scholarly journals Design of Highly Selective Solvent Extraction System of Metal Ions Utilizing Macrocyclic Ligand as Ion-size Selective Masking Reagent

2004 ◽  
Vol 17 (1) ◽  
pp. 1-7
Author(s):  
Shigeo UMETANI
Keyword(s):  
Solvent Extraction ◽  
Metal Ions ◽  
Macrocyclic Ligand ◽  
Extraction System ◽  
Selective Solvent ◽  
Solvent Extraction System ◽  
Selective Solvent Extraction ◽  
Ion Size

scholarly journals Selective solvent extraction of various metal ions with tris(2,6-dimethoxyphenyl)phosphine from hydrochloric acid solutions.

1988 ◽  
Vol 4 (4) ◽  
pp. 431-432 ◽  
Author(s):  
Yuko YAMASHOJI ◽  
Takahiro KAWAGUCHI ◽  
Takayuki MATSUSHITA ◽  
Masanori WADA ◽  
Minoru TANAKA ◽  
...  
Keyword(s):  
Solvent Extraction ◽  
Hydrochloric Acid ◽  
Metal Ions ◽  
Acid Solutions ◽  
Selective Solvent ◽  
Hydrochloric Acid Solutions ◽  
Selective Solvent Extraction

Highly Selective Solvent Extraction of Copper(II) from Transition Metal Ions with DibutylN,N′-Bis(8-quinolyl)malonamide

1989 ◽  
Vol 18 (11) ◽  
pp. 2073-2076 ◽  
Author(s):  
Kazuhisa Hiratani ◽  
Kazuhiro Taguchi ◽  
Kozaburo Ohhashi ◽  
Hiroshi Nakayama
Keyword(s):  
Solvent Extraction ◽  
Transition Metal ◽  
Metal Ions ◽  
Transition Metal Ions ◽  
Selective Solvent ◽  
Selective Solvent Extraction

Selective Single-Step Separation of a Mixture of Three Metal Ions by a Triphasic Ionic-Liquid-Water-Ionic-Liquid Solvent Extraction System

2015 ◽  
Vol 21 (33) ◽  
pp. 11757-11766 ◽  
Author(s):  
Tom Vander Hoogerstraete ◽  
Jonas Blockx ◽  
Hendrik De Coster ◽  
Koen Binnemans
Keyword(s):  
Ionic Liquid ◽  
Solvent Extraction ◽  
Metal Ions ◽  
Liquid Water ◽  
Single Step ◽  
Extraction System ◽  
Solvent Extraction System

scholarly journals Solvent Extraction Equilibrium in the CuSO4–H2SO4–LIX 984–ESCAID 103 Systern

1999 ◽  
Vol 23 (8) ◽  
pp. 518-519
Author(s):  
Francisco Jose Alguacil ◽  
Jaime Simpson ◽  
Patricio Navarro
Keyword(s):  
Solvent Extraction ◽  
Thermodynamic Model ◽  
Distribution Coefficients ◽  
Extraction System ◽  
Extraction Equilibrium ◽  
Solvent Extraction System ◽  
Measured Distribution

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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