• Proceedings of the KSEEG Conference
• /
• 2002.04a
• /
• pp.234-236
• /
• 2002

• Membrane Journal
• /
• v.8 no.4
• /
• pp.228-234
• /
• 1998

Among various water contaminents, organic compounds like phenol are difficult to be removed or destroyed by conventional methods under the unusual discharge conditions. The separation of phenol from aqueous solution has been carried out by several methods recently: absorption by an activated carbon, solvent extraction and liquid membrane technology. The liquid membrane based on water-oil emulsification has been tested as an alternative technology of the conventional technology. In this work, tri-n-butyl phosphate(TBP) and liquid polymers were examined as a liquid membrane in the supported liquid membrane(SLM). The feed concentration of phenol was varied and various types of liquid membranes were used to examine their effects on separation of phenol. It was found that TBP, polypropylene glycol 4000(PPG 4000) and polybutytene glycol 500(PBG 500) were proper carriers because mass transfer rates through them were much higher than or similar to that through methyl isobutyl ketone(MIBK) which was used as a conventional solvent in a solvent extraction process.

• Proceedings of the Korean Institute of Resources Recycling Conference
• /
• 2002.05a
• /
• pp.101-102
• /
• 2002

• Proceedings of the Korean Environmental Sciences Society Conference
• /
• 1999.10a
• /
• pp.198-199
• /
• 1999

• Proceedings of the Membrane Society of Korea Conference
• /
• 1999.10b
• /
• pp.114-116
• /
• 1999

• Proceedings of the Membrane Society of Korea Conference
• /
• 1998.10a
• /
• pp.31-36
• /
• 1998

1. 서론 : 산업이 고도로 발달함에 따라 야기되는 환경오염의 심각성이 날로 더해가고 있다. 특히 원자력 관련시설중 핵연료 재활용 공정에서 발생되는 방사성 폐기물의 처리기술에 대한 개발이 무엇보다도 시급한 실정이다. 핵연료 재활용 조작은 고준위 및 중준위 방사능 액체 폐기물을 발생시키며 이러한 방사능 액체 폐기물의 주요핵종은 긴 반감기를 갖는 것들이다. 이러한 방사능 액체 폐기물의 무해한 저장을 위해서 세계적으로 노력해 왔으며 고준위 폐기물은 유리화한후 심층매립을 하는 것이 가장 안전한 방법으로 고려되고 있다.(생략)

• Journal of Environmental Science International
• /
• v.9 no.6
• /
• pp.517-522
• /
• 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.

• Journal of Environmental Science International
• /
• v.9 no.2
• /
• pp.159-164
• /
• 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.