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 Toluene (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
363.15 |
1955.00 |
0.0436 |
0.0158 |
363.15 |
1955.00 |
0.0878 |
0.0287 |
363.15 |
1955.00 |
0.1327 |
0.0425 |
363.15 |
1955.00 |
0.1781 |
0.0559 |
363.15 |
1955.00 |
0.2242 |
0.0681 |
363.15 |
1955.00 |
0.2709 |
0.0809 |
363.15 |
1955.00 |
0.3182 |
0.0970 |
363.15 |
1955.00 |
0.3662 |
0.1100 |
363.15 |
1955.00 |
0.4149 |
0.1220 |
363.15 |
1955.00 |
0.4643 |
0.1330 |
363.15 |
1955.00 |
0.5144 |
0.1440 |
363.15 |
1955.00 |
0.5652 |
0.1510 |
363.15 |
1955.00 |
0.6168 |
0.1540 |
363.15 |
1955.00 |
0.6691 |
0.1590 |
363.15 |
1955.00 |
0.7222 |
0.1610 |
363.15 |
1955.00 |
0.7761 |
0.1570 |
363.15 |
1955.00 |
0.8308 |
0.1460 |
363.15 |
1955.00 |
0.8864 |
0.1210 |
363.15 |
1955.00 |
0.9428 |
0.0745 |
413.15 |
1824.00 |
0.0220 |
0.0105 |
413.15 |
1824.00 |
0.0441 |
0.0221 |
413.15 |
1824.00 |
0.0887 |
0.0403 |
413.15 |
1824.00 |
0.1338 |
0.0587 |
413.15 |
1824.00 |
0.1796 |
0.0779 |
413.15 |
1824.00 |
0.2259 |
0.0942 |
413.15 |
1824.00 |
0.2728 |
0.1110 |
413.15 |
1824.00 |
0.3204 |
0.1300 |
413.15 |
1824.00 |
0.3686 |
0.1480 |
413.15 |
1824.00 |
0.4174 |
0.1700 |
413.15 |
1824.00 |
0.4668 |
0.1880 |
413.15 |
1824.00 |
0.5169 |
0.2030 |
413.15 |
1824.00 |
0.5677 |
0.2190 |
413.15 |
1824.00 |
0.6192 |
0.2320 |
413.15 |
1824.00 |
0.6714 |
0.2390 |
413.15 |
1824.00 |
0.7243 |
0.2410 |
413.15 |
1824.00 |
0.7779 |
0.2330 |
413.15 |
1824.00 |
0.8323 |
0.2080 |
413.15 |
1824.00 |
0.8874 |
0.1700 |
413.15 |
1824.00 |
0.9433 |
0.1030 |
413.15 |
1824.00 |
0.9715 |
0.0561 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Toluene (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
363.15 |
1955.00 |
0.0436 |
0.0158 |
363.15 |
1955.00 |
0.0878 |
0.0287 |
363.15 |
1955.00 |
0.1327 |
0.0425 |
363.15 |
1955.00 |
0.1781 |
0.0559 |
363.15 |
1955.00 |
0.2242 |
0.0681 |
363.15 |
1955.00 |
0.2709 |
0.0809 |
363.15 |
1955.00 |
0.3182 |
0.0970 |
363.15 |
1955.00 |
0.3662 |
0.1100 |
363.15 |
1955.00 |
0.4149 |
0.1220 |
363.15 |
1955.00 |
0.4643 |
0.1330 |
363.15 |
1955.00 |
0.5144 |
0.1440 |
363.15 |
1955.00 |
0.5652 |
0.1510 |
363.15 |
1955.00 |
0.6168 |
0.1540 |
363.15 |
1955.00 |
0.6691 |
0.1590 |
363.15 |
1955.00 |
0.7222 |
0.1610 |
363.15 |
1955.00 |
0.7761 |
0.1570 |
363.15 |
1955.00 |
0.8308 |
0.1460 |
363.15 |
1955.00 |
0.8864 |
0.1210 |
363.15 |
1955.00 |
0.9428 |
0.0745 |
413.15 |
1824.00 |
0.0220 |
0.0105 |
413.15 |
1824.00 |
0.0441 |
