• 상하수도학회지
• /
• 제20권1호
• /
• pp.115-121
• /
• 2006

The purpose of this study was to investigate applicability of pretreatment on the existing biological treatment for domestic wastewater reclamation. From Jar Tests, it was found that optimum dosage of coagulant was PAC 0.5mg/L and $FeCl_3$ 180mg/L for urban sewage. In this study, PAC 0.5mg/L was selected considering sludge production and the amount of coagulant required. In a continuous experiment performed with combining chemical coagulation and biological treatment, a considerable removal efficency was obtained in term of BOD, SS, T-N, T-P and ABS. When the raw sewage was supplied into the pre-chamical treatment facility, the removal of BOD and SS was 48.3% and 81.1%. However T-N removal was very low which means T-N consists of $NH_3-N$ mostly. T-P was almost completely recluced by the chemical addition. The effluent BOD & SS was 57~76 and 21~43mg/L, which could reduce the size of biological treatment facility. From the cost estimation pre-chemical treatment could save around half of the area required for biological treatment with post ceagulation.

• 한국물환경학회지
• /
• 제23권1호
• /
• pp.122-130
• /
• 2007

This study was conducted to evaluate water treatment characteristics according to vegetated wetland(V) and open water(O) arrangements in free water surface constructed wetland. Three pilot-scale wetlands, V-V, O-V and V-O, were built and operated. $BOD_5$ was a slightly reduced at all the arrangements because the influent concentration was so low as background concentration of constructed wetlands. While T-N and T-P removal efficiency showed higher than 50% for all cases. The O-V arrangement showed the highest removal efficiency: 20% for $BOD_5$, 56% for SS, 59% for T-N and 72% for T-P. Effluent concentration of the O-V were significantly low compared with those from the V-O. O-V arrangement would be beneficial in the light of pollutant removal efficiency as well as construction cost.

• 한국양식학회지
• /
• 제12권1호
• /
• pp.47-56
• /
• 1999

순환여과식 어류 양식 시설에서 호기성 미생물의 질산화 작용에 의하여 암모니아는 질산염으로 산화되어 축적되며 이를 제거하기 위하여 협기성 미생물을 이용한 탈질산화 과정을 많이 이용하고 있다. 이 과정에서 혐기성 미생물에 의한 탈질산화 효율은 외부 탄소원의 종류, 수리학적 체류시간(hydraulic retention time, HRT) 및 외부 탄소원 농도에 대한 수중 질산염의 농도비율 ($COD/NO_3^-N$, C;N)에 따라 달라진다. 따라서 우리 나라 순환여과식 양식장에서 일반적으로 이용되고 있는 선라이트 골판을 여과 재료로 한 침지식 여과조를 탈질 여과조로 이용하여 적정 유기 탄소원 제거 조건을 구명하기 위해 질산염의 농도를 순환여과식 양어장의 일반적인 농도인 $20.0mg/\ell$로 고정하고 외부 탄소원으로 메탄올과 글루코스를 사용하여 HRT와 C:N 비율 변화에 따른 적정 제거 조건을 알아보았다. 외부 탄소원의 종류에 따른 질산성질소의 제거 효율은 어떤 실험 조건에서도 메탄올이 글루코스보다 높게 나왔으며 HRT의 경우 글루코스와 메탄올 어느 쪽도 HRT 4시간 보다 8시간에서 효율이 좋았다. (P<0.05). HRT 8시간에서 C:N의 비율 3,4,5,6 중에서 5까지는 효율이 증가하여 글루코스의 경우 최대 제거 효율은 76.5%였고 일간 제거속도는 $223.5 g/m^2/day$였다. 그러나 외부 탄소원으로 메탄올을 사용할 경우 C:N 비율이 6으로 증가하면 효율이 감소되었다. HRT가 4시간일 경우 일간제거속도는 C:N 비율 5의 조건에서 메탄올이 $355.6g/m^2/day$로 가장 높았으나 배출수에 포함된 유기물 농도가 $40.9 mg/\ell$로 양어 용수에는 부적당하였다. 적정 제거 조건으로 생각되어지는 HRT 8시간, C:N 비율 5, 유기탄소원으로 메탄올을 사용하여 유입수의 질산성질소 농도를 $40.9 mg/\ell$ 로 높일 때 일간 제거속도는 질산성질소 농도가 20.6 mg/\ell$일 때 보다 2.2배가 증가하였다. 또한 배출수의 질산성질소 농도도 $5.6 mg/\ell$로 나타나 질산성질소의 일간제거속도는 높아졌으나 C:N 비율 5를 맞추기 위한 메탄올의 농도 증가로 인하여 배출수의 메탄올 농도가 $71.3 mg/\ell$로 증가하여 양식 dydt로는 부적당하였다. 따라서 선라이트 골판을 이용한 침지식 탈질조의 최적 운전 조건은 HRT 8시간, C:N 비율 5및 외부 탄소원으로 메탄올을 이용하는 것이 가장 좋은 결과를 나타내었다. 유입수의 질선성질소 농도가 증가하면서 질산성질소의 일간제거속도도 함께 증가하였고 이에 따라 수중 pH도 8.0에서 8.8까지 점차적으로 증가하는 결과를 나타내었다.

