Operational conditions:
Mole fraction of Ethanol, 2,2,2-trifluoro- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0055 | -0.0288 |
0.0109 | -0.0543 |
0.0203 | -0.0915 |
0.0306 | -0.1055 |
0.0402 | -0.1030 |
0.0498 | -0.0940 |
0.0599 | -0.0818 |
0.0700 | -0.0666 |
0.0795 | -0.0510 |
0.0899 | -0.0331 |
0.0994 | -0.0140 |
0.1100 | 0.0033 |
0.1193 | 0.0221 |
0.1299 | 0.0406 |
0.1385 | 0.0599 |
0.1486 | 0.0802 |
0.1983 | 0.1774 |
0.2988 | 0.3620 |
0.3988 | 0.5145 |
0.4955 | 0.6264 |
0.5989 | 0.6950 |
0.7078 | 0.6900 |
0.8079 | 0.5423 |
0.8980 | 0.3053 |
0.9054 | 0.2842 |
0.9202 | 0.2398 |
0.9301 | 0.2089 |
0.9387 | 0.1871 |
0.9528 | 0.1441 |
0.9646 | 0.1042 |
0.9732 | 0.0792 |
0.9880 | 0.0403 |
0.9952 | 0.0140 |
Operational conditions:
Mole fraction of Ethanol, 2,2,2-trifluoro- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0055 | -0.0288 |
0.0109 | -0.0543 |
0.0203 | -0.0915 |
0.0306 | -0.1055 |
0.0402 | -0.1030 |
0.0498 | -0.0940 |
0.0599 | -0.0818 |
0.0700 | -0.0666 |
0.0795 | -0.0510 |
0.0899 | -0.0331 |
0.0994 | -0.0140 |
0.1100 | 0.0033 |
0.1193 | 0.0221 |
0.1299 | 0.0406 |
0.1385 | 0.0599 |
0.1486 | 0.0802 |
0.1983 | 0.1774 |
0.2988 | 0.3620 |
0.3988 | 0.5145 |
0.4955 | 0.6264 |
0.5989 | 0.6950 |
0.7078 | 0.6900 |
0.8079 | 0.5423 |
0.8980 | 0.3053 |
0.9054 | 0.2842 |
0.9202 | 0.2398 |
0.9301 | 0.2089 |
0.9387 | 0.1871 |
0.9528 | 0.1441 |
0.9646 | 0.1042 |
0.9732 | 0.0792 |
0.9880 | 0.0403 |
0.9952 | 0.0140 |
Operational conditions:
Mole fraction of Ethanol, 2,2,2-trifluoro- (1) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0000 | 997.05 |
0.0048 | 1005.99 |
0.0103 | 1016.28 |
0.0186 | 1031.19 |
0.0223 | 1037.71 |
0.1002 | 1139.98 |
0.1985 | 1215.51 |
0.3000 | 1265.59 |
0.3983 | 1298.93 |
0.4965 | 1322.87 |
0.5995 | 1341.54 |
0.7303 | 1359.16 |
0.8390 | 1370.38 |
0.9062 | 1376.17 |
0.9696 | 1381.16 |
0.9800 | 1381.89 |
0.9899 | 1382.59 |
0.9950 | 1382.97 |
1.0000 | 1383.41 |
Operational conditions:
Mole fraction of Ethanol, 2,2,2-trifluoro- (1) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0000 | 997.05 |
0.0048 | 1005.99 |
0.0103 | 1016.28 |
0.0186 | 1031.19 |
0.0223 | 1037.71 |
0.1002 | 1139.98 |
0.1985 | 1215.51 |
0.3000 | 1265.59 |
0.3983 | 1298.93 |
0.4965 | 1322.87 |
0.5995 | 1341.54 |
0.7303 | 1359.16 |
0.8390 | 1370.38 |
0.9062 | 1376.17 |
0.9696 | 1381.16 |
0.9800 | 1381.89 |
0.9899 | 1382.59 |
0.9950 | 1382.97 |
1.0000 | 1383.41 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of Ethanol, 2,2,2-trifluoro- (1) - Liquid | Temperature, K - Liquid | Binary diffusion coefficient, m2/s - Liquid |
