• 유기물자원화
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• 제3권2호
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• pp.103-114
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• 1995

현재 미국이나 캐나다에서는 고농도 유기성 폐수의 처리에 대한 고온 호기성 소화 공정의 여러 가지 장점으로 인하여 활발한 연구 및 적용이 진행되고 있으며, 국내에서도 고농도 유기성 폐수 처리의 여러 문제점으로 관심이 고조되고 있다. 따라서 본 연구에서는 돈 분뇨 폐수를 대상으로 고온 호기성 소화 공정의 적용 타당성을 평가하기 위한 실험을 수행하였다. 그 결과 호기성 소화 슬럿지는 악취 및 부패 등의 측면에서는 상당히 안정화됨으로서 소화슬럿지의 습식사료화 및 액비화의 가능성을 보여주었다. 그러나 습식사료화는 국내 양돈 농가가 대부분 건식 사료 급이 체제를 이루고 있으므로 사료 급이 체제의 전환이 요구되고, 액비화의 경우는 초지 확보가 가능한 단위 농장에서만 적용이 가능하리라고 사료된다. 한편 고온 호기성 소화조의 온도 상승 원인을 조사한 실험 결과에 의하면 생물학적 활성으로 인하여 발생한 에너지보다 교반 에너지에 의한 온도상승이 훨씬 큰 것으로 나타나고 있어 ATAD의 기본 원리에 어긋나고 있어 고온 호기성 소화를 거친 돈 분뇨 폐수가 습식 사료화 될 수 없는 여건하에서 단순한 폐수 처리의 목적만으로 고온 호기성 소화조를 적용하는 것은 비경제적이라고 할 수 있다.

• 한국표면공학회지
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• 제35권6호
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• pp.401-407
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• 2002

Most of organic compounds discharged from industrial wastewater are treated by chemical oxidation, adsorption and biodegradable process. This process has been demanded a new advanced environmental wastewater treatment process. From this point of view, an electrochemical oxidation process using electrocatalysts has been developed for the destruction of organic compounds. Through this study, a ruthenium oxide/iridium oxide supported on titanium expanded metal was fabricated by thermal decomposition method and its performance was excellent during this experiment.

• 상하수도학회지
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• 제24권2호
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• pp.195-202
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• 2010

The evaluation of organic matters and nutrients removal was investigated for the synthetic wastewater and the high strength of dairy wastewater. Two different systems were performed for this research. System A composing of a single RBC with tapered aeration was fed with the synthetic wastewater for 74 days with 173L/day of influent, 200% of internal return and 100% of sludge return for the period 1 and 2. The feed conditions were maintained 346L/day of influent, 50% of internal return and sludge return for the period 3. The dairy wastewater was introduced to evaluate treatment efficiency for system B composing of dual RBCs and tapered aeration tanks for 50 days of experimental run time, in which hydraulic rates were maintained at the constant ratios of 346L/day, 50% of internal return and 50% of sludge return. The spiral string media made of nylon fibre was attached by Bacillus sp. in RBC for both systems. The specific area of string media was $1.4m^2$/m and biomass was maintained at the concentrations of 23g/m. The synthetic wastewater was supplied by 1,800mg/L of glucose, 500mg/L of $NH_4Cl$, and 500mg/L of $KH_2PO_4$ to system A. The dairy wastewater was supplied to system B from dairy production plant. The average influent concentrations were 1,334mg/L of BOD, 2,014mg/L of CODcr, 160mg/L of T-N, and 12mg/L of T-P in system A. The average influent concentrations of parameters were 1,006 mg/L for BOD, 1,875mg/L for $COD_{cr}$, 51.6mg/L for T-N and 8.9mg/L for T-P in system B. Results indicated that removal efficiencies of BOD and $COD_{cr}$ were more than 90% however, the removal efficiency of T-N was 87%, and that of T-P was 82% for system A. Removal efficiencies were 98.5% of BOD, 91.3% of nitrogen and 89% of phosphorus for system B. The removal efficiencies of organic matters, T-N and T-P were higher in system B than in system A. The effluent quality issued by the stringent national legislations for the discharge of the high strength of dairy products wastewater can be improved using sequential RBCsand tapered aeration reactors rather than a single RBC and tapered aeration reactors with Bacillus sp.

