Mixture of Ethanol, 2-ethoxy- + Methyl Alcohol
Datasets
-
Mole fraction (2)
-
Vapor or sublimation pressure, kPa (2)
Mole fraction of Methyl Alcohol (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Methyl Alcohol (2) - Liquid |
Mole fraction of Methyl Alcohol (2) - Gas |
| 327.36 |
1.0000 |
1.0000 |
| 328.12 |
0.9700 |
0.9980 |
| 329.19 |
0.9260 |
0.9950 |
| 330.96 |
0.8610 |
0.9900 |
| 333.10 |
0.7860 |
0.9830 |
| 335.56 |
1.0000 |
1.0000 |
| 335.89 |
0.7000 |
0.9730 |
| 336.00 |
0.9890 |
0.9990 |
| 336.36 |
0.9750 |
0.9980 |
| 336.59 |
0.6650 |
0.9690 |
| 336.71 |
0.9620 |
0.9970 |
| 337.25 |
0.9350 |
0.9950 |
| 338.21 |
0.8990 |
0.9920 |
| 338.30 |
0.6280 |
0.9640 |
| 339.09 |
0.8680 |
0.9890 |
| 339.47 |
0.8550 |
0.9880 |
| 339.83 |
0.5900 |
0.9570 |
| 340.06 |
0.8340 |
0.9860 |
| 340.77 |
0.5680 |
0.9520 |
| 341.73 |
0.7810 |
0.9800 |
| 343.42 |
0.7260 |
0.9730 |
| 345.01 |
0.4680 |
0.9290 |
| 345.39 |
0.6750 |
0.9650 |
| 346.09 |
0.4480 |
0.9230 |
| 346.33 |
0.6520 |
0.9610 |
| 348.04 |
0.4080 |
0.9120 |
| 348.32 |
0.6040 |
0.9520 |
| 349.39 |
0.5770 |
0.9470 |
| 350.25 |
0.3710 |
0.8950 |
| 350.54 |
0.5500 |
0.9410 |
| 351.43 |
0.3520 |
0.8870 |
| 352.68 |
0.5040 |
0.9280 |
| 353.68 |
0.3160 |
0.8690 |
| 354.29 |
0.4750 |
0.9180 |
| 355.18 |
0.2950 |
0.8530 |
| 356.56 |
0.2750 |
0.8390 |
| 358.15 |
0.2580 |
0.8260 |
| 359.72 |
0.3810 |
0.8810 |
| 361.47 |
0.2180 |
0.7890 |
| 362.54 |
0.2030 |
0.7720 |
| 365.92 |
0.2890 |
0.8210 |
| 366.36 |
0.1700 |
0.7230 |
| 368.30 |
0.2580 |
0.7940 |
| 369.45 |
0.1390 |
0.6780 |
| 369.64 |
0.2440 |
0.7800 |
| 370.78 |
0.2320 |
0.7680 |
| 378.75 |
0.0740 |
0.4990 |
| 383.11 |
0.1230 |
0.5930 |
| 384.35 |
0.0440 |
0.3490 |
| 386.53 |
0.0970 |
0.5200 |
| 389.60 |
0.0200 |
0.1790 |
| 392.78 |
0.0600 |
0.3840 |
| 394.56 |
0.0000 |
0.0000 |
| 395.43 |
0.0450 |
0.3090 |
| 399.52 |
0.0240 |
0.1840 |
| 405.25 |
0.0000 |
0.0000 |
Mole fraction of Methyl Alcohol (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Methyl Alcohol (2) - Liquid |
Mole fraction of Methyl Alcohol (2) - Gas |
| 327.36 |
1.0000 |
1.0000 |
| 328.12 |
0.9700 |
0.9980 |
| 329.19 |
0.9260 |
0.9950 |
| 330.96 |
0.8610 |
0.9900 |
| 333.10 |
0.7860 |
0.9830 |
| 335.56 |
1.0000 |
1.0000 |
| 335.89 |
0.7000 |
0.9730 |
| 336.00 |
0.9890 |
0.9990 |
| 336.36 |
0.9750 |
0.9980 |
| 336.59 |
0.6650 |
0.9690 |
| 336.71 |
