• Journal of the Korea Organic Resources Recycling Association
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• v.11 no.4
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• pp.120-129
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• 2003

The anodic alumina is synthesized using 0.3M oxalic acid and the barrier layers of the anodic alumina are removed using the 20wt% $H_2SO_4$ solution. The structure of the anodic alumina is analyzed by XRD and SEM. It is observed by SEM that the size of anodic alumina pore is about 60nm. And the uniformity of the anodic alumina surface under the 20wt% $H_2SO_4$ solution is poorer than the unifomity of the the normal anodic alumina surface. The anodic alumina and the carbon are used cathode and anode in$Cd(NO_3)_2{\cdot}4H_2O$, $Co(NO_3)_2{\cdot}6H_2O$ and $PbSO_4$ solutions. In this study, the constant D.C. electrical current is flowed in each solution for 24hours. It is found that the voltages so far as 4.6, 3.4 and 5.1V at $Cd(NO_3)_2{\cdot}4H_2O$, $Co(NO_3)_2{\cdot}6H_2O$ and $PbSO_4$ solutions increase with increasing the flowing current time and after the voltage does not change which values are 4.2, 2.7 and 2.4V, respectively. The amount of metal ions in solutions decrease with increasing the flowing current time until the flowing current time is 18hours and the metals are formed at the surface of anodic alumina. After the metal ions are removed using the anodic alumina, and $Cd^{2+}$, $Co^{2+}$ and $Pb^{2+}$ ions are removed again using flow cell with retriculate vitreous carbon(RVC) working electrode. The concentration of $Cd^{2+}$, and $Co^{2+}$ions decrease until the flowing time of the solutions is 20minutes and the concentration of $Pb^{2+}$ ion decreases until that time is 30minutes. In this case, the removal effects of $Cd^{2+}$, $Co^{2+}$ and $Pb^{2+}$ ions are 34.78, 28.79 and 86.38%, respectively. And it is possible that both $Cd^{2+}$ and $Co^{2+}$ions are adsorbed in pore of RVC at the same time and the removal effects of $Cd^{2+}$ and $Co^{2+}$ions are 32.30 and 31.37%.

• Journal of the Korean Chemical Society
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• v.19 no.2
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• pp.142-146
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• 1975

The formation of iron oxide hydroxide in a ferrous sulfate was studied in different contents of iron in the solution at a temperature range of 90 to $100^{\circ}C$ under 1${\sim}$3 atmospheres. The Mohr's salt thus formed was hydrolyzed under 1 to 3 atmospheres, in 14 to 72 g/l of iron content in the solution pH 3 or 6 for two hours at 90 to $100^{\circ}C$. The results obtained was as follows; 1) In Mohr's salt solution, as the iron content was increased, with decreasing the concentration of hydrogen ion, the yield of iron oxide hydroxide was gradually increased. 2) When iron content in Mohr's salt solution was 42.81 g/l, 91.5% of iron was recovered in the form of $\alpha$-goethite similar to yellow grade of natural goethite. 3) When $\alpha$-goethite obtained was calcined of $500^{\circ}C$, it was turned into ${\alpha}$-ferric oxide with a redish brown colour.

• Journal of the Mineralogical Society of Korea
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• v.23 no.4
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• pp.331-346
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• 2010

This study was carried out to leach valuable metals from galena using indigenous bacteria with no optimum pH conditions at room temperature. Even in these conditions, the rod-shaped indigenous bacteria, ranging from $0.4{\times}0.2{\mu}m$ to $0.5{\times}1.7{\mu}m$, were attached to the surface of the galena. For the 19 days of the bioleaching experiment, the content of Ph, Fe, Zn ions was found to be 347, 222 and 1.7 times higher than that of the control leaching agent, respectively. Numerous hexagonal column crystals were observed on the surface of galena. Those crystals may be formed from the biooxidation of galena by the indigenous bacteria. XRD analysis showed the peaks of anglesite observed in the bioleached galena. It is expected that more valuable elements can be leached out of the galena, if the bacteria is used under optimum pH and temperature conditions in future bioleaching experiments.

• Journal of the Korea Convergence Society
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• v.7 no.1
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• pp.155-160
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• 2016

The convergence process utilized both leaching and ion exchange techniques has been investigated for the heavy metals removal in the abandoned mine of Chungyang Province, Korea. The contaminated soil samples by heavy metals from Samkwang mine were analysed by statistical analyses. The highly contaminated soils was initially separated by the flotation process. The selectivity indices were increased with increasing flotation reagents. The selectivity of separation was then improved by the use of both leaching and ion exchange processes in order to extract the heavy metals. The results of this study showed that the higher the sulfuric acid concentration, the leaching rate of heavy metals was increased. The lecheate then was removed by the ion exchange method. The anticipating results might imply that convergence process utilized both leaching and ion exchange techniques would somehow apply for the removal of heavy metals in the abandoned mine.

• Membrane Journal
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• v.13 no.1
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• pp.47-53
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• 2003

Poly(ether ether ketone)(PEEK) was sulfonated using sulfuric acid and blended with polysulfone with various ratios. The blended polymer electrolyte membranes were characterized in terms of methanol permeability, proton conductivity and ion exchange capacity. As the amount of sulfonated PEEK increased, both methanol permeability and proton conductivity increased. This was due to the increase of ion exchange capacity. The experimental results indicated that the blend membrane with 20% polysulfone was the best choice In terms of the ratio of proton conductivity to methanol permeability.

