• 한국환경과학회지
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• 제5권3호
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• pp.361-367
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• 1996

An inverse fluidized-bed biofilm reactor (IFBBR) was used for the treatment of highly-emulsified oily wastewater. When the concentration of biomass which was cultivated in the synthetic wastewater reached to 6000 mg/1, the oily wastewater was employed to the reactor with a input COD concentration range of 50 mg/1 to 1900 mg/l. Virtually the IFBBR showed a high stability during the long operation period although soma fluctuation was observed. The COD removal efficiency was maintained over 9% under the condition that organic loading rate should be controlled under the value of 1.5 kgCOD/$m^3$/day, and F/M ratio is 1.0 kgCOD/kgVSS/day at $22{\circ}C$ and HRT of 12 hrs. As increasing organic loading rates, the biomass concentration was decreased steadily with decreasing of biofilm dry density rather than biofilm thickness. Based on the experimental jesuits, it was suggested that the decrease in biofilm dry density was caused by a loss of biomass inside the biofilm.

• 상하수도학회지
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• 제7권1호
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• pp.5-12
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• 1993

The objectives of this paper are to present data to illustrate how an advanced digestion process, two-phase digestion, can provide superior performance in terms of waste stabilization efficiency and net energy recovery. As the result, it is possible to separate enrichment cultures of acidogenic and methanogenic organisms in isolated environments by kinetic control involving manipulation of dilution rates. In single-phase digestion process, HRT and COD loading for effective operation were 14.29 days and 2.33kg $COD/m^3$ day, but two-phase digestion may be conducted efficiently at 7 days of HRT and 5.71kg $COD/m^3$ day of loading. Data from this studies showed that the two-phase process is better than single-phase digestion under all test conditions when compared on the bases of gas yield and production rate, reductions of COD and VS, buffer capacity, and unconverted volatile acids in the effluent.

• 한국관개배수논문집
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• 제21권1호
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• pp.55-63
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• 2014

A sedimentation basin for agricultural water quality improvement was researched to analyze the water quality purification characteristics. The sedimentation basin constructed at the inlet of Gamdon reservoir in Muan-gun, Jeollanam-do was selected as the research field of this study. The surface area of the sedimentation basin is $34,000m^2$, volume is $122,000m^3$, and hydraulic retention time is 0.3hr~7.3day. The average influent loading of SS was 156.6kg-SS/d, and the effluent loading was 67.5kg-SS/d with the average removal rate of 56.9%. The average influent loadings of BOD and COD were 33.0kg-BOD/d and 60.3kg-COD/d respectively, and the effluent loadings were 26.4kg-BOD/d and 48.6kg-COD/d with the average removal rate of 20.1% and 19.3% respectively. Therefore, the results of this study show that a sedimentation basin can purify SS and organic matters. The average influent loadings of T-N and T-P were 28.7kg-TN/d and 2.97kg-TP/d respectively, and the effluent loadings were 16.3kg-TN/d and 1.41kg-TP/d with the average removal rate of 43.0% and 52.6% respectively. In conclusion, the overall results of this study show that a sedimentation basin is a feasible alternative to purify organic matters and nutrients.

• 토지주택연구
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• 제2권1호
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• pp.87-92
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• 2011

음식물폐기물 처리 과정에서 발생되는 음폐수의 효율적인 처리를 위한 혐기소화공정을 선정하기 위하여, 단상 및 이상혐기소화공정을 대상으로 데모플랜트(일 5톤 처리용량)를 활용하여 성능을 비교하였다. TS, VS, tCOD 및 sCOD 처리율을 비교하여 보면 모든 항목에서 단상혐기소화공정의 처리율이 우수하였지만, 바이오가스는 오히려 이상혐기소화공정에서 더 많이 발생하였다. 이는 단상혐기소화공정의 경우 운전기간 동안 음폐수 투입량이 상대적으로 적어 처리효율은 뛰어 났지만, 음폐수 투입량 변동에 따른 바이오가스의 발생이 민감하게 반응을 한 결과로 해석된다. 이상혐기소화공정의 경우 총 COD가 상대적으로 매우 낮은 수준임에도 불구하고 바이오가스 발생량은 단상혐기소화공정보다 많이 발생되었다. 이는 음폐수 투입량이 일정하게 유지되었고, 산발효공정과 메탄발효공정이 분리되어 운영됨으로써 공정 전체가 안정적으로 운영되었기 때문인 것으로 판단된다. 음폐수처리를 위해서는 공정 선정이 중요하지만 단순 유기물처리율 비교만으로는 종합적인 평가가 어려우며, 이를 보완하기 위하여 원료성상, 투입량, 처리율, 운전기간, 바이오가스발생량 등을 종합하여 소화성능을 평가하여야 할 것이다.

