Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Diethyl carbonate (1) - Liquid | Viscosity, Pa*s - Liquid |
| 288.15 | 0.0588 | 0.0087 |
| 288.15 | 0.0918 | 0.0077 |
| 288.15 | 0.1840 | 0.0055 |
| 288.15 | 0.2839 | 0.0040 |
| 288.15 | 0.4001 | 0.0029 |
| 288.15 | 0.5109 | 0.0022 |
| 288.15 | 0.5980 | 0.0018 |
| 288.15 | 0.6927 | 0.0014 |
| 288.15 | 0.8073 | 0.0012 |
| 288.15 | 0.9275 | 0.0010 |
| 288.15 | 0.9531 | 0.0009 |
| 293.15 | 0.0526 | 0.0074 |
| 293.15 | 0.1047 | 0.0061 |
| 293.15 | 0.1967 | 0.0045 |
| 293.15 | 0.2955 | 0.0033 |
| 293.15 | 0.3964 | 0.0025 |
| 293.15 | 0.5031 | 0.0020 |
| 293.15 | 0.6040 | 0.0016 |
| 293.15 | 0.6995 | 0.0013 |
| 293.15 | 0.8175 | 0.0010 |
| 293.15 | 0.9124 | 0.0009 |
| 293.15 | 0.9531 | 0.0009 |
| 303.15 | 0.0535 | 0.0053 |
| 303.15 | 0.1003 | 0.0045 |
| 303.15 | 0.1902 | 0.0034 |
| 303.15 | 0.3002 | 0.0025 |
| 303.15 | 0.4112 | 0.0019 |
| 303.15 | 0.5038 | 0.0016 |
| 303.15 | 0.5934 | 0.0013 |
| 303.15 | 0.6981 | 0.0011 |
| 303.15 | 0.8151 | 0.0009 |
| 303.15 | 0.9138 | 0.0008 |
| 303.15 | 0.9548 | 0.0007 |
| 313.15 | 0.0567 | 0.0038 |
| 313.15 | 0.1109 | 0.0033 |
| 313.15 | 0.1956 | 0.0026 |
| 313.15 | 0.2893 | 0.0021 |
| 313.15 | 0.4005 | 0.0016 |
| 313.15 | 0.5067 | 0.0013 |
| 313.15 | 0.6044 | 0.0011 |
| 313.15 | 0.7038 | 0.0009 |
| 313.15 | 0.8041 | 0.0008 |
| 313.15 | 0.9092 | 0.0007 |
| 313.15 | 0.9540 | 0.0006 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Diethyl carbonate (1) - Liquid | Viscosity, Pa*s - Liquid |
| 288.15 | 0.0588 | 0.0087 |
| 288.15 | 0.0918 | 0.0077 |
| 288.15 | 0.1840 | 0.0055 |
| 288.15 | 0.2839 | 0.0040 |
| 288.15 | 0.4001 | 0.0029 |
| 288.15 | 0.5109 | 0.0022 |
| 288.15 | 0.5980 | 0.0018 |
| 288.15 | 0.6927 | 0.0014 |
| 288.15 | 0.8073 | 0.0012 |
| 288.15 | 0.9275 | 0.0010 |
| 288.15 | 0.9531 | 0.0009 |
| 293.15 | 0.0526 | 0.0074 |
| 293.15 | 0.1047 | 0.0061 |
| 293.15 | 0.1967 | 0.0045 |
| 293.15 | 0.2955 | 0.0033 |
| 293.15 | 0.3964 | 0.0025 |
| 293.15 | 0.5031 | 0.0020 |
| 293.15 | 0.6040 | 0.0016 |
| 293.15 | 0.6995 | 0.0013 |
| 293.15 | 0.8175 | 0.0010 |
| 293.15 | 0.9124 | 0.0009 |
| 293.15 | 0.9531 | 0.0009 |
| 303.15 | 0.0535 | 0.0053 |
| 303.15 | 0.1003 | 0.0045 |
| 303.15 | 0.1902 | 0.0034 |
| 303.15 | 0.3002 | 0.0025 |
| 303.15 | 0.4112 | 0.0019 |
| 303.15 | 0.5038 | 0.0016 |
| 303.15 | 0.5934 | 0.0013 |
| 303.15 | 0.6981 | 0.0011 |
| 303.15 | 0.8151 | 0.0009 |
| 303.15 | 0.9138 | 0.0008 |
| 303.15 | 0.9548 | 0.0007 |
| 313.15 | 0.0567 | 0.0038 |
| 313.15 | 0.1109 | 0.0033 |
| 313.15 | 0.1956 | 0.0026 |
| 313.15 | 0.2893 | 0.0021 |
| 313.15 | 0.4005 | 0.0016 |
| 313.15 | 0.5067 | 0.0013 |
| 313.15 | 0.6044 | 0.0011 |
| 313.15 | 0.7038 | 0.0009 |
| 313.15 | 0.8041 | 0.0008 |
| 313.15 | 0.9092 | 0.0007 |
| 313.15 | 0.9540 | 0.0006 |
Operational conditions:
| Mole fraction of Diethyl carbonate (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0913 | 0.7356 |
| 0.1276 | 0.9861 |
| 0.1764 | 1.2959 |
| 0.2484 | 1.6483 |
| 0.3155 | 1.9235 |
| 0.3740 | 2.0935 |
| 0.4304 | 2.2087 |
| 0.4910 | 2.2772 |
| 0.5699 | 2.2681 |
| 0.6268 | 2.2141 |
| 0.6895 | 2.0899 |
| 0.7492 | 1.9028 |
| 0.8111 | 1.6205 |
| 0.8705 | 1.2454 |
| 0.9357 | 0.6981 |
