Operational conditions:
Mole fraction of 2-Butanone (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.1361 | -0.3560 |
0.2283 | -0.5400 |
0.3187 | -0.6760 |
0.4093 | -0.7810 |
0.5090 | -0.8160 |
0.6091 | -0.7790 |
0.7055 | -0.6720 |
0.8028 | -0.5060 |
0.9030 | -0.2800 |
Operational conditions:
Mole fraction of 2-Butanone (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.1361 | -0.3560 |
0.2283 | -0.5400 |
0.3187 | -0.6760 |
0.4093 | -0.7810 |
0.5090 | -0.8160 |
0.6091 | -0.7790 |
0.7055 | -0.6720 |
0.8028 | -0.5060 |
0.9030 | -0.2800 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 2-Butanone (2) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.0627 | 977.942 |
293.15 | 0.1133 | 970.977 |
293.15 | 0.1564 | 964.888 |
293.15 | 0.2058 | 957.75 |
293.15 | 0.2538 | 950.572 |
293.15 | 0.3018 | 943.182 |
293.15 | 0.3464 | 936.057 |
293.15 | 0.3938 | 928.444 |
293.15 | 0.4435 | 920.205 |
293.15 | 0.4907 | 912.022 |
293.15 | 0.5508 | 901.21 |
293.15 | 0.5959 | 892.779 |
293.15 | 0.6529 | 881.753 |
293.15 | 0.7489 | 862.241 |
293.15 | 0.7938 | 852.894 |
293.15 | 0.8492 | 840.63 |
293.15 | 0.8981 | 829.68 |
293.15 | 0.9525 | 816.716 |
298.15 | 0.0760 | 972.066 |
298.15 | 0.1115 | 967.149 |
298.15 | 0.1566 | 960.718 |
298.15 | 0.2076 | 953.334 |
298.15 | 0.2589 | 945.633 |
298.15 | 0.2967 | 939.765 |
298.15 | 0.3471 | 931.809 |
298.15 | 0.3973 | 923.563 |
298.15 | 0.4477 | 915.055 |
298.15 | 0.4950 | 906.694 |
298.15 | 0.5471 | 897.284 |
298.15 | 0.5992 | 887.579 |
298.15 | 0.6921 | 869.471 |
298.15 | 0.7463 | 858.202 |
298.15 | 0.8007 | 846.555 |
298.15 | 0.8470 | 836.277 |
298.15 | 0.8993 | 824.346 |
298.15 | 0.9472 | 813.0 |
303.15 | 0.0641 | 969.669 |
303.15 | 0.1123 | 962.964 |
303.15 | 0.1581 | 956.434 |
303.15 | 0.2036 | 949.789 |
303.15 | 0.2591 | 941.381 |
303.15 | 0.3061 | 934.049 |
303.15 | 0.3513 | 926.789 |
303.15 | 0.4022 | 918.424 |
303.15 | 0.4472 | 910.653 |
303.15 | 0.5025 | 900.926 |
303.15 | 0.5536 | 891.605 |
303.15 | 0.5984 | 883.203 |
303.15 | 0.6489 | 873.485 |
303.15 | 0.6969 | 863.705 |
303.15 | 0.7543 | 851.719 |
303.15 | 0.8047 | 840.797 |
303.15 | 0.8497 | 830.818 |
303.15 | 0.8965 | 819.999 |
303.15 | 0.9524 | 806.615 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 2-Butanone (2) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.0627 | 977.942 |
293.15 | 0.1133 | 970.977 |
