SDS Volume (4902)

Volume 77. Nitroalkanes with Water or Organic Solvents: Binary and Multicomponent Systems, p 107

Original Measurements

Hankinson, R. W.; Thompson, D.; J. Chem. Eng. Data 10, 18-9 (1965).

Variables:

Temperature: 298 and 303 $\pu{K}$

Prepared by:

M.F. Chernysheva, V.P. Sazonov

Method/Apparatus/Procedure:

Two methods were used. The solubility data were determined by a modification of the 'cloud point' method described in Othmer, et al. [1]. 20 mL mixtures of (2) and (3) were placed in flasks, sealed and immersed in a constant temperature bath for approximately four hours. Each container in turn was opened, and the contents titrated from calibrated burettes with of (1). The (1)-rich portion of the solubility curve was obtained by reversing the procedure. The vessel containing the titrated mixture was continually agitated in a constant temperature bath. The equilibrium data were determined by the synthetic method described in Othmer, et al. [1]. Solutions consisting of all three components were made. These two-phase mixtures were then sealed in polyethylene containers and placed in the constant temperature bath. Each container was removed from the constant temperature bath, then the two phases were separated, and the refractive index of each phase was determined.

Source and Purity of Materials:
  1. Commercial Solvents Corp.; 99 mass% purity.
  2. Source not specified; purity not specified; distilled with a boiling range of ±0.1 K.
  3. Twice distilled.
Estimated Errors:

Ambient temperature: control: ±0.01 K

References

1 Othmer, D. F.; White, R. E.; Trueger, E.; Ind. Eng. Chem. 1941, 33(10), 1240-8.

Components:
  1. 1-Nitropropane, $\ce{ C3H7NO2 }$; [108-03-2] NIST WebBook
  2. Methanol, $\ce{ CH4O }$; [67-56-1] NIST WebBook
  3. Water, $\ce{ H2O }$; [7732-18-5] NIST WebBook
Experimental Data

None

$T$ (°C) $T$ ($\pu{K}$) 100w1 100w2 $x_{1}$ $x_{2}$
25.00298.15 2.113.3 5 x 10-30.081
25.00298.15 2.723.3 6 x 10-30.150
25.00298.15 3.131.1 7 x 10-30.209
25.00298.15 5.236.7 0.0130.259
25.00298.15 7.340.9 0.0190.302
25.00298.15 9.244.1 0.0250.339
25.00298.15 12.046.1 0.0350.370
25.00298.15 13.848.1 0.0410.399
25.00298.15 28.845.7 0.1020.452
25.00298.15 34.243.5 0.1290.457
25.00298.15 41.839.9 0.1730.458
25.00298.15 52.933.6 0.2490.439
25.00298.15 61.627.9 0.3230.407
25.00298.15 71.722.7 0.4430.390
25.00298.15 83.413.2 0.6110.269
30.00303.15 2.413.3 5 x 10-30.081
30.00303.15 3.223.2 7 x 10-30.150
30.00303.15 4.127.2 0.0100.181
30.00303.15 4.530.7 0.0110.208
30.00303.15 6.436.3 0.0160.259
30.00303.15 8.640.3 0.0230.301
30.00303.15 10.843.4 0.0300.338
30.00303.15 13.845.4 0.0400.369
30.00303.15 16.045.6 0.0480.382
30.00303.15 19.146.4 0.0600.405
30.00303.15 22.846.3 0.0750.424
30.00303.15 27.345.3 0.0950.438
30.00303.15 21.751.8 0.0730.486
30.00303.15 28.345.1 0.1000.441
30.00303.15 41.039.2 0.1660.441
30.00303.15 52.333.3 0.2430.430
30.00303.15 61.327.9 0.3200.404
30.00303.15 70.022.3 0.4140.367
30.00303.15 82.913.2 0.5990.265
1-Nitropropane-rich phase
$T$ (°C) $T$ ($\pu{K}$) 100w1 100w2 $x_{1}$ $x_{2}$
25.00298.15 93.94.7 0.8240.115
25.00298.15 86.910.2 0.6710.219
25.00298.15 75.219.5 0.4840.348
25.00298.15 65.226.1 0.3610.401
25.00298.15 54.232.9 0.2590.437
25.00298.15 48.135.9 0.2110.439
Water-rich phase
$T$ (°C) $T$ ($\pu{K}$) 100w1 100w2 $x_{1}$ $x_{2}$
25.00298.15 3.019.9 7 x 10-30.126
25.00298.15 3.222.9 7 x 10-30.147
25.00298.15 3.628.4 8 x 10-30.189
25.00298.15 4.532.3 0.0110.221
25.00298.15 6.137.9 0.0160.271
25.00298.15 8.442.3 0.0230.318

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