• Title/Summary/Keyword: 난분해성 유기물제거

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Oxidation of Organics Using a Direct Reaction of Peroxyl Radical and Ozone (페록시라디칼과 오존의 직접 반응을 이용한 유기물의 산화)

  • Choi, Seungpil;Kim, Jongoh
    • Journal of the Korean GEO-environmental Society
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    • v.11 no.8
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    • pp.41-47
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    • 2010
  • This study was conducted to assess the applicability of pilot scale system and to evaluate the treatment efficiency on operational parameters such as humic acid concentration, initial pH and air flow rate on the ozone/peroxyl radical reaction system. The decolorization of ozone/peroxyl radical system was higher than that of only process. Removal efficiency of ozone/peroxyl radical system was generally increased with the increase of intial concentration of humic acid but decreased over the range of 30mg/L. Treatment efficiency of HA at acid pH was smaller compared to that of neutral or basic pH and increased with increasing the air flow rate from 1L/min to 3L/min. In pilot-scale test, average removal of TOC and $COD_{Cr}$ was about 70% and 60%, respectively and ozone/peroxyl radical reaction system was indicated a potential in water treatment application.

Characteristics of treatment by Electrolysis with a change of electrodes in sanitary landfill leachate (전기분해법에서의 전극변화에 따른 위생매립장 침출수의 처리특성)

  • Huh, Mock;Kim, Byung-Hyun;Kim, Gwang-Jin
    • Journal of the Korea Organic Resources Recycling Association
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    • v.10 no.1
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    • pp.68-74
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    • 2002
  • This study was performed to examine the availability of electrolysis for removal of remaining biologically refractoty humus and residual color of leachate which is biologically pretreated in domestic waste matter sanitary landfill by recycling to landfill. The obtained results were as follows; 1) The electrolysis of leachate through covered bed represented that the removal efficiency of CODcr and color range from 70~80%, in color removal the only electrolysis for a treatment of leachate meet the critia of effluent. 2) The highest removal efficiency was represented in pH 7~8. 3) At anode used Al, Fe, Stainless the removal efficiency of CODcr and color was high in order of Fe, Al, stainless, in considering the settled ability of reaction product in economic or after electro coagulation the removal efficiency was highest when anode was the Fe electrode. 4) In this study conditions for removed both CODcr and Color ar the same time represented thar anode was used Fe, electrode-distance was 2cm and reaction time was 40min in 8volts.

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Removal Properties of Methylene Blue in Catalytic Ozonation (촉매오존화에 의한 메틸렌 블루 제거특성)

  • Chung, Jae-Woo
    • Journal of the Korea Organic Resources Recycling Association
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    • v.25 no.3
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    • pp.5-12
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    • 2017
  • Effects of operating parameters such as activated carbon dose, gaseous $O_3$ concentration and pH on the properties of methylene blue(MB) degradation in a catalytic ozonation were investigated through a series of batch experiments. Activated carbon catalyzed the self-decomposition of ozone, generating $OH{\cdot}$, thus promoting MB degradation. Thus the increase of activated carbon dose enhanced the MB and TOC removal. The higher gaseous ozone concentration injected, the promoted MB and TOC removal obtained through the enhanced mass transfer. The MB removal was not significantly affected by the variation of aqueous pH. Catalytic ozonation can be considered as an efficient alternative in treating refractory pollutants in textile wastewater with faster and higher dye and TOC removal compared with ozonation and adsorption.

Treatment of TNT Red Water by the Ozone-based Advanced Oxidation Processes (오존을 산화제로 사용한 다양한 고급산화 공정에 의한 TNT Red Water의 처리)

  • Jun, Jun Chul;Kwon, Tae Ouk;Moon, Il Shik
    • Korean Chemical Engineering Research
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    • v.45 no.3
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    • pp.298-303
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    • 2007
  • Several combinations of ozone based advanced oxidation processes were tested for the treatment of red water (RW) containing recalcitrant chemical pollutants produced from 2,4,6-trinitrotoluene (TNT) manufacturing process. $O_3$, $UV/O_3$, $UV/O_3/H_2O_2$, $UV/O_3/H_2O_2/Fe^{2+}$ processes were tested for the treatment of RW. The order of organic and color removal efficiency was found to be : $O_3{\leq}UV/O_3$ < $UV/O_3/H_2O_2$ < $UV/O_3/H_2O_2/Fe^{2+}$. The optimum conditions for the removal of organic and color in the $UV/O_3/H_2O_2/Fe^{2+}$ process were 0.053 g/min of ozone flow rate, 10 mM of $H_2O_2$ concentration and 0.1 mM of $FeSO_4$ concentration. Organic and color removal efficiencies were 96 and 100 % respectively in the $UV/O_3/H_2O_2/Fe^{2+}$ process. tert-butyl alcohol (t-buOH) was used as the hydroxyl radical scavenger. Enhancement of hydroxyl radical production was achieved by the combination of ozone with several oxidants such as UV, $H_2O_2$, $Fe^{2+}$.

