• 한국축산시설환경학회지
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• 제10권2호
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• pp.81-86
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• 2004

본 연구는 유지관리비가 적게 소요되고 관리가 용이한 에너지절감형 축산뇨오수 처리기술을 개발하기 위하여 목편 살수여상과 활성오니를 정화기술하는 처리기술을 연구하였다. 1. 스크레파 축사의 축산뇨오수 처리를 위한 목편칩 살수여상 활성오니 연계 시스템을 개발하였다. 처리공정은 축산뇨오수 원수$\to$스크린$\to$목편칩 살수여상$\to$활성오니$\to$침전/오존처리 공정으로 처리하였다. 2. 처리결과 축산뇨오수 원수의 BOD 8,620mg/$\iota$ 에서 최종처리수의 BOD는 58mg/$\iota$로 처리되었다. 또한 COD_{Mn},은 원수 4,290mg/$\iota$에서 232mg/$\iota$, SS 2,228mg/$\iota$에서 49.5mg/$\iota$, T-N 4,223mg/$\iota$에서 395mg/$\iota$, T-P 97.4mg/$\iota$에서 8.0mg/$\iota$로 처리되었다. 3. SS는 목편살수여상조에서 $71.1\%$가 제거되어 활성오니 처리 대비 슬러지 발생량이 $70\%$ 절감되었다.

• 한국농공학회논문집
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• 제49권2호
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• pp.75-86
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• 2007

This process which has a connection of biofilter and sulfur-limestone has been developed to treat organic substances including BOD, COD and SS etc. and to treat sulfur-limestone is for denitrification.. The whole process consists of chemical reaction tank, sedimentation tank, trickling filter, denitrification tank The trickling filter is equipped with a reactor filled with absorptive filter, and the sulfur denitrification tank is filled with sulfur-limestone mixed media. After setting up practical facilities whose capacity is 60 tons a day, we have observed the removal efficiencies of pollutants through 60 experiments during Summer and Winter seasons. The average concentration of polluted water was BOD for 3.6 mg/L, $COD_{Mn}$ for 11.3 mg/L, SS for 2.8 mg/L, T-N for 8.6 mg/L, and T-P for 0.8 mg/L, and the rate of treatment efficiencies 96.5%, 84.7%, 96.5%, 79.2%, and 80.8%, respectively was found through the experiments. The average treatment efficiency for BOD and $COD_{Mn}$ was 85.0% and 55.7%, respectively and the average removal efficiency for NH4+-N was 84.9% in the trickling filter. The removal efficiency in the denitrification tank is as follows; The removal rate of $NO_3^--N$ was as high as 93.2% within the compass of pH 6.3 to 7.3 through $16.8{\sim}37.0mg/L$ flown into $NO_3^--N$ and $0.1{\sim}8.3mg/L$ outflown. It had observed that this process has implemented highly efficient and advanced treatment without external carbon sources and internal recycle during its process. In conclusion, this process is suitable for a sewerage in a small village due to the merits of low power consumption and easy maintenance.

• 상하수도학회지
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• 제23권1호
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• pp.129-135
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• 2009

PPCP (pharmaceuticals and personal care products) is known as micropollutant that is released from wastewater treatment plant. Research represents that these contaminants have increased in the last 10 years. This study tries to make four different trickling filter systems using plastic fiber media to remove PPCP such as acetaminophen, ibuprofen, caffeine. The results of the experiment that compares the process efficiencies of four different systems (A, B, C and D) using HBC media show that almost all the reactor has around 95% removal efficiency. Slope type HBC reactor has twice higher efficiency rather than submerged type reactor to remove PPCP in water system. In 8 hours, 89% of acetaminophen, ibuprofen, caffeine are removed in slope type reactor while 39% of them in submerged type.