0.9620 |
0.9970 |
| 337.25 |
0.9350 |
0.9950 |
| 338.21 |
0.8990 |
0.9920 |
| 338.30 |
0.6280 |
0.9640 |
| 339.09 |
0.8680 |
0.9890 |
| 339.47 |
0.8550 |
0.9880 |
| 339.83 |
0.5900 |
0.9570 |
| 340.06 |
0.8340 |
0.9860 |
| 340.77 |
0.5680 |
0.9520 |
| 341.73 |
0.7810 |
0.9800 |
| 343.42 |
0.7260 |
0.9730 |
| 345.01 |
0.4680 |
0.9290 |
| 345.39 |
0.6750 |
0.9650 |
| 346.09 |
0.4480 |
0.9230 |
| 346.33 |
0.6520 |
0.9610 |
| 348.04 |
0.4080 |
0.9120 |
| 348.32 |
0.6040 |
0.9520 |
| 349.39 |
0.5770 |
0.9470 |
| 350.25 |
0.3710 |
0.8950 |
| 350.54 |
0.5500 |
0.9410 |
| 351.43 |
0.3520 |
0.8870 |
| 352.68 |
0.5040 |
0.9280 |
| 353.68 |
0.3160 |
0.8690 |
| 354.29 |
0.4750 |
0.9180 |
| 355.18 |
0.2950 |
0.8530 |
| 356.56 |
0.2750 |
0.8390 |
| 358.15 |
0.2580 |
0.8260 |
| 359.72 |
0.3810 |
0.8810 |
| 361.47 |
0.2180 |
0.7890 |
| 362.54 |
0.2030 |
0.7720 |
| 365.92 |
0.2890 |
0.8210 |
| 366.36 |
0.1700 |
0.7230 |
| 368.30 |
0.2580 |
0.7940 |
| 369.45 |
0.1390 |
0.6780 |
| 369.64 |
0.2440 |
0.7800 |
| 370.78 |
0.2320 |
0.7680 |
| 378.75 |
0.0740 |
0.4990 |
| 383.11 |
0.1230 |
0.5930 |
| 384.35 |
0.0440 |
0.3490 |
| 386.53 |
0.0970 |
0.5200 |
| 389.60 |
0.0200 |
0.1790 |
| 392.78 |
0.0600 |
0.3840 |
| 394.56 |
0.0000 |
0.0000 |
| 395.43 |
0.0450 |
0.3090 |
| 399.52 |
0.0240 |
0.1840 |
| 405.25 |
0.0000 |
0.0000 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Methyl Alcohol (2) - Liquid |
Vapor or sublimation pressure, kPa - Gas |
| 327.36 |
1.0000 |
66.66 |
| 328.12 |
0.9700 |
66.66 |
| 329.19 |
0.9260 |
66.66 |
| 330.96 |
0.8610 |
66.66 |
| 333.10 |
0.7860 |
66.66 |
| 335.56 |
1.0000 |
93.32 |
| 335.89 |
0.7000 |
66.66 |
| 336.00 |
0.9890 |
93.32 |
| 336.36 |
0.9750 |
93.32 |
| 336.59 |
0.6650 |
66.66 |
| 336.71 |
0.9620 |
93.32 |
| 337.25 |
0.9350 |
93.32 |
| 338.21 |
0.8990 |
93.32 |
| 338.30 |
0.6280 |
66.66 |
| 339.09 |
0.8680 |
93.32 |
| 339.47 |
0.8550 |
93.32 |
| 339.83 |
0.5900 |
66.66 |
| 340.06 |
0.8340 |
93.32 |
| 340.77 |
0.5680 |
66.66 |
| 341.73 |
0.7810 |
93.32 |
| 343.42 |
0.7260 |
93.32 |
| 345.01 |
0.4680 |
66.66 |
| 345.39 |
0.6750 |
93.32 |
| 346.09 |
0.4480 |
66.66 |
| 346.33 |
0.6520 |
93.32 |
| 348.04 |
0.4080 |
66.66 |
| 348.32 |
0.6040 |
93.32 |
| 349.39 |
0.5770 |
93.32 |
| 350.25 |
0.3710 |
66.66 |
| 350.54 |
0.5500 |
93.32 |
| 351.43 |
0.3520 |
66.66 |
| 352.68 |
0.5040 |
93.32 |
| 353.68 |
