Mixture of Acetonitrile + Water

Datasets

1. Activity coefficient (4)
2. Mole fraction (10)
3. C_p,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
4. η - Viscosity, Pa*s (2)
5. P_vap - Vapor or sublimation pressure, kPa (2)
6. n₀ - Refractive index (Na D-line) (2)
7. ρ_l - Mass density, kg/m3 (10)
8. c_sound,fluid - Speed of Sound, m/s (4)
9. γ - Surface tension liquid-gas, N/m (4)
10. T_boil - Boiling temperature at pressure P, K (10)
11. Vapor Liquid Equilibrium at Constant Pressure (3)
12. Azeotropic temperature, K (2)
13. Excess molar volume, m3/mol (2)

Activity coefficient of Acetonitrile (1) [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Mole fraction = 0 (Liquid)

Activity coefficient of Acetonitrile (1) - Liquid
12.04
11.81

Activity coefficient of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Water (2) - Liquid	Activity coefficient of Water (2) - Liquid
298.15	0.0000	8.19

Activity coefficient of Acetonitrile (1) [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Mole fraction = 0 (Liquid)

Activity coefficient of Acetonitrile (1) - Liquid
12.04
11.81

Activity coefficient of Water (2) [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Water (2) - Liquid	Activity coefficient of Water (2) - Liquid
298.15	0.0000	8.19

Mole fraction of Acetonitrile (1) [ref]

Operational condition: Pressure, kPa = 102.5 (Liquid)

Mole fraction of Acetonitrile (1) - Liquid	Mole fraction of Acetonitrile (1) - Gas
0.0420	0.4311
0.1872	0.6329
0.2815	0.6480
0.3901	0.6550
0.4897	0.6620
0.5955	0.6662
0.7024	0.6888
0.7992	0.7260
0.9266	0.8181

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
0.0102	0.0628
0.0433	0.4445
0.0739	0.5218
0.1228	0.5592
0.2632	0.6282
0.3754	0.6421
0.4889	0.6535
0.5935	0.6669
0.6962	0.6939
0.7792	0.7258
0.8596	0.7741
0.9549	0.9015
1.0000	1.0000

Henry's Law constant (molality scale), kPa*kg/mol of Acetonitrile (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Henry's Law constant (molality scale), kPa*kg/mol of Acetonitrile (1) - Liquid
274.15	0.2101
294.65	1.4114
294.65	1.546
296.15	1.6992
310.15	5.3649
320.15	12.648
331.15	6.1692

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
0.0120	0.1760
0.0170	0.2260
0.0280	0.3190
0.0490	0.3910
0.0610	0.4530
0.0900	0.5030
0.1110	0.5470
0.1610	0.5780
0.1870	0.5930
0.3550	0.6120
0.6540	0.6370
0.7290	0.6920
0.8850	0.7970
0.9160	0.8330
0.9390	0.8570
0.9470	0.8800
0.9510	0.9010
0.9670	0.9250
0.9820	0.9640
1.0000	1.0000

Azeotropic composition: mole fraction of Acetonitrile (1) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of Acetonitrile (1) - Liquid
101.30	0.7140

Mole fraction of Acetonitrile (1) [ref]

Operational condition: Pressure, kPa = 102.5 (Liquid)

Mole fraction of Acetonitrile (1) - Liquid	Mole fraction of Acetonitrile (1) - Gas
0.0420	0.4311
0.1872	0.6329
0.2815	0.6480
0.3901	0.6550
0.4897	0.6620
0.5955	0.6662
0.7024	0.6888
0.7992	0.7260
0.9266	0.8181

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
0.0102	0.0628
0.0433	0.4445
0.0739	0.5218
0.1228	0.5592
0.2632	0.6282
0.3754	0.6421
0.4889	0.6535
0.5935	0.6669
0.6962	0.6939
0.7792	0.7258
0.8596	0.7741
0.9549	0.9015
1.0000	1.0000

Henry's Law constant (molality scale), kPa*kg/mol of Acetonitrile (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Henry's Law constant (molality scale), kPa*kg/mol of Acetonitrile (1) - Liquid
274.15	0.2101
294.65	1.4114
294.65	1.546
296.15	1.6992
310.15	5.3649
320.15	12.648
331.15	6.1692

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
0.0120	0.1760
0.0170	0.2260
0.0280	0.3190
0.0490	0.3910
0.0610	0.4530
0.0900	0.5030
0.1110	0.5470
0.1610	0.5780
0.1870	0.5930
0.3550	0.6120
0.6540	0.6370
0.7290	0.6920
0.8850	0.7970
0.9160	0.8330
0.9390	0.8570
0.9470	0.8800
0.9510	0.9010
0.9670	0.9250
0.9820	0.9640
1.0000	1.0000

Azeotropic composition: mole fraction of Acetonitrile (1) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of Acetonitrile (1) - Liquid
101.30	0.7140

