Datasets
-
Activity coefficient (6)
-
Mole fraction (40)
-
η - Viscosity, Pa*s (2)
-
Excess molar enthalpy (molar enthalpy (2)
-
Pc - Critical pressure, kPa (2)
-
n0 - Refractive index (Na D-line) (4)
-
ρl - Mass density, kg/m3 (4)
-
γ - Surface tension liquid-gas, N/m (6)
-
Tc - Critical temperature, K (2)
-
Vapor Liquid Equilibrium at Constant Pressure (3)
Activity coefficient of Ethyl Acetate (1)
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0 (Liquid)
Temperature, K - Liquid |
Activity coefficient of Ethyl Acetate (1) - Liquid |
273.35 |
44.5 |
283.15 |
54.9 |
293.15 |
64.8 |
293.15 |
68.0 |
298.15 |
69.2 |
303.15 |
73.6 |
313.15 |
80.1 |
Activity coefficient of Ethyl Acetate (1)
[ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Mole fraction = 0 (Liquid)
Temperature, K - Liquid |
Activity coefficient of Ethyl Acetate (1) - Liquid |
303.25 |
76.5 |
313.25 |
85.0 |
323.25 |
90.1 |
333.25 |
94.7 |
343.25 |
96.2 |
Activity coefficient of Ethyl Acetate (1)
[ref]
Fixed |
Measured |
Mole fraction of Ethyl Acetate (1) - Liquid |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Activity coefficient of Ethyl Acetate (1) - Liquid |
0.0000 |
313.15 |
101.00 |
71.0 |
Activity coefficient of Ethyl Acetate (1)
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0 (Liquid)
Temperature, K - Liquid |
Activity coefficient of Ethyl Acetate (1) - Liquid |
273.35 |
44.5 |
283.15 |
54.9 |
293.15 |
64.8 |
293.15 |
68.0 |
298.15 |
69.2 |
303.15 |
73.6 |
313.15 |
80.1 |
Activity coefficient of Ethyl Acetate (1)
[ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Mole fraction = 0 (Liquid)
Temperature, K - Liquid |
Activity coefficient of Ethyl Acetate (1) - Liquid |
303.25 |
76.5 |
313.25 |
85.0 |
323.25 |
90.1 |
333.25 |
94.7 |
343.25 |
96.2 |
Activity coefficient of Ethyl Acetate (1)
[ref]
Fixed |
Measured |
Mole fraction of Ethyl Acetate (1) - Liquid |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Activity coefficient of Ethyl Acetate (1) - Liquid |
0.0000 |
313.15 |
101.00 |
71.0 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
283.15 |
0.1085 |
298.15 |
0.1280 |
313.15 |
0.1690 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 2 |
Mole fraction of Water (2) - Liquid mixture 2 |
283.15 |
0.9814 |
298.15 |
0.9858 |
313.15 |
0.9858 |
Mole fraction of Water (2)
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid mixture 1 |
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
101.32 |
298.20 |
0.9824 |
Mole fraction of Water (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 2 |
298.20 |
101.32 |
0.1323 |
Mole fraction of Ethyl Acetate (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Ethyl Acetate (1) - Liquid mixture 1 |
288.20 |
0.0194 |
303.20 |
0.0166 |
318.20 |
0.0142 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
288.20 |
0.1255 |
303.20 |
0.1492 |
318.20 |
0.1940 |
Mass fraction of Water (2)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid mixture 1)
- Pressure, kPa = 101 (Liquid mixture 1)
Mass fraction of Water (2) - Liquid mixture 1 |
0.0432 |
0.9160 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
95 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
