IUPAC-NIST Solubility Database
NIST Standard Reference Database 106


Glass Ball as Bullet Solubility System: Nitroethane with Methanol, 1,2-Ethanediol and Cyclohexane

Components:
   (1) 1,2-Ethanediol; C2H6O2 ; [107-21-1]  NIST Chemistry WebBook for detail
   (2) Cyclohexane; C6H12; [110-82-7]  NIST Chemistry WebBook for detail
   (3) Methanol; CH4O; [67-56-1]  NIST Chemistry WebBook for detail
   (4) Nitroethane; C2H5NO2; [79-24-3]  NIST Chemistry WebBook for detail

Original Measurements:
   Chrapec, J.; Rzoska, S.; Ziolo, J., Phase Transitions 4, 73-80 (1983).

Variables:
   Temperature = 296 K to 307 K

Prepared By:
   V. P. Sazonov and N. V. Sazonov

Experimental Remarks:

   The solubility temperatures of liquid phases were determined in quaternary mixtures with a constant mass relationship of (1), (2) and (3), and also in quaternary mixtures with a constant mass relationship of (1), (2) and (4).

Estimated tricritical point of quaternary system is 37.5 ± 1 °C at x1 = 0.45, x2 = 0.06, x3 = 0.09 and x4 = 0.45 (100 w1 = 45.1, 100 w2 = 2.6, 100 w3 = 7.5 and 100 w4 = 44.9, compilers).

Experimental Data:   (Notes on the Nomenclature)
  

