• Title/Summary/Keyword: 충진복극전해조

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Continuous Removal of Nitrate and Coliform using Bipolar ZVI Packed Bed Electrolytic Cell (영가철 충진 복극전해조를 이용한 질산성질소 및 대장균의 연속식 제거)

  • Jeong, Joo-Young;Park, Jeong-Ho;Choi, Won-Ho;Park, Joo-Yang
    • Journal of Korean Society of Water and Wastewater
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    • v.25 no.5
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    • pp.651-658
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    • 2011
  • Nitrate is a common contaminant in industrial wastewater and ground water. The maximum contaminant level set by EPA for nitrate of 10 mg/L as N. In this study, nitrate was removed using bipolar ZVI packed bed electrolytic cell that maximized the contact area between each electrode and contaminants under 600 V. Also this study investigates the simultaneously deals with removal of ammonia by operating air stripping tower. In addition to the air stripping also helped to precipitate iron ions to the form of iron oxides. Bipolar ZVI packed bed electrolytic cell was also effective in removing coliform by electrical power. In the continuous experiments for the simulated wastewater (initial nitrate for 25 mg/L as N), maximum 96.3% removal of nitrate was achieved in the applied 600 V at the flow rate of 6 mL/min.

Continuous Nitrate Removal using Bipolar ZVI Packed Bed Electrolytic Cell (영가철(Fe0) 충진 복극전해조를 이용한 질산성질소의 연속식 제거 연구)

  • Jeong, Joo-Young;Kim, Han-Ki;Shin, Ja-Won;Park, Joo-Yang
    • KSCE Journal of Civil and Environmental Engineering Research
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    • v.32 no.1B
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    • pp.79-84
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    • 2012
  • Nitrate is a common contaminant in groundwater aquifer. The present study investigates the performance of the bipolar zero valent iron (ZVI, $Fe^0$) packed bed electrolytic cell in removing nitrate in different operating conditions. The packing mixture consists of ZVI as electronically conducting material and silica sand as non-conducting material between main cathode and anode electrodes. In the continuous experiments for the simulated wastewater (contaminated groundwater, initial nitrate about 30 mg/L as N and electrical conductivity about 300 ${\mu}S/cm$), over 99% removal of nitrate was achieved in the applied voltage 600 V and at the flow rate of 20 mL/min. The optimum packing ratio (v/v) and flow rate were determined to be 1:1~2:1 (silica sand to ZVI), 30 mL/ min respectively. Effluent pH was proportional to nitrate influx concentration, and ammonia which is the final product of nitrate reduction was about 60% of nitrate influx. Magnetite was observed on the surface of the used ZVI as major oxidation product.

Removal of Nitrate Nitrogen for Batch Reactor by ZVI Bipolar Packed Bed Electrolytic Cell (영가철 충진 회분식 복극전해조에 의한 질산성 질소 제거)

  • Jeong, Joo Young;Park, Jeong Ho;Choi, Won Ho;Park, Joo Yang
    • KSCE Journal of Civil and Environmental Engineering Research
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    • v.31 no.2B
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    • pp.187-192
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    • 2011
  • Nitrate nitrogen is common contaminant in groundwater aquifers, its concentration is regulated many countries below 10 mg/L as N (As per WHO standards) in drinking water. An attempt was made to get optimal results for the treatment of nitrate nitrogen in groundwater by conducting various experiments by changing the experimental conditions for ZVI bipolar packed bed electrolytic cell. From the experimental results it is evident that the nitrate nitrogen removal is more effective when the reactor conditions are maintained in acidic range but when the acidic environment changes to alkaline due to the hydroxide formed during the process of ammonia nitrogen there by increasing the pH reducing the hydrogen ions required for reduction which leads to low effectiveness of the system. In the ZVI bipolar packed bed electrolytic cell, the packing ratio of 0.5~1:1 was found to be most effective for the treatment of nitrate nitrogen because ZVI particles are isolated and individual particle act like small electrode with low packing ratio. It is seen that formation of precipitate and acceleration of clogging incrementally for packing ratio more than 2:1, decreasing the nitrate nitrogen removal rate. When the voltage is increased it is seen that kinetics and current also increases but at the same time more electric power is consumed. In this experiment, the optimum voltage was determined to be 50V. At that time, nitrate nitrogen was removed by 94.9%.

Removal of Nitrate in Groundwater by Bipolar ZVI Packed Bed Electrolytic Cell at Field Pilot (지하수중의 질산성질소 제거를 위한 영가철 충진 복극전해조의 현장적용에 관한 연구)

  • Na, So-Jeong;Jeong, Joo-Young;Kim, Han-Ki;Park, Joo-Yang
    • Journal of Korean Society of Water and Wastewater
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    • v.25 no.6
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    • pp.989-994
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    • 2011
  • Nitrate contamination of groundwater is a common problem throughout intensive agriculture areas (non-point source pollution). Current processes (e.g. ion exchange and membrane separation) for nitrate removal have various disadvantages. The objective of this study was to evaluate electrochemical method such as electroreduction using bipolar ZVI packed bed electrolytic cell to remove nitrate from groundwater at field pilot. In addition ammonia stripping tower continuously removed up to 77.0% of ammonia. Bipolar ZVI packed bed electrolytic cell also removed E.coli. In the field pilot experiment for groundwater in 'I' city (average nitrate 30~35 mg N/L, pH 6.4), maximum 99.9% removal of nitrate was achieved in the applied 600 V.

