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IUPAC-NIST Solubility Database
NIST Standard Reference Database 106
Solubility System:
Ethanol with Toluene and Water
Components:
(1) Water; H2O; [7732-18-5]
NIST Chemistry WebBook
for detail
(2) Ethanol (ethyl alcohol); C2H6O; [64-17-5]
NIST Chemistry WebBook
for detail
(3) Methylbenzene (toluene); C7H8; [108-88-3]
NIST Chemistry WebBook
for detail
Original Measurements:
Ricna, K.; Matous, J.; Novak, J.P.; Kubicek, V., Collect. Czech. Chem. Commun. 54, 581 (1989).
Variables:
Temperature = 278 K
Prepared By:
A. Skrzecz
Experimental Data:
(Notes on the Nomenclature)
Compositions along the saturation curve
t/°C
T/K
Mass Fraction w
1
(compiler)
Mass Fraction w
2
(compiler)
Mole Fraction x
1
Mole Fraction x
2
5.0
278.15
0.8857
0.0732
0.8620
0.0356
5.0
278.15
0.7719
0.1281
0.7072
0.0587
5.0
278.15
0.6306
0.2302
0.5725
0.1045
5.0
278.15
0.3875
0.4261
0.3597
0.1978
5.0
278.15
0.2280
0.5711
0.2220
0.2780
5.0
278.15
0.0832
0.7443
0.0928
0.4151
5.0
278.15
0.0196
0.7814
0.0213
0.4251
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)
5.0
347.7
0.0000
0.9988
0.0000
0.9938
hydrocarbon-rich phase
5.0
347.7
0.0000
0.9957
0.0000
0.9783
hydrocarbon-rich phase
5.0
347.7
0.0000
0.9953
0.0000
0.9763
hydrocarbon-rich phase
5.0
347.7
0.0000
0.9887
0.0000
0.9447
hydrocarbon-rich phase
5.0
347.7
0.0000
0.9753
0.0000
0.8855
hydrocarbon-rich phase
5.0
347.7
0.0000
0.9588
0.0000
0.8197
hydrocarbon-rich phase
5.0
347.7
0.0039
0.9298
0.0061
0.7283
hydrocarbon-rich phase
5.0
347.7
0.0185
0.8763
0.0255
0.6037
hydrocarbon-rich phase
5.0
347.7
0.0276
0.8501
0.0361
0.5554
hydrocarbon-rich phase
5.0
347.7
0.0354
0.8274
0.0442
0.5171
hydrocarbon-rich phase
5.0
347.7
0.0550
0.7935
0.0655
0.4727
hydrocarbon-rich phase
5.0
347.7
0.0916
0.7267
0.0996
0.3951
hydrocarbon-rich phase
5.0
347.7
0.9971
0.0026
0.9980
0.0013
water-rich phase
5.0
347.7
0.9886
0.0104
0.9921
0.0052
water-rich phase
5.0
347.7
0.9887
0.0102
0.9919
0.0051
water-rich phase
5.0
347.7
0.9898
0.0072
0.9888
0.0036
water-rich phase
5.0
347.7
0.9818
0.0101
0.9744
0.0050
water-rich phase
5.0
347.7
0.9732
0.0108
0.9546
0.0053
water-rich phase
5.0
347.7
0.9351
0.0346
0.9080
0.0168
water-rich phase
5.0
347.7
0.8988
0.0496
0.8516
0.0235
water-rich phase
5.0
347.7
0.8786
0.0654
0.8331
0.0310
water-rich phase
5.0
347.7
0.8508
0.0879
0.8091
0.0418
water-rich phase
5.0
347.7
0.8478
0.0793
0.7895
0.0369
water-rich phase
5.0
347.7
0.8028
0.1106
0.7435
0.0512
water-rich phase
25.0
298.15
0.0000
0.9986
0.0000
0.9930
hydrocarbon-rich phase
25.0
298.15
0.0000
0.9949
0.0000
0.9745
hydrocarbon-rich phase
25.0
298.15
0.0000
0.9869
0.0000
0.9364
hydrocarbon-rich phase
25.0
298.15
0.0042
0.9532
0.0072
0.8082
hydrocarbon-rich phase
25.0
298.15
0.0119
0.9059
0.0176
0.6710
hydrocarbon-rich phase
25.0
298.15
0.0117
0.8994
0.0170
0.6530
hydrocarbon-rich phase
25.0
298.15
0.0219
0.8767
0.0305
0.6093
hydrocarbon-rich phase
25.0
298.15
0.0454
0.8222
0.0571
0.5171
hydrocarbon-rich phase
25.0
298.15
0.0806
0.7686
0.0947
0.4518
hydrocarbon-rich phase
25.0
298.15
0.1026
0.7399
0.1172
0.4227
hydrocarbon-rich phase
25.0
298.15
0.1136
0.7203
0.1265
0.4009
hydrocarbon-rich phase
25.0
298.15
0.9967
0.0028
0.9973
0.0014
water-rich phase
25.0
298.15
0.9941
0.0040
0.9932
0.0020
water-rich phase
25.0
298.15
0.9794
0.0144
