Operational condition: Pressure, kPa = 101.3 (Gas)
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Mole fraction of 1-Propanol, 2-methyl- (2) - Gas |
---|---|
0.0560 | 0.1200 |
0.1030 | 0.2090 |
0.3050 | 0.4900 |
0.3280 | 0.5150 |
0.3570 | 0.5610 |
0.3850 | 0.5980 |
0.4080 | 0.6220 |
0.4470 | 0.6570 |
0.4820 | 0.6820 |
0.5160 | 0.7000 |
0.5400 | 0.7270 |
0.5740 | 0.7530 |
0.5940 | 0.7650 |
0.6330 | 0.7890 |
0.6470 | 0.8080 |
0.6900 | 0.8370 |
0.7460 | 0.8730 |
0.7870 | 0.9000 |
0.8390 | 0.9250 |
0.8850 | 0.9520 |
0.9140 | 0.9630 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Mole fraction of 1-Propanol, 2-methyl- (2) - Gas |
---|---|
1.0000 | 1.0000 |
0.8847 | 0.9378 |
0.7892 | 0.8952 |
0.7146 | 0.8477 |
0.5666 | 0.7488 |
0.5080 | 0.7113 |
0.4355 | 0.6408 |
0.3892 | 0.5964 |
0.2163 | 0.4107 |
0.1822 | 0.3527 |
0.1404 | 0.2861 |
0.1034 | 0.2235 |
0.0295 | 0.0692 |
0.0000 | 0.0000 |
Operational condition: Pressure, kPa = 101.3 (Gas)
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Mole fraction of 1-Propanol, 2-methyl- (2) - Gas |
---|---|
0.0560 | 0.1200 |
0.1030 | 0.2090 |
0.3050 | 0.4900 |
0.3280 | 0.5150 |
0.3570 | 0.5610 |
0.3850 | 0.5980 |
0.4080 | 0.6220 |
0.4470 | 0.6570 |
0.4820 | 0.6820 |
0.5160 | 0.7000 |
0.5400 | 0.7270 |
0.5740 | 0.7530 |
0.5940 | 0.7650 |
0.6330 | 0.7890 |
0.6470 | 0.8080 |
0.6900 | 0.8370 |
0.7460 | 0.8730 |
0.7870 | 0.9000 |
0.8390 | 0.9250 |
0.8850 | 0.9520 |
0.9140 | 0.9630 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Mole fraction of 1-Propanol, 2-methyl- (2) - Gas |
---|---|
1.0000 | 1.0000 |
0.8847 | 0.9378 |
0.7892 | 0.8952 |
0.7146 | 0.8477 |
0.5666 | 0.7488 |
0.5080 | 0.7113 |
0.4355 | 0.6408 |
0.3892 | 0.5964 |
0.2163 | 0.4107 |
0.1822 | 0.3527 |
0.1404 | 0.2861 |
0.1034 | 0.2235 |
0.0295 | 0.0692 |
0.0000 | 0.0000 |
Operational conditions:
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Refractive index (Na D-line) - Liquid |
---|---|
0.0510 | 1.4047 |
0.0990 | 1.4042 |
0.1500 | 1.4037 |
0.1990 | 1.4032 |
0.2540 | 1.4026 |
0.3000 | 1.4021 |
0.3500 | 1.4016 |
0.4000 | 1.4011 |
0.4450 | 1.4006 |
0.5000 | 1.4 |
0.5490 | 1.3994 |
0.6000 | 1.3988 |
0.6500 | 1.3982 |
0.7000 | 1.3976 |
0.7510 | 1.397 |
0.7990 | 1.3964 |
0.8490 | 1.3957 |
0.8990 | 1.395 |
0.9500 | 1.3943 |
Operational conditions:
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Refractive index (Na D-line) - Liquid |
---|---|
0.0510 | 1.4047 |
0.0990 | 1.4042 |
0.1500 | 1.4037 |
0.1990 | 1.4032 |
0.2540 | 1.4026 |
0.3000 | 1.4021 |
0.3500 | 1.4016 |
0.4000 | 1.4011 |
0.4450 | 1.4006 |
