SDS Volume (3698)

Volume 69. Ternary Alcohol-Hydrocarbon-Water Systems, p None

Original Measurements

Timofeev, V. S.; Aristovich, V. Yu.; Sabylin, I. I.; Koshel'kov, V. A.; Pavlenko, T. G.; Serafimov, L. A.; Izv. Vyssh, Uchebn. Zaved.; Khim. Khim. Tekhnol. 18, 1219 (1975).

Variables:

Room Temp: 348.7 - 349.5 $\pu{K}$

Prepared by:

A. Skrzecz

Method/Apparatus/Procedure:

The method is described in [1]. Data are reported at the boiling point at 101.3 kPa together with liquid-liquid-vapor equilibrium data for the system.

Source and Purity of Materials:
  1. Source not specified.
  2. Source not specified.
  3. Source not specified.
Estimated Errors:

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

References

1 Koshelkov, V. A.; Pavlenko, T. G.; Timofeev, V. S.; Serafimov, L. A.; Uch. Zap. Mosk. Inst. Tonkoi Khim. Tekhnol. 1, 44 (1971).

Components:
  1. 1-Propanol, $\ce{ C3H8O }$; [71-23-8] NIST WebBook
  2. Heptane, $\ce{ C7H16 }$; [142-82-5] NIST WebBook
  3. Water, $\ce{ H2O }$; [7732-18-5] NIST WebBook
Experimental Data
Compositions of coexisting phases
$T$ (°C) $T$ ($\pu{K}$) $x_{1}$ $x_{2}$ w1 w2
76.3349.5 0.1010.888 0.06370.9342
76.3349.5 0.1530.036 0.33540.1316
76.1349.3 0.1180.865 0.07540.9214
76.1349.3 0.1690.059 0.33880.1972
75.9349.1 0.1510.823 0.09860.8963
75.9349.1 0.1920.056 0.37590.1828
75.5348.7 0.1730.798 0.11440.8799
75.5348.7 0.2230.062 0.41240.1912
76.2349.4 0.4300.330 0.40870.5230
76.2349.4 0.4300.330 0.40870.5230

(a) Critical solubility point.

Download Data   link to XML output link to JSON output link to JSON-LD output