• 제목/요약/키워드: Electrode Consumption

검색결과 196건 처리시간 0.029초

Electrodeposition of Silicon in Ionic Liquid of [bmpy]$Tf_2N$

  • 박제식;이철경
    • 한국재료학회:학술대회논문집
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    • 한국재료학회 2011년도 추계학술발표대회
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    • pp.30.1-30.1
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    • 2011
  • Silicon is one of useful materials in various industry such as semiconductor, solar cell, and secondary battery. The metallic silicon produces generally melting process for ingot type or chemical vapor deposition (CVD) for thin film type. However, these methods have disadvantages of high cost, complicated process, and consumption of much energy. Electrodeposition has been known as a powerful synthesis method for obtaining metallic species by relatively simple operation with current and voltage control. Unfortunately, the electrodeposition of the silicon is impossible in aqueous electrolyte solution due to its low oxidation-reduction equilibrium potential. Ionic liquids are simply defined as ionic melts with a melting point below $100^{\circ}C$. Characteristics of the ionic liquids are high ionic conductivities, low vapour pressures, chemical stability, and wide electrochemical windows. The ionic liquids enable the electrochemically active elements, such as silicon, titanium, and aluminum, to be reduced to their metallic states without vigorous hydrogen gas evolution. In this study, the electrodeposion of silicon has been investigated in ionic liquid of 1-butyl-3-methylpyrolidinium bis (trifluoromethylsulfonyl) imide ([bmpy]$Tf_2N$) saturated with $SiCl_4$ at room temperature. Also, the effect of electrode materials on the electrodeposition and morphological characteristics of the silicon electrodeposited were analyzed The silicon electrodeposited on gold substrate was composed of the metallic Si with single crystalline size between 100~200nm. The silicon content by XPS analysis was detected in 31.3 wt% and the others were oxygen, gold, and carbon. The oxygen was detected much in edge area of th electrode due to $SiO_2$ from a partial oxidation of the metallic Si.

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측면 연마된 광섬유 브래그 격자를 이용한 연속적인 광학적 RF 실시간 지연 (Continuous Photonic RF True-time Delay Using a Side-polished Fiber Bragg Grating with Heating Electrode)

  • 채호동;김도환;김형준;이상신;김효겸;이규호;김광택
    • 한국광학회지
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    • 제15권6호
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    • pp.591-596
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    • 2004
  • 본 논문에서는 히팅용 전극이 코팅된 측면 연마된 광섬유 브래그 격자를 이용한 광학적 RF 실시간 지연을 제안하고 제작하였다. 이 소자는 기계적인 움직임이나 진동 없이 전압에 의하여 연속적으로 정밀하게 시간 지연값을 제어할 수 있는 특징을 갖는다. 전극에 인가되는 전압에 의해 유발되는 열광학효과를 통하여 광섬유 격자로부터 반사되는 광신호의 반사 위치를 변화시킴으로써 광신호에 변조용 신호로 실려서 전달되는 RF 신호의 시간 지연을 조절할 수 있다. 측정된 최대 시간 지연은 소비 전력이 280 mW일 때 약100 ps이다.

1,2-Dichloroethane 내 백금 전극에서의 dicarboximide 레이저 염료에 대한 convolutive 순환 전압-전류법 연구 (Convolutive Cyclic Voltammetry Investigation of Dicarboximide Laser Dye at a Platinum Electrode in 1,2-Dichloroethane)

  • Al-Bishri, Hassan M.;El-Mossalamy, E.H.;El-Hallag, Ibrahim;El-Daly, Samy
    • 대한화학회지
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    • 제55권2호
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    • pp.169-176
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    • 2011
  • N,N-bis(2,5-di-tert-butylphenyl) - 3,4,9,10 perylenebis(dicarboximide) 레이저 염료에 대한 전기화학적 연구가 0.1 M tetrabutyl ammonium perchlorate(TBAP)/1,2 dichloroethane($CH_2Cl-CH_2Cl$) 용액내에서 백금 전극을 이용하여 순환 전압-전류법 및 디지털 시뮬레이션 기술과 결합된 convolution-deconvolution 전압-전류법으로 수행되었다. 연구에 사용된 염료는 두개의 전자를 순차적으로 소모하며 radiacal anion과 dianion으로(EE 메커니즘) 환원되었다. 전위를 positive scan으로 전환하면, 이 화합물은 두 개의 전자를 잃고 산화된 뒤 빠른 응집 과정($EC_1EC_2$ 메커니즘)을 거치게 된다. 이 화합물의 전극 반응 경로, 화학 및 전기화학적 파라미터는 순환 전압-전류법과 convolutive 전압-전류법을 이용하여 측정되었다. 이렇게 구한 전기화학적 파라미터는 디지털 시뮬레이션 방법을 통하여 검증되었다.

