SDS Volume (5149)

Volume 78. Acetonitrile Binary Systems, p None

Original Measurements

Schneider, G.; Z. Phys. Chem. 41, 327 (1964).

Variables:

Room Temp: 228 - 272 $\pu{K}$
Pressure: 0.1 - 157 $\pu{MPa}$

Prepared by:

V.P. Sazonov

Method/Apparatus/Procedure:

The synthetic method was used as reported elsewhere [1].

Source and Purity of Materials:
  1. Fluka AG; pure grade; twice distilled; purity better than 99.8 mole%; MP = -43.9°C.
  2. Twice distilled.
Estimated Errors:

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

References

1 Schneider, G.; Z. Phys. Chem. 37, 333 (1963).

Components:
  1. Acetonitrile, $\ce{ C2H3N }$; [75-05-8] NIST WebBook
  2. Water, $\ce{ H2O }$; [7732-18-5] NIST WebBook
Experimental Data

Monotectic equilibrium occurs at -10.0°C (263.2 K, compiler).A eutectic was reported at -45.6°C (227.6 K, compiler). Four-phase (two liquid and two solid) equilibrium is realized at -24.2°C (249.0 K, compiler) and 125.2 MPa.Region of immiscibility disappears at -19.0°C (254.2 K, compiler) and 156.6 MPa.

Table 2. Solubility temperatures of mixtures of the (1) and (2) depending on pressure
$T$ (°C) $T$ ($\pu{K}$) $P$ ($\pu{MPa}$) 100w1 $x_{1}$
-14.5258.739.6 34.8 0.192
-18.6254.673.2 34.8 0.192
-19.8253.484.3 34.8 0.192
-20.7252.594.9 34.8 0.192
-9.1264.129.7 40.0 0.229
-13.6259.659.6 40.0 0.229
-17.3255.988.9 40.0 0.229
-20.0252.2119.2 40.0 0.229
-3.9269.319.8 57.8 0.379
-4.7268.524.8 57.8 0.379
-5.9267.334.3 57.8 0.379
-7.9265.349.5 57.8 0.379
-9.7263.562.6 57.8 0.379
-9.7263.564.6 57.8 0.379
-11.7261.579.8 57.8 0.379
-13.0260.290.9 57.8 0.379
-13.4259.894.9 57.8 0.379
-17.5255.7140.4 57.8 0.379
-7.7265.519.8 74.9 0.571
-9.8263.439.4 74.9 0.571
-12.8260.459.6 74.9 0.571
-14.9258.378.8 74.9 0.571
-16.8256.499.0 74.9 0.571
-18.5254.7119.2 74.9 0.571
-20.2252.0138.4 74.9 0.571

(a) Solid-liquid equilibrium.

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