• 제목/요약/키워드: Pigment wastewater

검색결과 13건 처리시간 0.021초

감마선 처리가 섬유와 안료폐수의 생물독성에 미치는 영향 (Effect of Gamma-ray Treatment on Toxicity of Textile and Pigment Wastewaters)

  • 김은애;조훈제;박은주;김효진;김정규;정진호
    • 한국물환경학회지
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    • 제22권1호
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    • pp.145-149
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    • 2006
  • Textile and pigment wastewater samples collected from an industrial complex showed toxic effect on Daphnia magna. For textile wastewater, 48 h acute toxicity of effluent was not detected while toxic unit (TU) of influent was 1.79. The toxicity of influent was completely disappeared by gamma-ray treatment at 10 kGy or by suspended solids (SS) removal. In case of pigment wastewater, both influent and effluent were toxic to D. magna though the effluent satisfied current water quality standards. Gamma-ray treatment had little effect on the toxicity reduction of pigment wastewater since the toxicity was mainly caused by metal ions, in particular, Cr(VI). This work suggests the bioassay technique for monitoring adverse effects of wastewater should be introduced, and also shows the usefulness of gamma-rays as an advanced treatment technique for textile wastewater.

세라믹 담체를 이용한 안료폐수의 호기성처리 (Aerobic Treatment of Pigment Wastewater using Ceramic Support Carrier)

  • 박영식;안갑환
    • 한국환경과학회지
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    • 제10권4호
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    • pp.281-286
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    • 2001
  • Wastewater from the pigment industry has high levels of organics and is known as hardly biodegradable. The objective of this study is to evaluate the applicability of aerobic fixed-bed boifilm reactor packed with ceramic support carrier for the pigment wastewater treatment. Orange 2(widely used azo pigment) adsorption experiment onto biofilm and activated sludge, and continuous treatment experiments were performed. In batch adsorption experiment, maximum adsorption quantity of biofilm was at least two times higher than that of activated sludge. In continuous experiment using aerobic fixed-bed biodilm reactor, the influent concentration of COD and Orange 2 were 75~500mg/${\ell}$(0.45~3.00kg COD/$m^3.day), 5~50mg/$\ell$(0.03~0.30kg Orange 2/$m^3$.day), respectively. At a COD loading rate 2.5kg COD/$m^3$.day and Orange 2 loading rate of 0.18kg Orange 2/$m^3$.day, removal efficiency of COD and Orange 2 were over 95%, 97%, respectively.

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PAC-A/O 공정을 이용한 안료폐수의 질소 제거 특성 (Nitrogen removal characteristics of pigment wastewater using PAC-A/O process)

  • 정종식
    • 상하수도학회지
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    • 제32권1호
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    • pp.19-25
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    • 2018
  • The objectives of this study were to evaluate the removal characteristics of total nitrogen, the influence factor of denitrification and the optimum operating condition in the pigment wastewater treatment using PAC-A/O process. The operating conditions of PAC-A/O process were mean BOD volumetric loading $0.86kgBOD/m^3/day$, mean F/M ratio 0.072~0.13 kgBOD/kgMLVSS/day and mean C/N ratio 3.47, respectively. The conditions of anoxic process in the field plant test were mean pH 8.3~8.7 and mean temperature $34.1{\sim}44.0^{\circ}C$. The ORP bending point knee was eventually appeared in the ORP -107 mV and $NO_3{^-}-N$ removal efficiency was increased according to the ORP decrease. In the ORP -107 mV below condition, the removal efficiency of T-N and $NO_3{^-}-N$ was 92.3~95.0% and 98.5~99.7%. Denitrification rate was calculated to be 1.581~1.791 mg $NO_3{^-}-N/gMLSS/hr$. The experimental results showed that the ORP control in the PAC-A/O process could be an effective method for treatment of pigment wastewater.

Combination of Sequential Batch Reactor (SBR) and Dissolved Ozone Flotation-Pressurized Ozone Oxidation (DOF-PO2) Processes for Treatment of Pigment Processing Wastewater

  • Kim, Jeong-Hyun;Kim, Hyung-Suk;Lee, Byoung-Ho
    • Environmental Engineering Research
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    • 제16권2호
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    • pp.97-102
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    • 2011
  • This study investigates the treatment of pigment wastewater using a sequential batch reactor (SBR) followed by dissolved ozone flotation-pressurized ozone oxidation treatement (DOF-$PO_2$). The process efficiency has been evaluated at the lab scale on the basis of water quality parameters. In addition, the effect of pure oxygen and air was investigated on the removal of COD, BOD, and TN in the SBR process. It was observed that under comparable conditions the removal efficiencies of these water quality parameters using pure oxygen and air were similar. The effect of the recycle rate was also investigated for its impact on the water quality parameters using different ozone dissolving pressures in a DOF process in order to optimise conditions. The results conclude that the use of an SBR and ozone contact by DOF-$PO_2$ is a highly effective treatment for pigment wastewater and aids in the achievement of effluent discharge criteria.