• Journal of the Korean Chemical Society
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• v.27 no.5
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• pp.345-352
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• 1983

Using a column of macrorecticular gel beads impregnated with alcohol solution of diphenylcarbarzide (DPC), the enrichment of Cr(Ⅵ) ion in 0.1M sulfuric acid was investigated. The column performance was compared with respect to the types of solid support such as Amberlite XAD and Diaion HP. Diaion HP-20 was found to be most suitable for this purpose. The break through point was increased when increasing the amount of DPC absorbed in the resin and the concentrated sample solution showed higher break through capacity than the dilute one. The extraction of Cr(Ⅵ) was not affected by the presence of 100 ppm Fe(Ⅲ) which amounted to ten times of 10 ppm Cr(Ⅵ) and the presence of other metal ions which amounted to 100 times of 10 ppm Cr(Ⅵ). Because the used gel particles were effectively regenerated with methanol, they were able to be used repeatedly.

• Resources Recycling
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• v.17 no.1
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• pp.80-87
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• 2008

Cementation and solvent extraction processes were studied to separate nickel and iron ions from the $H_2SO_4$ leaching solution with 47 g/L $Fe(Fe^{2+}/Fe^{3+}=1.03),$, 23.5 g/L Ni and 0.90M $H_2SO_4$ which leached from Fe-Ni alloy. Iron powder was used as a reducing agent for the cementation of Ni ion from the leaching solution. The reduction percentage of Ni ion was $17{\sim}20%$ by adding 4 times stoichiometric amount of iron powder at $60{\sim}80$. This may result from the fact that the cementation of Ni ion occurred after the reduction of $Fe^{3+}$ to $Fe^{2+}$ and the neutralization of $H_2SO_4$ with iron powder. The cementation process was proved to be unfeasible for the separation/recovery of Ni ion from the leaching solution including $Fe^{3+}$ as a major component. $Fe^{2+}$ present in the leaching solution was converted to $Fe^{3+}$ for solvent extraction of Fe ion using D2EHPA in kerosene as a extractant. The oxidation of $Fe^{2+}$ to $Fe^{3+}$ was completed by the addition of 1.2 times stoichiometric amount of 35% $H_2SO_4$. 99.6% $Fe^{3+}$ was extracted from the leaching solution (23.5 g/L $Fe^{3+}$) by 4 stages cross-current extraction using 20 vol.% D2EHPA in kerosene. $NiSO_4$ solution with 98.5% purity was recovered from the $H_2SO_4$ leaching solution of scrapped Fe-Ni alloy.

• Proceedings of the Korean Society of Soil and Groundwater Environment Conference
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• 2002.04a
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• pp.225-228
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• 2002

서울 지하철 A설계구간에서의 전체 21개 지하수 시료에 대하여 수질분석을 실시하였다. 배경수질은 주로 Ca-HCO$_3$ type으로 전 지역에서의 물-암석 반응 자체는 큰 차이가 없음을 보인다. 본 조사에서 실시한 분석요소 중, 먹는 물 기준치를 초과하지 않은 시료는 3개이며, 나머지 18개 시료는 중금속과 불소, 황산염 등에 의해 이미 오염되어 있는 것으로 나타났다. 지하수 오염도는 BH-l~5 지역에서 보이는 카드뮴에 의한 오염현상과 BH-6~23 지역에서 보이는 다른 중금속 이온들에 의한 오염으로 뚜렷한 지역적인 차이가 보이는데, 이는 자연적인 지하매질과 지하수의 물-암석 반응에 의한 것이기보다는, 이들 지역에 매립된 인위적인 오염물질의 차이에 의해 결정되는 것으로 추정된다.

• Journal of Welding and Joining
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• v.13 no.4
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• pp.24-29
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• 1995

전자제품의 고기능화에 따라 Controller의 중요성은 점점 증대되고 있다. 따라서 Controller(이하 PCB라 칭함)의 제조 공정에서 납땜 관련 Board 재료, Flux, Flux 탄화 연기 등은 식물의 고사 현상등 지구환경을 위협하고 있다. 특히, 자동차 매연이나 도장 또는 PCB 납땜시 SOX, NOX, 탄화수소계등이 휘발하게 되며 아황산 가스 나 질소 산화물이 대기중에서 물과 반응하여 황산 또는 질산으로 변하여 PH 5.6이하 의 산성비를 내리게 한다. 이 산성비는 삼림피해 어류감소 등 생태계를 파괴하고 콘 크리트 철재등 건축 자재물을 부사시킨다. 또한 바람에 의해 인접국가에도 막대한 피해를 주고 있다. 특히 폐가전제품의 PCB 접합부에 산성비가 접촉되면 Pb 이온이 용출되어 토양 및 수질오염, 인체피해 등 심각한 영향을 미치게 된다. 최근 이와관련 세계 각국의 규제 움직임이 활발해지고 있어, 본 논문은 전자기기 제품의 심장인 PCB 와 관계된 환경오염 대상물질의 규제동향과 심각성 및 이에 대한 환경피해 Mechanism 을 분석하여 실장기술에 있어서 총체적인 환경대응 방안을 모색하고자 한다.

• Journal of the Korean Chemical Society
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• v.18 no.3
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• pp.153-156
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• 1974

The kinetics of gas evolution in the reaction between hydrazine and iodine in a sulfuric acid medium has been studied at $25^{\circ}$. The rate is first order in hydrazine and iodine concentration. The iodide ion retards the reaction whereas the effect of hydrogen ion concentration is rather complicated. The rate of gas evolution is very close to that of iodine consumption.