293.20 |
0.1267 |
293.20 |
0.9828 |
313.20 |
0.1830 |
313.20 |
0.9837 |
Mole fraction of Ethyl Acetate (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethyl Acetate (1) - Liquid |
Mole fraction of Ethyl Acetate (1) - Gas |
308.15 |
0.0009 |
0.0390 |
308.15 |
0.0026 |
0.1320 |
308.15 |
0.0049 |
0.2510 |
308.15 |
0.0074 |
0.3050 |
308.15 |
0.0151 |
0.6940 |
308.15 |
0.8710 |
0.7710 |
308.15 |
0.9310 |
0.8870 |
308.15 |
0.9800 |
0.9610 |
323.15 |
0.0011 |
0.0460 |
323.15 |
0.0026 |
0.1090 |
323.15 |
0.0052 |
0.2380 |
323.15 |
0.0074 |
0.3150 |
323.15 |
0.0151 |
0.7780 |
323.15 |
0.8730 |
0.8780 |
323.15 |
0.9300 |
0.9280 |
323.15 |
0.9800 |
0.9820 |
343.15 |
0.0009 |
0.0340 |
343.15 |
0.0025 |
0.0940 |
343.15 |
0.0047 |
0.2000 |
343.15 |
0.0072 |
0.2460 |
343.15 |
0.0149 |
0.8290 |
343.15 |
0.8690 |
0.9230 |
343.15 |
0.9290 |
0.9480 |
343.15 |
0.9810 |
0.9860 |
Mole fraction of Ethyl Acetate (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 2)
Temperature, K - Liquid mixture 1 |
Mole fraction of Ethyl Acetate (1) - Liquid mixture 2 |
298.15 |
0.0139 |
318.15 |
0.0117 |
Mole fraction of Ethyl Acetate (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 2)
Temperature, K - Liquid mixture 1 |
Mole fraction of Ethyl Acetate (1) - Liquid mixture 1 |
298.15 |
0.8285 |
318.15 |
0.7946 |
Mass fraction of Water (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 2 |
308.20 |
101.30 |
0.0334 |
Mass fraction of Ethyl Acetate (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mass fraction of Ethyl Acetate (1) - Liquid mixture 1 |
308.20 |
101.30 |
0.0700 |
Mole fraction of Water (2)
[ref]
Operational conditions:
- Pressure, kPa = 101.3 (Liquid mixture 1)
- Temperature, K = 298 (Liquid mixture 1)
Mole fraction of Water (2) - Liquid mixture 1 |
0.9983 |
0.0299 |
Mole fraction of Ethyl Acetate (1)
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid mixture 1 |
Temperature, K - Liquid mixture 1 |
Mole fraction of Ethyl Acetate (1) - Liquid mixture 1 |
101.30 |
298.00 |
0.8468 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
298.15 |
0.9837 |
303.15 |
0.9845 |
308.15 |
0.9851 |
313.15 |
0.9856 |
318.15 |
0.9860 |
323.15 |
0.9863 |
328.15 |
0.9866 |
333.15 |
0.9867 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 2 |
298.15 |
0.1733 |
303.15 |
0.1885 |
308.15 |
0.1997 |
313.15 |
0.2111 |
318.15 |
0.2179 |
323.15 |
0.2259 |
328.15 |
0.2333 |
333.15 |
0.2414 |
Mole fraction of Water (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
293.20 |
101.33 |
0.9819 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
283.20 |
0.1120 |
323.20 |
0.1890 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 2 |
283.20 |
0.9810 |
323.20 |
0.9780 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
283.15 |
0.1085 |
298.15 |
0.1280 |
313.15 |
0.1690 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 2 |
Mole fraction of Water (2) - Liquid mixture 2 |
283.15 |
0.9814 |
298.15 |
0.9858 |
313.15 |
0.9858 |
Mole fraction of Water (2)
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid mixture 1 |
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
