Datasets
-
Azeotropic composition: mole fraction (4)
-
ρl - Mass density, kg/m3 (2)
-
γ - Surface tension liquid-gas, N/m (2)
-
Tboil - Boiling temperature at pressure P, K (2)
-
Azeotropic temperature, K (2)
Azeotropic composition: mole fraction of Propane, 2-ethoxy-2-methyl- (2)
[ref]
Pressure, kPa - Liquid |
Azeotropic composition: mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid |
75.00 |
0.9720 |
94.00 |
0.9550 |
Mole fraction of Propane, 2-ethoxy-2-methyl- (2)
[ref]
Fixed |
Measured |
Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid |
Pressure, kPa - Gas |
Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Gas |
0.0000 |
50.00 |
0.0000 |
0.0000 |
75.00 |
0.0000 |
0.0000 |
94.00 |
0.0000 |
0.0540 |
50.00 |
0.2670 |
0.0550 |
75.00 |
0.2440 |
0.0560 |
94.00 |
0.2290 |
0.1000 |
50.00 |
0.4080 |
0.1030 |
75.00 |
0.3810 |
0.1030 |
94.00 |
0.3590 |
0.1430 |
50.00 |
0.5050 |
0.1450 |
75.00 |
0.4650 |
0.1450 |
94.00 |
0.4430 |
0.1900 |
94.00 |
0.5120 |
0.1910 |
50.00 |
0.5790 |
0.1910 |
75.00 |
0.5380 |
0.2360 |
50.00 |
0.6350 |
0.2370 |
94.00 |
0.5670 |
0.2380 |
75.00 |
0.5940 |
0.2820 |
75.00 |
0.6380 |
0.2820 |
94.00 |
0.6090 |
0.2840 |
50.00 |
0.6780 |
0.3330 |
75.00 |
0.6740 |
0.3330 |
94.00 |
0.6520 |
0.3340 |
50.00 |
0.7130 |
0.3710 |
50.00 |
0.7330 |
0.3720 |
75.00 |
0.7000 |
0.3750 |
94.00 |
0.6780 |
0.4270 |
94.00 |
0.7060 |
0.4280 |
50.00 |
0.7600 |
0.4290 |
75.00 |
0.7290 |
0.4810 |
94.00 |
0.7330 |
0.4820 |
50.00 |
0.7840 |
0.4840 |
75.00 |
0.7540 |
0.5350 |
50.00 |
0.8020 |
0.5360 |
75.00 |
0.7730 |
0.5370 |
94.00 |
0.7560 |
0.5840 |
50.00 |
0.8190 |
0.5840 |
94.00 |
0.7750 |
0.5860 |
75.00 |
0.7920 |
0.6350 |
50.00 |
0.8360 |
0.6370 |
75.00 |
0.8110 |
0.6370 |
94.00 |
0.7960 |
0.6830 |
50.00 |
0.8520 |
0.6850 |
75.00 |
0.8270 |
0.6850 |
94.00 |
0.8140 |
0.7320 |
50.00 |
0.8650 |
0.7320 |
75.00 |
0.8460 |
0.7330 |
94.00 |
0.8330 |
0.7710 |
50.00 |
0.8810 |
0.7730 |
75.00 |
0.8620 |
0.7730 |
94.00 |
0.8500 |
0.8310 |
50.00 |
0.9030 |
0.8310 |
75.00 |
0.8880 |
0.8320 |
94.00 |
0.8780 |
0.9090 |
50.00 |
0.9350 |
0.9100 |
75.00 |
0.9270 |
0.9100 |
94.00 |
0.9220 |
0.9610 |
50.00 |
0.9680 |
0.9610 |
75.00 |
0.9640 |
0.9610 |
94.00 |
0.9620 |
1.0000 |
50.00 |
1.0000 |
1.0000 |
75.00 |
1.0000 |
1.0000 |
94.00 |
1.0000 |
Azeotropic composition: mole fraction of Propane, 2-ethoxy-2-methyl- (2)
