• 상하수도학회지
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• 제21권4호
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• pp.445-452
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• 2007

This study was carried out to examine effect of post-chlorine dosage reduction by ozonation and GAC process in the field plant for 3years in the "G" water purification plant in Seoul. And it is to compare GAC with BAC process in removal effects of TOC, THMs, THMFP, $UV_{254}$. As a result, chlorine dosage of ozonation and GAC(=BAC) is less demand than GAC. Seasonal reduction of chlorine demand is from about 37% to 59% with BAC, and from 24 to 46% with GAC. Higher reduction in BAC could be achieved. The efficiency of chlorine demand reduction with ozonation was depending on the organic carbon removal. $UV_{254}$ concentration is less about 0.13~0.74L/mg.m in BAC than GAC. Therefore, the combination of ozonation and GAC was more effective in reducing post-chlorine than the single GAC. TOC was also monitored, and results show that a linear relationship between TOC and chlorine demand is appropriate under each treatment process. It means that removal of organic matter(TOC) from finished water is necessary to reduce post-chlorine dosage in clear well and to minimize order of chlorine in distribution systems.

• 대한환경공학회지
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• 제22권3호
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• pp.505-510
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• 2000

본 연구는 부영양화시 다량 발생하고, 독소생성의 주원인 종으로 알려진 Microcystis aeruginosa의 정수처리 중 응집공정에서 전염소처리의 영향을 조사하였다. Microcystis aeruginosa를 실험실에서 배양하여, $10^5cell/mL$가 되도록 인공시료를 만들었다. 전염소처리의 염소주입량은 각각 0.2, 1.0, 10 mg-Cl/L으로 하였고, 반응시간은 1시간과 1분으로 하였다. 응집 후 모든 시료의 탁도는 응집제를 0.4 mg-Al/L 주입한 후 매우 낮게 나타났으므로 탁도 유발물질은 염소주입량에 의한 영향이 매우 낮은 것으로 나타났다. 염소량이 증가함에 따라 응집 후 잔류알루미늄은 감소하였고, $UV_{254}$는 증가하였다. 적당한 염소농도(1.0 mg-Cl/L)에서는 반응시간이 길어짐에 따라 $UV_{254}$가 증가하였다.

• 상하수도학회지
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• 제21권2호
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• pp.195-201
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• 2007

A submerged flat-sheet membrane separation system integrated with PAC (powdered activated carbon) was used in this research in order to investigate the effects of PAC on the efficiencies of operation and treatment and to evaluate the performance of the system. The experiments were carried out under operating conditions of a filtration rate of 0.38 m/d, water temperature of $20-28^{\circ}C$, and PAC dose of 0 g/L (Run-A) and 20 g/L (Run-B). The influent concentrations of TOC (total organic carbon), $NH_4{^+}-N$ (ammonia nitrogen) and $UV_{254}$ (UV absorbance at 254 nm) were 2.48 mg/L, 1.4 mg/L and 2.53 1/m, respectively. TOC removal of 43.2 and 73.6%, ammonia nitrogen removal of 4.9 and 15.9%, and $UV_{254}$ removal of 20.6 and 31.6% were obtained for Run-A and Run-B, respectively. During an experimental period of 33 days, no change was found in TMP (Run-B), but the TMP in Run-A increased by 5 kPa after 29 days. This research showed that the filtrate quality and the performance efficiency were enhanced when PAC was introduced into the filtration system.

• 한국환경과학회지
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• 제11권9호
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• pp.955-960
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• 2002

The recycled washwater, which has different water quality and is produced about 5 to 20% of the total water volume treated, affects the unit operation of water treatment, especially coagulation process. However, the effects of recycled washwater on unit operation of water treatment have not been fully investigated. In this study, effects of recycled washwater on coagulation process were investigated to find the optimum coagulation condition by analyzing turbidity, $UV_{254}$, TOC removal efficiencies. In addition, effects of recycled washwater on residual Al after coagulation were studied by analyzing soluble and particulate Al. The size distribution and fractal dimension of coagulated also analyzed. The recycled washwater was lower pH than the raw water. And the recycled washwater had higher $UV_{254}$, TOC and residual Al concentration than the raw water. Residual Al concentration of recycled washwater was about 50 times higher than that of raw water. Optimum coagulant dosages on the blending recycled washwater and the raw water for turbidity, $UV_{254}$ and Al removal were lower than that on the raw water. However, TOC removal increased by increasing coagulant dosage. The size and fractal dimension of coagulated particle produced in the blending recycled washwater were larger, which imply faster settling velocity, than those produced in the raw water only.

