• Title/Summary/Keyword: Common anode bed

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Cathodic Protection of Buried Gas Pipelines Using Common Anode Beds (공용양극을 이용한 가스배관의 전기방식)

  • Ha, Y.C.;Kim, D.K.;Bae, J.H.;Ha, T.H.;Lee, H.G.
    • Journal of the Korean Institute of Gas
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    • v.12 no.1
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    • pp.19-24
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    • 2008
  • Due to industrialization and urbanization, underground metallic utilities with different owners have been rapidly increased and cathodic protection (CP) methods, especially impressed current CP systems, have been widely adopted to protect their utilities from corrosion with expanded recognition of this method. The stray current interference problem as well as the difficulty in spatial security for system installation, however, came to a ramification of which each owner couldn't resolve for himself. In this respect, this paper illustrates a field-diagnosed example for mutual interference due to separately operated CP systems and suggests an alternative method to overcome the interference situation by design and field-assessment of a common anode bed cathodic protection system.

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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.