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Acetonitrile (1) - Liquid	Temperature, K - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
0.0000	283.15	75.52
0.0000	298.15	75.29
0.0000	313.15	75.27
0.0000	328.15	75.34
0.0112	283.15	76.78
0.0112	298.15	76.64
0.0112	313.15	76.74
0.0112	328.15	76.89
0.0194	283.15	77.58
0.0194	298.15	77.54
0.0194	313.15	77.70
0.0194	328.15	77.90
0.0286	283.15	78.38
0.0286	298.15	78.45
0.0286	313.15	78.67
0.0286	328.15	78.89
0.0383	283.15	79.10
0.0383	298.15	79.27
0.0383	313.15	79.51
0.0383	328.15	79.77
0.0497	283.15	79.91
0.0497	298.15	80.02
0.0497	313.15	80.18
0.0497	328.15	80.51
0.0611	283.15	80.52
0.0611	298.15	80.57
0.0611	313.15	80.80
0.0611	328.15	81.00
0.0702	283.15	80.89
0.0702	298.15	80.95
0.0702	313.15	81.21
0.0702	328.15	81.46
0.0804	283.15	81.26
0.0804	298.15	81.33
0.0804	313.15	81.57
0.0804	328.15	81.90
0.0910	283.15	81.66
0.0910	298.15	81.73
0.0910	313.15	81.99
0.0910	328.15	82.33
0.1007	283.15	81.99
0.1007	298.15	82.06
0.1007	313.15	82.36
0.1007	328.15	82.70
0.2124	283.15	85.36
0.2124	298.15	85.66
0.2124	313.15	86.24
0.2124	328.15	86.82
0.3063	283.15	87.72
0.3063	298.15	88.31
0.3063	313.15	89.08
0.3063	328.15	89.92
0.3987	283.15	89.89
0.3987	298.15	90.70
0.3987	313.15	91.59
0.3987	328.15	92.56
0.4856	283.15	91.57
0.4856	298.15	92.38
0.4856	313.15	93.42
0.4856	328.15	94.38
0.6011	283.15	93.03
0.6011	298.15	93.96
0.6011	313.15	94.89
0.6011	328.15	95.86
0.7107	283.15	93.70
0.7107	298.15	94.44
0.7107	313.15	95.33
0.7107	328.15	96.16
0.8024	283.15	93.56
0.8024	298.15	94.16
0.8024	313.15	94.79
0.8024	328.15	95.62
0.9005	283.15	92.77
0.9005	298.15	93.28
0.9005	313.15	93.87
0.9005	328.15	94.55
0.9091	283.15	92.66
0.9091	298.15	93.17
0.9091	313.15	93.75
0.9091	328.15	94.42
0.9203	283.15	92.52
0.9203	298.15	93.01
0.9203	313.15	93.59
0.9203	328.15	94.24
0.9316	283.15	92.36
0.9316	298.15	92.85
0.9316	313.15	93.41
0.9316	328.15	94.06
0.9402	283.15	92.25
0.9402	298.15	92.73
0.9402	313.15	93.29
0.9402	328.15	93.94
0.9496	283.15	92.11
0.9496	298.15	92.59
0.9496	313.15	93.14
0.9496	328.15	93.77
0.9604	283.15	91.94
0.9604	298.15	92.40
0.9604	313.15	92.95
0.9604	328.15	93.58
0.9711	283.15	91.77
0.9711	298.15	92.22
0.9711	313.15	92.76
0.9711	328.15	93.38
0.9803	283.15	91.61
0.9803	298.15	92.06
0.9803	313.15	92.59
0.9803	328.15	93.21
0.9910	283.15	91.42
0.9910	298.15	91.87
0.9910	313.15	92.39
0.9910	328.15	93.00
1.0000	283.15	91.25
1.0000	298.15	91.69
1.0000	313.15	92.21
1.0000	328.15	92.82

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Acetonitrile (1) - Liquid	Temperature, K - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
0.0000	283.15	75.52
0.0000	298.15	75.29
0.0000	313.15	75.27
0.0000	328.15	75.34
0.0112	283.15	76.78
0.0112	298.15	76.64
0.0112	313.15	76.74
0.0112	328.15	76.89
0.0194	283.15	77.58
0.0194	298.15	77.54
0.0194	313.15	77.70
0.0194	328.15	77.90
0.0286	283.15	78.38
0.0286	298.15	78.45
0.0286	313.15	78.67
0.0286	328.15	78.89
0.0383	283.15	79.10
0.0383	298.15	79.27
0.0383	313.15	79.51
0.0383	328.15	79.77
0.0497	283.15	79.91
0.0497	298.15	80.02
0.0497	313.15	80.18
0.0497	328.15	80.51
0.0611	283.15	80.52
0.0611	298.15	80.57
0.0611	313.15	80.80
0.0611	328.15	81.00
0.0702	283.15	80.89
0.0702	298.15	80.95
0.0702	313.15	81.21
0.0702	328.15	81.46
0.0804	283.15	81.26
0.0804	298.15	81.33
0.0804	313.15	81.57
0.0804	328.15	81.90
0.0910	283.15	81.66
0.0910	298.15	81.73
0.0910	313.15	81.99
0.0910	328.15	82.33
0.1007	283.15	81.99
0.1007	298.15	82.06
0.1007	313.15	82.36
0.1007	328.15	82.70
0.2124	283.15	85.36
0.2124	298.15	85.66
0.2124	313.15	86.24
0.2124	328.15	86.82
0.3063	283.15	87.72
0.3063	298.15	88.31
0.3063	313.15	89.08
0.3063	328.15	89.92
0.3987	283.15	89.89
0.3987	298.15	90.70
0.3987	313.15	91.59
0.3987	328.15	92.56
0.4856	283.15	91.57
0.4856	298.15	92.38
0.4856	313.15	93.42
0.4856	328.15	94.38
0.6011	283.15	93.03
0.6011	298.15	93.96
0.6011	313.15	94.89
0.6011	328.15	95.86
0.7107	283.15	93.70
0.7107	298.15	94.44
0.7107	313.15	95.33
0.7107	328.15	96.16
0.8024	283.15	93.56
0.8024	298.15	94.16
0.8024	313.15	94.79
0.8024	328.15	95.62
0.9005	283.15	92.77
0.9005	298.15	93.28
0.9005	313.15	93.87
0.9005	328.15	94.55
0.9091	283.15	92.66
0.9091	298.15	93.17
0.9091	313.15	93.75
0.9091	328.15	94.42
0.9203	283.15	92.52
0.9203	298.15	93.01
0.9203	313.15	93.59
0.9203	328.15	94.24
0.9316	283.15	92.36
0.9316	298.15	92.85
0.9316	313.15	93.41
0.9316	328.15	94.06
0.9402	283.15	92.25
0.9402	298.15	92.73
0.9402	313.15	93.29
0.9402	328.15	93.94
0.9496	283.15	92.11
0.9496	298.15	92.59
0.9496	313.15	93.14
0.9496	328.15	93.77
0.9604	283.15	91.94
0.9604	298.15	92.40
0.9604	313.15	92.95
0.9604	328.15	93.58
0.9711	283.15	91.77
0.9711	298.15	92.22
0.9711	313.15	92.76
0.9711	328.15	93.38
0.9803	283.15	91.61
0.9803	298.15	92.06
0.9803	313.15	92.59
0.9803	328.15	93.21
0.9910	283.15	91.42
0.9910	298.15	91.87
0.9910	313.15	92.39
0.9910	328.15	93.00
1.0000	283.15	91.25
1.0000	298.15	91.69
1.0000	313.15	92.21
1.0000	328.15	92.82

