• 한국지반환경공학회 논문집
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• 제15권9호
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• pp.5-12
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• 2014

슬러지의 안정화, 휘발성 고형물 감소, 바이오가스 생산을 위해 혐기성 소화공정이 슬러지의 처리 방안으로 연구됐다. 본 연구에서는 하 폐수 슬러지(MWS, IWS), 혼합슬러지(Mix), 탈수슬러지(MWSC)를 대상으로 바이오가스 생산 가능성을 살펴보기 위해 Total solids, Volatile solids, 원소분석, BMP 실험을 하였다. Total solids 함량은 11.2~20.6 %의 값을 가지며 Volatile solids의 함량은 TS의 62.1~83.1 %의 값을 가지고 있다. C/N비는 4.96~8.33의 값을 나타났다. BMP test를 한 결과 혼합슬러지의 경우 약 20일, 하 폐수 슬러지의 경우 약 16~17일에 메탄발생이 종료되었다. 탈수케이크는 약 10일까지 메탄이 발생하였으며 가장 빨리 메탄발생이 종료되었다. 누적 메탄발생량의 경우 혼합슬러지가 395.50 mL $CH_4/g$ VS으로 가장 높은 누적 메탄 발생량을 가진다. 누적 이산화탄소 발생량은 탈수케이크를 제외하고 비슷한 값을 보이고 있다.

• 대한환경공학회지
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• 제35권6호
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• pp.407-414
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• 2013

가축분뇨 공공처리시설 및 개별농가에서도 적용이 가능하도록 경제적이고 운영이 비교적 쉽고 간단하며 부지가 적게 소요되는 컴팩트한 처리시설을 개발하기 위하여 안성에 있는 M농가에 실규모의 처리시설(100톤/일)을 설치하고 공공처리시설 방류수 수질기준까지 처리할 수 있도록 운영하였다. 벨트프레스 탈수기를 통해 고액분리된 액상 가축분뇨는 MBR/NF/RO를 통해 처리되고 NF/RO농축수 및 가축분뇨처리 슬러지는 혼합한 뒤 탈질을 거쳐 응집가압부상을 통해 처리된다. MBR/NF/RO처리수와 가압부상조 유출수를 혼합 방류하면 공공처리장 수질기준 BOD 30 mg/L, T-N 60 mg/L, T-P 8 mg/L 이하가 달성된다. 가압부상 농축 슬러지는 벨트프레스 탈수기로 유입되어 고상 가축분뇨와 함께 탈수되어 분리된 고형물의 수분함량은 90%로 톱밥과 혼합되어 퇴비로 활용된다.

• 한국산학기술학회논문지
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• 제17권3호
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• pp.86-92
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• 2016

본 연구는 가황촉진제 제조공정에서 발생되는 MBT 폐수의 생물학적 처리가능성을 평가하였다. MBT 폐수는 미생물 활동을 저하시키기 때문에 생물학적으로 처리가 불가능하였지만, 7일의 순응기간을 거쳐 약 10%의 COD가 제거되었다. MBT 폐수의 화학적 전처리를 위한 최적조건은 pH 3.5, 2시간동안 교반 후 $Fe^{3+}$를 주입하여 펜톤산화를 한 경우였다. 또한, 펜톤처리 된 MBT 폐수를 제지폐수와 혼합하여 활성슬러지공정에서 처리했을 경우 MBT 폐수의 COD가 약 20% 제거되었다.

• 환경위생공학
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• 제9권1호
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• pp.29-37
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• 1994

