Mixture of Acetonitrile + Dimethyl Sulfoxide

Datasets

1. Mole fraction (4)
2. η - Viscosity, Pa*s (6)
3. ρ_l - Mass density, kg/m3 (8)
4. c_sound,fluid - Speed of Sound, m/s (2)
5. T_boil - Boiling temperature at pressure P, K (4)

Mole fraction of Acetonitrile (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetonitrile (1) - Liquid	Mole fraction of Acetonitrile (1) - Gas
0.0295	0.5056
0.0603	0.7008
0.0911	0.8156
0.1215	0.8662
0.1801	0.9198
0.2123	0.9398
0.2556	0.9531
0.2803	0.9590
0.3314	0.9675
0.3727	0.9722
0.4237	0.9766
0.5032	0.9816
0.5319	0.9829
0.5800	0.9848
0.6331	0.9865
0.7000	0.9883
0.7222	0.9888
0.7918	0.9903
0.8309	0.9911
0.8876	0.9925
0.9204	0.9935
0.9700	0.9962

Mole fraction of Acetonitrile (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetonitrile (1) - Liquid	Mole fraction of Acetonitrile (1) - Gas
0.0000	0.0000
0.0340	0.2280
0.0790	0.4980
0.1350	0.7250
0.1690	0.8010
0.2140	0.8620
0.2580	0.8980
0.2920	0.9160
0.3370	0.9340
0.3820	0.9470
0.4160	0.9550
0.5060	0.9710
0.5840	0.9810
0.6290	0.9850
0.6740	0.9890
0.7190	0.9920
0.7980	0.9960
0.8430	0.9970
0.9130	0.9990
0.9660	1.0000
1.0000	1.0000

Mole fraction of Acetonitrile (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetonitrile (1) - Liquid	Mole fraction of Acetonitrile (1) - Gas
0.0295	0.5056
0.0603	0.7008
0.0911	0.8156
0.1215	0.8662
0.1801	0.9198
0.2123	0.9398
0.2556	0.9531
0.2803	0.9590
0.3314	0.9675
0.3727	0.9722
0.4237	0.9766
0.5032	0.9816
0.5319	0.9829
0.5800	0.9848
0.6331	0.9865
0.7000	0.9883
0.7222	0.9888
0.7918	0.9903
0.8309	0.9911
0.8876	0.9925
0.9204	0.9935
0.9700	0.9962

Mole fraction of Acetonitrile (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetonitrile (1) - Liquid	Mole fraction of Acetonitrile (1) - Gas
0.0000	0.0000
0.0340	0.2280
0.0790	0.4980
0.1350	0.7250
0.1690	0.8010
0.2140	0.8620
0.2580	0.8980
0.2920	0.9160
0.3370	0.9340
0.3820	0.9470
0.4160	0.9550
0.5060	0.9710
0.5840	0.9810
0.6290	0.9850
0.6740	0.9890
0.7190	0.9920
0.7980	0.9960
0.8430	0.9970
0.9130	0.9990
0.9660	1.0000
1.0000	1.0000

Viscosity, Pa*s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mass fraction of Dimethyl Sulfoxide (2) - Liquid	Viscosity, Pa*s - Liquid
0.2000	0.0004
0.4000	0.0005
0.6000	0.0007

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Dimethyl Sulfoxide (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0995	0.0004
298.15	0.2061	0.0005
298.15	0.2936	0.0006
298.15	0.4055	0.0007
298.15	0.5051	0.0009
298.15	0.6001	0.0011
298.15	0.7006	0.0013
298.15	0.8072	0.0015
298.15	0.8947	0.0018
298.15	1.0000	0.0020
303.15	0.2936	0.0005
303.15	0.4055	0.0007
303.15	0.5051	0.0008
303.15	0.6001	0.0010
303.15	0.2061	0.0005
303.15	0.7006	0.0012
303.15	0.0995	0.0004
303.15	0.8072	0.0014
303.15	0.8947	0.0016
303.15	1.0000	0.0018
308.15	0.5051	0.0008
308.15	0.6001	0.0009
308.15	0.2936	0.0005
308.15	0.0995	0.0004
308.15	0.7006	0.0011
308.15	0.8072	0.0013
308.15	0.2061	0.0005
308.15	0.8947	0.0015
308.15	0.4055	0.0006
308.15	1.0000	0.0017
313.15	0.6001	0.0008
313.15	0.0995	0.0004
313.15	0.2936	0.0005
313.15	0.7006	0.0010
313.15	0.5051	0.0007
313.15	0.4055	0.0006
313.15	0.8072	0.0012
313.15	0.8947	0.0014
313.15	0.2061	0.0004
313.15	1.0000	0.0015
318.15	0.4055	0.0006
318.15	0.8072	0.0011
318.15	0.2936	0.0005
318.15	0.2061	0.0004
318.15	0.5051	0.0007
318.15	0.0995	0.0003
318.15	0.6001	0.0008
318.15	0.8947	0.0012
318.15	1.0000	0.0014
318.15	0.7006	0.0009
323.15	0.2936	0.0004
323.15	0.4055	0.0005
323.15	0.8072	0.0010
323.15	0.8947	0.0011
323.15	0.7006	0.0009
323.15	0.2061	0.0004
323.15	0.6001	0.0008
323.15	0.0995	0.0003
323.15	0.5051	0.0006
323.15	1.0000	0.0013

