• 제목/요약/키워드: $TiO_2$/UV Process

검색결과 195건 처리시간 0.027초

오존, 광촉매 및 오존-복합 공정을 이용한 Rhodamine B의 색도와 COD 제거 (Color and COD Removal of Rhodamine B Using Ozone, Photocatalyst and Ozone-Complex Process)

  • 김동석;박영식
    • 대한환경공학회지
    • /
    • 제29권6호
    • /
    • pp.662-669
    • /
    • 2007
  • Rhodamine B(RhB) 폐수의 색도와 COD 제거를 위해 $O_3$, $UV/TiO_2$, $O_3/UV$$O_3/UV/TiO_2$ 공정과 같은 고급산화법의 영향을 연구하였다. 오존 공정의 경우 오존 농도가 높을수록 탈색속도가 높아졌으며, $UV/TiO_2$$O_3/UV/TiO_2$ 공정의 최적 $TiO_2$ 농도는 0.4 g/L 였다. $O_3/UV$ 공정은 오존 공정에 비해 초기 탈색속도상수가 높고 탈색종결시간도 줄어드는 것으로 나타났다. 실험에 적용한 공정의 초기 탈색속도상수의 순서는 $O_3/UV/TiO_2>O_3/UV>O_3>UV/TiO_2$로 나타났다. 모든 공정의 탈색속도가 COD로 표시한 무기화 속도보다 빠르고, COD는 처리에 시간이 더 소요되는 것으로 나타났다. COD 제거속도는 $O_3/UV/TiO_2>O_3/UV>UV/TiO_2{\geqq}O_3$의 순서로 나타났다. 네 공정 중에서 광촉매와 오존 공정을 조합한 $O_3/UV/TiO_2$ 공정이 염료 폐수와 같은 폐수의 색도와 COD 제거에 적절한 것으로 나타났다.

UV/TiO2/H2O2 공정을 이용한 휴믹산과 중금속 제거 (The Removal of Humic Acid and Heavy Metals Using UV/TiO2/H2O2)

  • 김종오;정종태;최원열
    • 한국지반환경공학회 논문집
    • /
    • 제7권4호
    • /
    • pp.5-13
    • /
    • 2006
  • 본 연구는 지표수에서 휴믹산을 포함한 중금속을 제거하기 위해 $UV/TiO_2/H_2O_2$ 공정을 적용하여 각 실험인자에 대한 처리효율을 실험적으로 검토하였다. 휴믹산과 중금속을 제거하는데 있어 $UV/TiO_2/H_2O_2$ 공정은 $UV/TiO_2$ 공정보다 훨씬 더 높은 제거효율을 보여 주었다. $TiO_2$ 주입량과 UV 세기를 증가시킴에 따라 휴믹산과 중금속 제거율은 증가했다. 그러나 0.3 g/L 이상의 $TiO_2$ 주입량에서는 제거율이 감소했다. 산화제로 사용된 과산화수소의 첨가는 휴믹산과 중금속 제거에 있어 긍정적인 효과를 보여주었으며 특히 50 mg/L의 과산화수소 농도에서 가장 좋은 제거효율을 나타내었다.

  • PDF

광산화시스템을 이용한 염색폐수의 유기물 처리효율 및 잔류미생물의 독성 평가 (Organic Removal Efficiency and Toxicity Evaluation of Persistent Microorganism from Dye Wastewater Treatment using a Photooxidation system)

  • 정호준;이동석
    • 산업기술연구
    • /
    • 제29권A호
    • /
    • pp.83-88
    • /
    • 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.

  • PDF

고급산화공정에 의한 안료폐수 처리: 비교 연구 (Degradation of Dye Wastewater by Advanced Oxidation Process: A Comparative Study)

  • 박영식
    • 한국환경과학회지
    • /
    • 제15권1호
    • /
    • pp.67-75
    • /
    • 2006
  • The degradation of Rhodamine B (RhB) in water was investigated in laboratory-scale experiments, using five advanced oxidation Processes (AOPs) $UV/H_2O_2$, lenten, photo-lenten, $UV/TiO_2,\;UV/TiO_2/H_2O_2$. The photodegradation experiments were carried out in a fluidized bed photoreactor equipped with an immersed 32 W UV-C lamp as light source. initial decolorization rate and COD removal efficiency were evaluated and compared. The results obtained showed that the initial decolorization rate constant was quite different for each oxidation process. The relative order of decolorization was: photo-fenton > $UV/TiO_2/H_2O_2$ > fenton > $UV/H_2O_2$ > $UV/TiO_2$ > UV > $H_2O_2$. The relative order of COD removal was different from decolorization: photo-fenten ${\fallingdotseq}$ $UV/TiO_2/H_2O_2\;>\;UV/TiO_2\;>\;fenton\;>\;UV/H_2O_2$. The Photo-lenten and $UV/TiO_2/H_2O_2$ processes seem to be appropriate for decolorization and COD removal of dye wastewater.