Plasma Aided Flotation for Removing Organic Substances and Killing Microorganisms

  • Yu, Seung-Min;Hong, Eun-Jeong;Yu, Seung-Yeol;Park, Jun-Seok;No, Tae-Hyeop
    • Proceedings of the Korean Vacuum Society Conference
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    • 2014.02a
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    • pp.122-122
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    • 2014
  • 수중방전을 환경분야에 적용하기 위한 플라즈마 부상법이 개발되었다. 플라즈마 부상법은 물 속에서 발생시킨 플라즈마가 가지고 있는 주요특성 중 물리적 특징인 쇼크웨이브, UV조사, 버블생성 등과 화학적 특징인 OH라디칼 및 염소산화물 생성 등을 이용하여 물 속에 존재하는 용존성 및 입자성 물질을 부상분리 기법으로 제거하는 공법이다. 유기물을 제거하는 기작으로는 침전, 여과, 분해 등이 있고, 이를 구현하기 위한 공정으로 중력침강법, 부상분리법, 멤브레인법, 미생물법 등이 있다. 이 중에서 가압공기부상법은 침강법에 비해 부지면적을 적게 소모하고 처리시간이 50% 이상 감소되는 특징이 있다. 가압공기부상법은 물 속에 공기를 과포화시킨 후 노즐을 통해 재분사할 때 발생하는 압력차에 의해 미세기포가 발생함을 이용하여 유기물을 분리하는 공법이다. 그러나, 가압용 장비 및 반송수가 필요하고, 미생물분리는 불가능한 단점이 있다. 이에 본 연구에서는 미생물살균과 유기물 분리가 동시에 일어나는 플라즈마를 이용한 부상분리기법을 개발하였다. 본 연구에서는 난분해성 용존유기물인 휴믹산 100 mg/L의 플라즈마 공기부상법에 의한 제거능을 확인하였다. 용존성 휴믹산을 입자성 물질로 전환하여 플록을 형성시키고자 알루미늄설페이트(Al2(SO4) $3{\cdot}18H2O$)를 100 mg/L 주입하였고, 침출수와 같이 염도가 높은 물을 모사하고자 35 g/L의 염화나트륨을 첨가한 상태에서 방전을 실시하였다. 방전에 사용된 전원은 EESYS사에서 제작한 펄스형 고전압 전원장치를 사용하였고 최대 15 kW의 출력 중 6 kW의 전력을 인가하였다. 전극 한 개는 2 mm 텅스텐봉을 세라믹튜브로 감싼 구조로 총 사용전극은 28개이다. 전극 한 개당 대략 200 Watt의 전력이 소모되며 이 때 최대의 버블이 생성됨을 확인하였다. 전극 1개에서 생성되는 버블의 부피는 14 mL/min 로 측정되었다. 버블의 크기는 평균 70 um이고 가압공기부상법에서 최적공기크기로 제시하고 있는 40~80 um 의 버블은 약 80% 가량 생성된다. 본 연구에서 사용된 반응시스템에서의 물의 높이는 약 500 mm 이고 전체 40 L의 수조가 3개의 벽으로 분리되어 4개의 수조로 분리되었다. 각 수조는 하부에 7개의 전극을 포함하고 있다. 플라즈마 발생시 생성되는 기포는 약 1분 방전 후에 포화농도에 도달하며 방전종료 후 약 4분간 수체 내에 남아있게 된다. 이를 공정에 적용하여 1분 방전 및 4분 휴지의 순서로 플라즈마를 인가하였다. 휴믹산 용액의 유량을 2 lpm 으로 운전하였을 때 최종 처리율은 94% 이고 이때의 대장균 살균능은 99%이다.