101.32 |
298.20 |
0.9824 |
Mole fraction of Water (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 2 |
298.20 |
101.32 |
0.1323 |
Mole fraction of Ethyl Acetate (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Ethyl Acetate (1) - Liquid mixture 1 |
288.20 |
0.0194 |
303.20 |
0.0166 |
318.20 |
0.0142 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
288.20 |
0.1255 |
303.20 |
0.1492 |
318.20 |
0.1940 |
Mass fraction of Water (2)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid mixture 1)
- Pressure, kPa = 101 (Liquid mixture 1)
Mass fraction of Water (2) - Liquid mixture 1 |
0.0432 |
0.9160 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
95 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
293.20 |
0.1267 |
293.20 |
0.9828 |
313.20 |
0.1830 |
313.20 |
0.9837 |
Mole fraction of Ethyl Acetate (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethyl Acetate (1) - Liquid |
Mole fraction of Ethyl Acetate (1) - Gas |
308.15 |
0.0009 |
0.0390 |
308.15 |
0.0026 |
0.1320 |
308.15 |
0.0049 |
0.2510 |
308.15 |
0.0074 |
0.3050 |
308.15 |
0.0151 |
0.6940 |
308.15 |
0.8710 |
0.7710 |
308.15 |
0.9310 |
0.8870 |
308.15 |
0.9800 |
0.9610 |
323.15 |
0.0011 |
0.0460 |
323.15 |
0.0026 |
0.1090 |
323.15 |
0.0052 |
0.2380 |
323.15 |
0.0074 |
0.3150 |
323.15 |
0.0151 |
0.7780 |
323.15 |
0.8730 |
0.8780 |
323.15 |
0.9300 |
0.9280 |
323.15 |
0.9800 |
0.9820 |
343.15 |
0.0009 |
0.0340 |
343.15 |
0.0025 |
0.0940 |
343.15 |
0.0047 |
0.2000 |
343.15 |
0.0072 |
0.2460 |
343.15 |
0.0149 |
0.8290 |
343.15 |
0.8690 |
0.9230 |
343.15 |
0.9290 |
0.9480 |
343.15 |
0.9810 |
0.9860 |
Mole fraction of Ethyl Acetate (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 2)
Temperature, K - Liquid mixture 1 |
Mole fraction of Ethyl Acetate (1) - Liquid mixture 2 |
298.15 |
0.0139 |
318.15 |
0.0117 |
Mole fraction of Ethyl Acetate (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 2)
Temperature, K - Liquid mixture 1 |
Mole fraction of Ethyl Acetate (1) - Liquid mixture 1 |
298.15 |
0.8285 |
318.15 |
0.7946 |
Mass fraction of Water (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 2 |
308.20 |
101.30 |
0.0334 |
Mass fraction of Ethyl Acetate (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mass fraction of Ethyl Acetate (1) - Liquid mixture 1 |
308.20 |
101.30 |
0.0700 |
Mole fraction of Water (2)
[ref]
Operational conditions:
- Pressure, kPa = 101.3 (Liquid mixture 1)
- Temperature, K = 298 (Liquid mixture 1)
Mole fraction of Water (2) - Liquid mixture 1 |
0.9983 |
0.0299 |
Mole fraction of Ethyl Acetate (1)
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid mixture 1 |
Temperature, K - Liquid mixture 1 |
Mole fraction of Ethyl Acetate (1) - Liquid mixture 1 |
101.30 |
298.00 |
0.8468 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
298.15 |
0.9837 |
303.15 |
0.9845 |
308.15 |
0.9851 |
313.15 |
0.9856 |
318.15 |
0.9860 |
323.15 |
0.9863 |
328.15 |
0.9866 |
333.15 |
0.9867 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 2 |
298.15 |
0.1733 |
303.15 |
0.1885 |
308.15 |
0.1997 |
313.15 |
0.2111 |
318.15 |
0.2179 |
323.15 |
0.2259 |
328.15 |
0.2333 |
333.15 |
0.2414 |
