• 한국물환경학회지
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• 제20권1호
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• pp.18-23
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• 2004

In this research, a 2-stage intermittently aerated activated sludge system(IA) and intermittently aerated dynamic flow activated sludge system(DF) were investigated for the removal of nutrients in domestic wastewater. Wastewater was characterized by low C/N( organics/nitrogen) ratio. $COD_{cr}$, $BOD_s$, TKN and TP concentrations of domestic wastewater were 235, 47, 32 and 5.4 mg/L, respectively. Three sets of IA and one set of DF were operated. Three of four systems were added with fermented settled sludge taken from primary settling tank as an external electron donor and the other(IA) for control reactor was operated without addition of electron donor. All systems were operated at same sludge retention time of 20 days and hydraulic retention time of 12hrs. The supplemental electron donor was supplied into the anoxic mode. A higher denitrification rate was observed from the reactors with fermented settled sludge as an electron donor for denitrification compared to that of without addition of organic source. The result of this study indicates that the settled primary sludge, if the fermented at the acid stage, was an excellent electron donor for denitrification. 81 % of TN and 80% of TP were removed from the systems with the supplemental organic source added. However, the control reactor without addition of electron donor showed only 39% of TN and 43% of TP.

• 한국물환경학회지
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• 제25권5호
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• pp.704-712
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• 2009

Advanced Phase Isolation Ditch (APID) process was studied to develop economic retrofitting technology, for the plants where retrofitting of common activated sludge process is required. In this study, to evaluate and monitor the effluent water quality ($BOD_5$, SS, T-N, and T-P) and operating conditions (Influent, SVI, SRT, and HRT) as process capable and stable parameters for treating municipal wastewater, a demonstration plant was installed and operated in the existing sewage treatment plant of P city. During this study, the average effluent $BOD_5$, SS, T-N, and T-P concentrations were 7.7, 5.6, 10.8, and 1.6 mg/L. Trend analysis of influent $BOD_5$, SS, T-N, and T-P in APID process were illustrated that APID process need for more strong APID process management on the winter session, such as developing new intermediated aeration mode, operating methods, and managements strategy. At the application of control chart, the signal of uncommon effects at APID process was determined much higher existing control chart tntr conventional control chart in this study. These results indicate that conventional control chart has been collected and determined cleary signal at only stable situation. Therefore, newly developed APID process of dynamic control chart can be one of the useful tool for monitoring and management process.

• 한국물환경학회지
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• 제22권2호
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• pp.203-208
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• 2006

A continuous feed and cyclic draw SBR process was developed to overcome flow rate fluctuation and to maximize organic matters utilization efficiency for nitrogen and phosphorus removal. The developed SBR process was operated with two parallel reactors. Influent was supplied to one reactor which was not obligately aerated. At the same time, the other reactor was just aerated without supplying influent. In addition this mode was changed periodically. Cycle time was 6hr and aeration time ratio($t_{aer}/t_{total}$) was 0.33, respectively. $COD_{cr}$ and SS removal efficiencies of 95% or higher were achieved. Nitrogen removal was so greatly influenced by influent $COD_{cr}/T-N$ ratio. At influent $COD_{cr}/T-N$ ratio of 5.7, removal efficiencies of ammonia-N, T-N and T-P were 96%, 78% and 55%, respectively. Influent $COD_{cr}/T-N$ of 4 or higher ratio was necessary to achieve 60% or higher nitrogen removal. Organic matters of influent was efficiently utilized in denitrification reaction and consumed COD has a good correlation with removed T-N(about 6.5 mgCOD/mgTN). Continuous feed and cyclic draw SBR process could be one of alternative processes for the removal of nutrients in rural area where $COD_{cr}/T-N$ ratio was low and fluctuation of flow rate was severe.

• Journal of Animal Science and Technology
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• 제45권4호
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• pp.641-648
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• 2003

본 연구에서는 돈사 폐수내의 인과 질소를 함께 결정화하여 회수하고 그 상등액을 전기분해 시키는 회분식 돈사 폐수공정에서의 오염물질 부하량과 수처리시간 변화에 따른 처리효율의 변화 및 각 오염물질 제거특성을 파악하였다. Struvite 형성을 위한 Mg원으로는 $MgCl_2$를 사용하였고 주입량은 폐수내 인 기준 1.3 Mole이었다. 총 4개의 운전(Run I, II, III, IV)에서 얻어진 평균 제거효율과 그 제거특성을 분석한 결과 인의 경우 부하량 변화에 따른 처리효율의 변화는 관찰되지 않았으며 제거의 주요 역할을 하는 반응조는 Struvite 반응조로서 적정 Mg원만 제공된다면 pH 조절제 첨가 없이 폭기만으로도 부하량에 관계없이 88% 이상의 제거가 MAP 형성을 통해 얻어지는 것으로 나타났다. 높은 암모니아성 질소 제거효율을 유지하기 위한 적정 부하량은 약 100g/$m^3$.d로서 동 부하량 이하에서는 부하량이 증가함에 따라 제거량도 증가하면서 90% 이상의 높은 효율과 일정한 제거특성을 보인 반면 그 이상에서는 불안정한 제거특성을 나타내면서 제거효율이 감소하였다. TOCs의 경우에는 부하량 변화에 따른 처리효율 변화는 관찰되지 않았으며, 그 제거효율은 수처리 시간에 의존적인 것으로 나타났다 ($r^2$ = 0.97). 색도 제거 효율은 전기분해조 용적기준 수처리시간 2일 이상에서 94%의 매우 높고 일정한 효율을 얻을 수 있었다.

