• 한국유체기계학회 논문집
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• 제18권2호
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• pp.54-59
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• 2015

The performance of UV reactor which is used in water treatment is strongly affected by UV fluence rate and water flow in the UV reactor. Therefore, CFD tools are widely used in designing process of UV reactors. This paper describes the development of a computational fluid dynamics (CFD) methodology that can be used to calculate the performance of open channel type UV reactor used in wastewater treatment plant. All computations were performed using commercial CFD code, CFX, by considering three dimensional, steady, incompressible flow. The Eulerian-Eulerian multi-phase method were used to capture the water-air interface. The MSSS model, provided by UVCalc3D, was used to calculate the UV intensity field. The numerical predictions and calculated UV Dose were compared with experimental dataset to validate the CFD methodology. The reactor performance based on MS2 log reduction was well matched with measurements within 6%.

• 대한전기학회:학술대회논문집
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• 대한전기학회 2005년도 추계학술대회 논문집 전기기기 및 에너지변환시스템부문
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• pp.223-225
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• 2005

This paper presents a novel prototype of a current source resonant inverter using insulated gate bipolar transistors for driving a streamer reactor, streamer generation technology has been recognized as one of the best methods for water treatment, disinfection, industrial wastes utilization, and so on. However, some technological difficulties related to efficient streamer production have been significant problems restricting streamer usage in the industrial plants. Introduced in this paper is a pulse density modulated high frequency inverter for a plasma generate, which is developed with the aim to improve power conversion and control characteristics of the streamer reactor by using advances in power electronic technology. The developed system implements the feedforward control-based pulse density modulation control scheme with pulse width modulation feedback control strategy to compensate temperature and other environmental influences on streamer discharge.

• 상하수도학회지
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• 제26권4호
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• pp.521-533
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• 2012

Interest in application of ultraviolet light technology for primary disinfection that used for the treatment of water for consumption and wastewater has increased significantly in recent years. Analysis of these systems has been carried out using Computational Fluid Dynamics (CFD) procedure. It offers advantages over other techniques in specific circumstances. CFD has emerged as a powerful tool to aid design of a UV reactor by providing the UV dose delivered by the proposed reactor design and allowing engineers to evaluate alternative designs in much less time and at a reasonable cost. In this study, five different configurations of the apparatus depending on the location of the exit are evaluated in terms of maximum dose, minimum dose, flow patterns, particle tracks and transient dose. The configuration 3 results have higher minimum UV dose value and uniform particle distribution of the UV dose on the outlet than other's.

• 한국지하수토양환경학회지:지하수토양환경
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• 제20권1호
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• pp.36-40
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• 2015

This study examined the disinfection in combined sewer overflows (CSOs) by pulsed ultraviolet (PUV). The reflectors (stainless steel. mirror, aluminium foil, aluminium (1050), aluminium (6061), aluminium (5052), and aluminium mirror) of PUV irradiation was performed in a 90 L stainless reactor at a constant temperature of $20^{\circ}C$ and an applied power of 4000 W. The reflection efficiency of reflectors were showed 1.00 (aluminium mirror) ~ 1.48 (aluminium foil) does. The case of a rough surface analysis using SEM showed high reflectance, was the case of a smooth surface and a low reflectivity. Pseudo first-order rate constant calculated results, has a higher reflectivity values were more than twice as high compared to the low reflectivity. Affected Total coliforms disinfection time, depending on the type of reflector is considered.

• 한국환경과학회지
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• 제24권11호
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• pp.1393-1404
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• 2015

Ten empirical disinfection models for the plasma process were used to find an optimum model. The variation of model parameters in each model according to the operating conditions (first voltage, second voltage, air flow rate, pH, incubation water concentration) were investigated in order to explain the disinfection model. In this experiment, the DBD (dielectric barrier discharge) plasma reactor was used to inactivate Phytophthora capsici which cause wilt in tomato plantation. Optimum disinfection models were chosen among ten models by the application of statistical SSE (sum of squared error), RMSE (root mean sum of squared error), $r^2$ values on the experimental data using the GInaFiT software in Microsoft Excel. The optimum models were shown as Log-linear+Tail model, Double Weibull model and Biphasic model. Three models were applied to the experimental data according to the variation of the operating conditions. In Log-linear+Tail model, $Log_{10}(N_o)$, $Log_{10}(N_{res})$ and $k_{max}$ values were examined. In Double Weibull model, $Log_{10}(N_o)$, $Log_{10}(N_{res})$, ${\alpha}$, ${\delta}_1$, ${\delta}_2$, p values were calculated and examined. In Biphasic model, $Log_{10}(N_o)$, f, $k_{max1}$ and $k_{max2}$ values were used. The appropriate model parameters for the calculation of optimum operating conditions were $k_{max}$, ${\alpha}$, $k_{max1}$ at each model, respectively.

