Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 2-Propen-1-ol (1) - Liquid | Mole fraction of 2-Propen-1-ol (1) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0040 | 0.0380 |
| 0.0070 | 0.0630 |
| 0.0130 | 0.1070 |
| 0.0260 | 0.1660 |
| 0.0370 | 0.2000 |
| 0.0540 | 0.2570 |
| 0.0770 | 0.2910 |
| 0.1210 | 0.3380 |
| 0.2480 | 0.3850 |
| 0.3910 | 0.4280 |
| 0.5350 | 0.4870 |
| 0.6400 | 0.5490 |
| 0.7240 | 0.6160 |
| 0.7770 | 0.6540 |
| 0.8160 | 0.7040 |
| 0.8350 | 0.7260 |
| 0.8870 | 0.7890 |
| 0.9180 | 0.8370 |
| 0.9580 | 0.9110 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Temperature, K - Gas | Mole fraction of 2-Propen-1-ol (1) - Gas |
|---|---|
| 372.95 | 0.0080 |
| 372.08 | 0.0430 |
| 371.21 | 0.0750 |
| 370.13 | 0.1150 |
| 369.04 | 0.1550 |
| 367.79 | 0.1990 |
| 366.88 | 0.2330 |
| 364.90 | 0.3050 |
| 363.83 | 0.3470 |
| 362.88 | 0.4040 |
| 362.41 | 0.4590 |
| 362.68 | 0.5020 |
| 363.66 | 0.6120 |
| 364.93 | 0.6960 |
| 366.07 | 0.7640 |
| 367.13 | 0.8270 |
| 368.04 | 0.8790 |
| 368.70 | 0.9190 |
| 369.23 | 0.9510 |
| 369.80 | 0.9870 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 2-Propen-1-ol (1) - Liquid | Mole fraction of 2-Propen-1-ol (1) - Gas |
|---|---|
| 1.0000 | 1.0000 |
| 0.9566 | 0.9048 |
| 0.9149 | 0.8059 |
| 0.8029 | 0.6652 |
| 0.7250 | 0.6098 |
| 0.5201 | 0.4829 |
| 0.4540 | 0.4720 |
| 0.3936 | 0.4436 |
| 0.2406 | 0.4113 |
| 0.1560 | 0.3612 |
| 0.0852 | 0.3109 |
| 0.0564 | 0.2557 |
| 0.0392 | 0.2348 |
| 0.0147 | 0.1191 |
| 0.0070 | 0.0564 |
| 0.0000 | 0.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 2-Propen-1-ol (1) - Liquid | Mole fraction of 2-Propen-1-ol (1) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0040 | 0.0380 |
| 0.0070 | 0.0630 |
| 0.0130 | 0.1070 |
| 0.0260 | 0.1660 |
| 0.0370 | 0.2000 |
| 0.0540 | 0.2570 |
| 0.0770 | 0.2910 |
| 0.1210 | 0.3380 |
| 0.2480 | 0.3850 |
| 0.3910 | 0.4280 |
| 0.5350 | 0.4870 |
| 0.6400 | 0.5490 |
| 0.7240 | 0.6160 |
| 0.7770 | 0.6540 |
| 0.8160 | 0.7040 |
| 0.8350 | 0.7260 |
| 0.8870 | 0.7890 |
| 0.9180 | 0.8370 |
| 0.9580 | 0.9110 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Temperature, K - Gas | Mole fraction of 2-Propen-1-ol (1) - Gas |
|---|---|
| 372.95 | 0.0080 |
| 372.08 | 0.0430 |
| 371.21 | 0.0750 |
| 370.13 | 0.1150 |
| 369.04 | 0.1550 |
| 367.79 | 0.1990 |
| 366.88 | 0.2330 |
| 364.90 | 0.3050 |
| 363.83 | 0.3470 |
| 362.88 | 0.4040 |
| 362.41 | 0.4590 |
| 362.68 | 0.5020 |
| 363.66 | 0.6120 |
| 364.93 | 0.6960 |
| 366.07 | 0.7640 |
| 367.13 | 0.8270 |
| 368.04 | 0.8790 |
| 368.70 | 0.9190 |
| 369.23 | 0.9510 |
| 369.80 | 0.9870 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 2-Propen-1-ol (1) - Liquid | Mole fraction of 2-Propen-1-ol (1) - Gas |
|---|---|
| 1.0000 | 1.0000 |
| 0.9566 | 0.9048 |
| 0.9149 | 0.8059 |
| 0.8029 | 0.6652 |
| 0.7250 | 0.6098 |
| 0.5201 | 0.4829 |
| 0.4540 | 0.4720 |
| 0.3936 | 0.4436 |
| 0.2406 | 0.4113 |
| 0.1560 | 0.3612 |
| 0.0852 | 0.3109 |
| 0.0564 | 0.2557 |
| 0.0392 | 0.2348 |
| 0.0147 | 0.1191 |
