Operational condition: Pressure, kPa = 101.32 (Gas)
| Mole fraction of Formic acid, butyl ester (1) - Liquid | Mole fraction of Formic acid, butyl ester (1) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0300 | 0.1300 |
| 0.0520 | 0.2080 |
| 0.0730 | 0.2730 |
| 0.0960 | 0.3380 |
| 0.1230 | 0.4040 |
| 0.1440 | 0.4500 |
| 0.1670 | 0.4910 |
| 0.1910 | 0.5270 |
| 0.2220 | 0.5730 |
| 0.2570 | 0.6120 |
| 0.2940 | 0.6490 |
| 0.3140 | 0.6640 |
| 0.3430 | 0.6870 |
| 0.3850 | 0.7200 |
| 0.4370 | 0.7520 |
| 0.4830 | 0.7830 |
| 0.5030 | 0.7920 |
| 0.5380 | 0.8120 |
| 0.5700 | 0.8230 |
| 0.6280 | 0.8500 |
| 0.6700 | 0.8660 |
| 0.7230 | 0.8860 |
| 0.7580 | 0.9000 |
| 0.8120 | 0.9190 |
| 0.8590 | 0.9360 |
| 0.8950 | 0.9490 |
| 0.9310 | 0.9640 |
| 0.9560 | 0.9740 |
| 0.9750 | 0.9830 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.32 (Gas)
| Mole fraction of Formic acid, butyl ester (1) - Liquid | Mole fraction of Formic acid, butyl ester (1) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0300 | 0.1300 |
| 0.0520 | 0.2080 |
| 0.0730 | 0.2730 |
| 0.0960 | 0.3380 |
| 0.1230 | 0.4040 |
| 0.1440 | 0.4500 |
| 0.1670 | 0.4910 |
| 0.1910 | 0.5270 |
| 0.2220 | 0.5730 |
| 0.2570 | 0.6120 |
| 0.2940 | 0.6490 |
| 0.3140 | 0.6640 |
| 0.3430 | 0.6870 |
| 0.3850 | 0.7200 |
| 0.4370 | 0.7520 |
| 0.4830 | 0.7830 |
| 0.5030 | 0.7920 |
| 0.5380 | 0.8120 |
| 0.5700 | 0.8230 |
| 0.6280 | 0.8500 |
| 0.6700 | 0.8660 |
| 0.7230 | 0.8860 |
| 0.7580 | 0.9000 |
| 0.8120 | 0.9190 |
| 0.8590 | 0.9360 |
| 0.8950 | 0.9490 |
| 0.9310 | 0.9640 |
| 0.9560 | 0.9740 |
| 0.9750 | 0.9830 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Formic acid, butyl ester (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 291.15 | 0.1030 | 0.4960 |
| 291.15 | 0.1970 | 0.7970 |
| 291.15 | 0.2800 | 1.02 |
| 291.15 | 0.3510 | 1.148 |
| 291.15 | 0.4200 | 1.229 |
| 291.15 | 0.4760 | 1.257 |
| 291.15 | 0.5250 | 1.258 |
| 291.15 | 0.5840 | 1.215 |
| 291.15 | 0.6320 | 1.154 |
| 291.15 | 0.6840 | 1.063 |
| 291.15 | 0.7370 | 0.9460 |
| 291.15 | 0.7940 | 0.7960 |
| 291.15 | 0.8490 | 0.6160 |
| 291.15 | 0.9040 | 0.4150 |
| 291.15 | 0.9540 | 0.2220 |
| 318.15 | 0.0820 | 0.4520 |
| 318.15 | 0.1690 | 0.8010 |
| 318.15 | 0.2530 | 1.067 |
| 318.15 | 0.3380 | 1.25 |
| 318.15 | 0.4120 | 1.345 |
| 318.15 | 0.4770 | 1.381 |
| 318.15 | 0.5330 | 1.372 |
| 318.15 | 0.5770 | 1.331 |
| 318.15 | 0.6160 | 1.287 |
| 318.15 | 0.6410 | 1.24 |
| 318.15 | 0.6860 | 1.159 |
| 318.15 | 0.7340 | 1.049 |
| 318.15 | 0.7820 | 0.9140 |
| 318.15 | 0.8300 | 0.7610 |
| 318.15 | 0.8780 | 0.5830 |