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Remediation Technique for PCBs-and Phenols-Contaminated Soils by Surfactant-Enhanced Desorption (계면활성제 탈착촉진법을 이용한 폴리클로네이티드 바이페닐(PCBs)과 페놀류(Phenols)에 의하여 오염된 지반의 정화방안)

  • 박준범;윤현석;김준섭
    • Journal of the Korean Geotechnical Society
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    • v.15 no.5
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    • pp.241-257
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    • 1999
  • Subsurface contamination of industrial hazardous organic substances is a serious social issue. Decomposing the hydrophobic organic compounds in the subsurface is technically difficult and the compounds can last as long-term contaminant sources of groundwater once they are sorbed on the soil. Although the danger of contaminated subsurface has long been recognized little was known about the effective remediation technique. Focusing on the remediation of the p-Cresol and 3, 5-Dichlorobiphenyl among subsurface contaminants, this paper studies the surfactant-enhanced desorption technique. Nonionic surfactant(Triton X-100) and anionic surfactant(SDS ) were used as desorbing solvents for extracting organic compound sorbed on soil particles. Sorption characteristics of soils and organic compounds were analyzed and the applications of surfactant solution were studied through batch tests and the flexible-wall permeameter tests. As a result of the sorption isotherm tests, a log-log linear relation was obtained between the linear-partition coefficient, $K_p$ and the octanol-water partition coefficient, $K_{ow}$ of each organic compound. The result of the batch test also showed that Triton X-100 at 0.5% of solution desorbs the 3, 5-Dichlorobiphenyl 28 times more than the water in the batch tests. The surfactant-enhanced subsurface remediation technique becomes more effective when the contaminants are hydrophobic and hard to be decomposed.

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Treatment of dyeing wastewater using Moving Bed Bioractor (부유메디아 생물막 공정을 이용한 염색폐수처리)

  • Shin, Dong-Hoon;Lee, Sang-Hun;Ryu, Seung-Han;Park, Jun-Hyung;Jo, Seog-Jin
    • Proceedings of the Korean Society of Dyers and Finishers Conference
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    • 2011.03a
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    • pp.110-110
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    • 2011
  • 염색공업 폐수는 그 성분이 일반적으로 매우 복잡하며, 작업공정의 가동 사항에 따라 수질 변동이 큰것이 특징으로, 각 공정에서 배출되는 염료, 보조화학물질, PVA(Polyvinyl alchol), 전분, wax 등이 포함되어 있으며 pH가 높고, 색도로 인해 하천에 방류될 경우 확산성이 높아 미생물에 의한 자정작용을 방해하여 하천의 수중생태계를 파괴할 우려가 있다. 이러한 염색산업에서 발생하는 폐수는 일반적으로 응집침전, 부상분리법 등의 전처리한 후 활성오니공정으로 처리하는 방법이 널리 이용되고 있으나, 이들 처리공정으로는 폐수 속에 포함되어 있는 다양한화학적 구조의 색소성분 및 유해물질을 완벽하게 제거하는 것이 어려운 실정이다. 유기물 함량이 높은 염색폐수를 처리하기 위해 제안된 기술로는 산소활성슬러지법, 유동상 및 고정상 생물막법, 포괄고정화법 등이 있다. 이러한 기술들중 기존의 처리공정을 증축없이도 처리효율을 높일 수 있는 방법으로 담체를 이용한 부유메디아 생물막공정(Moving-Bed BioReactor, MBBR)이 있다. 이공정은 미생물이 부착, 성장할 수 있는 공극율과 비표면적이 큰 담체를 이용하므로 반응조내의 부유 미생물 뿐만 아니라 담체에 고농도로 부착된 부착 미생물에 의해서도 유기물을 제거하기 때문에 다른 공정들에 비해 처리효율이 뛰어나고 기존의 활성슬러지 공정에 비해 갑작스러운 부하변동 및 유독성 폐수유입에 대해서도 안정적으로 운전이 가능한 장점이 있다. 본연구에서는 부유메디아 생물반응기(Moving-Bed BioReactor, MBBR)을 이용하여 염색폐수내 $COD_{Mn}$, 색도 및 난분해성 물질인 PVA 저감에 대한 Lab-scale test 수행하였다. 실험에 사용된 염색폐수의 수질은 평균 pH 13, $COD_{Mn}$ 900 mg/L, SS 135 mg/L, 색도 1,134 [C.U.], PVA 593 mg/L였으며, 2L의 반응기를 사용하여 회분식 실험을 수행였다. 본 실험에서는 호기성 미생물에 의한 염색폐수의 생분해가 유지되는데 필요한 최적의 용존산소 농도와 이에 필요한 공기 폭기량을 결정하기 위하여 i) DO uptake rate측정과 ii) 담체의 충진율, iii) COD/N ratio, iv) Air 유량, v) 담체내 흡착제의 종류, vi) $Ca^{2+}$ 첨가가 염색폐수의 생분해에 미치는 영향을 살펴보았다. 운전시간을 7일로 하여 COD, 색도, PVA 등을 측정한 결과 담체를 첨가한 경우가 담체를 첨가하지 않은 경우 보다 제거효율이 뛰어났다. 특히 충진율 30%(C/N 3)의 경우에서 COD, 색도, PVA의 제거율이 각각 평균 65%, 70%, 60%로 가장 높은 제거효율을 나타내었다.

