• 상하수도학회지
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• 제25권4호
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• pp.591-596
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• 2011

Surface floating air cathode microbial fuel cell (MFC) having horizontal flow was developed for the application of MFC technology. RVC (Reticulated vitreous carbon) coated with anyline was used as anode electrode and carbon cloth coated with Pt (5.0 g Pt/$m^2$, GDE LT250EW, E-TEK) was used as cathode electrode. As results of continuous operation with changing the flow rate from 4.3 mL/min to 9.5 mL/min, maximum power density of 4.5 W/$m^3$ was acquired at 5.4 mL/min, which was at 0.35 m/hr of flow velocity under anode electrode. When the ratio of cathode surface area to anode surface area($A_c/A_a$) was changed to 1.0, 0.5, and 0.25, the maximum power density of 2.7 W/$m^3$ was shown at the ratio of 1.0. As the ratio decreased from 1.0 to 0.25, the power density also decreased, which is caused by increasing the internal resistance resulted from reducing the surface area to contact with oxygen. Actually, internal resistances of the ratio of 1.0, 0.5, and 0.25 were 63.75${\Omega}$, 142.18${\Omega}$, and 206.12${\Omega}$, respectively.

• Corrosion Science and Technology
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• 제11권6호
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• pp.242-246
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• 2012

This measurement represents the effectiveness of sacrificial anode cathodic protection (SACP) system in a coastal bridge structure. To verify the cathodic protection (CP) effect, the monitoring sensor (DMS-100) that could measure potential, corrosion rate, current, concrete resistivity, and temperature was embedded. The measurement conducted for three years after CP system was installed. Specifically, due to the fact that fresh water and sea water was repeated in the bridge structure, this bridge structure presented special CP behavior. Measurement factors were CP potential, CP current, concrete resistivity, and depolarization potential. In addition, visual inspection was also carried out. As a result of current and depolarization measurement, CP system was well activated in most piers.

• 해양환경안전학회지
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• 제2권1호
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• pp.67-75
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• 1996

An innovative batch electrolytic system consisted of electrolytic basin, which was equipped with DSA(Dimensionally Stable Anode) type insoluble electrode, Ti/IrO2 anode and H-C metal cathode, and flotation separator was developed for the efficient treatment of shipboard emulsified oily wastewater. The electorod cleance and current density of elecrolytic basin to ensure maximum treatment efficiency of oily wastewater was evaluated as 6 mm, 3 A/dm3, respectively. The electrolytic efficiency of oily wastewater was affected by the operationtemperature, and it means that the temperature controller to ensure the stabiity of the process is required. The conductivity in the electrolytic basin was increased with the percentage of sea water in the oily wastewater, and over 90% of treatment efficiency of oily wastewater could be obtained at 7% of sea water. The oil removal rate was increased according to the increase of the quantity of electricity, and the maximum value of electrilyic rate constant was 288 mgoil/A.min. The information obtained from this study might be used for development of an efficient continuous electrolytic system treating the emulsified oily wastewater.

• Journal of Electrochemical Science and Technology
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• 제7권1호
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• pp.76-81
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• 2016

An anatase TiO₂ nanotube array (NTA) was fabricated by anodization and successive heat treatments. When the anatase TiO₂ NTA was cathodically polarized, its color changed to blue, and it could be used as an electrochemically active anode for an oxygen evolution reaction (OER) in alkaline water electrolysis. The structure of the blue anatase TiO₂ NTA was controlled by the anodization conditions and its catalytic activity increased with an increase of the surface area. The activity of the blue anatase TiO₂ NTA gradually reduced with the continued OER because of the partial oxidation of Ti³⁺ to Ti⁴⁺. However, an intermittent cathodic regeneration process could significantly slow its reduction rate. The blue anatase TiO₂ NTA could be an alternative anode for alkaline water electrolysis.