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetonitrile (1) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0009
298.15	0.0510	0.0010
298.15	0.1169	0.0010
298.15	0.1971	0.0009
298.15	0.2728	0.0008
298.15	0.3601	0.0007
298.15	0.4417	0.0006
298.15	0.5204	0.0005
298.15	0.6012	0.0005
298.15	0.6671	0.0004
298.15	0.7398	0.0004
298.15	0.8253	0.0004
298.15	0.8860	0.0004
298.15	0.9389	0.0003
298.15	0.9990	0.0003
298.15	1.0000	0.0003
303.15	0.0000	0.0008
303.15	0.0510	0.0009
303.15	0.1169	0.0009
303.15	0.1971	0.0008
303.15	0.2728	0.0007
303.15	0.3601	0.0006
303.15	0.4417	0.0006
303.15	0.5204	0.0005
303.15	0.6012	0.0004
303.15	0.6671	0.0004
303.15	0.7398	0.0004
303.15	0.8253	0.0004
303.15	0.8860	0.0003
303.15	0.9389	0.0003
303.15	0.9990	0.0003
303.15	1.0000	0.0003
308.15	0.0000	0.0007
308.15	0.0510	0.0008
308.15	0.1169	0.0008
308.15	0.1971	0.0007
308.15	0.2728	0.0007
308.15	0.3601	0.0006
308.15	0.4417	0.0005
308.15	0.5204	0.0005
308.15	0.6012	0.0004
308.15	0.6671	0.0004
308.15	0.7398	0.0004
308.15	0.8253	0.0003
308.15	0.8860	0.0003
308.15	0.9389	0.0003
308.15	0.9990	0.0003
308.15	1.0000	0.0003
313.15	0.0000	0.0007
313.15	0.0510	0.0007
313.15	0.1169	0.0007
313.15	0.1971	0.0007
313.15	0.2728	0.0006
313.15	0.3601	0.0005
313.15	0.4417	0.0005
313.15	0.5204	0.0004
313.15	0.6012	0.0004
313.15	0.6671	0.0004
313.15	0.7398	0.0003
313.15	0.8253	0.0003
313.15	0.8860	0.0003
313.15	0.9389	0.0003
313.15	0.9990	0.0003
313.15	1.0000	0.0003
318.15	0.0000	0.0006
318.15	0.0510	0.0007
318.15	0.1169	0.0007
318.15	0.1971	0.0006
318.15	0.2728	0.0005
318.15	0.3601	0.0005
318.15	0.4417	0.0004
318.15	0.5204	0.0004
318.15	0.6012	0.0004
318.15	0.6671	0.0004
318.15	0.7398	0.0003
318.15	0.8253	0.0003
318.15	0.8860	0.0003
318.15	0.9389	0.0003
318.15	0.9990	0.0003
318.15	1.0000	0.0003

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetonitrile (1) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0009
298.15	0.0510	0.0010
298.15	0.1169	0.0010
298.15	0.1971	0.0009
298.15	0.2728	0.0008
298.15	0.3601	0.0007
298.15	0.4417	0.0006
298.15	0.5204	0.0005
298.15	0.6012	0.0005
298.15	0.6671	0.0004
298.15	0.7398	0.0004
298.15	0.8253	0.0004
298.15	0.8860	0.0004
298.15	0.9389	0.0003
298.15	0.9990	0.0003
298.15	1.0000	0.0003
303.15	0.0000	0.0008
303.15	0.0510	0.0009
303.15	0.1169	0.0009
303.15	0.1971	0.0008
303.15	0.2728	0.0007
303.15	0.3601	0.0006
303.15	0.4417	0.0006
303.15	0.5204	0.0005
303.15	0.6012	0.0004
303.15	0.6671	0.0004
303.15	0.7398	0.0004
303.15	0.8253	0.0004
303.15	0.8860	0.0003
303.15	0.9389	0.0003
303.15	0.9990	0.0003
303.15	1.0000	0.0003
308.15	0.0000	0.0007
308.15	0.0510	0.0008
308.15	0.1169	0.0008
308.15	0.1971	0.0007
308.15	0.2728	0.0007
308.15	0.3601	0.0006
308.15	0.4417	0.0005
308.15	0.5204	0.0005
308.15	0.6012	0.0004
308.15	0.6671	0.0004
308.15	0.7398	0.0004
308.15	0.8253	0.0003
308.15	0.8860	0.0003
308.15	0.9389	0.0003
308.15	0.9990	0.0003
308.15	1.0000	0.0003
313.15	0.0000	0.0007
313.15	0.0510	0.0007
313.15	0.1169	0.0007
313.15	0.1971	0.0007
313.15	0.2728	0.0006
313.15	0.3601	0.0005
313.15	0.4417	0.0005
313.15	0.5204	0.0004
313.15	0.6012	0.0004
313.15	0.6671	0.0004
313.15	0.7398	0.0003
313.15	0.8253	0.0003
313.15	0.8860	0.0003
313.15	0.9389	0.0003
313.15	0.9990	0.0003
313.15	1.0000	0.0003
318.15	0.0000	0.0006
318.15	0.0510	0.0007
318.15	0.1169	0.0007
318.15	0.1971	0.0006
318.15	0.2728	0.0005
318.15	0.3601	0.0005
318.15	0.4417	0.0004
318.15	0.5204	0.0004
318.15	0.6012	0.0004
318.15	0.6671	0.0004
318.15	0.7398	0.0003
318.15	0.8253	0.0003
318.15	0.8860	0.0003
318.15	0.9389	0.0003
318.15	0.9990	0.0003
318.15	1.0000	0.0003

