• 자원리싸이클링
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• 제12권5호
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• pp.36-41
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• 2003

슬래그는 철분함량이 높아 자원으로의 활용이 가능하나 시장상황에 따라 매립되는 등 재활용이 활발히 이루어지지 않은 실정이다. 따라서 본 연구에서는 슬래그의 재활용이 즘 더 용이하도록 슬래그 내에 존재하는 철분 회수의 중요한 방법인 자력선별 방안에 대하여 고찰하였다. 수재 슬래그, 수냉 전로 슬래그, 공냉 전로 슬래그를 시료로 사용하였고 자장의 세기, 드럼의 회전속도, 슬래그의 투입량에 따른 철분 회수량에 대하여 조사하였다. 철분함량이 적은 수재슬래그는 피더의 진동수 및 드럼의 회전수가 느릴수록 회수율이 증가하였으며 0.5mm 이상의 입도에서 자력선별시 고품위의 철분을 얻을 수 있었다. 수냉의 전로 슬래그의 경우 피더의 진동수가 빠를수록, 드럼의 회전수가 느릴수록 회수율이 증가하는 것으로 조사되었고 입도의 크기가 작아질수록 입도별 회수율이 증가하는 것으로 관찰되었다. 공냉의 전로 슬래그는 피더의 진동수가 낮은 경우 드럼의 회전수가 감소할수록, 높은 경우는 드럼의 회전수가 증가할수록 회수율이 증가하는 것으로 나타났다. 또한 자력선별시 자장의 세기를 증가시키면 회수율은 증가하나 금속철 이외의 철 화합물의 혼입이 많아져 품위가 낮아지는 것으로 관찰되었다.

• 자원환경지질
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• 제8권3호
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• pp.165-168
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• 1975

The grade and recovery rate and its sulphur content of iron concentrate compared respectively as varied with redcued size using the Crocket Magnetic Separator and the Wet-Drum-Magnetic Separator in the magnetic separation test of iron ore from Yangyang mine. The content of sulphur was decreased distinctly as the size was finer. In case of the sample of -100 mesh, using the Crocket Magnetic Separator, the sulphur content of iron ore was decreased to 0.10% and its grade increased to 67.0%, but the recovery rate was no more than 85.1%. In the Wet-Drum type, the grade and the recovery rate of concentrate was better than those in the Crocket Magnetic Separation, but the content of sulphur was more than that in the Crocket Magnetic Separation. The Crocket type is suitable for less sulphur content while the Wet-Drum Magnetic Separator is suitable for better the grade recovery rate of the magnetic concentrate.

• Applied Biological Chemistry
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• 제46권2호
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• pp.130-133
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• 2003

Hemoglobin(Hgb)의 가수분해물로부터 heme-iron을 분리하는데 영향을 미치는 Hgb의 농도, 가수분해도(DH, degree of hydrolysis), 투석용액의 pH, 투석막의 pore size에 대하여 조사하였다. 가수분해에 사용된 Hgb의 농도가 높아짐에 따라 heme-iron의 회수율은 증가하였으나, peptide의 제거율과 HP ratio(총 peptide 중 heme-iron이 차지하는 비율)는 Hgb의 농도에 따른 큰 차이를 볼 수 없었다. Hgb의 가수분해도가 8%, 16%, 24%로 증가함에 따라 투석에 의한 peptide의 제거가 용이하게 이루어져 HP ratio가 13.7%, 20.7%, 31%로 증가하였다. 투석용액에 $KH_2PO_4$를 25 mM이 되도록 첨가할 때는 HP ratio가 25.7%이었으나,50 mM이상의 농도에서는 30.0-32.5%로 증가하였다. 투석용액의 pH 높을수록 heme-iron의 용해도가 증가하여 투석막을 통한 heme-iron의 세출이 많아졌다. Peptide의 제거율은 투석막이 2kDa에서 5kDa로 커질 때 74.5%에서 87.5%의 큰 폭으로 증가하였으며, heme-iron의 회수율은 투석막의 크기에 따라 감소하여 2kDa에서는 86.5%, 15kDa에서는 79.6%, 25kDa에서 63.1%로 급감하였다. 투석법에 의해 분리, 건조된 heme-iron제품의 heme-iron과 peptide의 함량은 각각 21.7%와 77.0%이었으며, HP ratio는 28.2%, 수율은 6,5%이었다.