0.0005 | 283.20 | 0.0000 |
0.0005 | 288.20 | 0.0000 |
0.0005 | 293.20 | 0.0000 |
0.0005 | 298.20 | 0.0000 |
0.0005 | 303.20 | 0.0000 |
0.0005 | 308.20 | 0.0000 |
0.0005 | 313.20 | 0.0000 |
0.0010 | 283.20 | 0.0000 |
0.0010 | 288.20 | 0.0000 |
0.0010 | 293.20 | 0.0000 |
0.0010 | 298.20 | 0.0000 |
0.0010 | 303.20 | 0.0000 |
0.0010 | 308.20 | 0.0000 |
0.0010 | 313.20 | 0.0000 |
0.0050 | 283.20 | 0.0000 |
0.0050 | 288.20 | 0.0000 |
0.0050 | 293.20 | 0.0000 |
0.0050 | 298.20 | 0.0000 |
0.0050 | 303.20 | 0.0000 |
0.0050 | 308.20 | 0.0000 |
0.0050 | 313.20 | 0.0000 |
0.0093 | 283.20 | 0.0000 |
0.0093 | 288.20 | 0.0000 |
0.0093 | 293.20 | 0.0000 |
0.0093 | 298.20 | 0.0000 |
0.0093 | 303.20 | 0.0000 |
0.0093 | 308.20 | 0.0000 |
0.0093 | 313.20 | 0.0000 |
0.0101 | 283.20 | 0.0000 |
0.0101 | 288.20 | 0.0000 |
0.0101 | 293.20 | 0.0000 |
0.0101 | 298.20 | 0.0000 |
0.0101 | 303.20 | 0.0000 |
0.0101 | 308.20 | 0.0000 |
0.0101 | 313.20 | 0.0000 |
0.0496 | 283.20 | 0.0000 |
0.0496 | 288.20 | 0.0000 |
0.0496 | 293.20 | 0.0000 |
0.0496 | 298.20 | 0.0000 |
0.0496 | 303.20 | 0.0000 |
0.0496 | 308.20 | 0.0000 |
0.0496 | 313.20 | 0.0000 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of Ethanol, 2,2,2-trifluoro- (1) - Liquid | Temperature, K - Liquid | Binary diffusion coefficient, m2/s - Liquid |
0.0005 | 283.20 | 0.0000 |
0.0005 | 288.20 | 0.0000 |
0.0005 | 293.20 | 0.0000 |
0.0005 | 298.20 | 0.0000 |
0.0005 | 303.20 | 0.0000 |
0.0005 | 308.20 | 0.0000 |
0.0005 | 313.20 | 0.0000 |
0.0010 | 283.20 | 0.0000 |
0.0010 | 288.20 | 0.0000 |
0.0010 | 293.20 | 0.0000 |
0.0010 | 298.20 | 0.0000 |
0.0010 | 303.20 | 0.0000 |
0.0010 | 308.20 | 0.0000 |
0.0010 | 313.20 | 0.0000 |
0.0050 | 283.20 | 0.0000 |
0.0050 | 288.20 | 0.0000 |
0.0050 | 293.20 | 0.0000 |
0.0050 | 298.20 | 0.0000 |
0.0050 | 303.20 | 0.0000 |
0.0050 | 308.20 | 0.0000 |
0.0050 | 313.20 | 0.0000 |
0.0093 | 283.20 | 0.0000 |
0.0093 | 288.20 | 0.0000 |
0.0093 | 293.20 | 0.0000 |
0.0093 | 298.20 | 0.0000 |
0.0093 | 303.20 | 0.0000 |
0.0093 | 308.20 | 0.0000 |
0.0093 | 313.20 | 0.0000 |
0.0101 | 283.20 | 0.0000 |
0.0101 | 288.20 | 0.0000 |
0.0101 | 293.20 | 0.0000 |
0.0101 | 298.20 | 0.0000 |
0.0101 | 303.20 | 0.0000 |
0.0101 | 308.20 | 0.0000 |
0.0101 | 313.20 | 0.0000 |
0.0496 | 283.20 | 0.0000 |
0.0496 | 288.20 | 0.0000 |
0.0496 | 293.20 | 0.0000 |
0.0496 | 298.20 | 0.0000 |
0.0496 | 303.20 | 0.0000 |
0.0496 | 308.20 | 0.0000 |
0.0496 | 313.20 | 0.0000 |