0.0221 |
413.15 |
1824.00 |
0.0887 |
0.0403 |
413.15 |
1824.00 |
0.1338 |
0.0587 |
413.15 |
1824.00 |
0.1796 |
0.0779 |
413.15 |
1824.00 |
0.2259 |
0.0942 |
413.15 |
1824.00 |
0.2728 |
0.1110 |
413.15 |
1824.00 |
0.3204 |
0.1300 |
413.15 |
1824.00 |
0.3686 |
0.1480 |
413.15 |
1824.00 |
0.4174 |
0.1700 |
413.15 |
1824.00 |
0.4668 |
0.1880 |
413.15 |
1824.00 |
0.5169 |
0.2030 |
413.15 |
1824.00 |
0.5677 |
0.2190 |
413.15 |
1824.00 |
0.6192 |
0.2320 |
413.15 |
1824.00 |
0.6714 |
0.2390 |
413.15 |
1824.00 |
0.7243 |
0.2410 |
413.15 |
1824.00 |
0.7779 |
0.2330 |
413.15 |
1824.00 |
0.8323 |
0.2080 |
413.15 |
1824.00 |
0.8874 |
0.1700 |
413.15 |
1824.00 |
0.9433 |
0.1030 |
413.15 |
1824.00 |
0.9715 |
0.0561 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
353.15 (Liquid)
Mole fraction of Toluene (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
5.29 |
0.0014 |
5.38 |
0.0027 |
5.46 |
0.0050 |
5.58 |
0.0087 |
5.79 |
0.0131 |
6.03 |
0.0208 |
6.45 |
0.0308 |
6.99 |
0.0445 |
7.70 |
0.0613 |
8.55 |
0.0821 |
9.58 |
0.1068 |
10.79 |
0.1355 |
12.13 |
0.1709 |
13.72 |
0.2094 |
15.39 |
0.2512 |
17.11 |
0.2947 |
18.83 |
0.3395 |
20.52 |
0.3847 |
22.14 |
0.4251 |
23.46 |
0.4297 |
23.66 |
0.4681 |
24.85 |
0.4733 |
25.10 |
0.5134 |
26.27 |
0.5155 |
26.41 |
0.5614 |
27.69 |
0.6108 |
29.08 |
0.6607 |
30.42 |
0.7104 |
31.71 |
0.7589 |
32.92 |
0.8046 |
34.03 |
0.8469 |
35.05 |
0.8812 |
35.87 |
0.9109 |
36.59 |
0.9355 |
37.19 |
0.9548 |
37.68 |
0.9698 |
38.06 |
0.9793 |
38.32 |
0.9856 |
38.48 |
0.9903 |
38.62 |
0.9940 |
38.72 |
0.9966 |
38.78 |
0.9987 |
38.85 |
1.0000 |
38.92 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
353.15 (Liquid)
Mole fraction of Toluene (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
5.29 |
0.0014 |
5.38 |
0.0027 |
5.46 |
0.0050 |
5.58 |
0.0087 |
5.79 |
0.0131 |
6.03 |
0.0208 |
6.45 |
0.0308 |
6.99 |
0.0445 |
7.70 |
0.0613 |
8.55 |
0.0821 |
9.58 |
0.1068 |
10.79 |
0.1355 |
12.13 |
0.1709 |
13.72 |
0.2094 |
15.39 |
0.2512 |
17.11 |
0.2947 |
18.83 |
0.3395 |
20.52 |
0.3847 |
22.14 |
0.4251 |
23.46 |
0.4297 |
23.66 |
0.4681 |
24.85 |
0.4733 |
25.10 |
0.5134 |
26.27 |
0.5155 |
26.41 |
0.5614 |
27.69 |
0.6108 |
29.08 |
0.6607 |
30.42 |
0.7104 |
31.71 |
0.7589 |
32.92 |
0.8046 |
34.03 |
0.8469 |
35.05 |
0.8812 |
35.87 |
0.9109 |
36.59 |
0.9355 |
37.19 |
0.9548 |
37.68 |
0.9698 |
38.06 |
0.9793 |
38.32 |
0.9856 |
38.48 |
0.9903 |
38.62 |
0.9940 |
38.72 |
0.9966 |
38.78 |
0.9987 |
38.85 |
1.0000 |
38.92 |
Sources