Ca(OH)2촉매를 이용한 플라즈마 반응에 의한 황산화물(유해가스)의 제거에 관한 연구 (A study of decomposition of sulfur oxides(harmful gas) using calcium dihydroxide catalyst by plasma reactions)

  • 김다영;황명환;우인성
    • 대한안전경영과학회지
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    • 제16권2호
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    • pp.237-246
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    • 2014
  • Researches on the elimination of sulfur and nitrogen oxides with catalysts and absorbents reported many problems related with elimination efficiency and complex devices. In this study, decomposition efficiency of harmful gases was investigated. It was found that the efficiency rate can be increased by moving the harmful gases together with SPCP reactor and the catalysis reactor. Calcium hydroxide($Ca(OH)_2$), CaO, and $TiO_2$ were used as catalysts. Harmful air polluting gases such as $SO_2$ were measured for the analysis of decomposition efficiency, power consumption, and voltage according to changes to the process variables including frequency, concentration, electrode material, thickness of electrode, number of electrode winding, and additives to obtain optimal process conditions and the highest decomposition efficiency. The standard sample was sulfur oxide($SO_2$). Harmful gases were eliminated by moving them through the plasma generated in the SPCP reactor and the $Ca(OH)_2$ catalysis reactor. The elimination rate and products were analyzed with the gas analyzer (Ecom-AC,Germany), FT-IR(Nicolet, Magna-IR560), and GC-(Shimazu). The results of the experiment conducted to decompose and eliminate the harmful gas $SO_2$ with the $Ca(OH)_2$ catalysis reactor and SPCP reactor show 96% decomposition efficiency at the frequency of 10 kHz. The conductivity of the standard gas increased at the frequencies higher than 20 kHz. There was a partial flow of current along the surface. As a result, the decomposition efficiency decreased. The decomposition efficiency of harmful gas $SO_2$ by the $Ca(OH)_2$ catalysis reactor and SPCP reactor was 96.0% under 300 ppm concentration, 10 kHz frequency, and decomposition power of 20 W. It was 4% higher than the application of the SPCP reactor alone. The highest decomposition efficiency, 98.0% was achieved at the concentration of 100 ppm.

전극 간격에 따른 전기화학적 처리를 통한 폐수처리에 관한 연구 (A Study on Wastewater Treatment by Electrochemical Treatment with Various Electrode Interval)

  • 송주영
    • 한국응용과학기술학회지
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    • 제36권2호
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    • pp.417-423
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    • 2019
  • 전기화학적 처리를 통해 합성폐수 내의 질산성 질소, 인을 제거하는 새로운 폐수처리 공정 시스템 개발을 위한 연구를 수행하였다. 전류밀도에 따른 제거율은 전류밀도가 높아질수록 질산성 질소의 높은 제거효율을 얻었고, 전극 스위칭시간에 따른 $NO_3^-$ 제거율은 스위칭 간격이 1 min일 때 높은 질산성 질소 제거효율을 얻었다. 전류밀도에 따른 총인 제거율은 전류밀도와 간격의 변화에 크게 영향을 받지 않으면서 90%이상 처리되는 것으로 나타났고, 스위칭시간(1 min간격)의 증가에 따른 총인 제거율은 증가한 것으로 나타났다. 반면 COD의 경우는 전기화학적 처리를 통해서는 처리되지 않는 것으로 나타났으며 오히려 전극이 용출되면서 증가하는 결과를 얻었다. 또한, 전극의 소모율은 스위칭 간격이 짧을수록 적은 것으로 나타났다. 최종적으로 전기화학적 처리(전류밀도 $50mA/cm^2$, 스위칭 간격 1 min, 유량 540 mL/min)를 통해 질소 98.1%, 인 90% 이상의 제거 효율을 얻을 수 있었다.

