• 산업기술연구
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• 제29권A호
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• pp.83-88
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• 2009

The removal efficiency of organic compounds and the toxicity evaluation of microorganism have been studied in dye wastewater treatment using $UV/TiO_2$ and $UV/H_2O_2$ photooxidation system. Sample waters tested in this work were raw dye wastewater and dye wastewater treated in $UV/TiO_2$ and $UV/H_2O_2$ photooxidation system respectively. Total organic carbon(TOC) removal rate was 50% in $UV/TiO_2$ process and 80% in $UV/H_2O_2$ process. It has been investigated with colony counting agar method and paper disk method whether the type of treatment process has affected the microorganism growth. In the raw wastewater, more than four types of microorganisms have survived. But, little of microorganisms were alive at TOC removal rate of 50% in $UV/TiO_2$ system. In contrast to that, two types of microorganisms were found at TOC removal rate of 80% in $UV/H_2O_2$ system.

• 환경위생공학
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• 제15권4호
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• pp.26-34
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• 2000

In order to treat the dyeing wastewater, the $UV/TiO_2/H_2O_2$ system was investigated, and proper pretreatment methods were examined to reduce the load on the system considering economical and technical efficiency. The results of this study were as follows: 1. $UV/TiO_2/H_2O_2$ system with pretreatment process was adopted, the result of Chemical coagulation and pH control units was $pH{\;}11{\;}{\rightarrow}{\;}coagulation{\;}{\rightarrow}{\;}pH{\;}4$ and the optimum dosage of $FeCl_3$ was $600mg/{\ell}$. 2. Proper dosage of $TiO_2$ in the $UV/TiO_2/H_2O_2$ system with pretreatment process was $2g/{\ell}$ and $H_2O_2$ was $1000mg/{\ell}$, UV contact time was 20min to get $200mg/{\ell}$ of $COD_{Cr}$.

• 산업기술연구
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• 제20권A호
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• pp.51-56
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• 2000

The Photocatalytic decolorization and degradation of commercial dyes were studied using a batch reactor. Degussa P25 titanium dioxide and $H_2O_2$ were used as the photocatalyst and proved to be effective for dyes degradation when they were irradiated with UV light. The light source was a 20W low pressure mercury lamp. Three different kinds of dyes, such as direct dye(congo red), acid dye (acid black) and disperse dye(disperse blue) were tested. Extending the UV only treatment up to 120min, direct dye was decolorized to 60% and degraded to 30% as COD. On the other side, acid and disperse dyes were eliminated less than 10% as color and COD. But, color and COD were eliminated about 90% for all of the three dyes by $UV/H_2O_2$ system. And then the most effective decolorization was done for direct dye with 96% removal efficiency by $UV/TiO_2$ system at 120min with 500mg/L of $TiO_2$.

• 대한환경공학회지
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• 제22권7호
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• pp.1307-1318
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• 2000

원자력 발전소에서 발생되는 제염폐수에 함유된 Oxalic acid와 Citric acid를 고급산화방법(Advanced Oxidation Process) 중의 하나인 $UV/H_2O_2$를 적용하여 이들 물질의 분해특성 및 최적처리조건을 파악하고자 하였다. 이를 위하여 각각의 물질에 대하여 $H_2O_2$나 UV를 단독사용할 경우, pH 및 과산화수소의 주입량 변화, Oxalic acid와 Citric acid의 농도변화에 따른 분해특성에 대하여 조사하였다. $H_2O_2$나 UV만으로도 완전분해가 가능한 반면 Citric acid는 같은 파장의 UV만으로는 분해가 잘되지 않는 것으로 조사되었다. 또한 과산화수소와는 두 물질 모두 반응성이 없는 것으로 조사되었다. 산화공정에서 반응속도상수, 반응시간, 제거효율, 과산화수소 소모량 등에 대한 결과를 종합한 결과 Oxalic acid의 경우 pH 4 이하의 낮은 pH에서, Citric acid는 pH 4~6 정도의 약산성 부근에서 높은 분해효율을 나타내는 것으로 조사되었다. 최적 pH에서는 과산화수소의 주입량이 증가할수록 두 물질 모두 제거효율이 증가하는 것으로 조사되었으나 과산화수소의 주입량이 200 mg/L 이상을 초과하는 경우에는 과산화수소에 의한 OH radical trap에 의하여 제거효율이 감소하는 것으로 조사되었다. 이상의 결과 $UV/H_2O_2$ 광분해에 의한 Oxalic acid와 Citric acid의 처리시 pH 4에서 과산화수소 주입량 200 mg/L일 경우 가장 효율적인 것으로 조사되었다.

