Structural insights into the multinuclear speciation of tetravalent cerium in the tri-n-butyl phosphate–n-dodecane solvent extraction system

2017 ◽  
Vol 19 (32) ◽  
pp. 21304-21316 ◽  
Author(s):  
Mark R. Antonio ◽  
Ross J. Ellis ◽  
Shanna L. Estes ◽  
Mrinal K. Bera

Macroscopic phase behaviors in the liquid–liquid extraction are explained by microscopic, reverse micellar fluid structures containing tetranuclear Ce(iv) clusters revealed by use of X-ray spectroscopy and scattering of the light and dense organic phases.

2016 ◽  
Vol 8 (32) ◽  
pp. 6158-6167 ◽  
Author(s):  
Arjun Kokare ◽  
Vishal Suryavanshi ◽  
Sunil Zanje ◽  
Gurupad Kore ◽  
Mansing Anuse

Herein, we have developed a solvent extraction system for lead(ii) with N-n-octylcyclohexylamine from HCl medium.


2014 ◽  
Vol 118 (43) ◽  
pp. 12486-12500 ◽  
Author(s):  
Wei Bu ◽  
Miroslav Mihaylov ◽  
Daniel Amoanu ◽  
Binhua Lin ◽  
Mati Meron ◽  
...  

2011 ◽  
Vol 110 (10) ◽  
pp. 102214 ◽  
Author(s):  
Wei Bu ◽  
Binyang Hou ◽  
Miroslav Mihaylov ◽  
Ivan Kuzmenko ◽  
Binhua Lin ◽  
...  

1983 ◽  
Vol 15 (6-7) ◽  
pp. 149-159 ◽  
Author(s):  
V C Blok ◽  
G P Slater ◽  
E M Giblin

Several commercially available adsorbents were compared with solvent extraction methods for their utility in recovering trace organics from water. The adsorbents examined included Amberlite XAD-2, XAD-4 and XAD-8, Ambersorb XE340 and XE348 and Tenax-GC. All were found to produce high artifact levels, even after extensive clean-up, making them unsuitable for the analysis of trace organics in water. Quantitatively, Likens-Nickerson or continuous liquid-liquid extraction with méthylene chloride gave better recoveries than the adsorbents. Qualitatively, extractive methods were preferred as they yielded much lower levels of impurities than the adsorbents. These methods of recovering trace organics were evaluated using a standard mixture of compounds added to the water at a level of 55 µg/l. Likens-Nickerson extraction gave comparable recoveries of this mixture at 55 µg/l and 11 µg/l.


1999 ◽  
Vol 23 (8) ◽  
pp. 518-519
Author(s):  
Francisco Jose Alguacil ◽  
Jaime Simpson ◽  
Patricio Navarro

A previously determined thermodynamic model for extraction equilibrium is used as a basis to predict experimentally measured distribution coefficients for the CuSO4–H2SO4–LIX 984–Escaid 103 solvent extraction system at 25 °C and aqueous copper concentrations in the range 0.01–2.0 gL−1, the copper loading isotherm is also obtained.


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