• Title/Summary/Keyword: Phosphorous removal

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Simultaneous Removal of Organic Pollutants, N, P, and Antibiotics from Liquid Fertilizer using a Microbubble and Catalyst Coupling System (마이크로버블/촉매 융합 시스템을 이용한 액비 내 유기오염물질, N, P 및 항생제 동시 제거)

  • Lee, Dong Gwan;Sim, Young Ho;Paek, Yee;Kwon, Jin Kyung;Jang, Jae Kyung
    • Journal of Environmental Science International
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    • v.28 no.11
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    • pp.983-991
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    • 2019
  • This study investigated the use of a hydroxyl-radicals-generated microbubble/catalyst (MB/Cat) system for removing organic pollutants, nitrogen, and phosphorous from liquid fertilizer produced by livestock wastewater treatment. Use of the MB/Cat system aims to improve the quality of liquid fertilizer by removing pollutants originally found in the wastewater. In addition, a reduction effect has been reported for antibiotics classified as representative non-biodegradable matter. Samples of liquid fertilizer produced by an aerobic biological reactor for swine wastewater treatment were first analyzed for initial concentrations of pollutants and antibiotics. When the MB/Cat system was applied to the liquid fertilizer, TCOD, TOC, $BOD_5$, and $NH_3-N$, and $PO_4-P$ removal efficiencies were found to be approximately 52%, 51%, 30%, 21%, and 66%, respectively. Additionally, Amoxicillin hydrate was removed by 10%, and Chlortetracycline HCl and Florfenicol were not present at detectable levels These findings confirm that the MB/Cat system can be used with livestock wastewater treatment to improve liquid fertilizer quality and to process wastewater that is safe for agricultural re-use.

Evaluation of Improvement on Sediment for Practical Application in Prawn Farm (새우 양식장에 적용을 위한 저질개선 평가)

  • Kim Woo-Hang;Kim Doo Hee
    • Proceedings of KOSOMES biannual meeting
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    • 2004.05b
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    • pp.81-84
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    • 2004
  • Control of Sediment is very important in prawn farm due to the eruption of toxic material such as W1ionized H2S, NH3 and NO2-. In this study, column test study, column with filter media such as activated carbon, zeolite, oyster shell and iron chloride to evaluate the reduction of toxicity from sediment ammonia-N(NH3) was effectively removed by Zeolite and oyster shell. It was indicated that ammonium ion(NH4+) was removed by ion exchange of zeolite. And the ammonia in the column of oyster shell was existed as the form of NH4+, which is not toxic for prawn because oyster shell was stably kept around pH 8. Therefore, some of ammonia(NH3) was reduced by oyster shell. Hydrogen sulfide and COD were effectively removed by adsorption of activated carbon and a partial removal of hydrogen sulfide was accomplished by Oyster shell. Phosphorous was removed by activated carbon, oyster shell and iron chloride. In prawn farm, the concentration of ammonia was increased with increase of pH by algae photosynthesis in the column of activated carbon, zeolite and iron chloride, but it was revealed that pH was stably kept in the column of oyster shell.

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Advanced Treatment of Wastewater from Food Waste Disposer in Modified Ludzack-Ettinger Type Membrane Bioreactor

  • Lee, Jae-Woo;Jutidamrongphan, Warangkana;Park, Ki-Young;Moon, Se-Heum;Park, Chul
    • Environmental Engineering Research
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    • v.17 no.2
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    • pp.59-63
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    • 2012
  • This paper proposes a modified Ludzack-Ettinger (MLE) type membrane bioreactor (MBR) as a method of treatment for wastewater from food waste disposer. Micro-membrane filtration allows for an extremely low concentration of suspended solids in the effluent. The effluent of the reactor in question is characterized by a relatively high level of non-biodegradable organics, containing a substantial amount of soluble microbial products and biomass. Results obtained in this paper by measurement of membrane fouling are consistent with biomass concentration in the reactor, as opposed to chemical oxygen demand (COD). The MLE process is shown to be effective for the treatment of wastewater with a high COD/N ratio of 20, resulting in are markedly high total nitrogen removal efficiency. Denitrification could be improved at a higher internal recycle ratio. Despite the low concentration of influent phosphorus, the phosphorus concentration of the outflow is seen to be relatively high. This is because outflow phosphorous concentration is related to COD consumption, and the process operates at along solids retention time.

