• 한국지하수토양환경학회지:지하수토양환경
• /
• 제15권2호
• /
• pp.10-17
• /
• 2010

Advanced oxidation processes (AOPs) have advantages to reduce the processing time and mineralize contaminants dissolved in groundwater. Recently, remediation techniques for organic contamination in groundwater have been studied, and technology using $UV/H_2O_2$ is generally accepted as one of the most powerful and reliable alternative for the remediation of groundwater contamination. In this study, $UV/H_2O_2$ technology, which generates hydroxyl radical ($\cdot$ OH) as known for strong non-selective oxidant, was used to degrade chlorinated solvents (TCE and PCE), and it was expanded to apply continuous stirred tank reactor (CSTR) system (i.e. combinations of three CSTR). The tested parameters for CSTR system were retention time and groundwater/$H_2O_2$ injection volume ratio. To find optimum parameters for CSTR system, various retention time (6 min ~ 90 min) and groundwater/$H_2O_2$ injection volume ratio (5/1 ~ 119/1) were tested. Other conditions for CSTR were adapted from the batch test results, which concentration of $H_2O_2$ and UV dose were 29.4 mM (0.1%) and 4.3 kWh/L, respectively. Based on the experimental results, the optimum parameters for CSTR system were 20 min for retention time and 119/1 for groundwater/$H_2O_2$ injection volume ratio. Applying these optimum conditions, chlorinated solvents (TCE and PCE) were removed at 99.9% and 99.6%. Moreover, the effluent concentrations of TCE and PCE are 0.036 mg/L and 0.087 mg/L, respectively, which are satisfied the regulatory level (TCE 0.3 mg/L, PCE 0.1 mg/L). Consequently, the CSTR system using $UV/H_2O_2$ technology can achieve high removal efficiency in the event of treatment of groundwater contaminated by chlorinated solvents (TCE and PCE).

• 상하수도학회지
• /
• 제36권2호
• /
• pp.59-79
• /
• 2022

Conventional wastewater treatment plants (WWTPs) do not fully remove micropollutants. Enhanced treatment of sewage effluents is being considered or implemented in some countries to minimize the discharge of problematic micropollutants from WWTPs. Representative enhanced sewage treatment technologies for micropollutant removal were reviewed, including their current status of research and development. Advanced oxidation processes (AOPs) such as ozonation and UV/H₂O₂ and adsorption processes using powdered (PAC) and granular activated carbon (GAC) were mainly discussed with focusing on process principles for the micropollutant removal, effect of process operation and water matrix factors, and technical and economic feasibility. Pilot- and full-scale studies have shown that ozonation, PAC, and GAC can achieve significant elimination of various micropollutants at economically feasible costs(0.16-0.29 €/m³). Considering the current status of domestic WWTPs, ozonation and PAC were found to be the most feasible options for the enhanced sewage effluent treatment. Although ozonation and PAC are all mature technologies, a range of technical aspects should be considered for their successful application, such as energy consumption, CO₂ emission, byproduct or waste generation, and ease of system construction/operation/maintenance. More feasibility studies considering domestic wastewater characteristics and WWTP conditions are required to apply ozonation or PAC/GAC adsorption process to enhance sewage effluent treatment in Korea.