• Environmental Engineering Research
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• 제11권2호
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• pp.84-90
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• 2006

UV-catalytic oxidation technique was applied for the treatment of bio-refractory character of the leachate, which is generally present in the form of adsorbable organic halogens (AOX). Destruction of AOX was likely to be governed by pH adjustment, quantitative measurement of oxidants, and the selection of oxidation model type. Peroxide induced degradation ($UV/H_2O_2$) facilitated the chemical oxidation of organic halides in acidic medium, however, the system showed least AOX removal efficiency than the other two systems. Increased dosage of hydrogen peroxide (from 0.5 time to 1.0 time concentration) even did not contribute to a significant increase in the removal rate of AOX. In ozone induced degradation system ($UV/O_3$), alkaline medium (pH 10) favored the removal of AOX and the removal rate was found 11% higher than the rate at pH 3. Since efficiency of the $UV/O_3$ increases with the increase of pH, therefore, more OH-radicals were available for the destruction of organic halides. UV-light with the combination of both ozone and hydrogen peroxide ($UV/H_2O_2$ 0.5 time/$O_3$ 25 mg/min) showed the highest removal rate of AOX and the removal efficiency was found 26% higher than the removal efficiency of $UV/O_3$. The system $UV/H2O_2/O_3$ got the economic preference over the other two systems since lower dose of hydrogen peroxide and relatively shorter reaction time were found enough to get the highest AOX removal rate.

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

• 상하수도학회지
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• 제18권3호
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• pp.377-384
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• 2004

In the present study, a feasibility of an advanced oxidation process using UV/Hydrogen peroxide($H_2O_2$) system equipped with a medium pressure lamp for secondary effluent reclamation was investigated. Initial concentration of $H_2O_2$ and pH were changed to determine the optimum operation condition for the system. The removal efficiency of color was than 80% with 14.3mg/L of initial $H_2O_2$ and 5 minute of contact time in the UV/$H_2O_2$ system. The color removal was analyzed using first-order reaction equation. The dependence of rate constant (k) on initial $H_2O_2$ represented the rational relationship with maximum value. Residual $H_2O_2$ caused increase of effluent COD, since analyzing agent, dichromate, reacted with $H_2O_2$ in the sample. Therefore, excess initial concentration of $H_2O_2$ would significantly affect effluent COD measurement. At pH variation experiment, both residual $H_2O_2$ and color showed peak in the neutral pH range with the same pattern. Effect of $H_2O_2$ dose also enhanced color removal but raised residual $H_2O_2$ problem in the continuous operation UV system. In conclusion, these results indicated that medium pressure UV/$H_2O_2$ system could be used to control color in the secondary effluent for reclamation and reuse.

• 환경위생공학
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• 제15권4호
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• pp.27-27
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• 2000

In order to treat the dyeing wastewater, the UV/TiO₂/H₂O₂ system was investigated, and proper pretreatment methods were examined to reduce the load on the system considering economical and technical efficiency. The results of this study were as follows: 1.UV/TiO₂/H₂O₂ system with pretreatment process was adopted, the result of Chemical coagulation and pH control units was pH 11→ coagulation → pH 4 and the optimum dosage of FeCl₃ was 600㎎/ℓ 2. Proper dosage of TiO₂in the UV/TiO₂/H₂O₂ system with pretreatment process was 2g/ℓ and H₂O₂ was 1000㎎/ℓ, UV contact time was 20min to get below 200㎎/ℓ of $COD_{Cr}$

• 분석과학
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• 제13권2호
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• pp.234-240
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• 2000

수질계의 부식산을 화학적 산화처리하기 위한 방법의 하나로 광산화공정을 도입하여 부식산의 특성 변화를 조사하였다. 광산화공정은 UV단독, UV/$TiO_2$ 및 UV/$H_2O_2$ 시스템을 실험하였다. UV 단독 조사시 TOC 제거율은 pH 7-9에서 가장 높았으며, 흡광도는 강알카리성 영역에서 감소율이 향상된 결과를 보였다. 각 시스템별로 처리도를 보면, UV/$TiO_2$ 시스템의 경우 $TiO_2$ 의 농도가 50ppm 일때 TOC 제거와 흡광도 감소의 효율이 높았으며 50ppm 이상을 투입해도 처리율에 변화가 없었다. UV/$H_2O_2$ 시스템에서는 과산화수소의 농도가 20mM이 최적의 주입농도로 조사되었으며, 그 이상 투입할 경우 TOC와 흡광도의 처리율이 저하되었다. 탄산이온을 첨가할 경우, TOC 제거율 및 UV 흡광도의 감소율 모두 감소하며, TOC 제거율이 흡광도 감소율에 비해 상대적으로 더 크게 나타났다.

• 상하수도학회지
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• 제11권4호
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• pp.133-141
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• 1997

In order to treat the landfill leachate, $UV/TiO_2/H_2O_2$ system connected with biological treatment was investigated, and proper pretreatment methods were examined to reduce the load on the system considering economical and technical efficiency. It was more profitable to put $H_2O_2$ into the system in the early stage for the sample which was treated with $H_2SO_4$ to decrease alkalinity and with $FeCl_3-6H_2O$ flocculation. Because the required reaction time run up by increasing $H_2O_2$ input amount, though the COD was reduced slightly, the optimal $H_2O_2$ input amount should be determined for the desired COD and the economical efficiency. The appropriate way to get the lowest COD in the shortest time was the method to treat the sample which was controlled to pH 3.5 after adjusting to pH 12 and put 500 ppm $H_2O_2$ into the system. In that case, to increase $H_2O_2$ input amount was not profitable for the system efficiency. The sufficient photocatalytic excited time was required to reduce the photocatalytic decomposition time for the sample which was gone through the alkali state.