• 한국환경과학회지
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• 제22권8호
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• pp.999-1007
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• 2013

Electrochemical degradation of phenol was evaluated at DSA (dimensionally stable anode), JP202 (Ru, 25%; Ir, 25%; other, 50%) electrode for being a treatment method in non-biodegradable organic compounds such as phenol. Experiments were conducted to examine the effects of applied current (1.0~4.0 A), electrolyte type (NaCl, KCl, $Na_2SO_4$, $H_2SO_4$) and concentration (0.5~3.0 g/L), initial phenol concentration (12.5~100.0 mg/L) on phenol degradation and $UV_{254}$ absorbance as indirect indicator of by-product degraded phenol. It was found that phenol concentration decreased from around 50 mg/L to zero after 10 min of electrolysis with 2.5 g/L NaCl as supporting electrolyte at the current of 3.5 A. Although phenol could be completely electrochemical degraded by JP202 anode, the degradation of phenol COD was required oxidation time over 60 min due to the generation of by-products. $UV_{254}$ absorbance can see the impact of as an indirect indicator of the creation and destruction of by-product. The initial removal rate of phenol is 5.63 times faster than the initial COD removal rate.

• 한국환경과학회지
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• 제22권7호
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• pp.915-923
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• 2013

Decomposition of non-biodegradable contaminants such as phenol contained in water was investigated using a dielectric barrier discharge (DBD) plasma reactor in the aqueous solutions with continuous oxygen bubbling. Effects of various parameters on the removal of phenol in aqueous solution with high-voltage streamer discharge plasma are studied. In order to choose plasma gas, gas of three types (argon, air, oxygen) were investigated. After the selection of gas, effects of 1st voltage (80 ~ 220 V), oxygen flow rate (2 ~ 7 L/min), pH (3 ~ 11), and initial phenol concentration (12.5 ~ 100.0 mg/L) on phenol degradation and change of $UV_{254}$ absorbance were investigated. Absorbance of $UV_{254}$ can be used as an indirect indicator of phenol degradation and the generation and disappearance of the non-biodegradable organic compounds. Removal of phenol and COD were found to follow pseudo first-order kinetics. The removal rate constants for phenol and COD of phenol were $5.204{\times}10^{-1}min^{-1}$ and $3.26{\times}10^{-2}min^{-1}$, respectively.

• 대한의용생체공학회:의공학회지
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• 제17권4호
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• pp.479-490
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• 1996

To utilize collagen as an implantable biomateriall the mcct widely used bovine skin origin Type I collagen was investigated Pepsin treated, Type I atelocollagen was extracted and crosslinked by the ultraviolet(W) ray with wavelength of 254nm or by various concentrations of glutaraldehyde to produce collagen membranes. The crosslink rates of the specimens were observed by a polarized light microscope, a scanning electron microscope, and a Fourier transform infrared (FT-lR) spectrometer. The followings are concluded 1. The collagen membranes produced by both 2.5% glutaraldehyde solution and 254nm UV ray irra- diation demonstrated similar morphologies on polarized light microscopic and scanning electron microscopic views. 2. The chemical structures of the crosslinked membranes by glutaraldehyde over 2.5% in concentrations revealed similar intensities to that of the UV ray irradiated one in FT-lR investigation. 3. To obtain optimal croulink in bovine stalin origin Type I atelocollagen, 2.5% glutaraldehyde solution or UV ray irradiation with 254nm wavelength is acceptable.

