• Title/Summary/Keyword: Phosphate Removal

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Low Concentrated Nitrogen-Phosphate Removal of 4 Strains of Marine Bacteria Applied to Ceramic Media (세라믹 담체에 적용된 해양박테리아 4종의 저농도 질소-인 제거)

  • Lee, Gunsup;Kim, SoJung;Chung, Youngjae;Kim, Dongguin;Lee, Sang-Seob;Auh, Chung-Kyoon;Lee, Taek-Kyun
    • Journal of the Korea Academia-Industrial cooperation Society
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    • v.13 no.10
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    • pp.4910-4916
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    • 2012
  • Changes of low concentrated nitrogen-phosphate removal efficiency were investigated in 4 strains of marine bacteria applied to ceramic media. Marine bacteria were isolated and identified from Gwangyang bay. Growth rates and removal efficiencies of $NH_3$-N of 4 strains of marine bacteria applied to ceramic media were increased approximately 3 fold and over 30% than control group, respectively. A. hydrophila and P. diminuta had highest ${NO_3}^-$-N and phosphate removal efficiencies, respectively. This results showed that ceramic media is very nice material for improvement of nitrogen-phosphate removal efficiency and isolated marine bacteria may be useful to control nitrogen-phosphate at low concentration in field.

Relation between Leaching Characteristics of the positive Ions and Phosphate Removal by granular Converter Slag for the different Conditions and Concentrations of Phosphate (인산염 농도와 폐수조건 변화에 따른 입상 전로슬래그의 양이온 용출 특성과 인산염 제거의 관계에 관한 연구)

  • Lee, In-Gu;Lee, Sang-Ho
    • Journal of the Korea Academia-Industrial cooperation Society
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    • v.8 no.2
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    • pp.372-379
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    • 2007
  • The converter slag can be used to remove phosphate ion into the form of solid state from the wastewater. This research aims to evaluate the change of pH, alkalinity, leaching of positive ion in the wastewater and the removal of phosphate from the initial condition of wastewater. The change of pH was abruptly increased upto pH 11 for the initial condition of pH from 7.0 to 8.5 fer 0.5 unit of pH. The alkalinity was steadily increased from 10 hours of reaction time not same as pH increase. The removal of phosphate was very effective till 10 hours of reaction then it was slow after that time. The positive ion, magnesium ion was leached from the concentration of 2.0 mg/L to 4.3mg/L at the reaction time of 27 hours and 36 hours. Therefore, converter slag can be used to remove the phosphate in the form of Struvite from the wastewater.

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A Study on Phosphate Removal Efficiency by Pre-Treatment Conditioning of Oyster Shells (굴 패각의 전처리 조건에 따른 인산염 제거효율에 관한 연구)

  • Woo, Hee-Eun;Kim, Kyeongmin;Lee, In-Cheol;Kim, Kyunghoi
    • Journal of the Korean Society of Marine Environment & Safety
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    • v.24 no.2
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    • pp.196-202
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    • 2018
  • In this study, we investigated phosphate removal efficiency according to pretreatment (pyrolysis temperature, pyrolysis time, particle size) of oyster shells as a basic study for their recycling. And XAFS analysis and isothermal adsorption experiments were performed to investigate the phosphate removal characteristics of oyster shells. As a result, the removal efficiency was good at $600^{\circ}C$ pyrolysis temperature with 6 hour pyrolysis time and 0.355 ~ 0.075 mm particle size. Isothermal adsorption experiments showed that the Langmuir model is suitable for adsorption of oyster shells. XAFS analysis showed that calcium phosphate formed on the oyster shell pyrolyzed at $600^{\circ}C$. In other words, it was confirmed that the formation of calcium phosphate by the calcium ion elution of the oyster shell contributes to the decrease of phosphate concentration.

