IUPAC-NIST Solubility Database
NIST Standard Reference Database 106


Glass Ball as Bullet Solubility System: Nitroethane with 2,2,4-Trimethylpentane

Components:
   (1) 2,2,4-Trimethylpentane; C8H18; [540-84-1]  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:

                 Quantitative solubility data for the system nitroethane (1) + 2,2,4-trimethylpentane (2) were reported in the publications listed in Table 1.

              Beysens and Tufeu7 determined of the variation of the critical temperature as a function of pressure (from 500 to 12500 kPa). All original data are compiled immediately following this Critical Evaluation.
              The data point for the nitroethane-rich phase at 298 K (Hsu and Clever3) is marked disagreement with other studies and is therefore rejected. The table below has been prepared on the basis of all other reported data. Values obtained by the evaluator by graphical interpolation or extrapolation from the data sheets are presented in the Table 2 and Table 3. Data are "recommended" if two or more apparently reliable studies are is reasonable (± 5 % relative) agreement. All other data are regarded as tentative only.

              The upper critical solution temperature (USCT) has been reported as 302.15 K,6 302.7 K,2 303.0 K,1 303.18 K,4 and 303.20 K.5 The UCST of Battler and Rowley6 is rejected. Thus, the recommended value is: Tc = (303.0 ± 0.2) K.
              The corresponding critical solution composition has been reported as xcl = 0.491 (Vreeland and Dunlap1), xcl = 0.569 (Beysens4) and xcl = 0.5692 (Tanaka and Wada5). The xcl of Vreeland and Dunlap1 is rejected. The data average xcl = 0.569. This value is recommended.
              The recommended and tentative values for the mutual solubility reported in Table 2 and Table 3 have been approximated by an equation based on the scaling law (described in the preface to this volume) for which the following parameters were derived: a1 = 0.95870, a2 = -0.24393, b1 = 1.50442, b2 = 1.68914 (mean standard error of estimate was 0.0118).
              For this approximation, recommended values of UCST and xcl have been used. This relationship is presented in Fig. 7 together with experimental data reported in several references.1,2,4

Experimental Data:   (Notes on the Nomenclature)

Table 1. Summary of solubility data for the system nitroethane + 2,2,4-trimethylpentane
AuthorT/KReferenceSolubilityMethod
Vreeland and Dunlap298 to 3031mutualsynthetic
Hwa et al.275 to 3032mutualanalytical/synthetic
Hsu and Clever2983mutualnot stated
Beysens297 to 3044mutualsynthetic
Tanaka and Wada3035UCSTnot stated
Battler and Rowley293 and 3026mutualnot stated
Table 2. Recommended and tentative values for the mutual solubilities of nitroethane and 2,2,4-trimethylpentane
T/K102 * Mass Fraction w1w1 NoteMole Fraction x1x1 NoteComment(s)
278.2 8.7tentative0.126tentativehydrocarbon-rich phase
283.210.7tentative0.155tentativehydrocarbon-rich phase
288.213.2tentative0.188tentativehydrocarbon-rich phase
293.215.3tentative0.212tentativehydrocarbon-rich phase
298.222.3recommended0.304recommendedhydrocarbon-rich phase
300.228.9recommended0.382recommendedhydrocarbon-rich phase
302.233.3recommended0.432recommendedhydrocarbon-rich phase
Table 3. Recommended and tentative values for the mutual solubilities of nitroethane and 2,2,4-trimethylpentane
T/K102 * Mass Fraction w2w2 NoteMole Fraction x2x2 NoteComment(s)
278.214.5tentative0.100tentativenitroethane-rich phase
283.216.6tentative0.115tentativenitroethane-rich phase
288.219.5tentative0.137recommendednitroethane-rich phase
293.223.4recommended0.167recommendednitroethane-rich phase
298.228.7recommended0.209recommendednitroethane-rich phase
300.231.8recommended0.234recommendednitroethane-rich phase
302.238.2recommended0.288recommendednitroethane-rich phase
View Figure 1 for this Evaluation

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

   1  Vreeland, J.; Dunlap, R., J. Phys. Chem. 61, 329-33 (1957).
   2  Hwa, S.C.P.; Techo, R.; Ziegler, W.T., J. Chem. Eng. Data 8, 409-11 (1963).
   3  Hsu, K.Y.; Clever, H.L., J. Chem. Eng. Data 20, 268-71 (1975).
   4  Beysens, D., J. Chem. Phys. 71, 2557-65 (1979).
   5  Tanaka, H.; Wada, Y., Chem. Phys. 78, 143-9 (1983).
   6  Battler, J.R.; Rowley, R.L., J. Chem. Eng. Data 35, 334-8 (1990).
   7  Beysens D.; Tufeu, R., Rev. Phys. Appl. 14, 907-9 (1979).