0.5000 | 1.4 |
0.5490 | 1.3994 |
0.6000 | 1.3988 |
0.6500 | 1.3982 |
0.7000 | 1.3976 |
0.7510 | 1.397 |
0.7990 | 1.3964 |
0.8490 | 1.3957 |
0.8990 | 1.395 |
0.9500 | 1.3943 |
Operational conditions:
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0510 | 805.95 |
0.0990 | 805.61 |
0.1500 | 805.25 |
0.1990 | 804.88 |
0.2540 | 804.48 |
0.3000 | 804.15 |
0.3500 | 803.77 |
0.4000 | 803.39 |
0.4450 | 803.05 |
0.5000 | 802.62 |
0.5490 | 802.23 |
0.6000 | 801.83 |
0.6500 | 801.42 |
0.7000 | 800.64 |
0.7510 | 800.19 |
0.7990 | 799.74 |
0.8490 | 799.27 |
0.8990 | 798.8 |
0.9500 | 798.31 |
Operational conditions:
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0510 | 805.95 |
0.0990 | 805.61 |
0.1500 | 805.25 |
0.1990 | 804.88 |
0.2540 | 804.48 |
0.3000 | 804.15 |
0.3500 | 803.77 |
0.4000 | 803.39 |
0.4450 | 803.05 |
0.5000 | 802.62 |
0.5490 | 802.23 |
0.6000 | 801.83 |
0.6500 | 801.42 |
0.7000 | 800.64 |
0.7510 | 800.19 |
0.7990 | 799.74 |
0.8490 | 799.27 |
0.8990 | 798.8 |
0.9500 | 798.31 |
Operational condition: Pressure, kPa = 101.3 (Gas)
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0560 | 402.33 |
0.1030 | 400.73 |
0.3050 | 395.19 |
0.3280 | 394.73 |
0.3570 | 393.77 |
0.3850 | 393.05 |
0.4080 | 392.41 |
0.4470 | 391.51 |
0.4820 | 390.74 |
0.5160 | 390.22 |
0.5400 | 389.51 |
0.5740 | 388.88 |
0.5940 | 388.43 |
0.6330 | 387.87 |
0.6470 | 387.39 |
0.6900 | 386.27 |
0.7460 | 385.18 |
0.7870 | 384.51 |
0.8390 | 383.60 |
0.8850 | 382.80 |
0.9140 | 382.33 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
1.0000 | 380.73 |
0.8847 | 382.81 |
0.7892 | 384.37 |
0.7146 | 385.84 |
0.5666 | 388.66 |
0.5080 | 389.69 |
0.4355 | 391.58 |
0.3892 | 392.60 |
0.2163 | 396.56 |
0.1822 | 397.96 |
0.1404 | 399.22 |
0.1034 | 400.20 |
0.0295 | 403.17 |
0.0000 | 404.71 |
Operational condition: Pressure, kPa = 101.3 (Gas)
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0560 | 402.33 |
0.1030 | 400.73 |
0.3050 | 395.19 |
0.3280 | 394.73 |
0.3570 | 393.77 |
0.3850 | 393.05 |
0.4080 | 392.41 |
0.4470 | 391.51 |
0.4820 | 390.74 |
0.5160 | 390.22 |
0.5400 | 389.51 |
0.5740 | 388.88 |
0.5940 | 388.43 |
0.6330 | 387.87 |
0.6470 | 387.39 |
0.6900 | 386.27 |
0.7460 | 385.18 |
0.7870 | 384.51 |
0.8390 | 383.60 |
0.8850 | 382.80 |
0.9140 | 382.33 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
1.0000 | 380.73 |
0.8847 | 382.81 |
0.7892 | 384.37 |
0.7146 | 385.84 |
0.5666 | 388.66 |
0.5080 | 389.69 |
0.4355 | 391.58 |
0.3892 | 392.60 |
0.2163 | 396.56 |
0.1822 | 397.96 |
0.1404 | 399.22 |
0.1034 | 400.20 |
0.0295 | 403.17 |
0.0000 | 404.71 |