• 한국분말야금학회:학술대회논문집
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• 한국분말야금학회 2006년도 Extended Abstracts of 2006 POWDER METALLURGY World Congress Part 1
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• pp.597-598
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• 2006

Gas filtration at high temperature from industrial processes offers various advantages such as increasing process efficiency, improving heat recovery and materials resource recovery, etc. At the same time, it is an advanced environment protection technology. This paper describes a newly developed metallic filter element. The manufacturing process of sintered $Fe_3Al$ metallic powder and the mechanical and filtration characteristics of this filter element were investigated. In this work, the phase constituent changes of the $Fe_3Al$ powder during sintering were studied. The newly developed filter elements were found to have excellent corrosion resistance, good thermal resistance, high strength and high filtration efficiency.

• 자원리싸이클링
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• 제28권3호
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• pp.21-25
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• 2019

The utilization of incineration ash from municipal waste must be promoted to solve the social problem on the shortage of final disposal site. In this research, metals should be recovered to avoid the damage of the crushing machine during the utilization of incineration ash in cement industry. In fact, incineration bottom ash from municipal waste contains iron in 3-5%. Nonferrous metal and stainless steel in 1% is also included. The research and development on the physical recovery process was performed not only to remove the metals but also to recover high grade products. Metals were separated from incineration ash in Maruya Co. Ltd.. In fact, iron scrap recovered by magnetic separation can be selled. After that, mixed metal was separated from incineration ash using screen. In this research, mixed metal tried to divided copper, aluminum, brass and stainless steel using drum type magnetic separation, eddy current separation and high magnetic separation. As a result, recovered iron had an 80% for the grade. Aluminum was recovered by eddy current separation without copper and brass.

• 청정기술
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• 제27권3호
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• pp.240-246
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• 2021

COF (Chip on film)용 폐에칭용액 내 구리가 약 3.5% 함유되어 있으며, 철 시편을 사용한 시멘테이션을 통해 구리를 회수하고자 하였다. 철 시편 3종류(플레이트, 칩, 분말)에 따른 시멘테이션 반응에 미치는 영향을 조사하였으며, 구리의 회수율을 높이고자 구리에 대한 철의 몰 비를 변수로 하였다. 반응 전·후 용액 내 시간에 따른 구리 농도의 변화를 확인하였으며, 몰 비를 증가시킬수록 초기 용액 내 구리 함량이 급격히 줄어드는 경향이 나타났다. 상온에서 1시간의 시멘테이션 반응 후 철 시편의 비표면적 값이 큰 플레이트, 칩, 분말 순으로 구리의 회수율이 증가하였다. 회수된 분말은 X선 회절 분석기(X-ray diffraction, XRD), 주사전자현미경(scanning electron microscopy, SEM) 및 에너지 분산형 분광분석법(Energy-dispersive X-ray spectroscopy, EDM) 분석을 통해 결정상과 결정 형태를 확인하였으며, 철 분말의 경우에는 회수된 구리 분말에 미반응된 철 성분이 혼재하였다. 구리에 대한 철의 몰 비 4의 조건으로 철 칩을 사용하였을 때, 구리 회수율 약 98.4%로 최적 조건으로 달성하였다.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 2002년도 추계학술발표회
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• pp.122-124
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• 2002