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Acetonitrile (1) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.0000	298.15	0.0020
0.0000	303.15	0.0018
0.0000	308.15	0.0017
0.0000	313.15	0.0015
0.0000	318.15	0.0014
0.0249	298.15	0.0019
0.0249	303.15	0.0018
0.0249	308.15	0.0016
0.0249	313.15	0.0015
0.0249	318.15	0.0013
0.0518	298.15	0.0018
0.0518	303.15	0.0017
0.0518	308.15	0.0015
0.0518	313.15	0.0014
0.0518	318.15	0.0013
0.0759	298.15	0.0018
0.0759	303.15	0.0016
0.0759	308.15	0.0015
0.0759	313.15	0.0014
0.0759	318.15	0.0012
0.1079	298.15	0.0017
0.1079	303.15	0.0015
0.1079	308.15	0.0014
0.1079	313.15	0.0013
0.1079	318.15	0.0012
0.1570	298.15	0.0015
0.1570	303.15	0.0014
0.1570	308.15	0.0013
0.1570	313.15	0.0012
0.1570	318.15	0.0011
0.1998	298.15	0.0014
0.1998	303.15	0.0013
0.1998	308.15	0.0012
0.1998	313.15	0.0011
0.1998	318.15	0.0010
0.2609	298.15	0.0013
0.2609	303.15	0.0012
0.2609	308.15	0.0011
0.2609	313.15	0.0010
0.2609	318.15	0.0009
0.3034	298.15	0.0012
0.3034	303.15	0.0011
0.3034	308.15	0.0010
0.3034	313.15	0.0009
0.3034	318.15	0.0008
0.3548	298.15	0.0011
0.3548	303.15	0.0010
0.3548	308.15	0.0009
0.3548	313.15	0.0008
0.3548	318.15	0.0007
0.4110	298.15	0.0010
0.4110	303.15	0.0009
0.4110	308.15	0.0008
0.4110	313.15	0.0007
0.4110	318.15	0.0007
0.4696	298.15	0.0009
0.4696	303.15	0.0008
0.4696	308.15	0.0007
0.4696	313.15	0.0006
0.4696	318.15	0.0006
0.5084	298.15	0.0008
0.5084	303.15	0.0007
0.5084	308.15	0.0007
0.5084	313.15	0.0006
0.5084	318.15	0.0005
0.5566	298.15	0.0007
0.5566	303.15	0.0007
0.5566	308.15	0.0006
0.5566	313.15	0.0005
0.5566	318.15	0.0005
0.6053	298.15	0.0007
0.6053	303.15	0.0006
0.6053	308.15	0.0005
0.6053	313.15	0.0005
0.6053	318.15	0.0004
0.6666	298.15	0.0006
0.6666	303.15	0.0005
0.6666	308.15	0.0005
0.6666	313.15	0.0004
0.6666	318.15	0.0004
0.7114	298.15	0.0005
0.7114	303.15	0.0005
0.7114	308.15	0.0004
0.7114	313.15	0.0004
0.7114	318.15	0.0004
0.7688	298.15	0.0005
0.7688	303.15	0.0004
0.7688	308.15	0.0004
0.7688	313.15	0.0004
0.7688	318.15	0.0003
0.8081	298.15	0.0005
0.8081	303.15	0.0004
0.8081	308.15	0.0004
0.8081	313.15	0.0004
0.8081	318.15	0.0003
0.8510	298.15	0.0004
0.8510	303.15	0.0004
0.8510	308.15	0.0004
0.8510	313.15	0.0003
0.8510	318.15	0.0003
0.9009	298.15	0.0004
0.9009	303.15	0.0004
0.9009	308.15	0.0003
0.9009	313.15	0.0003
0.9009	318.15	0.0003
0.9502	298.15	0.0004
0.9502	303.15	0.0003
0.9502	308.15	0.0003
0.9502	313.15	0.0003
0.9502	318.15	0.0003
0.9771	298.15	0.0004
0.9771	303.15	0.0003
0.9771	308.15	0.0003
0.9771	313.15	0.0003
0.9771	318.15	0.0003
1.0000	298.15	0.0003
1.0000	303.15	0.0003
1.0000	308.15	0.0003
1.0000	313.15	0.0003
1.0000	318.15	0.0003

Viscosity, Pa*s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mass fraction of Dimethyl Sulfoxide (2) - Liquid	Viscosity, Pa*s - Liquid
0.2000	0.0004
0.4000	0.0005
0.6000	0.0007