고전압 전극 두께와 집진판 간격에 따른 전기집진기의 미세먼지 집진효율 및 오존발생 특성 (Characteristics of particulate matter collection efficiency and ozone emission rate of an electrostatic precipitator by thickness of high-voltage electrode and distance of collection plates)

  • 이재인;우상희;김종범;이승복;배귀남
    • 한국입자에어로졸학회지
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    • 제14권4호
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    • pp.171-180
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    • 2018
  • To optimize the shape of the electrostatic precipitator for the removal of particulate matter in subway environments, the wind-tunnel experiments were carried out to characterize collection efficiency and ozone emission rate. As a standardized parameter, power consumption divided by the square of flow velocity, was increased, the $PM_{10}$ collection efficiency increased. If the standardized parameter is higher than 1.0 due to high power consumption or low flow velocity, increase in thickness of electrodes from 1 to 2 mm, or increase in distance of collection plates from 5 to 10 cm did not change the $PM_{10}$ collection efficiency much. Increase in thickness of high-voltage electrodes, however, can cause decrease in $PM_{10}$ collection efficiency by 28% for low power consumption and high flow velocity. The ozone emission rate decreased as distance of collection plates became wider, because the ozone emission rate per unit channel was constant, and the number of collection channels decreased as the distance of collection plates increased. When the distance of collection plates was narrow, the ozone emission rate increased with the increase of the thickness of electrodes, but the difference was negligible when the distance of collection plates was wide. It was found that the electrostatic precipitator having a thin high-voltage electrodes and a narrow distance of collection plates is advantageous. However, to increase the thickness of high-voltage electrodes, or to increase the distance of collection plates is needed, it is necessary to increase the applied voltage or reduce the flow rate to compensate reduction of the collection efficiency.

Characteristics of Carbon Nanotube FED

  • Uemura, Sashiro;Yotani, Junko;Nagasako, Takeshi;Kurachi, Hiroyuki;Yamada, Hiromu;Ezaki, Tomotaka;Maesoba, Tsuyoshi;Nakao, Takehiro;Ito, Masaaki;Saito, Yahachi;Yumura, Motoo
    • 한국정보디스플레이학회:학술대회논문집
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    • 한국정보디스플레이학회 2004년도 Asia Display / IMID 04
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    • pp.860-865
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    • 2004
  • Field emission display(FED) using carbon nanotubes (CNT) as field emitters is expected to large-area panels with high luminance and low power consumption. In order to perform the uniform luminance with low driving voltage, we introduced a new electrode to apply higher electric potential over the CNT cathode in 2003.[1] In the study, we described the luminance uniformity of the panel and the improvement of emission uniformity by increasing the emission-site density. The luminance uniformity of the several ideal dots which were selected over the display area in the panel was 2.8%. [2] The CNT cathode was irradiated by excimer-laser, which was effective to improve emission uniformity and lower driving voltage. A prototype of CNT-FED character display was performed for middle size message displays. The prototype panel had 48 x 480-dots and the resolution was 1-mm. The panel realized high luminance at low power consumption. It will be important characteristics for legible and ubiquitous displays. [3]

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플라즈마 방전에 의한 $SO_x, NO_x$의 분해 (Decomposition of $SO_x, NO_x$ by Plasma Discharge)

  • 우인성;강현춘
    • 한국안전학회지
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    • 제14권1호
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    • pp.73-77
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    • 1999
  • In this study, $SO_2$ and $NO_2$ reduction have been investigated by using coil type plasma reactor. The experiments have been carried out changing discharge power, gas flow rate frequency and electrode style to obtain the decomposition rate. Decomposition rates of $SO_2$ and $NO_2$ were obtained 20~98% at gas flow rate 100ml/min~1,000ml/min and discharge power 5~25w respectively. The energy efficiency is very good at the high frequency power. The decomposition rate of $SO_2$ for 5kHz power supply is only 90%, but for 10kHz power supply is very high, more than 98% for 15w. The decomposition rate is increasing according to the residence time or the power consumption of the discharge. About 15W discharge power for 17$cm^2$ reactor is necessary to obtain the decomposition rate of $SO_2$ and $NO_2$ of more than 85% or 98%. From these experiments, the consumption power of the decomposition rate of 98% in 300ppm $NO_2$ gas in nitrogen gas proved to be 18W and 300ppm $SO_2$ gas to be 15w.