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetonitrile (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
298.15	0.0200	5.49
298.15	0.0500	8.40
298.15	0.1000	11.13
298.15	0.2000	12.44
298.15	0.3000	12.66
298.15	0.4000	12.70
298.15	0.5000	12.75
298.15	0.6500	12.79
298.15	0.7500	12.90
298.15	0.8500	12.80
298.15	0.9500	12.26
323.15	0.0200	18.62
323.15	0.0500	27.00
323.15	0.1000	32.27
323.15	0.2000	35.89
323.15	0.3000	36.79
323.15	0.4000	37.46
323.15	0.5000	37.60
323.15	0.6500	37.99
323.15	0.7500	38.12
323.15	0.8500	37.63
323.15	0.9500	35.34

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetonitrile (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
298.15	0.0200	5.49
298.15	0.0500	8.40
298.15	0.1000	11.13
298.15	0.2000	12.44
298.15	0.3000	12.66
298.15	0.4000	12.70
298.15	0.5000	12.75
298.15	0.6500	12.79
298.15	0.7500	12.90
298.15	0.8500	12.80
298.15	0.9500	12.26
323.15	0.0200	18.62
323.15	0.0500	27.00
323.15	0.1000	32.27
323.15	0.2000	35.89
323.15	0.3000	36.79
323.15	0.4000	37.46
323.15	0.5000	37.60
323.15	0.6500	37.99
323.15	0.7500	38.12
323.15	0.8500	37.63
323.15	0.9500	35.34

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mass fraction of Acetonitrile (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0477	1.3404
0.0473	1.3425

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mass fraction of Acetonitrile (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0477	1.3404
0.0473	1.3425

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetonitrile (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	997.05
298.15	0.0510	978.98
298.15	0.1169	954.73
298.15	0.1971	924.74
298.15	0.2728	900.14
298.15	0.3601	876.35
298.15	0.4417	857.17
298.15	0.5204	841.27
298.15	0.6012	826.9
298.15	0.6671	816.3
298.15	0.7398	805.64
298.15	0.8253	794.81
298.15	0.8860	787.78
298.15	0.9389	782.44
298.15	1.0000	776.69
303.15	0.0000	995.65
303.15	0.0510	975.65
303.15	0.1169	951.24
303.15	0.1971	921.1
303.15	0.2728	896.29
303.15	0.3601	872.19
303.15	0.4417	852.79
303.15	0.5204	836.65
303.15	0.6012	822.15
303.15	0.6671	811.49
303.15	0.7398	800.78
303.15	0.8253	789.89
303.15	0.8860	782.84
303.15	0.9389	777.52
303.15	1.0000	771.89
308.15	0.0000	994.03
308.15	0.0510	972.14
308.15	0.1169	947.08
308.15	0.1971	916.51
308.15	0.2728	891.33
308.15	0.3601	866.86
308.15	0.4417	846.98
308.15	0.5204	830.76
308.15	0.6012	816.07
308.15	0.6671	805.22
308.15	0.7398	794.39
308.15	0.8253	783.52
308.15	0.8860	776.44
308.15	0.9389	771.07
308.15	1.0000	765.46
313.15	0.0000	992.22
313.15	0.0510	969.11
313.15	0.1169	943.32
313.15	0.1971	912.69
313.15	0.2728	887.31
313.15	0.3601	862.67
313.15	0.4417	842.61
313.15	0.5204	826.18
313.15	0.6012	811.38
313.15	0.6671	800.45
313.15	0.7398	789.71
313.15	0.8253	778.81
313.15	0.8860	771.75
313.15	0.9389	766.36
313.15	1.0000	760.86
318.15	0.0000	990.21
318.15	0.0510	965.89
318.15	0.1169	939.05
318.15	0.1971	908.03
318.15	0.2728	882.39
318.15	0.3601	857.41
318.15	0.4417	837.06
318.15	0.5204	820.41
318.15	0.6012	805.44
318.15	0.6671	794.36
318.15	0.7398	783.69
318.15	0.8253	772.68
318.15	0.8860	765.67
318.15	0.9389	760.29
318.15	1.0000	754.76

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 279.15 (Liquid)

Mole fraction of Acetonitrile (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	999.9
0.0530	986.6
0.0910	974.3
0.1460	955.5
0.1870	941.9
0.2960	909.5
0.3760	888.4
0.5180	859.0
0.6920	831.5
0.8890	807.2