Anaerobic treatment of wastewater of the red- bean processing industry was carried out and discussed an anaerobic sludge bed reactor( ASBR) as a preliminary study to evaluate applicability of given processes. The dimension of reactor were same as 0.09m- ID$\times $1.5m- height. The type of substrate and the hydraulic retention time( HRT) were considered as experimental variables. The synthetic wastewater with glucose in the laboratory, the wastewater from the red bean processing industry mixed with synthetic wastewater with variation of mixing percent were fed as substrate. The hydraulic retention time was changed from one day to five days. The gas production, the methane content in produced gas, efficiencies of COD removal and 55 removal were evaluated as principal characteristics. With synthetic wastewater as a substrate and at a hydraulic retention time of one day, characteristics of ASBR was the gas production(12$\ell$/day ), the methane content of produced gas(60%), the efficiency of COD removal(92%) and 55 removal(30%). With the real wastewater and at a hydraulic retention time of one day, the gas production and the efficiency of COD removal of the ASBR decreased with the proportion of real wastewater. The gas production and the efficiency of COD removal with real wastewater only was decreased to 70% and 87% of those with synthetic wastewater only, respectively. However, the methane content in produced gas and the efficiency of 55 removal with real wastewater only was increased significantly by 1.25 times and two times of those with synthetic wastewater only, respectively. However, the methane content in produced gas and the efficiency of 55 removal with real wastewater only was increased significantly by 1.25 times and two times of those with synthetic wastewater only, respectively. With real wastewater only as a substrate in the ASBR, the gas production was decreased with an increase of HRT, but the efficiency of COD removal increased with HRTI like the usual trend reported. As a conclusion, the wastewater of the red- bean Processing industry could be treated by anaerobic digestion successfully in the ASBR.Anaerobic treatment of wastewater of the red- bean processing industry was carried out and discussed an anaerobic sludge bed reactor( ASBR) as a preliminary study to evaluate applicability of given processes. The dimension of reactor were same as 0.09m- ID$\times $1.5m- height. The type of substrate and the hydraulic retention time( HRT) were considered as experimental variables. The synthetic wastewater with glucose in the laboratory, the wastewater from the red bean processing industry mixed with synthetic wastewater with variation of mixing percent were fed as substrate. The hydraulic retention time was changed from one day to five days. The gas production, the methane content in produced gas, efficiencies of COD removal and 55 removal were evaluated as principal characteristics. With synthetic wastewater as a substrate and at a hydraulic retention time of one day, characteristics of ASBR was the gas production(12$\ell$/day ), the methane content of produced gas(60%), the efficiency of COD removal(92%) and 55 removal(30%). With the real wastewater and at a hydraulic retention time of one day, the gas production and the efficiency of COD removal of the ASBR decreased with the proportion of real wastewater. The gas production and the efficiency of COD removal with real wastewater only was decreased to 70% and 87% of those with synthetic wastewater only, respectively. However, the methane content in produced gas and the efficiency of 55 removal with real wastewater only was increased significantly by 1.25 times and two times of those with synthetic wastewater only, respectively. However, the methane content in produced gas and the efficiency of 55 removal with real wastewater only was increased significantly by 1.25 times and two times of those with synthetic wastewater only, respectively. With real wastewater only as a substrate in the ASBR, the gas production was decreased with an increase of HRT, but the efficiency of COD removal increased with HRTI like the usual trend reported. As a conclusion, the wastewater of the red- bean Processing industry could be treated by anaerobic digestion successfully in the ASBR.

• 상하수도학회지
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• 제19권1호
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• pp.38-46
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• 2005

In this research, we tried to combine the coagulation/sedimentation process as pre-treatment with UF membrane filtration to reduce the membrane fouling and to improve the permeate water quality. We used the Jet Mixed Separator (JMS) as coagulation/sedimentation process. We observed that the HPC and E.Coli can't be removed through the direct UF memebrane filtation of surface water. The removal efficiency of dissolved organic substances, indicated by E260 and DOC, was 40% and 15%, respectively. However, the removal efficiency of it increased two time as a result of combination of JMS process as coagulation/sedimentation pre-treatment. This was resulted from the formation of high molecular humic micro-floc through JMS process. The accumulation amount of irreversible cake layer which was not removed by backwashing was less than direct UF membrane filtration of surface water. Moreover, the loading rate of fouling induced substances, such as humic substances and suspended substances, on membrane surface decreased drastically through JMS process. As a result, the accumulation amount of irreversible cake on membrane surface was decreased.

• 상하수도학회지
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• 제22권2호
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• pp.245-250
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• 2008

Adsorption experiment was carried out to find the adsorption capacity and characteristics of heavy metals(Cd, Pb) onto soil and mixed soil with food compost. Result showed that mixed soil having higher organic content adsorbed more heavy metal than soil, indicating that food compost can be used effectively to prevent soil pollution. Linear adsorption isotherm which adopted to find the adsorption characteristics was used to calculate Retardation Factor(R). The value of Retardation Factor(R)s of Pb and Cd in mixed soil, found as 34.54, 24.42 respectively, are higher than those in soil which were found as 4.64, 3.67, respectively. The value of Retardation Factor(R) using Freundlich adsorption isotherm could be presented by the functions of concentration and showed similar result as the linear one. But Freundlich adsorption isotherm showed higher relationship than linear one and the retardation factor(R) from freundlich adsorption isotherm was thought as more effective method to assess adsorption capacity because it could reflect gradient and intercept of the isotherm.