• 한국환경과학회지
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• 제24권2호
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• pp.221-228
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• 2015

In this research traditional Buddhist dietary life style was studied as an alternative for both saving water and decreasing water pollution from household. A traditional dietary life style for the Buddhist monks, called Balwoo Gongyang, and its modernized one for citizens, called Dish Gongyang were examined with water use amount, wastewater quality and pollutant loading rate, and were compared with the kitchen wastewater from household. And several types of natural detergent were also examined to compare their effect on the wastewater quality and pollutant loading rate. This research was carried out using the wastewater from Balwoo and Dish Gongyang in J building located in Seoul. Wastewater generation from Balwoo Gongyang that was about $1.0{\ell}$/capita/day was very low compare to that from dish washing in normal household($32.6{\ell}$/capita/day). In case of Dish Gongyang, water generation was 1.8 times higher than that from Balwoo Gongyang, but it was just 1/19.2 of normal household. When the wastewater quality of Balwoo Gongyang was compared with the kitchen wastewater of normal household, SS was 1/16($15mg/{\ell}$), COD was 1/7($22.1mg/{\ell}$), BOD was 1/9($24.1mg/{\ell}$) and T-N was 1/16($1.7mg/{\ell}$). Pollutant loading rate from Balwoo Gongyang was very low, COD 18.0 mg/capita/day, SS 12.3 mg/capita/day and it was 1/290, 1/639 of that from dish washing wastewater from normal household, respectively. Pollutant loading rate from Dish Gongyang was also low 1/13(SS)~1/144(TN) compared to dish washing wastewater from normal household. As a natural detergent, used water from washing rice showed very low pollutant loading rate. It was concluded that Dish Gongyang that was a modernized and simplified dietary life style of Balwoo Gongyang, was very eco-friendly. Especially when it was combined with natural detergents using by-product from cooking process, its effect on the water pollution was very low.

• 유기물자원화
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• 제8권4호
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• pp.78-85
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• 2000

음식물쓰레기의 산발효 침출액은 중온의 UASB 반응조에서 매우 효과적으로 처리되었다. COD 제거율은 부하율 $15.8g\;COD/{\ell}{\cdot}d$까지 96%이상의 효율을 유지하였으며, 메탄생성율은 $5.5{\ell}/{\ell}{\cdot}d$까지 증가하였다. 제거된 COD 중에서는 92%가 메탄으로 전환되었고 나머지는 미생물로 전환된 것으로 보인다. 부하율 $18.7g\;COD/{\ell}{\cdot}d$ 이상에서는 COD 제거율이 크게 감소하였는데, 이는 10.6 h 이하의 짧은 HRT에 의한 슬러지의 부상 및 washout에 기인한다. SMA(specific methanogenic activity) 값은 뷰틸산에 대하여 가장 컸고, 프로피온산에 대하여 가장 작았는데, 이는 유출수 중에서 잔류 프로피온산의 농도가 가장 높았던 사실과 일치한다. 대표적인 미생물은 Methanosaeta였으며, 운전기간 동안 슬러지의 입경이 증가하여 식종균에는 전체 양의 64.3%가 1.4 mm보다 작았지만 운전 후에는 75.1%가 1.4 mm 이상을 차지하였다.