0.9770
0.0072
water-rich phase
25.0
298.15
0.9245
0.0473
0.9062
0.0232
water-rich phase
25.0
298.15
0.8706
0.0702
0.8236
0.0332
water-rich phase
25.0
298.15
0.8817
0.0623
0.8349
0.0295
water-rich phase
25.0
298.15
0.8327
0.0975
0.7857
0.0460
water-rich phase
25.0
298.15
0.7892
0.1254
0.7374
0.0586
water-rich phase
25.0
298.15
0.6808
0.2065
0.6349
0.0963
water-rich phase
25.0
298.15
0.6670
0.2152
0.6200
0.1000
water-rich phase
25.0
298.15
0.6669
0.2149
0.6194
0.0998
water-rich phase
50.0
323.15
0.0000
0.9986
0.0000
0.9928
hydrocarbon-rich phase
50.0
323.15
0.0000
0.9982
0.0000
0.9908
hydrocarbon-rich phase
50.0
323.15
0.0000
0.9935
0.0000
0.9674
hydrocarbon-rich phase
50.0
323.15
0.000
0.9905
0.0000
0.9534
hydrocarbon-rich phase
50.0
323.15
0.0016
0.9877
0.0030
0.9447
hydrocarbon-rich phase
50.0
323.15
0.0027
0.9586
0.0047
0.8252
hydrocarbon-rich phase
50.0
323.15
0.0041
0.9491
0.0067
0.7929
hydrocarbon-rich phase
50.0
323.15
0.0051
0.9353
0.0081
0.7481
hydrocarbon-rich phase
50.0
323.15
0.0219
0.9055
0.0331
0.6856
hydrocarbon-rich phase
50.0
323.15
0.0213
0.8894
0.0306
0.6403
hydrocarbon-rich phase
50.0
323.15
0.0307
0.8716
0.0428
0.6082
hydrocarbon-rich phase
50.0
323.15
0.0807
0.7977
0.1021
0.5045
hydrocarbon-rich phase
50.0
323.15
0.1041
0.7613
0.1256
0.4592
hydrocarbon-rich phase
50.0
323.15
0.1387
0.7175
0.1603
0.4146
hydrocarbon-rich phase
50.0
323.15
0.9860
0.0055
0.9757
0.0027
water-rich phase
50.0
323.15
0.9752
0.0147
0.9672
0.0073
water-rich phase
50.0
323.15
0.9000
0.0571
0.8669
0.0275
water-rich phase
50.0
323.15
0.8598
0.0906
0.8333
0.0439
water-rich phase
50.0
323.15
0.8342
0.1023
0.7961
0.0488
water-rich phase
50.0
323.15
0.8126
0.1162
0.7719
0.0522
water-rich phase
50.0
323.15
0.7755
0.1393
0.7294
0.0655
water-rich phase
50.0
323.15
0.7379
0.1637
0.6888
0.0764
water-rich phase
50.0
323.15
0.5546
0.3231
0.5390
0.1570
water-rich phase
50.0
323.15
0.4574
0.4085
0.4553
0.2033
water-rich phase
50.0
323.15
0.3218
0.5284
0.3320
0.2726
water-rich phase
Method/Apparatus/Procedure:
The titration method was used for solubility measurements. Water was added from a calibrated hypodermic syringe (controlled by a micrometer screw) to a binary ethanol-toluene mixture of known mass and composition until persistent turbidity was observed. The direct analytical method was used for liquid-liquid equilibrium measurements. A mixture was stirred vigorously for 2-3 h in a thermostated cell,
1
and after phase separation samples were taken for analysis. A were taken for analysis. A small amount of tetrahydrofuran was added as an internal standard and homogenization agent in glc analysis. Calibration standards were analyzed separately for each phase prior to each sample analysis by glc. Conditions of the glc analysis were: glass column (2.5 mm I.d., 1.5 m), Poropak Q, 200°C, carrier gas H
2
, thermal conductivity detector.
Source and Purity of Materials:
(1) Source not specified "extra fine," distilled with benzene; 0.1% H
2
O by the Karl Fischer method; p(25°C)=0.784 98 g cm
-3
, n(25°C,D)=1.3605.
(2) Lachema Neratovice, A. R. grade; shaken five times with H
2
SO
4
conc., three times with H
2
O, then with NaOH, dried Na, distilled; p(25°C)=0.861 24 g/cm
3
, n(25°C,D)=1.4939.
(3) Doubly distilled.
Estimated Errors:
Solubility: Not reported.
Temperature: Temp. ±0.05 K.