• 한국원자력학회:학술대회논문집
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• 한국원자력학회 2005년도 추계학술발표회
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• pp.1007-1008
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• 2005

• 유기물자원화
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• 제23권1호
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• pp.45-51
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• 2015

본 연구에서는 비귀금속 촉매인 iron(II) phthalocyanine (FePc)와 cobalt tetramethoxyphenylporphyrin(CoTMPP)를 환원전극촉매로 이용하여 미생물연료전지의 연속운전을 진행하였다. 연속운전은 유기물 부하 (0.5~3 g COD/L/d)와 HRT (0.25~1 day)의 조건을 달리 운전하여 미생물연료전지의 성능을 평가하였다. 미생물연료전지의 전력밀도는 환원전극의 성능에 크게 영향을 받았으며, 최대전력밀도는 $3.3W/m^3$로 백금을 사용한 미생물연료전지에서 나타났다. 하지만, HRT의 조건을 달리 한 실험에서 FePc를 사용한 미생물연료전지가 백금을 사용한 미생물연료전지와 유사한 성능을 나타냈으며, 연속운전에서 백금 촉매를 대체할 수 있는 적합한 물질로 나타났다. 반면에 CoTMPP를 사용한 미생물연료전지는 연속운전에서 내부 저항의 급격한 증가로 전력밀도가 급격히 감소하였다.

• 유기물자원화
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• 제15권2호
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• pp.136-146
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• 2007

상향류 혐기성 블랭킷 반응조를 이용한 매립지 침출수 처리시 입상슬러지 첨가 유무에 상관없이 성공적인 처리가 가능하였다. 입상슬러지의 첨가는 초기 운전기간를 현저히 단축할 수 있었다. 수리학적 체류시간 1일과 $4-8kgCOD/m^3.d$ 의 유기물 부하율에서 Control 반응조와 Granule 반응조의 COD 제거율은 90% 이상을 유지하였다. 실험기간 동안 입상슬러지 첨가 유무에 상관없이 슬러지 표면과 반응조 벽면에 무기 침전물이 축적되었다. 비메탄 활성도는 미생물의 기질에 대한 적응도와 유기물 부하량이 증가함에 따라 증가하였다. Granule 반응조의 최대 비메탄 활성도의 값은 $0.57gCOD/g{\cdot}VSS{\cdot}.d$로 나타났다. 비록 본 연구에서는 과도한 무기물 축적으로 인한 비메탄 활성도의 저감은 발생하지 않았으나 무기물의 제거를 위하여 유입수의 전처리 공정이 필요할 것으로 판단된다.

• Environmental Engineering Research
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• 제25권1호
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• pp.114-122
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• 2020

This study was aimed at using the Central Composite Design (CCD) and Box-Behnken Design (BBD) to compare the efficiency and to elucidate the main interacting parameters in the upflow anaerobic sludge blanket (UASB) reactor, namely: Organic Loading Rate (OLR), Hydraulic Retention Times (HRT) and pH at a constant temperature of 35℃. Optimum HRT (15 h), OLR (3.5 kg.m^-3.d^-1) and pH (7) resulted in biogas production of 5,800 mL/d and COD removal of 80.8%. BBD produced a higher desirability efficiency of 94% as compared to the CCD which was 92%. The regression quadratic models developed with high R² values of 0.961 and 0.978 for both CCD and BBD, respectively, demonstrated that the interaction models could be used to pilot the design space. BBD model developed was more reliable with a higher prediction of biogas production (5,955.4 ± 225.3 mL/d) and COD removal (81.5 ± 1.014%), much close to the experimental results at a 95% confidence level. CCD model predictions was greater in terms of COD removal (82.6 ± 1.06% > 80.8%) and biogas production (4,636.31 mL/d ± 439.81 < 5,800 mL/d) which was less than the experimental results. Therefore, RSM can be adapted for optimizing various wastewater treatment processes.

• 유기물자원화
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• 제14권4호
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• pp.151-160
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• 2006

침출수의 혐기성 처리시 오염물질 거동과 미생물 특성을 평가하기 위하여 10개월간 실험을 수행하였다. 상향류 혐기성 슬러지 블랭킷 (UASB) 반응조의 경우 최대 유기물 부하 $20kgCOD/m^3.d$까지 약 90%의 COD 제거율을 나타내었다. 높은 유기물 부하 ($18-20kgCOD/m^3.d$)에서는 프로피온산의 농도가 상대적으로 증가하여 프로피온산의 초산으로의 전환이 율속단계로 나타났다. UASB 반응조를 이용한 침출수 처리는 높은 유기물 제거능에도 불구하고 입상슬러지와 반응조 내부 등의 무기물 축적으로 인한 운전상의 문제가 발생하였다. 입상슬러지 내 주된 무기물의 성분은 칼슘화합물로 나타났다. 본 연구에서는 비메탄 활성도의 급격한 감소는 발생되지 않았으나 무기물 축적으로 인한 운전상의 문제를 저감하기 위해서는 무기물 제거를 위한 전처리 공정의 도입이 필요할 것으로 판단된다.

