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 |
288.15 | 0.0502 | 0.6110 |
288.15 | 0.0983 | 1.054 |
288.15 | 0.1494 | 1.397 |
288.15 | 0.2006 | 1.681 |
288.15 | 0.2484 | 1.89 |
288.15 | 0.2989 | 2.06 |
288.15 | 0.3486 | 2.183 |
288.15 | 0.3972 | 2.265 |
288.15 | 0.4484 | 2.314 |
288.15 | 0.4981 | 2.342 |
288.15 | 0.5504 | 2.316 |
288.15 | 0.6006 | 2.23 |
288.15 | 0.6485 | 2.135 |
288.15 | 0.6985 | 1.992 |
288.15 | 0.7508 | 1.767 |
288.15 | 0.8000 | 1.531 |
288.15 | 0.8514 | 1.233 |
288.15 | 0.8990 | 0.8370 |
288.15 | 0.9485 | 0.4810 |
298.15 | 0.0502 | 0.6110 |
298.15 | 0.0983 | 1.108 |
298.15 | 0.1494 | 1.499 |
298.15 | 0.2006 | 1.773 |
298.15 | 0.2484 | 2.053 |
298.15 | 0.2989 | 2.247 |
298.15 | 0.3486 | 2.358 |
298.15 | 0.3972 | 2.463 |
298.15 | 0.4484 | 2.504 |
298.15 | 0.4981 | 2.542 |
298.15 | 0.5504 | 2.49 |
298.15 | 0.6006 | 2.401 |
298.15 | 0.6485 | 2.29 |
298.15 | 0.6985 | 2.104 |
298.15 | 0.7508 | 1.907 |
298.15 | 0.8000 | 1.634 |
298.15 | 0.8514 | 1.298 |
298.15 | 0.8990 | 0.9120 |
298.15 | 0.9485 | 0.4660 |
313.15 | 0.0502 | 0.6900 |
313.15 | 0.0983 | 1.224 |
313.15 | 0.1494 | 1.657 |
313.15 | 0.2006 | 2.002 |
313.15 | 0.2484 | 2.271 |
313.15 | 0.2989 | 2.46 |
313.15 | 0.3486 | 2.605 |
313.15 | 0.3972 | 2.709 |
313.15 | 0.4484 | 2.737 |
313.15 | 0.4981 | 2.725 |
313.15 | 0.5504 | 2.664 |
313.15 | 0.6006 | 2.57 |
313.15 | 0.6485 | 2.427 |
313.15 | 0.6985 | 2.251 |
313.15 | 0.7508 | 1.998 |
313.15 | 0.8000 | 1.701 |
313.15 | 0.8514 | 1.358 |
313.15 | 0.8990 | 0.9870 |
313.15 | 0.9485 | 0.5550 |
328.15 | 0.0502 | 0.7040 |
328.15 | 0.0983 | 1.256 |
328.15 | 0.1494 | 1.674 |
328.15 | 0.2006 | 2.086 |
328.15 | 0.2484 | 2.314 |
328.15 | 0.2989 | 2.565 |
328.15 | 0.3486 | 2.723 |
328.15 | 0.3972 | 2.77 |
328.15 | 0.4484 | 2.825 |
328.15 | 0.4981 | 2.811 |
328.15 | 0.5504 | 2.739 |
328.15 | 0.6006 | 2.604 |
328.15 | 0.6485 | 2.453 |
328.15 | 0.6985 | 2.24 |
328.15 | 0.7508 | 1.971 |
328.15 | 0.8000 | 1.662 |
328.15 | 0.8514 | 1.31 |
328.15 | 0.8990 | 0.9030 |
328.15 | 0.9485 | 0.4960 |
338.15 | 0.0502 | 0.6940 |
338.15 | 0.0983 | 1.245 |
338.15 | 0.1494 | 1.701 |
338.15 | 0.2006 | 2.089 |
338.15 | 0.2484 | 2.338 |
338.15 | 0.2989 | 2.55 |
338.15 | 0.3486 | 2.71 |
338.15 | 0.3972 | 2.798 |