• 한국양식학회지
• /
• 제16권4호
• /
• pp.252-256
• /
• 2003

양식장에서 생성되는 어류의 노폐물이나 미섭취되고 남은 사료분은 고농도의 질소와 인을 함유하고 있으나 미처리된 상태로 처리하고 있어 그에 따른 처리방안이 요구된다. 본 연구에서는 기존의 처리공정의 대용으로 생태공학적 처리로서 경제적으로 질소와 인 제거를 위해 실내재배조에 물상추를 적용하였다. 앙식장 배출수 처리를 위한 생물여과상의 처리효율을 향상시키기 위하여 물상추 여과조를 설치하여 다양한 조건하에 시도되었다. 실험 재료인 수초는 물상추를 재배하였고, 6개의 수조(62${\times}$60${\times}$86cm)에 재배조 용량이 80 L가 되도록 채우고 수리학적 체류시간(hydraulic retention time; HRT)을 1, 2, 4, 8일로 하여 운영하였다. HRT 8일인 경우 1차 배출수를 대상으로 하였을 경우 BOD, T-N, T-P의 제거율은 92.8, 79.0 및 93.6%로 각각 나타났다.

• 한국물환경학회지
• /
• 제25권1호
• /
• pp.96-101
• /
• 2009

The aim of this research was to apply experimental design methodology to optimizetion the photolytic degradation of N-nitrosodimethylamine (NDMA). Reactions were mathematically described as a function of parameters such as pH, initial NDMA concentration, and UV intensity using the Box-Behnken method. The results showed that the responses of NDMA removal (%) in photolysis were significantly affected by the synergistic effect of linear term of pH, initial NDMA concentration and UV intensity. The application of Response Surfase Methodology (RSM) using the Box-Behnken method yielded the following regression equation, which is an empirical relationship between the removal (%) of NDMA and test variables in coded unit: Y = 50.929 + 16.073(UV) - 7.909(NDMA) - 27.432(pH) - 11.385(UV)(NDMA) - 7.363(UV)(pH) +13.811(NDMA)(pH). The model predictions agreed well with the experimentally observed result ($R_2(ad.)=89%$).

• Journal of Periodontal and Implant Science
• /
• 제31권3호
• /
• pp.531-542
• /
• 2001

Periodontal debridement is most important procedure in periodontal treatment, because periodontal disease is the biofilm infection. The use of ultrasonic instrument has many clinical advantages compared to classical hand instrument. The introduction of newly developed ultrasonic scaler tips made the use of ultrasonic scaler popular. However the study of tooth substance removal according to the working parameters of ultrasonic scaler with newly developed tips is not sufficient. The purpose of this study is to evaluate the effects of working parameters of piezoelectric ultrasonic scaler with curette tip on casting gold removal. The working parameters was standardized by the sledge device which controls lateral force(0.5 N, 1.0 N, 2.0 N) and power setting was adjusted 2, 4, 8 in P mode and S mode and instrumentation time was 5 seconds. The defect depth and width were measured with profile meter and defect surface was examined by SME. The depth of defect was significantly large in S mode( $39.58{\pm}19.35{\mu}m$) compared to P mode( $8.37{\pm}6.98{\mu}m$). There was significant decrease of depth of defect between 1.0N($32.87{\pm}27.18{\mu}m$) and 2.0N( $14.86{\pm}15.04{\mu}m$). The area of defect was also significantly large in S mode($4482.42{\pm}3551.71{\mu}m^2$) compared to P mode( $922.06{\pm}960.32{\mu}m^2$). There was significant decrease of area of defect between 1.0N($3889.12{\pm}3936.00{\mu}m$) and 2.0N( $974.66{\pm}986.01{\mu}m$). The change of mode did not effect on the width of the defect. The change of power setting did not effect on the depth, width, and area of defect. In spite of limitation of this study it could be concluded that the use of piezoelectric ultrasonic scaler with curette tip on S mode could make significant tooth substance loss.