Operational conditions:
| Mole fraction of Diethyl carbonate (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0913 | 0.7356 |
| 0.1276 | 0.9861 |
| 0.1764 | 1.2959 |
| 0.2484 | 1.6483 |
| 0.3155 | 1.9235 |
| 0.3740 | 2.0935 |
| 0.4304 | 2.2087 |
| 0.4910 | 2.2772 |
| 0.5699 | 2.2681 |
| 0.6268 | 2.2141 |
| 0.6895 | 2.0899 |
| 0.7492 | 1.9028 |
| 0.8111 | 1.6205 |
| 0.8705 | 1.2454 |
| 0.9357 | 0.6981 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Diethyl carbonate (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0588 | 834.94 |
| 288.15 | 0.0918 | 838.6 |
| 288.15 | 0.1840 | 849.27 |
| 288.15 | 0.2839 | 861.63 |
| 288.15 | 0.4001 | 877.04 |
| 288.15 | 0.5109 | 892.89 |
| 288.15 | 0.5980 | 906.21 |
| 288.15 | 0.6927 | 921.66 |
| 288.15 | 0.8073 | 941.89 |
| 288.15 | 0.9275 | 965.14 |
| 288.15 | 0.9531 | 970.42 |
| 293.15 | 0.0526 | 830.75 |
| 293.15 | 0.1047 | 836.45 |
| 293.15 | 0.1967 | 847.03 |
| 293.15 | 0.2955 | 859.15 |
| 293.15 | 0.3964 | 872.38 |
| 293.15 | 0.5031 | 887.37 |
| 293.15 | 0.6040 | 902.57 |
| 293.15 | 0.6995 | 918.01 |
| 293.15 | 0.8175 | 938.67 |
| 293.15 | 0.9124 | 956.76 |
| 293.15 | 0.9531 | 964.98 |
| 303.15 | 0.0535 | 823.7 |
| 303.15 | 0.1003 | 828.65 |
| 303.15 | 0.1902 | 838.63 |
| 303.15 | 0.3002 | 851.69 |
| 303.15 | 0.4112 | 865.89 |
| 303.15 | 0.5038 | 878.58 |
| 303.15 | 0.5934 | 891.62 |
| 303.15 | 0.6981 | 907.98 |
| 303.15 | 0.8151 | 927.85 |
| 303.15 | 0.9138 | 946.1 |
| 303.15 | 0.9548 | 954.16 |
| 313.15 | 0.0567 | 816.83 |
| 313.15 | 0.1109 | 822.42 |
| 313.15 | 0.1956 | 831.59 |
| 313.15 | 0.2893 | 842.35 |
| 313.15 | 0.4005 | 856.05 |
| 313.15 | 0.5067 | 870.12 |
| 313.15 | 0.6044 | 884.01 |
| 313.15 | 0.7038 | 899.18 |
| 313.15 | 0.8041 | 915.66 |
| 313.15 | 0.9092 | 934.43 |
| 313.15 | 0.9540 | 942.96 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Diethyl carbonate (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0588 | 834.94 |
| 288.15 | 0.0918 | 838.6 |
| 288.15 | 0.1840 | 849.27 |
| 288.15 | 0.2839 | 861.63 |
| 288.15 | 0.4001 | 877.04 |
| 288.15 | 0.5109 | 892.89 |
| 288.15 | 0.5980 | 906.21 |
| 288.15 | 0.6927 | 921.66 |
| 288.15 | 0.8073 | 941.89 |
| 288.15 | 0.9275 | 965.14 |
| 288.15 | 0.9531 | 970.42 |
| 293.15 | 0.0526 | 830.75 |
| 293.15 | 0.1047 | 836.45 |
| 293.15 | 0.1967 | 847.03 |
| 293.15 | 0.2955 | 859.15 |
| 293.15 | 0.3964 | 872.38 |
| 293.15 | 0.5031 | 887.37 |
| 293.15 | 0.6040 | 902.57 |
| 293.15 | 0.6995 | 918.01 |
| 293.15 | 0.8175 | 938.67 |
| 293.15 | 0.9124 | 956.76 |
| 293.15 | 0.9531 | 964.98 |
| 303.15 | 0.0535 | 823.7 |
| 303.15 | 0.1003 | 828.65 |
| 303.15 | 0.1902 | 838.63 |
| 303.15 | 0.3002 | 851.69 |
| 303.15 | 0.4112 | 865.89 |
| 303.15 | 0.5038 | 878.58 |
| 303.15 | 0.5934 | 891.62 |
| 303.15 | 0.6981 | 907.98 |
| 303.15 | 0.8151 | 927.85 |
| 303.15 | 0.9138 | 946.1 |
| 303.15 | 0.9548 | 954.16 |
| 313.15 | 0.0567 | 816.83 |
| 313.15 | 0.1109 | 822.42 |
| 313.15 | 0.1956 | 831.59 |
| 313.15 | 0.2893 | 842.35 |
| 313.15 | 0.4005 | 856.05 |
| 313.15 | 0.5067 | 870.12 |
| 313.15 | 0.6044 | 884.01 |
| 313.15 | 0.7038 | 899.18 |
| 313.15 | 0.8041 | 915.66 |
| 313.15 | 0.9092 | 934.43 |
| 313.15 | 0.9540 | 942.96 |