IUPAC-NIST Solubility Database
NIST Standard Reference Database 106


Glass Ball as Bullet Solubility System: Nitroethane with Decane

Components:
   (1) Decane; C10H22; [124-18-5]  NIST Chemistry WebBook for detail
   (2) Nitroethane; C2H5NO2; [79-24-3]  NIST Chemistry WebBook for detail

Evaluator:
   V P. Sazonov, Technical University, Samara, Russia, May, 2000.

Critical Evaluation:

                  Solubilities in the system nitroethane (1) + decane (2) were reported in three publications. Francis1 determined the upper critical solution temperature (UCST). Hwa et al.2 measured of the mutual solubilities of the two components between 275 and 326 K by the synthetic and analytical methods. Clever et al.3 determined solubility of nitroethane in decane at 331.2 K by synthetic method.
              The upper critical solution temperature has been reported as 323.2 K (Francis1) and 325.8 K (Hwa et al.2). The critical solution concentration is determined as xcl = 0.63 ± 0.01 by the evaluator on the basis of the solubility curve of binary system.2
              The experimental data reported in Hwa et al.2 have been approximated (with the same weighing factor) by an equation based on the scaling law (described in the preface to this volume) for which the following parameters were derived:

                             a1 = 0.79747, a2 = 0.15937, b1 = 1.22859, b2 = -1.55933 (mean standard error of estimate was 0.0430).

               For this approximation values xcl and UCST from Hwa et al.2 were used. In the opinion of the evaluator, all experimental solubility data and the smoothed mutual solubility, calculated by this equation, may be treated as tentative. The results of calculations for selected temperatures are presented in Table. This relationship together with experimental points2 are also presented in Fig. 9.

Experimental Data:   (Notes on the Nomenclature)

Mutual solubility of nitroethane and decane
T/K102 * Mass Fraction w1Mole Fraction x1Comment(s)
278.2 3.90.072hydrocarbon-rich phase
283.2 5.40.098hydrocarbon-rich phase
288.2 7.00.125hydrocarbon-rich phase
293.2 8.80.154hydrocarbon-rich phase
298.210.70.186hydrocarbon-rich phase
303.213.00.221hydrocarbon-rich phase
308.215.70.261hydrocarbon-rich phase
313.218.90.307hydrocarbon-rich phase
318.223.30.365hydrocarbon-rich phase
319.224.30.379hydrocarbon-rich phase
320.225.50.394hydrocarbon-rich phase
321.226.90.411hydrocarbon-rich phase
322.228.50.430hydrocarbon-rich phase
323.230.40.453hydrocarbon-rich phase
324.232.90.482hydrocarbon-rich phase
325.236.80.525hydrocarbon-rich phase
Mutual solubility of nitroethane and decane
T/K102 * Mass Fraction w1Mole Fraction x1Comment(s)
278.297.00.984nitroethane-rich phase
283.295.00.973nitroethane-rich phase
288.293.00.962nitroethane-rich phase
293.290.90.950nitroethane-rich phase
298.288.40.935nitroethane-rich phase
303.285.70.919nitroethane-rich phase
308.282.60.900nitroethane-rich phase
313.278.80.876nitroethane-rich phase
318.273.80.842nitroethane-rich phase
319.272.60.834nitroethane-rich phase
320.271.20.824nitroethane-rich phase
321.269.60.813nitroethane-rich phase
322.267.80.800nitroethane-rich phase
323.265.70.784nitroethane-rich phase
324.262.90.763nitroethane-rich phase
325.258.50.728nitroethane-rich phase
View Figure 1 for this Evaluation

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

   1  Francis, A.W., Critical Solution Temperatures. Adv. Chem. Ser. 31 (1961).
   2  Hwa, S.C.P.; Techo, R.; Ziegler, W.T., J. Chem. Eng. Data 8, 409-11 (1963).
   3  Clever, H.L.; Pirkle, Q.R. Jr.; Allen, B.J. Jr.; Derrick, M.E., J. Chem. Eng. Data 17, 31-4 (1972).