[ref]
Pressure, kPa - Liquid |
Azeotropic composition: mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid |
75.00 |
0.9720 |
94.00 |
0.9550 |
Mole fraction of Propane, 2-ethoxy-2-methyl- (2)
[ref]
Fixed |
Measured |
Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid |
Pressure, kPa - Gas |
Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Gas |
0.0000 |
50.00 |
0.0000 |
0.0000 |
75.00 |
0.0000 |
0.0000 |
94.00 |
0.0000 |
0.0540 |
50.00 |
0.2670 |
0.0550 |
75.00 |
0.2440 |
0.0560 |
94.00 |
0.2290 |
0.1000 |
50.00 |
0.4080 |
0.1030 |
75.00 |
0.3810 |
0.1030 |
94.00 |
0.3590 |
0.1430 |
50.00 |
0.5050 |
0.1450 |
75.00 |
0.4650 |
0.1450 |
94.00 |
0.4430 |
0.1900 |
94.00 |
0.5120 |
0.1910 |
50.00 |
0.5790 |
0.1910 |
75.00 |
0.5380 |
0.2360 |
50.00 |
0.6350 |
0.2370 |
94.00 |
0.5670 |
0.2380 |
75.00 |
0.5940 |
0.2820 |
75.00 |
0.6380 |
0.2820 |
94.00 |
0.6090 |
0.2840 |
50.00 |
0.6780 |
0.3330 |
75.00 |
0.6740 |
0.3330 |
94.00 |
0.6520 |
0.3340 |
50.00 |
0.7130 |
0.3710 |
50.00 |
0.7330 |
0.3720 |
75.00 |
0.7000 |
0.3750 |
94.00 |
0.6780 |
0.4270 |
94.00 |
0.7060 |
0.4280 |
50.00 |
0.7600 |
0.4290 |
75.00 |
0.7290 |
0.4810 |
94.00 |
0.7330 |
0.4820 |
50.00 |
0.7840 |
0.4840 |
75.00 |
0.7540 |
0.5350 |
50.00 |
0.8020 |
0.5360 |
75.00 |
0.7730 |
0.5370 |
94.00 |
0.7560 |
0.5840 |
50.00 |
0.8190 |
0.5840 |
94.00 |
0.7750 |
0.5860 |
75.00 |
0.7920 |
0.6350 |
50.00 |
0.8360 |
0.6370 |
75.00 |
0.8110 |
0.6370 |
94.00 |
0.7960 |
0.6830 |
50.00 |
0.8520 |
0.6850 |
75.00 |
0.8270 |
0.6850 |
94.00 |
0.8140 |
0.7320 |
50.00 |
0.8650 |
0.7320 |
75.00 |
0.8460 |
0.7330 |
94.00 |
0.8330 |
0.7710 |
50.00 |
0.8810 |
0.7730 |
75.00 |
0.8620 |
0.7730 |
94.00 |
0.8500 |
0.8310 |
50.00 |
0.9030 |
0.8310 |
75.00 |
0.8880 |
0.8320 |
94.00 |
0.8780 |
0.9090 |
50.00 |
0.9350 |
0.9100 |
75.00 |
0.9270 |
0.9100 |
94.00 |
0.9220 |
0.9610 |
50.00 |
0.9680 |
0.9610 |
75.00 |
0.9640 |
0.9610 |
94.00 |
0.9620 |
1.0000 |
50.00 |
1.0000 |
1.0000 |
75.00 |
1.0000 |
1.0000 |
94.00 |
1.0000 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 101.3 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0572 |
795.04 |
0.1043 |
791.43 |
0.1752 |
786.11 |
0.2085 |
783.67 |
0.2700 |
779.29 |
0.3317 |
775.03 |
0.3732 |
772.24 |
0.4205 |
769.2 |
0.4756 |
765.72 |
0.5326 |
762.15 |
0.5639 |
760.27 |
0.6210 |
756.93 |
0.6820 |
