Mixture of Propylamine + Heptane
Datasets
-
Mole fraction (2)
-
Excess molar volume, m3/mol (2)
Mole fraction of Heptane (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Heptane (2) - Liquid |
Mole fraction of Heptane (2) - Gas |
298.15 |
0.0574 |
0.0204 |
298.15 |
0.1084 |
0.0364 |
298.15 |
0.1936 |
0.0575 |
298.15 |
0.3082 |
0.0832 |
298.15 |
0.4073 |
0.1059 |
298.15 |
0.4729 |
0.1274 |
298.15 |
0.5690 |
0.1503 |
298.15 |
0.6777 |
0.1891 |
298.15 |
0.8022 |
0.2622 |
298.15 |
0.9213 |
0.4330 |
298.15 |
0.9611 |
0.5891 |
298.15 |
0.9771 |
0.6956 |
303.15 |
0.0086 |
0.0033 |
303.15 |
0.0230 |
0.0085 |
303.15 |
0.0502 |
0.0181 |
303.15 |
0.0536 |
0.0195 |
303.15 |
0.1003 |
0.0339 |
303.15 |
0.2248 |
0.0664 |
303.15 |
0.3355 |
0.0916 |
303.15 |
0.4353 |
0.1149 |
303.15 |
0.4953 |
0.1320 |
303.15 |
0.5799 |
0.1579 |
303.15 |
0.7023 |
0.2071 |
303.15 |
0.8308 |
0.3004 |
303.15 |
0.9056 |
0.4184 |
Mole fraction of Heptane (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Heptane (2) - Liquid |
Mole fraction of Heptane (2) - Gas |
298.15 |
0.0574 |
0.0204 |
298.15 |
0.1084 |
0.0364 |
298.15 |
0.1936 |
0.0575 |
298.15 |
0.3082 |
0.0832 |
298.15 |
0.4073 |
0.1059 |
298.15 |
0.4729 |
0.1274 |
298.15 |
0.5690 |
0.1503 |
298.15 |
0.6777 |
0.1891 |
298.15 |
0.8022 |
0.2622 |
298.15 |
0.9213 |
0.4330 |
298.15 |
0.9611 |
0.5891 |
298.15 |
0.9771 |
0.6956 |
303.15 |
0.0086 |
0.0033 |
303.15 |
0.0230 |
0.0085 |
303.15 |
0.0502 |
0.0181 |
303.15 |
0.0536 |
0.0195 |
303.15 |
0.1003 |
0.0339 |
303.15 |
0.2248 |
0.0664 |
303.15 |
0.3355 |
0.0916 |
303.15 |
0.4353 |
0.1149 |
303.15 |
0.4953 |
0.1320 |
303.15 |
0.5799 |
0.1579 |
303.15 |
0.7023 |
0.2071 |
303.15 |
0.8308 |
0.3004 |
303.15 |
0.9056 |
0.4184 |
Excess molar volume, m3/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mole fraction of Heptane (2) - Liquid |
Excess molar volume, m3/mol - Liquid |
0.0381 |
1.2600e-07 |
0.0917 |
3.0200e-07 |
0.1923 |
5.6900e-07 |
0.2931 |
7.6800e-07 |
0.3942 |
9.0100e-07 |
0.4005 |
9.0700e-07 |
0.4867 |
9.6800e-07 |
0.4901 |
9.6800e-07 |
0.4946 |
9.6500e-07 |
0.4963 |
9.6900e-07 |
0.5793 |
9.6800e-07 |
0.5866 |
9.6500e-07 |
0.5963 |
9.5600e-07 |
0.7057 |
8.5900e-07 |
0.7181 |
8.4400e-07 |
0.7991 |
6.9300e-07 |
0.8008 |
6.8900e-07 |
0.8986 |
4.1100e-07 |
0.9006 |
4.0300e-07 |
0.9475 |
2.2500e-07 |
0.9482 |
2.2300e-07 |
0.9645 |
1.5600e-07 |
0.9817 |
8.2000e-08 |
0.9905 |
4.2000e-08 |
Excess molar volume, m3/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mole fraction of Heptane (2) - Liquid |
Excess molar volume, m3/mol - Liquid |
0.0381 |
1.2600e-07 |
0.0917 |
3.0200e-07 |
0.1923 |
5.6900e-07 |
0.2931 |
7.6800e-07 |
0.3942 |
9.0100e-07 |
0.4005 |
9.0700e-07 |
0.4867 |
9.6800e-07 |
0.4901 |
9.6800e-07 |
0.4946 |
9.6500e-07 |
0.4963 |
9.6900e-07 |
0.5793 |
9.6800e-07 |
0.5866 |
9.6500e-07 |
0.5963 |
9.5600e-07 |
0.7057 |
8.5900e-07 |
0.7181 |
8.4400e-07 |
0.7991 |
6.9300e-07 |
0.8008 |
6.8900e-07 |
0.8986 |
4.1100e-07 |
0.9006 |
4.0300e-07 |
0.9475 |
2.2500e-07 |
0.9482 |
2.2300e-07 |
0.9645 |
1.5600e-07 |
0.9817 |
8.2000e-08 |
0.9905 |
4.2000e-08 |
Sources