| 318.15 | 0.9250 | 0.3850 |
| 318.15 | 0.9680 | 0.1870 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Formic acid, butyl ester (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 291.15 | 0.1030 | 0.4960 |
| 291.15 | 0.1970 | 0.7970 |
| 291.15 | 0.2800 | 1.02 |
| 291.15 | 0.3510 | 1.148 |
| 291.15 | 0.4200 | 1.229 |
| 291.15 | 0.4760 | 1.257 |
| 291.15 | 0.5250 | 1.258 |
| 291.15 | 0.5840 | 1.215 |
| 291.15 | 0.6320 | 1.154 |
| 291.15 | 0.6840 | 1.063 |
| 291.15 | 0.7370 | 0.9460 |
| 291.15 | 0.7940 | 0.7960 |
| 291.15 | 0.8490 | 0.6160 |
| 291.15 | 0.9040 | 0.4150 |
| 291.15 | 0.9540 | 0.2220 |
| 318.15 | 0.0820 | 0.4520 |
| 318.15 | 0.1690 | 0.8010 |
| 318.15 | 0.2530 | 1.067 |
| 318.15 | 0.3380 | 1.25 |
| 318.15 | 0.4120 | 1.345 |
| 318.15 | 0.4770 | 1.381 |
| 318.15 | 0.5330 | 1.372 |
| 318.15 | 0.5770 | 1.331 |
| 318.15 | 0.6160 | 1.287 |
| 318.15 | 0.6410 | 1.24 |
| 318.15 | 0.6860 | 1.159 |
| 318.15 | 0.7340 | 1.049 |
| 318.15 | 0.7820 | 0.9140 |
| 318.15 | 0.8300 | 0.7610 |
| 318.15 | 0.8780 | 0.5830 |
| 318.15 | 0.9250 | 0.3850 |
| 318.15 | 0.9680 | 0.1870 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Formic acid, butyl ester (1) - Liquid | Mass density, kg/m3 - Liquid |
| 291.15 | 0.0000 | 719.27 |
| 291.15 | 0.0650 | 725.74 |
| 291.15 | 0.1154 | 731.16 |
| 291.15 | 0.1638 | 736.66 |
| 291.15 | 0.2124 | 742.4 |
| 291.15 | 0.2547 | 747.71 |
| 291.15 | 0.3139 | 755.51 |
| 291.15 | 0.3612 | 762.09 |
| 291.15 | 0.4045 | 768.45 |
| 291.15 | 0.4499 | 775.41 |
| 291.15 | 0.4945 | 782.58 |
| 291.15 | 0.5506 | 792.09 |
| 291.15 | 0.5967 | 800.32 |
| 291.15 | 0.6472 | 809.92 |
| 291.15 | 0.7021 | 820.98 |
| 291.15 | 0.7535 | 831.93 |
| 291.15 | 0.7975 | 841.89 |
| 291.15 | 0.8473 | 853.87 |
| 291.15 | 0.8981 | 866.85 |
| 291.15 | 0.9467 | 880.12 |
| 291.15 | 1.0000 | 895.73 |
| 298.15 | 0.0000 | 713.85 |
| 298.15 | 0.0657 | 720.31 |
| 298.15 | 0.1117 | 725.13 |
| 298.15 | 0.1632 | 730.81 |
| 298.15 | 0.2059 | 735.86 |
| 298.15 | 0.2625 | 742.86 |
| 298.15 | 0.3087 | 748.88 |
| 298.15 | 0.3544 | 755.1 |
| 298.15 | 0.4033 | 762.14 |
| 298.15 | 0.4479 | 768.85 |
| 298.15 | 0.4960 | 776.5 |
| 298.15 | 0.5560 | 786.59 |
| 298.15 | 0.5977 | 794.07 |
| 298.15 | 0.6481 | 803.48 |
| 298.15 | 0.7058 | 814.99 |
| 298.15 | 0.7541 | 825.28 |
| 298.15 | 0.8000 | 835.49 |
| 298.15 | 0.8469 | 846.73 |
| 298.15 | 0.8977 | 859.57 |
| 298.15 | 0.9467 | 872.86 |
| 298.15 | 1.0000 | 888.33 |
| 308.15 | 0.0000 | 705.97 |
| 308.15 | 0.0624 | 711.99 |
| 308.15 | 0.1149 | 717.4 |
| 308.15 | 0.1612 | 722.45 |
| 308.15 | 0.2069 | 727.67 |
