• 청정기술
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• 제17권4호
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• pp.363-369
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• 2011

고농도의 암모니아성질소를 함유하는 폐수의 처리에 전기투석공정의 적용성이 실험적으로 평가되었다. 처리 성능은 전기투석공정의 운전인자 중 유입농도, 운전전압, 그리고 유속이 암모니아성질소의 제거효율에 미치는 영향으로 측정되었다. 한계전류밀도는 유입농도와 유입유속이 증가함에 따라 선형적으로 증가하였고, 유입농도에 따라 목표농도에 도달하는 시간은 직선적인 비례관계를 보였다. 상대적으로 큰 암모니아성질소의 이온당량전도도와 이온이동도로 인하여 유입유속의 증가는 제거속도를 지속적으로 증가시켰다. 또한 운전전압의 증가에 따라 제거속도는 증가하였다. 본 연구에 사용된 전기투석모듈에서 고농도의 암모니아성질소를 제거하는 운전조건으로 유입유속은 3.2 L/min, 운전전압은 한계전류밀도에 해당하는 전압의 80~90%가 추천된다.

• 청정기술
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• 제15권4호
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• pp.280-286
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• 2009

고농도의 질산성 질소를 함유하는 폐수의 처리에 전기투석법의 적용 가능성을 평가하기 위하여 전기투석 공정의 운전인자 중 유입농도, 운전전압, 그리고 유속이 질산성 질소의 제거효율에 미치는 영향을 실험적으로 평가하였다. 한계전류밀도는 유입농도와 유입유속이 증가함에 따라 선형적으로 증가하였다. 유입농도와 목표농도에 도달하는 시간은 직선적으로 비례관계를 보였고, 농축액의 초기농도가 제거속도에 미치는 영향은 거의 없었다. 저속에서 유입유속의 증가는 제거속도를 증가시켰지만, 일정속도 이상에서는 제거속도에 미치는 영향이 미미하였다. 운전전압의 증가에 따라 제거속도는 증가하였지만 그 증가속도는 점차 저하되었다. 본 연구에 사용된 전기투석모듈에서 고농도의 질산성 질소를 제거하는 최적 운전조건으로 유입유속 1.6 L/min, 한계전류밀도의 80~90%의 해당하는 운전전압이 권장된다.

• 마이크로전자및패키징학회지
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• 제18권1호
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• pp.29-33
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• 2011

전류밀도는 전기도급법에서 생산성과 직접적인 연관이 있고, 생산성의 증가를 위해선 고전류밀도가 필요하다. 회전전극(RDE)의 회전 속도를 증가시키면 고유속을 얻을 수 있다. 유속 조절을 위해 회전전극과 원통형 회전 전극을 사용하였고, 전압과 전류의 관계를 알아보기 위해 정전류, 정전압 실험과 linear sweep voltammetry 실시하였다. 회전 전극의 회전 속도가 400 rpm이상 조건에서, 수소가 발생하지 않고 1000 A/$m^2$이상의 최대전류멸도가 가능하였다. $25^{\circ}C$와 $62^{\circ}C$ 조건에서 구리의 확산계수는 각각 $5.5{\times}10^6\;cm^2\;s^{-1}$와 $10.5{\times}10^6\;cm^2\;s^{-1}$로 계산되었다. 수소가 발생하지 않으면서 안정적으로 구리를 전착할 수 있는 조건은 -0.05 V (vs Ag/AgCl)이었다. 첨가제인 glue와 thiourea-를 넣음으로써 구리의 침상성장을 막을 수 있었다. 표면 거칠기는 UV-Vis Spectrophotometer를 아용하여 분석되었다. 600 nm 영역에서 반사도는 측정 되었고 표면 거철기가 개선될수록 표면 반사도가 증가하였다.

