• 제목/요약/키워드: Photocatalytic decolorization

검색결과 27건 처리시간 0.031초

UV/$TiO_2$ 시스템을 이용한 Rhodamine B의 색도 제거 (Decolorization of Rhodamine B Using UV/$TiO_2$ System)

  • 박영식;나영수;안갑환
    • 한국환경보건학회지
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    • 제28권5호
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    • pp.59-64
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    • 2002
  • The photocatalytic decolorization of the Rhodamine B (RhB) was studied using a UV/TiO$_2$ reactor. Yakuri titanium dioxide(anatase) was used as the suspended photocatalyst and proved to be effective for decolorization irradiated with UV light (254 mm). The photocatalyzed dioxide concentrations, light intensity and air flow rates. In 0.01 mM RhB, color could be completely photodegraded after 3 hours. Absorption spectrum of an aqueous solution containing RhB showed a continued diminution of the RhB concentration in the solution bulk : concomitantly, no new absorption peaks appeared. This confirmed the decolorization of RhB, i.e., the break up of the chromopore. The optimum loaded titanium dioxide for the decolorization was 0.75 g/(equation omitted). The light intensity showed exponential decay with distance. The decay of light intensity of RhB solution showed different tendency from TiO$_2$. These results suggested that the photocatalytic decolorization of dyes may be available method for decolorizing in wastewater.

충전층 반응기와 고정화 TiO2/UV를 이용한 Rhodamine B의 광촉매 탈색 (Photocatalytic Decolorization of Dye Using Packed-bed Reactor and Immobilized TiO2/UV System)

  • 김동석;박영식
    • 한국환경과학회지
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    • 제16권3호
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    • pp.255-260
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    • 2007
  • The photocatalytic decolorization of Rhodamine B (RhB) was studied using packed-bed reactor and immobilized $TiO_2/UV$ System. The 20 W UV-A, UV-B and UV-C lamps were employed as the light source. The effect of shape and surface polishing extent of reflector, distance between the reactor and reflector, reactor material were investigated. The results showed that the order of the initial reaction constant with reflector shape was round > polygon > W > rhombus. The optimum distance between the reactor and reflector was 2 cm. The initial reaction constant of quartz reactor was 1.46 times higher than that of tile PVDF reactor.

UV/TiO2와 유동층 반응기를 이용한 안료의 광촉매 탈색 (Photocatalytic Decolorization of Dye usingUV/TiO2 and Fluidized Bed Reactor)

  • 박영식
    • 한국환경과학회지
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    • 제13권10호
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    • pp.921-928
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    • 2004
  • The photocatalytic decolorization of Rhodamine B (RhB) was studied using immobilized $TiO_2$ and fluidized bed reactor. Immobilized $TiO_2$(length: 1$\~$2 mm, width: 1$\~$3 mm, thickness: 0.5$\~$2 mm) onto silicone sealant was employed as the photocatalyst and a 30 W germicidal lamp was used as the light source and the reactor volume was 4.8 L. The effects of parameters such as the amounts of photocatalyst, initial concentration, initial pH, superficial velocity, $H_2O_2$ and anion additives. ($NO_3^{-},\;SO_4^{2-},\;Cl^{-},\;CO_3^{2-}$) The results showed that the optimum dosage of the immobilized $TiO_2$ were 87.0 g/L. Initial removal rate of RhB of the immobilized $TiO_2$ was 1.5 times higher than that of the powder $TiO_2$ because of the adsorption onto the surface of immobilized $TiO_2$ In the conditions of acidic pH, initial reaction rate was increased slowly and reaction time was shorted. The effect of anion type on the reaction rate was not much.

광측매반응에 의한 Reactive Black 5의 색도제거 연구 (Decolorization of Reactive Black 5 by Photocatalytic Oxidation)

  • 양정목;송진수;박철환;김상용
    • 청정기술
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    • 제14권3호
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    • pp.211-217
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    • 2008
  • 본 연구에서는 광촉매 산화반응을 이용한 반응성염료(Reactive Black 5)의 오염부하 저감율(TOC, 색도 제거율)을 조사하였다. 광촉매 반응활성의 주요한 인자로서 염료농도, $TiO_2$ 주입량 및 pH조건을 최적화하였으며, 실험에 적용된 최적의 조건은 각각 100 mg/L, 2g/L, pH 4.9였다. 용존산소의 경우에는 산소의 농도가 증가함에 따라 처리속도도 함께 증가하였다. 새로운 $TiO_2$를 적용한 경우와 MF 세라믹 분리막에 의해 재생된 $TiO_2$를 각각 적용하여 실험한 결과 색도 제거율과 처리속도에는 약간의 차이를 보였으나, 반응 전반에는 영향을 주지 않았다.

