SDS Volume (3697)

Volume 69. Ternary Alcohol-Hydrocarbon-Water Systems, p 1117

Original Measurements

Rabinovich, I. B.; Pugachevich, P. P.; Zh. Fiz. Khim. 48, 2525 (1974).

Variables:

Temperature: 293 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.
References

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

Experimental Data

1-Propanol with Heptane and Water

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 Values:
Compositions of coexisting phases
T (°C)T (K)x1x2w1w2
20.0 293.15 1.7 x 10-1 8.2 x 10-1 1.10 x 10-1 8.88 x 10-1
20.0 293.15 2.3 x 10-1 7.3 x 10-1 1.58 x 10-1 8.34 x 10-1
20.0 293.15 2.7 x 10-1 6.8 x 10-1 1.90 x 10-1 7.99 x 10-1
20.0 293.15 3.3 x 10-1 6.2 x 10-1 2.39 x 10-1 7.50 x 10-1
20.0 293.15 3.9 x 10-1 5.5 x 10-1 2.94 x 10-1 6.92 x 10-1
20.0 293.15 1.4 x 10-1 1 x 10-3 3.51 x 10-1 4 x 10-3
20.0 293.15 2.7 x 10-1 2 x 10-2 5.23 x 10-1 6.5 x 10-2
20.0 293.15 3.3 x 10-1 4 x 10-2 5.64 x 10-1 1.14 x 10-1
20.0 293.15 4.0 x 10-1 7 x 10-2 5.92 x 10-1 1.73 x 10-1
20.0 293.15 4.4 x 10-1 1.1 x 10-1 5.80 x 10-1 2.42 x 10-1

The authors described both branches of the solubility curve by the following equations obtained by the least-squares method.

x'1=0.6788-0.1927x'3-49.0x'23

x"1=0.0896+8.335x"3-3689.0x"23

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