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Novel 90Sr-90Y generator system based on a cross-flow hollow fiber supported liquid membrane contactor

机译:基于错流中空纤维支撑液膜接触器的新型90Sr-90Y发生器系统

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摘要

Separation of yttrium(III) from strontium(II) with 15% (v/v) di(2-ethylhexyl)phosphoric acid (DEHPA) in dodecane was carried out in a hollow fiber supported liquid membrane (SLM) extraction system operated under closed-loop recirculation of the donor and acceptor phase. The donor phase was a mixture of 5.7 mmol dm-3 of Sr(II) and 0.23 mmol dm-3 of Y(III) in 0.1 mol dm-3 HCl, the acceptor solution was 3 mol dm-3 HCl, and the donor to acceptor phase volume ratio was 6.2. At the donor flow rate of 4.7 cm3 min-1 and the acceptor flow rate of 0.8 cm3 min-1, the yield of Y(III) in the acceptor phase reached 60% after 360 min with a molar ratio of Y(III) to Sr(II) in the acceptor of 250:1, as compared to 1:25 in the donor phase. The yield of Y(III) was 72% at the acceptor flow rate to 1.9 cm3 min-1, but a breakthrough of Sr(II) through liquid membrane increased from 0.02 to 0.2%.
机译:在中空纤维支撑的液膜(SLM)萃取系统中,在含有十二烷的15%(v / v)二(2-乙基己基)磷酸(DEHPA)中分离锶(II)中的钇(III)供体和受体阶段的循环再循环。供体相为5.7 mmol dm-3的Sr(II)和0.23 mmol dm-3的Y(III)在0.1 mol dm-3 HCl中的混合物,受体溶液为3 mol dm-3 HCl,供体与受体相的体积比为6.2。在给体流速为4.7 cm3 min-1和受体流速为0.8 cm3 min-1的情况下,在360分钟后,受体相的Y(III)的收率达到60%,摩尔比为Sr(II)在受体中的比例为250:1,而在施主阶段的比例为1:25。 Y(III)的产率在受体流速为1.9 cm3 min-1时为72%,但Sr(II)通过液膜的穿透率从0.02增加到0.2%。

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