• 한국환경보건학회지
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• 제24권1호
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• pp.62-69
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• 1998

It has been studied that the measurement of odor component emission at confectionery manufacture. The objects of this study were to investigate reduction of offensive odor. The survey effects of odorous materials are presented as follows. The countermeasure of operating process is to minimize sludge sediment in each unit facility. Especially, in summer, we have to clean the sludge frequently, because anaerobic decomposing is likely to occur easily. The sludge or scum from sedimentation tank pond, and floating tank should be treated quickly. We should avoid overloading operation. In the case of overloading, dissolved oxygen should be increased, the quality of wastewater input should be decreased. When dried cakes from condense tank or floating tank are left in treatment plant, we should cover, to prevent diffusion of smell with masking materials. The seasonal condition of operating should be fixed and the kind of coagulants should be changed because the wastewater in each season have different loading rates and organic materials. Odorous materials are very sensitive to the seasonal temperature variation. Especially, when the amount of rainfall is small and the high temperature of maintenance in long periods, air diffusion rate is large, so odorous materials can make great effect on surroundings comparision with other periods. To reduce odorous gas, as short term method, we had better take ceramic addition method. Especially, in summer we should take ceramic addition method. Also, as long term method, the size of wastewater treatment facility is the most important in the normal operating of wastewater treatment facility. But wastewater treatment facilities in this factory are too old, treatment process is old fashion, and the size is too small. So, large wastewater quantity to treat in summer. As results, the expansion of wastewater treatment facility and the process of improvement are required. Restriction level of odor was exceed. As it is overloaded in summer, the basis cause of odor is that the size of wastewater treatment facility is small. The prediction of air quality equilibrium density variation show that the odorous materials from working place are Amine materials whose smell strength is about 2.5(a little strong degree). We can suppose that in summer is sensitive to temperature variation, smell strength is larger as to reduce the origin of odor. We must expand wastewater treatment facility and improve the process A.S.A.P.

• Journal of Microbiology and Biotechnology
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• 제28권4호
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• pp.630-637
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• 2018

The high rate algal ponds (HRAP) powered and mixed by a paddlewheel have been widely used for over 50 years to culture microalgae for the production of various products. Since light incidence is limited to the surface, water depth can affect microalgal growth in HRAP. To investigate the effect of water depth on microalgal growth, a mixed microalgal culture constituting three major strains of microalgae including Chlorella sp., Scenedesmus sp., and Stigeoclonium sp. (CSS), was grown at different water depths (20, 30, and 40 cm) in the HRAP, respectively. The HRAP with 20cm of water depth had about 38% higher biomass productivity per unit area ($6.16{\pm}0.33g{\cdot}m^{-2}{\cdot}d^{-1}$) and required lower nutrients and energy consumption than the other water depths. Specifically, the algal biomass of HRAP under 20cm of water depth had higher settleability through larger floc size (83.6% settleability within 5 min). These results indicate that water depth can affect the harvesting process as well as cultivation of microalgae. Therefore, we conclude that water depth is an important parameter in HRAP design for mass cultivation of microalgae.

• 물과 미래
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• 제25권2호
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• pp.61-66
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• 1992

본 실험은 3개의 F/M 비 0.36, 0.2, 0.1 mg COD/daymg MLSS로 실험실 규모의 활성슬러지법에 의해 전선공장폐수를 처리사고, 유입수와 유출수의 Daphnia magna에 대한 급성독성을 연구하였다. Daphnia Magna를 이용하여 실험실 bioassay를 수행한 결과는 다음과 같다. 1) 유입수의 24hr, 48hr-LC50은 각각 17.33%, 11.73%이었다. 2) F/M 비 0.36, 0.20, 0.10 mg COD/daymg MLSS로 운반된 유출수의 24hr-LC50은 각각 26.69%, 32.70%, 38.36%ldau, 48hr-LC50은 각각 14.58%, 27.88%, 31.58% 이었다. 3) 활성슬러지 시스템의 유출수와 그 유출수의 여과액에 대한 48hr-LC50의 비는 F/Mql 변화에 따라 각각 1.58, 1.83, 1.47로, 여과함으로써 독성이 감소하였다. 4) 활성슬러지 시스템의 유출수를 다시 활성\ulcorner으로 흡착한 처리수는 Daphnia magna에 거의 독성을 주지 않았다.