• 한국지하수토양환경학회지:지하수토양환경
• /
• 제12권5호
• /
• pp.105-114
• /
• 2007

Advanced oxidation processes(AOPs)는 강력한 산화제인 hydroxyl radical(${\cdot}OH$)를 생성하여 오염물질을 산화시키는 기법이다. 본 연구에서는 DNAPL인 trichloroethylene(TCE)과 tetrachloroethylene(PCE)의 수리학적 특성을 고려하여 우수한 고도산화처리기법($UV/Fe^{3+}$-chelating agent/$H_2O_2$기법, $UV/H_2O_2$기법)의 적용성 평가를 실시하였다. TCE, PCE 처리에 있어 가장 높은 분해효율을 보인 기법은 $UV/H_2O_2$기법으로 pH 6의 중성조건에서 TCE의 경우 150분 만에 99.92%의 TCE 분해를 나타내었고($[H_2O_2]$ = 147 mM, UV dose = 17.4 kwh/L), PCE의 경우 반응 2시간에 99.99%가 분해되었다($[H_2O_2]$ = 29.4 mM, UV dose = 52.2 kwh/L). 또한, $UV/Fe^{3+}$-chelating agent/$H_2O_2$기법을 적용하였을 경우, TCE는 90분 만에 99.9% (UV dose = 34.8 kwh/L, $[Fe^{3+}]$ = 0.1 mM, [Oxalate] = 0.6 mM, $[H_2O_2]$ = 147 mM) PCE는 반응시간 6시간 만에 99.81% (UV dose = 17.4 kwh/L, $[Fe^{3+}]$ = 0.1 mM, [Oxalate] = 0.6 mM, $[H_2O_2]$ = 29.4 mM)의 빠른 분해경향을 보였다. 이러한 결과는 기존의 고도산화처리기법 중 modified Fenton 반응에 UV를 적용함으로서 반응 중 $H_2O_2$의 재생산을 증가시킬 수 있음을 보여주고 있다. 또한, Fe(III) 이온의 Fe(II) 이온으로의 환원을 용이하게 하여 기존 Fenton 반응에 비해 처리시간의 단축 및 분해효율의 향상을 기대할 수 있을 것이다. 그리고, oxalate나 acetate같은 저분자 유기산 착제의 적용으로 pH의 안정성과 분해효율의 향상이 가능하고, 철이온 및 oxalate나 acetate와 같은 물질이 자연상에 존재함에 따라 보다 경제적이고 친환경적인 실용적 처리기법 도출이 가능할 것이다.

• 한국입자에어로졸학회지
• /
• 제13권3호
• /
• pp.127-132
• /
• 2017

In this paper, the effect of the irradiation of the median-frequency of ultrasonic wave on the aqueous solution have been investigated. In addition, the decomposition ability of radical species was observed using phytoncide oil of 0.1 wt %. By observing the degree of decomposition while maintaining magnetic stirring, the unirradiated aqueous solution maintained turbid condition and the particle size of the oil was the same as the initial size. On the other hand, the irradiated aqueous solution presented that the transparency degree became good after 3 days and became to the same as the original purified water after one week. The particle size of the after 3 days was about 0.1 to $0.5{\mu}m$. From these results it could be demonstrated that when a medium frequency (about 400 kHz) is applied to the aqueous solution, decomposition ability of radical species are formed and the medium frequency irradiation system can be possible to purify the turbid aqueous solution.

• 한국물환경학회지
• /
• 제21권3호
• /
• pp.284-288
• /
• 2005

In this study, photochemical advanced oxidation processes (AOPs) utilizing the Photo Fenton reaction ($Fe^{2+}+H_2O_2+UV$) were investigated in lab-scale experiments for the treatment of livestock wastewater. For the experimets, the livestock wastewater was pretreated by coagulation with $3,000mg/L\;FeCl_3$. The optimal conditions for Photo-Fenton processes were determined: pH was 5, the concentration of ferrous ion (Fe II) was 0.01 M. The concentration of hydrogen peroxide was 0.1 M, and molar ratio ($Fe^{2+}/H_2O_2$) was 0.1. The optimal reaction time was 80 min. Under the optimal condition of Photo-Fenton process, chemical oxygen demand (COD), color and fecal coliform removal efficiencies were about 79, 70, and 99.4%, respectively and sludge production was 7.5 mL from 100 mL of solution.