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질소 제거를 위한 전기화학적 처리 공정의 최적 운전조건 및 폐수 성상에 따른 영향에 관한 연구 (A Study on the Optimum Operating Conditions and Effects of Wastewater Characteristics in Electrochemical Nitrogen Removal Process)

  • 심주현;강세한;서형준;송수성
    • 대한환경공학회지
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    • 제31권1호
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    • pp.29-34
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    • 2009
  • 표면처리폐수 내 질산성 질소를 제거하기 위한 전기화학적 처리공정에서 전극간격, 환원제, 1단 처리수 반송, 타 물질과 동시 처리 등 네 가지 조건을 변화시키며 실험을 진행하였다. 실험 결과, 전극간격은 10 mm일 때 질산성 질소 제거효율이 높았으며 10 mm 보다 전극간격이 좁아질 경우 농도분극 현상의 증가로 인해 제거효율이 감소하며 10 mm 보다 넓어질 경우 전압이 상승하여 에너지 소모가 증가하였다. 환원제 영향에 대한 실험 결과, 질산성 질소가 환원되는 과정에서 수소가 소모되기 때문에 수소이온 농도가 높은 산성조건에서 더 원활한 환원반응이 이루어졌으며 아연을 1.2배 투입할 경우 질산성 질소와의 반응량이 증가하여 질산성 질소 제거효율이 증가하였다. 1단 처리수를 반송할 경우 난류가 형성되어 환원전극에 부착된 아연이 탈착되어 재 이용되고 내부 확산이 증가하여 농도분극현상이 감소함으로 인해 질산성 질소 제거효율이 증가하였으며 아연 투입량 감소 효과가 나타났다. 암모니아성 질소는 질산성 질소 제거에 영향을 미치지 않았고 폐수 내 염소성분이 충분할 경우 질산성 질소와 동시 처리에도 문제가 없는 것으로 나타났다. 중금속은 환원되는 과정에서 전자를 소모하여 질산성 질소 제거효율은 감소하지만 전류밀도 증가나 본 장치의 전단을 중금속 제거용으로 사용하는 방법 등으로 해결이 가능할 것으로 생각한다.

마이크로 가스센서의 저전력 구동을 위한 마이크로 플랫폼의 제작과 특성 (Fabrication and Characteristics of Micro Platform for Micro Gas Sensor with Low Power Consumption)

  • 장웅진;박광범;김인호;박순섭;박효덕;이인규;박준식
    • 센서학회지
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    • 제20권5호
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    • pp.317-321
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    • 2011
  • A Micro platform for micro gas sensor consisted of micro heater, insulator, and sensing electrode on 2 ${\mu}m$ thick $SiN_x$ membrane. Three types of micro platforms were designed and fabricated with membrane sizes. Total size of micro platform was 2.6 mm by 2.6 mm. Measured power consumptions were 28 mW, 28 mW, and 32.5 mW for Type 1, Type 2, and Type 3. At this moment, temperatures of membranes on the platforms were $295^{\circ}C$, $297^{\circ}C$, and $296^{\circ}C$, respectively. Fabricated micro platform considered appropriate to apply for low power consumption micro gas sensor. Micro gas sensors were prepared by the sequence that $SnO_2$ nanopowder pastes were dropped on membrane of Type 1 platforms, dried in oven, heat-treated with micro heaters in platforms. One of the micro gas sensors was tested for gas response to 1157 ppm, 578 ppm, and 231 ppm of methane and 1.68 ppm, 0.84 ppm, and 0.42 ppm of $NO_2$.