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Dimethyl Sulfoxide (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0995	0.0004
298.15	0.2061	0.0005
298.15	0.2936	0.0006
298.15	0.4055	0.0007
298.15	0.5051	0.0009
298.15	0.6001	0.0011
298.15	0.7006	0.0013
298.15	0.8072	0.0015
298.15	0.8947	0.0018
298.15	1.0000	0.0020
303.15	0.2936	0.0005
303.15	0.4055	0.0007
303.15	0.5051	0.0008
303.15	0.6001	0.0010
303.15	0.2061	0.0005
303.15	0.7006	0.0012
303.15	0.0995	0.0004
303.15	0.8072	0.0014
303.15	0.8947	0.0016
303.15	1.0000	0.0018
308.15	0.5051	0.0008
308.15	0.6001	0.0009
308.15	0.2936	0.0005
308.15	0.0995	0.0004
308.15	0.7006	0.0011
308.15	0.8072	0.0013
308.15	0.2061	0.0005
308.15	0.8947	0.0015
308.15	0.4055	0.0006
308.15	1.0000	0.0017
313.15	0.6001	0.0008
313.15	0.0995	0.0004
313.15	0.2936	0.0005
313.15	0.7006	0.0010
313.15	0.5051	0.0007
313.15	0.4055	0.0006
313.15	0.8072	0.0012
313.15	0.8947	0.0014
313.15	0.2061	0.0004
313.15	1.0000	0.0015
318.15	0.4055	0.0006
318.15	0.8072	0.0011
318.15	0.2936	0.0005
318.15	0.2061	0.0004
318.15	0.5051	0.0007
318.15	0.0995	0.0003
318.15	0.6001	0.0008
318.15	0.8947	0.0012
318.15	1.0000	0.0014
318.15	0.7006	0.0009
323.15	0.2936	0.0004
323.15	0.4055	0.0005
323.15	0.8072	0.0010
323.15	0.8947	0.0011
323.15	0.7006	0.0009
323.15	0.2061	0.0004
323.15	0.6001	0.0008
323.15	0.0995	0.0003
323.15	0.5051	0.0006
323.15	1.0000	0.0013

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Acetonitrile (1) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.0000	298.15	0.0020
0.0000	303.15	0.0018
0.0000	308.15	0.0017
0.0000	313.15	0.0015
0.0000	318.15	0.0014
0.0249	298.15	0.0019
0.0249	303.15	0.0018
0.0249	308.15	0.0016
0.0249	313.15	0.0015
0.0249	318.15	0.0013
0.0518	298.15	0.0018
0.0518	303.15	0.0017
0.0518	308.15	0.0015
0.0518	313.15	0.0014
0.0518	318.15	0.0013
0.0759	298.15	0.0018
0.0759	303.15	0.0016
0.0759	308.15	0.0015
0.0759	313.15	0.0014
0.0759	318.15	0.0012
0.1079	298.15	0.0017
0.1079	303.15	0.0015
0.1079	308.15	0.0014
0.1079	313.15	0.0013
0.1079	318.15	0.0012
0.1570	298.15	0.0015
0.1570	303.15	0.0014
0.1570	308.15	0.0013
0.1570	313.15	0.0012
0.1570	318.15	0.0011
0.1998	298.15	0.0014
0.1998	303.15	0.0013
0.1998	308.15	0.0012
0.1998	313.15	0.0011
0.1998	318.15	0.0010
0.2609	298.15	0.0013
0.2609	303.15	0.0012
0.2609	308.15	0.0011
0.2609	313.15	0.0010
0.2609	318.15	0.0009
0.3034	298.15	0.0012
0.3034	303.15	0.0011
0.3034	308.15	0.0010
0.3034	313.15	0.0009
0.3034	318.15	0.0008
0.3548	298.15	0.0011
0.3548	303.15	0.0010
0.3548	308.15	0.0009
0.3548	313.15	0.0008
0.3548	318.15	0.0007
0.4110	298.15	0.0010
0.4110	303.15	0.0009
0.4110	308.15	0.0008
0.4110	313.15	0.0007
0.4110	318.15	0.0007
0.4696	298.15	0.0009
0.4696	303.15	0.0008
0.4696	308.15	0.0007
0.4696	313.15	0.0006
0.4696	318.15	0.0006
0.5084	298.15	0.0008
0.5084	303.15	0.0007
0.5084	308.15	0.0007
0.5084	313.15	0.0006
0.5084	318.15	0.0005
0.5566	298.15	0.0007
0.5566	303.15	0.0007
0.5566	308.15	0.0006
0.5566	313.15	0.0005
0.5566	318.15	0.0005
0.6053	298.15	0.0007
0.6053	303.15	0.0006
0.6053	308.15	0.0005
0.6053	313.15	0.0005
0.6053	318.15	0.0004
0.6666	298.15	0.0006
0.6666	303.15	0.0005
0.6666	308.15	0.0005
0.6666	313.15	0.0004
0.6666	318.15	0.0004
0.7114	298.15	0.0005
0.7114	303.15	0.0005
0.7114	308.15	0.0004
0.7114	313.15	0.0004
0.7114	318.15	0.0004
0.7688	298.15	0.0005
0.7688	303.15	0.0004
0.7688	308.15	0.0004
0.7688	313.15	0.0004
0.7688	318.15	0.0003
0.8081	298.15	0.0005
0.8081	303.15	0.0004
0.8081	308.15	0.0004
0.8081	313.15	0.0004
0.8081	318.15	0.0003
0.8510	298.15	0.0004
0.8510	303.15	0.0004
0.8510	308.15	0.0004
0.8510	313.15	0.0003
0.8510	318.15	0.0003
0.9009	298.15	0.0004
0.9009	303.15	0.0004
0.9009	308.15	0.0003
0.9009	313.15	0.0003
0.9009	318.15	0.0003
0.9502	298.15	0.0004
0.9502	303.15	0.0003
0.9502	308.15	0.0003
0.9502	313.15	0.0003
0.9502	318.15	0.0003
0.9771	298.15	0.0004
0.9771	303.15	0.0003
0.9771	308.15	0.0003
0.9771	313.15	0.0003
0.9771	318.15	0.0003
1.0000	298.15	0.0003
1.0000	303.15	0.0003
1.0000	308.15	0.0003
1.0000	313.15	0.0003
1.0000	318.15	0.0003

