• 한국산학기술학회논문지
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• 제11권10호
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• pp.4055-4068
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• 2010

본 연구는 고도처리공법을 적용하여 수년간 가동 중인 하수처리시설에 대한 운전현황을 측정 분석하여, 고도처리공법 적용의 적정성을 평가하고자 하였다. 단위공정별 처리효율은, BOD의 경우 1차침전지 35, 생물반응조 87, 최종방류수 48 %, T-N의 경우 1차침전지 18, 생물반응조 40, 최종방류수 25 %, T-P의 경우 1차침전지 23,, 생물반응조 38, 최종방류수25 % 등으로, 각 단위공정별로 양호한 처리효율을 나타내었다. 생물반응조 내의 미생물 관측 결과, 다양한 종류의 세균과 원생동물 및 후생동물이 관측되었고, 담체의 세균 부착기능이 안정적으로 유지되고 있음을 알 수 있었다. 최종방류수질은 BOD 5.5, COD 9.9, SS 4.6, T-N 11.8, T-P 0.99 mg/L으로 방류수 수질기준보다 낮은 양호한 수질상태를 나타내었다.

• 한국막학회:학술대회논문집
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• 한국막학회 1998년도 제6회 하계 Workshop (98 한국막학회, 국립환경연구원 국제 Workshop, 수자원 보전과 막분리 공정)
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• pp.113-133
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• 1998

In activated sludge process, sludge settling condition is affected by organic loading rate or operation condition, and if settling condition is getting worse, it is common that overall process fails due to wash-out of biomass causing low concentration in the aeration tank. Also activated sludge process has such several problems as requiring large area, consuming a lot of power and producing large volume of sludge. Increased public concern over health and the environment combined with a strong desire to reduce capital, operating and maintenance costs, have created a need for innovative technologies for building new high quality effluents which vail meet 21st century crkeria. MBR(Membrane Bioreactor) process consists of a biological reactor and ultrafiltration(UF) membrane system that replaces the conventional clarifier of an activated sludge process. The main operating advantages of this system are that the quality of the effluent is independent of the settleability of the mixed liquor and that the effluent is free of suspended solids in any operating condition. It is possible to eliminate clarifier and to reduce the volume of aeration tank because it can afford to accumulate high biomass concentration in the bioreactor(20, 000~30, 000mg/L), which would not be possible in a conventional activated sludge process. Therefore, this process reduces overall treatment plant area. In addition to those advantages, Longer SRT condition enables higher sludge digestion in MBR process so the sludge volume produced is 50 to 70% lower than that of conventional activated sludge process There are two kinds of MBR process according to the allocations of membrane. One is cross flow type MBR of which module is located outside of the bioreactor and mixed liquor is driven into the membrane module. The other is submerged type MBR process of which module is submerged in the bioreactor and mixed liquor is generally sucked from the lumen side. addition to that the cake layer is often removed by the uplifting flow of bubbling air. A submerged MBR process is superior to a crossflow MBR in regard to the power consumption because suction pressure of a submerged MBR is generally lower than that of a crossflow MBR which has recirculation pump. A submerged MBR, therefore, has the potential to be applied to small wastewater treatment plants that need low cost treatment systems.

• 유기물자원화
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• 제31권2호
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• pp.19-38
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• 2023

하수처리장에서 생물학적 질소 제거를 위한 질산화, 탈질 과정 중 6대 온실가스 중 하나인 아산화질소가 발생한다. 이번 연구에서는 온실가스 발생량을 정량할 수 있는 컴퓨터 시뮬레이션 프로그램인 EQPS를 이용해 합류식 하수를 처리하는 MLE 공법 하수처리장의 내부반송유량, 수온 그리고 유입수의 일차침전지 by-pass %에 따라 아산화질소가 가장 적게 발생하는 운전 조건을 찾았다. 내부반송 유량은 유입 유량의 200 %이고, 생물반응조 수온이 20 ℃이고 일차침전지에서 생물반응조로 by-pass 되는 유입수가 15 %일 때 아산화질소 배출 계수가 가장 적은 조건임을 확인했다. 또한 깊은 수심에서 공기를 주입하는 심층폭기는 상대적으로 적은 공기공급을 필요로 하기 때문에 일반적인 폭기조에 비해 적은량의 아산화질소가 발생함을 확인하였다.