• 한국해양공학회지
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• 제25권2호
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• pp.85-91
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• 2011

Many protection methods such as surface coating, electric protection, or other methods have been applied to the numerous steel structures widely used in continental and marine areas to control their corrosion, which is done from an economic point of view. Most of these steel structures are primarily protected by coating methods. However, some steel piles under seawater are protected by the electric protection method, that is, either using an impressed current or a sacrificial anode method. Furthermore, environmental contamination may cause a severely corrosive environment, which, in turn, causes the accelerated corrosion of steel structures. Subsequently, coated steel structures could deteriorate more rapidly than the designed lifetime because of the acid rain caused by air pollution, etc. Therefore, a coating of marine paint exposed to seawater, that is, underwater hardening painting, is increasingly required to be fast drying as well as highly corrosion resistant. In this study, five types of underwater hardening paints were prepared with different resin series and additives. Their corrosion and water resistances were investigated using electrochemical methods such as corrosion potential, polarization curves, impedance and cyclic voltammogram measurements, etc. Even though it is generally accepted that the corrosion resistance of bare steel tends to increase with a shift of the corrosion potential in the noble direction, the corrosion resistance of a sample with a coating exhibited a relatively better tendency when it had a lower corrosion potential in this study. The corrosion current density was also decreased with a decrease in the diffusion limiting current density, which may mean that there is some relationship between corrosion and water resistance. The S sample of the ceramic resin series showed the relatively best corrosion and water resistance among those of samples, while the worst corrosion and water resistance were observed for the R sample of the epoxy resin series. The corrosion and water resistance of those samples tended to deteriorate with an increase in the immersion days, and their corrosion and water resistances were considered to be apparently improved by the types of resin and additives.

• Korean Membrane Journal
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• 제7권1호
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• pp.28-33
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• 2005

The feasibility of producing sulfuric acid and ammonia water from ammonium sulfate was investigated by an integrated process including ammonia stripping (AS) and electrodialysis with bipolar membrane (EDBM). It was suggested that the production of sulfuric acid using ammonia stripping-electrodialysis with bipolar membrane (ASEDBM) was effective in obtaining high concentration of sulfuric acid compared with EDBM alone. AS was carried out over pH 11 and within the range of temperatures, $20^{\circ}C{\~}60^{\circ}C$. Sodium sulfate obtained using AS was used as the feed solution of EDBM. The recovery of ammonia increased from $40\%$ to $80\%$ at $60^{\circ}C$ due to the increased mobility of ammonium ion. A pilot-scale EDBM system, which is composed of two compartments and 10 cell pairs with an effective membrane area of $200 cm^2$ per cell, was used for the recovery of sulfuric acid. The performance was examined in the range of 0.1 M${\~}$1.0 M concentration of concentrate compartment and of $25 mA/cm^2{\~}62.5 mA/cm^2$ of current density. The maximum current efficiency of $64.9\%$ was obtained at 0.1 M sulfuric acid because the diffusion rate at the anion exchange membrane decreased as the sulfuric acid of the concentrate compartment decreased. It was possible to obtain the 2.5 M of sulfuric acid in the $62.5 mA/cm^2$ with a power consumption of 13.0 kWh/ton, while the concentration of sulfuric acid was proportional to the current density below the limiting current density (LCD). Thus, the integrating process of AS-EDBM enables to recover sulfuric acid from the wastewaters containing ammonium sulfate.

• 한국수소및신에너지학회논문집
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• 제20권6호
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• pp.479-484
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• 2009

The effect of anode gas channel height on gas diffusion and cell performance in a 100 $cm^2$ class molten carbonate single cell is investigated. Single cell separators with three different channel height are used. The effect of the gas channel height on the distribution of the reactive gas concentration is evaluated by the two-dimensional concentration diffusion equation. The overpotential caused by concentration drop with different channel height is estimated by the voltage decay related to diffusion of reactants, well known as concentration polarization, using limiting current density. The estimation could have the possibility to identify the reactant mass transfer polarization in the complicate factors of the overall electrodes.

