Operational conditions:
Mole fraction of Ethane, 1,1,1-trichloro- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0303 | -0.0605 |
0.0662 | -0.1350 |
0.1039 | -0.2080 |
0.1525 | -0.2939 |
0.2006 | -0.3745 |
0.2534 | -0.4429 |
0.3046 | -0.5090 |
0.3555 | -0.5549 |
0.4018 | -0.5823 |
0.4556 | -0.5831 |
0.5054 | -0.5816 |
0.5576 | -0.5713 |
0.6104 | -0.5898 |
0.6634 | -0.5882 |
0.7153 | -0.5638 |
0.7694 | -0.5100 |
0.8172 | -0.4905 |
0.8714 | -0.4329 |
0.9228 | -0.3277 |
0.9649 | -0.1827 |
Operational conditions:
Mole fraction of Ethane, 1,1,1-trichloro- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0303 | -0.0605 |
0.0662 | -0.1350 |
0.1039 | -0.2080 |
0.1525 | -0.2939 |
0.2006 | -0.3745 |
0.2534 | -0.4429 |
0.3046 | -0.5090 |
0.3555 | -0.5549 |
0.4018 | -0.5823 |
0.4556 | -0.5831 |
0.5054 | -0.5816 |
0.5576 | -0.5713 |
0.6104 | -0.5898 |
0.6634 | -0.5882 |
0.7153 | -0.5638 |
0.7694 | -0.5100 |
0.8172 | -0.4905 |
0.8714 | -0.4329 |
0.9228 | -0.3277 |
0.9649 | -0.1827 |
Operational condition: Pressure, kPa = 95.3 (Liquid)
Mole fraction of Ethane, 1,1,1-trichloro- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 473.25 |
0.1005 | 439.35 |
0.1937 | 415.35 |
0.3592 | 387.15 |
0.4683 | 374.85 |
0.6059 | 363.65 |
0.7193 | 356.85 |
0.8367 | 351.35 |
0.9275 | 347.85 |
1.0000 | 345.45 |
Operational condition: Pressure, kPa = 95.3 (Liquid)
Mole fraction of Ethane, 1,1,1-trichloro- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 473.25 |
0.1005 | 439.35 |
0.1937 | 415.35 |
0.3592 | 387.15 |
0.4683 | 374.85 |
0.6059 | 363.65 |
0.7193 | 356.85 |
0.8367 | 351.35 |
0.9275 | 347.85 |
1.0000 | 345.45 |