Mixture of Isopropyl Alcohol + Dimethyl Sulfoxide

Datasets

1. Mole fraction (2)
2. η - Viscosity, Pa*s (2)
3. ρ_l - Mass density, kg/m3 (2)
4. γ - Surface tension liquid-gas, N/m (2)
5. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of Isopropyl Alcohol (1) [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Isopropyl Alcohol (1) - Liquid	Mole fraction of Isopropyl Alcohol (1) - Gas
355.33	1.0000	1.0000
357.51	0.9032	0.9983
359.14	0.8481	0.9972
360.75	0.8051	0.9961
364.71	0.7091	0.9925
368.77	0.6138	0.9869
374.24	0.5225	0.9776
376.78	0.4832	0.9726
381.24	0.4149	0.9623
386.47	0.3561	0.9483
389.52	0.3207	0.9371
398.61	0.2491	0.9015
405.21	0.2009	0.8675
414.02	0.1512	0.8045
425.63	0.1022	0.6991
429.39	0.0890	0.6560
437.48	0.0635	0.5481
441.94	0.0496	0.4695
450.41	0.0286	0.3120
463.38	0.0000	0.0000

Mole fraction of Isopropyl Alcohol (1) [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Isopropyl Alcohol (1) - Liquid	Mole fraction of Isopropyl Alcohol (1) - Gas
355.33	1.0000	1.0000
357.51	0.9032	0.9983
359.14	0.8481	0.9972
360.75	0.8051	0.9961
364.71	0.7091	0.9925
368.77	0.6138	0.9869
374.24	0.5225	0.9776
376.78	0.4832	0.9726
381.24	0.4149	0.9623
386.47	0.3561	0.9483
389.52	0.3207	0.9371
398.61	0.2491	0.9015
405.21	0.2009	0.8675
414.02	0.1512	0.8045
425.63	0.1022	0.6991
429.39	0.0890	0.6560
437.48	0.0635	0.5481
441.94	0.0496	0.4695
450.41	0.0286	0.3120
463.38	0.0000	0.0000

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Dimethyl Sulfoxide (2) - Liquid	Viscosity, Pa*s - Liquid
303.15	0.0000	0.0018
303.15	0.1001	0.0015
303.15	0.2011	0.0014
303.15	0.3005	0.0013
303.15	0.4007	0.0013
303.15	0.4994	0.0013
303.15	0.6010	0.0014
303.15	0.7010	0.0015
303.15	0.7994	0.0016
303.15	0.9005	0.0017
303.15	1.0000	0.0018
308.15	0.0000	0.0016
308.15	0.1001	0.0014
308.15	0.2011	0.0012
308.15	0.3005	0.0012
308.15	0.4007	0.0012
308.15	0.4994	0.0012
308.15	0.6010	0.0013
308.15	0.7010	0.0013
308.15	0.7994	0.0014
308.15	0.9005	0.0015
308.15	1.0000	0.0017
313.15	0.0000	0.0014
313.15	0.1001	0.0012
313.15	0.2011	0.0011
313.15	0.3005	0.0011
313.15	0.4007	0.0011
313.15	0.4994	0.0011
313.15	0.6010	0.0012
313.15	0.7010	0.0012
313.15	0.7994	0.0013
313.15	0.9005	0.0014
313.15	1.0000	0.0015
318.15	0.0000	0.0012
318.15	0.1001	0.0011
318.15	0.2011	0.0010
318.15	0.3005	0.0010
318.15	0.4007	0.0010
318.15	0.4994	0.0010
318.15	0.6010	0.0011
318.15	0.7010	0.0011
318.15	0.7994	0.0012
318.15	0.9005	0.0013
318.15	1.0000	0.0014
323.15	0.0000	0.0010
323.15	0.1001	0.0010
323.15	0.2011	0.0009
323.15	0.3005	0.0009
323.15	0.4007	0.0009
323.15	0.4994	0.0009
323.15	0.6010	0.0010
323.15	0.7010	0.0010
323.15	0.7994	0.0011
323.15	0.9005	0.0012
323.15	1.0000	0.0013

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Dimethyl Sulfoxide (2) - Liquid	Viscosity, Pa*s - Liquid
303.15	0.0000	0.0018
303.15	0.1001	0.0015
303.15	0.2011	0.0014
303.15	0.3005	0.0013
303.15	0.4007	0.0013
303.15	0.4994	0.0013
303.15	0.6010	0.0014
303.15	0.7010	0.0015
303.15	0.7994	0.0016
303.15	0.9005	0.0017
303.15	1.0000	0.0018
308.15	0.0000	0.0016
308.15	0.1001	0.0014
308.15	0.2011	0.0012
308.15	0.3005	0.0012
308.15	0.4007	0.0012
308.15	0.4994	0.0012
308.15	0.6010	0.0013
308.15	0.7010	0.0013
308.15	0.7994	0.0014
308.15	0.9005	0.0015
308.15	1.0000	0.0017
313.15	0.0000	0.0014
313.15	0.1001	0.0012
313.15	0.2011	0.0011
313.15	0.3005	0.0011
313.15	0.4007	0.0011
313.15	0.4994	0.0011
313.15	0.6010	0.0012
313.15	0.7010	0.0012
313.15	0.7994	0.0013
313.15	0.9005	0.0014
313.15	1.0000	0.0015
318.15	0.0000	0.0012
318.15	0.1001	0.0011
318.15	0.2011	0.0010
318.15	0.3005	0.0010
318.15	0.4007	0.0010
318.15	0.4994	0.0010
318.15	0.6010	0.0011
318.15	0.7010	0.0011
318.15	0.7994	0.0012
318.15	0.9005	0.0013
318.15	1.0000	0.0014
323.15	0.0000	0.0010
323.15	0.1001	0.0010
323.15	0.2011	0.0009
323.15	0.3005	0.0009
323.15	0.4007	0.0009
323.15	0.4994	0.0009
323.15	0.6010	0.0010
323.15	0.7010	0.0010
323.15	0.7994	0.0011
323.15	0.9005	0.0012
323.15	1.0000	0.0013