• 자원리싸이클링
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• 제2권2호
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• pp.27-38
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• 1993

본 연구에서는 제철소에서 발생하는 전로 dust를 사용하여 심강법(분급)에 의한 철산화물을 분리하여 고순도의 철분말을 회수하였으며, 아래와 같은 결론을 얻었다. 가. 전로 dust의 물성 1) 재항의 1제강, 2제강 C/F(Clarifier) dust, 광장의 E/C(Evaporation coolar), dust, 중국강철공사(C.S.C) OM(Clarifier underflow) dust 금철분이 63~72%로 높고, Metal Fe 가 21~50% 함유되어 있으며, 기타 산화물로는 CaO, MgO, Al$_{2}O_{3}$, SiO$_{2}$ 등이 있다. 2) 재항의 1제강, 2제강 C/F dust, 광양의 E/C, E/P dust, 중국강철공사(C.S.C), OM(clarifier underflow) dust 입자의 형상은 청입이 주로 구형으로 응고된 모양이었으며, 일반적으로는 출립의 외각부는 magnetite, hematite 등으로 산화가 진해되어 있다. 3) 전로 dust 들에 대한 X-ray 회절분석결과, 재항의 1제강, 2제강, C/F dust, 광양의 E/C, E/P dust는 ${\alpha}$-Fe, FeO(wusute)가 중성분으로 존재하며 그 밖에 FE$_{3}O_{4}$9magnetite), Fe$_{2}O_{3}$ CaO가 소량으로 존재하고 있었으며, 중국강철공사(C.S.D) OM(underflow) dust는 ${\alpha}$-Fe, ${\alpha}Fe_{2}O_{3}$, graphite가 주성분으로 존재하며, 그 밖에 $Fe_{3}O_{4}$, Fe$_{2}O_{3}$, ZnO이 소량으로 존재하고 있었다. 4) 순수한 순철분말과 전로 dust를 구성하고 있는 순철은 마광에 따른 입자의 분쇄보다는 마광시 구형의 입자가 소성변형으로 인해 flake형상으로 변하여 체질입도분석시 입도의 증가를 초래하였으며, 반면 철산화물은 마광에 따른 입자의 미세화가 발생함을 볼 수 있었다. 나. 철분구 외수 실험 1) 광양의 dust를 40분간 마광하여 심강(분급)실험을 행했을 때 Fe 99.17% 품위 철분말을 37.8% 회수할 수 있었다. 2) 재항의 C/F dust를 40분간 마광하여 심강(분급)실험을 행했을 때 Fe 98.38% 품위의 철분말을 44.42% 회수할 수 있었다. 3) 70 gauss 자석을 사용하여 자력선별을 행했을 때 +65-200 mesh 사이에서 Fe 품위 98% 이상의 철분말을 회수 할 수 있으나 회수율(14%)이 낮다.

• 한국농공학회지
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• 제42권6호
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• pp.83-89
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• 2000

A depot encircled with contact oxidation canal has been developed to improve water qualityr. The depot is aimed to settle suspended solid in the flow. The oxidation canal is to contact the pollutants and oxygen in the surface of gravel filter to purify the water. The deposit of the pollutant in the depot is released by the drainage culvert located at the bottom of it. Aeration nozzle is installed to supply enough oxygen to the gravel filter layers in the bottom of the detent the flow and improve oxidation efficiency. From the experiment it is founded that 91% of SS, 39% of TN, 63% of TP and 77% of COD were removed in the system. The treatment efficiency of total nitrogen is rather lower than any other components, however, it would be higher when some floating vegetation is added in the primary clarifier. The depot and oxidation canal system would be useful to purify the flows in the mouth of the reservoirs or at the outlet of the drainage canal.

