SDS Volume (4884)

Volume 77. Nitroalkanes with Water or Organic Solvents: Binary and Multicomponent Systems, p None

Original Measurements

Kozlov, L. M.; Volpert, V. I.; Tr.; Kazan, Khim. -Tekhnol. Inst. 40, 240-5 (1969).

Variables:

Room Temp: 252 - 332 $\pu{K}$

Prepared by:

N.I. Lisov, V.P. Sazonov

Method/Apparatus/Procedure:

The synthetic method was used. No experimental details given.

Source and Purity of Materials:
  1. Not specified.
  2. Not specified.
  3. Narrow fraction of liquid paraffin separated in the interval of (195 to 270)°C is treated by urea; MP = 9°C.
Estimated Errors:

Ambient temperature: Not specified.
Mass concentration (m/v) (1): Not specified.

Components:
  1. Nitroethane, $\ce{ C2H5NO2 }$; [79-24-3] NIST WebBook
  2. Toluene, $\ce{ C7H8 }$; [108-88-3] NIST WebBook
  3. Paraffins, [8002-74-2] NIST WebBook
Experimental Data

The temperatures of phase transitions were determined in ternary mixtures with a constant mass relationship of (1) and (2) as 5.0:95.0, 10.0:90.0, 30.0:70.0, 50.0:50.0, 70.0:30.0, 80.0:20.0, 90.0:10.0 and 95.0:5.0 respectively (see Tables 1 and 2).

Table 1. Solubility temperatures of the solid phase
$T$ (°C) $T$ ($\pu{K}$) 100w1 100w2
-21.5251.7 4.9594.07
-18.0255.2 4.7090.24
-16.0257.2 4.2285.84
-12.0261.2 3.8571.15
-9.5263.7 2.9751.86
-2.8270.4 2.5431.72
-1.0272.2 1.5627.99
1.5274.7 1.1118.83
5.0278.2 0.439.67
8.0281.2 0.071.82
-20.8252.4 9.9389.28
-18.0255.2 9.4188.17
-12.0261.2 7.9472.00
-10.0263.2 6.9763.06
-6.5266.7 4.5040.30
-2.0271.2 3.5331.34
2.0275.2 2.2617.68
5.0278.2 1.508.37
7.2280.4 0.924.13
8.0281.2 0.101.39
-20.2253.0 30.2369.17
-17.0256.2 29.0067.95
-14.3258.9 27.0063.98
-10.0263.2 25.1657.84
-6.5266.7 19.9253.23
-4.0269.2 17.9844.94
-0.5272.7 14.0631.88
2.0275.2 10.0421.36
3.3276.5 5.0211.86
8.0281.2 0.541.56
-15.5257.7 47.5051.85
-9.0264.2 47.8247.66
-3.5269.7 41.0543.45
-0.7272.5 34.9037.16
1.0274.2 26.9926.90
1.0274.2 25.1027.60
1.8275.0 20.1019.92
4.8278.0 9.008.85
7.0280.2 2.562.40
8.0281.2 0.921.09
-7.5265.7 70.4228.68
2.5275.7 60.027.91
2.5275.7 44.8520.25
3.5276.7 39.9817.60
4.5277.7 25.2010.82
5.3278.5 20.059.83
6.8280.0 13.955.97
7.5280.7 9.933.84
8.0281.2 2.701.29
8.0281.2 1.680.72
-0.5272.7 79.5019.61
4.5277.7 75.1319.74
4.5277.7 70.1016.94
4.8278.0 65.5815.37
5.0278.2 50.012.92
6.0279.2 19.955.05
7.5280.7 15.094.91
8.0281.2 9.853.08
8.3281.5 6.091.92
8.3281.5 2.460.54
3.0276.2 90.078.27
5.0278.2 84.929.95
6.0279.2 76.1015.25
6.0279.2 74.8010.10
7.3280.5 18.461.51
8.2281.4 14.921.38
8.2281.4 11.041.27
8.2281.4 9.050.90
8.2281.4 6.001.05
8.5281.7 1.800.26
4.0277.7 94.984.35
8.0281.2 90.464.48
8.0281.2 84.936.12
8.0281.2 79.985.07
8.2281.4 14.991.05
8.2281.4 9.951.07
8.2281.4 6.500.44
8.5281.7 2.530.47
8.5281.7 1.280.46
8.8282.0 0.240.20

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