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Distribution of Biota and Removal Efficiency of Organic Matter in Natural Wetland (농촌배수처리용 습지의 생물상 및 유기물 제거율)

  • Kim, Bum-Chul;Jeon, Man-Sik;Jung, Geun;Jung, Yeon-Sook;Hwang, Gil-Soon
    • Korean Journal of Environmental Biology
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    • v.17 no.4
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    • pp.407-414
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    • 1999
  • Distribution of biota and removal efficiency of organic matter in natural wetland systems were examined from June to October 1998. The aquatic macrophyte communities were consisted of 13 families and 22 species. The composition of occurrence species were as follows: Phragmites communis Trinius are 35%, Persicaria thunbergii Nakai are 19%, Typha angustifolia L. are 17%, Bidens tripartita L. are 16%, Echinochloa crus-galli (L.) Beauv. are 12% and others are l%. The fauna collected from 5 sites consisted of total 6 classes of macroinvertebrates. The composition of occurrence classes were as follows: Insecta are 76%, O1igochaeta are 19%, Gastrapoda are 4% and others are 1%. These included 18 families, 7 orders of Insects. The larve and mosquito and midges were found in wetlands. Preventive strategies are needed for the suppression of mosquito at the stage of wetland planning and design. In wetland, removal efficiency of dissolved organic carbon is low because of primary production and the background level of DOC in the wetland discharge seems to be 5 mgC/1, but those of BOD was ca. 50%. Wetlands receiving water of low concentration can not work as purification field.

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A Study of the Improvement in an Anaerobic Digester for Sludge Reduction (슬러지 저감을 위한 혐기성 소화조 개선에 관한 연구)

  • Kim, Hong-Seok;Lee, Tae-Jin
    • Journal of Korean Society of Environmental Engineers
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    • v.33 no.7
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    • pp.516-522
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    • 2011
  • The largest problem of domestic anaerobic digestion is low digestion efficiency. Reasons of the problem would be low organic matters input, low mixing efficiency in digestion tank, refractory excess sludge etc.. In this study, screw attached disk-type concentration system and a mechanical mixing system, solubilization facility improvements were performed to solve problems. Through these improvements, the sludge conc. of the concentrator increased 2.6-fold and the volume reduction efficiency was increased 3.0-fold. In addition, the dead-space is reduced by mechanical agitation. Anaerobic digester gas production in the digestion tank is increased from $193.8m^3$ to $386.0m^3$ per day. Digestion efficiency is improved to 54.6% from 47.6%. Digestion gas production is increased from $0.30Nm^3/kg$ VS to $0.42Nm^3/kg$ VS.

Removal of Ammonia Nitrogen and Organics from Piggery Wastewater Using BACC Process-I. Comparison of Activated Sludge Process (BACC를 이용한 축산폐수의 암모니아성 질소 및 유기물의 제거 I. 활성슬러지 공정과의 비교)

  • 성기달;류원률;김인환;조무환
    • KSBB Journal
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    • v.16 no.2
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    • pp.133-139
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    • 2001
  • To treat piggery wastewaters containing refractory compounds including nitrogen, biological treatments were investigated. In biological treatment, the removal efficiencies of organics and nitrogen by the activated sludge process and bioreactor using a BACC (Biological Activated Carbon Cartridge) media filled with granular activated carbon were examined. The results were as follows; in the biological process, when the approximate influent BOD concentration of 620 mg/L, through dilution, was treated by the activated sludge process, the process should be operated at a HRT of over 8 days to maintain an effluent BOD concentration of lower than 100 mg/L. In the treatment of piggery wastewater using a BACC bioreactor, when the HRT was 200 hours, the BOD, COD(sub)cr, and TKN removal efficiency of the effluent were 94, 75 and 64.3%, respectively. Comparing the BACC bioreactor with the activated sludge process, when the volumetric loading rate was 0.3 g BOD/L.day, the specific substrate removal rate of BOD was 0.14 g BOD removed/L.day in the activated sludge process which compared with 0.27 g BOD removed/L$.$day in the BACC bioreactor. The BACC bioreactor showed on average a 2-fold higher removal rate and was superior to the activated sludge process in wastewater treatment in terms of variations of loading time and high loading time. Therefore, the BACC process can effectively treat piggery wastewater containing high concentrations of nitrogen and organic compounds.

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