Mole fraction of Water (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
293.20 |
101.33 |
0.9819 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
283.20 |
0.1120 |
323.20 |
0.1890 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 2 |
283.20 |
0.9810 |
323.20 |
0.9780 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.0258 |
0.0004 |
298.15 |
0.0450 |
0.0004 |
298.15 |
0.0748 |
0.0005 |
298.15 |
0.0853 |
0.0005 |
298.15 |
0.1053 |
0.0005 |
298.15 |
0.1258 |
0.0005 |
318.15 |
0.0250 |
0.0004 |
318.15 |
0.0496 |
0.0004 |
318.15 |
0.0750 |
0.0004 |
318.15 |
0.0999 |
0.0004 |
318.15 |
0.1254 |
0.0004 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.0258 |
0.0004 |
298.15 |
0.0450 |
0.0004 |
298.15 |
0.0748 |
0.0005 |
298.15 |
0.0853 |
0.0005 |
298.15 |
0.1053 |
0.0005 |
298.15 |
0.1258 |
0.0005 |
318.15 |
0.0250 |
0.0004 |
318.15 |
0.0496 |
0.0004 |
318.15 |
0.0750 |
0.0004 |
318.15 |
0.0999 |
0.0004 |
318.15 |
0.1254 |
0.0004 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 353.15 (Liquid)
- Pressure, kPa = 1272 (Liquid)
Mole fraction of Ethyl Acetate (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0096 |
0.0209 |
0.0201 |
0.0446 |
0.0441 |
0.0917 |
0.0580 |
0.1190 |
0.0733 |
0.1490 |
0.0905 |
0.1820 |
0.0905 |
0.1830 |
0.1096 |
0.2200 |
0.1313 |
0.2640 |
0.1559 |
0.3110 |
0.1842 |
0.3640 |
0.2169 |
0.4300 |
0.2554 |
0.5050 |
0.3012 |
0.5940 |
0.3565 |
0.7040 |
0.4249 |
0.8380 |
0.5114 |
1.003 |
0.5639 |
1.104 |
0.6244 |
1.226 |
0.6949 |
1.357 |
0.8258 |
1.201 |
0.8781 |
0.9400 |
0.9359 |
0.5920 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 353.15 (Liquid)
- Pressure, kPa = 1272 (Liquid)
Mole fraction of Ethyl Acetate (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0096 |
0.0209 |
0.0201 |
0.0446 |
0.0441 |
0.0917 |
0.0580 |
0.1190 |
0.0733 |
0.1490 |
0.0905 |
0.1820 |
0.0905 |
0.1830 |
0.1096 |
0.2200 |
0.1313 |
0.2640 |
0.1559 |
0.3110 |
0.1842 |
0.3640 |
0.2169 |
0.4300 |
0.2554 |
0.5050 |
0.3012 |
0.5940 |
0.3565 |
0.7040 |
0.4249 |
0.8380 |
0.5114 |
1.003 |
0.5639 |
1.104 |
0.6244 |
1.226 |
0.6949 |
1.357 |
0.8258 |
1.201 |
0.8781 |
0.9400 |
0.9359 |
0.5920 |
Critical pressure, kPa
[ref]
Mole fraction of Ethyl Acetate (1) - Liquid |
Critical pressure, kPa - Liquid |
0.2100 |
13710.00 |
0.3800 |
8840.00 |
0.5800 |
6170.00 |
0.8100 |
4730.00 |
Critical pressure, kPa
[ref]
Mole fraction of Ethyl Acetate (1) - Liquid |
Critical pressure, kPa - Liquid |
0.2100 |
13710.00 |
0.3800 |
8840.00 |
0.5800 |
6170.00 |
0.8100 |
4730.00 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
95 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Refractive index (Na D-line) - Liquid |
293.20 |
0.1267 |
1.3725 |
293.20 |
0.9828 |
1.3387 |
313.20 |
0.1830 |
1.3623 |
313.20 |
0.9837 |
1.334 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Ethyl Acetate (1) - Liquid |
Refractive index (Na D-line) - Liquid |
293.15 |
0.0090 |
1.3341 |
293.15 |
0.0270 |
1.3352 |
293.15 |
0.0450 |
1.3368 |
293.15 |
0.0640 |
1.3384 |
293.15 |
0.0820 |
1.3391 |
298.15 |
0.0090 |
1.3335 |
298.15 |
0.0270 |
1.3348 |
298.15 |
0.0450 |
1.3364 |
298.15 |
0.0640 |
1.338 |
