Mixture of 1-Hexyne + n-Propyl acetate
Datasets
-
Mole fraction (2)
-
Excess molar enthalpy (molar enthalpy (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
Mole fraction of n-Propyl acetate (2)
[ref]
Fixed |
Measured |
Mole fraction of n-Propyl acetate (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of n-Propyl acetate (2) - Gas |
0.0000 |
273.15 |
0.0000 |
0.0000 |
283.15 |
0.0000 |
0.0000 |
293.15 |
0.0000 |
0.0000 |
298.15 |
0.0000 |
0.0000 |
303.15 |
0.0000 |
0.0000 |
313.15 |
0.0000 |
0.0000 |
323.15 |
0.0000 |
0.0000 |
333.15 |
0.0000 |
0.0000 |
343.15 |
0.0000 |
0.0000 |
353.15 |
0.0000 |
0.0000 |
363.15 |
0.0000 |
0.1510 |
273.15 |
0.0334 |
0.1510 |
283.15 |
0.0374 |
0.1510 |
293.15 |
0.0414 |
0.1510 |
298.15 |
0.0435 |
0.1510 |
303.15 |
0.0455 |
0.1510 |
313.15 |
0.0495 |
0.1510 |
323.15 |
0.0535 |
0.1510 |
333.15 |
0.0576 |
0.1510 |
343.15 |
0.0616 |
0.1510 |
353.15 |
0.0655 |
0.1510 |
363.15 |
0.0695 |
0.2671 |
273.15 |
0.0665 |
0.2671 |
283.15 |
0.0740 |
0.2671 |
293.15 |
0.0815 |
0.2671 |
298.15 |
0.0852 |
0.2671 |
303.15 |
0.0889 |
0.2671 |
313.15 |
0.0962 |
0.2671 |
323.15 |
0.1034 |
0.2671 |
333.15 |
0.1105 |
0.2671 |
343.15 |
0.1175 |
0.2671 |
353.15 |
0.1244 |
0.2671 |
363.15 |
0.1312 |
0.3758 |
273.15 |
0.1067 |
0.3758 |
283.15 |
0.1178 |
0.3758 |
293.15 |
0.1287 |
0.3758 |
298.15 |
0.1340 |
0.3758 |
303.15 |
0.1393 |
0.3758 |
313.15 |
0.1498 |
0.3758 |
323.15 |
0.1600 |
0.3758 |
333.15 |
0.1700 |
0.3758 |
343.15 |
0.1797 |
0.3758 |
353.15 |
0.1893 |
0.3758 |
363.15 |
0.1986 |
0.5278 |
273.15 |
0.1863 |
0.5278 |
283.15 |
0.2025 |
0.5278 |
293.15 |
0.2182 |
0.5278 |
298.15 |
0.2259 |
0.5278 |
303.15 |
0.2334 |
0.5278 |
313.15 |
0.2481 |
0.5278 |
323.15 |
0.2623 |
0.5278 |
333.15 |
0.2761 |
0.5278 |
343.15 |
0.2893 |
0.5278 |
353.15 |
0.3022 |
0.5278 |
363.15 |
0.3146 |
0.6405 |
273.15 |
0.2727 |
0.6405 |
283.15 |
0.2924 |
0.6405 |
293.15 |
0.3113 |
0.6405 |
298.15 |
0.3205 |
0.6405 |
303.15 |
0.3294 |
0.6405 |
313.15 |
0.3467 |
0.6405 |
323.15 |
0.3633 |
0.6405 |
333.15 |
0.3792 |
0.6405 |
343.15 |
0.3944 |
0.6405 |
353.15 |
0.4090 |
0.6405 |
363.15 |
0.4230 |
0.7766 |
273.15 |
0.4305 |
0.7766 |
283.15 |
0.4527 |
0.7766 |
293.15 |
0.4735 |
0.7766 |
298.15 |
0.4834 |
0.7766 |
303.15 |
0.4931 |
0.7766 |
313.15 |
0.5115 |
0.7766 |
323.15 |
0.5289 |
0.7766 |
333.15 |
0.5454 |
0.7766 |
343.15 |
0.5609 |
0.7766 |
353.15 |
0.5758 |
0.7766 |
363.15 |
0.5898 |
0.9044 |
273.15 |
0.6787 |
0.9044 |
283.15 |
0.6967 |
0.9044 |
293.15 |
0.7130 |
0.9044 |
298.15 |
0.7207 |
0.9044 |
303.15 |
0.7280 |
0.9044 |
313.15 |
0.7418 |
0.9044 |
323.15 |
0.7546 |