Electrolytic Treatment of Ammonium Nitrogen and Nitrate Nitrogen by Bipolar Packed Bed Electrolytic Cell (충전복극전해조에 의한 암모니아성 및 질산성 질소의 전해처리)

  • Yun, Churl-Jong;Yu, Hyun-Chul;Kim, Jung-Sup;Lee, Bong-Seob;Kawk, Myoung-Hwa;Park, Seung-Cho
    • Journal of Korean Society of Environmental Engineers
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    • v.27 no.7
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    • pp.686-689
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    • 2005
  • This study was conducted to investigate the effect of ammonium and nitrate nitrogen removal to applied voltage, electrolytic time and activated carbon packing height. Batch bipolar packed bed electrolytic cell reactor was packed with $4{\times}8$ mesh granular activated carbon (GAC). Afterward electrolysis was performed in 20 V for 30 min. As a result, as the filling height adjusted to 80 mm high, the removal efficiency of ammonium nitrogen was 99.9%. and as the electrolytic time varied to 60 min, the removal efficiency of ammonium nitrogen was 97.6%. and in case of continuous electrolytic treatment of ammonium and nitrate nitrogen removal efficiency of total nitrogen was over 80% in bipolar packed bed electrolytic cell reactor for 72 hours as the packing height, sample concentration and input rate of sample adjusted to 280 mm, 30 mg/L, 6.7 mL/min, respectively.

Research on Remediation of Trichloroethylene using Zero Valent Iron Bipolar Packed Bed Electrodes (영가철 충진 복극전해조를 이용한 TCE 정화기법에 관한 연구)

  • Park, Yu-Ri;Shin, Ja-Won;Park, Joo-Yang
    • KSCE Journal of Civil and Environmental Engineering Research
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    • v.32 no.1B
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    • pp.85-91
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    • 2012
  • Permeable Reactive Barriers (PRBs) using zero valent iron (ZVI, $Fe^0$) is a promising technology for in-situ remediation of trichloroethylene (TCE) forming dense non aqueous phase liquid (DNAPL). The objective of this study is to develop an enhanced treatment method of trichloroethylene-contaminated groundwater using ZVI packed bed with direct current (D.C.). A column experiment was performed to investigate degradation efficiency of TCE that was performed in three different combination of control (only sand), ZVI column (ZVI:sand, packing ratio 1:2(v/v)) and bipolar column (ZVI:sand=1:2(v/v) with electric current) in the test columns. As the results of this study, the degradation efficiency of TCE was improved with simultaneous application of both bipolar column compared to that used ZVI column. Because ZVI particles are isolated and individual particles act like small electrodes. In this experiment, it was indicated a basic material for application of bipolar packed bed as electro-PRBs that was effective degradation of TCE.

Fluoride Removal by Granular Aluminium Bipolar Packed Bed Electrolytic Cell (입자상 알루미늄 충전복극전해조에 의한 불소제거)

  • Ha, Ji-Young;Park, Jung-Hoon;Woo, Sung-Hoon;Park, Seung-Cho
    • Journal of Korean Society of Environmental Engineers
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    • v.29 no.6
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    • pp.684-688
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    • 2007
  • The results of potentiostatic electrolysis of aqueous solution containing fluoride by bipolar packed bed electrolytic cell filled with granular aluminium were summarized. Removal efficiency of fluoride ion which it analyzed with ion chromatograph were 53, 73, 90% in applied voltage. Control the concentration of supporting electrolyte were 10, 30, 50, 70 mg/L and volume of packing material were 0, 25, 50, 75%, respectively, the quantity of electricity was $2.58A{\cdot}hr$ when the concentration of supporting electrolyte was 50 mg/L and the volume of packing material was 75%. As the results of electrolytsis of fluoride aqueous solution containing fluoride 10, 30, 50, 70 mg/L for 3 hours at 10 V, the removal efficiency of fluoride were 93.3, 80, 68.6%. Then the quantity of electricity were 2.58, 3.89, $5.43A{\cdot}hr$ and the fluoride removal amounts per quantity of electricity were 4.0, 3.5, $2.0mg/A{\cdot}hr$.

Treatment of ETA wastewater using GAC as particle electrodes in three-dimensional electrode reactor (활성탄 충진 3D 복극전기분해조를 이용한 ETA 처리)

  • Kim, Ran;Kim, Yu-Jin;Shin, Ja-Won;Kim, Jeong-Joo;Park, Joo-Yang
    • Journal of Korean Society of Water and Wastewater
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    • v.27 no.2
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    • pp.241-249
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    • 2013
  • Ethanolamine (ETA) is widely used for alkalinization of water in steam cycles of nuclear power plants with pressurized water reactor. When ETA contained wastewater was released, it could increase COD and T-N. The treatment of the COD and T-N from ETA wastewater was investigated using the GAC as particle electrodes in three-dimensional electrode reactor (TDE). This study evaluated the effectiveness of GAC as particle electrode using different packing ratio at 300 V. The results showed that GAC-TDE could reduce ETA much more efficiently than ZVI-TDE at the mass ratio of GAC to insulator, 1:2. Additionally, The effect of applied electric potential to COD and T-N reduction was investigated. The results showed the high COD, T-N reduction and current efficiency at the low electric potential. Using the GAC-TDE will provide a better ETA reduction with reducing electrical potential dissipation.