298.15 |
0.0820 |
1.3388 |
303.15 |
0.0090 |
1.3331 |
303.15 |
0.0270 |
1.3342 |
303.15 |
0.0450 |
1.3358 |
303.15 |
0.0640 |
1.3377 |
303.15 |
0.0820 |
1.3383 |
308.15 |
0.0090 |
1.3327 |
308.15 |
0.0270 |
1.3337 |
308.15 |
0.0450 |
1.3353 |
308.15 |
0.0640 |
1.3368 |
308.15 |
0.0820 |
1.3378 |
313.15 |
0.0090 |
1.3321 |
313.15 |
0.0270 |
1.3332 |
313.15 |
0.0450 |
1.3346 |
313.15 |
0.0640 |
1.3358 |
313.15 |
0.0820 |
1.3373 |
318.15 |
0.0090 |
1.3317 |
318.15 |
0.0270 |
1.3326 |
318.15 |
0.0450 |
1.3342 |
318.15 |
0.0640 |
1.3352 |
318.15 |
0.0820 |
1.3365 |
293.15 |
0.0000 |
1.3335 |
298.15 |
0.0000 |
1.333 |
303.15 |
0.0000 |
1.3323 |
308.15 |
0.0000 |
1.332 |
313.15 |
0.0000 |
1.3316 |
318.15 |
0.0000 |
1.3312 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
95 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Refractive index (Na D-line) - Liquid |
293.20 |
0.1267 |
1.3725 |
293.20 |
0.9828 |
1.3387 |
313.20 |
0.1830 |
1.3623 |
313.20 |
0.9837 |
1.334 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Ethyl Acetate (1) - Liquid |
Refractive index (Na D-line) - Liquid |
293.15 |
0.0090 |
1.3341 |
293.15 |
0.0270 |
1.3352 |
293.15 |
0.0450 |
1.3368 |
293.15 |
0.0640 |
1.3384 |
293.15 |
0.0820 |
1.3391 |
298.15 |
0.0090 |
1.3335 |
298.15 |
0.0270 |
1.3348 |
298.15 |
0.0450 |
1.3364 |
298.15 |
0.0640 |
1.338 |
298.15 |
0.0820 |
1.3388 |
303.15 |
0.0090 |
1.3331 |
303.15 |
0.0270 |
1.3342 |
303.15 |
0.0450 |
1.3358 |
303.15 |
0.0640 |
1.3377 |
303.15 |
0.0820 |
1.3383 |
308.15 |
0.0090 |
1.3327 |
308.15 |
0.0270 |
1.3337 |
308.15 |
0.0450 |
1.3353 |
308.15 |
0.0640 |
1.3368 |
308.15 |
0.0820 |
1.3378 |
313.15 |
0.0090 |
1.3321 |
313.15 |
0.0270 |
1.3332 |
313.15 |
0.0450 |
1.3346 |
313.15 |
0.0640 |
1.3358 |
313.15 |
0.0820 |
1.3373 |
318.15 |
0.0090 |
1.3317 |
318.15 |
0.0270 |
1.3326 |
318.15 |
0.0450 |
1.3342 |
318.15 |
0.0640 |
1.3352 |
318.15 |
0.0820 |
1.3365 |
293.15 |
0.0000 |
1.3335 |
298.15 |
0.0000 |
1.333 |
303.15 |
0.0000 |
1.3323 |
308.15 |
0.0000 |
1.332 |
313.15 |
0.0000 |
1.3316 |
318.15 |
0.0000 |
1.3312 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
95 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
293.20 |
0.1267 |
905.4 |
293.20 |
0.9828 |
998.227 |
313.20 |
0.1830 |
882.844 |
313.20 |
0.9837 |
990.48 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0269 |
895.32 |
298.15 |
0.0469 |
896.13 |
298.15 |
0.0722 |
897.09 |
298.15 |
0.0892 |
897.9 |
298.15 |
0.1045 |
898.48 |
298.15 |
0.1249 |
899.5 |
318.15 |
0.0249 |
870.81 |
318.15 |
0.0524 |
871.8 |
318.15 |
0.0766 |
872.73 |
318.15 |
0.1003 |
873.94 |
318.15 |
0.1255 |
875.08 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
95 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
293.20 |
0.1267 |
905.4 |
293.20 |
0.9828 |
998.227 |
313.20 |
0.1830 |
882.844 |
313.20 |
0.9837 |
990.48 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0269 |
895.32 |
298.15 |
0.0469 |
896.13 |
298.15 |
0.0722 |
897.09 |
298.15 |
0.0892 |
897.9 |
298.15 |
0.1045 |
898.48 |
298.15 |
0.1249 |
899.5 |
318.15 |
0.0249 |
870.81 |
318.15 |
0.0524 |
871.8 |
318.15 |
0.0766 |
872.73 |
318.15 |
0.1003 |
