Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Diethyl malonate (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
288.20 | 0.0501 | 0.3970 |
288.20 | 0.1004 | 0.7020 |
288.20 | 0.1491 | 0.9740 |
288.20 | 0.1995 | 1.178 |
288.20 | 0.2507 | 1.329 |
288.20 | 0.2985 | 1.454 |
288.20 | 0.3517 | 1.564 |
288.20 | 0.3990 | 1.63 |
288.20 | 0.4509 | 1.676 |
288.20 | 0.4985 | 1.7 |
288.20 | 0.5503 | 1.692 |
288.20 | 0.6013 | 1.653 |
288.20 | 0.6504 | 1.588 |
288.20 | 0.6967 | 1.503 |
288.20 | 0.7465 | 1.371 |
288.20 | 0.8002 | 1.188 |
288.20 | 0.8497 | 0.9720 |
288.20 | 0.9027 | 0.6880 |
288.20 | 0.9498 | 0.3750 |
298.20 | 0.0501 | 0.4230 |
298.20 | 0.1004 | 0.7750 |
298.20 | 0.1491 | 1.033 |
298.20 | 0.1995 | 1.261 |
298.20 | 0.2507 | 1.446 |
298.20 | 0.2985 | 1.586 |
298.20 | 0.3517 | 1.701 |
298.20 | 0.3990 | 1.778 |
298.20 | 0.4509 | 1.821 |
298.20 | 0.4985 | 1.848 |
298.20 | 0.5503 | 1.828 |
298.20 | 0.6013 | 1.789 |
298.20 | 0.6504 | 1.716 |
298.20 | 0.6967 | 1.613 |
298.20 | 0.7465 | 1.473 |
298.20 | 0.8002 | 1.265 |
298.20 | 0.8497 | 1.014 |
298.20 | 0.9027 | 0.7210 |
298.20 | 0.9498 | 0.3960 |
313.20 | 0.0501 | 0.4760 |
313.20 | 0.1004 | 0.8590 |
313.20 | 0.1491 | 1.168 |
313.20 | 0.1995 | 1.41 |
313.20 | 0.2507 | 1.62 |
313.20 | 0.2985 | 1.78 |
313.20 | 0.3517 | 1.898 |
313.20 | 0.3990 | 1.981 |
313.20 | 0.4509 | 2.032 |
313.20 | 0.4985 | 2.045 |
313.20 | 0.5503 | 2.031 |
313.20 | 0.6013 | 1.962 |
313.20 | 0.6504 | 1.875 |
313.20 | 0.6967 | 1.764 |
313.20 | 0.7465 | 1.59 |
313.20 | 0.8002 | 1.347 |
313.20 | 0.8497 | 1.084 |
313.20 | 0.9027 | 0.7470 |
313.20 | 0.9498 | 0.4410 |
328.20 | 0.0501 | 0.4970 |
328.20 | 0.1004 | 0.9290 |
328.20 | 0.1491 | 1.271 |
328.20 | 0.1995 | 1.531 |
328.20 | 0.2507 | 1.757 |
328.20 | 0.2985 | 1.926 |
328.20 | 0.3517 | 2.053 |
328.20 | 0.3990 | 2.134 |
328.20 | 0.4509 | 2.184 |
328.20 | 0.4985 | 2.203 |
328.20 | 0.5503 | 2.165 |
328.20 | 0.6013 | 2.087 |
328.20 | 0.6504 | 1.994 |
328.20 | 0.6967 | 1.85 |
328.20 | 0.7465 | 1.658 |
328.20 | 0.8002 | 1.392 |
328.20 | 0.8497 | 1.125 |
328.20 | 0.9027 | 0.7770 |
328.20 | 0.9498 | 0.4240 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Diethyl malonate (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
288.20 | 0.0501 | 0.3970 |
288.20 | 0.1004 | 0.7020 |
288.20 | 0.1491 | 0.9740 |
288.20 | 0.1995 | 1.178 |
288.20 | 0.2507 | 1.329 |
288.20 | 0.2985 | 1.454 |
288.20 | 0.3517 | 1.564 |
288.20 | 0.3990 | 1.63 |
288.20 | 0.4509 | 1.676 |
288.20 | 0.4985 | 1.7 |
288.20 | 0.5503 | 1.692 |
288.20 | 0.6013 | 1.653 |
288.20 | 0.6504 | 1.588 |
288.20 | 0.6967 | 1.503 |
288.20 | 0.7465 | 1.371 |
288.20 | 0.8002 | 1.188 |
288.20 | 0.8497 | 0.9720 |
288.20 | 0.9027 | 0.6880 |
288.20 | 0.9498 | 0.3750 |
298.20 | 0.0501 | 0.4230 |
298.20 | 0.1004 | 0.7750 |
298.20 | 0.1491 | 1.033 |
298.20 | 0.1995 | 1.261 |
