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IUPAC-NIST Solubility Database
NIST Standard Reference Database 106
Solubility System:
1-Proponal with Nonane (n-nonane) 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) Nonane (n-nonane); C9H20; [111-84-2]
NIST Chemistry WebBook
for detail
Original Measurements:
Koshelkov, V.A.; Pavlenko, T.G.; Titova, V.N.; Timofeev, V.S.; Serafimov, L.A., Tr. Altai. Politekh. Inst. Im, I. I. Polzunova 41, 84 (1974).
Variables:
Temperature = 359 K - 363 K
Prepared By:
A. Skrzecz
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)
90.0
363.2
0.019
0.979
0.040
0.951
hydrocarbon-rich phase
90.0
363.2
0.261
0.050
0.101
0.009
water-rich phase
87.0
360.2
0.045
0.953
0.091
0.897
hydrocarbon-rich phase
87.0
360.2
0.378
0.085
0.171
0.018
water-rich phase
86.0
359.2
0.067
0.930
0.131
0.851
hydrocarbon-rich phase
86.0
359.2
0.478
0.088
0.243
0.021
water-rich phase
85.5
358.7
0.096
0.900
0.182
0.797
hydrocarbon-rich phase
85.5
358.7
0.540
0.136
0.321
0.038
water-rich phase
86.0
359.2
0.284
0.704
0.435
0.505
hydrocarbon-rich phase
86.0
359.2
0.662
0.151
0.488
0.052
water-rich phase
88.0
361.2
0.326
0.659
0.475
0.450
hydrocarbon-rich phase
88.0
361.2
0.626
0.251
0.543
0.102
water-rich phase
Method/Apparatus/Procedure:
The method was not specified. Experiments were made at boiling temperatures of mixtures. Temperatures were read and estimated by the compiler from the authors' graphs.
Source and Purity of Materials:
(1) Source not specified.
(2) Source not specified.
(3) Source not specified.
Estimated Errors:
Solubility: Not reported.
Temperature: Temp. ± 0.5K (compiler).