Water Digital Twin for High-tech Electronics Industrial Wastewater Treatment System (I): e-ASM Development and Digital Simulation Implementation (첨단 전자산업 폐수처리시설의 Water Digital Twin(I): e-ASM 모델 개발과 Digital Simulation 구현)

  • Shim, Yerim;Lee, Nahui;Jeong, Chanhyeok;Heo, SungKu;Kim, SangYoon;Nam, KiJeon;Yoo, ChangKyoo
    • Clean Technology
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    • v.28 no.1
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    • pp.63-78
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    • 2022
  • Electronics industrial wastewater treatment facilities release organic wastewaters containing high concentrations of organic pollutants and more than 20 toxic non-biodegradable pollutants. One of the major challenges of the fourth industrial revolution era for the electronics industry is how to treat electronics industrial wastewater efficiently. Therefore, it is necessary to develop an electronics industrial wastewater modeling technique that can evaluate the removal efficiency of organic pollutants, such as chemical oxygen demand (COD), total nitrogen (TN), total phosphorous (TP), and tetramethylammonium hydroxide (TMAH), by digital twinning an electronics industrial organic wastewater treatment facility in a cyber physical system (CPS). In this study, an electronics industrial wastewater activated sludge model (e-ASM) was developed based on the theoretical reaction rates for the removal mechanisms of electronics industrial wastewater considering the growth and decay of micro-organisms. The developed e-ASM can model complex biological removal mechanisms, such as the inhibition of nitrification micro-organisms by non-biodegradable organic pollutants including TMAH, as well as the oxidation, nitrification, and denitrification processes. The proposed e-ASM can be implemented as a Water Digital Twin for real electronics industrial wastewater treatment systems and be utilized for process modeling, effluent quality prediction, process selection, and design efficiency across varying influent characteristics on a CPS.

A Study on the Filtration of BNR Process Effluent (BNR공정 처리수의 여과에 관한 연구)

  • Kim, Seong-Young;Bum, Bong-Su;Cho, Kwang-Myeung
    • Journal of Korean Society of Environmental Engineers
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    • v.22 no.5
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    • pp.895-905
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    • 2000
  • This study was performed to investigate the removal efficiencies of pollutants at various filtration rates and the quality of the filtered water along the depth of filter media during treatment of a BNR process effluent by a dual-media gravitational rapid filtration. The results of the experiments at filtration rates of 200, 300 and 400 m/day using the effluent of a pilot scale 4-stage BNR plant showed that turbidity of the filtered water was below 2.6 NTU, satisfying the Korean standard for water for reuse. Even though the SS removal efficiency deteriorated as the filtration rate increased, the average SS concentration of the filtered water was 1.3 mg/L at all filtration rates. Simultaneous biological nitrification and denitrification was observed with nitrification efficiencies of 17.4, 18.8 and 14.3%, and denitrification efficiencies of 32.3, 27.7 and 21.4% respectively at filtration rates of 200, 300 and 400 m/day. At the latter period of each filtration cycle, the effluent T-P concentration was higher than influent T-P concentration by 6.1 to 21.4% due to phosphorous release under DO-deficient condition.

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Efficiency of Apatite and Limestone in Removing Arsenic from Acid Rock Drainage at the Goro Abandoned Mine (인회석 및 석회석을 이용한 고로폐광산 ARD 내의 비소 저감효율 연구)