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mass fraction of Dimethyl Sulfoxide (2) - Liquid	Mass density, kg/m3 - Liquid
0.2000	829.3
0.4000	883.3
0.6000	945.6

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Dimethyl Sulfoxide (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0995	820.43
303.15	0.0995	815.06
308.15	0.0995	809.67
313.15	0.0995	804.26
318.15	0.0995	798.81
323.15	0.0995	793.34
303.15	0.2061	857.6
298.15	0.2061	862.88
308.15	0.2061	852.28
313.15	0.2061	846.95
318.15	0.2061	841.59
323.15	0.2061	836.19
303.15	0.2936	891.05
308.15	0.2936	885.81
298.15	0.2936	896.29
313.15	0.2936	880.52
318.15	0.2936	875.23
323.15	0.2936	869.91
308.15	0.4055	924.82
303.15	0.4055	929.99
313.15	0.4055	919.62
298.15	0.4055	935.15
318.15	0.4055	914.41
323.15	0.4055	909.18
313.15	0.5051	951.43
308.15	0.5051	956.58
303.15	0.5051	961.71
318.15	0.5051	946.27
298.15	0.5051	966.82
323.15	0.5051	941.1
313.15	0.6001	979.59
308.15	0.6001	984.67
318.15	0.6001	974.52
298.15	0.6001	994.77
303.15	0.6001	989.72
323.15	0.6001	969.42
298.15	0.7006	1022.53
303.15	0.7006	1017.55
318.15	0.7006	1002.73
313.15	0.7006	1007.58
308.15	0.7006	1012.57
323.15	0.7006	997.71
308.15	0.8072	1040.36
318.15	0.8072	1030.38
298.15	0.8072	1050.32
303.15	0.8072	1045.34
313.15	0.8072	1035.36
323.15	0.8072	1025.37
298.15	0.8947	1071.95
308.15	0.8947	1062.01
303.15	0.8947	1066.98
313.15	0.8947	1057.03
318.15	0.8947	1052.04
323.15	0.8947	1047.05
318.15	1.0000	1075.6
303.15	1.0000	1090.62
298.15	1.0000	1095.62
313.15	1.0000	1080.6
308.15	1.0000	1085.61
323.15	1.0000	1070.66

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 81.5 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetonitrile (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	1100.41
293.15	0.0563	1087.32
293.15	0.1195	1072.32
293.15	0.1751	1058.54
293.15	0.2996	1025.83
293.15	0.3723	1005.56
293.15	0.4529	981.91
293.15	0.5273	959.0
293.15	0.5790	942.39
293.15	0.6896	904.94
293.15	0.7579	880.41
293.15	0.8337	851.62
293.15	0.9330	811.3
293.15	1.0000	781.97
303.15	0.0000	1090.37
303.15	0.0563	1077.27
303.15	0.1195	1062.27
303.15	0.1751	1048.48
303.15	0.2996	1015.69
303.15	0.3723	995.38
303.15	0.4529	971.68
303.15	0.5273	948.69
303.15	0.5790	932.08
303.15	0.6896	894.48
303.15	0.7579	869.88
303.15	0.8337	841.0
303.15	0.9330	800.6
303.15	1.0000	771.15
313.15	0.0000	1080.34
313.15	0.0563	1067.22
313.15	0.1195	1052.21
313.15	0.1751	1038.38
313.15	0.2996	1005.54
313.15	0.3723	985.18
313.15	0.4529	961.4
313.15	0.5273	938.36
313.15	0.5790	921.68
313.15	0.6896	883.96
313.15	0.7579	859.27
313.15	0.8337	830.29
313.15	0.9330	789.76
313.15	1.0000	760.2
323.15	0.0000	1070.3
323.15	0.0563	1057.17
323.15	0.1195	1042.11
323.15	0.1751	1028.38
323.15	0.2996	995.35
323.15	0.3723	974.94
323.15	0.4529	951.09
323.15	0.5273	927.96
323.15	0.5790	911.22
323.15	0.6896	873.36
323.15	0.7579	848.57
323.15	0.8337	819.48
323.15	0.9330	778.79
323.15	1.0000	749.12
333.15	0.0000	1060.27
333.15	0.0563	1047.11
333.15	0.1195	1032.03
333.15	0.1751	1018.15
333.15	0.2996	985.14
333.15	0.3723	964.64
333.15	0.4529	940.71
333.15	0.5273	917.5
333.15	0.5790	900.68
333.15	0.6896	862.66
333.15	0.7579	837.77
333.15	0.8337	808.55
333.15	0.9330	767.68
333.15	1.0000	737.87