Mass density, kg/m3 [ref]

Operational conditions:

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

Molality, mol/kg of Water (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	776.389
0.1197	776.819
0.1729	777.019
0.2244	777.174
0.2674	777.435
0.3192	777.518
0.4188	777.923
0.5198	778.218
0.6210	778.584
0.7217	778.921
0.8212	779.276
0.9205	779.631
1.0198	779.949

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mass fraction of Acetonitrile (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.1000	293.15	983.2
0.2000	293.15	964.2
0.4000	293.15	918.7
0.1000	303.15	978.7
0.2000	303.15	958.2
0.4000	303.15	910.9
0.1000	313.15	973.5
0.2000	313.15	951.6
0.4000	313.15	902.8

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 81.5 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Water (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	781.97
293.15	0.0417	785.6
293.15	0.0833	789.62
293.15	0.1568	797.67
293.15	0.2095	804.01
293.15	0.3247	819.96
293.15	0.4127	834.27
293.15	0.4960	849.71
293.15	0.5704	864.78
293.15	0.6361	880.12
293.15	0.7201	902.94
293.15	0.7961	926.99
293.15	0.8788	956.73
293.15	0.9573	984.72
293.15	1.0000	998.2
303.15	0.0000	771.15
303.15	0.0417	774.79
303.15	0.0833	778.83
303.15	0.1568	786.95
303.15	0.2095	793.33
303.15	0.3247	809.63
303.15	0.4127	824.27
303.15	0.4960	840.11
303.15	0.5704	855.57
303.15	0.6361	871.32
303.15	0.7201	894.74
303.15	0.7961	919.47
303.15	0.8788	950.35
303.15	0.9573	980.43
303.15	1.0000	995.64
313.15	0.0000	760.2
313.15	0.0417	763.85
313.15	0.0833	767.91
313.15	0.1568	776.09
313.15	0.2095	782.6
313.15	0.3247	799.11
313.15	0.4127	814.05
313.15	0.4960	830.25
313.15	0.5704	846.08
313.15	0.6361	862.22
313.15	0.7201	886.22
313.15	0.7961	911.61
313.15	0.8788	943.52
313.15	0.9573	975.45
313.15	1.0000	992.21
323.15	0.0000	749.12
323.15	0.0417	752.77
323.15	0.0833	756.84
323.15	0.1568	765.06
323.15	0.2095	771.62
323.15	0.3247	788.38
323.15	0.4127	803.6
323.15	0.4960	820.14
323.15	0.5704	836.32
323.15	0.6361	852.82
323.15	0.7201	877.38
323.15	0.7961	903.39
323.15	0.8788	936.28
323.15	0.9573	969.87
323.15	1.0000	988.03
333.15	0.0000	737.87
333.15	0.0417	741.52
333.15	0.0833	745.6
333.15	0.1568	753.85
333.15	0.2095	760.47
333.15	0.3247	777.43
333.15	0.4127	792.91
333.15	0.4960	809.77
333.15	0.5704	826.29
333.15	0.6361	843.13
333.15	0.7201	868.22
333.15	0.7961	894.84
333.15	0.8788	928.67
333.15	0.9573	963.64
333.15	1.0000	983.19

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetonitrile (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	997.05
298.15	0.0510	978.98
298.15	0.1169	954.73
298.15	0.1971	924.74
298.15	0.2728	900.14
298.15	0.3601	876.35
298.15	0.4417	857.17
298.15	0.5204	841.27
298.15	0.6012	826.9
298.15	0.6671	816.3
298.15	0.7398	805.64
298.15	0.8253	794.81
298.15	0.8860	787.78
298.15	0.9389	782.44
298.15	1.0000	776.69
303.15	0.0000	995.65
303.15	0.0510	975.65
303.15	0.1169	951.24
303.15	0.1971	921.1
303.15	0.2728	896.29
303.15	0.3601	872.19
303.15	0.4417	852.79
303.15	0.5204	836.65
303.15	0.6012	822.15
303.15	0.6671	811.49
303.15	0.7398	800.78
303.15	0.8253	789.89
303.15	0.8860	782.84
303.15	0.9389	777.52
303.15	1.0000	771.89
308.15	0.0000	994.03
308.15	0.0510	972.14
308.15	0.1169	947.08
308.15	0.1971	916.51
308.15	0.2728	891.33
308.15	0.3601	866.86
308.15	0.4417	846.98
308.15	0.5204	830.76
308.15	0.6012	816.07
308.15	0.6671	805.22
308.15	0.7398	794.39
308.15	0.8253	783.52
308.15	0.8860	776.44
308.15	0.9389	771.07
308.15	1.0000	765.46
313.15	0.0000	992.22
313.15	0.0510	969.11
313.15	0.1169	943.32
313.15	0.1971	912.69
313.15	0.2728	887.31
313.15	0.3601	862.67
313.15	0.4417	842.61
313.15	0.5204	826.18
313.15	0.6012	811.38
313.15	0.6671	800.45
313.15	0.7398	789.71
313.15	0.8253	778.81
313.15	0.8860	771.75
313.15	0.9389	766.36
313.15	1.0000	760.86
318.15	0.0000	990.21
318.15	0.0510	965.89
318.15	0.1169	939.05
318.15	0.1971	908.03
318.15	0.2728	882.39
318.15	0.3601	857.41
318.15	0.4417	837.06
318.15	0.5204	820.41
318.15	0.6012	805.44
318.15	0.6671	794.36
318.15	0.7398	783.69
318.15	0.8253	772.68
318.15	0.8860	765.67
318.15	0.9389	760.29
318.15	1.0000	754.76

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 279.15 (Liquid)

