Operational condition: Pressure, kPa = 1000 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 | 0.0500 | 0.5360 |
298.15 | 0.1000 | 0.9932 |
298.15 | 0.1500 | 1.3757 |
298.15 | 0.2000 | 1.6901 |
298.15 | 0.2500 | 1.9583 |
298.15 | 0.3000 | 2.1605 |
298.15 | 0.3500 | 2.318 |
298.15 | 0.4000 | 2.4467 |
298.15 | 0.4500 | 2.5235 |
298.15 | 0.5000 | 2.5527 |
298.15 | 0.5500 | 2.5314 |
298.15 | 0.6000 | 2.4584 |
298.15 | 0.6500 | 2.3625 |
298.15 | 0.7000 | 2.2059 |
298.15 | 0.7500 | 1.9822 |
298.15 | 0.8000 | 1.7235 |
298.15 | 0.9000 | 1.0533 |
298.15 | 0.9500 | 0.5618 |
328.15 | 0.0500 | 0.5207 |
328.15 | 0.1000 | 0.9562 |
328.15 | 0.1500 | 1.3351 |
328.15 | 0.2000 | 1.6691 |
328.15 | 0.2500 | 1.9328 |
328.15 | 0.3000 | 2.1566 |
328.15 | 0.3500 | 2.3247 |
328.15 | 0.4000 | 2.4397 |
328.15 | 0.4500 | 2.5189 |
328.15 | 0.5000 | 2.5452 |
328.15 | 0.5500 | 2.5246 |
328.15 | 0.6000 | 2.4646 |
328.15 | 0.6500 | 2.3525 |
328.15 | 0.7000 | 2.1996 |
328.15 | 0.7500 | 1.9643 |
328.15 | 0.8000 | 1.7203 |
328.15 | 0.9000 | 1.0263 |
328.15 | 0.9500 | 0.5369 |
Operational condition: Pressure, kPa = 1000 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 | 0.0500 | 0.5360 |
298.15 | 0.1000 | 0.9932 |
298.15 | 0.1500 | 1.3757 |
298.15 | 0.2000 | 1.6901 |
298.15 | 0.2500 | 1.9583 |
298.15 | 0.3000 | 2.1605 |
298.15 | 0.3500 | 2.318 |
298.15 | 0.4000 | 2.4467 |
298.15 | 0.4500 | 2.5235 |
298.15 | 0.5000 | 2.5527 |
298.15 | 0.5500 | 2.5314 |
298.15 | 0.6000 | 2.4584 |
298.15 | 0.6500 | 2.3625 |
298.15 | 0.7000 | 2.2059 |
298.15 | 0.7500 | 1.9822 |
298.15 | 0.8000 | 1.7235 |
298.15 | 0.9000 | 1.0533 |
298.15 | 0.9500 | 0.5618 |
328.15 | 0.0500 | 0.5207 |
328.15 | 0.1000 | 0.9562 |
328.15 | 0.1500 | 1.3351 |
328.15 | 0.2000 | 1.6691 |
328.15 | 0.2500 | 1.9328 |
328.15 | 0.3000 | 2.1566 |
328.15 | 0.3500 | 2.3247 |
328.15 | 0.4000 | 2.4397 |
328.15 | 0.4500 | 2.5189 |
328.15 | 0.5000 | 2.5452 |
328.15 | 0.5500 | 2.5246 |
328.15 | 0.6000 | 2.4646 |
328.15 | 0.6500 | 2.3525 |
328.15 | 0.7000 | 2.1996 |
328.15 | 0.7500 | 1.9643 |
328.15 | 0.8000 | 1.7203 |
328.15 | 0.9000 | 1.0263 |
328.15 | 0.9500 | 0.5369 |
Operational condition: Pressure, kPa = 95.8 (Liquid)
Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 361.25 |
0.1510 | 355.95 |
0.2630 | 353.95 |
0.3430 | 353.05 |
0.4162 | 352.35 |
0.5510 | 351.95 |
0.6200 | 351.85 |
0.7101 | 351.95 |
0.8302 | 352.35 |
0.9072 | 352.95 |
1.0000 | 353.15 |
Operational condition: Pressure, kPa = 95.8 (Liquid)
Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 361.25 |
0.1510 | 355.95 |
0.2630 | 353.95 |
0.3430 | 353.05 |
0.4162 | 352.35 |
0.5510 | 351.95 |
0.6200 | 351.85 |
0.7101 | 351.95 |
0.8302 | 352.35 |
0.9072 | 352.95 |
1.0000 | 353.15 |