Operational condition: Pressure, kPa = 101.32 (Liquid)
| Mole fraction of n-Propyl acetate (1) - Liquid | Mole fraction of n-Propyl acetate (1) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0146 | 0.0061 |
| 0.0276 | 0.0102 |
| 0.0579 | 0.0170 |
| 0.1101 | 0.0241 |
| 0.1455 | 0.0303 |
| 0.1744 | 0.0352 |
| 0.2135 | 0.0400 |
| 0.3165 | 0.0574 |
| 0.4148 | 0.0791 |
| 0.5263 | 0.1092 |
| 0.6412 | 0.1542 |
| 0.7303 | 0.2110 |
| 0.7819 | 0.2622 |
| 0.8189 | 0.3160 |
| 0.8530 | 0.3782 |
| 0.8810 | 0.4411 |
| 0.9150 | 0.5433 |
| 0.9401 | 0.6420 |
| 0.9615 | 0.7451 |
| 0.9734 | 0.8131 |
| 0.9817 | 0.8650 |
| 0.9902 | 0.9250 |
| 0.9951 | 0.9611 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.32 (Liquid)
| Mole fraction of n-Propyl acetate (1) - Liquid | Mole fraction of n-Propyl acetate (1) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0146 | 0.0061 |
| 0.0276 | 0.0102 |
| 0.0579 | 0.0170 |
| 0.1101 | 0.0241 |
| 0.1455 | 0.0303 |
| 0.1744 | 0.0352 |
| 0.2135 | 0.0400 |
| 0.3165 | 0.0574 |
| 0.4148 | 0.0791 |
| 0.5263 | 0.1092 |
| 0.6412 | 0.1542 |
| 0.7303 | 0.2110 |
| 0.7819 | 0.2622 |
| 0.8189 | 0.3160 |
| 0.8530 | 0.3782 |
| 0.8810 | 0.4411 |
| 0.9150 | 0.5433 |
| 0.9401 | 0.6420 |
| 0.9615 | 0.7451 |
| 0.9734 | 0.8131 |
| 0.9817 | 0.8650 |
| 0.9902 | 0.9250 |
| 0.9951 | 0.9611 |
| 1.0000 | 1.0000 |
Operational conditions:
| Mole fraction of n-Propyl acetate (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0667 | 0.2240 |
| 0.1334 | 0.4060 |
| 0.2047 | 0.6170 |
| 0.2753 | 0.7800 |
| 0.3414 | 0.9140 |
| 0.4028 | 0.9880 |
| 0.4610 | 1.026 |
| 0.5088 | 1.031 |
| 0.5257 | 1.025 |
| 0.5824 | 0.9730 |
| 0.6434 | 0.8960 |
| 0.7089 | 0.7870 |
| 0.7812 | 0.6360 |
| 0.8537 | 0.4460 |
| 0.9242 | 0.2490 |
Operational conditions:
| Mole fraction of n-Propyl acetate (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0667 | 0.2240 |
| 0.1334 | 0.4060 |
| 0.2047 | 0.6170 |
| 0.2753 | 0.7800 |
| 0.3414 | 0.9140 |
| 0.4028 | 0.9880 |
| 0.4610 | 1.026 |
| 0.5088 | 1.031 |
| 0.5257 | 1.025 |
| 0.5824 | 0.9730 |
| 0.6434 | 0.8960 |
| 0.7089 | 0.7870 |
| 0.7812 | 0.6360 |
| 0.8537 | 0.4460 |
| 0.9242 | 0.2490 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of n-Propyl acetate (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0000 | 621.4 |
| 298.15 | 0.0101 | 623.7 |
| 298.15 | 0.0346 | 629.8 |
| 298.15 | 0.0754 | 640.0 |
| 298.15 | 0.1377 | 655.9 |
| 298.15 | 0.1977 | 671.4 |
| 298.15 | 0.2830 | 693.6 |
| 298.15 | 0.3439 | 709.7 |
| 298.15 | 0.4072 | 726.4 |
| 298.15 | 0.4881 | 747.7 |
| 298.15 | 0.5218 | 756.5 |
| 298.15 | 0.5968 | 776.4 |
| 298.15 | 0.6565 | 792.1 |
| 298.15 | 0.7085 | 805.9 |
| 298.15 | 0.8437 | 841.6 |
| 298.15 | 0.9205 | 861.8 |
| 298.15 | 1.0000 | 882.5 |
| 291.15 | 0.0000 | 628.2 |
| 291.15 | 0.0121 | 631.2 |
| 291.15 | 0.0427 | 638.8 |
