• Journal of the Korean Electrochemical Society
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• v.24 no.4
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• pp.113-119
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• 2021

In this study, impurity free V^3.5+ electrolytes were prepared using formic acid as a reducing agent and PtD/C as a catalyst and it was applied to VRFB. The well-oriented 3D dendrite structure of the PtD/C catalyst showed high catalytic activity in formic acid oxidation reaction and vanadium reduction reaction. As a result, the conversion ratio of electrolyte using the PtD/C was 2.73 mol g^-1 h^-1, which was higher than that of 1.67 mol g^-1 h^-1 of Pt/C prepared by the polyol method. In addition, in the VRFB charging and discharging experiment, the V^3.5+ electrolyte produced by the catalytic reaction showed the same performance as the standard V^3.5+ electrolyte prepared by the electrolytic method, thus proving that it can be used as an electrolyte for VRFB.

• Proceedings of the Korean Institute of Surface Engineering Conference
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• 2016.11a
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• pp.125.1-125.1
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• 2016

마그네슘 합금은 소재 특성상 표면처리가 필수불가결하다. 금속의 다양한 표면처리 방법 중 마그네슘 합금은 크게 화학적 반응을 이용해 산화막을 생성해 피막을 올리는 화성처리법과, 전해액 내에 침지시켜 전기를 걸어주어 금속 표면에 플라즈마 아크를 통해 산화막을 생성하는 PEO공법 두 가지 방법이 있다. 본 연구에서는 마그네슘 합금 소재에 PEO공법을 적용한 산화피막의 공정 변수에 따른 특성을 SEM, EDS, SST, potentiodynamic polarization 등으로 분석하였다.

• Proceedings of the KAIS Fall Conference
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• 2007.11a
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• pp.356-358
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• 2007

본 논문에서는 농도가 다른 EC계의 전해질 용액 중에서 흑연의 Cyclic voltammetry(CV)를 측정하였다. CV후 전극표면에 생성된 SEI를 투과형 전자현미경으로 분석한 결과, PC계에서 얻어지는 결과와 유사하게 충 방전 반응 및 생성된 SEI의 성질이 전해질의 농도에 크게 의존하고 있음을 확인하였다.

• Proceedings of the Korean Institute of Surface Engineering Conference
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• 2016.11a
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• pp.144-144
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• 2016

플라즈마 전해 산화법(Plasma electrolytic oxidation)에 의해 형성된 코팅층은 특유의 기공구조로 인해 부식 환경에 노출 시 부식액의 침투가 급속히 이루어지는 단점이 있다. 이를 극복하기 위한 방법으로 유기코팅, sol-gel법, 폴리머 코팅 등에 의해 기공을 봉공(sealing)하는 방법이 제안되고 있다. 본 연구에서는 Al 합금의 플라즈마 전해 산화 처리 후 질산 세륨 수용액(Cerium nitrate solution)에 의한 봉공 효과를 확인하고자 하였다. PEO 코팅을 위한 전해액은 2g/L의 KOH와 $2g/L\;Na_2SiO_3$를 증류수에 용해시켜 준비하였다. PEO 코팅층은 Al 시편을 전해액 내에 위치시켜 양극으로 하고 STS를 음극으로 하여 $0.1A/cm^2$의 펄스 정전류밀도(주파수: 100Hz, 듀티비: 20%)를 15분 동안 인가하여 형성시켰다. 봉공을 위한 실링액은 증류수에 $0.3g/L\;H_2O_2$와 $1g/L\;H_3BO_3$를 첨가하고, $Ce(NO_3)_3$를 농도 변수로 첨가하여 준비하였으며, PEO 코팅 처리된 시편을 실링액에 침지하여 실링액의 농도와 침지시간을 달리하여 봉공을 실시하였다. 제작된 PEO 코팅층에 대해 SEM, EDS, XRD를 이용한 표면분석을 실시하였으며, 내식성을 확인하고자 동전위분극시험을 실시하였다. 연구 결과, 세륨 실링 처리된 PEO 코팅 층에서 미량의 세륨 성분이 검출되었으나, 세륨계 화합물 생성에 의한 마이크로 크기의 기공의 폐쇄는 관찰되지 않았다. 또한, 전기화학적 특성 평가 결과 실링 처리된 PEO 코팅층의 경우 Al 모재에 비해 2차수 정도 감소된 부식전류밀도를 나타내었다. 이 같은 내식성의 향상은 세륨 성분에 의한 부식 억제 효과 때문으로 판단된다.

• Transactions of the Korean hydrogen and new energy society
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• v.9 no.1
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• pp.8-15
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• 1998

The catalytic hydrogenation of carbon dioxide has been studied for the fixation of carbon dioxide to mitigate global warming problems, but it needed hydrogen, which the price is still high. Recently, the electrochemical reduction of carbon dioxide has been drawn attractions because carbon dioxide could be converted to the valuable chemicals such as methane, ethane and alcohols electrochemically in the electrolyte solution using a catalytic electrode. This system is simple because the water electrolysis and hydrogenation take place at the same time using the surplus electricity at midnight. In this work, a continuous electrochemical reduction system was fabricated, which was composed of the reduction electrode (copper or perovskite type, $2{\times}2cm^2$), reference electrode(platinum, $2{\times}6cm^2$), standard electrode(Ag/AgCl), and potassium bicarbonate electrolyte solution saturated with carbon dioxide. The quality and quantity of the products and reduction current were analyzed, according to the electrolyte concentration and electrode type.

