IUPAC-NIST Solubility Database
NIST Standard Reference Database 106


Glass Ball as Bullet Solubility System: Ethanol with Hexane (n-hexane) with Water

Components:
   (1) Water; H2O; [7732-18-5]  NIST Chemistry WebBook for detail
   (2) Ethanol (ethyl alcohol); C2H6O; [64-17-5]  NIST Chemistry WebBook for detail
   (3) Hexane (n-hexane); C6H14; [110-54-3]  NIST Chemistry WebBook for detail

Original Measurements:
   Moriyoshi, T.; Uosaki, Y.; Matsuura, H.; Nishimoto, W., J. Chem. Thermodyn, 20, 551 (1988).

Variables:
   Temperature = 298 K

Prepared By:
   A. Skrzecz

Experimental Data:   (Notes on the Nomenclature)
  
Compositions of coexisting phases
t/°CT/KMass Fraction w1 (compiler) Mass Fraction w2 (compiler)Mole Fraction x1Mole Fraction x2Comment(s)
25.00298.150.0140.9860.0260.974hydrocarbon-rich phase
25.00298.150.0170.9830.0310.966hydrocarbon-rich phase
25.00298.150.0230.9770.0420.956hydrocarbon-rich phase
25.00298.150.0250.9720.0460.943hydrocarbon-rich phase
25.00298.150.0340.9640.0620.930hydrocarbon-rich phase
25.00298.150.0420.9550.0760.914hydrocarbon-rich phase
25.00298.150.0580.9410.1020.890hydrocarbon-rich phase
25.00298.150.0690.9280.1200.865hydrocarbon-rich phase
25.00298.150.1000.8980.1700.818hydrocarbon-rich phase
25.00298.150.1140.8800.1900.784hydrocarbon-rich phase
25.00298.150.1640.8280.2620.705hydrocarbon-rich phase
25.00298.150.1780.8130.2790.683hydrocarbon-rich phase
25.00298.150.2160.7700.3260.621hydrocarbon-rich phase
25.00298.150.2280.7580.3410.605hydrocarbon-rich phase
25.00298.150.2470.7380.3640.581hydrocarbon-rich phase
25.00298.150.0120.9880.0220.978hydrocarbon-rich phase
25.00298.150.0210.9790.0380.959hydrocarbon-rich phase
25.00298.150.0270.9730.0490.950hydrocarbon-rich phase
25.00298.150.0350.9630.0640.930hydrocarbon-rich phase
25.00298.150.0360.9640.0650.935hydrocarbon-rich phase
25.00298.150.0410.9570.0740.916hydrocarbon-rich phase
25.00298.150.0590.9400.1050.892hydrocarbon-rich phase
25.00298.150.1250.8710.2080.775hydrocarbon-rich phase
25.00298.150.1580.8350.2540.718hydrocarbon-rich phase
25.00298.150.0100.9890.0190.978hydrocarbon-rich phase
25.00298.150.0180.9810.0340.965hydrocarbon-rich phase
25.00298.150.0200.9800.0360.964hydrocarbon-rich phase
25.00298.150.0250.9750.0460.953hydrocarbon-rich phase
25.00298.150.0310.9690.0570.943hydrocarbon-rich phase
25.00298.150.0350.9650.0630.934hydrocarbon-rich phase
25.00298.150.0430.9550.0760.912hydrocarbon-rich phase
25.00298.150.1020.8950.1730.814hydrocarbon-rich phase
25.00298.150.1220.8740.2030.779hydrocarbon-rich phase
25.00298.150.1540.8400.2490.725hydrocarbon-rich phase
25.00298.150.0130.9870.0240.974hydrocarbon-rich phase
25.00298.150.0160.9840.0290.971hydrocarbon-rich phase
25.00298.150.0210.9790.0390.961hydrocarbon-rich phase
25.00298.150.0220.9780.0410.959hydrocarbon-rich phase
25.00298.150.0250.9750.0460.954hydrocarbon-rich phase
25.00298.150.0350.9650.0640.936hydrocarbon-rich phase
25.00298.150.1030.8940.1760.813hydrocarbon-rich phase
25.00298.150.1220.8740.2040.779hydrocarbon-rich phase
25.00298.150.0080.9900.0150.975hydrocarbon-rich phase
25.00298.150.0110.9880.0200.975hydrocarbon-rich phase
25.00298.150.0120.9870.0230.975hydrocarbon-rich phase
25.00298.150.0170.9830.0310.969hydrocarbon-rich phase
25.00298.150.0310.9660.0560.932hydrocarbon-rich phase
25.00298.150.0510.9480.0910.904hydrocarbon-rich phase
25.00298.150.0880.9100.1510.839hydrocarbon-rich phase
25.00298.150.1990.8790.2000.790hydrocarbon-rich phase
25.00298.150.5330.0030.3100.001water-rich phase
25.00298.150.5990.0090.3730.003water-rich phase
