• Proceedings of the KIEE Conference
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• 1996.07c
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• pp.1520-1522
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• 1996

전기 이중층 콘덴서는 일반적인 콘덴서와 백업용 이차 전지의 중간적 성격을 갖는 디바이스로서 직류 전압 인가시 전하는 진해액과 활성탄의 계면에 전기이중층을 이루며 축적된다. 본 논문에서는 탄화 및 활성화 조건을 달리하여 활성탄 전극을 제조하고 세공 면적, 비표면적, 겉보기 밀도차 기공율을 측정,검토하였으며 여러가지 유기 용매에 tetraethylammonium tetrafluoroborate를 각각 첨가하여 제조한 전해액의 전기전도도를 정하고 이들 전해액과 활성탄 전극을 이용하여 전기 이중층 콘텐서를 제작한 후 정전용량, 활성탄 전극의 안정 전위, 체적용량 밀도, 중량용량 밀도 등을 검토하였다.

• Journal of the Korean Electrochemical Society
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• v.5 no.1
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• pp.7-12
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• 2002

The gas diffusion electrodes as oxygen cathodes f3r the brine electrolysis process were investigated. The gas diffusion electrode consists of a reaction layer, a gas diffusion layer, and a current distributor. The reaction layer was made from hydrophilic carbon black, hydrophobic carbon black, PTFE(polyterafluoroethylene), and Ag catalyst loaded by the silver mirror reaction or impregnation method. The gas diffusion layer was made from hydrophobic carbon black and PTFE, and Ni mesh was used as the current distributor in the reaction layer. The result that the gas diffusion electrode $(10wt\%\;Ag\;catalyst\;and\;20wt\%\;binder)$ manufactured by applying impregnation method to the carbon black f3r reaction layer showed the better performance was obtained from experiments. From the half-cell test, the measured overpotential of this oxygen cathode was about 700mV, And through the electrolysis experiment under the condition of $80^{\circ}C,\;32wt\%$ NaOH, and $300mA/cm^2$, the electrolysis voltage of this electrode was about 2.2 V, The gas diffusion electrodes manufactured in the present research were capable of continuous operations for three months.

• Journal of Korean Society of Environmental Engineers
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• v.27 no.7
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• pp.686-689
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• 2005

This study was conducted to investigate the effect of ammonium and nitrate nitrogen removal to applied voltage, electrolytic time and activated carbon packing height. Batch bipolar packed bed electrolytic cell reactor was packed with $4{\times}8$ mesh granular activated carbon (GAC). Afterward electrolysis was performed in 20 V for 30 min. As a result, as the filling height adjusted to 80 mm high, the removal efficiency of ammonium nitrogen was 99.9%. and as the electrolytic time varied to 60 min, the removal efficiency of ammonium nitrogen was 97.6%. and in case of continuous electrolytic treatment of ammonium and nitrate nitrogen removal efficiency of total nitrogen was over 80% in bipolar packed bed electrolytic cell reactor for 72 hours as the packing height, sample concentration and input rate of sample adjusted to 280 mm, 30 mg/L, 6.7 mL/min, respectively.

• Resources Recycling
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• v.25 no.1
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• pp.60-67
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• 2016

A scale-up test with a continuous solvent extraction and electro-winning system was carried out to separate and recover copper from a synthetic sulfuric acid solution (Cu 10.5 g/L, Co 2.0 g/L, Ni 15.0 g/L, Fe 0.2 g/L). The solution was introduced into mixer-settlers with four stages of extraction and two stages of stripping for continuous countercurrent solvent extraction to separate copper from nickel and cobalt. The loading was carried out using 40% LIX 84-I(v/v) as extractant with a phase ratio of A : O = 1 : 1. Meanwhile, the stripping was undertaken at a phase ratio of A : O = 1 : 1.5 using depleted electrolyte containing 35.0 g/L Cu and 180 g/L $H_2SO_4$ as stripping solution. The extraction and stripping efficiencies were found to be 96.7% and 91.0%, respectively. The copper composition of the stripped solution (pregnant electrolyte) was 50.0 g/L Cu with impurities of 25 ppm nickel, 5 ppm cobalt and 3 ppm iron. In the electro-winning process, copper metal of 99.833 purity was yielded with current efficiency of 98.9% and current density of $1.50A/dm^2$.

• Proceedings of the Korean Society of Precision Engineering Conference
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• 2004.10a
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• pp.42-45
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• 2004

Electrochemical discharge machining (ECDM) has been found to be suitable for the micro-hole machining of nonconductive materials such as ceramics or glass compared with existing conventional and also non-conventional machining methods. However this machining process has some problems such as low geometric accuracy and low machining efficiency due to the random spark generation at the end of the electrode. This paper proposes the methods to improve the geometric accuracy of micro-hole using powder mixed ECDM process. The experimental results show the effects of powder producing improved geometric accuracy of machined hole and decreased concentration of spark energy.