• 환경위생공학
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• 제16권3호
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• pp.28-33
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• 2001

Photosynthetic bacteria (PSB), strains IP-4 and IP-6-7 were isolated from nature, and were studied for swine wastewater treatment. It was confirmed that these PSB were very effective for the COD treatment. Growth of those PSB were increased to 4.5 fold in organic-acids (acetate, propionate and butyrate) added medium than cultivation in Lascelles basal medium and the amount of bacteriochlorophyll a were increased to 5 folds. The COD removal rate in swine wastewater using PSB, strains IP-4 and IP6-7 were obtained 91% and 85%, respectively.

• 생명과학회지
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• 제24권8호
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• pp.887-894
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• 2014

유기염소계 난분해성 산업폐수처리에 효과적인 미생물제제 개발을 위하여 PCP (pentachlorophenol)와 TCE (trichloroethylene) 등과 같은 유기계 염소화합물이 오염되어있는 토양 및 산업폐수로부터 PCP 분해활성이 높은 GP5, GP19와 TCE 분해활성이 높은 GA6, GA15를 분리하였다. 이들 분리균주 GP5, GP19, GA6, GA15등은 Acetobactor sp., Pseudomonas sp., Arthrobacer sp., Xanthomonas sp.과 유사한 것으로 나타나 최종적으로 Acetobacter sp. GP5, Pseudomonas sp. GP19, Arthrobacer sp. GA6, Xanthomoas sp. GA15로 명명하였다. 유기염소계 산업폐수의 처리를 위한 복합미생물제제 OC17은 PCP와 TCE를 분해하는 4개의 분리 분리균주와 방향족화합물 분해균주인 Acinetobacter sp. KN11, Neisseria sp. GN13의 배양액을 혼합하여 제조하였다. 복합미생물제제 OC17은 $2.8{\times}10^9CFU/g$의 균체수를 갖고 있으며, 밀도는 $0.299g/cm^3$, 수분함량은 26.8%를 나타내었다. 복합미생물 제제 OC17은 PCP 500 mg/l가 포함되어있는 인공폐수를 이용한 실험에서 배양 65시간에 87%의 분해효율을 나타내었고, TCE (300 uM)의 분해효율은 배양 50시간에 90%의 분해효율을 나타내었다. 복합미생물제제 OC17을 이용한 유기 염소계 산업폐수의 처리효율 시험을 위한 연속배양 실험 에서 10일간 처리 하였을 때 91%의 COD 제거효율을 나타내었다.

• 상하수도학회지
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• 제18권2호
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• pp.165-173
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• 2004

Behavior of hazardous organic compounds including bisphenol A, phtalic acid, and phosphoric acid in low pressure nanofiltration process were investigated. In the case of NTR729HF, rejection of all target organic compounds except 2-H-Benzothiazol and 2-isopropyl phenol was more than 90%. The lowest rejection for 2-H-Benzothiazol was observed in another membranes. The UTC60 and UTC20 showed similar rejection characteristics of hazardous organic compounds. Although the rejection of Bisphenol A, n-buthyl benzenesulfoneamide, N-ethyl-p-toluensulfonamide, 2-H-benzothiazol, p-t-butylphenol and 2-isopropyl phenol was less than 30%, the rejection of tributyl phosphate, triethyl phosphate, camphor, 2,2,4 trimethyl 1,3 pentandiol and diphenyl amine was more than 90% in the case of UTC60 and UTC20. The rejection characteristics of various hazardous organic compounds were converted into one parameter Ks, which was proposed in the diffusion-convection model. The Ks of hazardous organic compounds were discussed by comparing with their solute size represented by Stokes radius. The diffusion convection model considering Ks was successful to interpret rejection characteristics of hazardous organic compounds by low-pressure nanofiltration membranes.

