• 제목/요약/키워드: liquid membrane permeator

검색결과 2건 처리시간 0.015초

지지막을 이용하는 액막 추출기 내에서 아연 이온의 이동 (Transport of Zinc Ion in a Contained Liquid Membrane Permeator with Two Micro-Porous Films)

  • 주창식;이석희;이민규;홍성수;하홍두;정석기
    • 한국환경과학회지
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    • 제9권2호
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    • pp.159-164
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    • 2000
  • For the purpose of development of a liquid membrane permeator which separates metal ions from aqueous solutions continuously and effectively, a continuous membrane permeator with the membrane solution trapped between extraction and stripping phases by two micro-porous hydrophilic films was manufactured. Experimental researches on the separation of zinc ion from aqueous solutions were performed in the liquid membrane permeator with 30 vol % D2EHPA solution in kerosine as liquid membrane. As results, the liquid membrane permeator separates zinc ion from aqueous solutions continuously and effectively in the wide range of operating conditions. A simple mass transfer rate model using equilibrium constant of the extraction reaction for the system used were proposed, and the model was compared with experimental results of separation of zinc ion in the permeator. And the effects of operating factors, such as space time, pH of extraction solution, extraction temperature, on the separation rate of zinc ion in the permeator were experimentally examined.

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지지막을 이용한 액막 추출기에 의한 합성해수 중의 $Sr^{2+}$ 이온 분리 (Separation of $Sr^{2+}$ Ion from Seawater by Liquid Membrane Permeator with Two Micro-Porous Films)

  • 주창식;이회근;정갑섭
    • 한국환경과학회지
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    • 제9권6호
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    • pp.517-522
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    • 2000
  • Separation of strontium ion from synthetic seawater in the contained liquid membrane permeator with two micro-porous films was performed. The permeator consisted of a liquid membrane and two cells for aqueous solutions. The liquid membrane consisted of $D_2EHPA(di-2-ethylhexy1-phosphoric acid)$ and DCH18C6 (dicyclohexano-18-crown-6),diluted to 30 vol% with kerosine and was trapped between two micro-porous hydrophilic films. This liquid membrane separated two aqueous solutions, one of which was synthetic seawater and the other of which was the stripping solutions consisting of 1mol/L $H_2SO_4$ solution. The effects of various operating parameters on the extraction rate and equilibrium extraction ratio of strontium ion from synthetic seawater were experimentally examined. The addition of DCH18C6 to the $D_2EHPA$ solution caused synergy effect on the extraction of strontium ion. The permeator extracted strontium ion from synthetic seawater effectively with high membrane life time.

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