Operational condition: Temperature, K = 298.15 (Liquid)
Mole fraction of Valeric anhydride (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0248 | 0.1962 |
0.0484 | 0.3620 |
0.0709 | 0.4948 |
0.0923 | 0.6106 |
0.1128 | 0.7091 |
0.1324 | 0.7914 |
0.1511 | 0.8656 |
0.1691 | 0.9273 |
0.1914 | 0.9980 |
0.2126 | 1.0588 |
0.2327 | 1.1104 |
0.2518 | 1.154 |
0.2699 | 1.1916 |
0.2827 | 1.2236 |
0.3038 | 1.251 |
0.3195 | 1.2743 |
0.3411 | 1.3166 |
0.3488 | 1.3261 |
0.3569 | 1.3348 |
0.3654 | 1.3438 |
0.3743 | 1.3518 |
0.3837 | 1.3601 |
0.3935 | 1.3667 |
0.4025 | 1.373 |
0.4118 | 1.3778 |
0.4217 | 1.3828 |
0.4320 | 1.386 |
0.4428 | 1.3891 |
0.4542 | 1.3915 |
0.4644 | 1.3918 |
0.4750 | 1.392 |
0.4861 | 1.3899 |
0.4978 | 1.3876 |
0.5100 | 1.3837 |
0.5229 | 1.3772 |
0.5342 | 1.3701 |
0.5461 | 1.3626 |
0.5585 | 1.3531 |
0.5715 | 1.3402 |
0.5851 | 1.3268 |
0.5993 | 1.311 |
0.6122 | 1.2943 |
0.6257 | 1.2746 |
0.6398 | 1.2535 |
0.6545 | 1.229 |
0.6699 | 1.2016 |
0.6861 | 1.1702 |
0.7003 | 1.1395 |
0.7151 | 1.1073 |
0.7305 | 1.0692 |
0.7467 | 1.0283 |
0.7635 | 0.9823 |
0.7811 | 0.9312 |
0.7967 | 0.8840 |
0.8129 | 0.8312 |
0.8298 | 0.7737 |
0.8474 | 0.7092 |
0.8657 | 0.6403 |
0.8849 | 0.5628 |
0.9022 | 0.4906 |
0.9202 | 0.4082 |
0.9389 | 0.3213 |
0.9584 | 0.2211 |
0.9788 | 0.1170 |
Operational condition: Temperature, K = 298.15 (Liquid)
Mole fraction of Valeric anhydride (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0248 | 0.1962 |
0.0484 | 0.3620 |
0.0709 | 0.4948 |
0.0923 | 0.6106 |
0.1128 | 0.7091 |
0.1324 | 0.7914 |
0.1511 | 0.8656 |
0.1691 | 0.9273 |
0.1914 | 0.9980 |
0.2126 | 1.0588 |
0.2327 | 1.1104 |
0.2518 | 1.154 |
0.2699 | 1.1916 |
0.2827 | 1.2236 |
0.3038 | 1.251 |
0.3195 | 1.2743 |
0.3411 | 1.3166 |
0.3488 | 1.3261 |
0.3569 | 1.3348 |
0.3654 | 1.3438 |
0.3743 | 1.3518 |
0.3837 | 1.3601 |
0.3935 | 1.3667 |
0.4025 | 1.373 |
0.4118 | 1.3778 |
0.4217 | 1.3828 |
0.4320 | 1.386 |
0.4428 | 1.3891 |
0.4542 | 1.3915 |
0.4644 | 1.3918 |
0.4750 | 1.392 |
0.4861 | 1.3899 |
0.4978 | 1.3876 |
0.5100 | 1.3837 |
0.5229 | 1.3772 |
0.5342 | 1.3701 |
0.5461 | 1.3626 |
0.5585 | 1.3531 |
0.5715 | 1.3402 |
0.5851 | 1.3268 |
0.5993 | 1.311 |
0.6122 | 1.2943 |
0.6257 | 1.2746 |
0.6398 | 1.2535 |
0.6545 | 1.229 |
0.6699 | 1.2016 |
0.6861 | 1.1702 |
0.7003 | 1.1395 |
0.7151 | 1.1073 |
0.7305 | 1.0692 |
0.7467 | 1.0283 |
0.7635 | 0.9823 |
0.7811 | 0.9312 |
0.7967 | 0.8840 |
0.8129 | 0.8312 |
0.8298 | 0.7737 |
0.8474 | 0.7092 |
0.8657 | 0.6403 |
0.8849 | 0.5628 |
0.9022 | 0.4906 |
0.9202 | 0.4082 |
0.9389 | 0.3213 |
0.9584 | 0.2211 |
0.9788 | 0.1170 |