• Corrosion Science and Technology
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• 제2권1호
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• pp.41-46
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• 2003

Flow-Accelerated Corrosion behavior concerning both activation and mass transfer process of SA106 Gr.C steel was studied using rotating cylinder electrode in room temperature alkaline solution by DC and AC electrochemical techniques. Passive film was tanned from pH 9.8 by step oxidation of ferrous product into hydroxyl compound. Corrosion potential shifted slightly upward with rotating velocity through the diffusion of cathodic species. Corrosion current density increased with rotating velocity in pH 6.98, while it soon saturated from 1000 rpm at above pH 9.8. On the other hand the limiting current increased with rotating speed regardless of pH values. It seems that activation process, which represents formation of passive film on the bare metal surface, controls the entire corrosion kinetics

• 대한전기학회:학술대회논문집
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• 대한전기학회 2006년도 학술대회 논문집 전문대학교육위원
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• pp.208-211
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• 2006

We have analyzed operating characteristics of hybrid-type superconducting fault current limiter (SFCL) according to the parallel connection of secondary windings with $YBa_{2}Cu_{3}O_{7}$ (YBCO) films. The turn ratio between the primary and secondary windings of each reactor was 63:21. Hybrid-type SFCL using a transformer with parallel reactors could reduce the unbalanced quench caused by differences of the critical current density between YBCO films. We found that hybrid-type SFCL having parallel connection induced simultaneous quench between the superconducting elements. The quench-starting point at this time was almost same. When the applied voltage was 200V, the limiting current in the hybrid-type SFCL with a serial connection was lowered to 34 percent than that in the SFCL with a parallel connection. In the meantime, when the voltage generated in the superconducting elements was the same, the current value in the parallel connection was 60 percent less than in the serial connection. The voltage generated in the primary winding also showed the similar behavior. In conclusion, we found that the fault current was limited more effectively in the SFCL with the serial connection but the power burden of the superconducting elements was reduced in the parallel connection.

• KIEE International Transaction on Electrical Machinery and Energy Conversion Systems
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• 제3B권4호
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• pp.165-172
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• 2003

Low voltage circuit breakers are widely used in power distribution systems to interrupt fault current rapidly and to assure the reliability of the power supply. This paper is focused on understanding the interrupting capability, more specifically of the contacts and the arc runner, based on the shape of the contact system in the current molded case circuit breaker (hereafter MCCB). Moreover, in order to improve the interrupting capability of the circuit breaker, the estimation and analysis of the interrupting capability, based on the 3-D magnetic flux analysis, were developed. Furthermore, this paper also presents results of the estimation and analysis of the interrupting capability when applied to different model breakers. In addition, this paper analyzes the efficiency of the interrupting tests by forming false current paths consisting of a three-division cascade arc runner in the contact system. With regards to the interrupting test, there is a need to assure that the optimum design required to analyze the electromagnetic forces of the contact system generated by the current and flux density be present. Based on the results of this study, this paper presents both computational analysis and test results for the newly developed MCCB 460V/225A/50㎄ contact system.

• 한국전기전자재료학회논문지
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• 제29권5호
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• pp.298-302
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• 2016

In this work, $LiMn_2O_4$ and $LiNi_{1/3}Mn_{1/3}Co_{1/3}O_2$ cathode materials are mixed by some specific ratios to enhance the practical capacity, energy density and cycle performance of battery. At present, the most used cathode material in lithium ion batteries for EVs is spinel structure-type $LiMn_2O_4$. $LiMn_2O_4$ has advantages of high average voltage, excellent safety, environmental friendliness, and low cost. However, due to the low rechargeable capacity (120 mAh/g), it can not meet the requirement of high energy density for the EVs, resulting in limiting its development. The battery of $LiMn_2O_4-LiNi_{1/3}Mn_{1/3}Co_{1/3}O_2$ (50:50 wt%) mixed cathode delivers a energy density of 483.5 mWh/g at a current rate of 1.0 C. The accumulated capacity from $1^{st}$ to 150th cycles was 18.1 Ah/g when the battery is cycled at a current rate of 1.0 C in voltage range of 3.2~4.3 V.