• 한국수산과학회지
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• 제29권2호
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• pp.230-237
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• 1996

본 연구는 살수여상공법을 양어장 순환수 처리 장치로 설치하여 유기물질 제거 효율, 암모니아 제거효율, 동력학적 상수, 슬러지 생산량과 산소소요량 등의 최적 운전방법을 도출하였다. 유기물질 부하율이 $0.500\~0.082kg\;COD/m^3/day$에서 $66.4\~81.2\%$의 SCOD 제거 효율과 $74.5\~84.0\%$의 SBOD 제거 효율을 보였다. 암모니아 부하율이 $0.271\~0.044kg\;NH_4^+-N/M^3/day$에서 $43.7\~61.8\%$ 의 암모니아성 질소 제거 효율을 보였으며 암모니아 제거량은 $27.2\~119.5mg\;NH_4^+-N/L/day$로 나타났다. Eckenfelder 식에 의해 구한 K, n값은 각각 $0.168\;min^{-1}$과, 0.132로 나타났으며 총 생성된 슬러지 생산량은 0.233g VSS/day로 kg BOD 제거량당 생성되는 슬러지 생산량은 0.572 kg VSS/kg $BOD_{rem}$로 나타났다. 산소소요량은 3.89mg $O_2/L/hr$로 수리학적부하가 $6.712\~40.341\;m^3/m^2/day$에서 $1.33\~7.22\;mg\;O_2/L/hr$로 수리학적 부하가 증가할수록 산소소요량이 증가하였으며 미생물당 산소소모율은 1.08kg $O_2/kg$ VSS로 나타났다.

• 한국환경보건학회지
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• 제32권5호
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• pp.469-477
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• 2006

When denitrification was connected with a single stream process by using biofilter and sulfur-limestone, it was found that such connection enabled highly efficient nitrification without special unit operation of microorganisms or injection of external carbon sources which is being shown in general biological treatment processes. It was observed that in the trickling filter bed, decomposition of organic substances and highly efficient nitrification by both the forced pressure feed trickling and the air fan were simultaneously done. In the denitrification tank where sulfur-limestone was mixed at a certain ratio, limestone was used by autotrophic microorganisms as a source of supply for alkalinity, and nitrate $NO_{3}^{-}$-N was denitrified into nitrogen gas. And in the sulfur-limestone autotrophic denitrification, $NO_{3}^{-}-N\;or\;NO_{2}^{-}-N$ was denitrified as a sulfur compound in reduction state was oxidized into a final output of $SO_{4}^{-2}$. The mean concentration of the discharge water was 8.6 mg/l for T-N and 0.8 mg/l for T-P, respectively, and their mean treatment efficiency was 79.2% and 80.8%, respectively. Implementing highly efficient denitrification without injection of an external organic carbon source or internal return, it is concluded that the proposed process is suitable for a sewerage in a small village with the merits of low power consumption and easy maintenance.

• Fisheries and Aquatic Sciences
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• 제1권2호
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• pp.242-249
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• 1998

The engineering aspect of water treatment processes in the recirculating aquaculture system was studied. To recycle the water in the aquaculture system, a wastewater treatment process was required to maintain high water quality for the growth and health of the cultured fish. In this study, three different biofilm processes were used to reduce the concentration of organic matters and ammonia from the recirculating water - two phase fluidized bed, three phase fluidized bed, and trickling filter. The objectives of this research were to evaluate the optimum treatment conditions of the biofilm processes for the recirculating aquaculture system, and thereby reduce the volume of biofilm processes, which are commonly used for the recycle water treatment processes for aquaculture. The result of this study showed that the removal efficiency of organic matters by trickling filter was found to be lower than that of the fluidized bed. In the trickling filter system, anthracite showed better organic removal efficiency than crushed stone as a media. In the two phase fluidized bed, the maximum removal efficiency of either organics or ammonia was obtained when both the packing rate of media was maintained to $40\%$ of total reactor depth excepting sediment zone and the bed expansion rate was maintained to $100\%$. When 100 tilapia (Oreochromis niloticus) of each average 200g was reared, the pollutant production rate was 0.07g $NH_4\;^+-N/kg$ fish/day and 0.06g P04-3-P/kg fish/day, and sludge production rate was 0.39 g SS/kg fish/day. In the two phase and three phase fluidized bed, the volume of water treatment tank could be calculated from an empirical equation by using the relationship between the influent COD to $NH_4\;^+-N$ ratio (C/N, -), media concentration (Cm, g/L), influent ammonia nitrogen concentration (Ni, mg/L), effluent ammonia nitrogen concentration (Ne, mg/L), bed expansion rate $(E,\;\%)$, and influent flowrate $(Q,\;m^3/hr)$. The empirical equation from this study is $$V_2\;=\;10^{3.1279}\;C/N^{3.5461}\;C_m\;^{-3.7473}\;N_i\;^{4.6477}\;E^{0.0326}\;N_e\;^{-0..8849}\;Q\;(Two\;Phase\;FB) V_3\;=\;10^{11.7507}\;C/N^{-1.2330}\;C_m\;^{-6.5715}\;N_i\;^{1.5091}\;N_e\;^{-1.8489}\;Q (Three\;Phase\;FB)$$