| 0.0070 | 0.0564 |
| 0.0000 | 0.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 2-Propen-1-ol (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 373.40 |
| 0.0040 | 372.15 |
| 0.0070 | 371.52 |
| 0.0130 | 370.40 |
| 0.0260 | 368.73 |
| 0.0370 | 367.62 |
| 0.0540 | 366.24 |
| 0.0770 | 365.24 |
| 0.1210 | 364.00 |
| 0.2480 | 363.02 |
| 0.3910 | 362.70 |
| 0.5350 | 362.66 |
| 0.6400 | 363.18 |
| 0.7240 | 363.92 |
| 0.7770 | 364.60 |
| 0.8160 | 365.22 |
| 0.8350 | 365.55 |
| 0.8870 | 366.61 |
| 0.9180 | 367.33 |
| 0.9580 | 368.55 |
| 1.0000 | 369.90 |
Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of 2-Propen-1-ol (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0010 | 372.95 |
| 0.0040 | 372.08 |
| 0.0080 | 371.21 |
| 0.0130 | 370.13 |
| 0.0200 | 369.04 |
| 0.0320 | 367.79 |
| 0.0430 | 366.88 |
| 0.0850 | 364.90 |
| 0.1290 | 363.83 |
| 0.2720 | 362.88 |
| 0.4010 | 362.41 |
| 0.5350 | 362.68 |
| 0.7360 | 363.66 |
| 0.8210 | 364.93 |
| 0.8750 | 366.07 |
| 0.9130 | 367.13 |
| 0.9440 | 368.04 |
| 0.9630 | 368.70 |
| 0.9780 | 369.23 |
| 0.9950 | 369.80 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 2-Propen-1-ol (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 1.0000 | 369.75 |
| 0.9566 | 368.24 |
| 0.9149 | 366.44 |
| 0.8029 | 364.31 |
| 0.7250 | 362.97 |
| 0.5201 | 361.85 |
| 0.4540 | 361.84 |
| 0.3936 | 361.95 |
| 0.2406 | 362.35 |
| 0.1560 | 363.30 |
| 0.0852 | 364.43 |
| 0.0564 | 365.60 |
| 0.0392 | 367.25 |
| 0.0147 | 369.95 |
| 0.0070 | 371.64 |
| 0.0000 | 373.15 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 2-Propen-1-ol (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 373.40 |
| 0.0040 | 372.15 |
| 0.0070 | 371.52 |
| 0.0130 | 370.40 |
| 0.0260 | 368.73 |
| 0.0370 | 367.62 |
| 0.0540 | 366.24 |
| 0.0770 | 365.24 |
| 0.1210 | 364.00 |
| 0.2480 | 363.02 |
| 0.3910 | 362.70 |
| 0.5350 | 362.66 |
| 0.6400 | 363.18 |
| 0.7240 | 363.92 |
| 0.7770 | 364.60 |
| 0.8160 | 365.22 |
| 0.8350 | 365.55 |
| 0.8870 | 366.61 |
| 0.9180 | 367.33 |
| 0.9580 | 368.55 |
| 1.0000 | 369.90 |
Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of 2-Propen-1-ol (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0010 | 372.95 |
| 0.0040 | 372.08 |
| 0.0080 | 371.21 |
| 0.0130 | 370.13 |
| 0.0200 | 369.04 |
| 0.0320 | 367.79 |
| 0.0430 | 366.88 |
| 0.0850 | 364.90 |
| 0.1290 | 363.83 |
| 0.2720 | 362.88 |
| 0.4010 | 362.41 |
| 0.5350 | 362.68 |
| 0.7360 | 363.66 |
| 0.8210 | 364.93 |
| 0.8750 | 366.07 |
| 0.9130 | 367.13 |
| 0.9440 | 368.04 |
| 0.9630 | 368.70 |
| 0.9780 | 369.23 |
| 0.9950 | 369.80 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 2-Propen-1-ol (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 1.0000 | 369.75 |
| 0.9566 | 368.24 |
| 0.9149 | 366.44 |
| 0.8029 | 364.31 |
| 0.7250 | 362.97 |
| 0.5201 | 361.85 |
| 0.4540 | 361.84 |
| 0.3936 | 361.95 |
| 0.2406 | 362.35 |
| 0.1560 | 363.30 |
| 0.0852 | 364.43 |
| 0.0564 | 365.60 |
| 0.0392 | 367.25 |
| 0.0147 | 369.95 |
| 0.0070 | 371.64 |
| 0.0000 | 373.15 |