• 한국신재생에너지학회:학술대회논문집
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• 2010.06a
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• pp.146.2-146.2
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• 2010

PEMFC를 구성하는 여러 부품 중 핵심부품은 MEA(Membrane Electrode Assembly)으로서 실제 연료전지 반응이 일어나며 연료전지의 성능을 결정하는 부품이다. 그러나 PEMFC의 특성 상 촉매로 귀금속인 Pt가 사용됨에 따라 경제성이 확보된 MEA의 성능을 얻기 위해선 현재 Pt 담지량을 0.3mg/$cm^2$ 이하로 크게 감소시키면서 Pt촉매의 고분산화와 미반응 사이트의 감소가 필요하다. 본 연구에서는 Pt 촉매의 미반응 사이트를 줄이고자 전기영동법에 의해 카본전극(carbon black + GDL) 상에 Pt 나노입자를 직접 석출시켜 Pt/C 촉매 전극을 제조 하였다. 본 실험에서는 가장 좋은 Pt 나노입자의 석출거동을 나타낸 30mA/$cm^2$, pH 2, duty cycle 25% 조건을 기준으로 하여 electro-deposition time을 통한 석출량 제어와 carbon paper의 wet proofing 정도에 따른 Pt의 석출거동을 조사하였으며, 종래의 방법으로 제조한 Pt/C 촉매전극의 전기화학적 특성과 비교 분석하였다. 전기영동 석출법에 사용된 Pt나노입자는 $H_2PtCl_6{\cdot}6H_2O$로부터 화학적 환원법으로 합성한 2~3nm 입경을 갖는 Pt콜로이드를 사용하였으며, magnetic stirring과 항온 ($20^{\circ}C$)을 유지하여 실험하였다. 전기영동 석출량 제어는 electro-deposition time을 5~25분까지 5분 간격으로 나누어 실험하였고 카본전극을 구성하는 carbon paper의 wet proofing 정도가 Pt 나노입자 석출거동에 미치는 영향을 조사하기 위하여 20, 40, 60%의 서로 다른 wet proofing 값을 갖는 carbon paper를 사용하여 Pt/C 촉매 전극을 제조하였다. 전기영동법으로 석출된 카본블랙 전극 상 Pt나노입자의 분산도와 담지량는 각각 FE-SEM과 TGA 장비를 사용하여 측정하였고, 제조된 Pt/C 촉매 전극의 전기화학적 촉매 특성은 cyclic voltammetry(CV)법으로 측정하였다.

• Applied Biological Chemistry
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• v.36 no.5
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• pp.326-331
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• 1993

Three antioxidants were isolated: (-)-epigallocatechin and (-)-epigallo catechin gallate from Theae Folium generally called green tea, and gallic acid from Moutan Cortex. They inhibited $Fe^{3+}-ADP/ascorbate-induced$ lipid peroxidation in rat liver microsomal fraction, showing $IC_{50}$, the concentration of antioxidants which is required to inhibit 50% of the peroxidation for microsomal membranes at 1 mg protein/ml, to be $0.2\;{\mu}g/ml$, $0.4\;{\mu}g/ml$ and $2.5\;{\mu}g/ml$, respectively.

• Journal of the Korean Electrochemical Society
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• v.6 no.2
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• pp.130-133
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• 2003

3,4-dihydroxybenzoic acid(3,4-DHBA) was electropolymerized on glassy carbon electrode to give the GC/p-3,4-DHBA type electrode which was modified with dopamine by the help of 1-(3-dimethylaminopropyl)-3-ethyl carbodiimide hydrochloride(EDC) acting as a coupling agent. The carboxylic sites on the polymeric surface of p-3,4-DHBA and mine group at the dopamine gave a QCA(Au)/p-3,4-DHBA-dopamine type of modified electrodes. The o-quinone moieties at the electrode surface exhibited high selectivity to titanium ions in solution. The redox process of the electrode is hydroquinone : quinone +$2H^+2e^-$, which had two strong and two weak pairs of peaks at CV. The modified electrode can deposit Ti(IV) ions as much as $4.13\times10^{-5}gcm^{-2}$. The calibration curve of the electrodes, log of the surface coverage-normalized redox response vs log[Ti], exhibited an excellent correlation$(r{\geq}0.997)$ for titanium concentrations ranging from $5.25\times10^{-4}\;to\;5.25\tiems10^{-8}M.$.

• Korean Journal of Environmental Biology
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• v.19 no.2
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• pp.93-99
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• 2001

There are several ways to remove and treat toxic heavy metals in the environment: chemical, physical and biological ways. The biological treatment utilizes the natural reactions of microorganisms living in the environments. These reactions include biosorption and bioaccumulation, oxidation and reduction, methylation and demethylation, metal - organic complexation and insoluble complex formation. The biological reactions provide a crucial key technology in the remediation of heavy metal-contaminated soils and waters. According to recent reports, various kinds of heavy metal species were removed by microorganisms and the new approaches and removal conditions to remediate the metals were also tried and reported elsewhere. This was mostly carried out by microorganisms such as fungi, bacteria and alga. In addition, a recent development of molecular biology shed light on the enhancing the microorganism's natural remediation capability as well as improving the current biological treatment.