안료폐수의 탈색연구 (Color Removal of the Wastewater containing the Pigml:mts using Wastewater Treatment Technologies)

  • 이병규;조성웅
    • 대한환경공학회지
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    • 제22권3호
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    • pp.429-439
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    • 2000
  • Lake Red C(바롬) 계열 및 Lithol Rubine(칼슘) 계열의 안료나 이들의 혼합물이 포함된 안료폐수에 대하여 여러 가지 폐수처리 및 탈색기법을 적용하였다. 우선, 오존처리법에서는 전체적으로 오존주입량 증가에 따른 폐수의 $COD_{Mn}$ 감소는 다소 있었지만 일부의 Lithol Rubine 계열을 제외하고는 탈색효과는 아주 미미하였다. Fenton 산화법 및 전기분해법의 적용에 있어서는 폐수시료 모두 좋은 $COD_{Mn}$ 감소효과가 있었고 일부의 Lithol Rubine 계열 안료폐수의 색깔제거 효과도 관찰되었다. UF와 RO를 이용한 막분리법의 적용에서는, UF 자체만 적용한 여기에 경우에도 상당한 $COD_{Mn}$ 제거효과가 있었고, 약간의 색깔 제거효과가 있었다. UF 적용후 여기에 RO를 적용하였더니 방류수 기준을 충분히 만족할 수 있을 정도로 아주 우수한 $COD_{Mn}$ 제거효과가 관찰되었다. 또한 색깔제거 측면에서도 거의 100%의 색도제거가 확인되었고, 처리수의 pH도 중성에 가까워서 이를 재활용할 수도 있을 것으로 판단된다.

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물리, 화학 및 생물학적 방법에 의한 안료폐수의 적정처리 및 재이용 가능성 평가 (The Appropriate Treatment and Reuse Ability Assessment of Pigment Wastewater by Physical, Chemical, and Biological Process)

  • 정종식;옥치상
    • 한국환경과학회지
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    • 제7권1호
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    • pp.81-88
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    • 1998
  • This study was conducted to assess the characteristics of plgment wastewater and the removal rates of appropriate treatment by physical, chemical and biological Process, and the possibility of reuse for effluent. Based on the results, the wastewater qualities of pigment were pH 5.1$\pm$3.4, temperature 43.0$\pm$ 15.$0^{\circ}C$, BOD 1,431.4$\pm$589.6mg/l, COD 2,282.8$\pm$466.5mg/l, turbidity 1,340$\pm$820NTU, color 243.0$\pm$147.0unit, Pb 36.5$\pm$9.5mg/l and $Cr^+6$ 10.3$\pm$ 1.3mg/l, respectively. The removal rates of adsorption by activated carbon and filter process were BOD 40.6% , COD 57.0% , turbidity 89.6%, color 87.2%, Pb 86.0% and $Cr^+6$ 10.6%, respectively. And the removal rates of reduction, neutralization, coagulation and aP floatation process were BOD 18.2%, COD 24.3%, turbidity 74.3%, color 56.7%, Pb 68.6% and $Cr^+6$ 97.8%, respectively. The removal rates of activated sludge process were BOD 95.9%, COD 86.0%, turbidity 27.8%, color 25. 2%. Pb 26.9% and $Cr^+6$ 50.0% , respectively. The total removal rates of treatment by physical, chemical and biological process were BOD 98.0% , COD 95.4%, turbidity 98.1%, color 95.8%, Pb 97.0% and $Cr^+6$ 99.0%, respectively. According to the test results for possibility of reuse with coagulation-adsorption by activated carbon process of effluent, COD was higher than that of raw water and others were similar to that of raw water thus, it Is considered to be reused.

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메리골드 안료를 이용한 친환경 텍스타일 프린팅(1): 바인더의 종류와 혼합비율의 효과 (Eco-friendly Textile Printing using Marigold Pigment(1): Effect of Binder Type and Mixing Ratio)

  • 여영미;신윤숙
    • 한국염색가공학회지
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    • 제31권4호
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    • pp.233-240
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    • 2019
  • Dyeing is an essential process for improving the value of textile products, but it is considered as one of industries causing pollution because of producing wastewater containing hazardous chemicals as well as using a large amount of water and energy. Global demand for greener technologies in textile field is getting much more attention and accordingly, the use of eco-friendly natural dyes is growing much larger. In textile printing, both dyes and pigments can be used. Pigment printing is more simple process and requires less water and less energy, compared to dye printing. In this study, the organic pigment was prepared from the marigold colorant. Samples were stencil printed, pressed(70℃, 3min) and then heat treated(150℃, 5min). The uptake of polyacrylic acid as a chemical binder was the lowest. In particular, marigold pigments were excellent in color and texture when Guar Gum and Sodium Alginate were used as binders. In addition, the light and washing fastness was rated very high as 4, 4/5 grades, and the rubbing fastness was also excellent as 3 and 4 grades.