  • Park, Myung-Ho;Lee, Young-Woo;Hur, Yon-Kang;Park, Hae-Cheol;Sa, Sung-Oh;Choi, Jung-Chan
    • The Journal of Engineering Geology
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    • v.21 no.3
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    • pp.231-237
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    • 2011
  • An active apatite drainage system has been developed at the Goro abandoned mine, comprising a grit cell, a reaction cell, and a precipitation pond. Leachate from an abandoned adit and tailing ponds is collected in a pipeline and is transported to the apatite drainage system under the influence of the hydraulic gradient. The results of a laboratory experiment performed in 2004 indicate that the reaction cell requires 38.8 ton/year of apatite and that precipitate will have to be removed from the precipitation pond every 3 months. The purpose of this study is to evaluate a laboratory test on the efficiency of limestone and apatite in removing arsenic from ARD (acid rock drainage), and to evaluate the suitability of materials for use as a precipitant for the leachate treatment disposal system. The laboratory tests show that the arsenic removal ratios of limestone and apatite are 67.4%-98.3%, and the arsenic removal ratio of apatite is inversely proportional to its grain size. The arsenic compounds are assumed to be Johnbaumnite and Ca-arsenic hydrate. Therefore, apatite and phosphorous limestone can be used as a precipitant for the removal of arsenic, although it is difficult to remove arsenic from ARD when it occurs in low concentrations.

Application of Subsurface Flow Wetland using the Phragmites australis for Water Quality Improvement of the Agricultural Reservoi (농업용 저수지 수질개선을 위한 지하흐름 갈대 인공습지의 적용)

  • Nam, Gui Sook;Pae, Yo Sop;Kim, Hyung Joong;Lee, Sang Joon;Lee, Gwang Sik
    • Journal of Wetlands Research
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    • v.6 no.4
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    • pp.59-69
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    • 2004
  • Constructed wetlands are regarded as an important water treatment system for agricultural water quality improvement and management. The purpose of this study is to evaluate the application of subsurface flow wetland(SFW), using the Pharagmites australis as macrophytes, and to clarify the basic and essential factors to be considered in the construction and management of constructed wetlands. This study was carried out relatively short hydraulic residence time(HRT), 6hr ~ 72hr (3days), using eutrophic reservoir water with relatively low concentrations of influent and large quantity to be treated. The effluent satisfied the criteria of agricultural water quality. Removal efficiencies of Biochemical oxygen demand(BOD), Chemical oxygen demand(COD), Suspended solids(SS) and Chlorophyll a(Chl-a) were high in HRT 24hr, not any more significant increasement of removal efficiencies in HRT 48hr and 72hr. However, removal efficiencies of nitrogen and phosphorus increased as HRT increased, showing the highest efficiency at the 72hr of HRT in nitrogen, and 48hr in phosphorous. The SFW was very effective system for reservoir water quality improvement, and had the advantages of the reduction of purchasing cost to land required, lack of odors, and harmful insects, especially mosquito, the improvement of the scenic beauty and minimal risk of public exposure. Therefore, it was evaluated that the SFW was very available water treatment system for the water quality improvement of agricultural reservoir. However, it was need to consider with application of the SFW in high cost of construction and troublesome of management.

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Nitrogen and Phosphorus Removal Characteristics of a New Biological Nutrient Removal Process with Pre-Denitrification by Pilot Scale and Computer Simulation Program (선단무산소조를 이용한 영양소제거공정(Bio-NET)의 질소·인 제거 특성)

  • Oh, Young-Khee;Oh, Sung-Min;Hwang, Yenug-Sang;Lee, Kung-Soo;Park, No-Yeon;Ko, Kwang-Baik
    • Journal of Korean Society of Environmental Engineers
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    • v.22 no.1
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    • pp.121-132
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    • 2000
  • This study is to investigate the performance of a new BNR process using predenitrification scheme focusing on nitrogen removal and the possibility of adapting a computer simulation scheme in BNR process development. By using a pre-denitrification basin, higher $COD/NO_3-N$ ratio could be sustained in this BNR process. The results of the investigation showed a SDNR value of 9.04mg/gMv/hr. In the anoxic tank, the average value of SPRR of 6.25mgP/gMv/hr was observed to be very sensitive to SCOD load of influents. By calibrating internal parameters (stoichiometric and kinetic parameters) of the simulation model, the results of simulation for various BNR processes gave good agreement with observed data. The major adjustment was given with three parameters, maximum specific growth rate of heterotrophic biomass, short chain fatty acid (SCFA) limit, and phosphorous release rate. With the series of simulations on varying operational conditions, the simulation by computer program can be a useful tool for process selection, and design and operation of municipal wastewater treatment plant.

