tin was improved to 88% by employing the first and second smelting step. Electrorefining of the crude tin thus obtained led to pure tin with purity higher than 99.9%.

A Study of the Metal Recovery from the Aluminium Scrap (Al 스크랩으로부터 금속회수에 관한 연구)

  • 김준수;임병모;윤의박
    • Resources Recycling
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    • v.4 no.1
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    • pp.25-30
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    • 1995
  • In the preparatIon of reclaimed aluminium lllgot from alumimum scrap, the aluminium recovery was studied a as a function of the preliminary treatment of samples, addition of flux and melting atmosphere. AI dross is produced by an oxidation reaction at the surface of liquid metal. The recovery of AI metal increases u up to maximum 95% by adding salt up to 7%, The recovery of AI metal in the compacted chip bale without oil removal mcrease about 14% compared io non-compacted chip. In the case of the AI seed melting process, the recovery of Al metal of the crushed and compacted chip hale is 97%, In meltmg of alumimum scrap under the atmosphere of carbon and nitrogen gas, the recovery of AI metal increase, but it is decreased when the mixture of salt and carbon powder is added excessively.

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Recovery of Precious Metals from Waste PCB and Auto Catalyst Using Arc Furnace (귀금속 함유 폐기물로부터 아크로를 이용한 유가금속 회수)

  • Ban Bong-Chan;Kim Chang-Min;Kim Young-Im;Kim Dong-Sn
    • Resources Recycling
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    • v.11 no.6
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    • pp.3-11
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    • 2002
  • Recently, waste printed circuit board (PCB) has significantly increased in its amount due to the rapid development of electronic industries. Since several kinds of noxious materials and also valuable metals are contained in it, the waste PCB is in an urgent need of recycling for the dual purposes for the prevention of environmental pollution and recovery of valuable resources. Also, the catalyst which equipped in the exhaust pipes of automobiles to reduce emission of air pollutants contains precious met-als so that their recovery from the waste auto-catalysts is required. In this study, the recovery of valuable metals from waste PCB and auto-catalyst by arc furnace melting process has been investigated, which is known to be very stable and suitable f3r less production of pollutants due to its high operating temperature. The effect of the kind of flux on the recovery of precious metals was examined by using quicklime, converter slag, and copper slag as the flux. In addition, the influence of direct and alternating current and the applying direction of direct current has been investigated. It was observed that using converter or copper slag as a flux was more desirable for a higher efficiency in the precious metal recovery compared with quicklime. For the effect of current, application of direct current taking the bottom as a negative pole generally showed a better efficiency for the extraction of valuable metals from waste PCB, which was also observed for the case of waste auto-catalyst. The average recovery of precious metals from both wastes by arc furnace melting process was very high, which was up to in the range of 95~97%.

The Optimization of Hydrometallurgical Process for Recovery of Zinc from Electric Arc Furnace Dust (Part I : leaching process) (습식산화법을 이용한 제강분진 내 아연회수를 위한 최적조건 도출에 관한 연구(Part I; 침출공정))

  • Moon, Dea-Hyun;Ahn, Sang-Woo;Kim, Han-lae;Kim, Ji-Tae;Chang, Soon-Woong
    • Resources Recycling
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    • v.24 no.3
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    • pp.27-33
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    • 2015
  • EAFD (Electric Arc Furnace Dust) is considered as pernicious pollutant, assigned hazardous waste. Since this dust is a by-product of industry, it contains valuable metals such as Fe, Zn, Ni, Cu which can be turned into resources by recycling process. In this study, hydrometallurgical process was applied to recover Zn from Electric Arc Furnace Dusts. The result showed 95% Zn recovery at 3M $H_2SO_4$, Solids/Liquid ratio 1:2 and aeration of 1.8L/min for 2hr. However there was 80% Zn recovery at lower $H_2SO_4$ concentration apply for pilot scale plant.

A Study on the Recovery of Mn Component from the Spent Manganese Batteries with Ammonium Sulfate (廢 망간電池로부터 黃酸 암모늄에 의한 Mn 성분의 분리 회수에 관한 연구)

  • 박용성;우제원;황영애
    • Resources Recycling
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    • v.9 no.6
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    • pp.3-8
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    • 2000
  • A reaction between the depolarizing mixture in the spent manganese batteries and ($NH_4$)$_2$$SO_4$was carried out to find a new process for the extraction of Mn component from the spent manganese batteries. The optimum conditions were as follows : the reaction temperature $425^{\circ}C$, ($NH_4$)$_2$$SO_4$weight ratio to the depolarizing mixture in the spent manganese batteries 12.0, reaction time 60 min. Under above conditions manganese was extracted 93.5%.

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Recent Trends and Future Perspectives of the Magnesium Recovery based on Electrolysis (전해 기반 마그네슘 회수 기술의 관련 동향 및 향후 전망)

  • Sang-hun Lee
    • Resources Recycling
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    • v.33 no.2
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    • pp.16-23
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    • 2024
  • The electrolysis for extracting magnesium from seawater or brine primarily involves recovery of magnesium via precipitation as the form of magnesium hydroxide. The technology is classified into cation-exchange membranes (CEM), anion-exchange (AEM) membranes, electrodialysis, and membraneless methods. Recent research has focused on enhancing the efficiency and selectivity of magnesium recovery from seawater or brine containing magnesium, with expectations of effective magnesium recovery even with normal seawater. In a future, the optimization of the selective and efficient recovery of magnesium and various valuable substances through long-term operation of scaled-up systems is crucial with enhancing economic and environmental viability. It is essential to realistically estimate operational costs considering the membrane's lifespan and replacement cycle. Also, detailed and practical process models should be developed based on monitoring data on various factors.

A Case Report on the Sea-Trial of the Seabed Drill System and Its Technical Trend (해저 착저식 시추기 시험시추 보고 및 기술 동향)

  • Pak, Sang Joon;Kim, Hyun-Sub
    • Economic and Environmental Geology
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    • v.49 no.6
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    • pp.479-490
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    • 2016
  • Seabed drilling system has recently been used to drill seafloor mineral resources. This case report highlights the procedure and result of sea-trial of seabed drilling system at off-shore of Japan on March, 2016 as well as briefs an international-technical trend of seabed drilling system. In case of having less than 100 m drill depth, seabed drilling system is favorable for seafloor mineral deposits which are mostly distributed within a narrow district and situated between 1000~3000 m water depth, compared with vessel-mounted drilling system. The system is featured by the remotely-operated drill gear, which has top drives, drill strings and mud system on it. The core samples are generally recovered to ship with seabed driller after a dive. In this sea-trail, recovery rate of core samples averagely shows about 55% and the recovered rocks mostly correspond to fresh and/or weak-altered basalt. In case of drilling hydrothermal ore deposit, the recovery rate would be lower than 55% because of the fragile nature of ores. Alternatively it is used to collect cutting chips through riser or bins in order to increase the recovery rates. Recently a reverse circulation method is taken considered to acquire the better cutting-chips. Three-leg type outrigger system and four-leg type leveling system are the competing landing-instruments of seabed drill system. However the landing efficiency using these gears has to be further monitored due to lack of case reports.