0.9044 |
333.15 |
0.7664 |
0.9044 |
343.15 |
0.7774 |
0.9044 |
353.15 |
0.7877 |
0.9044 |
363.15 |
0.7973 |
1.0000 |
273.15 |
1.0000 |
1.0000 |
283.15 |
1.0000 |
1.0000 |
293.15 |
1.0000 |
1.0000 |
298.15 |
1.0000 |
1.0000 |
303.15 |
1.0000 |
1.0000 |
313.15 |
1.0000 |
1.0000 |
323.15 |
1.0000 |
1.0000 |
333.15 |
1.0000 |
1.0000 |
343.15 |
1.0000 |
1.0000 |
353.15 |
1.0000 |
1.0000 |
363.15 |
1.0000 |
Mole fraction of n-Propyl acetate (2)
[ref]
Fixed |
Measured |
Mole fraction of n-Propyl acetate (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of n-Propyl acetate (2) - Gas |
0.0000 |
273.15 |
0.0000 |
0.0000 |
283.15 |
0.0000 |
0.0000 |
293.15 |
0.0000 |
0.0000 |
298.15 |
0.0000 |
0.0000 |
303.15 |
0.0000 |
0.0000 |
313.15 |
0.0000 |
0.0000 |
323.15 |
0.0000 |
0.0000 |
333.15 |
0.0000 |
0.0000 |
343.15 |
0.0000 |
0.0000 |
353.15 |
0.0000 |
0.0000 |
363.15 |
0.0000 |
0.1510 |
273.15 |
0.0334 |
0.1510 |
283.15 |
0.0374 |
0.1510 |
293.15 |
0.0414 |
0.1510 |
298.15 |
0.0435 |
0.1510 |
303.15 |
0.0455 |
0.1510 |
313.15 |
0.0495 |
0.1510 |
323.15 |
0.0535 |
0.1510 |
333.15 |
0.0576 |
0.1510 |
343.15 |
0.0616 |
0.1510 |
353.15 |
0.0655 |
0.1510 |
363.15 |
0.0695 |
0.2671 |
273.15 |
0.0665 |
0.2671 |
283.15 |
0.0740 |
0.2671 |
293.15 |
0.0815 |
0.2671 |
298.15 |
0.0852 |
0.2671 |
303.15 |
0.0889 |
0.2671 |
313.15 |
0.0962 |
0.2671 |
323.15 |
0.1034 |
0.2671 |
333.15 |
0.1105 |
0.2671 |
343.15 |
0.1175 |
0.2671 |
353.15 |
0.1244 |
0.2671 |
363.15 |
0.1312 |
0.3758 |
273.15 |
0.1067 |
0.3758 |
283.15 |
0.1178 |
0.3758 |
293.15 |
0.1287 |
0.3758 |
298.15 |
0.1340 |
0.3758 |
303.15 |
0.1393 |
0.3758 |
313.15 |
0.1498 |
0.3758 |
323.15 |
0.1600 |
0.3758 |
333.15 |
0.1700 |
0.3758 |
343.15 |
0.1797 |
0.3758 |
353.15 |
0.1893 |
0.3758 |
363.15 |
0.1986 |
0.5278 |
273.15 |
0.1863 |
0.5278 |
283.15 |
0.2025 |
0.5278 |
293.15 |
0.2182 |
0.5278 |
298.15 |
0.2259 |
0.5278 |
303.15 |
0.2334 |
0.5278 |
313.15 |
0.2481 |
0.5278 |
323.15 |
0.2623 |
0.5278 |
333.15 |
0.2761 |
0.5278 |
343.15 |
0.2893 |
0.5278 |
353.15 |
0.3022 |
0.5278 |
363.15 |
0.3146 |
0.6405 |
273.15 |
0.2727 |
0.6405 |
283.15 |
0.2924 |
0.6405 |
293.15 |
0.3113 |
0.6405 |
298.15 |
0.3205 |
0.6405 |
303.15 |
0.3294 |
0.6405 |
313.15 |
0.3467 |
0.6405 |
323.15 |
0.3633 |
0.6405 |
333.15 |
0.3792 |
0.6405 |
343.15 |
0.3944 |
0.6405 |
353.15 |
0.4090 |
0.6405 |
363.15 |
0.4230 |
0.7766 |
273.15 |
0.4305 |
0.7766 |
283.15 |
0.4527 |
0.7766 |
293.15 |
0.4735 |
0.7766 |
298.15 |
0.4834 |
0.7766 |
303.15 |
0.4931 |
0.7766 |
313.15 |
0.5115 |
0.7766 |
323.15 |
0.5289 |
0.7766 |
333.15 |
0.5454 |
0.7766 |
343.15 |
0.5609 |
0.7766 |