753.59 |
0.7188 |
751.55 |
0.7551 |
749.37 |
0.8334 |
745.06 |
0.8737 |
742.66 |
0.9142 |
740.45 |
0.9567 |
737.98 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 101.3 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0572 |
795.04 |
0.1043 |
791.43 |
0.1752 |
786.11 |
0.2085 |
783.67 |
0.2700 |
779.29 |
0.3317 |
775.03 |
0.3732 |
772.24 |
0.4205 |
769.2 |
0.4756 |
765.72 |
0.5326 |
762.15 |
0.5639 |
760.27 |
0.6210 |
756.93 |
0.6820 |
753.59 |
0.7188 |
751.55 |
0.7551 |
749.37 |
0.8334 |
745.06 |
0.8737 |
742.66 |
0.9142 |
740.45 |
0.9567 |
737.98 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Temperature, K =
298.15 (Liquid)
Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
0.0670 |
0.0236 |
0.1710 |
0.0228 |
0.3150 |
0.0221 |
0.4120 |
0.0215 |
0.5790 |
0.0208 |
0.7630 |
0.0203 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Temperature, K =
298.15 (Liquid)
Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
0.0670 |
0.0236 |
0.1710 |
0.0228 |
0.3150 |
0.0221 |
0.4120 |
0.0215 |
0.5790 |
0.0208 |
0.7630 |
0.0203 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
50.00 |
352.76 |
0.0000 |
75.00 |
362.57 |
0.0000 |
94.00 |
368.34 |
0.0540 |
50.00 |
347.18 |
0.0550 |
75.00 |
357.21 |
0.0560 |
94.00 |
363.28 |
0.1000 |
50.00 |
343.40 |
0.1030 |
75.00 |
353.75 |
0.1030 |
94.00 |
359.97 |
0.1430 |
50.00 |
340.59 |
0.1450 |
75.00 |
351.23 |
0.1450 |
94.00 |
357.19 |
0.1900 |
94.00 |
355.03 |
0.1910 |
50.00 |
338.14 |
0.1910 |
75.00 |
348.81 |
0.2360 |
50.00 |
336.15 |
0.2370 |
94.00 |
353.28 |
0.2380 |
75.00 |
346.84 |
0.2820 |
75.00 |
345.36 |
0.2820 |
94.00 |
351.88 |
0.2840 |
50.00 |
334.53 |
0.3330 |
75.00 |
344.03 |
0.3330 |
94.00 |
350.46 |
0.3340 |
50.00 |
333.04 |
0.3710 |
50.00 |
332.12 |
0.3720 |
75.00 |
343.07 |
0.3750 |
94.00 |
349.43 |
0.4270 |
94.00 |
348.42 |
0.4280 |
50.00 |
330.94 |
0.4290 |
75.00 |
341.73 |
0.4810 |
94.00 |
347.44 |
0.4820 |
50.00 |
329.91 |
0.4840 |
75.00 |
340.92 |
0.5350 |
50.00 |
329.19 |
0.5360 |
75.00 |
340.19 |
0.5370 |
94.00 |
346.69 |
0.5840 |
50.00 |
328.48 |
0.5840 |
94.00 |
346.01 |
0.5860 |
75.00 |
339.56 |
0.6350 |
50.00 |
327.78 |
0.6370 |
75.00 |
338.85 |
0.6370 |
94.00 |
345.30 |
0.6830 |
50.00 |
327.26 |
0.6850 |
75.00 |
338.43 |
0.6850 |
94.00 |
344.94 |
0.7320 |
50.00 |
326.84 |
0.7320 |
75.00 |
337.94 |
0.7330 |
94.00 |
