| Project/Area Number |
63550708
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| Research Category |
Grant-in-Aid for General Scientific Research (C)
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| Allocation Type | Single-year Grants |
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| Research Field |
化学工学
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| Research Institution | Kyoto Institute of Technology |
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Principal Investigator |
TERAMOTO Masaaki Kyoto Institute of Technology, Chemistry and Materials Technology, Professor, 工芸学部, 教授 (60026086)
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| Co-Investigator(Kenkyū-buntansha) |
MATSUYAMA Hideto Kyoto Institute of Technology, Chemistry and Materials Technology, Assistant, 工芸学部, 助手 (50181798)
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| Project Period (FY) |
1988 – 1989
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| Project Status |
Completed (Fiscal Year 1989)
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| Budget Amount *help |
¥2,000,000 (Direct Cost: ¥2,000,000)
Fiscal Year 1989: ¥800,000 (Direct Cost: ¥800,000)
Fiscal Year 1988: ¥1,200,000 (Direct Cost: ¥1,200,000)
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| Keywords | Solvent Extraction / Liquid Membrane / Aqueous Complexing Agent / Rare Earth Metal / Nonequilibrium Separation / 液膜法 / 酸性有機リン化合物 |
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| Research Abstract |
In this work, the selective separations of erbium(Er) and yttrium(Y) by both the solvent extraction and the supported liquid membrane were carried out with a complexing agent, diethylenetriaminepentaacetic acid(DTPA) in the aqueous phase. The purpose of this work is to elucidate the separation mechanism and to establish the experimental conditions in which the highest selectivity can be obtained.
First, kinetics of the exchange reactions between rare earth metal ions and their DTPA complexes were studied in order to elucidate the dissociation mechanism of the DTPA complexes. The dissociation rate constants of the DTPA complexes are very important for the clarification of the separation mechanism of the solvent extraction and the liquid membrane containing DTPA in the aqueous phase. It was found that the obtained dissociation rate constant of Y-DTPA complex was about 5.8 times that of Er-DTPA complex.
Further, the extractions of Er^<3+> and Y^<3+> from an aqueous phase containing DTPA were carried out. The selectivity obtained was about 5.5, which was much larger than that by the usual solvent extraction, 1.43. The selectivities for the various cases were studied in detail. The extraction rates and selectivities were quantitatively analyzed by taking account of the dissociation reaction of DTPA complexes in the aquous stagnant layer.
Furthermore, by using the supported liquid membrane system with, DTPA in the aquous feed phase, the separation of Er^<3+> and Y^<3+> was investigated. This separation method has the feature that the highest selectivity can be obtained when the mass transfer accompaning the dissociation reaction of DTPA complexes in the aqueous stagnant layer is rate-determining. The experimental results were satisfactorily simulated.
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