IUPAC-NIST Solubility Database
NIST Standard Reference Database 106


Glass Ball as Bullet Solubility System: Acetonitrile with Pentane

Components:
   (1) Acetonitrile; C2H3N; [75-05-8]  NIST Chemistry WebBook for detail
   (2) Pentane; C5H12; [109-66-0]  NIST Chemistry WebBook for detail

Evaluator:
   Valerii P. Sazonov and Nikolai V. Sazonov, Technical University, Samara, Russia, September, 2001

Critical Evaluation:

           Solubilities in the system comprising acetonitrile and pentane have been reported in three publications.

        Sinegubova1 studied the mutual solubilities of acetonitrile (1) and pentane (2) between 298 and 341K by the synthetic method. Rakotondramanama et al.2 measured the mutual solubilities of (1) and (2) by the titration method between 298 and 303 K. McLure et al.3 determined the upper critical solution temperature of (1) and (2) by the synthetic method.

        The upper critical solution temperature has been reported as 341.2 K3 and 341.4 K.1 These data are in reasonable agreement and thus their average value: UCST = 341.3 ± 0.1 K is recommended. The corresponding critical solution composition has been not reported but was calculated by the evaluators from reported data1 to be xcl = 0.53.

        Reported1,2 experimental values have been approximated by an equation based on the scaling law (described in the introduction to this volume) for which the following parameters have been derived:

a1 = 0.9063, a2= -0.1988, b1 = 3.1067, b2 = -2.7492

(mean standard error of estimate was 0.0036).
        For approximation xcl and UCST determined by Sinegubova1 have been used. In the opinion of the evaluators, the mutual solubilities calculated by this equation may be treated as tentative. The results of calculations for the selected temperatures are presented in the following table. This relationship together with experimental data1,2 are also presented in Fig. 6.
        Solubilities in the system comprising acetonitrile and pentane have been reported in three publications.

        Sinegubova1 studied the mutual solubilities of acetonitrile (1) and pentane (2) between 298 K and 341K by the synthetic method. Rakotondramanama et al.2 measured the mutual solubilities of (1) and (2) by the titration method between 298 K and 303 K. McLure et al.3 determined the upper critical solution temperature of (1) and (2) by the synthetic method.

        The upper critical solution temperature has been reported as 341.2 K3 and 341.4 K.1 These data are in reasonable agreement and thus their average value: UCST = 341.3 ± 0.1 K is recommended. The corresponding critical solution composition has been not reported but was calculated by the evaluators from reported data1 to be xcl = 0.53.

        Reported1,2 experimental values have been approximated by an equation based on the scaling law (described in the introduction to this volume) for which the following parameters have been derived:

a1 = 0.9063, a2= –0.1988, b1 = 3.1067, b2 = -2.7492

(mean standard error of estimate was 0.0036).
        For approximation xcl and UCST determined by Sinegubova1 have been used. In the opinion of the evaluators, the mutual solubilities calculated by this equation may be treated as tentative. The results of calculations for the selected temperatures are presented in the following table. This relationship together with experimental data1,2 are also presented in Fig. 6.

Experimental Data:   (Notes on the Nomenclature)

Interpolated mutual solubility of acetonitrile (1)  and pentane (2)
T/K102 * Mass Fraction w1Mole Fraction x1Comment(s)
293.2  2.90.050Hydrocarbon-rich phase
298.2  3.70.063Hydrocarbon-rich phase
303.2  4.60.078Hydrocarbon-rich phase
308.2  5.60.094Hydrocarbon-rich phase
313.2  6.80.114Hydrocarbon-rich phase
318.2  8.30.137Hydrocarbon-rich phase
323.310.20.166Hydrocarbon-rich phase
328.212.50.201Hydrocarbon-rich phase
333.215.80.248Hydrocarbon-rich phase
338.221.50.325Hydrocarbon-rich phase
339.223.50.350Hydrocarbon-rich phase
340.226.20.384Hydrocarbon-rich phase
340.728.20.408Hydrocarbon-rich phase
341.231.80.450Hydrocarbon-rich phase
293.287.40.924Acetonitrile-rich phase
298.285.20.910Acetonitrile-rich phase
303.282.90.895Acetonitrile-rich phase
308.280.50.879Acetonitrile-rich phase
313.278.00.862Acetonitrile-rich phase
318.275.30.843Acetonitrile-rich phase
323.372.30.821Acetonitrile-rich phase
328.268.80.795Acetonitrile-rich phase
333.264.60.762Acetonitrile-rich phase
338.257.90.707Acetonitrile-rich phase
339.255.80.689Acetonitrile-rich phase
340.252.70.662Acetonitrile-rich phase
340.750.50.642Acetonitrile-rich phase
341.246.70.606Acetonitrile-rich phase
View Figure 6 for this Evaluation

References: (Click a link to see its experimental data associated with the reference)

   1  Sinegubova, S.I., Dissertation, Saratov University 1978.
   2  Rakotondramanana, S.; Borredon, M.E.; Mollnier, J., J. Chem. Eng. Data 32, 308-11 (1987).
   3  McLure, I.A.; Rodriguez, A.T.; Ingham, P.A.; Steele, J.F., Fluid Phase Equilib. 8, 271 (1982).