• 상하수도학회지
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• 제13권4호
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• pp.35-44
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• 1999

In this study, it was attempted to remove nitrate and carbon in a single-stage reactor using acetate as substrate. Hybrid type upflow sludge baffled filter reactor was adopted using anaerobic sludge. Sludge bed in the bottom of reactor was intended to remove carbon and nitrate by denitrification and methanogenesis. And floating media in the upper part of reactor were intended to remove remaining carbon which was not removed due to the inhibition of nitrogen oxide on methane producing bacteria. The reactor removed over 96% of COD and most of nitrate with volumetric loading rate of $4.0kgCOD/m^3{\cdot}day$, hydraulic retention time of 24hr, 4,000mgCOD/L, and $266mgNO_3-N/L$. Nitrate in anaerobic sludge was converted to nitrogen gas(denitrification) or ammonia (ammonification) according to pH of influent, COD removal efficiency was easily affected by the change of volumetric loading rates and nitrate concentration. And when influent pH was about 4.7, most nitrate changed to ammonia while when influent pH was about 6.8~7.0, most nitrate denitrified independent of $COD/NO_3-N$ ratio. Most granules were gray and a few were black. In gray-colored granule, black inner side was covered with gray substance and SEM illustrated Methanoccoci type microorganisms which were compact spherical shape. Anaerobic filter removed residual COD effectively which was left in sludge bed due to the inhibition of nitrogen oxide.

• 한국환경과학회지
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• 제11권3호
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• pp.209-214
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• 2002

The lab-scale anaerobic continuous reactor which was filled with the sludge of anaerobic digestion from Suyoung wastewater treatment plant was operated by feeding of various concentrations and flow rates. This experiment indicated that more than 6,870 mgCOD/L of substrate concentration was required to promote good metabolism and growth of anaerobic biomass. And increasing loading rate slowly was also required in order to treat substrate of higher concentration and higher loading rate. The substrate concentration of about 10,000 mgCOD/L was adequate to generate biogas efficiently. The pH was sharply decreased at the onset of higher leading rate, but the pH was restabilized soon at 8. During the experiment, the amount of the attached biomass was kept constant.

• Applied Biological Chemistry
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• 제37권4호
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• pp.303-309
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• 1994

광합성세균을 이용한 농축산가의 소규모 가축 폐수처리공정 개발을 위한 연구의 일환으로 고농도에서 유기산의 자화율이 높은 Rhodopseudomonas palustris KK14를 사용하여 돈분폐수처리공정의 최적화를 flask-scale 및 laboratory-scale에서 실시하였다. 반연속식으로 실시한 flask-scale에서 광합성세균 반응조는 HRT 6일, 광합성세균오니량 5%(v/v), 반송오니량 10%(v/v)로 했을 때 안정된 83%의 COD 제거율 및 적절한 $4{\sim}5\;g/l$의 MLSS가 유지되었다. 산생성 반응조와 광합성세균 반응조의 working volume을 각각 5.2 l와 15 l로 scale-up한 실험실적 실험에서는 원폐수 대비 COD와 BOD의 제거율이 각각 95%와 96%를 나타냈으며 광합성세균 반응조의 COD 용적부하율 및 오니부하율은 각각 $3kg\;COD/m^3/day$와 1.1kg COD/kg MLSS/day를 유지함으로써 적당한 MLSS농도가 유지되었고 부가적으로 폐수처리가 진행되면서 악취가 제거되는 효과를 나타내었다.

• Environmental Engineering Research
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• 제23권1호
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• pp.70-75
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• 2018

A pilot scale anaerobic fixed-bed with a reactor volume of $2.8m^3$ was built to treat slaughterhouse wastewater. Bamboo rings were chosen as support media mainly because of their cheaper price in underdeveloped countries. Even with their lower porosity and specific surface, the reactor performance showed a maximum 95% COD removal efficiency at an organic loading rate (OLR) of $1kg\;COD/m^3-d$ with its corresponding hydraulic retention time (HRT) of 7.5 d. At a higher OLR of $4.0kg\;COD/m^3-d$, the COD removal efficiency of 75% was achieved with an HRT of 2 d. No big difference in COD removal efficiencies was found between the reactors operated in both upflow and downflow modes. Their operational behavior and effluent characteristics were similar. The effluent COD/TKN ratio of 6.67 at an OLR of $4.0kg\;COD/m^3-d$ was only marginal acceptable range for a subsequent biological denitrification process. Otherwise carbon supplementation is required at a lower OLR.