• Journal of Soil and Groundwater Environment
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• v.7 no.3
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• pp.79-84
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• 2002

The optimal operation conditions, including voltage applied, reaction time, distance between electrodes. and electrode material. were investigated for the treatment of soil flushing effluent using electrofloatation. When 3V was applied for 1 hour, 88% oil-water separation efficiency was achieved. In case of 6V and above, 90% efficiencies were achieved. As reaction time and distance between electrodes were longer, separation efficiencies were higher and lower, respectively. Separation efficiencies for different anode materials were copper > aluminum > iron > titanium. It might result from the differences of their electrical conductivities.

• Journal of Nuclear Fuel Cycle and Waste Technology(JNFCWT)
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• v.8 no.1
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• pp.71-76
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• 2010

The electrorefining process, one of main processes which are composed of pyroprocess to recover the useful elements from spent fuel, and the domestic development of electrorefiner have been reviewed. The electrorefiner is composed of an anode basket containing reduced spent fuel such as uranium, transuranic and rare earth elements, and a solid cathode, which are in LiCl-KCl eutectic electrolyte. Oxidation (dissolution) reaction occurs on the anode and a pure uranium is electrochemically reduced (deposited) on the solid cathode. By application of graphite cathode, which has a self-scrapping characteristics for the uranium deposits, and a recovery of the fallen deposits by a screw conveyer, a high-throughput continuous electrorefiner with a capacity of 20 kgU/day has been developed.

• Resources Recycling
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• v.26 no.3
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• pp.17-25
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• 2017

Electric arc furnace steelmaking dust has various physicochemical properties as volatile components generated in the melting process of steel scraps in an electric arc furnace, which is captured in oxide form as fine powder by reacting with oxygen in the air. In order to efficiently recycle these electric arc furnace dust, a kinetic basic experiment and a pilot production test were carried out in parallel. As a result, it was found that the electric arc furnace dust contain a large amount of Cl and alkali components, thus it was expected that the compounds have a great adverse effect on the actual operation for the recycling. It was confirmed that the volatilization behavior was progressing actively at $1100^{\circ}C$ and the electric arc furnace dust was melted at $1250^{\circ}C$. These results are the same as a result of pilot test for the formation behavior of zinc oxide and reduced iron. These results should be useful as basic data for designing the recycling plant of the electric arc furnace dust and establishing the operating conditions.

• Economic and Environmental Geology
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• v.46 no.1
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• pp.29-37
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• 2013

In order to apply the silver cementation method using Fe powder from pregnant thiourea leaching solution. Parameters such as the amount of Fe powder addition, agitation speed, and temperature were investigated. The silver cementation rate was increased by the increasing of Fe powder addition, agitation speed, and temperature. The highest silver cementation rate was found when the addition of Fe powder was 50 g/L at the agitation speed of 500 rpm. The silver cementation rate increase with increasing temperature according to the Arrhenius equation and obeys $1^{st}$ order kinetics. The activation energy from the kinetics data was found to be between 13.73 KJ/mol and 17.02 KJ/mol. In the XRD analysis, goethite was detected in the precipitate of the thiourea leach solution. This indicates that an oxidation-reduction reaction had occurred in the thiourea solution due to the addition of the Fe powder.

• Journal of Korean Society of Environmental Engineers
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• v.36 no.11
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• pp.758-763
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• 2014

Soil microbial fuel cells (SMFC) have gained a great attention as an eco-friendly technology that can simultaneously generate electricity and treat organic pollutants from the contaminated soil. We evaluated the effect of electrode spacing and size on the performance of SMFC treating soil contaminated with organic pollutants. Maximum power density decreased with increase in electrode distance or decrease in electrode size, likely due to higher internal resistance. The maximum voltage and power density decreased from 326 mV and $19.5mW/m^2$ with 4 cm of electrode distance to 222 mV and $5.9mW/m^2$ with 9 cm of electrode distance. In case of electrode size test, the maximum voltage and power density generated was 291 mV, $0.34mW/m^3$ when both of anode and cathode area were $64cm^2$ with 4 cm of electrode distance. The maximum voltage decreased by 19~29% when the anode area decreased to $16cm^2$ while only 3~12% of voltage decreased with cathode area decrease. The maximum power density decreased by 49~68% with decreasing anode size, and by 29~47% with decreasing cathode size. These results showed that the anode area had more significant effects than the cathode area on the power generation of SMFC which has a high internal resistance due to a coexistence of soil and wastewater in the reactor.

• Journal of the Korean Ceramic Society
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• v.40 no.5
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• pp.488-493
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• 2003

Nickel fine powders were prepared from aqueous nickel chloride solution containing organic solvents and the effect of the addition of the organic solvent on the formation of nickel powders were investigated. All products were spherical particles in the range of 0.1∼1.0 $\mu\textrm{m}$ and the agglomeration of particles did not appear. In case of containing 40 vol% of 1-propanol, the particle size reduction and homogeneity of the powders were remarkable. The average particle size and the specific surface area of the powders produced with 40 vol% of 1-propanol were 0.3 $\mu\textrm{m}$ and 16.4 m$^2$/g respectively. The reduction reaction time by hydrazine decreased with increasing of the content of 1-propanol, and was 5 min for 40 vol% of 1-propanol. The oxidation of synthesized nickel powders occurred at 320$^{\circ}C$ and weight loss at 300$^{\circ}C$ was due to dehydration of Ni(OH)$_2$.