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3 C. J. Pedersen, J. Am. Chem. Soc., 1967, 89, 7017.
4 W. J. McDowell, G. N. Case, J. A. McDonough and R. A. Bartsch,
Anal. Chem., 1992, 64, 3013.
data point. For proper weighting of the data in SXLSQI model-
ing (see below), experimental precision for each data point was
estimated from a combination of replicate determinations,
volumetric error, and counting precision. From these consider-
ations, the precision was taken to be constant at 3% for all
data points.
5 W. J. McDowell, Sep. Sci. Technol., 1988, 23, 1251; L. Tusek,
P. R. Danesi and R. Chiarizia, J. Inorg. Nucl. Chem., 1975, 37, 1538.
6 R. M. Izatt, J. S. Bradshaw, S. A. Nielsen, J. D. Lamb, J. J.
Christensen and D. Sen, Chem. Rev., 1985, 85, 271; R. M. Izatt,
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G. N. Case and F. I. Case, Solvent Extr. Ion Exch., 1986, 4, 217;
B. P. Hay, D. Zhang and J. R. Rustad, Inorg. Chem., 1996, 35, 2650.
7 R. A. Sachleben, Y. Deng, D. R. Bailey and B. A. Moyer, Solvent
Extr. Ion Exch., 1996, 14, 995; Y. Deng, R. A. Sachleben and
B. A. Moyer, J. Chem. Soc., Faraday Trans., 1995, 23, 4215.
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Analysis. The caesium distribution from aqueous solutions to
the 1,2-DCE phase was determined by gamma-counting tech-
niques (137Cs tracer) using a 3 inch NaI(Tl) crystal through-hole
type detector (Packard Cobra Quantum Model 5003). Caesium
distribution ratios DCs, defined as the ratio of total organic- and
aqueous-phase caesium concentrations [Cs]org/[Cs]aq, were
obtained directly as the ratio of background-corrected count
rates per mL. In control experiments, no extraction within
background was observed for 1,2-DCE (without crown ether)
equilibrated with aqueous CsNO3 or CsClO4 solutions under
the experimental conditions employed.
9 R. A. Sachleben, J. C. Bryan, J. M. Lavis, C. M. Starks and
J. H. Burns, Tetrahedron, 1997, 53, 13567.
10 T. G. Levitskaia, J. C. Bryan, R. A. Sachleben, J. D. Lamb and
B. A. Moyer, J. Am. Chem. Soc., 2000, 122, 554.
Data treatment. The caesium distribution ratios DCs were
used as input by the solvent extraction modeling program
SXLSQI.21 Nonideality effects were taken into account by use
of Pitzer parameters for aqueous ions, the Hildebrand–Scott
treatment for non-ionic effects in the organic phase, and the
Debye–Hückel treatment for electrostatic effects in the organic
phase.21,23–25,27,28 All constants are thus corrected to infinite dilu-
tion. The program converts the molar concentration to the
molality scale employed in the Pitzer treatment using Masson
coefficients.29 The solubility parameters and molar volumes of
the ligand were estimated from group contributions.23 Param-
eters used in the SXLSQI program are summarized in the
electronic supplementary information.
11 A. H. Bond, R. Chiarizia, V. J. Huber, M. L. Dietz, A. W. Herlinger
and B. P. Hay, Anal. Chem., 1999, 71, 2757; M. L. Dietz, A. H.
Bond, M. Clapper and J. W. Finch, Radiochim. Acta, 1999, 85, 119.
12 J. C. Bryan, K. Kavallieratos and R. A. Sachleben, Inorg. Chem.,
2000, 39, 1568; J. C. Bryan, R. A. Sachleben, G. J. Bunick and
B. P. Hay, Inorg. Chim. Acta, 1999, 290, 86.
13 G. G. Talanova, N. S. A. Elkarim, V. S. Talanov, R. E. Hanes, Jr.,
H.-S. Hwang, R. A. Bartsch and R. D. Rogers, J. Am. Chem. Soc.,
1999, 121, 11281.
14 J. C. Bryan, G. J. Bunick and R. A. Sachleben, Acta Crystallogr.,
Sect. C: Cryst. Struct., 1999, 55, 250.
15 J. C. Bryan, J. M. Lavis, B. P. Hay and R. A. Sachleben, Acta
Crystallogr., Sect. C: Cryst. Struct., 2000, 56, 391.
16 J. Dale, Isr. J. Chem., 1980, 20, 3.
17 T. Steiner, Crystallogr. Rev., 1996, 6, 1.
18 J. Czapkiewicz and B. Czapkiewicz-Tutaj, J. Chem. Soc., Faraday
Trans. 1, 1980, 76, 1663.
19 I. M. Kolthoff, M. K. Chantooni and W.-J. Wang, J. Chem. Eng.
Data, 1993, 38, 556.
20 T. J. Haverlock, P. V. Bonnesen, R. A. Sachleben and B. A. Moyer,
J. Inclusion Phenom. Macrocyclic Chem., 2000, 36, 21.
21 C. F. Baes, Jr., B. A. Moyer, G. N. Case and F. I. Case, Sep. Sci.
Technol., 1990, 25, 1675; C. F. Baes, Jr., SXLSQI, A Program for
Modeling Solvent Extraction Systems, Report ORNL/TM-13604,
Oak Ridge National Laboratory, 1998; C. F. Baes, Jr., Solvent Extr.
Ion Exch., in the press.
22 B. A. Moyer, in Comprehensive Supramolecular Chemistry, ed. G. W.
Gokel, Pergamon, Oxford, 1996, vol. 1, p. 377.
23 A. F. M. Barton, CRC Handbook of Solubility Parameters and Other
Cohesion Parameters, CRC Press, Boca Raton, Florida, 1991.
24 K. S. Pitzer, in Activity Coefficients in Electrolyte Solutions, ed. K. S.
Pitzer, CRC Press, Boca Raton, Florida, 1991, ch. 3.
25 E. J. Henley and J. D. Seader, Equilibrium-Stage Separation
Operation in Chemical Engineering; John Wiley & Sons, New York,
1981.
26 J. C. Bryan, R. A. Sachleben, J. M. Lavis, M. C. Davis, J. H. Burns
and B. P. Hay, Inorg. Chem., 1998, 37, 2749.
Acknowledgements
This research was sponsored by the Division of Chemical
Sciences, Geosciences, and Biosciences, Office of Basic Energy
Sciences, US Department of Energy, under contract DE-AC05-
00OR22725 with Oak Ridge National Laboratory, managed
and operated by UT-Battelle, LLC.
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