• 유기물자원화
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• 제20권3호
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• pp.52-59
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• 2012

처리공정별 연계처리수질을 검토한 결과 생물학적처리만 거친 생물반응조 처리수의 경우 연계부하율이 $COD_{Mn}$의 경우 1.67%(설계수질 기준), 2.59%(운영수질 기준), T-P의 경우 3.69%(설계수질 기준), 7.67%(운영수질 기준)로 다소 높게 나타났으나 하수처리장 운영에 미치는 영향은 거의 없을 것으로 판단된다. 또한, 고도처리공정인 산화부상분리 처리수 및 생물여과 처리수의 경우 연계부하율은 1% 내외로 고도처리설비 설치 시 과대 설비설치의 우려가 있다. 따라서 S하수처리장의 경제성 및 안정적인 운영을 고려할 경우 생물학적처리인 생물반응조를 거친 처리수를 연계하는 것이 바람직할 것으로 판단된다.

• 한국융합학회논문지
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• 제11권10호
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• pp.213-217
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• 2020

천연 광물질, 식물질, 정수장 슬러지를 이용하여 친환경적인 수수질정화제와 이를 활용하는 오폐수복합처리시스템을 개발하였다. 오폐수복합처리시스템은 오염수 유입, 수질정화제 투입, 가압부상장치 가동, 슬러지 부상, 슬러지 수거 및 처리수 배출의 과정을 거친다. 이 장치를 축분 탈리액, 육계 세척수, 공장 폐수, 하수종말처리장 및 연못의 녹조제거에 적용하여 우수한 제거율을 얻었다. 유기성 폐기물 정화에 천연 수질정화제를 활용한 예는 조사되지 못했다.

• 한국염색가공학회지
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• 제10권4호
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• pp.45-52
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• 1998

Reuse of wastewater become an important consideration to solve the environmental pollution problems in recent industriallzation and urbanization. Especially, he characteristic of dyeing process is subject to use much water and thus has serious problems for removal of color and organic pollutants in their wastewater. This report is divided into two main parts ： The purpose of the first part was to determine if alkaline wastewater discharged from textile dyeing operation factory could be flocculated directly by Fenton oxidation method. This study was conducted to investigate Fenton reagent dose and reaction condition of Fenton method as pretreatment for dyeing wastewater in K dyeing industry were investigated. In the second part of this research, to treat dyeing wastewater it was found that the most effective way is to use ultrafiltation and reverse osmosis at the conditions of the pH 7.0~8.0 and operating pressure of $2.5~35kg_f/cm^2$. This paper is mainly dealt with the application on reuse system of dyeing wastewater treatment using ultrafiltration and reverse osmosis membranes. The results showed that dyeing wastewater could be reused by chemical, filter and membrane sequential treatment process.

• 한국초전도ㆍ저온공학회논문지
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• 제23권3호
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• pp.20-25
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• 2021

Milking parlor wastewater contains high concentration suspended solid (SS), nitrogen, and/or phosphate as well as organic compounds. A new biological wastewater process by magnetic separation, magnetic activated sludge (MAS) process, was applied to milking parlor wastewater treatment process. A three step wastewater treatment process of coagulation sedimentation / ammonia stripping (C/S), magnetic activated sludge process and contact oxidation (CO) was proposed for removal of these pollutants. First step, C/S process recovered 96% TN and 96% PO₄^3--P as resource for fertilizer from the wastewater. 81% biochemical oxygen demand (BOD) in wastewater was removed after MAS process. As a results, all pollutant concentrations satisfied Japanese effluent standards. Most of residual BOD and SS were removed by the CO process. It was estimated that the proposed process could reduce the process space to 1/7.