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Surface Modification Reaction of Photocatalytic Titanium Dioxide with Triethoxysilane for Improving Dispersibility

  • Lee, Myung-Jin;Kim, Ji-Ho;Park, Young-Tae
    • Bulletin of the Korean Chemical Society
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    • 제31권5호
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    • pp.1275-1279
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    • 2010
  • We have carried out the surface modification of photocatalytic $TiO_2$ with triethoxysilane through dehydrogenation reaction and characterized the modified photocatalyst by spectroscopic methods, such as FT-IR, solid-state $^{29}Si$ MAS NMR, XPS, and XRF, etc. We also examined photocatalytic activity of the immobilized photocatalytic titanium dioxide with triethoxysilane by decolorization reaction of dyes such as cong red and methylene blue under visible light. Dispersion test showed that the photocatalytic titanium dioxide immobilized with triethoxysilane group has kept higher dispersibility than titanium dioxide itself. No appreciable precipitation takes place even after standing for 24 h in the 4:6 mixture ratio of ethanol and water.

스펀지에 고정한 광촉매를 이용한 안료의 탈색 (Decolorization of Dye Using Immobilized Photocatalyst onto Sponge)

  • 김동석;박영식
    • 한국환경보건학회지
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    • 제31권5호
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    • pp.415-422
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    • 2005
  • The photocatalytic decolorization of Reactive Red 2B(RR2B) was studied using immobilized photocatalyst/UV System. Two pairs of 20 W UV-B and UV-C lamps were employed as the light source. Immobilization of $TiO_2$ was carried out using sponge (as the photocatalyst body) and silicone sealant(as the binder). The effects of parameters such as the thickness, pore size of sponge photocatalyst and attached material on the reactor bottom were investigated. The results showed that the optimum thickness of sponge photocatalyst was 1 cm. Decolorization of reactor which had the bottom coated $TiO_2$ was higher than that of reactor attached aluminum plate. Decolorization of photocatalyst with large pore size(mean pore size, 3.8 mm) was higher than that of the small(mean pore size, 1.75 mm). Initial decolorization of RR2B could be descrived using the Langmuir-Hinshelwood(L-H) model and gave constant values of $0.55mg/l{\cdot}min(k)\;and\;2.65{\times}10^{-2}l/mg(K)$, respectively.

회전원판 광촉매 반응기(Rotating Disk Photocatalytic Reactor)를 이용한 Rhodamine B의 색 제거 (Decolorization of Rhodamine B using Rotating Disk Photocatalytic Reactor)

  • 박영식
    • 한국물환경학회지
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    • 제21권1호
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    • pp.46-51
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    • 2005
  • The photocatalytic oxidation of Rhodamine B (RhB) was studied using immobilized $TiO_2$ and rotating disk photocatalytic reactor. Immobilized $TiO_2$ onto the surface of the aluminum plate was employed as the photocatalyst and two 20 W germicidal lamps and two 20 W UV-BLB lamps were used as the light source and the reactor volume was 1.0 L. The effects of parameters such as the number of rotating disk, rpm of rotating disk, the number of coating, $H_2O_2$ and photo-fenton amounts, and the concentrations of anions and cations ($NO_3{^-}$, $SO_4{^{2-}}$, $Cl^-$, $Ca^{2+}$, $Zn^{2+}$, $Na^+$) were examined.

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

  • 김동석;박영식
    • 한국환경과학회지
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    • 제17권9호
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    • pp.1023-1032
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    • 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.

염료폐수 용액의 광축매-광화학 반응 (Photocatalytic-Photochemical Reaction of Wastewater Dyes in aqueous Solution)

  • 김삼혁;최칠남;정오진
    • 한국환경과학회지
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    • 제8권2호
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    • pp.241-248
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    • 1999
  • The photocatalytic decolorization and photodegradation of wastewater contamininated with dyes such as methyleneblue tetrahydrate(MBT), methyl orange(MO), phenol red(PR) and the mixed dyes have been studied using a batch reactor in the presence of aerotropic and titania. Degussa P25 titanium oxide was used as the photocatalyst and proved to be effective for the dyes-degradation when irradiated with UV-light source emitting the wavelength of 253.7 nm in the presence of air. In addition to removing the color from the wastewater, the photocatalytic reaction simultaneously reduced the COD and optical density which suggests that the dissolved organic compounds have been photooxidized. The reaction rate of disappearance of the dyes were measured as a function of the irradiation times. The photooxidative procedure of the aquatic solution have the first order reaction-kinetics. The rate constants were increased in the order of PR < MBT < $gL^{-1}-TiO_2$ powder were irradiated with the UV -light source.

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GF/C에 고정된 TiO2와 유동층 반응기를 이용한 Rhodamine B의 광촉매 탈색 (Photocatalytic Decolorization of Rhodamine B using Immobilized TiO2 onto GF/C and Fluidized Bed Reactor)

  • 박영식;안갑환
    • 한국환경과학회지
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    • 제12권12호
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    • pp.1277-1284
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    • 2003
  • The photocatalytic oxidation of Rhodamine B (RhB) was studied using immobilized TiO$_2$ and fluidized bed reactor. Immobilized TiO$_2$ onto GF/C was employed as the photocatalyst and a 30 W germicidal lamp was used as the light source and the reactor volume was 4.8 L. The effects of parameters such as the amounts of photocatalyst, initial concentration, initial pH, air flow rate and anion additives (NO$_3$$\^$-/, SO$_4$$\^$2-/, Cl$\^$-/, CO$_3$$\^$2-/) competing for reaction. The results showed that the optimum dosage of the immobilized TiO$_2$ was 40.0 g/L. Initial removal rate of immobilized TiO$_2$ was expressed Langmuir - Hinshelwood equation.