• 한국미생물·생명공학회지
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• 제8권2호
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• pp.135-142
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• 1980

The process of biological treatment of organic wastewater is principally associated with those of self-purification in the natural water environment. The treatment system has e intensive function of stabilizing wastewater more effectively than in natural water, which is like natural water concentrated in a small space. Biological treatment of wastewater involves activated sludge and various modified process, trickling filter, rotating disk, oxidation ditch, etc. for aerobic decomposition and anaerobic processes such as anaerobic decomposition and methane fermentation. The basic characteristic of these processes is the use of mixed culture for the conversion of pollutants. This review forcuses on the various kinds of microorganisms related to each treatment processes. Kinetic analysis of the activated sludge process is discussed in order to understand the basis of control and maintenance of the biological treatment process.

• Korean Chemical Engineering Research
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• 제53권4호
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• pp.482-488
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• 2015

생물학적 방법에 의한 대기오염물질 처리는 기존의 처리방법을 대체할 수 있는 방법으로 각광을 받고 있다. 생물학적 처리방법은 유기화합물 또는 악취가 포함된 저농도 고유량의 공기를 처리하는데 효과적이다. 생물살수여과법을 이용한 대기오염물질 제거에서 물질전달 연구는 공정 최적화를 위해 매우 중요한 부분이다. 본 연구에서는 3상의 물질전달이 이루어지는 생물살수여과법에서 기체/액체(살수액), 기체/고체(미생물), 액체/고체 물질전달 실험방법 개발과 물질전달 현상을 고찰하였다. 또한 본 연구에서는 각 상간에서 물질전달에 영향을 미치는 인자로 동적적체량, 기/액 유량비, 반응기내 미생물량, 살수액 순환량 등에 대해 고찰하였다.

• 한국수산과학회지
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• 제12권3호
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• pp.175-179
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• 1979

대체로 활성슬럿지 공법에서 가장 큰 문제점은 처리후의 미생물의 분리, 슬럿지 반송, 잉여슬럿지의 소화이다. 반면에 생물학적 고정막을 이용한 RBC, 실수여과상, 고정층활성 슬럿지 공법들은 이와같은 문제가 해소된다. 최근 침전시설 및 농축조를 설치할 필요가 없느 반고정망 활성슬럿지 공법이 개발되었다. 이 공법은 최종 처분할 슬럿지량도 감소되며, 유출수의 수질도 양호하고 최대축척용량으로 유출수의 수질은 추정할 수 있으나, 반응조가 동적인 수리학적 양상의 결여 되어있었다. 따라서 본 연구에서는 반응조가 좀더 동적 수리학적 양상이 되도록 설계하여 운전하였으며 그 운전결과는 다음과 같다. REMSMAS 공법은 침전시설 및 농축시설없이도 양호한 유출수를 얻을 수 있었으며 슬럿지 부착능력도 RESMAS 공법이나 FAST 공법 보다 크게 나타났으며 최대축척용량에 도달되는 한계운전기일은 대략 유기물부하량에 비례하였다.

• Korean Chemical Engineering Research
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• 제53권4호
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• pp.489-495
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• 2015

대기오염물질처리를 위한 생물살수여과법에서 물질전달현상을 이해하기 위한 선행 실험결과를 기초로 각각의 운전조건에서 기체/액체(살수액), 기체/고체(미생물)와 액체/고체에서의 model을 이용하여 물질전달계수를 평가하였다. 생물살수여과법에서 기/액에서는 정상상태물질수지, 그리고 액/고와 기/고에서는 동적물질수지를 이용하여 물질전달 model을 확립하고 그 결과를 고찰하였다. 물질전달 model은 여과탑을 일정크기 구획하여, 각 구획에서 동적 물질수지식을 수치해석 전산코드를 이용해 계산하였다. 동적물질수지식을 이용하여 계산된 결과는 실험결과와 비교하여 생물살수여과법에서 기/액, 기/고, 액/고 각상간의 물질전달계수($K_La$)를 산정하였다. 본 연구에서는 대기오염제어를 위한 생물살수여과법에서 물질전달계수를 결정하기 위한 실험방법개발과 model을 이용하여 물질전달현상을 고찰하였다.