• 공업화학
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• 제10권6호
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• pp.929-933
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• 1999

염산 수용액을 전해액으로 하여 물의 전기분해가 일어나는 조건에서 양극에 충전된 납-흡착 활성탄으로부터 납의 제거 실험결과, 흐름 조건으로서 양극부와 음극부의 유량이 동일한 경우 전체 유량 10 mL/min이 적당하며 전류 증가는 양극에서의 pH를 감소시키고 양극에서의 pH 감소가 납의 제거율 증가를 가져옴을 알 수 있었다. 물의 전기분해를 이용하는 본 방법은 산세척법에 비하여 약품 사용량을 줄이면서 납-흡착 활성탄으로부터 납을 효과적으로 제거할 수 있는 방법임을 알 수 있었다.

• Journal of Electrochemical Science and Technology
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• 제14권3호
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• pp.283-292
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• 2023

Currently, spray coating has attracted interest in the mass production of anode catalyst layers for proton exchange membrane water electrolysis (PEMWE). The solvent in the spray ink is a critical factor for the catalyst dispersion in ink, the microstructure of the catalyst layer, and the PEMWE performance. Herein, various pure organic solvents were examined as a substitute for conventional isopropanol-deionized water (IPA-DIW) mixture for ink solvent. Among the polar solvents that exhibited better IrO₂ dispersion over nonpolar solvents, 2-butanol (2-BuOH) was selected as a suitable candidate. The PEMWE single cells were fabricated using 2-BuOH at various ionomer contents, spray nozzle types, and drying temperatures, and their performance was compared to the cells fabricated using a conventional IPA-DIW mixture. The PEMWE single cells with 2-BuOH solvent showed good performances comparable to the conventional IPA-DIW mixture case and highly durable performances under accelerated degradation tests.

• 상하수도학회지
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• 제26권3호
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• pp.409-421
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• 2012

Ethanolamine (ETA) is mainly used to prevent corrosion of pipe in secondary cooling system of nuclear power plant. Condensed ETA in wastewater could increase COD and T-N when it was emitted to natural water system. Compared to conventional treatments, electrochemical oxidation process using packed bed bipolar electrodes was adopted to treat COD and T-N. According to arrangement of feeder electrode, single packed bed bipolar electrode reactor and multi-paired packed bed bipolar reactor were developed and conventional zero-valent iron (ZVI) was selected as conducting bipolar electrode. Bipolar electrodes were coordinated three-dimensionally in the reactor. The experimental results showed that COD and T-N was little removed in unit system at different pH condition (pH 8 and 11) on 100V. However, in multi-paired system that applied 600V, COD was eliminated 80.85% (anode-cathode-anode, A-C-A) and 85.11% (cathode-anode-cathode, C-A-C), respectively. T-N was also removed 96.88% (A-C-A) and 90.63% (C-A-C), simultaneously. Current efficiency was estimated both single and multi-paired system. At unit bipolar packed bed reactor, current efficiency was almost zero, however in multi-paired system, current efficiency was 300~500% at A-C-A and 250~350% at C-A-C. Current efficiency was over 100% hence it was confirmed that this system is more effective than conventional electrochemical oxidation system.

• 전기화학회지
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• 제8권4호
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• pp.155-161
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• 2005

상용 CFD 프로그램인 FLUENT v5.3을 이용하여 용융탄산염 연료전지 스택의 수치 모사를 행하였다. FLUENT에 포함되어 있는 보존식들을 이용하면서, 사용자 정의함수를 이용하여 포함시킨 코드를 통해 전기화학적 반응과 부반응인 수성가스전이반응에 의한 질량과 가스 조성 변화 및 열이동을 고려하여 정확한 계산 결과를 얻고자 하였다. 모사에 사용된 스택은 6kW급과 25kW급 스택으로 각각 20개와 40개의 단위전지를 수직으로 적층한 형태이며 스택내로 주입되는 가스는 coflow형태로 각각의 채널을 흘러가게 설계되어 있다. 모사를 통해 알아본 스택 내 압력분포는 가스 흐름방향으로 압력강하가 일어나며 anode 채널보다 cathode 채널에서의 압력차가 더 크게 나타났다. 채널 내 속도분포는 전극 반응에 의한 질량 및 부피변화로 인해 anode 채널에서는 가스흐름 방향으로 속도가 증가하는 반면 cathode 채널에서는 속도가 감소하는 경향을 보였다. 스택 내 온도분포는 가스 흐름방향으로 증가하는 경향을 보였고, 계산결과와 실험결과가 대체로 일치함을 확인할 수 있었다. 수성가스전이반응을 포함한 모델과 그렇지 않은 모델을 비교한 결과 가스의 주입구 부분에서는 수성가스전이반응에 의해 흡열 반응이, 출구 부분에서는 발열반응이 일어나고, 이로 인해 입구와 출구의 온도차가 더 커짐을 확인하였다. 따라서 상용화 스택인 수백 kW급 이상의 대형 스택을 모사하기 위해서는 수성가스전이반응을 고려해야할 것으로 생각된다.