| 291.15 | 0.0780 | 647.7 |
| 291.15 | 0.1417 | 664.0 |
| 291.15 | 0.2048 | 680.3 |
| 291.15 | 0.2734 | 698.2 |
| 291.15 | 0.3338 | 714.1 |
| 291.15 | 0.3934 | 729.8 |
| 291.15 | 0.4636 | 748.4 |
| 291.15 | 0.5224 | 763.9 |
| 291.15 | 0.5876 | 781.1 |
| 291.15 | 0.6565 | 799.3 |
| 291.15 | 0.7136 | 814.4 |
| 291.15 | 0.7697 | 829.2 |
| 291.15 | 0.8277 | 844.6 |
| 291.15 | 0.8911 | 861.3 |
| 291.15 | 0.9230 | 869.7 |
| 291.15 | 1.0000 | 889.6 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of n-Propyl acetate (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0000 | 621.4 |
| 298.15 | 0.0101 | 623.7 |
| 298.15 | 0.0346 | 629.8 |
| 298.15 | 0.0754 | 640.0 |
| 298.15 | 0.1377 | 655.9 |
| 298.15 | 0.1977 | 671.4 |
| 298.15 | 0.2830 | 693.6 |
| 298.15 | 0.3439 | 709.7 |
| 298.15 | 0.4072 | 726.4 |
| 298.15 | 0.4881 | 747.7 |
| 298.15 | 0.5218 | 756.5 |
| 298.15 | 0.5968 | 776.4 |
| 298.15 | 0.6565 | 792.1 |
| 298.15 | 0.7085 | 805.9 |
| 298.15 | 0.8437 | 841.6 |
| 298.15 | 0.9205 | 861.8 |
| 298.15 | 1.0000 | 882.5 |
| 291.15 | 0.0000 | 628.2 |
| 291.15 | 0.0121 | 631.2 |
| 291.15 | 0.0427 | 638.8 |
| 291.15 | 0.0780 | 647.7 |
| 291.15 | 0.1417 | 664.0 |
| 291.15 | 0.2048 | 680.3 |
| 291.15 | 0.2734 | 698.2 |
| 291.15 | 0.3338 | 714.1 |
| 291.15 | 0.3934 | 729.8 |
| 291.15 | 0.4636 | 748.4 |
| 291.15 | 0.5224 | 763.9 |
| 291.15 | 0.5876 | 781.1 |
| 291.15 | 0.6565 | 799.3 |
| 291.15 | 0.7136 | 814.4 |
| 291.15 | 0.7697 | 829.2 |
| 291.15 | 0.8277 | 844.6 |
| 291.15 | 0.8911 | 861.3 |
| 291.15 | 0.9230 | 869.7 |
| 291.15 | 1.0000 | 889.6 |
Operational condition: Pressure, kPa = 101.32 (Liquid)
| Mole fraction of n-Propyl acetate (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 309.24 |
| 0.0146 | 309.88 |
| 0.0276 | 310.21 |
| 0.0579 | 310.83 |
| 0.1101 | 311.59 |
| 0.1455 | 312.60 |
| 0.1744 | 313.21 |
| 0.2135 | 313.91 |
| 0.3165 | 316.48 |
| 0.4148 | 319.77 |
| 0.5263 | 324.20 |
| 0.6412 | 330.46 |
| 0.7303 | 336.62 |
| 0.7819 | 341.02 |
| 0.8189 | 344.98 |
| 0.8530 | 348.96 |
| 0.8810 | 352.67 |
| 0.9150 | 357.79 |
| 0.9401 | 362.12 |
| 0.9615 | 366.04 |
| 0.9734 | 368.43 |
| 0.9817 | 370.32 |
| 0.9902 | 372.10 |
| 0.9951 | 373.21 |
| 1.0000 | 374.34 |
Operational condition: Pressure, kPa = 101.32 (Liquid)
| Mole fraction of n-Propyl acetate (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 309.24 |
| 0.0146 | 309.88 |
| 0.0276 | 310.21 |
| 0.0579 | 310.83 |
| 0.1101 | 311.59 |
| 0.1455 | 312.60 |
| 0.1744 | 313.21 |
| 0.2135 | 313.91 |
| 0.3165 | 316.48 |
| 0.4148 | 319.77 |
| 0.5263 | 324.20 |
| 0.6412 | 330.46 |
| 0.7303 | 336.62 |
| 0.7819 | 341.02 |
| 0.8189 | 344.98 |
| 0.8530 | 348.96 |
| 0.8810 | 352.67 |
| 0.9150 | 357.79 |
| 0.9401 | 362.12 |
| 0.9615 | 366.04 |
| 0.9734 | 368.43 |
| 0.9817 | 370.32 |
| 0.9902 | 372.10 |
| 0.9951 | 373.21 |
| 1.0000 | 374.34 |