• 한국물환경학회지
• /
• 제22권5호
• /
• pp.913-918
• /
• 2006

Both raw wastewater and effluent from a rubber products manufacturing factory were found to be toxic to Daphnia magna though the effluent satisfied current water quality standards. Thus, in order to reduce toxicity, advanced oxidation processes (AOPs) such as gamma-ray (${\gamma}-ray$) treatment and ozonation ($O_3$) were applied. A combined ${\gamma}-rays/O_3$ treatment at 20 kGy after coagulation significantly reduced toxicity of raw wastewater, changing 48-h toxic unit (TU) value from 201.21 to 23.92. However, toxicity of treated water was higher than that of effluent (TU = 12.15). This shows limitation of gamma-ray treatment to remove toxicity of raw wastewater. In case of effluent, the combined ${\gamma}-rays/O_3$ treatment at 20 kGy efficiently decomposed toxic compounds down to non toxic level. This work strongly supports the necessity of toxicity reduction evaluation as well as toxicity-based effluent management.

• 대한환경공학회지
• /
• 제39권5호
• /
• pp.246-254
• /
• 2017

호소, 하천 등에 다량의 영양염류의 유입과 수문학적, 지리학적, 생물학적 요소 등으로 인해 남조류가 대량 발생하게 되며 대표적 독성물질인 마이크로시스틴-LR(MC-LR)이 증가한다. MC-LR이 포함된 지표수를 적절하게 처리하기 위하여 정수처리공정에서는 고도산화공정을 적용하고 있다. 다양한 고도산화공정 중 특히 UV, $UV/H_2O_2$, $UV/O_3$, $UV/TiO_2$ 등에 대한 연구는 꾸준히 되어왔다. 기존의 UV램프의 짧은 교체주기, 수은 폐기물 발생, 큰 열 손실 등의 단점을 보완한 UV-LED를 MC-LR제거에 적용하였다. MC-LR 초기농도 $100{\mu}g/L$을 280 nm의 파장인 LED-L ($0.024mW/cm^2$)와 LED-H ($2.18mW/cm^2$)를 이용하여 산화시켰을 때 각각 최대 약 30%, 95.9%의 MC-LR 제거율을 나타냈다. LED-H를 조사 시 자연유기물 변화는 휴믹물질, UVD, SUVA가 감소하는 경향을 보였고 방향족 유기물이 지방족 유기물로 분해되어 저분자 물질이 되었다. $LED-H/H_2O_2$($H_2O_2$: 1, 2, 5, 10 mg/L)산화반응에 의한 MC-LR제거율은 LED-H 단독에 의한 MC-LR 제거율과 유사하였다. 남조류가 발생한 낙동강 원수를 대상으로 LED-L산화를 적용하여 수질분석을 통하여 특성변화를 확인하였다. DOC 및 TOC의 변화는 거의 없었으나 SUVA와 $UV_{254}$의 감소로 인하여 유기물의 분해되었으며 조류유래물질인 용존 및 총 MC-LR, geosmin, 2-MIB농도가 시간이 지남에 따라 서서히 감소하였다.

