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IUPAC-NIST Solubility Database
NIST Standard Reference Database 106
Solubility System:
1-Propanol with heptane and Water
Components:
(1) Water; H2O; [7732-18-5]
NIST Chemistry WebBook
for detail
(2) 1-Proponal (n-propanol, propyl alcohol, n-propyl alcohol); C3H8O; [71-23-8]
NIST Chemistry WebBook
for detail
(3) Heptane (n-heptane); C7H16; [142-82-5]
NIST Chemistry WebBook
for detail
Original Measurements:
Rabinovich, I.B.; Pugachevich, P.P., Zh. Fiz. Khim. 48, 2525 (1974).
Variables:
Temperature = 293 K
Prepared By:
A. Skrzecz
Experimental Remarks:
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'
2
3
x"
1
=0.0896+8.335x"
3
-3689.0x"
2
3
Experimental Data:
(Notes on the Nomenclature)
Compositions of coexisting phases
t/°C
T/K
Mass Fraction w
1
(compiler)
Mass Fraction w
2
(compiler)
Mole Fraction x
1
Mole Fraction x
2
Comment(s)
20.0
293.15
0.110
0.888
0.17
0.82
hydrocarbon-rich phase
20.0
293.15
0.158
0.834
0.23
0.73
hydrocarbon-rich phase
20.0
293.15
0.190
0.799
0.27
0.68
hydrocarbon-rich phase
20.0
293.15
0.239
0.750
0.33
0.62
hydrocarbon-rich phase
20.0
293.15
0.294
0.692
0.39
0.55
hydrocarbon-rich phase
20.0
293.15
0.351
0.004
0.14
0.001
water-rich phase
20.0
293.15
0.523
0.065
0.27
0.02
water-rich phase
20.0
293.15
0.564
0.114
0.33
0.04
water-rich phase
20.0
293.15
0.592
0.173
0.40
0.07
water-rich phase
20.0
293.15
0.580
0.242
0.44
0.11
water-rich phase
Method/Apparatus/Procedure:
The method is described in Ref. 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:
Solubility: Not reported.
Temperature: Not reported.
References:
1
V. A. Koshelkov, T. G. Pavlenko, V. S. Timofeev, and L. A. Serafimov, Uch. Zap. Mosk. Inst. Tonkoi Khim. Tekhnol. 1, 44 (1971).