298.20 | 0.2507 | 1.446 |
298.20 | 0.2985 | 1.586 |
298.20 | 0.3517 | 1.701 |
298.20 | 0.3990 | 1.778 |
298.20 | 0.4509 | 1.821 |
298.20 | 0.4985 | 1.848 |
298.20 | 0.5503 | 1.828 |
298.20 | 0.6013 | 1.789 |
298.20 | 0.6504 | 1.716 |
298.20 | 0.6967 | 1.613 |
298.20 | 0.7465 | 1.473 |
298.20 | 0.8002 | 1.265 |
298.20 | 0.8497 | 1.014 |
298.20 | 0.9027 | 0.7210 |
298.20 | 0.9498 | 0.3960 |
313.20 | 0.0501 | 0.4760 |
313.20 | 0.1004 | 0.8590 |
313.20 | 0.1491 | 1.168 |
313.20 | 0.1995 | 1.41 |
313.20 | 0.2507 | 1.62 |
313.20 | 0.2985 | 1.78 |
313.20 | 0.3517 | 1.898 |
313.20 | 0.3990 | 1.981 |
313.20 | 0.4509 | 2.032 |
313.20 | 0.4985 | 2.045 |
313.20 | 0.5503 | 2.031 |
313.20 | 0.6013 | 1.962 |
313.20 | 0.6504 | 1.875 |
313.20 | 0.6967 | 1.764 |
313.20 | 0.7465 | 1.59 |
313.20 | 0.8002 | 1.347 |
313.20 | 0.8497 | 1.084 |
313.20 | 0.9027 | 0.7470 |
313.20 | 0.9498 | 0.4410 |
328.20 | 0.0501 | 0.4970 |
328.20 | 0.1004 | 0.9290 |
328.20 | 0.1491 | 1.271 |
328.20 | 0.1995 | 1.531 |
328.20 | 0.2507 | 1.757 |
328.20 | 0.2985 | 1.926 |
328.20 | 0.3517 | 2.053 |
328.20 | 0.3990 | 2.134 |
328.20 | 0.4509 | 2.184 |
328.20 | 0.4985 | 2.203 |
328.20 | 0.5503 | 2.165 |
328.20 | 0.6013 | 2.087 |
328.20 | 0.6504 | 1.994 |
328.20 | 0.6967 | 1.85 |
328.20 | 0.7465 | 1.658 |
328.20 | 0.8002 | 1.392 |
328.20 | 0.8497 | 1.125 |
328.20 | 0.9027 | 0.7770 |
328.20 | 0.9498 | 0.4240 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Diethyl malonate (1) - Liquid | Mass density, kg/m3 - Liquid |
288.15 | 0.0000 | 794.044 |
288.15 | 0.0500 | 826.264 |
288.15 | 0.0999 | 853.923 |
288.15 | 0.1001 | 854.013 |
288.15 | 0.1500 | 878.005 |
288.15 | 0.2001 | 899.1 |
288.15 | 0.3000 | 934.365 |
288.15 | 0.4000 | 962.806 |
288.15 | 0.4498 | 974.929 |
288.15 | 0.4999 | 986.037 |
288.15 | 0.5501 | 996.293 |
288.15 | 0.6001 | 1005.602 |
288.15 | 0.6453 | 1013.442 |
288.15 | 0.6997 | 1022.161 |
288.15 | 0.7497 | 1029.613 |
288.15 | 0.8496 | 1043.02 |
288.15 | 0.8995 | 1049.081 |
288.15 | 1.0000 | 1060.326 |
298.15 | 0.0000 | 785.489 |
298.15 | 0.0500 | 817.293 |
298.15 | 0.0999 | 844.646 |
298.15 | 0.1001 | 844.731 |
298.15 | 0.1500 | 868.468 |
298.15 | 0.2001 | 889.366 |
298.15 | 0.3000 | 924.309 |
298.15 | 0.4000 | 952.511 |
298.15 | 0.4498 | 964.533 |
298.15 | 0.4999 | 975.577 |
298.15 | 0.5501 | 985.767 |
298.15 | 0.6001 | 995.034 |
298.15 | 0.6453 | 1002.818 |
298.15 | 0.6997 | 1011.524 |
298.15 | 0.7497 | 1018.928 |
298.15 | 0.8496 | 1032.313 |
298.15 | 0.8995 | 1038.363 |
298.15 | 1.0000 | 1049.603 |
313.15 | 0.0000 | 772.42 |
313.15 | 0.0500 | 803.619 |
313.15 | 0.0999 | 830.505 |
313.15 | 0.1001 | 830.589 |
313.15 | 0.1500 | 853.941 |
313.15 | 0.2001 | 874.536 |
313.15 | 0.3000 | 909.007 |
313.15 | 0.4000 | 936.881 |
313.15 | 0.4498 | 948.801 |
313.15 | 0.4999 | 959.71 |
313.15 | 0.5501 | 969.837 |