• Proceedings of the Korean Society of Dyers and Finishers Conference
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• 2003.04a
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• pp.66-71
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• 2003

오늘날 인간 생활에서 섬유제품은 인체와 가장 많이 접하고 있어서 인체의 분비물과 함께 미생물이 서식하여 인체 건강을 해치거나 악취를 발생시킨다. 이러한 현상은 섬유제품을 변색, 오염, 손상시키므로 항균, 소취성있는 섬유제품이 요구된다. 또한 섬유제품에 처리된 항균, 소취가공제는 안전성이 요구되며, 동시에 자연계에서 간단히 분해되고 유해물질을 생성하지 않아야 한다. (중략)

• Korean Journal of Materials Research
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• v.6 no.2
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• pp.228-234
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• 1996

BzCuO2 의 생성 자유에너지를 이중 이온교환된 Ba2+-$\beta$/$\beta$"-AI2O3를 전해질로 사용하여 다음과 같은 생성셀로부터 측정하였다. Au(po2=10-3)/Au+BaCuO2+CuO// Ba2+-$\beta$/$\beta$"-Au이 갈바닉셀에서 BzCuO2 의 임의의 생성식과 생성자유에너지는 다음과 같다. BaO+CuO=BaCuO2 $\Delta$fGo/kJ.mol-1=-77.3-3.3x10-3T/K.3x10-3T/K.

• Journal of Korean Society of Environmental Engineers
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• v.34 no.10
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• pp.702-708
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• 2012

Tetrafluoromethane ($CF_4$) has been used as etching and Chemical Vapor Deposition (CVD) gases for semiconductor manufacturing processes. These gases need to be removed efficiently because of their strong absorption of infrared radiation and long atmospheric lifetimes which cause the global warming effect. Also, the wastewater including the fluorine is caused by of the ground water pollution. Long-term consumption of water containing excessive fluoride can lead to fluorosis of the teeth and bones. The wastewater including the fluorine among the by-product which is generated by using the waterjet plasma after destroying $CF_4$ by HF is generated. The system which can remove the hydrogen fluoride among the wastewater by using the electrocoagulation using this wastewater the aluminum electrode was developed. The operating condition such as initial pH, electrocoagulation time, wastewater flow rate, current density were investigated experimentally using a electrocoagulation. Through the parametric studies, the highest hydrogen fluoride destruction of 85% was achieved at 3.5 initial pH, 10 min electrocoagulation time, 10 mL/min wastewater flow rate and $159A/m^2$ current density.

• Journal of the Korean Society of Fisheries and Ocean Technology
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• v.38 no.1
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• pp.79-88
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• 2002

13%Cr martensitic stainless steel has been used mainly with a material for fish pre-processing machinery. However, it has not very nice cutting section because of little of the carbon content. Therefore, SUS420J2 steel that contents 0.3%C with high-strength in spite of the rust is used with a material for fish pre-processing machinery. However, studies on the corrosion characteristics of SUS420J2 steel are relatively rare. Especially, the corrosion phenomenon may cause serious degradation because the fish pre-processing machinery is exposed always to seawater environment. In this paper, the immersion corrosion test was carried out at seawater environment (pH=7.52) on SUS420J2 steel specimens that have various post-treatment conditions and its corrosion characteristics were evaluated. From test results, the specimens such as base metal, vacuum heat treatment, electrolytic polishing and tempering after quenching tend somewhat sensitive from the corrosion. In the case of vacuum heat treatment specimen of continuous immersion during 360 days, the weight loss ratio was high about seven times when compared with the different specimens. On the contrary, SUS420J2 steel specimen that has the heat treatment of tempering after quenching and the electrolytic polishing was less sensitive from the corrosion, and the weight loss ratio was very low.

• Journal of the Korean Institute of Gas
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• v.4 no.1 s.9
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• pp.40-48
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• 2000

A fuel cell is an electrochemical device continuously converting the chemical energy in a fuel and an oxidant to electrical energy by going through an essentially invariant electrode-electrolyte system. Phosphoric acid fuel cell employs concentrated phosphoric acid as an electrolyte. The cell stack in the fuel cell, which is the most important part of the fuel cell system, is made up of anode where oxidation of the fuel occurs cathode where reduction of the oxidant occurs; and electrolyte, to separate the anode and cathode and to conduct the ions between them. Fuel cell performance is associated with many parameters such as operating and design parameters associated with the system configuration. In order to understand the design concepts of the phosphoric fuel cell and predict it's performance, we have here introduced the simulation of the fuel-cell stack which is core component and modeled in a 3-dimensional grid space. The concentration of reactants and products, and the temperature distributions according to the flow rates of an oxidant are computed by the help of a computational fluid dynamic code, i.e., FLUENT.