873.94 |
318.15 |
0.1255 |
875.08 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethyl Acetate (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
295.15 |
1.0000 |
0.0236 |
300.15 |
1.0000 |
0.0232 |
305.15 |
1.0000 |
0.0228 |
310.15 |
1.0000 |
0.0224 |
315.15 |
1.0000 |
0.0221 |
295.15 |
0.1000 |
0.0333 |
300.15 |
0.1000 |
0.0328 |
305.15 |
0.1000 |
0.0322 |
310.15 |
0.1000 |
0.0318 |
315.15 |
0.1000 |
0.0315 |
295.15 |
0.0900 |
0.0345 |
300.15 |
0.0900 |
0.0342 |
305.15 |
0.0900 |
0.0339 |
310.15 |
0.0900 |
0.0336 |
315.15 |
0.0900 |
0.0333 |
295.15 |
0.0800 |
0.0358 |
300.15 |
0.0800 |
0.0356 |
305.15 |
0.0800 |
0.0350 |
310.15 |
0.0800 |
0.0345 |
315.15 |
0.0800 |
0.0343 |
295.15 |
0.0700 |
0.0367 |
300.15 |
0.0700 |
0.0362 |
305.15 |
0.0700 |
0.0357 |
310.15 |
0.0700 |
0.0353 |
315.15 |
0.0700 |
0.0350 |
295.15 |
0.0600 |
0.0372 |
300.15 |
0.0600 |
0.0366 |
305.15 |
0.0600 |
0.0362 |
310.15 |
0.0600 |
0.0357 |
315.15 |
0.0600 |
0.0355 |
295.15 |
0.0500 |
0.0377 |
300.15 |
0.0500 |
0.0373 |
305.15 |
0.0500 |
0.0370 |
310.15 |
0.0500 |
0.0365 |
315.15 |
0.0500 |
0.0361 |
295.15 |
0.0400 |
0.0405 |
300.15 |
0.0400 |
0.0400 |
305.15 |
0.0400 |
0.0396 |
310.15 |
0.0400 |
0.0393 |
315.15 |
0.0400 |
0.0390 |
295.15 |
0.0300 |
0.0436 |
300.15 |
0.0300 |
0.0433 |
305.15 |
0.0300 |
0.0428 |
310.15 |
0.0300 |
0.0424 |
315.15 |
0.0300 |
0.0422 |
295.15 |
0.0200 |
0.0458 |
300.15 |
0.0200 |
0.0456 |
305.15 |
0.0200 |
0.0454 |
310.15 |
0.0200 |
0.0450 |
315.15 |
0.0200 |
0.0447 |
295.15 |
0.0100 |
0.0470 |
300.15 |
0.0100 |
0.0467 |
305.15 |
0.0100 |
0.0462 |
310.15 |
0.0100 |
0.0458 |
315.15 |
0.0100 |
0.0454 |
295.15 |
0.0000 |
0.0724 |
300.15 |
0.0000 |
0.0715 |
305.15 |
0.0000 |
0.0708 |
310.15 |
0.0000 |
0.0700 |
315.15 |
0.0000 |
0.0695 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Temperature, K =
298.15 (Liquid)
Mole fraction of Ethyl Acetate (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
0.0002 |
0.0696 |
0.0004 |
0.0677 |
0.0006 |
0.0652 |
0.0008 |
0.0637 |
0.0010 |
0.0623 |
0.0021 |
0.0573 |
0.0039 |
0.0512 |
0.0060 |
0.0467 |
0.0080 |
0.0434 |
0.0099 |
0.0405 |
0.0120 |
0.0378 |
0.0140 |
0.0352 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Temperature, K =
298.15 (Liquid)
Mole fraction of Ethyl Acetate (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
0.0000 |
0.0716 |
0.0011 |
0.0621 |
0.0013 |
0.0609 |
0.0014 |
0.0604 |
0.0017 |
0.0593 |
0.0018 |
0.0588 |
0.0025 |
0.0566 |
0.0033 |
0.0542 |
0.0044 |
0.0512 |
0.0054 |
0.0490 |
0.0061 |
0.0479 |
0.0080 |
0.0442 |
0.0089 |
0.0433 |
0.0118 |
0.0414 |
0.0141 |
0.0390 |
1.0000 |
0.0239 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethyl Acetate (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
295.15 |
1.0000 |
0.0236 |
300.15 |
1.0000 |
0.0232 |
305.15 |
1.0000 |
0.0228 |
310.15 |
1.0000 |
0.0224 |
315.15 |
1.0000 |
0.0221 |
295.15 |
0.1000 |
0.0333 |
300.15 |
0.1000 |
0.0328 |
305.15 |
0.1000 |
0.0322 |
310.15 |
0.1000 |
0.0318 |
315.15 |
0.1000 |
0.0315 |
295.15 |
0.0900 |
0.0345 |
300.15 |
0.0900 |
0.0342 |
305.15 |
0.0900 |
0.0339 |
310.15 |
0.0900 |
0.0336 |
315.15 |
0.0900 |