25.00298.150.6470.0140.4250.005water-rich phase
25.00298.150.6860.0190.4730.007water-rich phase
25.00298.150.7120.0430.5230.017water-rich phase
25.00298.150.7280.0560.5560.023water-rich phase
25.00298.150.7360.0960.6050.042water-rich phase
25.00298.150.7310.1230.6240.056water-rich phase
25.00298.150.7120.1790.6550.088water-rich phase
25.00298.150.6840.2250.6600.116water-rich phase
25.00298.150.6560.2660.6590.143water-rich phase
25.00298.150.5990.3410.6410.195water-rich phase
25.00298.150.5690.3750.6240.220water-rich phase
25.00298.150.5320.4210.6070.257water-rich phase
25.00298.150.5170.4390.5990.272water-rich phase
25.00298.150.5550.0030.3290.001water-rich phase
25.00298.150.6680.0170.4500.006water-rich phase
25.00298.150.7110.0310.5130.012water-rich phase
25.00298.150.7350.0470.5580.019water-rich phase
25.00298.150.7360.0580.5690.024water-rich phase
25.00298.150.7460.0790.6030.034water-rich phase
25.00298.150.7420.1230.6440.057water-rich phase
25.00298.150.6770.2460.6740.131water-rich phase
25.00298.150.6070.3370.6530.194water-rich phase
25.00298.150.5740.0030.3460.001water-rich phase
25.00298.150.6740.0170.4570.006water-rich phase
25.00298.150.7140.0290.5150.011water-rich phase
25.00298.150.7370.0440.5590.018water-rich phase
25.00298.150.7490.0590.5890.025water-rich phase
25.00298.150.7540.0650.6030.028water-rich phase
25.00298.150.7600.0950.6430.043water-rich phase
25.00298.150.6990.2440.6680.118water-rich phase
25.00298.150.6510.2880.6770.160water-rich phase
25.00298.150.6020.3490.6580.204water-rich phase
25.00298.150.6760.0110.4560.004water-rich phase
25.00298.150.7150.0290.5160.011water-rich phase
25.00298.150.7400.0400.5590.016water-rich phase
25.00298.150.7480.0460.5760.019water-rich phase
25.00298.150.7580.0610.6050.026water-rich phase
25.00298.150.7640.0910.6460.041water-rich phase
25.00298.150.6740.2640.6920.145water-rich phase
25.00298.150.6500.2970.6880.168water-rich phase
25.00298.150.6380.0060.4110.002water-rich phase
25.00298.150.6890.0160.4750.006water-rich phase
25.00298.150.7130.0260.5120.010water-rich phase
25.00298.150.7430.0370.5610.015water-rich phase
25.00298.150.7730.0800.6490.036water-rich phase
25.00298.150.7560.1440.6950.071water-rich phase
25.00298.150.7040.2330.7110.126water-rich phase
25.00298.150.6480.3040.6950.174water-rich phase
Method/Apparatus/Procedure:
   The experimental apparatus consisted of a high-pressure equilibrium cell, two hand operated pumps, a pressure exchanger, and two pressure gauges. The equilibrium cell, a stainless-steel cylinder of 50 cm3 capacity, with mechanical stirrer was immersed in a thermostat. The mixture, prepared by mass, were stirred under the desired conditions for at least 8 h and then allowed to settle for 2 h. Samples of each layer were withdrawn for glc  analysis (glass column, 3.2 mm I.d., 150 cm long, packed with PEG-6000 Shimalite F; T/K=343; thermal-conductivity detector equipped with electronic intergrator). Acetone was used as an inert standard. Compositions were determined from the peak-area ratio and the calibration curve. Analysis of each phase were done at least twice.

Source and Purity of Materials:
   (1) Source not specified; dried by refluxing with CaO, followed by the Lund-Bjerrum magnesium method, distilled.
   (2) Source not specified; shaken with conc. H2SO4, neutralized with aq. NaOH, dried over CaCI2, distilled.
   (3) De-ionized, distilled over KMnO4, redistilled.

Estimated Errors:
   Solubility: Not reported.
   Temperature: Temp. ±0.002 K (control of the thermostat); press. ±0.1 Mpa; composition ±0.003 mass fraction.