• 한국전기전자재료학회:학술대회논문집
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• 한국전기전자재료학회 2009년도 하계학술대회 논문집
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• pp.354-354
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• 2009

We have developed the prototypes of superconducting magnetic separation system with high temperature superconductor wire. This separation filter system consist of magnetized matrix SUS430 wire and acrylic frame. This study introduced rolled steel process coolant wastewater applied superconductor HGMS(High Gradient Magnetic Separation). HGMS treatment have acted high efficient method for various wastewater. We have surveyed superconducting magnetic separation technology and reviewed the status of related industries using applied superconductivity. In our basic preliminary experiment using HGMS, it was made clear that the fine para-magnetic particles in the wastewater obtained from rolling process of steel can be separated with high efficiency. We investigated the ability of magnetic flock formation, which used inorganic materials and polymer coagulants. We had a purpose to remove SS of coolant at steel factory. Maximum coagulation remove rate of SS 98%. Removing ratio of $Fe_3O_4$ fine particles in wastewater showed over than 99% in the wastewater containing magnetic fines after four times of repetition of separation.

• 한국전기전자재료학회:학술대회논문집
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• 한국전기전자재료학회 2010년도 하계학술대회 논문집
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• pp.44-44
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• 2010

Conventional water treatment facilities like precipitation process need large-scale equipment and wide space to purify the wastewater of paper factory. In case of massive waste water, high gradient magnetic separation (HGMS) parts are more effective to purify it rapidly and to occupy relatively small space, since large voids at filter with HGMS are adopted. Cryo-cooled Nb-Ti superconducting magnet with room temperature bore in diameter of 100 mm and 600 mm in height was used for magnetic separator. Magnetic filters were designed by the analysis of magnetic field distribution at superconducting magnets.

• 한국환경보건학회지
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• 제27권1호
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• pp.93-99
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• 2001

This study aims at finding out pertinent reaction conditions for treating high concentration ammonia contained in N-chemical factory wastewater with decompressed ammonia stripping method that was designed. And it also tries to investigate adsorption capability of removed ammonia to soil. The results from experiments are as follows ; 1. The removal rate of N $H_3$-N of synthetic wastewater was under 85% at pH 10 with decompressed ammonia stripping method. The reaction time in pressure 360 mmHg at pH 11 and 12 was shorter than in 460 mmHg, and the removal rate of N $H_3$-N with decompressed ammonia stripping method at 9$0^{\circ}C$ was 11~15% higher than air stripping 2. The optimum conditions for decompressed ammonia stripping with synthetic sample were shown as pH 12, temperature 9$0^{\circ}C$, internal reaction pressure 460 mmHg and reaction time 50 minutes. These conditions were applied to treat the wastewater containing organic-N 290.5mg/$\ell$, N $H_3$-N 168.9mg/$\ell$, N $O_2$-N 23.2mg/$\ell$, N $O_3$-N 252.4mg/$\ell$, T-N 735mg/$\ell$. Organic-N turned out to be removed 60%, the removal rate of N $H_3$-N IS 94%, T-N is 50%. But N $O_2$-N and N $O_3$-N were increased with 7.8% and 14.9% respectively. 3. The CO $D_{Sr}$ removal rate in decompressed ammonia stripping reaction was 42% and S $O_4$$^{2-}$ was removed 8.2%. It was turned out caused with higher pH and thermolysis. 4. In soil adsorption of ammonia desorbed from the decompressed stripping process of wastewater, the recovery rate was 76% in wet soil.

• Environmental Engineering Research
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• 제21권2호
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• pp.196-202
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• 2016

Membrane bioreactor (MBR) technology has previously been used by water industry to treat high salinity wastewater. In this study, an anoxic-oxic biofilm-membrane bioreactor (AOB-MBR) system has been developed to treat mustard tuber wastewater of 10% salinity (calculated as NaCl). To figure out the effects of operating conditions of the AOB-MBR on membrane fouling rate ($K_V$), response surface methodology was used to evaluate the interaction effect of the three key operational parameters, namely time interval for pump (t), aeration intensity ($U_{Gr}$) and transmembrane pressure (TMP). The optimal condition for lowest membrane fouling rate ($K_V$) was obtained: time interval was 4.0 min, aeration intensity was $14.6 m^3/(m^2{\cdot}h)$ and transmembrane pressure was 19.0 kPa. And under this condition, the treatment efficiency with different influent loads, i.e. 1.0, 1.9 and $3.3kgCODm^{-3}d^{-1}$ was researched. When the reactor influent load was less than $1.9kgCODm^{-3}d^{-1}$, the effluent could meet the third discharge standard of "Integrated Wastewater Discharge Standard". This study suggests that the model fitted by response surface methodology can predict accurately membrane fouling rate within the specified design space. And it is feasible to apply the AOB-MBR in the pickled mustard tuber factory, achieving satisfying effluent quality.