338.15 | 0.4484 | 2.82 |
338.15 | 0.4981 | 2.803 |
338.15 | 0.5504 | 2.735 |
338.15 | 0.6006 | 2.585 |
338.15 | 0.6485 | 2.439 |
338.15 | 0.6985 | 2.201 |
338.15 | 0.7508 | 1.927 |
338.15 | 0.8000 | 1.624 |
338.15 | 0.8514 | 1.274 |
338.15 | 0.8990 | 0.9380 |
338.15 | 0.9485 | 0.5190 |
348.15 | 0.0502 | 0.6660 |
348.15 | 0.0983 | 1.239 |
348.15 | 0.1494 | 1.696 |
348.15 | 0.2006 | 2.07 |
348.15 | 0.2484 | 2.334 |
348.15 | 0.2989 | 2.561 |
348.15 | 0.3486 | 2.701 |
348.15 | 0.3972 | 2.782 |
348.15 | 0.4484 | 2.812 |
348.15 | 0.4981 | 2.784 |
348.15 | 0.5504 | 2.699 |
348.15 | 0.6006 | 2.582 |
348.15 | 0.6485 | 2.415 |
348.15 | 0.6985 | 2.206 |
348.15 | 0.7508 | 1.934 |
348.15 | 0.8000 | 1.609 |
348.15 | 0.8514 | 1.241 |
348.15 | 0.8990 | 0.8820 |
348.15 | 0.9485 | 0.4850 |
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 |
288.15 | 0.0502 | 0.6110 |
288.15 | 0.0983 | 1.054 |
288.15 | 0.1494 | 1.397 |
288.15 | 0.2006 | 1.681 |
288.15 | 0.2484 | 1.89 |
288.15 | 0.2989 | 2.06 |
288.15 | 0.3486 | 2.183 |
288.15 | 0.3972 | 2.265 |
288.15 | 0.4484 | 2.314 |
288.15 | 0.4981 | 2.342 |
288.15 | 0.5504 | 2.316 |
288.15 | 0.6006 | 2.23 |
288.15 | 0.6485 | 2.135 |
288.15 | 0.6985 | 1.992 |
288.15 | 0.7508 | 1.767 |
288.15 | 0.8000 | 1.531 |
288.15 | 0.8514 | 1.233 |
288.15 | 0.8990 | 0.8370 |
288.15 | 0.9485 | 0.4810 |
298.15 | 0.0502 | 0.6110 |
298.15 | 0.0983 | 1.108 |
298.15 | 0.1494 | 1.499 |
298.15 | 0.2006 | 1.773 |
298.15 | 0.2484 | 2.053 |
298.15 | 0.2989 | 2.247 |
298.15 | 0.3486 | 2.358 |
298.15 | 0.3972 | 2.463 |
298.15 | 0.4484 | 2.504 |
298.15 | 0.4981 | 2.542 |
298.15 | 0.5504 | 2.49 |
298.15 | 0.6006 | 2.401 |
298.15 | 0.6485 | 2.29 |
298.15 | 0.6985 | 2.104 |
298.15 | 0.7508 | 1.907 |
298.15 | 0.8000 | 1.634 |
298.15 | 0.8514 | 1.298 |
298.15 | 0.8990 | 0.9120 |
298.15 | 0.9485 | 0.4660 |
313.15 | 0.0502 | 0.6900 |
313.15 | 0.0983 | 1.224 |
313.15 | 0.1494 | 1.657 |
313.15 | 0.2006 | 2.002 |
313.15 | 0.2484 | 2.271 |
313.15 | 0.2989 | 2.46 |
313.15 | 0.3486 | 2.605 |
313.15 | 0.3972 | 2.709 |
313.15 | 0.4484 | 2.737 |
313.15 | 0.4981 | 2.725 |
313.15 | 0.5504 | 2.664 |
313.15 | 0.6006 | 2.57 |
313.15 | 0.6485 | 2.427 |
313.15 | 0.6985 | 2.251 |
313.15 | 0.7508 | 1.998 |
313.15 | 0.8000 | 1.701 |
313.15 | 0.8514 | 1.358 |
