• 한국환경과학회지
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• 제25권2호
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• pp.331-336
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• 2016

In this study the optimum conditions for recovery of valuable metal in Electric Arc Furnace Dusts were investigated. 2M of $H_2SO_4$, 1~5 of solid/liquid ratio, 0~180 min of leaching time has been established for leaching condition, and for electrowinning, each of Pt, C, Zn, Pb anode and Zn, Cu cathode was compared respectively at pH 2, 4 and 6. The result of elemental analysis of Zn crystal, a lagre quantity of Fe and H has been observed with Zn and other heavy metal, therefore, impurities removing process would be requir for enhancing purity of Zn. As the result, about 60% of Zn has been recovered under condition of 2 M of $H_2SO_4$, 1:2 of S/L ratio at 120 min, and Pt or Pb for anode, Zn for cathode has been shown the highest efficiency of electrowinning at pH 6.

• 자원리싸이클링
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• 제21권2호
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• pp.41-46
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• 2012

전해채취법을 이용하여 무전해 니켈 도금폐액으로부터 니켈을 회수하기 위한 실험을 수행하였다. 이를 위해 우선 가성소다를 첨가하는 방법으로 무전해 니켈 도금폐액중의 니켈을 수산화물 형태로 침전분리하였다. 또한, 니켈 수산화물을 황산 용액으로 용해시킨 니켈 수용액을 대상으로 전기분해를 실시하였다. 실험결과, 가성소다를 첨가하여 pH 10 이상으로 조절하면 99% 이상의 Ni을 수산화물로 침전시킬 수 있는 것으로 나타났다. 한편, 니켈 수용액으로부터 전해채취를 통한 Ni의 석출시 전류밀도가 증가할수록 전류효율은 감소하는 것으로 나타났다.

• Nuclear Engineering and Technology
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• 제47권7호
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• pp.849-858
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• 2015

This study set the pyroprocess facility at an engineering scale as a cost object, and presented the cost consumed during the unit processes of the pyroprocess. For the cost calculation, the activity based costing (ABC) method was used instead of the engineering cost estimation method, which calculates the cost based on the conceptual design of the pyroprocess facility. The calculation results demonstrate that the pyroprocess facility's unit process cost is $194/kgHM for pretreatment, $298/kgHM for electrochemical reduction, $226/kgHM for electrorefining, and $299/kgHM for electrowinning. An analysis demonstrated that the share of each unit process cost among the total pyroprocess cost is as follows: 19% for pretreatment, 29% for electrochemical reduction, 22% for electrorefining, and 30% for electrowinning. The total unit cost of the pyroprocess was calculated at $1,017/kgHM. In the end, electrochemical reduction and the electrowinning process took up most of the cost, and the individual costs for these two processes was found to be similar. This is because significant raw material cost is required for the electrochemical reduction process, which uses platinum as an anode electrode. In addition, significant raw material costs are required, such as for $Li_3PO_4$, which is used a lot during the salt purification process.

• 한국재료학회:학술대회논문집
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• 한국재료학회 2001년도 추계 학술발표강연 및 논문개요집
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• pp.105-105
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• 2001

• 한국방사성폐기물학회:학술대회논문집
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• 한국방사성폐기물학회 2003년도 가을 학술논문집
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• pp.426-430
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• 2003

장수명핵종 소멸처리를 위한 건식분리공정에서 핵분열성물질인 우라늄을 장수명핵종과 분리할 필요가 있다. 본 실험은 $LiF-BeF_2$ 용융염에서 전해제련에 의한 우라늄 금속을 분리하기 위하여 분해전압 측정하였고, 인가전압에 따른 전해특성 파악 및 반응속도를 측정하였다. 측정결과 $500^{\circ}C$에서 $UF_4$와 $LiF-BeF_2$의 분해전압은 각각 -1.4volt와 -1.55volt이었다 우라늄의 전착속도는 우라늄 농도가 높을수록 증가하였다.

• 한국방사성폐기물학회:학술대회논문집
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• 한국방사성폐기물학회 2017년도 춘계학술논문요약집
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• pp.92-93
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• 2017

In this paper, CV behavior of electrowinning system was studied depending on the electrode connection mode of potentiostat. In this system, currents can be flown from electrodes to SUS parts because the LCC assembly was electrically connected between the SUS parts and electrolytic salt. Standard mode without ground line of multi tab or CE to ground mode is considered to be more reasonable than standard mode when using multi tab having ground line.

• 한국자원리싸이클링학회:학술대회논문집
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• 한국자원리싸이클링학회 2002년도 춘계임시총회 및 제 20회 학술발표대회
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• pp.111-112
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• 2002

• 한국원자력학회:학술대회논문집
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• 한국원자력학회 2005년도 춘계학술발표회
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• pp.307-308
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• 2005

• 한국재료학회지
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• 제26권12호
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• pp.681-687
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• 2016

Zirconium(Zr) nuclear fuel cladding tubes are made using a three-time pilgering and annealing process. In order to remove the oxidized layer and impurities on the surface of the tube, a pickling process is required. Zr is dissolved in HF and $HNO_3$ mixed acid during the process and pickling waste acid, including dissolved Zr, is totally discarded after being neutralized. In this study, the waste acid was recycled by adding $BaF_2$, which reacted with the Zr ion involved in the waste acid; $Ba_2ZrF_8$ was subsequently precipitated due to its low solubility in water. It is very difficult to extract zirconium from the as-recovered $Ba_2ZrF_8$ because its melting temperature is $1031^{\circ}C$. Hence, we tried to recover Zr using an electrowinning process with a low temperature molten salt compound that was fabricated by adding $ZrF_4$ to $Ba_2ZrF_8$ to decrease the melting point. Change of the Zr redox potential was observed using cyclic voltammetry; the voltage change of the cell was observed by polarization and chronopotentiometry. The structure of the electrodeposited Zr was analyzed and the electrodeposition characteristics were also evaluated.

• 한국재료학회지
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• 제25권12호
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• pp.694-702
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• 2015

Nd-Fe-B permanent magnets have been used in a wide variety of applications because of their high magnetic flux density. So, demand for neodymium has been increasing in worldwide. In this study, an electrowinning process was performed in $LiF-NdF_3-Nd_2O_3$ high temperature molten salts. However, a corrosion resistant material for use in the molten salt must be found for stable operation because of the harsh corrosion environment of the electrowinning process. Therefore, for this paper, boron nitride(BN), aluminum nitride(AlN), and silicon nitride($Si_3N_4$) were selected as protective and structural materials in the high temperature electrolyte. To investigate the characteristics of BN, AlN, and $Si_3N_4$, in molten salts, materials were immersed in the molten salts for 24, 72, 120, and 192 hours. Also, surface condition and stability were investigated by SEM and EDS and corrosion products were calculated by HSC chemistry. As a result, among BN, AlN, and $Si_3N_4$, AlN was found to show the best protective material properties.