| 308.15 | 0.2618 | 734.32 |
| 308.15 | 0.3057 | 739.95 |
| 308.15 | 0.3495 | 745.78 |
| 308.15 | 0.4009 | 753.02 |
| 308.15 | 0.4470 | 759.89 |
| 308.15 | 0.4934 | 767.11 |
| 308.15 | 0.5529 | 776.96 |
| 308.15 | 0.5977 | 784.75 |
| 308.15 | 0.6489 | 794.29 |
| 308.15 | 0.6998 | 804.2 |
| 308.15 | 0.7470 | 814.0 |
| 308.15 | 0.7985 | 825.37 |
| 308.15 | 0.8430 | 835.72 |
| 308.15 | 0.8967 | 849.15 |
| 308.15 | 0.9466 | 862.29 |
| 308.15 | 1.0000 | 877.73 |
| 318.15 | 0.0000 | 698.04 |
| 318.15 | 0.0713 | 704.73 |
| 318.15 | 0.1118 | 708.82 |
| 318.15 | 0.1652 | 714.49 |
| 318.15 | 0.2111 | 719.67 |
| 318.15 | 0.2652 | 726.04 |
| 318.15 | 0.3144 | 732.3 |
| 318.15 | 0.3589 | 738.19 |
| 318.15 | 0.4051 | 744.57 |
| 318.15 | 0.4601 | 752.65 |
| 318.15 | 0.4980 | 758.5 |
| 318.15 | 0.5578 | 768.27 |
| 318.15 | 0.5983 | 775.23 |
| 318.15 | 0.6527 | 785.12 |
| 318.15 | 0.7059 | 795.44 |
| 318.15 | 0.7565 | 805.93 |
| 318.15 | 0.7970 | 814.72 |
| 318.15 | 0.8495 | 826.77 |
| 318.15 | 0.9005 | 839.43 |
| 318.15 | 0.9466 | 851.6 |
| 318.15 | 1.0000 | 866.77 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Formic acid, butyl ester (1) - Liquid | Mass density, kg/m3 - Liquid |
| 291.15 | 0.0000 | 719.27 |
| 291.15 | 0.0650 | 725.74 |
| 291.15 | 0.1154 | 731.16 |
| 291.15 | 0.1638 | 736.66 |
| 291.15 | 0.2124 | 742.4 |
| 291.15 | 0.2547 | 747.71 |
| 291.15 | 0.3139 | 755.51 |
| 291.15 | 0.3612 | 762.09 |
| 291.15 | 0.4045 | 768.45 |
| 291.15 | 0.4499 | 775.41 |
| 291.15 | 0.4945 | 782.58 |
| 291.15 | 0.5506 | 792.09 |
| 291.15 | 0.5967 | 800.32 |
| 291.15 | 0.6472 | 809.92 |
| 291.15 | 0.7021 | 820.98 |
| 291.15 | 0.7535 | 831.93 |
| 291.15 | 0.7975 | 841.89 |
| 291.15 | 0.8473 | 853.87 |
| 291.15 | 0.8981 | 866.85 |
| 291.15 | 0.9467 | 880.12 |
| 291.15 | 1.0000 | 895.73 |
| 298.15 | 0.0000 | 713.85 |
| 298.15 | 0.0657 | 720.31 |
| 298.15 | 0.1117 | 725.13 |
| 298.15 | 0.1632 | 730.81 |
| 298.15 | 0.2059 | 735.86 |
| 298.15 | 0.2625 | 742.86 |
| 298.15 | 0.3087 | 748.88 |
| 298.15 | 0.3544 | 755.1 |
| 298.15 | 0.4033 | 762.14 |
| 298.15 | 0.4479 | 768.85 |
| 298.15 | 0.4960 | 776.5 |
| 298.15 | 0.5560 | 786.59 |
| 298.15 | 0.5977 | 794.07 |
| 298.15 | 0.6481 | 803.48 |
| 298.15 | 0.7058 | 814.99 |
| 298.15 | 0.7541 | 825.28 |
| 298.15 | 0.8000 | 835.49 |
| 298.15 | 0.8469 | 846.73 |
| 298.15 | 0.8977 | 859.57 |
| 298.15 | 0.9467 | 872.86 |
| 298.15 | 1.0000 | 888.33 |
| 308.15 | 0.0000 | 705.97 |
| 308.15 | 0.0624 | 711.99 |
| 308.15 | 0.1149 | 717.4 |
| 308.15 | 0.1612 | 722.45 |
| 308.15 | 0.2069 | 727.67 |
| 308.15 | 0.2618 | 734.32 |