293.15 | 0.1564 | 964.888 |
293.15 | 0.2058 | 957.75 |
293.15 | 0.2538 | 950.572 |
293.15 | 0.3018 | 943.182 |
293.15 | 0.3464 | 936.057 |
293.15 | 0.3938 | 928.444 |
293.15 | 0.4435 | 920.205 |
293.15 | 0.4907 | 912.022 |
293.15 | 0.5508 | 901.21 |
293.15 | 0.5959 | 892.779 |
293.15 | 0.6529 | 881.753 |
293.15 | 0.7489 | 862.241 |
293.15 | 0.7938 | 852.894 |
293.15 | 0.8492 | 840.63 |
293.15 | 0.8981 | 829.68 |
293.15 | 0.9525 | 816.716 |
298.15 | 0.0760 | 972.066 |
298.15 | 0.1115 | 967.149 |
298.15 | 0.1566 | 960.718 |
298.15 | 0.2076 | 953.334 |
298.15 | 0.2589 | 945.633 |
298.15 | 0.2967 | 939.765 |
298.15 | 0.3471 | 931.809 |
298.15 | 0.3973 | 923.563 |
298.15 | 0.4477 | 915.055 |
298.15 | 0.4950 | 906.694 |
298.15 | 0.5471 | 897.284 |
298.15 | 0.5992 | 887.579 |
298.15 | 0.6921 | 869.471 |
298.15 | 0.7463 | 858.202 |
298.15 | 0.8007 | 846.555 |
298.15 | 0.8470 | 836.277 |
298.15 | 0.8993 | 824.346 |
298.15 | 0.9472 | 813.0 |
303.15 | 0.0641 | 969.669 |
303.15 | 0.1123 | 962.964 |
303.15 | 0.1581 | 956.434 |
303.15 | 0.2036 | 949.789 |
303.15 | 0.2591 | 941.381 |
303.15 | 0.3061 | 934.049 |
303.15 | 0.3513 | 926.789 |
303.15 | 0.4022 | 918.424 |
303.15 | 0.4472 | 910.653 |
303.15 | 0.5025 | 900.926 |
303.15 | 0.5536 | 891.605 |
303.15 | 0.5984 | 883.203 |
303.15 | 0.6489 | 873.485 |
303.15 | 0.6969 | 863.705 |
303.15 | 0.7543 | 851.719 |
303.15 | 0.8047 | 840.797 |
303.15 | 0.8497 | 830.818 |
303.15 | 0.8965 | 819.999 |
303.15 | 0.9524 | 806.615 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 2-Butanone (2) - Liquid | Speed of sound, m/s - Liquid |
293.15 | 0.0627 | 1562.93 |
293.15 | 0.1133 | 1546.9 |
293.15 | 0.1564 | 1532.86 |
293.15 | 0.2058 | 1516.97 |
293.15 | 0.2538 | 1501.02 |
293.15 | 0.3018 | 1484.81 |
293.15 | 0.3464 | 1469.41 |
293.15 | 0.3938 | 1453.01 |
293.15 | 0.4435 | 1435.57 |
293.15 | 0.4907 | 1418.46 |
293.15 | 0.5508 | 1396.18 |
293.15 | 0.5959 | 1378.86 |
293.15 | 0.6529 | 1356.64 |
293.15 | 0.7489 | 1318.2 |
293.15 | 0.7938 | 1300.01 |
293.15 | 0.8492 | 1276.95 |
293.15 | 0.8981 | 1256.68 |
293.15 | 0.9525 | 1232.87 |
298.15 | 0.0760 | 1540.12 |
298.15 | 0.1115 | 1528.78 |
298.15 | 0.1566 | 1514.16 |
298.15 | 0.2076 | 1497.6 |
298.15 | 0.2589 | 1480.59 |
298.15 | 0.2967 | 1467.74 |
298.15 | 0.3471 | 1450.49 |
298.15 | 0.3973 | 1432.77 |
298.15 | 0.4477 | 1414.78 |
298.15 | 0.4950 | 1397.25 |
298.15 | 0.5471 | 1377.77 |