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Acetonitrile (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	298.15	1096.29
0.0249	298.15	1089.25
0.0518	298.15	1081.72
0.0759	298.15	1075.14
0.1079	298.15	1066.34
0.1570	298.15	1052.66
0.1998	298.15	1040.65
0.2609	298.15	1023.27
0.3034	298.15	1010.97
0.3548	298.15	995.86
0.4110	298.15	978.94
0.4696	298.15	960.84
0.5084	298.15	948.58
0.5566	298.15	933.09
0.6053	298.15	917.12
0.6666	298.15	896.67
0.7114	298.15	881.56
0.7688	298.15	862.03
0.8081	298.15	848.47
0.8510	298.15	833.49
0.9009	298.15	815.55
0.9502	298.15	797.01
0.9771	298.15	786.22
1.0000	298.15	776.69
0.0000	303.15	1091.44
0.0249	303.15	1084.41
0.0518	303.15	1076.88
0.0759	303.15	1070.33
0.1079	303.15	1061.51
0.1570	303.15	1047.83
0.1998	303.15	1035.83
0.2609	303.15	1018.44
0.3034	303.15	1006.18
0.3548	303.15	991.06
0.4110	303.15	974.15
0.4696	303.15	956.06
0.5084	303.15	943.78
0.5566	303.15	928.29
0.6053	303.15	912.34
0.6666	303.15	891.91
0.7114	303.15	876.87
0.7688	303.15	857.32
0.8081	303.15	843.81
0.8510	303.15	828.78
0.9009	303.15	810.84
0.9502	303.15	792.31
0.9771	303.15	781.49
1.0000	303.15	771.89
0.0000	308.15	1086.41
0.0249	308.15	1079.37
0.0518	308.15	1071.78
0.0759	308.15	1065.2
0.1079	308.15	1056.33
0.1570	308.15	1042.6
0.1998	308.15	1030.53
0.2609	308.15	1013.06
0.3034	308.15	1000.71
0.3548	308.15	985.53
0.4110	308.15	968.53
0.4696	308.15	950.36
0.5084	308.15	938.05
0.5566	308.15	922.51
0.6053	308.15	906.49
0.6666	308.15	886.05
0.7114	308.15	870.94
0.7688	308.15	851.38
0.8081	308.15	837.89
0.8510	308.15	822.79
0.9009	308.15	804.79
0.9502	308.15	786.06
0.9771	308.15	775.12
1.0000	308.15	765.46
0.0000	313.15	1081.59
0.0249	313.15	1074.57
0.0518	313.15	1066.98
0.0759	313.15	1060.43
0.1079	313.15	1051.61
0.1570	313.15	1037.81
0.1998	313.15	1025.77
0.2609	313.15	1008.31
0.3034	313.15	995.97
0.3548	313.15	980.82
0.4110	313.15	963.81
0.4696	313.15	945.65
0.5084	313.15	933.36
0.5566	313.15	917.82
0.6053	313.15	901.86
0.6666	313.15	881.45
0.7114	313.15	866.39
0.7688	313.15	846.81
0.8081	313.15	833.37
0.8510	313.15	818.29
0.9009	313.15	800.34
0.9502	313.15	781.54
0.9771	313.15	770.53
1.0000	313.15	760.86
0.0000	318.15	1076.46
0.0249	318.15	1069.43
0.0518	318.15	1061.81
0.0759	318.15	1055.25
0.1079	318.15	1046.39
0.1570	318.15	1032.57
0.1998	318.15	1020.45
0.2609	318.15	1002.91
0.3034	318.15	990.54
0.3548	318.15	975.32
0.4110	318.15	958.25
0.4696	318.15	940.03
0.5084	318.15	927.72
0.5566	318.15	912.19
0.6053	318.15	896.19
0.6666	318.15	875.79
0.7114	318.15	860.68
0.7688	318.15	841.15
0.8081	318.15	827.59
0.8510	318.15	812.61
0.9009	318.15	794.64
0.9502	318.15	775.55
0.9771	318.15	764.46
1.0000	318.15	754.76

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mass fraction of Dimethyl Sulfoxide (2) - Liquid	Mass density, kg/m3 - Liquid
0.2000	829.3
0.4000	883.3
0.6000	945.6