• 대한환경공학회지
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• 제22권10호
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• pp.1799-1808
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• 2000

본 연구에서는 구입이 용이한 황토를 이용하여 축산폐수외 화학적 응집 처리제로서의 적용가능성과 최적 응집조건을 찾고 기존에 사용되어 왔던 고분자 응집제(PAC, PACS, LAS)와 응집성능을 비교하였다. 연구 결과 황토와 생석회의 최적 혼합비율은 3:7이었으며, 이 혼합 응집제의 적정 주입량은 30 g/L이었다. 기존 응집제와 비교실험에서는 loess : lime = 3 : 7의 경우 탁도, SS, BOD, $COD_{er}$, T-P, TKN의 제거효율이 각각 95.8%, 92.5%, 71.6%, 71.1%, 98.2%. 32.5%를 나타내었다. Loess : lime = 3 : 7은 응집제로서 사용할 수 있으며, 생산된 슬러지는 토양개량제로서의 사용 가능성을 확인할 수 있었다.

• 한국환경과학회지
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• 제23권1호
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• pp.129-142
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• 2014

To treat chromaticity contained in effluents of dyeing wastewater efficiently, potent dye-degrading microorganisms were isolated from influent water, aeration- tank sludge, recycle water and settling-tank sludge located in leather and dyeing treatment plant. Six potent strains were finally isolated and identified as Comamonas testosteroni, Methylobacteriaceae bacterium, Stenotrophomonas sp., Kluyveromyces fragilis, Ascomycetes sp. and Basidiomycetes sp. When Basidiomycetes sp. was inoculated into ME medium containing basal mixed-dyes, 93% of color was removed after 8 days incubation. In the same experiment, the 1:1 mixed culture of Basidiomycetes sp. and photosynthetic bacterium exhibited 88% of color removal; however, it showed better color removal for single-color dyes. The aeration-tank and settling-tank samples revealed higher color removal (95-96%) for black dyes. The settling-tank sample also revealed higher color removal on basal mixed-dyes, which resulted in 90% color removal after 6-h incubation. From the above results, it is expected to achieve a higher color removal using the mixed microorganisms that were isolated from aeration-tank and settling-tank samples.

• 한국물환경학회지
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• 제28권6호
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• pp.796-803
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• 2012

Potential feasibility of nutrients removal and biofuel production with microalgae was evaluated in batch culture. Distribution of microalgae in fresh water including reservoir and river was investigated to search for the species with high content of lipid that could converted into biofuel. Green algae, Chlorella and Scenedesmus sp., these are known as species containing high lipid content for biodiesel production, were observed in both summer and autumn season. However another highly lipid-containing species, botryococcus sp. was not observed in this study. In mixed culture of microalgae using synthesized wastewater medium, green algae were found to be dominant, comparing to other species of diatoms and blue-green algae. And microalgae were also capable of removing nitrogen and phosphorus in batch experiments. During the culture period of 14 days, removal efficiencies of nitrate and phosphorus were 30% and 82%, respectively. Furthermore, content of the intracellular lipid extracted from algae cell was as favorable as 12-30% in the mixed culture where Scenedesmus and Chlorella sp. were dominant. Therefore the mixed culture of microalgae could be applied to biofuel production and tertiary wastewater treatment, even though there are economic barriers to overcome.

• 한국물환경학회지
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• 제22권3호
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• pp.492-497
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• 2006

Feasibility of simultaneous removal of organic materials and nitrogen in the wastewater from fisheries processing plant was evaluated using entrapped mixed microbial cell (EMMC) process. The experiment was performed using activated sludge from municipal sewage treatment plant which was immobilized with gel matrix by cellulose triacetate. It was found the stable operation at the treatment system which is composed of anoxic and oxic tank, was possible when the organic and nitrogen loading rates were increased stepwise. The organic and nitrogen loading rates were conducted from 0.65 to $1.72kgCOD/m^3/d$ and from 0.119 to $0.317kg\;T-N/m^3/d$ with four steps, respectively. The maximum nitrogen loading rate which could satisfy the regulated effluent standard of nitrogen concentration, was $0.3kg\;T-N/m^3/d$. The removal efficiency of total nitrogen was decreased apparently as increasing nitrogen loading rates, whereas the removal efficiency of ammonium nitrogen was effective at the all tested nitrogen loading rates. Therefore, it was concluded that nitrification was efficient at the system. Nitrate was removed efficiently at the anoxic tank. whereas the nitrification efficiency at the oxic tank ranged 94.0% to 96.9% at the tested loading rates. The removal efficiencies of chemical oxygen demand (COD) and those of total nitrogen at the entire system ranged from 94.2% to 96.6% and 73.4% to 83.4%, respectively.