353.15 |
0.5758 |
0.7766 |
363.15 |
0.5898 |
0.9044 |
273.15 |
0.6787 |
0.9044 |
283.15 |
0.6967 |
0.9044 |
293.15 |
0.7130 |
0.9044 |
298.15 |
0.7207 |
0.9044 |
303.15 |
0.7280 |
0.9044 |
313.15 |
0.7418 |
0.9044 |
323.15 |
0.7546 |
0.9044 |
333.15 |
0.7664 |
0.9044 |
343.15 |
0.7774 |
0.9044 |
353.15 |
0.7877 |
0.9044 |
363.15 |
0.7973 |
1.0000 |
273.15 |
1.0000 |
1.0000 |
283.15 |
1.0000 |
1.0000 |
293.15 |
1.0000 |
1.0000 |
298.15 |
1.0000 |
1.0000 |
303.15 |
1.0000 |
1.0000 |
313.15 |
1.0000 |
1.0000 |
323.15 |
1.0000 |
1.0000 |
333.15 |
1.0000 |
1.0000 |
343.15 |
1.0000 |
1.0000 |
353.15 |
1.0000 |
1.0000 |
363.15 |
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 n-Propyl acetate (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.1079 |
-0.1274 |
0.1967 |
-0.1994 |
0.3032 |
-0.2542 |
0.3950 |
-0.2760 |
0.4373 |
-0.2778 |
0.5003 |
-0.2738 |
0.5950 |
-0.2532 |
0.6575 |
-0.2315 |
0.6989 |
-0.2138 |
0.7967 |
-0.1590 |
0.8992 |
-0.0857 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of n-Propyl acetate (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.1079 |
-0.1274 |
0.1967 |
-0.1994 |
0.3032 |
-0.2542 |
0.3950 |
-0.2760 |
0.4373 |
-0.2778 |
0.5003 |
-0.2738 |
0.5950 |
-0.2532 |
0.6575 |
-0.2315 |
0.6989 |
-0.2138 |
0.7967 |
-0.1590 |
0.8992 |
-0.0857 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of n-Propyl acetate (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
273.15 |
4.91 |
0.0000 |
283.15 |
8.42 |
0.0000 |
293.15 |
13.81 |
0.0000 |
298.15 |
17.41 |
0.0000 |
303.15 |
21.75 |
0.0000 |
313.15 |
33.07 |
0.0000 |
323.15 |
48.74 |
0.0000 |
333.15 |
69.84 |
0.0000 |
343.15 |
97.60 |
0.0000 |
353.15 |
133.35 |
0.0000 |
363.15 |
178.53 |
0.1510 |
273.15 |
4.31 |
0.1510 |
283.15 |
7.43 |
0.1510 |
293.15 |
12.24 |
0.1510 |
298.15 |
15.47 |
0.1510 |
303.15 |
19.36 |
0.1510 |
313.15 |
29.57 |
0.1510 |
323.15 |
43.75 |
0.1510 |
333.15 |
62.93 |
0.1510 |
343.15 |
88.28 |
0.1510 |
353.15 |
121.05 |
0.1510 |
363.15 |
162.63 |
0.2671 |
273.15 |
3.85 |
0.2671 |
283.15 |
6.66 |
0.2671 |
293.15 |
11.01 |
0.2671 |
298.15 |
13.93 |
0.2671 |
303.15 |
17.47 |
0.2671 |
313.15 |
26.77 |
0.2671 |
323.15 |
39.74 |
0.2671 |
333.15 |
57.36 |
0.2671 |
343.15 |
80.73 |
0.2671 |
353.15 |
111.06 |
0.2671 |
363.15 |
149.70 |
0.3758 |
273.15 |
3.41 |
0.3758 |
283.15 |
5.92 |
0.3758 |
293.15 |
9.84 |
0.3758 |
298.15 |
12.48 |
0.3758 |
303.15 |
15.69 |
0.3758 |
313.15 |
24.15 |
0.3758 |
323.15 |
35.99 |
0.3758 |
333.15 |
52.15 |
0.3758 |
343.15 |
73.64 |
0.3758 |
353.15 |
101.64 |
0.3758 |
363.15 |
137.41 |
0.5278 |
273.15 |
2.78 |
0.5278 |
283.15 |
4.88 |
0.5278 |
