IUPAC-NIST Solubility Database
NIST Standard Reference Database 106


Glass Ball as Bullet Solubility System: 2-Propanol with Toluene and Water

Components:
   (1) Water; H2O; [7732-18-5]  NIST Chemistry WebBook for detail
   (2) 2-Propanol (isopropanol, isopropyl alcohol); C3H8O; [67-63-0]  NIST Chemistry WebBook for detail
   (3) Toluene (methylbenzene); C7H8; [108-88-3]  NIST Chemistry WebBook for detail

Original Measurements:
   Washburn, E.R.; Beguin, A.E., J. Am. Chem. Soc. 62, 579 (1940).

Variables:
   Temperature = 298 K

Prepared By:
   A. Skrzecz

Experimental Data:   (Notes on the Nomenclature)
  
Compositions along the saturation curve
t/°CT/KMass Fraction w1Mass Fraction w2Mole Fraction x1 (compiler)Mole Fraction x2 (compiler)
25.0298.150.04250.00130.01310.0003
25.0298.150.10760.00180.03490.0004
25.0298.150.16500.00300.05610.0007
25.0298.150.23400.00380.08420.0009
25.0298.150.30160.01070.11590.0027
25.0298.150.34380.01880.13850.0049
25.0298.150.39440.04220.17140.0120
25.0298.150.43640.06750.20440.0206
25.0298.150.47530.10740.24530.0362
25.0298.150.49570.14130.27560.0512
25.0298.150.51010.18270.30840.0720
25.0298.150.51170.22550.33330.0958
25.0298.150.50890.27730.36270.1289
25.0298.150.49610.33500.38820.1710
25.0298.150.48140.37360.39830.2016
25.0298.150.45590.42700.40520.2475
25.0298.150.42550.47090.39460.2848
25.0298.150.39050.52630.38610.3394
25.0298.150.34300.59280.36340.4097
25.0298.150.27450.68720.32280.5270
25.0298.150.21760.75500.27150.6144
25.0298.150.15970.82430.21270.7162
25.0298.150.10640.88480.14930.8096
25.0298.150.04310.95300.06360.9172
Compositions of coexisting phases
t/°CT/KMass Fraction w1Mass Fraction w2Mole Fraction x1 (compiler)Mole Fraction x2 (compiler)Comment(s)
25.00298.150.00890.99110.01360.9864hydrocarbon-rich phase
25.00298.150.02270.97640.03430.9612hydrocarbon-rich phase
25.00298.150.07450.91840.10690.8592hydrocarbon-rich phase
25.00298.150.14340.84300.19420.7444hydrocarbon-rich phase
25.00298.150.24900.71900.30190.5686hydrocarbon-rich phase
25.00298.150.30620.64350.34260.4696hydrocarbon-rich phase
25.00298.150.37900.54200.38050.3549hydrocarbon-rich phase
25.00298.150.44230.44350.39760.2600hydrocarbon-rich phase
25.00298.150.48570.36350.39620.1934hydrocarbon-rich phase
25.00298.150.49950.32600.38590.1643hydrocarbon-rich phase
25.00298.150.51000.27160.36020.1251hydrocarbon-rich phase
25.00298.150.51050.26400.35580.1200hydrocarbon-rich phase
25.00298.150.51200.23560.33960.1019hydrocarbon-rich phase
25.00298.150.06870.00010.02160.0000water-rich phase
25.00298.150.12160.00300.04000.0006water-rich phase
25.00298.150.19770.00280.06900.0006water-rich phase
25.00298.150.24140.00520.08750.0012water-rich phase
25.00298.150.29000.01020.11020.0025water-rich phase
25.00298.150.31400.01250.12220.0032water-rich phase
25.00298.150.34340.01460.13770.0038water-rich phase
25.00298.150.37400.02960.15700.0081water-rich phase
25.00298.150.39920.04330.17450.0123water-rich phase
25.00298.150.42100.05580.19110.0165water-rich phase
25.00298.150.44130.07090.20870.0219water-rich phase
25.00298.150.44730.08470.21670.0268water-rich phase
25.00298.150.46500.09500.23310.0311water-rich phase
Method/Apparatus/Procedure:
   The titration method, as described in Ref. 1, 2, was used. Refractive indexes of mixtures were measured by Abbe refractometer. Binary mixtures of known composition placed in small Erlenmeyer flasks were titrated with water or toluene from weighed pipettes and shaken mechanically in a constant temperature bath. Measured refractive indexes of saturated solutions were plotted for each component. These plots were used further to determine concentration of equilibrium  phases. Tie lines were obtained by adding alcohol to water-toluene mixtures and shaking the samples from time to time during the twenty-four hours while they were kept in constant temperature bath. After separation, refractive indexes of both phase were measured and concentration of each component was read from the plots. The sum of calculated phase concentrations was always equal to 1.0000±0.0001.

Source and Purity of Materials:
   (1) Eastman Kodak Company; refluxed with CaO, distilled, middle fraction was used; b.p.=81.7-81.9°C, d(25°C,4°C)=0.780 87, n(25°C,D)=1.3748.
   (2) Eastman Kodak Company; used as received; n(25°C,D)=1.4938.
   (3) Distilled over KMnO4.

Estimated Errors:
   Solubility: Not reported.
   Temperature: Temp. ±0.01°C.

References:
   1 R. Vold and E. R. Washburn, J. Am. Chem. Soc. 54, 4217 (1932).
   2 E. R. Washburn and H. C. Spencer, J. Am. Chem. Soc. 56, 361 (1934).