2019
DOI: 10.1021/acs.jced.8b01138
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Liquid–Liquid Equilibrium of Aqueous Two-Phase System Composed of Poly(Ethylene Oxide) 1500 and Sodium Nitrate

Abstract: Liquid–liquid equilibria of an aqueous two-phase system consisting of poly­(ethylene oxide) 1500, sodium nitrate, and water at 293.15, 313.15, and 333.15 K were studied. Binodal data and a complete phase diagram with equilibrium liquid-phase compositions were obtained by using conductometry and refractometry techniques. The equilibrium data for aqueous two-phase systems were correlated using the UNIQUAC model, and new binary interaction parameters were calculated.

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Cited by 37 publications
(15 citation statements)
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“…Traditionally, sulfuric, hydrochloric, and nitric acid solutions have been used in metal ion leaching from power source elements [27]. For the first time, this article studied the extraction of Ni(II), Co(II), Fe(III), Mn(II), Zn(II), Cu(II), and Al(III) from nitrate solutions in the aqueous two-phase systems based on poly(ethylene oxide) (PEO) 1500 which we proposed earlier [28]. The purpose of this work is to establish the interphase distribution regularities for a number of metals (Ni, Co, Fe, Mn, Cu, Zn, Al) in the PEO 1500-NaNO 3 -H 2 O extraction system.…”
Section: Introductionmentioning
confidence: 99%
“…Traditionally, sulfuric, hydrochloric, and nitric acid solutions have been used in metal ion leaching from power source elements [27]. For the first time, this article studied the extraction of Ni(II), Co(II), Fe(III), Mn(II), Zn(II), Cu(II), and Al(III) from nitrate solutions in the aqueous two-phase systems based on poly(ethylene oxide) (PEO) 1500 which we proposed earlier [28]. The purpose of this work is to establish the interphase distribution regularities for a number of metals (Ni, Co, Fe, Mn, Cu, Zn, Al) in the PEO 1500-NaNO 3 -H 2 O extraction system.…”
Section: Introductionmentioning
confidence: 99%
“…The metal ions extraction was carried out using nitrate two-phase aqueous systems, based on polyethylene glycol 1500 and with an initial metal concentration of 0.01mol•L -1 . Phase composition were chosen based on phase diagrams, PEG-1500 -NaNO3 [34]. The acid concentration in the salt phase was equal 0.01mol•L -1 (for the hydrolyze avoiding).…”
Section: Methodsmentioning
confidence: 99%
“…Two-phase water systems based on water-soluble polymers and inorganic salts can be an effective replacement for classical extraction systems. [19][20]. So, a system based on poly(ethylene glycol) and polypropylene glycol has shown its effectiveness for the transition metal ions without complexing agents [21][22][23], and with the addition of traditional extragents: Aliquat 336 [24], trioctylmethylammonium thiocyanate [25], potassium thiocyanate [26].…”
Section: Introductionmentioning
confidence: 99%