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IUPAC-NIST Solubility Database
NIST Standard Reference Database 106
Solubility System:
1-Butanol with Toluene and Water
Components:
(1) Water; H2O; [7732-18-5]
NIST Chemistry WebBook
for detail
(2) 1-Butanol (n-butanol, butyl alcohol, n-butyl alcohol); C4H10O; [71-36-3]
NIST Chemistry WebBook
for detail
(3) Toluene (methylbenzene); C7H8; [108-88-3]
NIST Chemistry WebBook
for detail
Original Measurements:
Fuoss, R.M., J. Am. Chem. Soc. 65, 78 (1943).
Variables:
Temperature = 303 K
Prepared By:
A. Skrzecz
Experimental Data:
(Notes on the Nomenclature)
Compositions along the saturation curve
t/°C
T/K
Mass Fraction w
1
Mass Fraction w
2
Mole Fraction x
1
(compiler)
Mole Fraction x
2
(compiler)
30.0
303.15
0.1966
0.7918
0.2231
0.7228
30.0
303.15
0.1995
0.7886
0.2260
0.7186
30.0
303.15
0.3833
0.5835
0.3874
0.4745
30.0
303.15
0.5101
0.4349
0.4696
0.3221
30.0
303.15
0.6072
0.3142
0.5131
0.2136
30.0
303.15
0.6771
0.2199
0.5299
0.1384
30.0
303.15
0.7371
0.1277
0.5280
0.0736
30.0
303.15
0.7724
0.0632
0.5151
0.0339
30.0
303.15
0.7938
0.0000
0.4834
0.0000
30.0
303.15
0.0732
0.9241
0.0884
0.8981
30.0
303.15
0.1977
0.7908
0.2244
0.7219
30.0
303.15
0.3865
0.5797
0.3897
0.4701
30.0
303.15
0.5603
0.3746
0.4961
0.2668
30.0
303.15
0.6711
0.2279
0.5284
0.1444
30.0
303.15
0.7614
0.0846
0.5204
0.0465
30.0
303.15
0.7938
0.0000
0.4834
0.0000
30.0
303.15
0.0732
0.9241
0.0884
0.8981
30.0
303.15
0.1494
0.8433
0.1742
0.7908
30.0
303.15
0.1976
0.7904
0.2238
0.7202
30.0
303.15
0.2745
0.7091
0.3008
0.6252
30.0
303.15
0.3385
0.6345
0.3526
0.5317
30.0
303.15
0.4800
0.4709
0.4525
0.3571
30.0
303.15
0.5607
0.3730
0.4946
0.2647
30.0
303.15
0.6175
0.3009
0.5166
0.2025
30.0
303.15
0.6753
0.2227
0.5300
0.1406
30.0
303.15
0.7061
0.1779
0.5323
0.1079
30.0
303.15
0.7473
0.1104
0.5257
0.0625
30.0
303.15
0.7788
0.0412
0.5016
0.0213
30.0
303.15
0.7938
0.0000
0.4834
0.0000
Compositions of coexisting phases
t/°C
T/K
Mass Fraction w
1
Mass Fraction w
2
Mole Fraction x
1
(compiler)
Mole Fraction x
2
(compiler)
Comment(s)
30.0
303.15
0.010
0.990
0.012
0.988
organic-rich phase
30.0
303.15
0.020
0.980
0.025
0.975
organic-rich phase
30.0
303.15
0.030
0.970
0.037
0.963
organic-rich phase
30.0
303.15
0.040
0.959
0.049
0.946
organic-rich phase
30.0
303.15
0.050
0.948
0.061
0.929
organic-rich phase
30.0
303.15
0.100
0.896
0.119
0.861
organic-rich phase
30.0
303.15
0.200
0.788
0.226
0.718
organic-rich phase
30.0
303.15
0.300
0.677
0.319
0.580
organic-rich phase
30.0
303.15
0.400
0.565
0.401
0.455
organic-rich phase
30.0
303.15
0.500
0.446
0.463
0.332
organic-rich phase
30.0
303.15
0.600
0.322
0.509
0.220
organic-rich phase
30.0
303.15
0.700
0.186
0.531
0.114
organic-rich phase
30.0
303.15
0.750
0.101
0.519
0.056
organic-rich phase
30.0
303.15
0.794
0.000
0.484
0.000
organic-rich phase
30.0
303.15
0.0085
0.0000
0.0021
0.0000
water-rich phase
30.0
303.15
0.0155
0.0000
0.0038
0.0000
water-rich phase
30.0
303.15
0.0200
0.0000
0.0049
0.0000
water-rich phase
30.0
303.15
0.0235
0.0000
0.0058
0.0000
water-rich phase
30.0
303.15
0.0255
0.0000
0.0063
0.0000
water-rich phase
30.0
303.15
0.0320
0.0000
0.0080
0.0000
water-rich phase
30.0
303.15
0.0375
0.0000
0.0094
0.0000
water-rich phase
30.0
303.15
0.0415
0.0000
0.0104
0.0000
water-rich phase
30.0
303.15
0.0455
0.0000
0.0115
0.0000
water-rich phase
30.0
303.15
0.0500
0.0000
0.0126
0.0000
water-rich phase
30.0
303.15
0.0540
0.0000
0.0137
0.0000
water-rich phase
30.0
303.15
0.0585
0.0000
0.0149
0.0000
water-rich phase
30.0
303.15
0.0635
0.0000
0.0162
0.0000
water-rich phase
30.0
303.15
0.0710
0.0000
0.0182
0.0000
water-rich phase
Method/Apparatus/Procedure:
The conductance method (set A) was used to obtain compositions along the saturation curve. Weighed mixtures of about 150 g of toluene and butanol in glass-stoppered Erlenmeyer flasks were placed in a thermostat and portions of water, containing a trace (<0.5%) of HCI, were added. As long as water dissolves in the organic phase, its conductance increases. With the appearance of an aqueous phase the conductance of the organic phase drops on further addition of water, because the aqueous phase extracts HCI from the organic phase. Set B and set C present the compositions of the saturated organic phase used for refractive index (on an Abbe refractometer) and density (in 25 mL pyknometer) measurements. The refractive index and density of binary butanol-water mixtures were measured in similar way. Solubility of toluene in the butanol-water mixture was estimated to be about 0.03% and its effect on density and refractive index of aqueous phase was assumed to be negligible. Large scale plots of composition functions for refractive index and density were used to determine the compositions of phases in equilibrium. To determine equilibrium, the mixture of three components were shaken together and after separation samples of both phases were taken for density and refractive index measurements.
Source and Purity of Materials:
(1) Source not specified, c.p. products; distilled; densities and refractive indexes were in agreement with "International Critical Tables".
(2) Source not specified, c.p. products; distilled; densities and refractive indexes were in agreement with "International Critical Tables".
(3) Not specified.
Estimated Errors:
Solubility: Not reported.
Temperature: Not reported.