• 상하수도학회지
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• 제19권3호
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• pp.323-329
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• 2005

Advanced processes such as ozonation or activated carbon filtration (ACF) in water treatment plants have been used in Korea since 1994. At present, seventeen drinking water treatment plants are currently operating. This survey compares the treatment performance of advanced processes in eight plants which have comparable water quality data. The three parameters (DOC, $UV_{254}$, and $KMnO_4$ consumption) of water quality were selected as an indicator of treatment efficiency. The treatment efficiency of ozonation and ACF processes was found to vary with large deviations in each plant. Treatment efficiency of DOC, $UV_{254}$, and $KMnO_4$ consumption by post ozonation ranged from 3 to 11%, 6 to 33%, and 12 to 28% respectively. On the other hand, for ACF, treatment efficiency of DOC, $UV_{254}$, and $KMnO_4$ consumption ranged from 7 to 38%, 8 to 48%, and 16 to 66% respectively. These large deviations indicate the advanced processes of water treatment plants to be further optimized.

• 한국방재학회 논문집
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• 제11권2호
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• pp.179-183
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• 2011

본 연구에서는 광 반응기 내부의 영향반경을 평가하기 위해 자외선(UV-C) 램프의 강도와 photochemical에 의한 OH 라디칼 생성량을 측정하였다. 또한 $TiO_2$ (Degussa P-25)를 농도별로 첨가하여 자외선 램프의 영향반경을 측정하였다. 광 반응기는 아크릴 재질의 bath 타입을 사용하였고, 254 nm의 파장을 가진 UV-C 자외선 램프를(SANKYO DENKI, 지름 : 2.2 cm, 길이 : 18.5 cm) 사용하였다. 램프의 소비전력은 10.5 W이고, OH 라디칼 생성량을 측정하기 위해 KI dosimetry를 사용하였다. 실험 결과로부터 광 반응기에서 자외선의 강도가 0.367 mW/$cm^2$이상 조사되어야하고, 거리는 13 cm 이내에서 OH 라디칼 생성에 영향을 미치는 것으로 나타났다. 또한 광촉매 반응기에서는 촉매의 농도로 인해 자외선의 영향반경이 매우 감소하는 것을 확인할 수 있었다.

• 대한화학회지
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• 제37권4호
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• pp.453-461
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• 1993

테프론 코일과 저압 수은 램프를 사용, 간단하게 제작된 광화학 반응기를 이용한 HPLC 검출 방법을 연구하였다. 4종의 티오카바메이트 시료들을검출함에 있어 UV, 형광 및 전기화학 검출기 등에서 광화학 반응을 통한 액체 크로마토그래피 후컬럼 검출법의 유용성을 알아보았다. 액체 크로마토그래피를 통해 분리된 티오카바메이트류에 254nm의 UV을 조사할 경우 4종의 시료는 모두 광반응이 일어나 형광을 통해 분리된 티오카바메이트류에 254nm의 UV을 조사할 경우 4종의 시료는 모두 광반응이 일어나 형광을 나타내거나, 전기화학 검출기에 큰 검출 응답을 나타내었다. UV 검출법의 경우 광반응 생성물은 광반응전보다 검출감도는 감소하였으나 장파장쪽에서 검출이 용이하였다. 형광 검출법의 경우 광반응전 4종의 티오카바메이트는 전혀 검출되지 않았으나, 광반응 후 MPTC,CPTC는 Ph 4.0, 50% 아세토니트릴 이동상 조건에서 5.0~9.3ng의 검출한계를 나타내었다. 전기화학 검출법에서는 광반응전 시료가 매우 작은 검출 응답을 보였고, 광반응 후 시료는 5~20배 이상의 검출감도가 증대되었으며 13.3~0.02ng의 검출한계를 나타내었다. 이때 최적 검출조건은 50% 아세토니트릴 $-0.5{\times}10^{-2}$ M 인산 완충용액, pH 7.0 이었다. 또한 티오카바메이트의 광반응물과 OPA-MERC를 반응 코일내에 유도체를 형성시켜 형광검출기로 검출해냄으로써 광분해물에서 1차 아민이 생성됨을 알 수 있었다.