• 한국물환경학회지
• /
• 제22권1호
• /
• pp.7-16
• /
• 2006

The present study evaluated effect of temperature on removals of organic matter (C), nitrogen (N) and phosphorus (P) in Modified-Dephanox (M-Dephanox) process, which is hybrid system, comparing with those of Modified-Ludzack Ettinger (MLE) under the suspended-growth bacteria, as control. M-Dephanox process was more stable than MLE process in the removal of C, N, P, especially in nitrification, as the temperature was decreased from $25^{\circ}C$ to $16^{\circ}C$. As the temperature was decreased from $25^{\circ}C$ to $16^{\circ}C$, the removal efficiency of $NH_4{^+}-N$ of M-Dephanox process was decreased by 3.8%, but that of MLE process decreased by 25.7%. T-N removal efficiency of M-Dephanox was higher than MLE process by 27.1% and 26.9% at $25^{\circ}C$ and $16^{\circ}C$ of temperature, respectively.

• 대한전기학회:학술대회논문집
• /
• 대한전기학회 1999년도 하계학술대회 논문집 E
• /
• pp.2010-2012
• /
• 1999

The product of electrons by Pulsed Corona Discharge leads to produce radicals which work on NO, and NO is finally removed. Energy efficiency for NO removal was improved with increasing peak voltage rather than with increasing pulse frequency. The rate of energy transfer increased with decreasing value of $C_p$( Pulse - Forming Capacitance 2.15, 1.06, 0.55, 0.36, 0.1[nF]. When the value of $C_p$ reached to 0.36 [nF], the energy efficiency for NO removal was maximized. And good agreement was obtained between chemical kinetic calculations and the experimental results.

• Advances in environmental research
• /
• 제5권3호
• /
• pp.169-178
• /
• 2016

This study aimed at determining the treatability of high-strength wastewater (chemical oxygen demand, COD>4000 mg/L) using combined anaerobic-aerobic granular sludge in lagoon systems. The lagoon systems were simulated in laboratory-scale aerated and non-aerated batch processes inoculated with dried granular microorganisms at a dose of 0.4 g/L. In the anaerobic batch, a removal efficiency of 25% was not attained until the 12th day. It took 14 days of aerobic operation to achieve sCOD removal efficiency of 94% at COD:N:P of 100:4:1. The best removal efficiency of sCOD (96%) was achieved in the sequential anaerobic-aerobic batch of 12 days and 2 days, respectively at COD:N:P ratio of 200:4:1. Sequential anaerobic-aerobic treatment can achieve efficient and cost effective treatment for high-strength wastewater in lagoon systems.

• KSBB Journal
• /
• 제22권4호
• /
• pp.191-196
• /
• 2007

본 연구는 급속한 산업 발전으로 인해 일어난 많은 수질오염 문제 중 생활하수의 처리방법에 관심을 기울여 생물막 공법을 이용하였는데, 이는 소규모 오폐수 처리장치에서 운전과 유지가 간단하고 활성슬러지 공정보다 넓은 부지를 필요로 하지 않기 때문이다. 생물막 공법 중 생물여상법의 변법을 적용한 Pilot 규모의 상향류식 충전탑형 반응기로 내부의 담체로는 폐토기와 폐비닐을 넣어 혐기조와 호기조를 구성하였고, 생활 오수로는 식당 오수를 이용하여 Lab.-Scale 실험 후 Pilot-Scale로 Scale-up하여 100여일 간에 걸쳐 실험을 수행하였다. 실험은 연속 포기시 일정 HRT에서 유기물과 질소, 인 제거율을 살펴보았다. 실험결과 $BOD_5$와 SS의 평균 제거율은 각각 94.33%와 87.77%로 높은 제거율을 보였으나, $COD_{Cr}$은 81.46%로 목표 제거율 90% 이상에 미치지 못하였고, T-N과 T-P도 각각 71.92%와 21.10%로 예상보다 약간 낮았다. 특히 $COD_{Cr}$와 T-N의 제거율은 지난 Lab.-Scale 때보다 약 10% 정도의 감소를 하여 Pilot-scale에 내외적인 문제가 작용한 것으로 보였다.