SDS Volume (4877)

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

Original Measurements

Erofeeva, L. F.; Zhuravlev, E. F.; Uch. Zap.; Perm. Gos. Univ. 178, 18-22 (1968).

Variables:

Room Temp: 291 - 455 $\pu{K}$

Prepared by:

N.I. Lisov, N.V. Sazonov, V.P. Sazonov

Method/Apparatus/Procedure:

Two methods were used. The solubility temperatures are determined by the synthetic method. The analytical method was used for determining of equilibrium liquid phase composition. Samples from coexisting liquid phases at equilibrium were analyzed by refractometry. No experimental details given.

Source and Purity of Materials:
  1. Source not specified; pure grade reagent; dried over $\ce{CaCl2}$ and distilled.
  2. Source not specified; pure grade reagent.
  3. Source not specified; pure grade reagent.
Estimated Errors:

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

Components:
  1. Nitroethane, $\ce{ C2H5NO2 }$; [79-24-3] NIST WebBook
  2. 1,2,3-Propanetriol, $\ce{ C3H8O3 }$; [56-81-5] NIST WebBook
  3. 1-Dodecanol, $\ce{ C12H26O }$; [112-53-8] NIST WebBook
Experimental Data

The solubility temperatures of liquid phases were determined in ternary mixtures with a constant mass content of (2), respectively 20.0, 50.0 and 70.0 mass % and in ternary mixtures with constant mass relationship of (1) and (3) as 10.0:90.0, 20.0:80.0, 30.0:70.0, 50.0:50.0, 80.0:20.0 and 90.0:10.0 respectively (see Tables 1 and 2).

Table 1. Solubility temperatures of two liquid phases
$T$ (°C) $T$ ($\pu{K}$) 100w1 100w2 $x_{1}$ $x_{2}$
19.2292.4 9.653.50 0.20320.0601
38.0311.2 9.623.80 0.20210.0651
49.0322.2 0.1198.90 1.4 x 10-30.9937
76.0349.2 0.2098.00 2.5 x 10-30.9886
79.8353.0 9.514.90 0.19820.0832
102.0375.2 9.425.80 0.19500.0979
114.0387.2 0.2997.10 3.6 x 10-30.9833
124.0397.2 9.366.40 0.19290.1075
146.0419.2 0.3396.70 4.1 x 10-30.9810
148.0421.2 9.188.20 0.18680.1360
18.0291.2 19.741.30 0.37520.0201
18.0291.2 19.522.40 0.36880.0370
18.4291.6 19.840.80 0.37820.0124
43.0316.2 19.403.00 0.36530.0460
54.0327.2 0.3898.10 4.7 x 10-30.9877
76.0349.2 19.124.40 0.35730.0670
87.0360.2 0.4897.60 5.9 x 10-30.9845
94.0367.2 19.005.00 0.35390.0759
112.0385.2 0.6097.00 7.4 x 10-30.9806
114.0387.2 18.825.90 0.34880.0891
133.0406.2 18.487.60 0.33940.1138
165.0438.2 18.248.80 0.33280.1309
182.0455.2 18.0010.0 0.32630.1478
25.2298.4 29.671.10 0.50750.0153
51.0324.2 29.103.00 0.49400.0415
52.0325.2 0.6098.00 7.4 x 10-30.9856
81.0354.2 0.7597.50 9.3 x 10-30.9820
82.0355.2 28.774.10 0.48630.0565
97.0370.2 28.534.90 0.48080.0673
103.5376.7 0.9097.00 0.01110.9784
110.5383.7 28.325.60 0.47590.0767
134.0407.2 27.877.10 0.46560.0967
157.0430.2 27.338.90 0.45340.1204
28.8302.0 49.550.90 0.70540.0104
40.0313.2 48.652.70 0.69050.0312
76.0349.2 1.2597.50 0.01540.9784
82.0355.2 47.704.60 0.67500.0531
105.0378.2 2.0096.00 0.02470.9654
106.0379.2 47.006.00 0.66360.0691
23.0296.2 79.680.40 0.90513.7 x 10-3
44.0317.2 79.201.00 0.90019.3 x 10-3
63.0336.2 78.821.60 0.89500.0148
81.0354.2 3.2096.00 0.03910.9569
89.0362.2 77.682.90 0.88410.0269
89.0362.2 76.883.90 0.87560.0362
114.0387.2 4.0095.00 0.04890.9462
48.0321.2 89.280.80 0.95056.9 x 10-3
68.0341.2 88.381.80 0.94220.0156
68.0341.2 3.4296.20 0.04170.9564
84.0357.2 4.0595.50 0.04930.9484
89.0362.2 87.213.10 0.93130.0270
108.0381.2 5.4094.00 0.06560.9314
120.0393.2 84.426.20 0.90530.0542

(*) The compilers extracted these data from the published graphs.

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