• 상하수도학회지
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• 제20권4호
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• pp.501-507
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• 2006

Dissolved air flotation (DAF) has been well known for the gravity separation process. The solids to be separated are transferred from the water body to the water surface using micro-air bubbles. DAF has also been used for enhancing solids-liquid separation of industrial and municipal wastewater by adding a its unit parallel to a sedimentation unit to reduce the hydraulic loading in the sedimentation clarifier. This study was to investigate flotation characteristics of activated sludge by the recent DAF technique without chemical agents. In addition, the effect on temperature in flotation of activated sludge and the thickening degree of activated sludge were studied.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2008년도 추계학술대회A
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• pp.1034-1039
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• 2008

Recently, the sludge suction collector is preferred rather than the scraper type sludge collector due to enhancement of the clarifier efficiency. The sludge suction collector is usually operated by the user's experience without any scientific and technical consideration. There are many factors that should be considered for higher quality of discharged water and stabilized flow in the rectangular sludge suction collector but, the optimal design on the inflow channel and orifices connecting with the inflow channel is needed for similar flow rates at the orifices. The 4 cases of channel geometry are considered and mass flow rates of each case at the orifices are evaluated using Computational Fluid Dynamics applied VOF(Volume of Fraction) model.

• Korean Membrane Journal
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• 제1권1호
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• pp.100-105
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• 1999

A novel system to thicken the concentrated colloidal solution from membrane water treat-ment processes was developed. A hollow-fiber microfilter(hydrophilic polyethylene nominal pore size 0.1 ${\mu}$m total surface area 0.42 m2) was installed in an acrylic housing that has an aeration port 5 cm below the membrane and a clarifier in the bottom. The concentrate was uniformly supplied from the top of the housing. Bacuum filtration caused downward flow of concentrate and as a result thickening interface. The addition of poly-aluminum chloride (PAC) resulted in rapid increase of trans-membrane pressure (TMP) and in no improvement of the filtered water turbidity and thickening process. Two types of con-centrate and concentrate turbidity had little effect on the increase of TMP and concentrate thickening. It was observed that for the same height of membrane housing membrane surface area to housing volume (A/V) ratio had significant effect on the increase of TMP. When the housing volume was increased ten times the increasing rate of TMP was three times faster as compared to the original housing. A hydraulic model successfully simulated the formation and sedimentation of thickening interface.

• 한국막학회:학술대회논문집
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• 한국막학회 1993년도 춘계 총회 및 학술발표회
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• pp.41-41
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• 1993

Recently, the advanced membrane separation technology has even been applied to the post treatment to biological process of wastewater treatment, since the efficiency of biological treatment significantly depends on maintaining a high biomass concentration in the bioreator. Particularly, anaerobic microbes in the biological system have slower growth rates than aerobic microbes and thus it takes a long hydaulic retention time(HRT) to prevent biomass washout in the completely mixed anaerobic digester. The anaerobic sludge also has poor settleability owing to its diffusible and somewhat filamentous nature. Moreover, the residual gasification and consequent sludge rise in the clarifier compartment become a considerable problem, which proves that complete separation of biological solids is difficult.

• 한국농공학회:학술대회논문집
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• 한국농공학회 1999년도 Proceedings of the 1999 Annual Conference The Korean Society of Agricutural Engineers
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• pp.789-794
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• 1999

The performance of a small on-site wastewater treatment system consisting of an anaerobic septic tank and upgraded absorbent biofilter was investgted . The anaerobic septic tank was used as a pre-treatment of the absorbent Biofitler instead of the primary clarifier. The treatment capacity of the system was examined by changing the hydraulinc loadings to the Absorbent Biofilter as 2.5㎥/day , 4.5㎥/day, 6.0㎥/day, respective. The effluent from the septic tank was fed into the Absorbent Bilfilter. Based on the experimental results, the quality of treated wastewater satisfied the regulation and the BOD and SS was removed down to approximately 5mg/$\ell$ and 1mg/$\ell$, respectively.