Datasets
-
Activity coefficient (4)
-
Mole fraction (10)
-
Cp,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
-
η - Viscosity, Pa*s (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
n0 - Refractive index (Na D-line) (2)
-
ρl - Mass density, kg/m3 (10)
-
csound,fluid - Speed of Sound, m/s (4)
-
γ - Surface tension liquid-gas, N/m (4)
-
Tboil - Boiling temperature at pressure P, K (10)
-
Vapor Liquid Equilibrium at Constant Pressure (3)
-
Azeotropic temperature, K (2)
-
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