313.15 | 0.8990 | 0.9870 |
313.15 | 0.9485 | 0.5550 |
328.15 | 0.0502 | 0.7040 |
328.15 | 0.0983 | 1.256 |
328.15 | 0.1494 | 1.674 |
328.15 | 0.2006 | 2.086 |
328.15 | 0.2484 | 2.314 |
328.15 | 0.2989 | 2.565 |
328.15 | 0.3486 | 2.723 |
328.15 | 0.3972 | 2.77 |
328.15 | 0.4484 | 2.825 |
328.15 | 0.4981 | 2.811 |
328.15 | 0.5504 | 2.739 |
328.15 | 0.6006 | 2.604 |
328.15 | 0.6485 | 2.453 |
328.15 | 0.6985 | 2.24 |
328.15 | 0.7508 | 1.971 |
328.15 | 0.8000 | 1.662 |
328.15 | 0.8514 | 1.31 |
328.15 | 0.8990 | 0.9030 |
328.15 | 0.9485 | 0.4960 |
338.15 | 0.0502 | 0.6940 |
338.15 | 0.0983 | 1.245 |
338.15 | 0.1494 | 1.701 |
338.15 | 0.2006 | 2.089 |
338.15 | 0.2484 | 2.338 |
338.15 | 0.2989 | 2.55 |
338.15 | 0.3486 | 2.71 |
338.15 | 0.3972 | 2.798 |
338.15 | 0.4484 | 2.82 |
338.15 | 0.4981 | 2.803 |
338.15 | 0.5504 | 2.735 |
338.15 | 0.6006 | 2.585 |
338.15 | 0.6485 | 2.439 |
338.15 | 0.6985 | 2.201 |
338.15 | 0.7508 | 1.927 |
338.15 | 0.8000 | 1.624 |
338.15 | 0.8514 | 1.274 |
338.15 | 0.8990 | 0.9380 |
338.15 | 0.9485 | 0.5190 |
348.15 | 0.0502 | 0.6660 |
348.15 | 0.0983 | 1.239 |
348.15 | 0.1494 | 1.696 |
348.15 | 0.2006 | 2.07 |
348.15 | 0.2484 | 2.334 |
348.15 | 0.2989 | 2.561 |
348.15 | 0.3486 | 2.701 |
348.15 | 0.3972 | 2.782 |
348.15 | 0.4484 | 2.812 |
348.15 | 0.4981 | 2.784 |
348.15 | 0.5504 | 2.699 |
348.15 | 0.6006 | 2.582 |
348.15 | 0.6485 | 2.415 |
348.15 | 0.6985 | 2.206 |
348.15 | 0.7508 | 1.934 |
348.15 | 0.8000 | 1.609 |
348.15 | 0.8514 | 1.241 |
348.15 | 0.8990 | 0.8820 |
348.15 | 0.9485 | 0.4850 |
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 | 805.6 |
288.15 | 0.1000 | 843.381 |
288.15 | 0.2000 | 877.394 |
288.15 | 0.3000 | 908.051 |
288.15 | 0.3500 | 922.305 |
288.15 | 0.3999 | 935.772 |
288.15 | 0.4495 | 948.602 |
288.15 | 0.5001 | 961.044 |
288.15 | 0.6001 | 984.156 |
288.15 | 0.6999 | 1005.333 |
288.15 | 0.8003 | 1025.057 |
288.15 | 0.9000 | 1043.277 |
288.15 | 1.0000 | 1060.326 |
298.15 | 0.0000 | 797.916 |
298.15 | 0.1000 | 835.034 |
298.15 | 0.2000 | 868.517 |
298.15 | 0.3000 | 898.746 |
298.15 | 0.3500 | 912.816 |
298.15 | 0.3999 | 926.126 |
298.15 | 0.4495 | 938.806 |
298.15 | 0.5001 | 951.116 |
298.15 | 0.6001 | 973.999 |
298.15 | 0.6999 | 995.001 |
298.15 | 0.8003 | 1014.571 |