Enhanced removal of phosphate on modified ion exchanger with competing ion (음이온 교환수지를 이용한 인제거 향상)

  • Nam, Ju-Hee;Lee, Sang-Hyup;Choi, Jae-Woo;Hong, Seok-Won;An, Byungryul
    • Journal of Korean Society of Water and Wastewater
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    • v.27 no.1
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    • pp.121-128
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    • 2013
  • The concern for dissolved phosphate in water/wastewater has been increasing because of the risk for eutrophication. A variety of conventional and advanced technologies were applied to meet the enforced new regulation of phosphate around the world. However, there still remained a lot of challenge because most introduced/developed method, for example, biological and physic-chemical treatment is not easy to satisfy the new regulation of phosphate in water. In order to meet the new regulation, the application of ion exchanger has been tried which showed that the removal efficiency for phosphate was strongly determined by in the presence of the competing ion, especially sulfate. As results, a new class of ion exchanger governed by ligand exchange was developed and investigated to increase the selectivity for phosphate. The current study using organic/inorganic anion exchanger developed with Lewis acid-base interaction confirms the selectivity for phosphate over sulfate. According to isotherm test and column test, the value of the maximum phosphate uptake (Q) showed 64 mg/g as $po{_4}^{3-}$ and the breakthrough for phosphate occurs after 1000 min and completely finishes at 2500 min, respectively.

Effects of pH, molar ratios and pre-treatment on phosphorus recovery through struvite crystallization from effluent of anaerobically digested swine wastewater

  • Kim, Daegi;Min, Kyung Jin;Lee, Kwanyong;Yu, Min Sung;Park, Ki Young
    • Environmental Engineering Research
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    • v.22 no.1
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    • pp.12-18
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    • 2017
  • Struvite precipitation has been proven to be an effective method in removing and recovering ammonia nitrogen (N) and phosphate phosphorus (P) from wastewater. In this study, effects of pH, molar ratios and pre-treatment of effluent of anaerobically digested swine wastewater were investigated to improve struvite crystallization. The magnesium : ammonium : phosphate ratio of 1.2 : 1.0 : 1.0 was found to be optimal, yet the molar ratio in the wastewater was 1 : 74.9 : 1.8. From the analysis, the optimum pH was between 8.0 and 9.0 for maximal phosphate P release and from 8.0 to 10.0 for maximal ammonia N and phosphate P removal from real wastewater. Analysis from Visual MINTEQ predicted the pH range of 7-11 for ammonia N and phosphate P removal and recovery as struvite. For pre-treatment, microwave pre-treatment was ineffective for phosphate P release but ultrasound pre-treatment showed up to 77.4% phosphate P release at 1,000 kJ/L of energy dose. Precipitates analysis showed that phosphorus and magnesium in the collected precipitate had almost same values as theoretical values, but the ammonia content was less than the theoretical value.

Effect of Humic Substances on the Simultaneous Removal of Nitrate and Phosphate in a Micellar-Enhanced Ultrafiltration (MEUF) (미셀 한외여과(MEUF)를 이용한 질산성 질소와 인산의 동시제거 시 휴믹산의 영향)

  • 김보경;백기태;김호정;양지원
    • Journal of Soil and Groundwater Environment
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    • v.8 no.3
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    • pp.30-36
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    • 2003
  • The effect of humic acid on the simultaneous removal of nitrate and phosphate was investigated in a micellar-enhanced ultrafiltration (MEUF). At the low molar ratio of cetylpyridinium chloride (CPC) to contaminants, the removal of nitrate was lower to 50% by 100 ppm of humic acid due to the competition for binding on micelles. At the molar ratio higher than 3, however, the removal of nitrate was over 80%. Phosphate was removed over 80% at the molar ratio higher than 1. The CPC and humic acid were rejected over 99 % by UF membrane. The flux did not decrease by 100 ppm of humic acid but rather slightly increased since the humic acid adsorbed on the membrane made the membrane more hydrophilic. As a result, humic acid did not diminish the performance of MEUF in the simultaneous removal of nitrate and phosphate.

Verification of Enhanced Phosphate Removal Capability in Pure Cultures of Acinetobacter calcoaceticus under Anaerobic/Aerobic Conditions in an SBR

  • Kim, Hyung-Jin;Krishna R. Pagilla
    • Biotechnology and Bioprocess Engineering:BBE
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    • v.7 no.6
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    • pp.335-339
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    • 2002
  • Laboratory experiments were conducted using pure cultures of Acinetobacter under an-aerobic/aerobic cyclic conditions to explain the release and uptake of soluble phosphate in an activated sludge process showing enhanced biological phosphate removal (EBPR). Under anaerobic/aerobic cyclic conditions in a Sequencing Batch Reactor (SBR), COD uptake concurrent with soluble phosphate release by Acinetobacter was not significant during the anaerobic periods, indicating that EBPR would not be established in pure cultures. However Acinetobacter cells accumulated higher phosphate content (5.2%) in SBR than that obtained (4.3%) from batch experiments. These results suggest that Acinetobacter sp. may not follow the proposed pattern of behavior of poly-P bacteria in EBPR activated sludge Plants.