313.15 | 0.6001 | 979.034 |
313.15 | 0.6453 | 986.788 |
313.15 | 0.6997 | 995.442 |
313.15 | 0.7497 | 1002.827 |
313.15 | 0.8496 | 1016.201 |
313.15 | 0.8995 | 1022.248 |
313.15 | 1.0000 | 1033.498 |
328.15 | 0.0000 | 758.958 |
328.15 | 0.0500 | 789.558 |
328.15 | 0.0999 | 815.983 |
328.15 | 0.1001 | 816.063 |
328.15 | 0.1500 | 839.005 |
328.15 | 0.2001 | 859.351 |
328.15 | 0.3000 | 893.394 |
328.15 | 0.4000 | 920.983 |
328.15 | 0.4498 | 932.802 |
328.15 | 0.4999 | 943.637 |
328.15 | 0.5501 | 953.695 |
328.15 | 0.6001 | 962.847 |
328.15 | 0.6453 | 970.577 |
328.15 | 0.6997 | 979.211 |
328.15 | 0.7497 | 986.588 |
328.15 | 0.8496 | 999.969 |
328.15 | 0.8995 | 1006.058 |
328.15 | 1.0000 | 1017.336 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Diethyl malonate (1) - Liquid | Mass density, kg/m3 - Liquid |
288.15 | 0.0000 | 794.044 |
288.15 | 0.0500 | 826.264 |
288.15 | 0.0999 | 853.923 |
288.15 | 0.1001 | 854.013 |
288.15 | 0.1500 | 878.005 |
288.15 | 0.2001 | 899.1 |
288.15 | 0.3000 | 934.365 |
288.15 | 0.4000 | 962.806 |
288.15 | 0.4498 | 974.929 |
288.15 | 0.4999 | 986.037 |
288.15 | 0.5501 | 996.293 |
288.15 | 0.6001 | 1005.602 |
288.15 | 0.6453 | 1013.442 |
288.15 | 0.6997 | 1022.161 |
288.15 | 0.7497 | 1029.613 |
288.15 | 0.8496 | 1043.02 |
288.15 | 0.8995 | 1049.081 |
288.15 | 1.0000 | 1060.326 |
298.15 | 0.0000 | 785.489 |
298.15 | 0.0500 | 817.293 |
298.15 | 0.0999 | 844.646 |
298.15 | 0.1001 | 844.731 |
298.15 | 0.1500 | 868.468 |
298.15 | 0.2001 | 889.366 |
298.15 | 0.3000 | 924.309 |
298.15 | 0.4000 | 952.511 |
298.15 | 0.4498 | 964.533 |
298.15 | 0.4999 | 975.577 |
298.15 | 0.5501 | 985.767 |
298.15 | 0.6001 | 995.034 |
298.15 | 0.6453 | 1002.818 |
298.15 | 0.6997 | 1011.524 |
298.15 | 0.7497 | 1018.928 |
298.15 | 0.8496 | 1032.313 |
298.15 | 0.8995 | 1038.363 |
298.15 | 1.0000 | 1049.603 |
313.15 | 0.0000 | 772.42 |
313.15 | 0.0500 | 803.619 |
313.15 | 0.0999 | 830.505 |
313.15 | 0.1001 | 830.589 |
313.15 | 0.1500 | 853.941 |
313.15 | 0.2001 | 874.536 |
313.15 | 0.3000 | 909.007 |
313.15 | 0.4000 | 936.881 |
313.15 | 0.4498 | 948.801 |
313.15 | 0.4999 | 959.71 |
313.15 | 0.5501 | 969.837 |
313.15 | 0.6001 | 979.034 |
313.15 | 0.6453 | 986.788 |
313.15 | 0.6997 | 995.442 |
313.15 | 0.7497 | 1002.827 |
313.15 | 0.8496 | 1016.201 |
313.15 | 0.8995 | 1022.248 |
313.15 | 1.0000 | 1033.498 |
328.15 | 0.0000 | 758.958 |
328.15 | 0.0500 | 789.558 |
328.15 | 0.0999 | 815.983 |
328.15 | 0.1001 | 816.063 |
328.15 | 0.1500 | 839.005 |
328.15 | 0.2001 | 859.351 |
328.15 | 0.3000 | 893.394 |
328.15 | 0.4000 | 920.983 |
328.15 | 0.4498 | 932.802 |
328.15 | 0.4999 | 943.637 |
328.15 | 0.5501 | 953.695 |
328.15 | 0.6001 | 962.847 |
328.15 | 0.6453 | 970.577 |
328.15 | 0.6997 | 979.211 |
328.15 | 0.7497 | 986.588 |
328.15 | 0.8496 | 999.969 |
328.15 | 0.8995 | 1006.058 |
328.15 | 1.0000 | 1017.336 |