캐로티노이드 , 키틴, 키토산의 원료로서 Crawfish 가공 폐기물의 이용 (Utilization of Crawfish Processing Wastes as Carotenoids, Chitin, and Chitosan Sources)

  • No, hong-Hyoon;Samuel P.Meyers
    • 한국식품영양과학회지
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    • 제21권3호
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    • pp.319-326
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    • 1992
  • The Louisiana crawfish industry comprises the largest concentration of crustacean aquaculture in the United States. Processing plants throughout the culture region annually generate as much as 80 million pounds of peeling waste during recovery of the 15% (by weight) edible tail meat. A commercial oil extraction process for recovery of carotenoid astaxanthin from crawfish waste has been developed. Crawfish pigment in its various forms finds applications as a source of red intensifying agents for use in aquaculture and poultry industries. Crawfish shell, separated in the initial pigment extraction step, is an excellent source of chitin. Applicable physicochemical procedures for isolation of chitin from crawfish shell and its conversion to chitosan have been developed. Crawfish chitosan has been demonstrated to be both an effective coagulant and ligand-exchange column material , respectively, for recovery of valuable organic compounds from seafood processing wastewater.

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재순환방식 튜브형 전해모듈시스템을 이용한 안료폐수의 전기화학적 산화 (Electrochemical Oxidation of Pigment Wastewater Using the Tube Type Electrolysis Module System with Recirculation)

  • 정종식
    • 대한환경공학회지
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    • 제38권8호
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    • pp.411-419
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    • 2016
  • 본 연구에서는 안료폐수 중에 포함되어 있는 유기물질과 질소를 처리함으로써 재순환방식을 이용한 튜브형 전해모듈시스템의 적용 가능성을 평가하였다. 튜브형 전해모듈은 내부 봉형 양극과 외부 튜브형 음극으로 이루어져있다. 양극의 재질은 $RuO_2$로 전착된 티타늄이었고 음극의 재질은 스테인리스 스틸이었다. 재순환형 튜브형 전해모듈시스템에서 오염물질의 제거율은 유량이 감소할수록 그리고 전류밀도가 증가할수록 높아졌다. 전해모듈시스템에서 체류시간이 180분일 때 염소산이온의 농도는 382.4~519.6 mg/L로 나타났다. 본 연구에서 사용한 재순환방식을 이용한 튜브형 전해모듈시스템에서 염소산이온의 생성은 전기화학적 산화의 중요한 인자 중의 하나이다. Bench scale의 재순환방식 튜브형 전해모듈시스템에서 전력량을 $4,500C/dm^2$으로 공급하였을 경우 $COD_{Mn}$은 89.6%, $COD_{Cr}$은 67.8%, T-N은 96.8% 그리고 색도는 74.2%가 제거되었으며, 이때 에너지 소모량은 $5.18kWh/m^3$이었다.

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

  • 김종규;정호진
    • 상하수도학회지
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    • 제18권3호
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    • pp.392-400
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    • 2004
  • This research uses the $TiO_2$/UV process to verify the most suitable condition and possibility to dispose dyeing wastewater that contains pigment and a large amount of pollutants. For this, this research has enforced experiments that compare photo adsorption, photolysis, and photo catalyst oxidation reaction, and also evaluated and analyzed the change of pH and $TiO_2$ dosage, irradiation rates of ultraviolet rays and the dosage change and injection method of $H_2O_2$. According to the results of the dyeing wastewater experiment of storehouse catalyst that uses the new form of $TiO_2$, the photo catalyst oxidation reaction proved to be more effective than photo adsorption and photolysis; 35%, 21% in the case of $TCOD_{cr}$ and 39%, 28% in the case of chromaticity. Taking into consideration the reaction time, amount of photo catalyst reaction and irradiation amount of ultraviolet rays, the decomposition efficiency of pH change proved to be most effective at pH 4. On the whole, the acidity area proved to be effective in dyeing water exclusion than neutral and alkalinity areas. Having evaluated the influence of $TiO_2$ dosage, not only does the decomposition efficiency continuously improve as the $TiO_2$ dosage increases but the shielding effect does not occur also when the $TiO_2$ is at a fixed state. The influence of ultraviolet irradiation amount concluded in the result that as the ultraviolet irradiation amount increases the decomposition efficiency continually increased, but in the case of chromaticity when the irradiation amount was higher than 37.8mW/cm2 the removal efficiency is slowed remarkably. The influence of $H_2O_2$ dosage evaluation reached the results that although the decomposition efficiency increases with the increase of $H_2O_2$ dosage, when above 150mg (total dosage: 1200mg) $H_2O_2$ consumes OH radical itself and reduces the decomposition efficiency. Also in the case of the $H_2O_2$ injection method rather than injecting in the whole amount of $H_2O_2$ (1200mg) needed at the beginning all at once, injecting divided quantities of $H_2O_2$ whenever the electric current density falls below 10mgfl reduces the wases of OH radical due to an excess of $H_2O_2$ and in tum heightens the decomposition efficiency.