• 상하수도학회지
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• 제10권1호
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• pp.78-84
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• 1996

The presence of ammonia, usually in the form of ammonium ion ($NH_4{^+}$), can enhance bacterial growth m the distribution system and make the production of drinking water more costly if ammonium must be removed to ensure good disinfection. Removal of ammonia by biological oxidation could be economical which prevents excess chlorine dosage In this research, effects of hydraulic retention time (HRT) and media type on the ammonia removal efficiencies of submerged biofilm reactor were investigated. The biofilm reactors combined the characteristics of high biological solids capture efficiency and good hydraulic control. The results indicate that biofilms can remove over 77 percent of the ammonia with HRT of longer than 2 hr even at low temperature ranging from 14.6 to $16.6^{\circ}C$. The HRT has a significant effect on nitrification. The overall nitrification and efficiency of ammonia removal increase with increasing HRT. It has also been observed that when the fibrous media was used, the ammonia removal, nitrification rate and endurance to shock improved.

• 한국양식학회지
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• 제13권2호
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• pp.137-145
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• 2000

삼상 유동층 반응조의 수처리 효율을 검토하기 위해 해수 순환여과 시설을 운전하였다. 수처리 시스템은 유동층 반응조, 카트리지 필터, 오존접촉조로 구성되어 있고, 전체 운전기간동안 사육조내 수질인자별 평균농도는 각각 COD 9mg/L, 총암모니아(TAN) 0.22mg/L, 아질산성 질소 0.05mg/L, 질산성 질소 20mg/L, 탁도 3.64 NTU, SS 9.5mg/L, pH 7.6, 알칼리도 70mg/L 등으로 나타나 양호한 수질조건을 유지할 수 있었다. 유동층 반응조의 TAN 부하량 범위는 4.3~32.9 g/$m^3$/day였고, 평균 제거율은 20 g/$m^3$/day으로 나타났다. 각 반응조의 TAN 제거율은 47~60%로 나타나 해수에서도 효과적인 암모니아 제거 특성을 나타내었다. 또한 유출수의 비이온성 암모니아 농도는 0.002 mg/L이하로 유지 할 수 있었다

• 생명과학회지
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• 제16권3호
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• pp.534-539
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• 2006