0.0333 |
295.15 |
0.0800 |
0.0358 |
300.15 |
0.0800 |
0.0356 |
305.15 |
0.0800 |
0.0350 |
310.15 |
0.0800 |
0.0345 |
315.15 |
0.0800 |
0.0343 |
295.15 |
0.0700 |
0.0367 |
300.15 |
0.0700 |
0.0362 |
305.15 |
0.0700 |
0.0357 |
310.15 |
0.0700 |
0.0353 |
315.15 |
0.0700 |
0.0350 |
295.15 |
0.0600 |
0.0372 |
300.15 |
0.0600 |
0.0366 |
305.15 |
0.0600 |
0.0362 |
310.15 |
0.0600 |
0.0357 |
315.15 |
0.0600 |
0.0355 |
295.15 |
0.0500 |
0.0377 |
300.15 |
0.0500 |
0.0373 |
305.15 |
0.0500 |
0.0370 |
310.15 |
0.0500 |
0.0365 |
315.15 |
0.0500 |
0.0361 |
295.15 |
0.0400 |
0.0405 |
300.15 |
0.0400 |
0.0400 |
305.15 |
0.0400 |
0.0396 |
310.15 |
0.0400 |
0.0393 |
315.15 |
0.0400 |
0.0390 |
295.15 |
0.0300 |
0.0436 |
300.15 |
0.0300 |
0.0433 |
305.15 |
0.0300 |
0.0428 |
310.15 |
0.0300 |
0.0424 |
315.15 |
0.0300 |
0.0422 |
295.15 |
0.0200 |
0.0458 |
300.15 |
0.0200 |
0.0456 |
305.15 |
0.0200 |
0.0454 |
310.15 |
0.0200 |
0.0450 |
315.15 |
0.0200 |
0.0447 |
295.15 |
0.0100 |
0.0470 |
300.15 |
0.0100 |
0.0467 |
305.15 |
0.0100 |
0.0462 |
310.15 |
0.0100 |
0.0458 |
315.15 |
0.0100 |
0.0454 |
295.15 |
0.0000 |
0.0724 |
300.15 |
0.0000 |
0.0715 |
305.15 |
0.0000 |
0.0708 |
310.15 |
0.0000 |
0.0700 |
315.15 |
0.0000 |
0.0695 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Temperature, K =
298.15 (Liquid)
Mole fraction of Ethyl Acetate (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
0.0002 |
0.0696 |
0.0004 |
0.0677 |
0.0006 |
0.0652 |
0.0008 |
0.0637 |
0.0010 |
0.0623 |
0.0021 |
0.0573 |
0.0039 |
0.0512 |
0.0060 |
0.0467 |
0.0080 |
0.0434 |
0.0099 |
0.0405 |
0.0120 |
0.0378 |
0.0140 |
0.0352 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Temperature, K =
298.15 (Liquid)
Mole fraction of Ethyl Acetate (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
0.0000 |
0.0716 |
0.0011 |
0.0621 |
0.0013 |
0.0609 |
0.0014 |
0.0604 |
0.0017 |
0.0593 |
0.0018 |
0.0588 |
0.0025 |
0.0566 |
0.0033 |
0.0542 |
0.0044 |
0.0512 |
0.0054 |
0.0490 |
0.0061 |
0.0479 |
0.0080 |
0.0442 |
0.0089 |
0.0433 |
0.0118 |
0.0414 |
0.0141 |
0.0390 |
1.0000 |
0.0239 |
Critical temperature, K
[ref]
Mole fraction of Ethyl Acetate (1) - Liquid |
Critical temperature, K - Liquid |
0.2100 |
592.50 |
0.3800 |
558.50 |
0.5800 |
538.40 |
0.8100 |
529.80 |
Critical temperature, K
[ref]
Mole fraction of Ethyl Acetate (1) - Liquid |
Critical temperature, K - Liquid |
0.2100 |
592.50 |
0.3800 |
558.50 |
0.5800 |
538.40 |
0.8100 |
529.80 |
Vapor Liquid Equilibrium at Constant Pressure
[ref]
Operational condition: Pressure, kPa =
101.33 (VLE)
Fixed |
Measured |
T [K] - VLE |
x1[mol/mol] of Ethyl Acetate (1) - Liquid |
y1[mol/mol] of Ethyl Acetate (1) - Vapour |
347.25 |
0.9400 |
0.8490 |
347.75 |
0.9580 |
0.8690 |
348.95 |
0.9760 |
0.9220 |
Vapor Liquid Equilibrium at Constant Pressure
[ref]
Operational condition: Pressure, kPa =
101.33 (VLE)
Fixed |
Measured |
T [K] - VLE |
x1[mol/mol] of Ethyl Acetate (1) - Liquid |
y1[mol/mol] of Ethyl Acetate (1) - Vapour |
347.95 |
0.9710 |
0.9140 |
348.15 |
0.9740 |
0.9270 |
348.75 |
0.9830 |
0.9470 |
349.05 |
0.9840 |
0.9530 |
348.85 |
0.9860 |
0.9540 |
Vapor Liquid Equilibrium at Constant Pressure