Mole fraction of Acetonitrile (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	999.9
0.0530	986.6
0.0910	974.3
0.1460	955.5
0.1870	941.9
0.2960	909.5
0.3760	888.4
0.5180	859.0
0.6920	831.5
0.8890	807.2

Mass density, kg/m3 [ref]

Operational conditions:

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

Molality, mol/kg of Water (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	776.389
0.1197	776.819
0.1729	777.019
0.2244	777.174
0.2674	777.435
0.3192	777.518
0.4188	777.923
0.5198	778.218
0.6210	778.584
0.7217	778.921
0.8212	779.276
0.9205	779.631
1.0198	779.949

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mass fraction of Acetonitrile (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.1000	293.15	983.2
0.2000	293.15	964.2
0.4000	293.15	918.7
0.1000	303.15	978.7
0.2000	303.15	958.2
0.4000	303.15	910.9
0.1000	313.15	973.5
0.2000	313.15	951.6
0.4000	313.15	902.8

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 81.5 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Water (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	781.97
293.15	0.0417	785.6
293.15	0.0833	789.62
293.15	0.1568	797.67
293.15	0.2095	804.01
293.15	0.3247	819.96
293.15	0.4127	834.27
293.15	0.4960	849.71
293.15	0.5704	864.78
293.15	0.6361	880.12
293.15	0.7201	902.94
293.15	0.7961	926.99
293.15	0.8788	956.73
293.15	0.9573	984.72
293.15	1.0000	998.2
303.15	0.0000	771.15
303.15	0.0417	774.79
303.15	0.0833	778.83
303.15	0.1568	786.95
303.15	0.2095	793.33
303.15	0.3247	809.63
303.15	0.4127	824.27
303.15	0.4960	840.11
303.15	0.5704	855.57
303.15	0.6361	871.32
303.15	0.7201	894.74
303.15	0.7961	919.47
303.15	0.8788	950.35
303.15	0.9573	980.43
303.15	1.0000	995.64
313.15	0.0000	760.2
313.15	0.0417	763.85
313.15	0.0833	767.91
313.15	0.1568	776.09
313.15	0.2095	782.6
313.15	0.3247	799.11
313.15	0.4127	814.05
313.15	0.4960	830.25
313.15	0.5704	846.08
313.15	0.6361	862.22
313.15	0.7201	886.22
313.15	0.7961	911.61
313.15	0.8788	943.52
313.15	0.9573	975.45
313.15	1.0000	992.21
323.15	0.0000	749.12
323.15	0.0417	752.77
323.15	0.0833	756.84
323.15	0.1568	765.06
323.15	0.2095	771.62
323.15	0.3247	788.38
323.15	0.4127	803.6
323.15	0.4960	820.14
323.15	0.5704	836.32
323.15	0.6361	852.82
323.15	0.7201	877.38
323.15	0.7961	903.39
323.15	0.8788	936.28
323.15	0.9573	969.87
323.15	1.0000	988.03
333.15	0.0000	737.87
333.15	0.0417	741.52
333.15	0.0833	745.6
333.15	0.1568	753.85
333.15	0.2095	760.47
333.15	0.3247	777.43
333.15	0.4127	792.91
333.15	0.4960	809.77
333.15	0.5704	826.29
333.15	0.6361	843.13
333.15	0.7201	868.22
333.15	0.7961	894.84
333.15	0.8788	928.67
333.15	0.9573	963.64
333.15	1.0000	983.19

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 279.15 (Liquid)

Mole fraction of Acetonitrile (1) - Liquid	Speed of sound, m/s - Liquid
0.0000	1430.4
0.0530	1540.0
0.0910	1549.6
0.1460	1511.8
0.1870	1476.2
0.2960	1451.0
0.3760	1425.0
0.5180	1387.2
0.6920	1352.0
0.8890	1321.0

Speed of sound, m/s [ref]

Operational conditions:

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

Molality, mol/kg of Water (2) - Liquid	Speed of sound, m/s - Liquid
0.0000	1281.3
0.1197	1281.5
0.1729	1282.0
0.2244	1282.2
0.2674	1282.4
0.3192	1282.2
0.4188	1282.6
0.5198	1283.0
0.6210	1284.0
0.7217	1284.3
0.8212	1284.7
0.9205	1285.5
1.0198	1286.5

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 279.15 (Liquid)

Mole fraction of Acetonitrile (1) - Liquid	Speed of sound, m/s - Liquid
0.0000	1430.4
0.0530	1540.0
0.0910	1549.6
0.1460	1511.8
0.1870	1476.2
0.2960	1451.0
0.3760	1425.0
0.5180	1387.2
0.6920	1352.0
0.8890	1321.0

Speed of sound, m/s [ref]

Operational conditions:

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

Molality, mol/kg of Water (2) - Liquid	Speed of sound, m/s - Liquid
0.0000	1281.3
0.1197	1281.5
0.1729	1282.0
0.2244	1282.2
0.2674	1282.4
0.3192	1282.2
0.4188	1282.6
0.5198	1283.0
0.6210	1284.0
0.7217	1284.3
0.8212	1284.7
0.9205	1285.5
1.0198	1286.5