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Dimethyl Sulfoxide (2) - Liquid	Mass density, kg/m3 - Liquid
303.15	0.0000	776.4
303.15	0.1001	806.4
303.15	0.2011	834.9
303.15	0.3005	865.0
303.15	0.4007	895.8
303.15	0.4994	926.6
303.15	0.6010	958.9
303.15	0.7010	991.1
303.15	0.7994	1023.3
303.15	0.9005	1056.9
303.15	1.0000	1090.7
308.15	0.0000	772.6
308.15	0.1001	802.2
308.15	0.2011	830.4
308.15	0.3005	860.4
308.15	0.4007	891.0
308.15	0.4994	921.6
308.15	0.6010	953.7
308.15	0.7010	985.6
308.15	0.7994	1017.6
308.15	0.9005	1051.0
308.15	1.0000	1084.7
313.15	0.0000	768.6
313.15	0.1001	798.2
313.15	0.2011	826.0
313.15	0.3005	856.3
313.15	0.4007	887.1
313.15	0.4994	917.9
313.15	0.6010	950.0
313.15	0.7010	982.2
313.15	0.7994	1014.5
313.15	0.9005	1048.2
313.15	1.0000	1082.3
318.15	0.0000	763.9
318.15	0.1001	793.2
318.15	0.2011	820.7
318.15	0.3005	850.6
318.15	0.4007	881.3
318.15	0.4994	911.9
318.15	0.6010	943.8
318.15	0.7010	975.7
318.15	0.7994	1007.6
318.15	0.9005	1041.0
318.15	1.0000	1075.1
323.15	0.0000	758.8
323.15	0.1001	787.9
323.15	0.2011	815.3
323.15	0.3005	845.2
323.15	0.4007	875.8
323.15	0.4994	906.5
323.15	0.6010	938.5
323.15	0.7010	970.4
323.15	0.7994	1002.3
323.15	0.9005	1035.8
323.15	1.0000	1070.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Dimethyl Sulfoxide (2) - Liquid	Mass density, kg/m3 - Liquid
303.15	0.0000	776.4
303.15	0.1001	806.4
303.15	0.2011	834.9
303.15	0.3005	865.0
303.15	0.4007	895.8
303.15	0.4994	926.6
303.15	0.6010	958.9
303.15	0.7010	991.1
303.15	0.7994	1023.3
303.15	0.9005	1056.9
303.15	1.0000	1090.7
308.15	0.0000	772.6
308.15	0.1001	802.2
308.15	0.2011	830.4
308.15	0.3005	860.4
308.15	0.4007	891.0
308.15	0.4994	921.6
308.15	0.6010	953.7
308.15	0.7010	985.6
308.15	0.7994	1017.6
308.15	0.9005	1051.0
308.15	1.0000	1084.7
313.15	0.0000	768.6
313.15	0.1001	798.2
313.15	0.2011	826.0
313.15	0.3005	856.3
313.15	0.4007	887.1
313.15	0.4994	917.9
313.15	0.6010	950.0
313.15	0.7010	982.2
313.15	0.7994	1014.5
313.15	0.9005	1048.2
313.15	1.0000	1082.3
318.15	0.0000	763.9
318.15	0.1001	793.2
318.15	0.2011	820.7
318.15	0.3005	850.6
318.15	0.4007	881.3
318.15	0.4994	911.9
318.15	0.6010	943.8
318.15	0.7010	975.7
318.15	0.7994	1007.6
318.15	0.9005	1041.0
318.15	1.0000	1075.1
323.15	0.0000	758.8
323.15	0.1001	787.9
323.15	0.2011	815.3
323.15	0.3005	845.2
323.15	0.4007	875.8
323.15	0.4994	906.5
323.15	0.6010	938.5
323.15	0.7010	970.4
323.15	0.7994	1002.3
323.15	0.9005	1035.8
323.15	1.0000	1070.0