Preparation of Solid-Phase Extractant by Immobilizing Di-(2-ethylhexyl)phosphoric Acid (D2EHPA) and Tri-butyl-phosphate (TBP) in Polysulfone and Removal Characteristics of Cu(II) (Polysulfone에 추출제 Di-(2-ethylhexyl)phosphoric acid (D2EHPA)와 tri-butyl-phosphate(TBP)를 고정화한 고체상 추출제의 제조와 Cu(II)의 제거 특성)

  • Kam, Sang-Kyu;Jeon, Jin-Woo;Lee, Min-Gyu
    • Journal of Environmental Science International
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    • v.24 no.1
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    • pp.1-7
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    • 2015
  • The solid-phase extractant PS-D2EHPA/TBP was prepared by immobilizing two extractants D2EHPA and TBP in polysulfone (PS). The prepared PS-D2EHPA/TBP was characterized by using fourier transform infrared spectrometer (FTIR) and scanning electron microscopy (SEM). The removal of Cu(II) from aqueous solution was investigated in batch system. The experiment data were obeyed the pseudo-second-order kinetic model. Equilibrium data were well fitted by Langmuir model and the removal capacity of Cu(II) by solid extractant PS-D2EHPA/TBP obtained from Langmuir model was 3.11 mg/g at 288 K. The removal capacity of Cu(II) was increased according to increasing pH from 2 to 6, but the removal capacity was decreased below pH 3 remarkably.

The Effect of Fixed Media and Recycling Ratio on Nutrients Removal in a Pilot-Scale Wastewater Treatment Unit (고정식 담체 유무와 반송비에 따른 소규모 하수처리 시스템 내 영양염류 제거 특성)

  • Hwang, Jae-Hoon;Cho, Dong-Wan;Kim, Chung-Hwan;Jeon, Byong-Hun
    • Journal of Korean Society of Environmental Engineers
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    • v.35 no.6
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    • pp.449-455
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    • 2013
  • The effect of recycling ratio and fixed media on nitrate and phosphate removal was investigated in a pilot-scale wastewater treatment unit using synthetic wastewater. Addition of fixed media increased nitrate removal from 45 to 58% while no noticeable change was observed for Chemical Oxygen Demand (COD) and phosphate removal (<5%). Nitrate removal efficiency also enhanced (Ca 7%) when the influent wastewater flow was doubled (2Q), however phosphate removal was decreased from 40.9 to 26.6% with the increasing recycling rate. The attached biomass analysis showed the presence of bacteria (73.4 $mg/cm^2$) on the surface of added media in anoxic reactor. Pseudomonas aeruginosa a common denitrifying bacterium dominated the bacterial growth (58%) in the anoxic reactor which was determined using Fluorescence In Situ Hybridization (FISH) analysis.

A study on the application of mill scale-derived magnetite particles for adsorptive removal of phosphate from wastewater (인제거용 흡착제로서 밀스케일로부터 선별된 마그네타이트 적용 연구)

  • Kim, Yunjung;Doliente, Jonica Ella;Choi, Younggyun
    • Journal of Korean Society of Water and Wastewater
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    • v.31 no.4
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    • pp.281-287
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    • 2017
  • Mill scale, an iron waste, was used to separate magnetite particles for the adsorption of phosphate from aqueous solution. Mill scale has a layered structure composed of wustite (FeO), magnetite ($Fe_3O_4$), and hematite ($Fe_2O_3$). Because magnetite shows the highest magnetic property among these iron oxides, it can be easily separated from the crushed mill scale particles. Several techniques were employed to characterize the separated particles. Mill scale-derived magnetite particles exhibited a strong uptake affinity to phosphate in a wide pH range of 3-7, with the maximum adsorptive removal of 100%, at the dosage of 1 g/L, pH 3-5. Langmuir isotherm model well described the equilibrium data, exhibiting maximum adsorption capacities for phosphate up to 4.95 and 8.79 mg/g at 298 and 308 K, respectively. From continuous operation of the packed-bed column reactor operated with different EBCT (empty bed contact time) and adsorbent particle size, the breakthrough of phosphate started after 8-22 days of operation. After regeneration of the column reactor with 0.1N NaOH solution, 95-98% of adsorbed phosphate could be detached from the column reactor.