Datasets
-
Excess molar enthalpy (molar enthalpy (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of n-Hexane (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 363.15 |
1982.00 |
0.0358 |
0.2340 |
| 363.15 |
1982.00 |
0.0726 |
0.4770 |
| 363.15 |
1982.00 |
0.1106 |
0.7040 |
| 363.15 |
1982.00 |
0.1498 |
0.9130 |
| 363.15 |
1982.00 |
0.1902 |
1.098 |
| 363.15 |
1982.00 |
0.2319 |
1.263 |
| 363.15 |
1982.00 |
0.2750 |
1.41 |
| 363.15 |
1982.00 |
0.3196 |
1.532 |
| 363.15 |
1982.00 |
0.3657 |
1.634 |
| 363.15 |
1982.00 |
0.4134 |
1.714 |
| 363.15 |
1982.00 |
0.4627 |
1.752 |
| 363.15 |
1982.00 |
0.5138 |
1.782 |
| 363.15 |
1982.00 |
0.5668 |
1.783 |
| 363.15 |
1982.00 |
0.6218 |
1.748 |
| 363.15 |
1982.00 |
0.6788 |
1.673 |
| 363.15 |
1982.00 |
0.7381 |
1.549 |
| 363.15 |
1982.00 |
0.7997 |
1.357 |
| 363.15 |
1982.00 |
0.8638 |
1.08 |
| 363.15 |
1982.00 |
0.9305 |
0.6570 |
| 413.15 |
1824.00 |
0.0179 |
0.1210 |
| 413.15 |
1824.00 |
0.0361 |
0.2470 |
| 413.15 |
1824.00 |
0.0733 |
0.4900 |
| 413.15 |
1824.00 |
0.1116 |
0.7110 |
| 413.15 |
1824.00 |
0.1510 |
0.9130 |
| 413.15 |
1824.00 |
0.1917 |
1.097 |
| 413.15 |
1824.00 |
0.2337 |
1.27 |
| 413.15 |
1824.00 |
0.2770 |
1.415 |
| 413.15 |
1824.00 |
0.3217 |
1.545 |
| 413.15 |
1824.00 |
0.3679 |
1.657 |
| 413.15 |
1824.00 |
0.4157 |
1.762 |
| 413.15 |
1824.00 |
0.4651 |
1.81 |
| 413.15 |
1824.00 |
0.5163 |
1.847 |
| 413.15 |
1824.00 |
0.5692 |
1.849 |
| 413.15 |
1824.00 |
0.6241 |
1.814 |
| 413.15 |
1824.00 |
0.6810 |
1.736 |
| 413.15 |
1824.00 |
0.7400 |
1.616 |
| 413.15 |
1824.00 |
0.8013 |
1.411 |
| 413.15 |
1824.00 |
0.8649 |
1.106 |
| 413.15 |
1824.00 |
0.9311 |
0.6610 |
| 413.15 |
1824.00 |
0.9652 |
0.3600 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of n-Hexane (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 363.15 |
1982.00 |
0.0358 |
0.2340 |
| 363.15 |
1982.00 |
0.0726 |
0.4770 |
| 363.15 |
1982.00 |
0.1106 |
0.7040 |
| 363.15 |
1982.00 |
0.1498 |
0.9130 |
| 363.15 |
1982.00 |
0.1902 |
1.098 |
| 363.15 |
1982.00 |
0.2319 |
1.263 |
| 363.15 |
1982.00 |
0.2750 |
1.41 |
| 363.15 |
1982.00 |
0.3196 |
1.532 |
| 363.15 |
1982.00 |
0.3657 |
1.634 |
| 363.15 |
1982.00 |
0.4134 |
1.714 |
| 363.15 |
1982.00 |
0.4627 |
1.752 |
| 363.15 |
1982.00 |
0.5138 |
1.782 |
| 363.15 |
1982.00 |
0.5668 |
1.783 |
| 363.15 |
1982.00 |
0.6218 |
1.748 |
| 363.15 |
1982.00 |
0.6788 |
1.673 |
| 363.15 |
1982.00 |
0.7381 |
1.549 |
| 363.15 |
1982.00 |
0.7997 |
1.357 |
| 363.15 |
1982.00 |
0.8638 |
1.08 |
| 363.15 |
1982.00 |
0.9305 |
0.6570 |
| 413.15 |
1824.00 |
0.0179 |
0.1210 |
| 413.15 |
1824.00 |
0.0361 |
0.2470 |
| 413.15 |
1824.00 |
0.0733 |