344.46 |
0.7710 |
50.00 |
326.34 |
0.7730 |
75.00 |
337.46 |
0.7730 |
94.00 |
344.08 |
0.8310 |
50.00 |
325.70 |
0.8310 |
75.00 |
336.96 |
0.8320 |
94.00 |
343.58 |
0.9090 |
50.00 |
325.36 |
0.9100 |
75.00 |
336.68 |
0.9100 |
94.00 |
343.46 |
0.9610 |
50.00 |
325.07 |
0.9610 |
75.00 |
336.60 |
0.9610 |
94.00 |
343.46 |
1.0000 |
50.00 |
324.94 |
1.0000 |
75.00 |
336.56 |
1.0000 |
94.00 |
343.48 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
50.00 |
352.76 |
0.0000 |
75.00 |
362.57 |
0.0000 |
94.00 |
368.34 |
0.0540 |
50.00 |
347.18 |
0.0550 |
75.00 |
357.21 |
0.0560 |
94.00 |
363.28 |
0.1000 |
50.00 |
343.40 |
0.1030 |
75.00 |
353.75 |
0.1030 |
94.00 |
359.97 |
0.1430 |
50.00 |
340.59 |
0.1450 |
75.00 |
351.23 |
0.1450 |
94.00 |
357.19 |
0.1900 |
94.00 |
355.03 |
0.1910 |
50.00 |
338.14 |
0.1910 |
75.00 |
348.81 |
0.2360 |
50.00 |
336.15 |
0.2370 |
94.00 |
353.28 |
0.2380 |
75.00 |
346.84 |
0.2820 |
75.00 |
345.36 |
0.2820 |
94.00 |
351.88 |
0.2840 |
50.00 |
334.53 |
0.3330 |
75.00 |
344.03 |
0.3330 |
94.00 |
350.46 |
0.3340 |
50.00 |
333.04 |
0.3710 |
50.00 |
332.12 |
0.3720 |
75.00 |
343.07 |
0.3750 |
94.00 |
349.43 |
0.4270 |
94.00 |
348.42 |
0.4280 |
50.00 |
330.94 |
0.4290 |
75.00 |
341.73 |
0.4810 |
94.00 |
347.44 |
0.4820 |
50.00 |
329.91 |
0.4840 |
75.00 |
340.92 |
0.5350 |
50.00 |
329.19 |
0.5360 |
75.00 |
340.19 |
0.5370 |
94.00 |
346.69 |
0.5840 |
50.00 |
328.48 |
0.5840 |
94.00 |
346.01 |
0.5860 |
75.00 |
339.56 |
0.6350 |
50.00 |
327.78 |
0.6370 |
75.00 |
338.85 |
0.6370 |
94.00 |
345.30 |
0.6830 |
50.00 |
327.26 |
0.6850 |
75.00 |
338.43 |
0.6850 |
94.00 |
344.94 |
0.7320 |
50.00 |
326.84 |
0.7320 |
75.00 |
337.94 |
0.7330 |
94.00 |
344.46 |
0.7710 |
50.00 |
326.34 |
0.7730 |
75.00 |
337.46 |
0.7730 |
94.00 |
344.08 |
0.8310 |
50.00 |
325.70 |
0.8310 |
75.00 |
336.96 |
0.8320 |
94.00 |
343.58 |
0.9090 |
50.00 |
325.36 |
0.9100 |
75.00 |
336.68 |
0.9100 |
94.00 |
343.46 |
0.9610 |
50.00 |
325.07 |
0.9610 |
75.00 |
336.60 |
0.9610 |
94.00 |
343.46 |
1.0000 |
50.00 |
324.94 |
1.0000 |
75.00 |
336.56 |
1.0000 |
94.00 |
343.48 |
Azeotropic temperature, K
[ref]
Pressure, kPa - Liquid |
Azeotropic temperature, K - Liquid |
75.00 |
336.51 |
94.00 |
343.36 |
Azeotropic temperature, K
[ref]
Pressure, kPa - Liquid |
Azeotropic temperature, K - Liquid |
75.00 |
336.51 |
94.00 |
343.36 |
Sources