자외선 활성화 원자층 성장 기술을 이용한 상온에서 TiO2 박막의 제조 (Fabrication of TiO2 Thin Films Using UV-enhanced Atomic Layer Deposition at Room Temperature)

  • 이병훈;성명모
    • 한국진공학회지
    • /
    • 제19권2호
    • /
    • pp.91-95
    • /
    • 2010
  • 상온에서 고품질의 $TiO_2$ 박막을 제조하기 위하여 titanium isopropoxide [Ti(OCH$(CH_3)_2)_4$, TIP]와 $H_2O$을 이용한 자외선 활성화 원자층 증착(UV-enhanced atomic layer deposition: UV-ALD) 기술을 개발하였다. UV-ALD 기술은 상온에서 자체제어 표면 반응(self-limitting surface reaction)을 통해 균일하고 고품위 등방 특성을 갖는 순수한 $TiO_2$ 박막 증착이 가능하였다. ALD 반응 시 조사되는 자외선은 Si 기질 위에 우수한 접착력을 가지는 고품질의 $TiO_2$ 박막을 얻는데 효과적이었다. UV-ALD 기술은 높은 단차비(aspect ratio)를 가지는 trench 기질 위에 균일한 $TiO_2$ 박막을 증착하는 데에 적용되었다.

$TiO_2/H_2O_2/UV$ 공정을 이용한 염색폐수처리에 관한 연구 (A Study on the Treatment of Dyeing Wastewater Using $TiO_2/H_2O_2/UV$ Processes)

  • 조일형;정효준;박경렬;성기석;이용규;이홍근
    • 환경위생공학
    • /
    • 제15권4호
    • /
    • pp.26-34
    • /
    • 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 $COD_{Cr}$.

  • PDF

광전기촉매 공정과 전기/UV 공정을 이용한 Rhodamine B의 색 제거 (Decolorization of a Rhodamine B Using Photoelectrocatalytic and Electrolytic/UV Process)

  • 김동석;박영식
    • 한국환경과학회지
    • /
    • 제17권9호
    • /
    • pp.1023-1032
    • /
    • 2008
  • The feasibility study of the application of the photoelectrocatalytic and electrolytic/UV decolorization of Rhodamine B (RhB) was investigated in the photoelectrocatalytic and electrolytic/UV process with $TiO_2$ photoelectrode and DSA (dimensionally stable anode) electrode. Three types of $TiO_2$ photoelectrode were used. Thermal oxidation electrode (Th-$TiO_2$) was made by oxidation of titanium metal sheet; sol-gel electrode (5G-$TiO_2$) and powder electrode (P-$TiO_2$) were made by coating and then heating a layer of titania sol-gel and slurry $TiO_2$ on titanium sheet. DSA electrodes were Ti and Ru/Ti electrode. The relative performance for RhB decolorization of each of the photoelecoodes and DSA electrodes is: Ru/Ti > Ti > SG-$TiO_2$ > Th-$TiO_2$. It was observed that photoelectrocatalytic decolorization of RhB is similar to the sum of the photocatalytic and electrolytic decolorization. Therefore the synergetic effect was not showed in pthotoelectrocatalytic reaction. $Na_{2}SO_{4}$ and NaCl showed different decolorization effect between pthotoelectrocatalytic and electrolytic/UV reaction. In the presence of the NaCl, RhB decolorization of Ru/Ti DSA electrode was higher than that of the other photoelectrode and Ti electrode. Optimum current, NaCl dosage and UV lamp power of the electrolytic/UV process (using Ru/Ti electrode) were 0.75 A, 0.5 g/L and 16 W, respectively.

