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IUPAC-NIST Solubility Database
NIST Standard Reference Database 106
Solubility System:
2-Propanol with Toluene and Water
Components:
(1) Water; H2O; [7732-18-5]
NIST Chemistry WebBook
for detail
(2) 2-Propanol (isopropanol, isopropyl alcohol); C3H8O; [67-63-0]
NIST Chemistry WebBook
for detail
(3) Toluene (methylbenzene); C7H8; [108-88-3]
NIST Chemistry WebBook
for detail
Original Measurements:
Washburn, E.R.; Beguin, A.E., J. Am. Chem. Soc. 62, 579 (1940).
Variables:
Temperature = 298 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)
25.0
298.15
0.0425
0.0013
0.0131
0.0003
25.0
298.15
0.1076
0.0018
0.0349
0.0004
25.0
298.15
0.1650
0.0030
0.0561
0.0007
25.0
298.15
0.2340
0.0038
0.0842
0.0009
25.0
298.15
0.3016
0.0107
0.1159
0.0027
25.0
298.15
0.3438
0.0188
0.1385
0.0049
25.0
298.15
0.3944
0.0422
0.1714
0.0120
25.0
298.15
0.4364
0.0675
0.2044
0.0206
25.0
298.15
0.4753
0.1074
0.2453
0.0362
25.0
298.15
0.4957
0.1413
0.2756
0.0512
25.0
298.15
0.5101
0.1827
0.3084
0.0720
25.0
298.15
0.5117
0.2255
0.3333
0.0958
25.0
298.15
0.5089
0.2773
0.3627
0.1289
25.0
298.15
0.4961
0.3350
0.3882
0.1710
25.0
298.15
0.4814
0.3736
0.3983
0.2016
25.0
298.15
0.4559
0.4270
0.4052
0.2475
25.0
298.15
0.4255
0.4709
0.3946
0.2848
25.0
298.15
0.3905
0.5263
0.3861
0.3394
25.0
298.15
0.3430
0.5928
0.3634
0.4097
25.0
298.15
0.2745
0.6872
0.3228
0.5270
25.0
298.15
0.2176
0.7550
0.2715
0.6144
25.0
298.15
0.1597
0.8243
0.2127
0.7162
25.0
298.15
0.1064
0.8848
0.1493
0.8096
25.0
298.15
0.0431
0.9530
0.0636
0.9172
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)
25.00
298.15
0.0089
0.9911
0.0136
0.9864
hydrocarbon-rich phase
25.00
298.15
0.0227
0.9764
0.0343
0.9612
hydrocarbon-rich phase
25.00
298.15
0.0745
0.9184
0.1069
0.8592
hydrocarbon-rich phase
25.00
298.15
0.1434
0.8430
0.1942
0.7444
hydrocarbon-rich phase
25.00
298.15
0.2490
0.7190
0.3019
0.5686
hydrocarbon-rich phase
25.00
298.15
0.3062
0.6435
0.3426
0.4696
hydrocarbon-rich phase
25.00
298.15
0.3790
0.5420
0.3805
0.3549
hydrocarbon-rich phase
25.00
298.15
0.4423
0.4435
0.3976
0.2600
hydrocarbon-rich phase
25.00
298.15
0.4857
0.3635
0.3962
0.1934
hydrocarbon-rich phase
25.00
298.15
0.4995
0.3260
0.3859
0.1643
hydrocarbon-rich phase
25.00
298.15
0.5100
0.2716
0.3602
0.1251
hydrocarbon-rich phase
25.00
298.15
0.5105
0.2640
0.3558
0.1200
hydrocarbon-rich phase
25.00
298.15
0.5120
0.2356
0.3396
0.1019
hydrocarbon-rich phase
25.00
298.15
0.0687
0.0001
0.0216
0.0000
water-rich phase
25.00
298.15
0.1216
0.0030
0.0400
0.0006
water-rich phase
25.00
298.15
0.1977
0.0028
0.0690
0.0006
water-rich phase
25.00
298.15
0.2414
0.0052
0.0875
0.0012
water-rich phase
25.00
298.15
0.2900
0.0102
0.1102
0.0025
water-rich phase
25.00
298.15
0.3140
0.0125
0.1222
0.0032
water-rich phase
25.00
298.15
0.3434
0.0146
0.1377
0.0038
water-rich phase
25.00
298.15
0.3740
0.0296
0.1570
0.0081
water-rich phase
25.00
298.15
0.3992
0.0433
0.1745
0.0123
water-rich phase
25.00
298.15
0.4210
0.0558
0.1911
0.0165
water-rich phase
25.00
298.15
0.4413
0.0709
0.2087
0.0219
water-rich phase
25.00
298.15
0.4473
0.0847
0.2167
0.0268
water-rich phase
25.00
298.15
0.4650
0.0950
0.2331
0.0311
water-rich phase
Method/Apparatus/Procedure:
The titration method, as described in Ref. 1, 2, was used. Refractive indexes of mixtures were measured by Abbe refractometer. Binary mixtures of known composition placed in small Erlenmeyer flasks were titrated with water or toluene from weighed pipettes and shaken mechanically in a constant temperature bath. Measured refractive indexes of saturated solutions were plotted for each component. These plots were used further to determine concentration of equilibrium phases. Tie lines were obtained by adding alcohol to water-toluene mixtures and shaking the samples from time to time during the twenty-four hours while they were kept in constant temperature bath. After separation, refractive indexes of both phase were measured and concentration of each component was read from the plots. The sum of calculated phase concentrations was always equal to 1.0000±0.0001.
Source and Purity of Materials:
(1) Eastman Kodak Company; refluxed with CaO, distilled, middle fraction was used; b.p.=81.7-81.9°C, d(25°C,4°C)=0.780 87, n(25°C,D)=1.3748.
(2) Eastman Kodak Company; used as received; n(25°C,D)=1.4938.
(3) Distilled over KMnO
4
.
Estimated Errors:
Solubility: Not reported.
Temperature: Temp. ±0.01°C.
References:
1
R. Vold and E. R. Washburn, J. Am. Chem. Soc. 54, 4217 (1932).
2
E. R. Washburn and H. C. Spencer, J. Am. Chem. Soc. 56, 361 (1934).