298.15 | 0.9000 | 1032.669 |
298.15 | 1.0000 | 1049.603 |
313.15 | 0.0000 | 786.069 |
313.15 | 0.1000 | 822.221 |
313.15 | 0.2000 | 854.953 |
313.15 | 0.3000 | 884.583 |
313.15 | 0.3500 | 898.402 |
313.15 | 0.3999 | 911.47 |
313.15 | 0.4495 | 923.966 |
313.15 | 0.5001 | 936.085 |
313.15 | 0.6001 | 958.66 |
313.15 | 0.6999 | 979.414 |
313.15 | 0.8003 | 998.792 |
313.15 | 0.9000 | 1016.712 |
313.15 | 1.0000 | 1033.498 |
328.15 | 0.0000 | 773.692 |
328.15 | 0.1000 | 808.976 |
328.15 | 0.2000 | 841.015 |
328.15 | 0.3000 | 870.102 |
328.15 | 0.3500 | 885.344 |
328.15 | 0.3999 | 896.55 |
328.15 | 0.4495 | 908.867 |
328.15 | 0.5001 | 920.835 |
328.15 | 0.6001 | 943.14 |
328.15 | 0.6999 | 963.679 |
328.15 | 0.8003 | 982.885 |
328.15 | 0.9000 | 1000.67 |
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 | 805.6 |
288.15 | 0.1000 | 843.381 |
288.15 | 0.2000 | 877.394 |
288.15 | 0.3000 | 908.051 |
288.15 | 0.3500 | 922.305 |
288.15 | 0.3999 | 935.772 |
288.15 | 0.4495 | 948.602 |
288.15 | 0.5001 | 961.044 |
288.15 | 0.6001 | 984.156 |
288.15 | 0.6999 | 1005.333 |
288.15 | 0.8003 | 1025.057 |
288.15 | 0.9000 | 1043.277 |
288.15 | 1.0000 | 1060.326 |
298.15 | 0.0000 | 797.916 |
298.15 | 0.1000 | 835.034 |
298.15 | 0.2000 | 868.517 |
298.15 | 0.3000 | 898.746 |
298.15 | 0.3500 | 912.816 |
298.15 | 0.3999 | 926.126 |
298.15 | 0.4495 | 938.806 |
298.15 | 0.5001 | 951.116 |
298.15 | 0.6001 | 973.999 |
298.15 | 0.6999 | 995.001 |
298.15 | 0.8003 | 1014.571 |
298.15 | 0.9000 | 1032.669 |
298.15 | 1.0000 | 1049.603 |
313.15 | 0.0000 | 786.069 |
313.15 | 0.1000 | 822.221 |
313.15 | 0.2000 | 854.953 |
313.15 | 0.3000 | 884.583 |
313.15 | 0.3500 | 898.402 |
313.15 | 0.3999 | 911.47 |
313.15 | 0.4495 | 923.966 |
313.15 | 0.5001 | 936.085 |
313.15 | 0.6001 | 958.66 |
313.15 | 0.6999 | 979.414 |
313.15 | 0.8003 | 998.792 |
313.15 | 0.9000 | 1016.712 |
313.15 | 1.0000 | 1033.498 |
328.15 | 0.0000 | 773.692 |
328.15 | 0.1000 | 808.976 |
328.15 | 0.2000 | 841.015 |
328.15 | 0.3000 | 870.102 |
328.15 | 0.3500 | 885.344 |
328.15 | 0.3999 | 896.55 |
328.15 | 0.4495 | 908.867 |
328.15 | 0.5001 | 920.835 |
328.15 | 0.6001 | 943.14 |
328.15 | 0.6999 | 963.679 |
328.15 | 0.8003 | 982.885 |
328.15 | 0.9000 | 1000.67 |
328.15 | 1.0000 | 1017.336 |