0.3160 |
66.66 |
| 354.29 |
0.4750 |
93.32 |
| 355.18 |
0.2950 |
66.66 |
| 356.56 |
0.2750 |
66.66 |
| 358.15 |
0.2580 |
66.66 |
| 359.72 |
0.3810 |
93.32 |
| 361.47 |
0.2180 |
66.66 |
| 362.54 |
0.2030 |
66.66 |
| 365.92 |
0.2890 |
93.32 |
| 366.36 |
0.1700 |
66.66 |
| 368.30 |
0.2580 |
93.32 |
| 369.45 |
0.1390 |
66.66 |
| 369.64 |
0.2440 |
93.32 |
| 370.78 |
0.2320 |
93.32 |
| 378.75 |
0.0740 |
66.66 |
| 383.11 |
0.1230 |
93.32 |
| 384.35 |
0.0440 |
66.66 |
| 386.53 |
0.0970 |
93.32 |
| 389.60 |
0.0200 |
66.66 |
| 392.78 |
0.0600 |
93.32 |
| 394.56 |
0.0000 |
66.66 |
| 395.43 |
0.0450 |
93.32 |
| 399.52 |
0.0240 |
93.32 |
| 405.25 |
0.0000 |
93.32 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Methyl Alcohol (2) - Liquid |
Vapor or sublimation pressure, kPa - Gas |
| 327.36 |
1.0000 |
66.66 |
| 328.12 |
0.9700 |
66.66 |
| 329.19 |
0.9260 |
66.66 |
| 330.96 |
0.8610 |
66.66 |
| 333.10 |
0.7860 |
66.66 |
| 335.56 |
1.0000 |
93.32 |
| 335.89 |
0.7000 |
66.66 |
| 336.00 |
0.9890 |
93.32 |
| 336.36 |
0.9750 |
93.32 |
| 336.59 |
0.6650 |
66.66 |
| 336.71 |
0.9620 |
93.32 |
| 337.25 |
0.9350 |
93.32 |
| 338.21 |
0.8990 |
93.32 |
| 338.30 |
0.6280 |
66.66 |
| 339.09 |
0.8680 |
93.32 |
| 339.47 |
0.8550 |
93.32 |
| 339.83 |
0.5900 |
66.66 |
| 340.06 |
0.8340 |
93.32 |
| 340.77 |
0.5680 |
66.66 |
| 341.73 |
0.7810 |
93.32 |
| 343.42 |
0.7260 |
93.32 |
| 345.01 |
0.4680 |
66.66 |
| 345.39 |
0.6750 |
93.32 |
| 346.09 |
0.4480 |
66.66 |
| 346.33 |
0.6520 |
93.32 |
| 348.04 |
0.4080 |
66.66 |
| 348.32 |
0.6040 |
93.32 |
| 349.39 |
0.5770 |
93.32 |
| 350.25 |
0.3710 |
66.66 |
| 350.54 |
0.5500 |
93.32 |
| 351.43 |
0.3520 |
66.66 |
| 352.68 |
0.5040 |
93.32 |
| 353.68 |
0.3160 |
66.66 |
| 354.29 |
0.4750 |
93.32 |
| 355.18 |
0.2950 |
66.66 |
| 356.56 |
0.2750 |
66.66 |
| 358.15 |
0.2580 |
66.66 |
| 359.72 |
0.3810 |
93.32 |
| 361.47 |
0.2180 |
66.66 |
| 362.54 |
0.2030 |
66.66 |
| 365.92 |
0.2890 |
93.32 |
| 366.36 |
0.1700 |
66.66 |
| 368.30 |
0.2580 |
93.32 |
| 369.45 |
0.1390 |
66.66 |
| 369.64 |
0.2440 |
93.32 |
| 370.78 |
0.2320 |
93.32 |
| 378.75 |
0.0740 |
66.66 |
| 383.11 |
0.1230 |
93.32 |
| 384.35 |
0.0440 |
66.66 |
| 386.53 |
0.0970 |
93.32 |
| 389.60 |
0.0200 |
66.66 |
| 392.78 |
0.0600 |
93.32 |
| 394.56 |
0.0000 |
66.66 |
| 395.43 |
0.0450 |
93.32 |
| 399.52 |
0.0240 |
93.32 |
| 405.25 |
0.0000 |
93.32 |
Sources