Abstract

Individual distribution constants (KD,A) of picrate ion (Pic−) and extraction constants (Kex±) of NaPic by some crown ethers (L) into benzene (Bz) at 25°C were calculated from data reported previously. These constants were defined asKD,Pic=Pic-o/[Pic-]andKex±=NaL+oPic-o/(Na+Lo[Pic-]), respectively. Here, the subscript “o” denotes an organic (o) phase and practically o = Bz. 15-Crown-5 ether (15C5), 18-crown-6 one (18C6), and their monobenzo (B) derivatives (B15C5 and B18C6) were selected as L. Interfacial equilibrium-potential differences (Δϕeq) at extraction were estimated at 298 K. A plot oflog⁡Kex±versus-Δϕeqfor the four L extraction systems gave a straight line with slope = 84 V−1. This slope was compared with those, reported before, of the dichloromethane (DCM), 1,2-dichloroethane (DCE), and nitrobenzene (NB) extraction systems. The slopes of the regression lines were in the order NB < DCM ≤ DCE < Bz. Also, the individual distribution constants of the complex ionNaL+and an ion-pair complex (NaL+Pic-) into Bz phase were calculated from the above extraction data. At least, a comparison between these values suggests that Bz molecules mainly interact withNaL+moiety ofNaL+Pic-.

Highlights

  • A presence of interfacial equilibrium-potential differences (Δφeq) at extraction processes with polar diluents, such as dichloromethane (DCM), 1,2-dichloroethene (DCE), and nitrobenzene (NB), has been clarified [1, 2]

  • Individual distribution constants of the ion-pair complexes NaL+Pic− and the complex ions (NaL+), which constitute parts of the complexes, into the four diluents were estimated from the above results and their properties for solute-solvent interaction were discussed

  • In the analysis of an overall extraction equilibrium, the following component equilibria were considered [2, 16]: L 󴀕󴀬 LBz (the equilibrium constant for this equilibrium: KD,L; sNNeaaeLLS+Peicc+tBizoP(niKc3D.󴀕5,N󴀬)a;LNPNicaa;+LseP+eicLSe(cK󴀕t󴀬1io; Nnsea3eL.5+S);e(NcKtaiNoLanLP;i3cs.eB5ze);󴀕S󴀬NecaNtLioaPLni+c3B.z5󴀕+)󴀬; picrate ion (Pic−)Bz (K1,Bz−1; see Section 3.2); and Na+ + Pic− 󴀕󴀬 NaPic. In addition to these equilibria, one can understand the presence of other component equilibria: NaL+ 󴀕󴀬 NaL+Bz (KD,NaL; see Section 3.2 and Table 1) and Pic− 󴀕󴀬 Pic−Bz (KD,Pic; see Section 1 and Table 1)

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Summary

Introduction

A presence of interfacial equilibrium-potential differences (Δφeq) at extraction processes with polar diluents, such as dichloromethane (DCM), 1,2-dichloroethene (DCE), and nitrobenzene (NB), has been clarified [1, 2]. Alkaline-earth metal (Ca-Ba) picrates [1] into NB In these studies [1, 2], an individual distribution constant (KD,A) of a pairing anion (A−), such as picrate ion (Pic−), has been determined in the course of Kex determination. Liquid/liquid interfaces had not been reported, except for our studies [1,2,3] and a description [11] with respect to the distribution of a simple salt, such as Bu4NBr. In the present paper, selecting benzene (Bz) as the representative less-polar diluent, we determined from available extraction data [12,13,14,15] Δφeq values at the Bz/w interface. Individual distribution constants of the ion-pair complexes NaL+Pic− and the complex ions (NaL+), which constitute parts of the complexes, into the four diluents were estimated from the above results and their properties for solute-solvent interaction were discussed

Experimental Section
Results and Discussion
Determination of Extraction Constants and Their Several
Conclusions
Check of the Employed Data by Benford’s Law
Empirical Parameters Which Express L’s Characteristics with Their Exchanges
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