• 한국물환경학회지
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• 제23권5호
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• pp.642-649
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• 2007

The effectiveness of add-on tertiary treatment processes for the polishing of the effluent of a biological nutrient removal (BNR) system from a modified $A^2/O$ process has been examined under the field condition with pilot-scale plants. The add-on treatment processes of 1) combined biofilm anoxic reactor and sand filtration, and 2) two-stage denitrification filter had been operated with various operating conditions. The experimental results indicated that two-stage denitrification filter could produced a better polished tertiary effluent. Filtration rate of $150m^3/m^2{\cdot}d$ for the 2-stage denitrifying filter could decrease the nitrate removal probably due to shorter detention time that caused insufficient reaction for denitrification. Two stage denitrification filter operated with M/N ratio of 3.0 and filtration rate of $100m^3/m^2{\cdot}d$ produced the tertiary effluent with nitrate and SS concentraitons of 2.8 mg/L and 2.3 mg/L, respectively. When the operating temperature reduced $30^{\circ}C$ to $18^{\circ}C$, $NO_3{^-}-N$ removal efficiency decreased from 73% to 68%.

• 한국광학회지
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• 제16권3호
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• pp.266-274
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• 2005

본 논문에서는 2차원 광결정 공진기의 결합을 통해 WDM시스템에 적합한 특성을 가지는 공진 필터를 설계하였다. 공진기간의 결합에 있어서 고려해야 할 요소를 시영역에서의 모드 결합이론(coupling modes in time)을 적용하여 이론적으로 분석하였으며, 전자회로 등가화를 이용하여 쉽게 그 요소를 결정할 수 있음을 보였다. 공진기 결합에 있어서 공진기 간의 간격에 따른 위상천이에 대해서 외부감쇄에 의한 Q-factor를 조정함으로써 보상할 수 있음을 확인하였고, 2차원 광결정 점결함 공진기를 이용하여 500GHz의 대역폭을 가지며 통과대역에서 0.5 dB 리플을 가지는 3차 Chebyshev 대역 통과 필터를 설계하였다.

• 대한전기학회:학술대회논문집
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• 대한전기학회 1997년도 하계학술대회 논문집 F
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• pp.2159-2161
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• 1997

This paper presents the investigations and the reduction methods for EMI in the Elevator(E/L) system. In the large capacity E/L. Power factor controlled IGBT converter is used, so that the conducted EMI level is mostly determined by a high frequency input current. We suggest the low cost EMI countermearsure for E/L system using by a LCL filter ed a low cost noise filter.

• 대한환경공학회지
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• 제27권5호
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• pp.499-506
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• 2005

본 연구에서는 2기의 부직포 여과막 생물반응조를 60분/60분의 포기/비포기 시간비에서 교대로 포기시키고 폐수를 주입시키면서 C/N비(COD/TKN)를 10에서 2까지 점감시켜 유입수의 C/N비가 유기물 및 질소 제거효율에 미치는 영향을 파악하였다. 실험에 사용된 폐수는 I시의 음식물 쓰레기 처리장에서 배출되는 침출수를 COD가 약 2,500 mg/L 정도 되도록 20배 희석시킨 것으로, C/N비는 염화암모늄($NH_4Cl$)을 첨가하여 조정하였다. 실험결과, $10{\sim}3$의 C/N비에서는 유출수의 COD 및 BOD 농도가 각각 $40{\sim}54\;mg/L$ 및 $1{\sim}4\;mg/L$로 나타났으며, 처리수의 SS농도는 항상 2.0 mg/L 미만으로 유지되었다. $10{\sim}5$의 C/N비에서는 96%의 총질소 제거효율를 보였으나 3 및 2.8의 C/N비에서는 총질소 제거효율이 각각 83% 및 81%로 낮아졌다. 2 및 2.6의 C/N비에서는 암모니아 독성에 의하여 처리수의 수질이 악화되었다. C/N비가 5에서 2.6으로 낮아질수록 질산화 미생물 분율이 10%에서 20%로 증가하였다. 알칼리도 소비량은 $10{\sim}5$의 C/N비에서는 $3.12{\sim}3.49\;g$ alkalinity/g T-N removed로 이론적인 값 3.57 g alkalinity/g T-N removed보다 낮았으나, 3 및 2.8의 C/N비에서는 4.63 및 4.87 g alkalinity/g T-N removed로 나타났다.

• 한국자동차공학회논문집
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• 제21권3호
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• pp.82-87
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• 2013

In this work, the 1L grade integrated metal DOC/DPF filter that can install in engine manifold position was developed to investigate the effect of platinum-coating amount of filter on the improvement of filter activation temperature and reduction of particulate matter (PM). This filter was installed in 2.9L CI engine which meets the EURO-4 emission regulation. Tests for PM reduction efficiency of filter were conducted under ND-13 mode with full-load test condition. It was revealed that the time to reach the activation temperature of metal filter ($280^{\circ}C$) was shorter as the amount of platinum-coating increased. This short activation time can be helpful for the reduction of CO and HC emissions during cold start condition. At the same time, PM reduced as the coating amount increased. The reduction percentage of $DOC_{40}$, $DOC_{20}$, and $DOC_0$ were 96.7% (2.34 mg/kW'h), 95.1% (3.47 mg/kW'h), and 94.5% (3.69 mg/kW'h) compared to previous result (71.4 mg/kW'h), respectively.