• Korean Chemical Engineering Research
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• 제55권1호
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• pp.107-114
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• 2017

고분자전해질 연료전지(PEMFC: polymer electrolyte membrane fuel cell)는 일산화탄소(CO)나 황화수소($H_2S$)가 포함된 연료가 주입될 경우 성능이 저하된다. 일반적으로 멀캅탄 계열의 부취제가 첨가된 탄화수소를 개질하여 생성된 수소에는 미량의 황화수소가 포함되어 있다. 본 연구에서는 황화수소를 수소에 첨가하여 anode에 주입하였을 경우에 연료전지 성능에 미치는 영향을 파악하고, 3가지 다른 회복방법인 순수 수소 주입법, 전위 순환법과 물 순환법을 적용한 경우의 회복률을 비교하여 보았다. PEMFC의 성능은 전기화학적 방법인 polarization curve, electrochemical impedance spectroscopy (EIS)와 cyclic voltammetry (CV)를 사용하여 분석하였다. 피독에 대한 회복방법인 순수 수소 주입법과 전위 순환법을 사용한 경우에는 회복률이 적었고, 물 순환법을 사용한 경우에는 초기에 대비하여 약 95% 이상 성능이 회복된 것을 확인하였다. 직접적으로 피독에 노출된 anode에 물을 흘린 경우의 성능회복률이 높았으며, cathode에 흘린 경우에도 물의 crossover에 의한 효과로 전위 순환법보다 우수한 회복률을 보였다. 이러한 연구결과로부터 황화수소 피독에 대한 회복기법을 구축함으로서 연료전지의 내구성을 향상시킬 수 있고, 불순물이 미량 함유된 저가 수소의 사용을 가능하게 함으로서 연료전지 보급에도 기여할 수 있을 것이다.

• 한국재료학회지
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• 제33권12호
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• pp.530-536
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• 2023

The theoretical capacity of silicon-based anode materials is more than 10 times higher than the capacity of graphite, so silicon can be used as an alternative to graphite anode materials. However, silicon has a much higher contraction and expansion rate due to lithiation of the anode material during the charge and discharge processes, compared to graphite anode materials, resulting in the pulverization of silicon particles during repeated charge and discharge. To compensate for the above issues, there is a growing interest in SiO_x materials with a silica or carbon coating to minimize the expansion of the silicon. In this study, spherical silica (SiO₂) was synthesized using TEOS as a starting material for the fabrication of such SiO_x through heating in a reduction atmosphere. SiO_x powder was produced by adding PVA as a carbon source and inducing the reduction of silica by the carbothermal reduction method. The ratio of TEOS to distilled water, the stirring time, and the amount of PVA added were adjusted to induce size and morphology, resulting in uniform nanosized spherical silica particles. For the reduction of the spherical monodisperse silica particles, a nitrogen gas atmosphere mixed with 5 % hydrogen was applied, and oxygen atoms in the silica were selectively removed by the carbothermal reduction method. The produced SiO_x powder was characterized by FE-SEM to examine the morphology and size changes of the particles, and XPS and FT-IR were used to examine the x value (O/Si ratio) of the synthesized SiO_x.