Operational condition: Pressure, kPa = 101.3 (Gas)
Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid | Mole fraction of 1-Propanol, 2-methyl- (1) - Gas |
---|---|
0.0330 | 0.0910 |
0.0770 | 0.1890 |
0.1180 | 0.2700 |
0.1650 | 0.3440 |
0.2180 | 0.4310 |
0.2700 | 0.4960 |
0.2930 | 0.5280 |
0.3270 | 0.5810 |
0.3560 | 0.6050 |
0.3830 | 0.6360 |
0.4050 | 0.6680 |
0.4460 | 0.6960 |
0.4710 | 0.7180 |
0.5030 | 0.7390 |
0.5170 | 0.7500 |
0.5460 | 0.7680 |
0.6580 | 0.8470 |
0.7590 | 0.9070 |
0.8690 | 0.9560 |
0.9170 | 0.9750 |
Operational condition: Pressure, kPa = 101.3 (Gas)
Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid | Mole fraction of 1-Propanol, 2-methyl- (1) - Gas |
---|---|
0.0330 | 0.0910 |
0.0770 | 0.1890 |
0.1180 | 0.2700 |
0.1650 | 0.3440 |
0.2180 | 0.4310 |
0.2700 | 0.4960 |
0.2930 | 0.5280 |
0.3270 | 0.5810 |
0.3560 | 0.6050 |
0.3830 | 0.6360 |
0.4050 | 0.6680 |
0.4460 | 0.6960 |
0.4710 | 0.7180 |
0.5030 | 0.7390 |
0.5170 | 0.7500 |
0.5460 | 0.7680 |
0.6580 | 0.8470 |
0.7590 | 0.9070 |
0.8690 | 0.9560 |
0.9170 | 0.9750 |
Operational conditions:
Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid | Refractive index (Na D-line) - Liquid |
---|---|
0.0500 | 1.4071 |
0.1000 | 1.4065 |
0.1500 | 1.4059 |
0.2000 | 1.4052 |
0.2490 | 1.4046 |
0.2990 | 1.4039 |
0.3500 | 1.4033 |
0.4000 | 1.4026 |
0.4500 | 1.4019 |
0.4990 | 1.4012 |
0.5490 | 1.4005 |
0.6000 | 1.3998 |
0.6500 | 1.3991 |
0.6990 | 1.3983 |
0.7500 | 1.3976 |
0.8000 | 1.3968 |
0.8500 | 1.396 |
0.9000 | 1.3952 |
0.9500 | 1.3945 |
Operational conditions:
Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid | Refractive index (Na D-line) - Liquid |
---|---|
0.0500 | 1.4071 |
0.1000 | 1.4065 |
0.1500 | 1.4059 |
0.2000 | 1.4052 |
0.2490 | 1.4046 |
0.2990 | 1.4039 |
0.3500 | 1.4033 |
0.4000 | 1.4026 |
0.4500 | 1.4019 |
0.4990 | 1.4012 |
0.5490 | 1.4005 |
0.6000 | 1.3998 |
0.6500 | 1.3991 |
0.6990 | 1.3983 |
0.7500 | 1.3976 |
0.8000 | 1.3968 |
0.8500 | 1.396 |
0.9000 | 1.3952 |
0.9500 | 1.3945 |
Operational conditions:
Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0500 | 810.3 |
0.1000 | 809.7 |
0.1500 | 809.09 |
0.2000 | 808.51 |
0.2490 | 807.94 |
0.2990 | 807.34 |
0.3500 | 806.75 |
0.4000 | 806.13 |
0.4500 | 805.53 |
0.4990 | 804.9 |
0.5490 | 804.29 |
0.6000 | 803.64 |
0.6500 | 803.01 |
0.6990 | 802.41 |
0.7500 | 801.73 |
0.8000 | 801.07 |
0.8500 | 800.39 |
0.9000 | 799.67 |
0.9500 | 798.84 |
Operational conditions:
Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0500 | 810.3 |
0.1000 | 809.7 |
0.1500 | 809.09 |
0.2000 | 808.51 |
0.2490 | 807.94 |
0.2990 | 807.34 |
0.3500 | 806.75 |
0.4000 | 806.13 |
0.4500 | 805.53 |
0.4990 | 804.9 |
0.5490 | 804.29 |
0.6000 | 803.64 |
0.6500 | 803.01 |
0.6990 | 802.41 |
0.7500 | 801.73 |
0.8000 | 801.07 |
0.8500 | 800.39 |
0.9000 | 799.67 |
0.9500 | 798.84 |
Operational condition: Pressure, kPa = 101.3 (Gas)
Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0330 | 409.10 |
0.0770 | 407.16 |
0.1180 | 405.35 |
0.1650 | 403.60 |
0.2180 | 401.45 |
0.2700 | 399.87 |
0.2930 | 398.85 |
0.3270 | 397.60 |
0.3560 | 396.64 |
0.3830 | 395.89 |
0.4050 | 394.94 |
0.4460 | 393.87 |
0.4710 | 393.07 |
0.5030 | 392.28 |
0.5170 | 391.92 |
0.5460 | 391.13 |
0.6580 | 388.36 |
0.7590 | 385.66 |
0.8690 | 383.48 |
0.9170 | 382.53 |
Operational condition: Pressure, kPa = 101.3 (Gas)
Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0330 | 409.10 |
0.0770 | 407.16 |
0.1180 | 405.35 |
0.1650 | 403.60 |
0.2180 | 401.45 |
0.2700 | 399.87 |
0.2930 | 398.85 |
0.3270 | 397.60 |
0.3560 | 396.64 |
0.3830 | 395.89 |
0.4050 | 394.94 |
0.4460 | 393.87 |
0.4710 | 393.07 |
0.5030 | 392.28 |
0.5170 | 391.92 |
0.5460 | 391.13 |
0.6580 | 388.36 |
0.7590 | 385.66 |
0.8690 | 383.48 |
0.9170 | 382.53 |