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Isopropyl Alcohol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
298.15	0.0440	0.0392
298.15	0.0850	0.0364
298.15	0.1570	0.0338
298.15	0.2450	0.0309
298.15	0.3380	0.0286
298.15	0.4410	0.0267
298.15	0.5370	0.0252
298.15	0.6190	0.0242
298.15	0.6760	0.0232
298.15	0.7190	0.0230
298.15	0.7510	0.0228
298.15	0.8600	0.0220
308.15	0.0440	0.0386
308.15	0.0850	0.0359
308.15	0.1570	0.0328
308.15	0.2450	0.0302
308.15	0.3380	0.0277
308.15	0.4410	0.0259
308.15	0.5370	0.0245
308.15	0.6190	0.0234
308.15	0.6760	0.0228
308.15	0.7190	0.0225
308.15	0.7510	0.0222
308.15	0.8600	0.0212
318.15	0.0440	0.0379
318.15	0.0850	0.0350
318.15	0.1570	0.0320
318.15	0.2450	0.0295
318.15	0.3380	0.0270
318.15	0.4410	0.0252
318.15	0.5370	0.0239
318.15	0.6190	0.0228
318.15	0.6760	0.0221
318.15	0.7190	0.0217
318.15	0.7510	0.0214
318.15	0.8600	0.0205
328.15	0.0440	0.0369
328.15	0.0850	0.0341
328.15	0.1570	0.0312
328.15	0.2450	0.0284
328.15	0.3380	0.0260
328.15	0.4410	0.0241
328.15	0.5370	0.0228
328.15	0.6190	0.0217
328.15	0.6760	0.0211
328.15	0.7190	0.0207
328.15	0.7510	0.0204
328.15	0.8600	0.0196
298.15	0.0000	0.0424
308.15	0.0000	0.0413
318.15	0.0000	0.0402
328.15	0.0000	0.0391
298.15	1.0000	0.0211
308.15	1.0000	0.0203
318.15	1.0000	0.0195
328.15	1.0000	0.0185

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Isopropyl Alcohol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
298.15	0.0440	0.0392
298.15	0.0850	0.0364
298.15	0.1570	0.0338
298.15	0.2450	0.0309
298.15	0.3380	0.0286
298.15	0.4410	0.0267
298.15	0.5370	0.0252
298.15	0.6190	0.0242
298.15	0.6760	0.0232
298.15	0.7190	0.0230
298.15	0.7510	0.0228
298.15	0.8600	0.0220
308.15	0.0440	0.0386
308.15	0.0850	0.0359
308.15	0.1570	0.0328
308.15	0.2450	0.0302
308.15	0.3380	0.0277
308.15	0.4410	0.0259
308.15	0.5370	0.0245
308.15	0.6190	0.0234
308.15	0.6760	0.0228
308.15	0.7190	0.0225
308.15	0.7510	0.0222
308.15	0.8600	0.0212
318.15	0.0440	0.0379
318.15	0.0850	0.0350
318.15	0.1570	0.0320
318.15	0.2450	0.0295
318.15	0.3380	0.0270
318.15	0.4410	0.0252
318.15	0.5370	0.0239
318.15	0.6190	0.0228
318.15	0.6760	0.0221
318.15	0.7190	0.0217
318.15	0.7510	0.0214
318.15	0.8600	0.0205
328.15	0.0440	0.0369
328.15	0.0850	0.0341
328.15	0.1570	0.0312
328.15	0.2450	0.0284
328.15	0.3380	0.0260
328.15	0.4410	0.0241
328.15	0.5370	0.0228
328.15	0.6190	0.0217
328.15	0.6760	0.0211
328.15	0.7190	0.0207
328.15	0.7510	0.0204
328.15	0.8600	0.0196
298.15	0.0000	0.0424
308.15	0.0000	0.0413
318.15	0.0000	0.0402
328.15	0.0000	0.0391
298.15	1.0000	0.0211
308.15	1.0000	0.0203
318.15	1.0000	0.0195
328.15	1.0000	0.0185

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Isopropyl Alcohol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
1.0000	355.33
0.9032	357.51
0.8481	359.14
0.8051	360.75
0.7091	364.71
0.6138	368.77
0.5225	374.24
0.4832	376.78
0.4149	381.24
0.3561	386.47
0.3207	389.52
0.2491	398.61
0.2009	405.21
0.1512	414.02
0.1022	425.63
0.0890	429.39
0.0635	437.48
0.0496	441.94
0.0286	450.41
0.0000	463.38

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Isopropyl Alcohol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
1.0000	355.33
0.9032	357.51
0.8481	359.14
0.8051	360.75
0.7091	364.71
0.6138	368.77
0.5225	374.24
0.4832	376.78
0.4149	381.24
0.3561	386.47
0.3207	389.52
0.2491	398.61
0.2009	405.21
0.1512	414.02
0.1022	425.63
0.0890	429.39
0.0635	437.48
0.0496	441.94
0.0286	450.41
0.0000	463.38

Sources

• Densities and viscosities of binary mixtures of {dimethylsulfoxide + aliphatic lower alkanols (C1 C3)} at temperatures from T = 303.15 K to T = 323.15 K
• Effect of temperature and composition on the surface tension and surface properties of binary mixtures containing DMSO and short chain alcohols
• Vapor Liquid Equilibria for Ternary Mixtures of Isopropyl Alcohol, Isopropyl Acetate, and DMSO at 101.3 kPa