• 도시과학
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• 제6권2호
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• pp.17-27
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• 2017

최근, 하천의 수질오염 및 악취발생으로 민원이 증가하여 하천환경개선에 큰 관심이 모아지고 있다. 본 연구의 목적은 하수 유입부에 대해 무인항공기(UAV)를 활용하여 RGB 및 적외 열 영상을 획득하고 하천제방 정비 계획 및 하천 오염 현황의 모니터링을 위한 응용성을 검토하였다. 특히, 하천 인근 공장에서 배출되는 폐수를 적외 열 영상으로 검출하여 폐수의 전파를 모니터링하였다. 또한 하천 제방 정비대상 지역과 인근지역에 대한 RGB영상을 SfM(Structure from Motion)기반 영상 해석을 통해 고정밀 3차원 모형을 제작하고 정확성을 검토하였다. 연구결과, UAV영상을 활용, 폐수유입에 따른 하천의 온도변화를 감지하여 수질오염의 유입부 및 전파 현상을 모니터링 할 수 있었다. 또한 고정밀 3차원 모델(수치지형도, 정사영상)을 제작, 정확성을 검토하고 하천의 제방정비를 위한 정밀 3차원 정보 및 식생 피복정보를 도출할 수 있었다.

• 멤브레인
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• 제24권1호
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• pp.63-68
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• 2014

주류를 제외한 과일 및 탄산음료 등을 제조하는 비알코올성 음료품 제조시설에서 발생되는 폐수는 높은 농도의 유기물과 낮은 농도의 질소, 인 등을 함유한다. 이러한 폐수의 처리 시설은 주로 호기성 공정과 약품응집 공정으로 구성하고 후단에 사여과지 또는 활성탄 공정을 추가하기도 한다. 하지만 이러한 방식은 긴 체류시간과 침전지 설치로 인해 많은 부지를 필요로 하는 문제가 있다. 본 연구에서는 부지소요 문제와 슬러지 유출로 인한 수질저하 문제를 해결하고자 W식품공장 폐수처리장 인근에 MBR pilot plant를 설치하고 장기간 운영을 통해 데이터를 확보하고 처리 효율을 평가하였다. 약 3개월간 음료수 제조공정 폐수를 평막을 적용한 MBR pilot plant로 운전조건을 변화하며 처리한 결과, 처리유량 $20m^3/day$, HRT 29 hr, 4Q 반송조건까지는 유기물 제거율 97% 이상으로 안정적인 처리가 가능했다. 하지만 그 이상의 운전조건에서는 생물반응조의 오염물질 제거율이 감소하였고 TMP가 급격히 증가하는 모습을 보였다.

• 에너지공학
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• 제10권3호
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• pp.195-205
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• 2001

염색가공공정은 에너지 다소비형이며, 염색조업을 수행하는 과정에서 약 4$0^{\circ}C$ 정도의 열원폐수를 다량으로 방출하고 있지만 이를 회수할 수 있는 기술개발이 이루어지지 않아서 아직 미활용되고 있다. 본 연구에서는 이와 같은 열원폐수의 열을 회수하여 이용할 수 있는 방안을 마련하기 위하여 먼저 염색공정의 특성을 고찰하고. 직물별, 공정별 에너지원단위를 조사한 결과 상대적으로 에너지원같위가 높은 T/C, T/R 교직물 업체나 폴리에스테르 염색업체에서 폐수열을 회수하여 이용하기에 적합한 것을 알 수 있다. 그리고 염색업체별, 계절별 폐수의 배출량과 온도를 조사한 결과 각 업체당 평균 폐수배출량은 20,470톤/월이고, 평균폐수온도는 41.$0^{\circ}C$로 나타났다 또한, 배관 침적, 폐쇄 등으로 폐열회수시스템의 안정적 운전이나 열교환기의 성능에 악영향을 끼칠 수 있는 SS의 경우 폴리에스테르 염색폐수가 가장 낮아 폴리에스테르 염색폐수가 폐열회수에 가장 유리할 것으로 판단되었다. 염색공장에서 기존에 사용하고 있는 시스템과 폐수열이용 시스템의 에너지단가를 비교해보면 폐열회수시스템에서 압축식 열펌프를 적용하면 에너지단가는 22.50원이 되어 매우 경제적이며, 증기생산을 위한 보일러 연료로 LNG를 사용하는 업체에 압축식 폐열회수시스템을 적용할 경우가 투자비 회수기간이 2.09년으로 경제성이 매우 우수한 것으로 나타나 열펌프시스템의 적용기술을 보급할 수 있는 기반을 마련하였다.