• 상하수도학회지
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• 제27권1호
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• pp.21-29
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• 2013

Present study was conducted to evaluate the performance of Anaerobic Hybrid Reactor (AHR) combined with two types of anaerobic attached growth reactors at mesophilic temperature ($37^{\circ}C$). The reactor was operated at the influent substrate condition of 19,400 mg/L soluble chemical oxygen demand (sCOD). The organic loading rate (OLR) and flow rate were varied in the range of $9.5{\sim}22.5kg/m^3$. day and 10.6 ~ 26.0 L/day respectively since start-up was done. The COD removal efficiency of 93 % was measured at the OLR of $14kg/m^3$. day in AHR. However a reduction in removal efficiency to as low as 85 % could have been related to a combined effect of high concentration suspended solids (SS) concentration over 3,800 mg/L. On the other hand the total COD removal efficiencies were measured to be 96.3 % and 96.2 % for AHR+APF and AHR+ADF respectively. The pH of the POME was adjusted to neutral range by using sodium bicarbonate at the initial stages of the reactor feed, later stages pH adjustment was not required as the pH was maintained in the desired neutral range due to self-buffering capacity of the reactor. The reactor proved to be economically acceptable and operationally stable. The biogas was measured to have $CH_4$ and $CO_2$ with a ratio of 35:65, and methane gas production rate was estimated to be $0.17{\sim}10.269L\;CH_4/g\;COD_{removed}$.

• 상하수도학회지
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• 제12권4호
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• pp.86-96
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• 1998

In this study, an intermittently aerated activated sludge process, modified process from conventional activated sludge process, was developed to treat high strength swine wastewater, which has been blamed as major pollutant for stream pollution. Therefore, the optimum cycle for oxic and anoxic period, SRT, and OLR were studied as design parameters. The effects of different time interval for oxic and anoxic period on nitrification and denitrification were examined by operating two reactors with 60/60min and 60/90min as oxic/anoxic period. Although the reactor with 60/60min showed complete denitrification of $NO_x-N$ generated during oxic period, the reactor with 60/90min showed incomplete nitrification due to the inactivity of nitrifier by accumulated $NH_3-N$ toxicity during anoxic period. Therefore, it is recommended to operate same interval for oxic and anoxic period. In order to determine the optimum cycle for oxic/anoxic period, four different reactors with 30/30, 60/60, 90/90 and 120/120min were examined. The reactor operation with 90/90min was optimum to get the most stable results in this study. However, the optimum cycle for oxic and anoxic period should be changed with characteristics of influent wastewater and operating conditions. According to lie operation results of three reactors with SRT of 15, 20 and 30days. The reactor with 2Odays SRT showed best removal efficiency of T-N. The optimum OLR would be $2.5Kg\;COD/m^3/day$ which showed the most stable nitrification and denitrification. Since characteristics of influent wastewater in the real system has a severe fluctuation, so it is very difficult to determine each interval for oxic and anoxic period. Therefore, ORP curves, describing the change of oxidation/reduction potential in reactor, can be used as a control parameter for automatic control of oxic and anoxic period. In other words, bending point (Nitrate Knee) of ORP curve during anoxic period could be used as a starting point of oxic period.

• Journal of Welding and Joining
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• 제13권2호
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• pp.60-67
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• 1995

The factors affecting on the fatigue strength of spot_welded specimens have been studied. The influence of initial overloads on the fatigue life of spot_welded tensile_shear specimens is investigated by considering fatigue crack initiation and crack propagation. The change of strain range and the influence of initial overload are correlated on the basis ol strain results. The results of this study are as follows. l) The initial absolute strain range decreased with initial overloads increase, and absolute strain range decreased before transformation of waveform of strain, but increased after transformation of waveform of strain. 2) In case of subsequent point of inflection of offset strain, the increment of this strain decreased with initial overload increase. 3) As initial overloads increase, the deformation behavior of spot welded parts is restricted after overloading.

• 한국에너지공학회:학술대회논문집
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• 한국에너지공학회 1997년도 추계학술발표회 논문집
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• pp.38-43
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• 1997

중수형 원전과 경수형 원전의 핵연료 교체방식, 핵연료 특성, 원전에 설치된 사찰장비 등의 안전조치 특성 관점에서 비교 분석되었는 바, 이는 중수형과 경수형 원전에 투입되는 사찰량의 차이가 10배 이상 투입되는 근본적인 원인으로 파악되었다. 특히 사찰량의 비교를 위하여 사찰시 수행되는 단위활동별로 소요시간을 측정하여 향후 국가 계량관리 검사 수행시 사찰량을 절감할 수 있는 요소들을 정확히 파악하여 사찰량 절감방안을 도출하는데 기여할 것으로 기대된다. 또한 우리나라가 보유하고 있는 원자력발전소 유형인 중수형과 경수형 원전에 대한 안전조치 측면에서의 특성을 상호 비교함으로써 안전조치 접근방법에 정확한 이해와 국가 계량관리 검사절차서의 개선에 기여할 것으로 기대된다.

• 한국물환경학회지
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• 제28권6호
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• pp.781-785
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• 2012

This study was carried out to treat the thermal elutriated acids of piggery wastewater using UASB process. The UASB reactor was operated at an organic loading rate (OLR) of $7.4\;kgCOD/m^3-day$ (6.5 ~ 9.0). During the start-up period, the low COD removal efficiency (20%) was caused by shock loading and instability in the reactor. It was mainly due to the high concentration amounts of ammonia nitrogen, which caused inhibitory and toxic effects to toward the anaerobic bacteria. In steady state, the UASB reactor showed a SCOD removal efficiency of 71% and a VS removal efficiency of 39%. The gas production and methane content were 1.3 L/day $(0.21\;m^3\;CH^4/kg$ COD removed) and 77%, respectively.