• 상하수도학회지
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• 제24권1호
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• pp.5-14
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• 2010

A pilot-scale biological aerated filter (BAF) was operated with an anaerobic, anoxic and oxic zone at $23{\pm}1^{\circ}C$. The influent sCOD and total nitrogen concentrations in the feedwater were approximately 250 mg/L and 35 mg N/L, respectively. sCOD removal at optimum hydraulic retention time (HRT) of 3 hours with recirculation rates of 100, 200 and 300% in the column was more than 96%. Total nitrogen removal was consistently above 80% for 4 and 6 hours HRT at 300% recirculation. For 3 hours HRT and 300% recirculation, total nitrogen removal was approximately 79%. Based on fitting results, the kinetic parameter values on nitrification and denitrification show that as recirculation rates increased, the rate of ammonia and nitrate transformation increased. The ammonium loading rates for maximum ammonium removed were 0.15 and 0.19 kg $NH_3$-N/$m^3$-day for 100% and 200% recirculation, respectively. The experimental results demonstrated that the BAF can be operated at an HRT of 3 hours with 200 - 300% recirculation rates with more than 96 % removal of sCOD and ammonium, and at least 75% removal of total nitrogen.

• 대한전기학회:학술대회논문집
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• 대한전기학회 2001년도 하계학술대회 논문집 B
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• pp.1064-1066
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• 2001

In this paper, the harmonic components generated by those two sources are analyzed separately based on the transfer function and shown as the closed form considering the switching frequency, speed of the control processor, gain of the controller, and the inductor and capacitor value of L-C filter. A design procedure is described with one flow chart and explained step by step.

• 한국세라믹학회지
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• 제28권9호
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• pp.675-682
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• 1991

Among many problems that need to be solved in the process of preparing multilayer chip LC filters, we studied the control of shrinkage in order to prevent the crack, warpage, and/or delamination which occurs at the interface between the inductance (L part) and the capacitance (C part). Shrinkage was controlled by compositions, powder size, calcining temperature and amount of organic binder. Capacitance sheet was prepared by mixing 65 wt% binder with the composition of 96 wt% TiO2 having an average particle size of 0.5 $\mu\textrm{m}$, 3 wt% CuO. After small amount of MnO2 and SiO2 added, it was calcined at 750$^{\circ}C$ for 2 hr. Inductance sheet was prepared by mixing 60 wt% binder with the composition of 49.5% mol% Fe2O3, 20.5 mol% ZnO, 20 mol% NiO and 10 mol% CuO which was calcined at 775$^{\circ}C$ for 2 hr. These sheets was laminated at 250 kg/$\textrm{cm}^2$, and cofired at 900$^{\circ}C$ for 2 hr to give rise to a multilayer chip LC filter without any warpage.

• 한국통신학회논문지
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• 제28권7C호
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• pp.688-695
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• 2003

본 논문에서는, 적응형 필터를 이용한 동기획득 시스템을 실제 환경에 효과적으로 사용하기 위해 두 가지 알고리즘을 제안한다. 첫째, 하나의 필터를 여러 개의 부 필터로 나누어 적응시키는 병렬 부필터 탐색 구조를 제시하여 실제 환경에서 요구되는 빠른 동기 획득 성능을 얻는다. 둘째, 적응 파라미터들을 수신 신호의 전력에 따라 조절해주는 파라미터 결정기법을 제안하여 이상적인 성능에서 큰 열화 없이 실제 환경에서 효율적으로 동작 가능하도록 한다. 제안된 시스템에 대해 통계적인 분석을 수행하고 모의 실험을 통해 평균 동기 획득 시간 성능을 검증한다. 병렬 부필터 탐색 구조를 적용한 시스템은 기존의 전체 필터 탐색 구조에 비해 16탭에서 1∼l.5dB, 64탭에서 5∼6dB의 성능 이득을 보이며, 제안된 파라미터 결정기법을 적용한 시스템은 16탭과 32탭에서 이상적인 성능에서 약 1∼2.5dB 정도의 열화만으로 실제 환경에서 효과적으로 동작함을 보여준다.

• Biotechnology and Bioprocess Engineering:BBE
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• 제5권6호
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• pp.456-459
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• 2000

A pilot scale experiment was performed for a year to develop a two-phase anaerobic process for piggery wastewater treatment (COD: 6,000mg/L, BOD: 4,000mg/L, SS: 500mg/L, pH 8.4, alkalinity 6,000mg/L). The acidogenic reactor had a total volume of 3㎥, and the methanogenic reactor, an anaerobic up-flow sludge filter, combining a filter and a sludge bed, was also of total volume 3㎥(1.5㎥ of upper packing material). Temperatures of the acidogenic and methanogenic reactors kept at 20$^{\circ}C$ and 35$^{\circ}C$, respectively. When the pH of the acidogenic reactor was controlled at 6.0-7.0 with HCl, the COD removal efficiency increased from 50 to 80% over a period of six months, and as a result, the COD of the final effluent fell in the range of 1,000-1,500 mg/L. BOD removal efficiency over the same period was above 90%, and 300 to 400 mg/L was maintained in the final effluent. The average SS in the final effluent was 270 mg/L. The methane production was 0.32㎥ CH$_4$/kg COD(sub)removed and methane content of the methanogenic reactor was high value at 80-90%. When the pH of the acidogenic reactor was not controlled over the final two months, the pH reached 8.2 and acid conversion decreased compared with that of pH controlled, while COD removal was similar to the pH controlled operation. Without pH control, the methane content in the gas from methanogenic reactor improved to 90%, compared to 80% with pH control.