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Dimethyl Sulfoxide (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0995	820.43
303.15	0.0995	815.06
308.15	0.0995	809.67
313.15	0.0995	804.26
318.15	0.0995	798.81
323.15	0.0995	793.34
303.15	0.2061	857.6
298.15	0.2061	862.88
308.15	0.2061	852.28
313.15	0.2061	846.95
318.15	0.2061	841.59
323.15	0.2061	836.19
303.15	0.2936	891.05
308.15	0.2936	885.81
298.15	0.2936	896.29
313.15	0.2936	880.52
318.15	0.2936	875.23
323.15	0.2936	869.91
308.15	0.4055	924.82
303.15	0.4055	929.99
313.15	0.4055	919.62
298.15	0.4055	935.15
318.15	0.4055	914.41
323.15	0.4055	909.18
313.15	0.5051	951.43
308.15	0.5051	956.58
303.15	0.5051	961.71
318.15	0.5051	946.27
298.15	0.5051	966.82
323.15	0.5051	941.1
313.15	0.6001	979.59
308.15	0.6001	984.67
318.15	0.6001	974.52
298.15	0.6001	994.77
303.15	0.6001	989.72
323.15	0.6001	969.42
298.15	0.7006	1022.53
303.15	0.7006	1017.55
318.15	0.7006	1002.73
313.15	0.7006	1007.58
308.15	0.7006	1012.57
323.15	0.7006	997.71
308.15	0.8072	1040.36
318.15	0.8072	1030.38
298.15	0.8072	1050.32
303.15	0.8072	1045.34
313.15	0.8072	1035.36
323.15	0.8072	1025.37
298.15	0.8947	1071.95
308.15	0.8947	1062.01
303.15	0.8947	1066.98
313.15	0.8947	1057.03
318.15	0.8947	1052.04
323.15	0.8947	1047.05
318.15	1.0000	1075.6
303.15	1.0000	1090.62
298.15	1.0000	1095.62
313.15	1.0000	1080.6
308.15	1.0000	1085.61
323.15	1.0000	1070.66

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 81.5 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetonitrile (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	1100.41
293.15	0.0563	1087.32
293.15	0.1195	1072.32
293.15	0.1751	1058.54
293.15	0.2996	1025.83
293.15	0.3723	1005.56
293.15	0.4529	981.91
293.15	0.5273	959.0
293.15	0.5790	942.39
293.15	0.6896	904.94
293.15	0.7579	880.41
293.15	0.8337	851.62
293.15	0.9330	811.3
293.15	1.0000	781.97
303.15	0.0000	1090.37
303.15	0.0563	1077.27
303.15	0.1195	1062.27
303.15	0.1751	1048.48
303.15	0.2996	1015.69
303.15	0.3723	995.38
303.15	0.4529	971.68
303.15	0.5273	948.69
303.15	0.5790	932.08
303.15	0.6896	894.48
303.15	0.7579	869.88
303.15	0.8337	841.0
303.15	0.9330	800.6
303.15	1.0000	771.15
313.15	0.0000	1080.34
313.15	0.0563	1067.22
313.15	0.1195	1052.21
313.15	0.1751	1038.38
313.15	0.2996	1005.54
313.15	0.3723	985.18
313.15	0.4529	961.4
313.15	0.5273	938.36
313.15	0.5790	921.68
313.15	0.6896	883.96
313.15	0.7579	859.27
313.15	0.8337	830.29
313.15	0.9330	789.76
313.15	1.0000	760.2
323.15	0.0000	1070.3
323.15	0.0563	1057.17
323.15	0.1195	1042.11
323.15	0.1751	1028.38
323.15	0.2996	995.35
323.15	0.3723	974.94
323.15	0.4529	951.09
323.15	0.5273	927.96
323.15	0.5790	911.22
323.15	0.6896	873.36
323.15	0.7579	848.57
323.15	0.8337	819.48
323.15	0.9330	778.79
323.15	1.0000	749.12
333.15	0.0000	1060.27
333.15	0.0563	1047.11
333.15	0.1195	1032.03
333.15	0.1751	1018.15
333.15	0.2996	985.14
333.15	0.3723	964.64
333.15	0.4529	940.71
333.15	0.5273	917.5
333.15	0.5790	900.68
333.15	0.6896	862.66
333.15	0.7579	837.77
333.15	0.8337	808.55
333.15	0.9330	767.68
333.15	1.0000	737.87

