Operational conditions:
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Tetrahydrofuran (3) - Liquid | Solvent: Amount ratio of component to other component of binary solvent of Propane, 2-methoxy-2-methyl- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0499 | 0.9996 | 0.0546 |
| 0.0499 | 3.0003 | 0.0402 |
| 0.0501 | 0.3333 | 0.1046 |
| 0.0999 | 0.9996 | 0.1313 |
| 0.1001 | 0.3333 | 0.2087 |
| 0.1004 | 3.0003 | 0.0740 |
| 0.1500 | 0.9996 | 0.1884 |
| 0.1500 | 3.0003 | 0.1076 |
| 0.1537 | 0.3333 | 0.2953 |
| 0.2000 | 0.3333 | 0.3593 |
| 0.2002 | 0.9996 | 0.2382 |
| 0.2005 | 3.0003 | 0.1360 |
| 0.2498 | 0.3333 | 0.4250 |
| 0.2500 | 0.9996 | 0.2812 |
| 0.2501 | 3.0003 | 0.1581 |
| 0.3001 | 0.3333 | 0.4825 |
| 0.3003 | 0.9996 | 0.3174 |
| 0.3005 | 3.0003 | 0.1802 |
| 0.3496 | 3.0003 | 0.1957 |
| 0.3498 | 0.3333 | 0.5259 |
| 0.3498 | 0.9996 | 0.3465 |
| 0.3990 | 0.3333 | 0.5613 |
| 0.3991 | 0.9996 | 0.3686 |
| 0.4007 | 3.0003 | 0.2100 |
| 0.4493 | 0.3333 | 0.5851 |
| 0.4493 | 3.0003 | 0.2172 |
| 0.4504 | 0.9996 | 0.3859 |
| 0.4988 | 3.0003 | 0.2242 |
| 0.4999 | 0.3333 | 0.5927 |
| 0.5008 | 0.9996 | 0.3959 |
| 0.5496 | 0.3333 | 0.6004 |
| 0.5496 | 0.9996 | 0.3978 |
| 0.5525 | 3.0003 | 0.2240 |
| 0.5999 | 0.3333 | 0.5910 |
| 0.6002 | 0.9996 | 0.3894 |
| 0.6002 | 3.0003 | 0.2202 |
| 0.6498 | 0.3333 | 0.5693 |
| 0.6498 | 3.0003 | 0.2117 |
| 0.6504 | 0.9996 | 0.3731 |
| 0.6998 | 0.3333 | 0.5341 |
| 0.7001 | 0.9996 | 0.3508 |
| 0.7003 | 3.0003 | 0.1971 |
| 0.7498 | 0.3333 | 0.4853 |
| 0.7502 | 0.9996 | 0.3189 |
| 0.7513 | 3.0003 | 0.1771 |
| 0.7987 | 3.0003 | 0.1543 |
| 0.7998 | 0.3333 | 0.4208 |
| 0.8003 | 0.9996 | 0.2775 |
| 0.8498 | 0.9996 | 0.2248 |
| 0.8500 | 0.3333 | 0.3460 |
| 0.8514 | 3.0003 | 0.1222 |
| 0.8988 | 3.0003 | 0.0872 |
| 0.9001 | 0.3333 | 0.2487 |
| 0.9003 | 0.9996 | 0.1623 |
| 0.9497 | 3.0003 | 0.0519 |
| 0.9500 | 0.9996 | 0.0849 |
| 0.9501 | 0.3333 | 0.1352 |
Operational conditions:
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Tetrahydrofuran (3) - Liquid | Solvent: Amount ratio of component to other component of binary solvent of Propane, 2-methoxy-2-methyl- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0499 | 0.9996 | 0.0546 |
| 0.0499 | 3.0003 | 0.0402 |
| 0.0501 | 0.3333 | 0.1046 |
| 0.0999 | 0.9996 | 0.1313 |
| 0.1001 | 0.3333 | 0.2087 |
| 0.1004 | 3.0003 | 0.0740 |
| 0.1500 | 0.9996 | 0.1884 |
| 0.1500 | 3.0003 | 0.1076 |
| 0.1537 | 0.3333 | 0.2953 |
| 0.2000 | 0.3333 | 0.3593 |
| 0.2002 | 0.9996 | 0.2382 |
| 0.2005 | 3.0003 | 0.1360 |
| 0.2498 | 0.3333 | 0.4250 |
| 0.2500 | 0.9996 | 0.2812 |
| 0.2501 | 3.0003 | 0.1581 |
| 0.3001 | 0.3333 | 0.4825 |
| 0.3003 | 0.9996 | 0.3174 |
| 0.3005 | 3.0003 | 0.1802 |
| 0.3496 | 3.0003 | 0.1957 |
| 0.3498 | 0.3333 | 0.5259 |
| 0.3498 | 0.9996 | 0.3465 |
| 0.3990 | 0.3333 | 0.5613 |
| 0.3991 | 0.9996 | 0.3686 |
| 0.4007 | 3.0003 | 0.2100 |
| 0.4493 | 0.3333 | 0.5851 |
| 0.4493 | 3.0003 | 0.2172 |
| 0.4504 | 0.9996 | 0.3859 |
| 0.4988 | 3.0003 | 0.2242 |
| 0.4999 | 0.3333 | 0.5927 |
| 0.5008 | 0.9996 | 0.3959 |
| 0.5496 | 0.3333 | 0.6004 |
| 0.5496 | 0.9996 | 0.3978 |
| 0.5525 | 3.0003 | 0.2240 |
| 0.5999 | 0.3333 | 0.5910 |
| 0.6002 | 0.9996 | 0.3894 |
| 0.6002 | 3.0003 | 0.2202 |
| 0.6498 | 0.3333 | 0.5693 |
| 0.6498 | 3.0003 | 0.2117 |
| 0.6504 | 0.9996 | 0.3731 |
| 0.6998 | 0.3333 | 0.5341 |
| 0.7001 | 0.9996 | 0.3508 |
| 0.7003 | 3.0003 | 0.1971 |
| 0.7498 | 0.3333 | 0.4853 |
| 0.7502 | 0.9996 | 0.3189 |
| 0.7513 | 3.0003 | 0.1771 |
| 0.7987 | 3.0003 | 0.1543 |
| 0.7998 | 0.3333 | 0.4208 |
| 0.8003 | 0.9996 | 0.2775 |
| 0.8498 | 0.9996 | 0.2248 |
| 0.8500 | 0.3333 | 0.3460 |
| 0.8514 | 3.0003 | 0.1222 |
| 0.8988 | 3.0003 | 0.0872 |
| 0.9001 | 0.3333 | 0.2487 |
| 0.9003 | 0.9996 | 0.1623 |
| 0.9497 | 3.0003 | 0.0519 |
| 0.9500 | 0.9996 | 0.0849 |
| 0.9501 | 0.3333 | 0.1352 |