• Title/Summary/Keyword: Di-2-ethylhexyl-phosphoric acid

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Treatment of Kimpo Landfill Leachate by Emulsion Liquid Membrane (에멀젼액막을 이용한 김포매립지 침출수의 처리)

  • Ro, Yun-Chan;Kim, Jong-Kuk;Park, Ham-Yong;Kim, Woo-Sik
    • Applied Chemistry for Engineering
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    • v.9 no.7
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    • pp.943-949
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    • 1998
  • This study is concerned with the treatment of landfill leachate by carrier meditated emulsion. Using the batch operation, the optimum conditions for the removal of anionic and cationic materials were obtained. The landfill leachate from the plant was experimented under these conditions. The experimental variables were surfactant (Arlacel80) concentration and carrier(Aiquat336, DEHPA) concentration in membrane phase and counter ion concentration in internal phase. More than 80%(COD) of landfill leachate component could be removed within 12 minutes. The most crucial experimental variable for the removal efficiency was carrier concentration in membrane phase. In the other variables, the reaction time was more effected than the removal efficiency.

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Evaluation of co- and Mutual Weparation for Actinide(III) and RE by a $(Zr-DEHPA)/n-dodecane-HNO_3$ Extraction System ($(Zr-DEHPA)/n-dodecane-HNO_3$ 금속함유 추출 계에 의한 악티나이드(III)및 RE의 공추출 및 상호 분리)

  • Lee, Eil-Hee;Lim, Jae-Kwan;Chung, Dong-Yong;Yang, Han-Beom;Kim, Kwang-Wook
    • Journal of Nuclear Fuel Cycle and Waste Technology(JNFCWT)
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    • v.5 no.2
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    • pp.123-132
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    • 2007
  • This study was performed to evaluate the co- and mutual separation for Am, Cm and RE elements from the simulated multi-component solution equivalent to real HLW level by a Zr-DEHPA(di-(2-ethylhexyl) phosphoric acid containing Zirconium)/$NDD(n-dodecane)-HNO_3$ extraction system. Zr-DEHPA was self-synthesized and the optimal condition of (15g/L Zr-1M DEHPA)/NDD-1M $HNO_3$ was selected taking into consideration of prevention of the third phase, and effects of concentration of DEHPA, nitric acid and impregnant amount of Zr on the co-extraction of Am, Cm and RE. In that condition, the extraction yields were 81% (Am), 85% (Cm), more than 80% (RE elements), 98% (Mo), 85% (Fe), 98% (U), 73% (Np), and less than 5% (other elements) so that the system developed for the co-extraction of Am-Cm/RE was proved to be available. For that, however, U, Np, Mo and Fe was elucidated to have to be removed in advance, and Zr inducing the third phase formation was found to be practically excluded. The co-extracted Am-Cm/RE were sequentially separated in an order of Am-Cm (stripping agent : 0.05 M DTPA-1M Lactic acid of pH 3.6)${\rightarrow}RE$ (stripping agent : 5M $HNO_3$), and then their separation factors were evaluated. At above conditions, Am of 65.4%, Cm of 63.9%, RE (except for Y) of more than 85% were stripped.

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