• 한국환경보건학회지
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• 제24권1호
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• pp.120-131
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• 1998

This study was performed to define the physicochemical characteristics of food waste and food wastewater, and to find the effect of moisture content variation and salinity variation on aerobic composting for food wastes. In moisture content variation experiment, the samples of 2-1, 2-2, 2-3 and 24 were prepared by the moisture content of 83.8%, 70.9%, 64.8% and 45.1%, respectively. In salinity variation experiment, the samples of 3-1, 3-2, 3-3 and 3-4 were prepared by the salinity of 0.99%, 1. 69%, 1.75% and 2.34%, respectively. In both experiments, aerobic composting reactors were operated by the mode which was composed of half an hour's stirring and 2 hour's aeration per day, for 45 days. The followings are the conclusions that were derived from this study. 1. In the study of physicochemical characteristics of food waste and food wastewater, the values of pH were 4.19 and 3.96, the values of salinity were 0.91% and 1.17%, and the values of conductivity were 7.6 mS/cm and 18.2 mS/cm, respectively. 2. In food waste, the moisture content was 60.3%, organic compound content was 96.1%, total carbon was 48.0%, total nitrogen was 1.5%(therefore, C/N ratio was 32), and the concentration of total phosphorus was 1.34 mg/kg. 3. The time of temperature ascending was delayed, the highest temperature was lowered, the duration period of high temperature was shortened by the increasing of moisture content. In the higher moisture content, anaerobic condition was formed, bad smell was released, insects were gathered and multiplicated, and the reaction rate of composting was reduced. 4. In moisture content experiment, C/N ratios were changed from the range of 31.2-34.8 at the beginning phase to that of 20.4-28.4 at the last phase. 5. In salinity experiment, the reduction rate of volume was increased(40.3%) when the salinity was decreased(0.99%). Also, the reduction rate of mass was increased(51.8%) when the salinity was decreased(0.99%). This fact denotes that salinity hinders the process of composting. 6. the concentrations of total nitrogen and total phosphorus were increased from 0.74% to 1.10%, and from 0.82 mg/kg to 3.44 mg/kg, respectively when the salinity was decreased from 2.34% to 0.99%.

• KSBB Journal
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• 제17권1호
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• pp.93-99
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• 2002

C. tropicalis ATCC 20336을 이용하여 높은 수율과 생산성으로 xylitol을 생산하기 위하여 glucose 배지에서 짧은 시간에 고농도로 세포를 배양한 후에 xylose를 첨가하여 xylitol로 전환하는 2단계 유가식 발효공정에 관한 연구를 수행하였다. Cell growth-stage에서의 배지공급 방법으로는 glucose가 모두 고갈된 후에 pH가 5.7 이상으로 올라가는 것을 신호로 glucose를 첨가하는 pH-stat 방법으로 18.5시간 배양에 의하여 67.9 g/L의 세포 농도를 얻었으며, ethanol 생성은 1.0 g/L로 매우 낮았다. Production-stage에서 최적의 초기 xylose 농도는 150 g/L이었으며, 이때에 2 g/L ($NH_4)_2SO_4$, 1 g/L $K_2HPO_4$, 0.2 g/L $MgSO_47H_2$O로 구성된 mineral salt를 2회 첨가에 의하여 xylitol의 생성이 향상되었다 그러나 0.2 vvm에서 1.0 vvm 사이의 통기조건에서는 xylitol의 생산에 큰 영향을 미치지 못하였다. 반면에 production-stage에서 yeast extract를 10 g/L가 되도록 첨가한 경우에 xylitol 수율과 생산성이 큰 폭으로 증가하였다. 즉 xylose 농도가 약 150 g/L이 되도록 232.5 g의 xylose를 2회 첨가한 경우에 배양액의 최종 부피는 1.67 L이 되었고, 이때의 xylitol 농도는 193 g/L이었으며, 수율은 70%이고 생산성은 3.55 g/L.h이었다.

• KSBB Journal
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• 제22권2호
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• pp.91-96
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• 2007

본 연구에서는 음식폐기물 효소당화액을 BC생산 배지원으로 이용하여, flask정치배양과 50 L로 규모확대한 공기순환배양기에서 BC생산성을 검토하고, 생산된 BC의 제반물성을 조사하였다. 전단력을 낮추기 위해 당화액배지에 agar를 첨가하여 10 L, 50 L 공기순환배양기에서 배양한 결과, 50 L 규모로 scale-up한 반응기에서 5.64 g/L로 10 L 공기순환배양기 (5.84 g/L)에서와 동등한 BC 농도가 얻어져 BC 대량생산에 효과적인 배양방법임이 입증되었다. 50 L 규모로 확대된 공기순환배양기를 이용하는 본 배양 방법은 BC의 저비용 대량생산을 위한 효율적인 생산 방법 중 하나가 되리라 사료된다. 또한, 당화액을 배지로 하여 공기순환 방법으로 제조한 BC의 물성을 정치배양 방법으로 제조한 BC의 물성과 비교 검토한 결과, 공기순환법으로 제조하였을 때 중합도 및 역학적 성질이 약간 저하하였으나 결정성은 비슷하였으며, 배양기 용량의 대소에 따른 물성의 변화는 거의 없었다.