Datasets
-
Mole fraction
-
Excess molar enthalpy (molar enthalpy
-
Pvap - Vapor or sublimation pressure, kPa
-
ρl - Mass density, kg/m3
Mole fraction of Butane, 2-ethoxy-2-methyl- (1)
[ref]
| Fixed |
Measured |
| Mole fraction of Butane, 2-ethoxy-2-methyl- (1) - Liquid |
Temperature, K - Liquid |
Mole fraction of Butane, 2-ethoxy-2-methyl- (1) - Gas |
| 0.0000 |
358.16 |
0.0000 |
| 0.0640 |
358.00 |
0.1350 |
| 0.0950 |
358.12 |
0.1870 |
| 0.1300 |
358.15 |
0.2350 |
| 0.1670 |
358.11 |
0.2790 |
| 0.2030 |
358.11 |
0.3160 |
| 0.2420 |
358.07 |
0.3510 |
| 0.2830 |
358.06 |
0.3840 |
| 0.3210 |
358.01 |
0.4120 |
| 0.3630 |
358.06 |
0.4400 |
| 0.3980 |
358.02 |
0.4620 |
| 0.4020 |
358.10 |
0.4650 |
| 0.4290 |
358.12 |
0.4810 |
| 0.4500 |
358.13 |
0.4930 |
| 0.4590 |
358.07 |
0.4980 |
| 0.4910 |
358.04 |
0.5160 |
| 0.5020 |
358.11 |
0.5230 |
| 0.5230 |
358.08 |
0.5340 |
| 0.5670 |
358.08 |
0.5590 |
| 0.5850 |
358.10 |
0.5690 |
| 0.6400 |
358.06 |
0.6010 |
| 0.7060 |
358.06 |
0.6430 |
| 0.7530 |
358.07 |
0.6760 |
| 0.7900 |
358.03 |
0.7050 |
| 0.8310 |
358.06 |
0.7430 |
| 0.8640 |
358.03 |
0.7770 |
| 0.9100 |
358.06 |
0.8350 |
| 0.9300 |
358.03 |
0.8640 |
| 0.9400 |
358.09 |
0.8790 |
| 1.0000 |
358.09 |
1.0000 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Butane, 2-ethoxy-2-methyl- (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.1011 |
0.2713 |
| 0.2007 |
0.5158 |
| 0.3008 |
0.7192 |
| 0.4013 |
0.8684 |
| 0.5005 |
0.9577 |
| 0.6008 |
0.9860 |
| 0.7012 |
0.9448 |
| 0.8001 |
0.8192 |
| 0.8990 |
0.5569 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Butane, 2-ethoxy-2-methyl- (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 0.0000 |
358.16 |
57.30 |
| 0.0640 |
358.00 |
61.80 |
| 0.0950 |
358.12 |
64.10 |
| 0.1300 |
358.15 |
66.10 |
| 0.1670 |
358.11 |
67.70 |
| 0.2030 |
358.11 |
69.00 |
| 0.2420 |
358.07 |
70.30 |
| 0.2830 |
358.06 |
71.30 |
| 0.3210 |
358.01 |
72.00 |
| 0.3630 |
358.06 |
73.00 |
| 0.3980 |
358.02 |
73.40 |
| 0.4020 |
358.10 |
73.40 |
| 0.4290 |
358.12 |
74.00 |
| 0.4500 |
358.13 |
73.90 |
| 0.4590 |
358.07 |
74.10 |
| 0.4910 |
358.04 |
74.30 |
| 0.5020 |
358.11 |
74.20 |
| 0.5230 |
358.08 |
74.50 |
| 0.5670 |
358.08 |
74.20 |
| 0.5850 |
358.10 |
74.60 |
| 0.6400 |
358.06 |
73.90 |
| 0.7060 |
358.06 |
72.90 |
| 0.7530 |
358.07 |
72.70 |
| 0.7900 |
358.03 |
71.80 |
| 0.8310 |
358.06 |
70.70 |
| 0.8640 |
358.03 |
69.50 |
| 0.9100 |
358.06 |
67.40 |
| 0.9300 |
358.03 |
66.10 |
| 0.9400 |
358.09 |
65.70 |
| 1.0000 |
358.09 |
61.30 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Butane, 2-ethoxy-2-methyl- (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 297.67 |
0.7012 |
770.2 |
| 297.67 |
0.8001 |
766.9 |
| 297.68 |
0.5005 |
777.9 |
| 297.68 |
0.6008 |
774.0 |
| 297.68 |
0.8990 |
763.8 |
| 297.69 |
0.1011 |
796.8 |
| 297.69 |
0.2007 |
791.6 |
| 297.69 |
0.3008 |
786.6 |
| 297.69 |
0.4013 |
782.0 |
Sources
Note: These property values are available through the Cheméo API. A free account gives you an access key.