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

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetonitrile (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
283.15	0.0051	0.0706
283.15	0.0101	0.0672
283.15	0.0151	0.0644
283.15	0.0217	0.0612
283.15	0.0298	0.0580
283.15	0.0377	0.0554
283.15	0.0486	0.0523
283.15	0.0593	0.0495
283.15	0.0871	0.0445
283.15	0.1011	0.0423
283.15	0.1431	0.0380
283.15	0.1615	0.0355
283.15	0.1847	0.0343
283.15	0.2068	0.0339
283.15	0.2327	0.0335
283.15	0.3098	0.0329
283.15	0.3971	0.0326
283.15	0.4878	0.0323
283.15	0.6557	0.0321
283.15	0.8056	0.0313
283.15	0.9592	0.0298
298.15	0.0149	0.0624
298.15	0.0298	0.0559
298.15	0.0516	0.0494
298.15	0.0653	0.0460
298.15	0.0860	0.0422
298.15	0.0950	0.0405
298.15	0.1023	0.0396
298.15	0.1227	0.0380
298.15	0.1403	0.0364
298.15	0.1570	0.0357
298.15	0.1855	0.0340
298.15	0.1950	0.0341
298.15	0.2541	0.0329
298.15	0.3256	0.0323
298.15	0.3959	0.0317
298.15	0.4851	0.0314
298.15	0.5913	0.0309
298.15	0.6930	0.0304
298.15	0.7968	0.0295
308.15	0.0217	0.0605
308.15	0.0298	0.0590
308.15	0.0377	0.0556
308.15	0.0727	0.0481
308.15	0.0871	0.0458
308.15	0.1304	0.0401
308.15	0.1431	0.0388
308.15	0.1615	0.0369
308.15	0.1847	0.0357
308.15	0.2068	0.0339
308.15	0.2327	0.0335
308.15	0.3098	0.0310
308.15	0.3971	0.0301
308.15	0.4999	0.0291
308.15	0.6557	0.0284
308.15	0.7775	0.0282
308.15	0.9592	0.0280

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

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of Water (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.2032	0.0295
0.4087	0.0309
0.5149	0.0314
0.6041	0.0317
0.7459	0.0329
0.8145	0.0340
0.8773	0.0380
0.8977	0.0396
0.9050	0.0405
0.9484	0.0494
0.9702	0.0559
0.9851	0.0624

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

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetonitrile (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
283.15	0.0051	0.0706
283.15	0.0101	0.0672
283.15	0.0151	0.0644
283.15	0.0217	0.0612
283.15	0.0298	0.0580
283.15	0.0377	0.0554
283.15	0.0486	0.0523
283.15	0.0593	0.0495
283.15	0.0871	0.0445
283.15	0.1011	0.0423
283.15	0.1431	0.0380
283.15	0.1615	0.0355
283.15	0.1847	0.0343
283.15	0.2068	0.0339
283.15	0.2327	0.0335
283.15	0.3098	0.0329
283.15	0.3971	0.0326
283.15	0.4878	0.0323
283.15	0.6557	0.0321
283.15	0.8056	0.0313
283.15	0.9592	0.0298
298.15	0.0149	0.0624
298.15	0.0298	0.0559
298.15	0.0516	0.0494
298.15	0.0653	0.0460
298.15	0.0860	0.0422
298.15	0.0950	0.0405
298.15	0.1023	0.0396
298.15	0.1227	0.0380
298.15	0.1403	0.0364
298.15	0.1570	0.0357
298.15	0.1855	0.0340
298.15	0.1950	0.0341
298.15	0.2541	0.0329
298.15	0.3256	0.0323
298.15	0.3959	0.0317
298.15	0.4851	0.0314
298.15	0.5913	0.0309
298.15	0.6930	0.0304
298.15	0.7968	0.0295
308.15	0.0217	0.0605
308.15	0.0298	0.0590
308.15	0.0377	0.0556
308.15	0.0727	0.0481
308.15	0.0871	0.0458
308.15	0.1304	0.0401
308.15	0.1431	0.0388
308.15	0.1615	0.0369
308.15	0.1847	0.0357
308.15	0.2068	0.0339
308.15	0.2327	0.0335
308.15	0.3098	0.0310
308.15	0.3971	0.0301
308.15	0.4999	0.0291
308.15	0.6557	0.0284
308.15	0.7775	0.0282
308.15	0.9592	0.0280

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

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of Water (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.2032	0.0295
0.4087	0.0309
0.5149	0.0314
0.6041	0.0317
0.7459	0.0329
0.8145	0.0340
0.8773	0.0380
0.8977	0.0396
0.9050	0.0405
0.9484	0.0494
0.9702	0.0559
0.9851	0.0624

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 102.5 (Liquid)

Mole fraction of Acetonitrile (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0420	361.20
0.1872	352.00
0.2815	351.15
0.3901	350.67
0.4897	350.40
0.5955	349.95
0.7024	349.80
0.7992	350.00
0.9266	351.05

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	373.12
0.0102	371.72
0.0433	359.96
0.0739	356.73
0.1228	353.49
0.2632	351.08
0.3754	350.37
0.4889	350.02
0.5935	349.79
0.6962	349.64
0.7792	349.80
0.8596	350.52
0.9549	352.79
1.0000	354.68

Boiling temperature at pressure P, K [ref]

Operational condition: Mole fraction = 0.1 (Liquid)

Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
2120.00	481.15
3140.00	500.15
5610.00	528.15
8350.00	553.15
10290.00	569.15

Boiling temperature at pressure P, K [ref]

Operational condition: Mole fraction = 0.1 (Gas)

Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
2120.00	493.15
3140.00	512.65
5610.00	538.15
8350.00	562.15
10290.00	578.15

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	373.15
0.0120	367.56
0.0170	365.88
0.0280	363.15
0.0490	360.05
0.0610	358.09
0.0900	355.25
0.1110	353.91
0.1610	352.44
0.1870	351.95
0.3550	350.65
0.6540	349.95
0.7290	350.00
0.8850	350.77
0.9160	351.24
0.9390	351.88
0.9470	352.29
0.9510	352.75
0.9670	353.25
0.9820	353.91
1.0000	354.75