The removal capacity of zero-valent iron for Cr(Ⅵ) was evaluated using batch kinetic tests. The rate constants for zero-valent iron dramatically increased as initial Cr(Ⅵ) concentration decreased. Generally, the reaction rates of Cr(Ⅵ) with zero-valent iron were faster than that of a biotic degradation of Cr(Ⅵ), and furthermore the reaction rates were inversely proportional to the initial Cr(Ⅵ) concentrations. After certain reaction time elapsed. no further decrease of Cr(Ⅵ) was observed, indicating a loss of iron reactivity. The loss of iron reactivity was primarily due to the passivation of iron surfaces with iron-Cr precipitates, but the reactivity of iron was recovered by adding iron-reducing bacteria. Even though the addition of bacteria itself removed Cr(Ⅵ), the combination of iron-reducing bactera and oxidized iron significantly enhanced the reaction rate for Cr(Ⅵ) removal. The results from column tests also confirmed that the innoculation of iron-reducing bacteria to the column containing completely oxidized iron partially enhanced the recovery of the iron reactivity.

• 자원리싸이클링
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• 제13권2호
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• pp.9-15
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• 2004

석유화학공정으로부터 폐기되는 폐산화철촉매를 이용하여 도금합성폐수중 크롬회수에 관한 연구를 회분식과 연속식으로 실시하였다. 도금합성제수 중 $CrO _{4}^{-2}$ 형태의 음이온으로 존재하는 6가 크롬은 폐산화철촉매의 등전점(pH 3.0)이하에서 폐촉매와 물리적 흡착을 한다. 한편, 6가 크롬은 pH 3.0 이상에서도 폐촉매의 수산화철과 산화환원반응에 의해 일부 환원되어 $Cr(OH)_3$로 침전한다. 컬럼을 이용한 크롬 연속회수실험에서 크롬합성폐수의 pH가 0.5∼2.0일 때 폐촉매의 크롬흡착량은 2.0∼2.3g/L이며, pH가 3.0에서는 1.5g/L이었다. 폐수 중 크롬농도가 50∼500mg/L로 높아질수록 폐촉매에 흡착한 크롬누적량은 1.29∼8.56g/L로 증가하지만, 유속이 30∼80 ml/mm으로 증가하여도 크롬 흡착누적량은 2.21∼2.49 mg/L로 거의 유사하였다.

• 한국초전도ㆍ저온공학회논문지
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• 제19권1호
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• pp.22-25
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• 2017

Steel slag has been considered as an industrial waste. A huge amount of slag is produced as a byproduct and the steel slag usually has been dumped in a landfill site. However the steel slag contains valuable resources such as iron, copper, manganese, and magnesium. Superconducting magnetic separation has been applied on recovery of the valuable resources from the steel slag and this process also has intended to reduce the waste to be dumped. Cryo-cooled Nb-Ti superconducting magnet with 100 mm bore and 600 mm of height was used as the magnetic separator. The separating efficiency was evaluated in the function of magnetic field. A steel slag was ground and analyzed for the composition. Iron containing minerals were successfully concentrated from less iron containing portion. The separation efficiency was highly dependent on the particle size giving higher separating efficiency with finer particle. The magnetic field also effects on the separation ratio. Current study showed that an appropriate grinding of slag and magnetic separation lead to the recovery of metal resources from steel slag waste rather than dumping all of the volume.

• 한국분말재료학회지
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• 제16권5호
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• pp.351-357
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• 2009

A two-step recovery method was developed to produce copper powders from copper chloride waste solution as byproducts of MoO$_3$ leaching process. The first step consisted of replacing noble copper ions with external Fe$^{3+}$ ions which were formed by dissolving iron scraps in the copper chloride waste solution. The replaced copper ions were subsequently precipitated as copper powders. The second step was cementation of entire solution mixture to separate (pure) copper powders from aqueous solution of iron chloride. Cementation process variables of temperature, time, and added amount of iron scraps were optimized by using design of experiment method and individual effects on yield and efficiency of copper powder recovery were investigated. Copper powders thus obtained from cementation process were further characterized using various analytical tools such as XRD, SEM-EDS and laser diffraction and scattering methods.Cementation process necessitated further purification of recovered copper powders and centrifugal separation method was employed, which successfully yielded copper powders of more than 99% purity and average 1$\sim$2$\mu$m in size.