4-nonylphenol의 오존산화 처리반응에 관한 연구 (A Study on Ozonation of 4-nonylphenol)

  • 이철규
    • 한국물환경학회지
    • /
    • 제33권6호
    • /
    • pp.736-743
    • /
    • 2017
  • In this study, 4-nonylphenol (4-NP), an endocrine disrupting chemical, was removed by ozone treatment processes under the various experimental conditions including UV irradiation, $TiO_2$ addition. The ozone flow rate and concentration were maintained at $1.0L{\cdot}min^{-1}$ and $70{\pm}5mg{\cdot}L^{-1}$. The pH, COD and TOC of the samples were obtained every 10 minutes for 60 minutes in laboratory scale batch reactor. We found that the combination of UV irradiation and $TiO_2$ addition for ozonation improves the removal efficiency of COD and TOC in 4-NP aqueous solution. In case of the $O_3/UV/TiO_2$ system, COD and TOC were greatly reduced to 85.3 ~ 94.0% and 89.2 ~ 97.2%, respectively. 4-NP degradation rate constants, $k_{COD}$ and $k_{TOC}$, were calculated based on the COD and TOC values. Significantly, $k_{COD}$ and $k_{TOC}$ were improved in the $O_3/UV/TiO_2$ treatment process compared with single $O_3$ process, because the oxidation and the mineralization of 4-NP were increased by generating of the hydroxyl radical. The $k_{COD}$ and $k_{TOC}$ were obtained to be $5.81{\times}10^{-4}{\sim}10.8{\times}10^{-4}sec^{-1}$ and $11.9{\times}10^{-4}{\sim}19.4{\times}10^{-4}sec^{-1}$ in the $O_3/UV/TiO_2$ process. Activation energy ($E_a$) of ozone oxidation reaction based on $k_{COD}$ and $k_{TOC}$ were increased in order of $O_3/UV/TiO_2$ < $O3/UV$ < $O_3/TiO_2$ < $O_3$ process. It was confirmed that the addition of $TiO_2$ and UV irradiation to the ozone oxidation reaction significantly reduced the $E_a$ value and the degradation of 4-NP.

TiO₂/H₂O₂/UV 공정을 이용한 염색폐수처리에 관한 연구 (A Study on the Treatment of Dyeing Wastewater Using TiO₂/H₂O₂/UV Processes)

  • 조일형;정효준;박경렬;성기석;이용규;이홍근
    • 환경위생공학
    • /
    • 제15권4호
    • /
    • pp.27-27
    • /
    • 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 $COD_{Cr}$

운전조건에 따른 O3/UV, TiO2/UV 및 O3/TiO2/UV 시스템의 BTEX 증기처리에 관한 비교 연구 (A Comparative Study on Degradation of BTEX Vapor by O3/UV, TiO2/UV, and O3/TiO2/UV System with Operating Conditions)

  • 김경진;박옥현
    • 한국대기환경학회지
    • /
    • 제24권1호
    • /
    • pp.91-99
    • /
    • 2008
  • A multilayer tower-type photoreactor, in which $TiO_2$-coated glass-tubes were installed, was used to measure the vapor-phase BTEX removal efficiencies by ozone oxidation ($O_3$/UV), photocatalytic oxidation ($TiO_2$/UV) and the combination of ozone and photocatalytic oxidation ($O_3/TiO_2$/UV) process, respectively. The experiments were conducted under various relative humidities, temperatures, ozone concentrations, gas flow rates and BTEX concentrations. As a result, the BTEX removal efficiency and the oxidation rate by $O_3/TiO_2$/UV system were highest, compared to $O_3$/UV and $TiO_2$/UV system. The $O_3/TiO_2$/UV system accelerated the low oxidation rate of low-concentration organic compounds and removed organic compounds to a large extent in a fixed volume of reactor in a short time. Therefore, $O_3/TiO_2$/UV system as a superimposed oxidation technology was developed to efficiently and economically treat refractory VOCs. Also, this study demonstrated feasibility of a technology to scale up a photoreactor from lab-scale to pilot-scale, which uses (i) a separated light-source chamber and a light distribution system, (ii) catalyst fixing to glass-tube media, and (iii) unit connection in series and/or parallel. The experimental results from $O_3/TiO_2$/UV system showed that (i) the highest BTEX removal efficiencies were obtained under relative humidity ranging from 50 to 55% and temperature ranging from 40 to $50^{\circ}C$, and (ii) the removal efficiencies linearly increased with ozone dosage and decreased with gas flow rate. When applying Langmuir-Hinshelwood model to $TiO_2$/UV and $O_3/TiO_2$/UV system, reaction rate constant for $O_3/TiO_2$/UV system was larger than that for $TiO_2$/UV system, however, it was found that adsorption constant for $O_3/TiO_2$/UV system was smaller than that for $TiO_2$/UV system due to competitive adsorption between organics and ozone.