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 102.5 (Liquid)

Mole fraction of Acetonitrile (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0420	361.20
0.1872	352.00
0.2815	351.15
0.3901	350.67
0.4897	350.40
0.5955	349.95
0.7024	349.80
0.7992	350.00
0.9266	351.05

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	373.12
0.0102	371.72
0.0433	359.96
0.0739	356.73
0.1228	353.49
0.2632	351.08
0.3754	350.37
0.4889	350.02
0.5935	349.79
0.6962	349.64
0.7792	349.80
0.8596	350.52
0.9549	352.79
1.0000	354.68

Boiling temperature at pressure P, K [ref]

Operational condition: Mole fraction = 0.1 (Liquid)

Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
2120.00	481.15
3140.00	500.15
5610.00	528.15
8350.00	553.15
10290.00	569.15

Boiling temperature at pressure P, K [ref]

Operational condition: Mole fraction = 0.1 (Gas)

Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
2120.00	493.15
3140.00	512.65
5610.00	538.15
8350.00	562.15
10290.00	578.15

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	373.15
0.0120	367.56
0.0170	365.88
0.0280	363.15
0.0490	360.05
0.0610	358.09
0.0900	355.25
0.1110	353.91
0.1610	352.44
0.1870	351.95
0.3550	350.65
0.6540	349.95
0.7290	350.00
0.8850	350.77
0.9160	351.24
0.9390	351.88
0.9470	352.29
0.9510	352.75
0.9670	353.25
0.9820	353.91
1.0000	354.75

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Acetonitrile (1) - Liquid	y1[mol/mol] of Acetonitrile (1) - Vapour
359.65	0.0290	0.2630
354.25	0.0930	0.5050
353.15	0.1420	0.5590
351.75	0.2540	0.6170
350.55	0.4020	0.6550
349.85	0.5070	0.6640
349.75	0.5270	0.6730
349.15	0.7180	0.7280
349.75	0.8390	0.7800
349.95	0.8560	0.7610
353.55	0.9860	0.9450

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 20 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Acetonitrile (1) - Liquid	y1[mol/mol] of Acetonitrile (1) - Vapour
333.35	0.0000	0.0000
331.85	0.0030	0.0640
317.95	0.0520	0.5070
309.85	0.1680	0.7320
307.65	0.5130	0.8100
307.25	0.7720	0.8350
307.75	0.9000	0.8600
309.15	0.9550	0.9100
309.75	0.9800	0.9550
309.85	1.0000	1.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 40 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Acetonitrile (1) - Liquid	y1[mol/mol] of Acetonitrile (1) - Vapour
346.65	0.0080	0.1070
337.85	0.0300	0.4200
327.15	0.1180	0.6860
324.85	0.3110	0.7320
324.55	0.5200	0.7460
324.25	0.7000	0.7720
324.35	0.8600	0.8080
324.75	0.9140	0.8350
325.45	0.9800	0.9140
326.35	0.9900	0.9530

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid	Azeotropic temperature, K - Liquid
101.30	349.85

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid	Azeotropic temperature, K - Liquid
101.30	349.85

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Water (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.5970	-5.6100e-07
0.6510	-5.8100e-07
0.7080	-5.6600e-07
0.7570	-5.5800e-07
0.8540	-4.8900e-07
0.8990	-4.1300e-07

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Water (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.5970	-5.6100e-07
0.6510	-5.8100e-07
0.7080	-5.6600e-07
0.7570	-5.5800e-07
0.8540	-4.8900e-07
0.8990	-4.1300e-07

Sources

• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Measurement of activity coefficients at infinite dilution for acetonitrile, water, limonene, limonene epoxide and their binary pairs
• A model for excess volumes of salty water-acetonitrile mixtures at 298.15 K
• Salting-out effect of sodium, potassium, carbonate, sulfite, tartrate and thiosulfate ions on aqueous mixtures of acetonitrile or 1-methyl-2-pyrrolidone: A liquid-liquid equilibrium study
• Isobaric vapor-liquid equilibrium of ethanenitrile + water + 1,2-ethanediol + 1-ethyl-3-methylimidazolium chloride
• The (water + acetonitrile) mixture revisited: A new approach for calculating partial molar volumes
• Isothermal compressibility and internal pressure studies of some non-electrolytes in aqueous solutions at low temperatures
• Molar heat capacities of the (water + acetonitrile) mixtures at T = (283.15, 298.15, 313.15, and 328.15) K
• Surface tension of non-ideal binary and ternary liquid mixtures at various temperatures and p = 81.5 kPa
• Measurement and correlation of isobaric vapour-liquid equilibrium for the (acetonitrile + water) system containing different ionic liquids at atmospheric pressure
• Pressure-Drop Method for Detecting Bubble and Dew Points of Multicomponent Mixtures at Temperatures of up to 573 K
• Compressibility Studies of Binary Solutions Involving Water as a Solute in Nonaqueous Solvents at T ) 298.15 K
• Experimental Data and Correlation of Surface Tensions of the Binary and Ternary Systems of Water + Acetonitrile + 2-Propanol at 298.15 K and Atmospheric Pressure
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Apparent Molar Volumes of 1-Alkyl (n = 2, 4, 6)-3-methylimidazolium Bromides in a Mixed-Solvent Medium of Acetonitrile + Water at Temperatures of (293.15, 303.15, and 313.15) K
• 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)
• Vapor Pressures for the Acetonitrile + Tetrabutylammonium Bromide, Water + Tetrabutylammonium Bromide, and Acetonitrile + Water + Tetrabutylammonium Bromide Systems