Solubility temperatures of the three liquid phases
t/°CT/K102 * Mass Fraction w1102 * Mass Fraction w2102 * Mass Fraction w3Mole Fraction x1 (compiler)Mole Fraction x2 (compiler)Mole Fraction x3 (compiler)Comment(s)
23.3296.55.348.821.90.1140.4470.243constant mass relationship methanol : nitroethane : 1,2-ethanediol = 7.0 : 64.2 : 28.8
24.3297.55.046.220.80.1080.4280.233constant mass relationship methanol : nitroethane : 1,2-ethanediol = 7.0 : 64.2 : 28.8
24.9298.13.229.513.30.0740.2910.159constant mass relationship methanol : nitroethane : 1,2-ethanediol = 7.0 : 64.2 : 28.8
25.4298.64.742.819.20.1030.4010.218constant mass relationship methanol : nitroethane : 1,2-ethanediol = 7.0 : 64.2 : 28.8
25.5298.73.733.615.10.0840.3260.177constant mass relationship methanol : nitroethane : 1,2-ethanediol = 7.0 : 64.2 : 28.8
25.7298.94.036.916.60.0900.3540.193constant mass relationship methanol : nitroethane : 1,2-ethanediol = 7.0 : 64.2 : 28.8
25.8299.04.440.018.00.0980.3790.206constant mass relationship methanol : nitroethane : 1,2-ethanediol = 7.0 : 64.2 : 28.8
24.3297.53.120.1 9.00.0740.2040.110constant mass relationship methanol : nitroethane : 1,2-ethanediol = 9.5 : 62.4 : 28.1
24.9298.17.247.421.40.1510.4250.232constant mass relationship methanol : nitroethane : 1,2-ethanediol = 9.5 : 62.4 : 28.1
25.8299.03.522.810.20.0820.2280.123constant mass relationship methanol : nitroethane : 1,2-ethanediol = 9.5 : 62.4 : 28.1
26.8300.06.945.020.30.1460.4070.222constant mass relationship methanol : nitroethane : 1,2-ethanediol = 9.5 : 62.4 : 28.1
27.0300.23.825.011.20.0880.2480.134constant mass relationship methanol : nitroethane : 1,2-ethanediol = 9.5 : 62.4 : 28.1
28.1301.36.441.818.80.1380.3840.209constant mass relationship methanol : nitroethane : 1,2-ethanediol = 9.5 : 62.4 : 28.1
28.2301.44.529.313.20.1020.2840.155constant mass relationship methanol : nitroethane : 1,2-ethanediol = 9.5 : 62.4 : 28.1
28.6301.84.932.514.60.1100.3110.169constant mass relationship methanol : nitroethane : 1,2-ethanediol = 9.5 : 62.4 : 28.1
28.7301.95.938.717.40.1290.3600.196constant mass relationship methanol : nitroethane : 1,2-ethanediol = 9.5 : 62.4 : 28.1
28.7301.95.435.616.00.1190.3360.183constant mass relationship methanol : nitroethane : 1,2-ethanediol = 9.5 : 62.4 : 28.1
24.5297.74.022.410.10.0930.2230.121constant mass relationship methanol : nitroethane : 1,2-ethanediol = 11.0 : 61.4 : 27.6
26.1299.38.547.621.40.1760.4190.228constant mass relationship methanol : nitroethane : 1,2-ethanediol = 11.0 : 61.4 : 27.6
26.8300.04.726.411.90.1070.2570.140constant mass relationship methanol : nitroethane : 1,2-ethanediol = 11.0 : 61.4 : 27.6
27.7300.98.346.020.70.1720.4090.222constant mass relationship methanol : nitroethane : 1,2-ethanediol = 11.0 : 61.4 : 27.6
28.1301.35.329.313.20.1190.2810.153constant mass relationship methanol : nitroethane : 1,2-ethanediol = 11.0 : 61.4 : 27.6
28.8302.07.843.819.70.1640.3930.214constant mass relationship methanol : nitroethane : 1,2-ethanediol = 11.0 : 61.4 : 27.6
29.1302.35.832.614.60.1290.3080.167constant mass relationship methanol : nitroethane : 1,2-ethanediol = 11.0 : 61.4 : 27.6
29.3302.66.335.015.70.1380.3270.177constant mass relationship methanol : nitroethane : 1,2-ethanediol = 11.0 : 61.4 : 27.6
29.4302.67.340.818.40.1550.3710.202constant mass relationship methanol : nitroethane : 1,2-ethanediol = 11.0 : 61.4 : 27.6
29.6302.86.838.217.20.1470.3520.191constant mass relationship methanol : nitroethane : 1,2-ethanediol = 11.0 : 61.4 : 27.6
26.0299.25.125.811.60.1160.2500.136constant mass relationship methanol : nitroethane : 1,2-ethanediol = 12.0 : 60.7 : 27.3
27.0300.29.648.621.80.1950.4220.229constant mass relationship methanol : nitroethane : 1,2-ethanediol = 12.0 : 60.7 : 27.3
27.6300.85.728.712.90.1280.2740.149constant mass relationship methanol : nitroethane : 1,2-ethanediol = 12.0 : 60.7 : 27.3
29.5302.76.332.114.40.1390.3020.164constant mass relationship methanol : nitroethane : 1,2-ethanediol = 12.0 : 60.7 : 27.3
29.8303.09.145.820.60.1870.4020.219constant mass relationship methanol : nitroethane : 1,2-ethanediol = 12.0 : 60.7 : 27.3
30.5303.77.035.215.80.1520.3250.177constant mass relationship methanol : nitroethane : 1,2-ethanediol = 12.0 : 60.7 : 27.3
30.8304.08.643.719.70.1790.3880.211constant mass relationship methanol : nitroethane : 1,2-ethanediol = 12.0 : 60.7 : 27.3
31.2304.47.638.517.30.1620.3500.190constant mass relationship methanol : nitroethane : 1,2-ethanediol = 12.0 : 60.7 : 27.3
31.3304.58.040.418.10.1690.3640.197constant mass relationship methanol : nitroethane : 1,2-ethanediol = 12.0 : 60.7 : 27.3
24.9298.1 5.625.811.60.1260.2490.135constant mass relationship methanol : nitroethane : 1,2-ethanediol = 13.0 : 60.0 : 27.0
26.8300.0 6.228.813.00.1380.2730.149constant mass relationship methanol : nitroethane : 1,2-ethanediol = 13.0 : 60.0 : 27.0
29.5302.710.448.021.60.2090.4130.225constant mass relationship methanol : nitroethane : 1,2-ethanediol = 13.0 : 60.0 : 27.0
29.9303.1 7.434.215.40.1600.3150.172constant mass relationship methanol : nitroethane : 1,2-ethanediol = 13.0 : 60.0 : 27.0
31.2304.4 8.137.216.70.1720.3370.183constant mass relationship methanol : nitroethane : 1,2-ethanediol = 13.0 : 60.0 : 27.0
31.4304.6 9.945.620.50.2020.3960.216constant mass relationship methanol : nitroethane : 1,2-ethanediol = 13.0 : 60.0 : 27.0
32.2305.4 8.740.218.10.1820.3590.196constant mass relationship methanol : nitroethane : 1,2-ethanediol = 13.0 : 60.0 : 27.0
32.4305.6 9.443.219.40.1940.3800.206constant mass relationship methanol : nitroethane : 1,2-ethanediol = 13.0 : 60.0 : 27.0
31.0304.210.647.921.50.2130.4110.223constant mass relationship methanol : nitroethane : 1,2-ethanediol = 13.2 : 59.9 : 26.9
31.9305.1 8.337.416.80.1760.3380.184constant mass relationship methanol : nitroethane : 1,2-ethanediol = 13.2 : 59.9 : 26.9
32.4305.610.447.021.10.2100.4050.220constant mass relationship methanol : nitroethane : 1,2-ethanediol = 13.2 : 59.9 : 26.9
33.2306.4 8.940.118.00.1860.3580.194constant mass relationship methanol : nitroethane : 1,2-ethanediol = 13.2 : 59.9 : 26.9
33.8307.0 9.944.920.20.2020.3910.213constant mass relationship methanol : nitroethane : 1,2-ethanediol = 13.2 : 59.9 : 26.9
33.8307.0 9.241.618.70.1910.3680.200constant mass relationship methanol : nitroethane : 1,2-ethanediol = 13.2 : 59.9 : 26.9
34.0307.2 9.442.519.10.1940.3750.204constant mass relationship methanol : nitroethane : 1,2-ethanediol = 13.2 : 59.9 : 26.9
Method/Apparatus/Procedure:
   The synthetic method was used. The solutions were placed in closed glass ampoules. The temperature at which the second meniscus appeared was estimated visually. No experimental details given.

Source and Purity of Materials:
   (1) Not specified.
   (2) Not specified.
   (3) Not specified. (4) not specified.

Estimated Errors:

   Temperature: ±0.1 K.