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Acetonitrile (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	298.15	1096.29
0.0249	298.15	1089.25
0.0518	298.15	1081.72
0.0759	298.15	1075.14
0.1079	298.15	1066.34
0.1570	298.15	1052.66
0.1998	298.15	1040.65
0.2609	298.15	1023.27
0.3034	298.15	1010.97
0.3548	298.15	995.86
0.4110	298.15	978.94
0.4696	298.15	960.84
0.5084	298.15	948.58
0.5566	298.15	933.09
0.6053	298.15	917.12
0.6666	298.15	896.67
0.7114	298.15	881.56
0.7688	298.15	862.03
0.8081	298.15	848.47
0.8510	298.15	833.49
0.9009	298.15	815.55
0.9502	298.15	797.01
0.9771	298.15	786.22
1.0000	298.15	776.69
0.0000	303.15	1091.44
0.0249	303.15	1084.41
0.0518	303.15	1076.88
0.0759	303.15	1070.33
0.1079	303.15	1061.51
0.1570	303.15	1047.83
0.1998	303.15	1035.83
0.2609	303.15	1018.44
0.3034	303.15	1006.18
0.3548	303.15	991.06
0.4110	303.15	974.15
0.4696	303.15	956.06
0.5084	303.15	943.78
0.5566	303.15	928.29
0.6053	303.15	912.34
0.6666	303.15	891.91
0.7114	303.15	876.87
0.7688	303.15	857.32
0.8081	303.15	843.81
0.8510	303.15	828.78
0.9009	303.15	810.84
0.9502	303.15	792.31
0.9771	303.15	781.49
1.0000	303.15	771.89
0.0000	308.15	1086.41
0.0249	308.15	1079.37
0.0518	308.15	1071.78
0.0759	308.15	1065.2
0.1079	308.15	1056.33
0.1570	308.15	1042.6
0.1998	308.15	1030.53
0.2609	308.15	1013.06
0.3034	308.15	1000.71
0.3548	308.15	985.53
0.4110	308.15	968.53
0.4696	308.15	950.36
0.5084	308.15	938.05
0.5566	308.15	922.51
0.6053	308.15	906.49
0.6666	308.15	886.05
0.7114	308.15	870.94
0.7688	308.15	851.38
0.8081	308.15	837.89
0.8510	308.15	822.79
0.9009	308.15	804.79
0.9502	308.15	786.06
0.9771	308.15	775.12
1.0000	308.15	765.46
0.0000	313.15	1081.59
0.0249	313.15	1074.57
0.0518	313.15	1066.98
0.0759	313.15	1060.43
0.1079	313.15	1051.61
0.1570	313.15	1037.81
0.1998	313.15	1025.77
0.2609	313.15	1008.31
0.3034	313.15	995.97
0.3548	313.15	980.82
0.4110	313.15	963.81
0.4696	313.15	945.65
0.5084	313.15	933.36
0.5566	313.15	917.82
0.6053	313.15	901.86
0.6666	313.15	881.45
0.7114	313.15	866.39
0.7688	313.15	846.81
0.8081	313.15	833.37
0.8510	313.15	818.29
0.9009	313.15	800.34
0.9502	313.15	781.54
0.9771	313.15	770.53
1.0000	313.15	760.86
0.0000	318.15	1076.46
0.0249	318.15	1069.43
0.0518	318.15	1061.81
0.0759	318.15	1055.25
0.1079	318.15	1046.39
0.1570	318.15	1032.57
0.1998	318.15	1020.45
0.2609	318.15	1002.91
0.3034	318.15	990.54
0.3548	318.15	975.32
0.4110	318.15	958.25
0.4696	318.15	940.03
0.5084	318.15	927.72
0.5566	318.15	912.19
0.6053	318.15	896.19
0.6666	318.15	875.79
0.7114	318.15	860.68
0.7688	318.15	841.15
0.8081	318.15	827.59
0.8510	318.15	812.61
0.9009	318.15	794.64
0.9502	318.15	775.55
0.9771	318.15	764.46
1.0000	318.15	754.76

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Dimethyl Sulfoxide (2) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0995	1299.53
303.15	0.0995	1280.08
308.15	0.0995	1260.6
313.15	0.0995	1241.15
318.15	0.0995	1221.75
323.15	0.0995	1202.37
303.15	0.2061	1303.77
298.15	0.2061	1322.57
308.15	0.2061	1284.95
313.15	0.2061	1266.14
318.15	0.2061	1247.36
323.15	0.2061	1228.62
303.15	0.2936	1327.8
308.15	0.2936	1309.93
298.15	0.2936	1346.2
313.15	0.2936	1290.99
318.15	0.2936	1272.67
323.15	0.2936	1254.35
308.15	0.4055	1336.21
303.15	0.4055	1354.11
313.15	0.4055	1318.82
298.15	0.4055	1372.01
318.15	0.4055	1300.48
323.15	0.4055	1282.68
313.15	0.5051	1342.48
308.15	0.5051	1359.99
303.15	0.5051	1377.53
318.15	0.5051	1325.02
298.15	0.5051	1395.1
323.15	0.5051	1307.59
313.15	0.6001	1364.06
308.15	0.6001	1381.26
318.15	0.6001	1346.87
298.15	0.6001	1415.77
303.15	0.6001	1398.51
323.15	0.6001	1329.74
298.15	0.7006	1439.25
303.15	0.7006	1422.21
318.15	0.7006	1371.16
313.15	0.7006	1388.0
308.15	0.7006	1405.15
323.15	0.7006	1354.25
308.15	0.8072	1427.02
318.15	0.8072	1393.45
298.15	0.8072	1460.77
303.15	0.8072	1443.88
313.15	0.8072	1410.29
323.15	0.8072	1376.76
298.15	0.8947	1480.86
308.15	0.8947	1447.24
303.15	0.8947	1464.04
313.15	0.8947	1431.0
318.15	0.8947	1413.84
323.15	0.8947	1397.24
318.15	1.0000	1423.3
303.15	1.0000	1473.57
298.15	1.0000	1490.47
313.15	1.0000	1439.99
308.15	1.0000	1456.77
323.15	1.0000	1406.7