• 공업화학
• /
• 제29권6호
• /
• pp.690-695
• /
• 2018

페니실린(PEN) 항생제의 분해를 위하여 오존, 과산화수소, 자외선으로 구성된 고도산화공정(AOP)을 적용하였다. 항생물질 분해효율은 흡광도(ABS) 및 총유기탄소(TOC) 분석으로 평가하였다. $O_3/H_2O_2/UV$와 $O_3/UV$ 조합이 ABS (9 min 동안 100%) 및 TOC 감소(60 min 동안 70%)에 가장 효과가 좋았으나 사용한 실험조건에서 항생제의 무기질화 및 독성제거는 완전하지 않았다. 항생물질에 의한 생독성은 Escherichia coli 민감도 및 Vibrio fischeri 생체형광 활성평가를 이용하였으며 $O_3/UV$에 의해 민감도는 9 min 동안 100% 감소, $O_3/H_2O_2/UV$에 의한 생체형광에 대한 독성은 60 min 동안 57% 감소하였다. 생물학적 분해를 위한 AOP 조합으로 $O_3/UV$ 조합을 선정하였으며 $BOD_5/COD$ 비율로 생분해도의 개선 여부를 간접 측정한 결과 $O_3/UV$로 30 min 처리함으로 $BOD_5/COD$ 비율이 약 4배 증가하였다. 페니실린 20 mg/L를 포함하는 인공폐수에 대하여 AOP 처리 후 Pseudomonas putida를 이용하여 호기적 생물학적 분해를 진행한 결과, $O_3/UV$ 전처리한 경우 페니실린의 완전 무기질화가 가능하였으며 전처리하지 않은 경우에 비하여 분해속도가 55% 증진되었다. 결론으로, 호기성 생물학적 처리를 위한 AOP 전처리로써 $O_3/UV$ 조합이 추천되며 페니실린의 완전 분해를 촉진할 수 있다.

• 한국지반환경공학회 논문집
• /
• 제14권5호
• /
• pp.57-63
• /
• 2013

본 연구에서는 전자빔공정에서 반응표면법의 하나인 Box-Behnken법을 이용하여 주요 인자로서 diazinon 농도($X_1$), 조사강도($X_2$)와 pH($X_3$)를 토대로 3개 수준으로 구성된 실험설계에 따라 diazinon의 제거와 무기화 특성에 대해 연구하였다. 우선 pH와 diazinon 농도의 영향이 반응표면법(RSM)에 적용될 적정 범위를 결정하기 위해 수행되었다. 통계적 접근은 회귀분석과 분산분석(ANOVA)를 각 인자별 정량적 비교를 도출하기 위해 적용하였으며, 인자별 영향은 조사강도>diazinon 농도>pH의 순으로 나타났다. 회귀모델은 최적화도구를 이용하여 운영조건의 영향을 고려한 최적점을 예측하였으며, 그에 따른 모델식은 $Y_1=81.73-5.58X_1+23.69X_2-14.23X{_2}^2+4.22X{_3}^2(R^2=99.7%)$, $Y_2=35.23-3.01X_1+10.79X_2-7.58X_2{^2}(R^2=97.9%)$로 도출하였다. 그에 따른 결과는 diazinon 농도 12.75mg/L와 조사강도 4.26kGy에서 diazinon 제거율 95.7%, TOC 저감율은 41.8%로 나타났다. pH 조건은 기존의 다른 고도산화공정(AOPs)에 비해 전자빔 공정에서는 유의한 영향이 없는 것으로 나타났다.

• 상하수도학회지
• /
• 제24권1호
• /
• pp.109-117
• /
• 2010

In the present study, the degradation characteristics of Lindane by Advanced Oxidation Processes(UV/$H_2O_2$, Photo-Fenton process) were studied. The degradation efficiency of Lindane in aqueous solution was investigated at various initial pH values, Fenton's reagent concentrations and initial concentrations of Lindane. GC-ECD was used to analyze lindane. Lindane has not been degraded without application of AOPs over two hours. But, approximately 5% of lindane was degraded with UV or $H_2O_2$ alone. Lindane with UV/$H_2O_2$ process showed approximately 7% higher removal efficiency than $H_2O_2$ process. In the UV/$H_2O_2$ process, the pH values did not affect the removal efficiency. The optimal mole ratio of $H_2O_2/Fe^{2+}$ for lindane degradation is about 1.0 in Photo-Fenton process. Also, the experimental results showed that lindane removal efficiency increased with the decrease of initial concentration of lindane. Under the same conditions, the order lindane of removal efficiency is as following : Photo-Fenton process > UV/$H_2O_2$ process > $H_2O_2$ process. In addition, intermediate products were identified by GC-MS techniques. Than PCCH(Pentachlorocyclohexene) was identified as a reaction intermediate of the Photo-Fenton process.