298.15 | 0.5992 | 1357.93 |
298.15 | 0.6921 | 1321.67 |
298.15 | 0.7463 | 1299.55 |
298.15 | 0.8007 | 1276.99 |
298.15 | 0.8470 | 1257.46 |
298.15 | 0.8993 | 1235.12 |
298.15 | 0.9472 | 1214.45 |
303.15 | 0.0641 | 1525.99 |
303.15 | 0.1123 | 1510.65 |
303.15 | 0.1581 | 1495.93 |
303.15 | 0.2036 | 1481.08 |
303.15 | 0.2591 | 1462.5 |
303.15 | 0.3061 | 1446.49 |
303.15 | 0.3513 | 1430.76 |
303.15 | 0.4022 | 1412.9 |
303.15 | 0.4472 | 1396.45 |
303.15 | 0.5025 | 1376.1 |
303.15 | 0.5536 | 1356.87 |
303.15 | 0.5984 | 1339.7 |
303.15 | 0.6489 | 1320.14 |
303.15 | 0.6969 | 1300.71 |
303.15 | 0.7543 | 1277.07 |
303.15 | 0.8047 | 1256.0 |
303.15 | 0.8497 | 1237.07 |
303.15 | 0.8965 | 1216.77 |
303.15 | 0.9524 | 1192.15 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 2-Butanone (2) - Liquid | Speed of sound, m/s - Liquid |
293.15 | 0.0627 | 1562.93 |
293.15 | 0.1133 | 1546.9 |
293.15 | 0.1564 | 1532.86 |
293.15 | 0.2058 | 1516.97 |
293.15 | 0.2538 | 1501.02 |
293.15 | 0.3018 | 1484.81 |
293.15 | 0.3464 | 1469.41 |
293.15 | 0.3938 | 1453.01 |
293.15 | 0.4435 | 1435.57 |
293.15 | 0.4907 | 1418.46 |
293.15 | 0.5508 | 1396.18 |
293.15 | 0.5959 | 1378.86 |
293.15 | 0.6529 | 1356.64 |
293.15 | 0.7489 | 1318.2 |
293.15 | 0.7938 | 1300.01 |
293.15 | 0.8492 | 1276.95 |
293.15 | 0.8981 | 1256.68 |
293.15 | 0.9525 | 1232.87 |
298.15 | 0.0760 | 1540.12 |
298.15 | 0.1115 | 1528.78 |
298.15 | 0.1566 | 1514.16 |
298.15 | 0.2076 | 1497.6 |
298.15 | 0.2589 | 1480.59 |
298.15 | 0.2967 | 1467.74 |
298.15 | 0.3471 | 1450.49 |
298.15 | 0.3973 | 1432.77 |
298.15 | 0.4477 | 1414.78 |
298.15 | 0.4950 | 1397.25 |
298.15 | 0.5471 | 1377.77 |
298.15 | 0.5992 | 1357.93 |
298.15 | 0.6921 | 1321.67 |
298.15 | 0.7463 | 1299.55 |
298.15 | 0.8007 | 1276.99 |
298.15 | 0.8470 | 1257.46 |
298.15 | 0.8993 | 1235.12 |
298.15 | 0.9472 | 1214.45 |
303.15 | 0.0641 | 1525.99 |
303.15 | 0.1123 | 1510.65 |
303.15 | 0.1581 | 1495.93 |
303.15 | 0.2036 | 1481.08 |
303.15 | 0.2591 | 1462.5 |
303.15 | 0.3061 | 1446.49 |
303.15 | 0.3513 | 1430.76 |
303.15 | 0.4022 | 1412.9 |
303.15 | 0.4472 | 1396.45 |
303.15 | 0.5025 | 1376.1 |
303.15 | 0.5536 | 1356.87 |
303.15 | 0.5984 | 1339.7 |
303.15 | 0.6489 | 1320.14 |
303.15 | 0.6969 | 1300.71 |
303.15 | 0.7543 | 1277.07 |
303.15 | 0.8047 | 1256.0 |
303.15 | 0.8497 | 1237.07 |
303.15 | 0.8965 | 1216.77 |
303.15 | 0.9524 | 1192.15 |