• Proceedings of the Korean Information Science Society Conference
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• 2004.10c
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• pp.580-582
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• 2004

본 논문에서는 사용자의 다양한 단말환경에 맞게 보다 효율적으로 컨텐츠 변환 서비스를 제공하는 최적의 컨텐츠 변환 노드(Contents Translation Node: CTN) 검색 메커니즘을 개발하였다 이 메커니즘은 컨텐츠 변환 노드로 구성된 서비스 오버레이 네트워크에서 노드부하가 적고, 근거리에 위치한 최적의 노드를 선택하여 신속하고 효율적인 서비스 제공을 가능케 하고 노드간의 부하 배분 기능을 지원한다 그리고 털러 노드 성능 요인들 간에 가중치를 적용하여 현재 상황에 맞게 시의적절한 최적의 노드를 선택할 수 있게 한다. 또한 본 논문에서는 이 메커니즘을 이용하여 인터넷 컨텐츠 최적화 서비스를 제공하는 인터넷 컨텐츠 분산 관리 시스템 (Internet Contents Distribution Management System: ICOMS)을 설계하였다.

• Proceedings of the KIEE Conference
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• 2007.11c
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• pp.187-190
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• 2007

To improve the power factor and reduce the harmonic contents of the system, the design of tunned filters for six-pulse thyrister converter which is used by electrolyzer system is discussed in this paper. Tunned filters are added to high-power rectifiers to keep the line current distortion within allowable limits and to improve the rectifier power factor. For electrolyzer system, the design procedure of tunned filters of AC 14.4kV power system are proposed by dynamic simulation. It is shown that these harmonic filters can meet most operational requirments. The the proposed design procedure is verified with the simulation and experimental results.

• 제어로봇시스템학회:학술대회논문집
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• 1991.10a
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• pp.76-80
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• 1991

This paper presents a merit of feedforward Dyamic Matrix Control(DMC) for electrolyzer process. The electrolyzer consists of anode part and cathode part that are separated by ion membrane. As the electolyzer process consumes a large amount of electricity, electric power change is inevitable in order to take advantage of the cheaper electricity during night. But the electric power change makes the electrolyzer control difficult because the electric power change affect the dynamics of the process. Feedforward DMC treats the electric power change as a load disturbance and gives the weighting value to the disturbance prediction part in the DMC algorithm. Feedforward DC shows better regulation performance than PID control and feedforward-feedback control for electrolyzer process.

• Proceedings of the Korean Institute of Surface Engineering Conference
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• 2015.11a
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• pp.326-326
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• 2015

본 연구에서는 전해도금을 이용하여 Ni-Pd 합금도금을 형성한 후 열처리 효과를 분석하였다. 전류밀도 $0.2{\sim}1.5A/dm^2$, $PdCl_2$ 1~5mM의 변화를 통해 Ni-Pd 합금도금의 함량을 변화시켰고 $100{\sim}400^{\circ}C$의 열처리를 하였다. 열처리 온도가 올라갈수록 경도는 급격히 떨어졌고 $300^{\circ}C$이후에서는 감소하였으나 감소폭이 작았다. 경도의 감소 원인은 열처리 후 Grain Size가 커지는 현상 때문이고 이는 XRD를 통해 확인하였다. 면저항의 경우 열처리를 하였을 경우 급격히 감소하고 $100^{\circ}C$ 이후에는 일정하였다.

• Proceedings of the Korean Institute of Surface Engineering Conference
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• 2018.06a
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• pp.66.2-66.2
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• 2018

금속의 양극산화 공정(anodizing)은 전해질 내 금속에 인위적으로 전위를 가해 금속 표면에 얇은 산화막(oxide layer)을 형성하여 금속의 내식성, 내마모성을 증가시키는 공정이다. 타이타늄은 가볍고 단단하여 산업분야에 유용하게 사용되며 이와 같은 양극산화 공정을 통해 내식성, 내마모성을 크게 높일 수 있다. 본 연구에서는 항공기 부품용 타이타늄의 최적 양극산화 조건을 찾기 위해 전압의 파형, 전해액의 조성에 따라 양극산화 실험을 진행하였다. SEM, AFM, EDS, 분광측색계, 색채색차계 등을 이용하여 각 조건에 해당하는 타이타늄의 산화막($Tio_2$)의 두께, crack 형태, pore 형태, 균일도, 표면 조도, 내전압, 색 수치를 분석하였다. 그 결과 전압 DC 140 V, 주성분이 KOH $Na_3PO_4{\cdot}12H_2O$인 전해액으로 이루어진 양극산화 조건에서 가장 균일하고 색 재현성이 우수한 타이타늄의 산화막($Tio_2$)을 형성하였다.