Carrier Facilitated Transport of Europium(III) Across Supported Liquid Membranes Containing N,N,N′,N′-tetra-2-ethylhexyl-3-oxapentane-diamide (T2EHDGA) as the Extractant

被引:11
作者
Panja, S. [2 ]
Mohapatra, P. K. [1 ]
Misra, S. K. [2 ]
Tripathi, S. C. [2 ]
机构
[1] Bhabha Atom Res Ctr, Div Radiochem, Bombay 400085, Maharashtra, India
[2] Bhabha Atom Res Ctr, Fuel Reproc Div, Bombay 400085, Maharashtra, India
关键词
actinide partitioning; europium(III); liquid membrane; solvent extraction; T2EHDGA; NITRIC-ACID; DIGLYCOLAMIDE TEHDGA; SOLVENT-EXTRACTION; N-DODECANE; PART I; TODGA; ACTINIDES; WASTE; LANTHANIDES; STABILITY;
D O I
10.1080/01496395.2011.580308
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Studies on the solvent extraction and pertraction behavior of europium(III) was carried out from acidic feed solutions using N,N,N',N'-tetra-2-ethylhexyl-3-oxapentane-diamide (T2EHDGA) in n-dodecane as the solvent. The nature of the extracted species from the solvent extraction studies conformed to Eu(NO3)(3)center dot 3T2EHDGA which is in variance with the analogous Eu(III) - TODGA (linear homolog of T2EHDGA) extraction system. The transport behavior of Eu(III) was investigated from a feed containing 3.0MHNO(3) into a receiver phase containing 0.01 M HNO3 across a PTFE flat sheet supported liquid membrane (SLM) containing 0.2 M T2EHDGA in n-dodecane as the carrier solvent and 30% iso-decanol as the phase modifier. Effects of feed acidity, carrier extractant concentration, membrane pore size, and Eu concentration in the feed on the transport rates of Eu(III) were also investigated. Membrane diffusion coefficient (D-o) for the pertracted species was calculated using the Wilke-Chang equation as 4.25 x 10(-6) cm(2) . s(-1). The influence of Eu concentration on the flux was also investigated. The role of temperature on the transport rates was investigated and the thermodynamic parameters were calculated.
引用
收藏
页码:1941 / 1949
页数:9
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