크립토스포리디움은 염소내성이 매우 강해 일반적인 표준정수처리공정의 소독으로는 제거가 불가능하다. 따라서 본 연구에서는 오존 및 UV를 이용한 단위소독공정에서 DAPI/PI 및 in vitro excystation을 이용하여 크립토스포리디움 불활성화를 평가하였으며, 또한 오존을 이용한 고도산화처리 파일럿에서는 세포배양법을 이용하여 크립토스포리디움 불활성화를 평가하였다. 오존 소독연구는 50 mL 용량의 piston type batch reactor에서 용존오존을 자동적으로 측정해주는 flow injection analysis (FIA) 시스템을 이용하여 실험한 결과, 1 log 제거에 필요한 CT값은 $25^{\circ}C$에서 DAPI/PI 및 in vitro excystation에 의해 각각 약 1.8, 2.2 $mg/L{\cdot}min$으로 나타났으며, 2 log 제거에 필요한 CT값은 각각 약 3.2, 3.8 $mg/L{\cdot}min$으로 나타났다. 또한 $5^{\circ}C$에서 크립토스포리디움 1 log 제거에 필요한 CT값은 DAPI/PI 방법에 의해 약 9.1 $mg/L{\cdot}min$으로 나타났으며, 2 log제거에 필요한 CT값은 14.8 $mg/L{\cdot}min$로 나타나, 같은 소독효과를 나타내기 위해서 저온에서는 상온에서보다 요존 요구량이 약 $4{\sim}5$배 정도 증가하여야 함을 확인하였다. 40 L규모의 오존 반응조를 이용한 파일럿 실험에서는 정수처리공정상 모래여과를 거친 물에 살아있는 크립토스포리디움을 접종한 것을 시료로 하여 연속적으로 흐르게 한 다음, 오존량을 변화시키고 체류시간은 5분으로 고정하여 불활성화를 평가하였다. 실험결과, 8 $mg/L{\cdot}min$의 CT값에서 DAPI/PI 및 excystation과 같은 생사판별법을 이용하였을 경우에는 약 0.2 log정도의 불활성화를 나타내었으며, 세포감염시험법을 이용하였을 경우에는 약 1.2 log정도의 불활성화를 나타냈다. 오존에 의한 크립토스포리디움의 소독능 평가에 단위공정 및 파일럿 실험 모두 2가지 생사판별법(DAPI/PI와 excystation) 사이에는 큰 차이를 나타내지 않았으나, 생사판별법과 세포감염시험법 사이에는 현저한 차이를 나타내었는데, 이는 세포감염시험법으로 측정하는 sporozoite 및 merozoite로의 분화과정이 생사판별법이 근거한 세포벽의 구조와 기능 유지 보다 더 오존 소독에 더 민감함을 알 수 있었다. 파일럿 실험에서의 CT값이 piston batch reactor에서의 CT값 보다 낮게 나타난 것은 파일럿 실험에서 수작업으로 인한 용존 오존 측정이 정밀하지 못하여 IOD가 농도에 반영되지 않았고, 반응조 규모(50 mL vs 40 L) 및 형태(회분식 vs 연속식)의 차이에 기인하는 것으로 여겨진다. 한편, UV를 이용한 단위공정에서는 크립토스포리디움 1, 2 log 제거에 필요한 IT값은 $25^{\circ}C$에서 각각 DAPI/PI 방법에 의해 약 25, 50 $mWs/cm^2$로 나타났으며, $5^{\circ}C$에서의 크립토스포리디움 1, 2 log제거에 필요한 IT값은 약 40, 80 $mWs/cm^2$로 나타났다. 온도 $20^{\circ}C$ 감소 시 약 60% 정도의 IT값이 더 필요한데, 이것은 저온에서는 약한 자외선을 발산하는 저압저출력 UV 램프의 특성 때문인 것으로 사료되었다.

• 상하수도학회지
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• 제34권3호
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• pp.183-190
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• 2020

Although membrane bio-reactor (MBR) has been widely applied for wastewater treatment plants, the membrane fouling problems are still considered as an obstacle to overcome. Thus, many studies and commercial developments on mitigating membrane fouling in MBR have been carried out. Recently, high voltage impulse (HVI) has gained attention for a possible alternative technique for desalting, non-thermal sterilization, bromate-free disinfection and mitigation of membrane fouling. In this study, it was verified if the HVI could be used for mitigation of membrane fouling, particularly the internal pore fouling in MBR. The HVI was applied to the fouled membrane under different conditions of electric fields (E) and contact time (t) of HVI in order to investigate how much of internal pore fouling was reduced. The internal pore fouling resistance (R_f) after HVI induction was reduced as both E and t increased. For example, R_f decreased by 19% when the applied E was 5 kV/cm and t was 80 min. However, the R_f decreased by 71% as the E increased to 15 kV/cm under the same contact time. The correlation between E and t that needed for 20% of R_f reduction was modeled based on kinetics. The model equation, E^1.54t = 1.2 × 10³ was obtained by the membrane filtration data that were obtained with and without HVI induction. The equation states the products of En and t is always constant, which means that the required contact time can be reduced in accordance with the increase of E.

• 한국물환경학회지
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• 제25권4호
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• pp.547-552
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• 2009

Because of refractory property of light, the travel path of UV light becomes longer than the straight line and shorter solely in water as UV light passes sequentially through air, quartz and water. Note that water significantly absorbs UV light. Hence, UV intensity shall be estimated to be lower when refraction is neglected than it is considered. Reflection is also critical for the design of UV radiation system. While the reflection at the interface of air and quartz is low enough to ignore, it is too high to be ignored at the interface of quartz and water. Assuming constant power, smaller length to width ratio of UV reactor is beneficial and single-lamp system is preferred to multi-lamps. Under the given cross section, optimal lamp positions could be decided. For example of an elliptical reactor with dual lamps, the optimal lamp locations shall be the 1/3 and 2/3 position of the longer axis.