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Dimethyl Sulfoxide (2) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0995	1299.53
303.15	0.0995	1280.08
308.15	0.0995	1260.6
313.15	0.0995	1241.15
318.15	0.0995	1221.75
323.15	0.0995	1202.37
303.15	0.2061	1303.77
298.15	0.2061	1322.57
308.15	0.2061	1284.95
313.15	0.2061	1266.14
318.15	0.2061	1247.36
323.15	0.2061	1228.62
303.15	0.2936	1327.8
308.15	0.2936	1309.93
298.15	0.2936	1346.2
313.15	0.2936	1290.99
318.15	0.2936	1272.67
323.15	0.2936	1254.35
308.15	0.4055	1336.21
303.15	0.4055	1354.11
313.15	0.4055	1318.82
298.15	0.4055	1372.01
318.15	0.4055	1300.48
323.15	0.4055	1282.68
313.15	0.5051	1342.48
308.15	0.5051	1359.99
303.15	0.5051	1377.53
318.15	0.5051	1325.02
298.15	0.5051	1395.1
323.15	0.5051	1307.59
313.15	0.6001	1364.06
308.15	0.6001	1381.26
318.15	0.6001	1346.87
298.15	0.6001	1415.77
303.15	0.6001	1398.51
323.15	0.6001	1329.74
298.15	0.7006	1439.25
303.15	0.7006	1422.21
318.15	0.7006	1371.16
313.15	0.7006	1388.0
308.15	0.7006	1405.15
323.15	0.7006	1354.25
308.15	0.8072	1427.02
318.15	0.8072	1393.45
298.15	0.8072	1460.77
303.15	0.8072	1443.88
313.15	0.8072	1410.29
323.15	0.8072	1376.76
298.15	0.8947	1480.86
308.15	0.8947	1447.24
303.15	0.8947	1464.04
313.15	0.8947	1431.0
318.15	0.8947	1413.84
323.15	0.8947	1397.24
318.15	1.0000	1423.3
303.15	1.0000	1473.57
298.15	1.0000	1490.47
313.15	1.0000	1439.99
308.15	1.0000	1456.77
323.15	1.0000	1406.7

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetonitrile (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0295	439.01
0.0603	421.43
0.0911	409.64
0.1215	400.63
0.1801	389.11
0.2123	384.56
0.2556	379.48
0.2803	376.98
0.3314	372.81
0.3727	370.01
0.4237	367.35
0.5032	363.87
0.5319	362.92
0.5800	361.58
0.6331	360.32
0.7000	358.99
0.7222	358.62
0.7918	357.61
0.8309	357.11
0.8876	356.45
0.9204	356.01
0.9700	355.29

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetonitrile (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	463.45
0.0340	455.42
0.0790	441.73
0.1350	424.08
0.1690	415.37
0.2140	406.38
0.2580	399.60
0.2920	395.50
0.3370	390.92
0.3820	387.04
0.4160	384.46
0.5060	378.42
0.5840	373.77
0.6290	371.26
0.6740	368.85
0.7190	366.53
0.7980	362.68
0.8430	360.64
0.9130	357.83
0.9660	355.75
1.0000	354.75

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetonitrile (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0295	439.01
0.0603	421.43
0.0911	409.64
0.1215	400.63
0.1801	389.11
0.2123	384.56
0.2556	379.48
0.2803	376.98
0.3314	372.81
0.3727	370.01
0.4237	367.35
0.5032	363.87
0.5319	362.92
0.5800	361.58
0.6331	360.32
0.7000	358.99
0.7222	358.62
0.7918	357.61
0.8309	357.11
0.8876	356.45
0.9204	356.01
0.9700	355.29

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetonitrile (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	463.45
0.0340	455.42
0.0790	441.73
0.1350	424.08
0.1690	415.37
0.2140	406.38
0.2580	399.60
0.2920	395.50
0.3370	390.92
0.3820	387.04
0.4160	384.46
0.5060	378.42
0.5840	373.77
0.6290	371.26
0.6740	368.85
0.7190	366.53
0.7980	362.68
0.8430	360.64
0.9130	357.83
0.9660	355.75
1.0000	354.75

Sources

• Conductometric study of some alkali metal halides in (dimethyl sulfoxide + acetonitrile) at T = 298.15 K
• Excess Molar Volumes, Excess Molar Isentropic Compressibilities, Viscosity Deviations, and Activation Parameters for 1-Ethyl-3-methyl-imidazolium Trifluoro-methanesulfonate + Dimethyl Sulfoxide and/or Acetonitrile at T = 298.15 to 323.15 K and P = 0.1 MPa
• Vapor-Liquid Equilibria for the Ternary System Acetonitrile + 1-Propanol + Dimethyl Sulfoxide and the Corresponding Binary Systems at 101.3 kPa
• Isobaric Vapor Liquid Equilibrium for the Extractive Distillation of Acetonitrile + Water Mixtures Using Dimethyl Sulfoxide at 101.3 kPa
• Densities and Volumetric Properties of Binary and Ternary Liquid Mixtures of Water (1) + Acetonitrile (2) + Dimethyl Sulfoxide (3) at Temperatures from (293.15 to 333.15) K and at Ambient Pressure (81.5 kPa)
• Density and Viscosity of Anhydrous Mixtures of Dimethylsulfoxide with Acetonitrile in the Range (298.15 to 318.15) K