Operational conditions:
Fixed | Measured | |
---|---|---|
Solvent: Amount ratio of component to other component of binary solvent of Cyclohexane (3) - Liquid | Mole fraction of Tetrahydrofuran (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.3413 | 0.0501 | 0.1605 |
0.3413 | 0.1000 | 0.2847 |
0.3413 | 0.1500 | 0.3962 |
0.3413 | 0.2000 | 0.5065 |
0.3413 | 0.2500 | 0.5943 |
0.3413 | 0.3001 | 0.6744 |
0.3413 | 0.3502 | 0.7407 |
0.3413 | 0.4000 | 0.7889 |
0.3413 | 0.4511 | 0.8146 |
0.3413 | 0.5006 | 0.8326 |
0.3413 | 0.5501 | 0.8387 |
0.3413 | 0.5996 | 0.8262 |
0.3413 | 0.6498 | 0.7973 |
0.3413 | 0.7001 | 0.7494 |
0.3413 | 0.7498 | 0.6838 |
0.3413 | 0.7996 | 0.5969 |
0.3413 | 0.8503 | 0.4888 |
0.3413 | 0.8999 | 0.3571 |
0.3413 | 0.9499 | 0.1939 |
0.9997 | 0.0500 | 0.1461 |
0.9997 | 0.0514 | 0.1465 |
0.9997 | 0.1000 | 0.2703 |
0.9997 | 0.1501 | 0.3757 |
0.9997 | 0.1999 | 0.4759 |
0.9997 | 0.2001 | 0.4766 |
0.9997 | 0.2503 | 0.5603 |
0.9997 | 0.3000 | 0.6326 |
0.9997 | 0.3502 | 0.6862 |
0.9997 | 0.4001 | 0.7199 |
0.9997 | 0.4507 | 0.7484 |
0.9997 | 0.5502 | 0.7609 |
0.9997 | 0.5997 | 0.7482 |
0.9997 | 0.6504 | 0.7184 |
0.9997 | 0.7003 | 0.6682 |
0.9997 | 0.7497 | 0.6038 |
0.9997 | 0.7999 | 0.5262 |
0.9997 | 0.8498 | 0.4266 |
0.9997 | 0.8997 | 0.3070 |
0.9997 | 0.9495 | 0.1666 |
2.9976 | 0.0500 | 0.1446 |
2.9976 | 0.0999 | 0.2625 |
2.9976 | 0.1501 | 0.3718 |
2.9976 | 0.2000 | 0.4607 |
2.9976 | 0.2502 | 0.5378 |
2.9976 | 0.3001 | 0.6035 |
2.9976 | 0.3501 | 0.6442 |
2.9976 | 0.3999 | 0.6785 |
2.9976 | 0.4501 | 0.6978 |
2.9976 | 0.4997 | 0.7020 |
2.9976 | 0.5498 | 0.7022 |
2.9976 | 0.6001 | 0.6841 |
2.9976 | 0.6498 | 0.6453 |
2.9976 | 0.7003 | 0.5996 |
2.9976 | 0.7501 | 0.5373 |
2.9976 | 0.7999 | 0.4606 |
2.9976 | 0.8501 | 0.3665 |
2.9976 | 0.9001 | 0.2417 |
2.9976 | 0.9500 | 0.1183 |
Operational conditions:
Fixed | Measured | |
---|---|---|
Solvent: Amount ratio of component to other component of binary solvent of Cyclohexane (3) - Liquid | Mole fraction of Tetrahydrofuran (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.3413 | 0.0501 | 0.1605 |
0.3413 | 0.1000 | 0.2847 |
0.3413 | 0.1500 | 0.3962 |
0.3413 | 0.2000 | 0.5065 |
0.3413 | 0.2500 | 0.5943 |
0.3413 | 0.3001 | 0.6744 |
0.3413 | 0.3502 | 0.7407 |
0.3413 | 0.4000 | 0.7889 |
0.3413 | 0.4511 | 0.8146 |
0.3413 | 0.5006 | 0.8326 |
0.3413 | 0.5501 | 0.8387 |
0.3413 | 0.5996 | 0.8262 |
0.3413 | 0.6498 | 0.7973 |
0.3413 | 0.7001 | 0.7494 |
0.3413 | 0.7498 | 0.6838 |
0.3413 | 0.7996 | 0.5969 |
0.3413 | 0.8503 | 0.4888 |
0.3413 | 0.8999 | 0.3571 |
0.3413 | 0.9499 | 0.1939 |
0.9997 | 0.0500 | 0.1461 |
0.9997 | 0.0514 | 0.1465 |
0.9997 | 0.1000 | 0.2703 |
0.9997 | 0.1501 | 0.3757 |
0.9997 | 0.1999 | 0.4759 |
0.9997 | 0.2001 | 0.4766 |
0.9997 | 0.2503 | 0.5603 |
0.9997 | 0.3000 | 0.6326 |
0.9997 | 0.3502 | 0.6862 |
0.9997 | 0.4001 | 0.7199 |
0.9997 | 0.4507 | 0.7484 |
0.9997 | 0.5502 | 0.7609 |
0.9997 | 0.5997 | 0.7482 |
0.9997 | 0.6504 | 0.7184 |
0.9997 | 0.7003 | 0.6682 |
0.9997 | 0.7497 | 0.6038 |
0.9997 | 0.7999 | 0.5262 |
0.9997 | 0.8498 | 0.4266 |
0.9997 | 0.8997 | 0.3070 |
0.9997 | 0.9495 | 0.1666 |
2.9976 | 0.0500 | 0.1446 |
2.9976 | 0.0999 | 0.2625 |
2.9976 | 0.1501 | 0.3718 |
2.9976 | 0.2000 | 0.4607 |
2.9976 | 0.2502 | 0.5378 |
2.9976 | 0.3001 | 0.6035 |
2.9976 | 0.3501 | 0.6442 |
2.9976 | 0.3999 | 0.6785 |
2.9976 | 0.4501 | 0.6978 |
2.9976 | 0.4997 | 0.7020 |
2.9976 | 0.5498 | 0.7022 |
2.9976 | 0.6001 | 0.6841 |
2.9976 | 0.6498 | 0.6453 |
2.9976 | 0.7003 | 0.5996 |
2.9976 | 0.7501 | 0.5373 |
2.9976 | 0.7999 | 0.4606 |
2.9976 | 0.8501 | 0.3665 |
2.9976 | 0.9001 | 0.2417 |
2.9976 | 0.9500 | 0.1183 |