| 308.15 | 0.3057 | 739.95 |
| 308.15 | 0.3495 | 745.78 |
| 308.15 | 0.4009 | 753.02 |
| 308.15 | 0.4470 | 759.89 |
| 308.15 | 0.4934 | 767.11 |
| 308.15 | 0.5529 | 776.96 |
| 308.15 | 0.5977 | 784.75 |
| 308.15 | 0.6489 | 794.29 |
| 308.15 | 0.6998 | 804.2 |
| 308.15 | 0.7470 | 814.0 |
| 308.15 | 0.7985 | 825.37 |
| 308.15 | 0.8430 | 835.72 |
| 308.15 | 0.8967 | 849.15 |
| 308.15 | 0.9466 | 862.29 |
| 308.15 | 1.0000 | 877.73 |
| 318.15 | 0.0000 | 698.04 |
| 318.15 | 0.0713 | 704.73 |
| 318.15 | 0.1118 | 708.82 |
| 318.15 | 0.1652 | 714.49 |
| 318.15 | 0.2111 | 719.67 |
| 318.15 | 0.2652 | 726.04 |
| 318.15 | 0.3144 | 732.3 |
| 318.15 | 0.3589 | 738.19 |
| 318.15 | 0.4051 | 744.57 |
| 318.15 | 0.4601 | 752.65 |
| 318.15 | 0.4980 | 758.5 |
| 318.15 | 0.5578 | 768.27 |
| 318.15 | 0.5983 | 775.23 |
| 318.15 | 0.6527 | 785.12 |
| 318.15 | 0.7059 | 795.44 |
| 318.15 | 0.7565 | 805.93 |
| 318.15 | 0.7970 | 814.72 |
| 318.15 | 0.8495 | 826.77 |
| 318.15 | 0.9005 | 839.43 |
| 318.15 | 0.9466 | 851.6 |
| 318.15 | 1.0000 | 866.77 |
Operational condition: Pressure, kPa = 101.32 (Liquid)
| Mole fraction of Formic acid, butyl ester (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 423.94 |
| 0.0300 | 419.32 |
| 0.0520 | 416.55 |
| 0.0730 | 414.14 |
| 0.0960 | 411.50 |
| 0.1230 | 408.81 |
| 0.1440 | 406.79 |
| 0.1670 | 404.87 |
| 0.1910 | 403.24 |
| 0.2220 | 400.98 |
| 0.2570 | 399.16 |
| 0.2940 | 397.13 |
| 0.3140 | 396.19 |
| 0.3430 | 394.85 |
| 0.3850 | 393.10 |
| 0.4370 | 391.35 |
| 0.4830 | 389.70 |
| 0.5030 | 389.24 |
| 0.5380 | 388.15 |
| 0.5700 | 387.60 |
| 0.6280 | 386.59 |
| 0.6700 | 385.69 |
| 0.7230 | 384.67 |
| 0.7580 | 384.01 |
| 0.8120 | 383.10 |
| 0.8590 | 381.87 |
| 0.8950 | 381.06 |
| 0.9310 | 380.42 |
| 0.9560 | 380.06 |
| 0.9750 | 379.74 |
| 1.0000 | 380.13 |
Operational condition: Pressure, kPa = 101.32 (Liquid)
| Mole fraction of Formic acid, butyl ester (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 423.94 |
| 0.0300 | 419.32 |
| 0.0520 | 416.55 |
| 0.0730 | 414.14 |
| 0.0960 | 411.50 |
| 0.1230 | 408.81 |
| 0.1440 | 406.79 |
| 0.1670 | 404.87 |
| 0.1910 | 403.24 |
| 0.2220 | 400.98 |
| 0.2570 | 399.16 |
| 0.2940 | 397.13 |
| 0.3140 | 396.19 |
| 0.3430 | 394.85 |
| 0.3850 | 393.10 |
| 0.4370 | 391.35 |
| 0.4830 | 389.70 |
| 0.5030 | 389.24 |
| 0.5380 | 388.15 |
| 0.5700 | 387.60 |
| 0.6280 | 386.59 |
| 0.6700 | 385.69 |
| 0.7230 | 384.67 |
| 0.7580 | 384.01 |
| 0.8120 | 383.10 |
| 0.8590 | 381.87 |
| 0.8950 | 381.06 |
| 0.9310 | 380.42 |
| 0.9560 | 380.06 |
| 0.9750 | 379.74 |
| 1.0000 | 380.13 |