[ref]
Operational condition: Pressure, kPa =
101.33 (VLE)
Fixed |
Measured |
T [K] - VLE |
x1[mol/mol] of Ethyl Acetate (1) - Liquid |
y1[mol/mol] of Ethyl Acetate (1) - Vapour |
372.0 |
0.0006 |
0.0406 |
369.35 |
0.0011 |
0.1256 |
359.65 |
0.0049 |
0.5910 |
349.35 |
0.0086 |
0.6680 |
343.7 |
0.0459 |
0.7140 |
343.6 |
0.6900 |
0.7070 |
343.65 |
0.7750 |
0.6990 |
344.6 |
0.8737 |
0.7650 |
346.5 |
0.9445 |
0.8650 |
348.7 |
0.9807 |
0.9411 |
Sources
-
Dortmund Data Bank Vapor-Liquid Equilibrium Data
-
Enhancement of liquid phase splitting of water + ethanol + ethyl acetate mixtures in the presence of a hydrophilic agent or an electrolyte substance
-
(Liquid + liquid) equilibria of (water + 1-propanol + solvent) at T = 298.2K
-
Experimental and calculated liquid-liquid equilibrium data for water + furfural + solvents
-
Temperature dependence of limiting activity coefficients, Henry's law constants, and related infinite dilution properties of C4-C6 isomeric n-alkyl ethanoates/ethyl n-alkanoates in water. Measurement, critical compilation, correlation, and recommended data
-
Phase equilibria and excess properties for binary systems in reactive distillation processes Part II. Ethyl acetate synthesis
-
Solubility and tie-line data for ternary aqueous mixtures of cyclopentanol with organic solvents at T = 298.2 K: Experiments and NRTL model
-
A model to calculate concentration-dependent surface tension of binary systems
-
Liquid-liquid equilibrium data for ternary systems of water + acetic acid + acetate esters at 293.2 K and 303.2 K and ~ 95 kPa
-
The potential of head-space gas chromatography for VLE measurements
-
Liquid-liquid equilibrium for ternary systems of ethyl acetate/isopropyl acetate + 2,2,3,3-tetrafluoro-1-propanol + water at 298.15, 318.15 K
-
Liquid-liquid equilibrium study for ternary systems of water + propargyl alcohol + solvents at 308.2 K: Measurement and thermodynamic modelling
-
Dependence of Refractive Index on Concentration and Temperature in Electrolyte Solution, Polar Solution, Nonpolar Solution, and Protein Solution
-
Liquid-Liquid Equilibrium for the Quaternary System Toluene + Water + Propionic Acid + Ethyl Acetate at 25 deg C and Atmospheric Pressure
-
Critical Properties of the Reacting Mixture in the Esterification of Acetic Acid with Ethanol
-
Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
-
Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes
-
Liquid-Liquid Equilibria for Water + Benzonitrile + Ethyl Acetate or + Butyl Acetate
-
Liquid-Liquid Equilibria for the Ternary Systems Water + 3-Methyl-2-cyclopentenone with Ethyl Acetate or Methyl tert-Butyl Ether at 293.2 K
-
Activity Coefficients at Infinite Dilution of Volatile Compounds in Water: Effect of Temperature and Salt Concentration
-
Viscosity and Density of Water + Ethyl Acetate + Ethanol Mixtures at 298.15 and 318.15 K and Atmospheric Pressure
-
Liquid-Liquid Equilibria of Water + 2-Butanol + (Methyl Methacrylate or Butyl Methacrylate or Isobutyl Methacrylate) at (288.2 and 318.2) K
-
Surface Tension Data of Aqueous Binary Mixtures of Methyl, Ethyl, Propyl, and Butyl Acetates at 298.15 K