Solvent Extraction Equilibrium of Zinc from Nitrate Solutions with 2-Ethylhexylphosphonic Acid Mono-2-ethylhexyl Ester

2012 ◽  
Vol 51 (50) ◽  
pp. 16433-16437 ◽  
Author(s):  
Chaitanya R. Adhikari ◽  
Hirokazu Narita ◽  
Mikiya Tanaka
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.


1991 ◽  
Vol 9 (4) ◽  
pp. 569-591 ◽  
Author(s):  
Carmen Pazos ◽  
Juan Pablo S. Curieses ◽  
José Coca

1998 ◽  
Vol 48 (3) ◽  
pp. 291-299 ◽  
Author(s):  
F.J Alguacil ◽  
A Cobo

1966 ◽  
Vol 44 (4) ◽  
pp. 521-525 ◽  
Author(s):  
A. Aboul-Seoud ◽  
M. Doheim

The distribution coefficients of aniline between n-heptane and aqueous sodium nitrate solutions were measured at different temperatures. The activity coefficients of aniline in aqueous sodium nitrate solutions were determined. The effect of sodium nitrate on the dissociation of the anilinium ion was studied at different temperatures by a modified distribution method. Attention was directed to the choice of the extracting solvent and of the analytical method. The effect of the presence of undissociated anilinium ions on the distribution coefficients was taken into consideration.K0, Kb, ΔH, ΔF, and ΔS for the dissociation of the anilinium ion were evaluated.


1982 ◽  
Author(s):  
J.E. Freer ◽  
D.H. Crump ◽  
K.M. Axler ◽  
D.G. Clifton ◽  
Hayter S.W. ◽  
...  

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