0.4900 |
| 413.15 |
1824.00 |
0.1116 |
0.7110 |
| 413.15 |
1824.00 |
0.1510 |
0.9130 |
| 413.15 |
1824.00 |
0.1917 |
1.097 |
| 413.15 |
1824.00 |
0.2337 |
1.27 |
| 413.15 |
1824.00 |
0.2770 |
1.415 |
| 413.15 |
1824.00 |
0.3217 |
1.545 |
| 413.15 |
1824.00 |
0.3679 |
1.657 |
| 413.15 |
1824.00 |
0.4157 |
1.762 |
| 413.15 |
1824.00 |
0.4651 |
1.81 |
| 413.15 |
1824.00 |
0.5163 |
1.847 |
| 413.15 |
1824.00 |
0.5692 |
1.849 |
| 413.15 |
1824.00 |
0.6241 |
1.814 |
| 413.15 |
1824.00 |
0.6810 |
1.736 |
| 413.15 |
1824.00 |
0.7400 |
1.616 |
| 413.15 |
1824.00 |
0.8013 |
1.411 |
| 413.15 |
1824.00 |
0.8649 |
1.106 |
| 413.15 |
1824.00 |
0.9311 |
0.6610 |
| 413.15 |
1824.00 |
0.9652 |
0.3600 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
353.15 (Liquid)
| Mole fraction of n-Hexane (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 0.0000 |
5.37 |
| 0.0023 |
7.48 |
| 0.0047 |
9.74 |
| 0.0073 |
12.06 |
| 0.0104 |
14.84 |
| 0.0137 |
17.81 |
| 0.0224 |
25.06 |
| 0.0335 |
33.47 |
| 0.0470 |
42.97 |
| 0.0634 |
52.94 |
| 0.0822 |
62.95 |
| 0.1042 |
72.79 |
| 0.1293 |
82.08 |
| 0.1602 |
91.16 |
| 0.1941 |
98.82 |
| 0.2310 |
105.12 |
| 0.2700 |
110.06 |
| 0.3105 |
113.89 |
| 0.3521 |
116.83 |
| 0.3942 |
119.11 |
| 0.4355 |
120.89 |
| 0.4600 |
121.63 |
| 0.4762 |
122.33 |
| 0.5081 |
123.16 |
| 0.5586 |
124.55 |
| 0.6109 |
125.87 |
| 0.6641 |
127.20 |
| 0.7173 |
128.59 |
| 0.7685 |
130.09 |
| 0.8170 |
131.75 |
| 0.8570 |
133.35 |
| 0.8921 |
135.00 |
| 0.9215 |
136.63 |
| 0.9448 |
138.11 |
| 0.9631 |
139.40 |
| 0.9748 |
140.27 |
| 0.9825 |
140.87 |
| 0.9888 |
141.36 |
| 0.9929 |
141.74 |
| 0.9960 |
142.02 |
| 0.9984 |
142.24 |
| 1.0000 |
142.40 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
353.15 (Liquid)
| Mole fraction of n-Hexane (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 0.0000 |
5.37 |
| 0.0023 |
7.48 |
| 0.0047 |
9.74 |
| 0.0073 |
12.06 |
| 0.0104 |
14.84 |
| 0.0137 |
17.81 |
| 0.0224 |
25.06 |
| 0.0335 |
33.47 |
| 0.0470 |
42.97 |
| 0.0634 |
52.94 |
| 0.0822 |
62.95 |
| 0.1042 |
72.79 |
| 0.1293 |
82.08 |
| 0.1602 |
91.16 |
| 0.1941 |
98.82 |
| 0.2310 |
105.12 |
| 0.2700 |
110.06 |
| 0.3105 |
113.89 |
| 0.3521 |
116.83 |
| 0.3942 |
119.11 |
| 0.4355 |
120.89 |
| 0.4600 |
121.63 |
| 0.4762 |
122.33 |
| 0.5081 |
123.16 |
| 0.5586 |
124.55 |
| 0.6109 |
125.87 |
| 0.6641 |
127.20 |
| 0.7173 |
128.59 |
| 0.7685 |
130.09 |
| 0.8170 |
131.75 |
| 0.8570 |
133.35 |
| 0.8921 |
135.00 |
| 0.9215 |
136.63 |
| 0.9448 |
138.11 |
| 0.9631 |
139.40 |
| 0.9748 |
140.27 |
| 0.9825 |
140.87 |
| 0.9888 |
141.36 |
| 0.9929 |
141.74 |
| 0.9960 |
142.02 |
| 0.9984 |
142.24 |
| 1.0000 |
142.40 |
Sources