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A study on characteristic by isolation of nitrogen synthetic microorganism and ammonia nitrogen removal in artificial wastewater (질소 합성 균주의 분리에 의한 특성검토와 합성폐수중의 암모니아성질소 제거)

  • Kim, Su-Il;Lee, Ki-Hyung;Phae, Jae-Gun
    • Journal of the Korea Organic Resources Recycling Association
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    • v.10 no.3
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    • pp.117-125
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    • 2002
  • This study experimented a possibility of advanced treatment through microorganism that converts $NH_3-N$ to organic nitrogen in wastewater contaminated by ammoniac nitrogen unlike conventional nitrogen removal process. After distributing three kinds of special bacteria that use $NH_3-N$ as a substrate, when those bacteria were cultured in no salt condition and salt condition (3% NaCl), M11 showed better growth in salt condition and M12 showed better growth in no salt condition. However M7l grew well in both no salt condition and salt condition. In the test of glucose effect, maximum growth and removal rate were observed in glucose concentration of 5g/L but in high concentration (1000mg/L as $NH_3-N$) of $NH_3-N$ growth and removal rate were low. Removal rate was the highest in 100mg/L $NH_3-N$ and the fact that concentration of $NO_2-N$ and $NO_3-N$ didn't increase assumed $NH_3-N$ was converted to organic nitrogen. Optimum concentration of $K_2HPO_4$ for phosphorous supply and buffer was 5g/L. Special bacteria distributed could use $NO_2-N$ and $NO_3-N$ as well as $NH_3-N$ as substrates. This study showed that when growth rate of bacteria was high removal rate also was high. It is possible to apply as a method to treat wastewater polluted by $NH_3-N$.

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Treatment Level of a Pond System for Ecological Treatment and Recycling of Animal Excreta (생태적 축산폐수 처리 및 재활용 연못시스템의 폐수처리수준)

  • Yang, Hong-Mo;Rhee, Chong-Ouk
    • Korean Journal of Environmental Agriculture
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    • v.17 no.1
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    • pp.70-75
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    • 1998
  • A model of pond system is developed for treatment and recycling of excreta from twenty-five adult dairy cattle. It is composed of wastewater treatment ponds and small fish ponds. Those are three facultative ponds in series; primary-secondary-tertiary pond and these are designed to rear carps without feeding. A pit is constructed at the bottom of primary pond for efficient sludge sedimentation and effective methane fermentation. It is contrived to block into it the penetration of oxygen dissolved in the upper layer of pond water. The excreta from the cattle housed in stalls are diluted by water used for clearing them. The washed excreta flow into the pit. The average yearly $BOD_5$ concentration of influent is 398.7mg/l. That of the effluent from primary, secondary and tertiary pond of the system is 49.18, 27.9, and 19.8.mg/l respectively. Approximate 88, 93, and 95 % of BOD5 are removed in each pond. The mean yearly SS concentration of influent is 360.5 mg/l That of the effluent from each pond is 53.4, 45.7, and32.7mg/l respectively. Approximate 86, 88, and 91% of SS are removed in each pond. The $BOD_5$ concentration of secondary and tertiary pond can satisfy 30mg/l secondary treatment standard. The SS concentration of effluent from tertiary pond, however, is slightly greater than the standard, which results from activities of carps growing in the pond. The average yearly total nitrogen concentration of influent is 206.8mg/l and that of the effluent from each pond is 48.6, 30.8, and 21.0mg/l respectively. Approximate 74, 88, and 90% of total nitrogen are removed in each pond. The mean yearly total phosphorous concentration of influent is 20.7mg/l and that of the effluent from each pond is 5.3, 3.2, and 2.1mg/l respectively. Approximate 97, 98, and 99% of total phosphorous are removed in each pond. The high removal of nitrogen and phosphorous results from active growth of algae in the upper layer of pond water. Important pond design parameters for southern part of Korea -- areal loading of BOD5, liquid depth, hydraulic detention time, free board, and pond arrangement -- are taken up.

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