293.15 |
8.19 |
0.5278 |
298.15 |
10.45 |
0.5278 |
303.15 |
13.19 |
0.5278 |
313.15 |
20.48 |
0.5278 |
323.15 |
30.78 |
0.5278 |
333.15 |
44.94 |
0.5278 |
343.15 |
63.94 |
0.5278 |
353.15 |
88.87 |
0.5278 |
363.15 |
120.94 |
0.6405 |
273.15 |
2.33 |
0.6405 |
283.15 |
4.15 |
0.6405 |
293.15 |
7.03 |
0.6405 |
298.15 |
9.00 |
0.6405 |
303.15 |
11.42 |
0.6405 |
313.15 |
17.87 |
0.6405 |
323.15 |
27.06 |
0.6405 |
333.15 |
39.77 |
0.6405 |
343.15 |
56.93 |
0.6405 |
353.15 |
79.56 |
0.6405 |
363.15 |
108.83 |
0.7766 |
273.15 |
1.81 |
0.7766 |
283.15 |
3.27 |
0.7766 |
293.15 |
5.63 |
0.7766 |
298.15 |
7.27 |
0.7766 |
303.15 |
9.28 |
0.7766 |
313.15 |
14.71 |
0.7766 |
323.15 |
22.53 |
0.7766 |
333.15 |
33.47 |
0.7766 |
343.15 |
48.38 |
0.7766 |
353.15 |
68.23 |
0.7766 |
363.15 |
94.11 |
0.9044 |
273.15 |
1.34 |
0.9044 |
283.15 |
2.48 |
0.9044 |
293.15 |
4.35 |
0.9044 |
298.15 |
5.66 |
0.9044 |
303.15 |
7.30 |
0.9044 |
313.15 |
11.76 |
0.9044 |
323.15 |
18.30 |
0.9044 |
333.15 |
27.57 |
0.9044 |
343.15 |
40.39 |
0.9044 |
353.15 |
57.66 |
0.9044 |
363.15 |
80.43 |
1.0000 |
273.15 |
1.01 |
1.0000 |
283.15 |
1.91 |
1.0000 |
293.15 |
3.43 |
1.0000 |
298.15 |
4.51 |
1.0000 |
303.15 |
5.87 |
1.0000 |
313.15 |
9.64 |
1.0000 |
323.15 |
15.25 |
1.0000 |
333.15 |
23.33 |
1.0000 |
343.15 |
34.64 |
1.0000 |
353.15 |
50.07 |
1.0000 |
363.15 |
70.64 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of n-Propyl acetate (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
273.15 |
4.91 |
0.0000 |
283.15 |
8.42 |
0.0000 |
293.15 |
13.81 |
0.0000 |
298.15 |
17.41 |
0.0000 |
303.15 |
21.75 |
0.0000 |
313.15 |
33.07 |
0.0000 |
323.15 |
48.74 |
0.0000 |
333.15 |
69.84 |
0.0000 |
343.15 |
97.60 |
0.0000 |
353.15 |
133.35 |
0.0000 |
363.15 |
178.53 |
0.1510 |
273.15 |
4.31 |
0.1510 |
283.15 |
7.43 |
0.1510 |
293.15 |
12.24 |
0.1510 |
298.15 |
15.47 |
0.1510 |
303.15 |
19.36 |
0.1510 |
313.15 |
29.57 |
0.1510 |
323.15 |
43.75 |
0.1510 |
333.15 |
62.93 |
0.1510 |
343.15 |
88.28 |
0.1510 |
353.15 |
121.05 |
0.1510 |
363.15 |
162.63 |
0.2671 |
273.15 |
3.85 |
0.2671 |
283.15 |
6.66 |
0.2671 |
293.15 |
11.01 |
0.2671 |
298.15 |
13.93 |
0.2671 |
303.15 |
17.47 |
0.2671 |
313.15 |
26.77 |
0.2671 |
323.15 |
39.74 |
0.2671 |
333.15 |
57.36 |
0.2671 |
343.15 |
80.73 |
0.2671 |
353.15 |
111.06 |
0.2671 |
363.15 |
149.70 |
0.3758 |
273.15 |
3.41 |
0.3758 |
283.15 |
5.92 |
0.3758 |
293.15 |
9.84 |
0.3758 |
298.15 |
12.48 |
0.3758 |
303.15 |
15.69 |
0.3758 |
313.15 |
24.15 |
0.3758 |
323.15 |
35.99 |
0.3758 |
333.15 |
52.15 |
0.3758 |
343.15 |
73.64 |
0.3758 |
353.15 |
101.64 |
0.3758 |
363.15 |
137.41 |
0.5278 |
273.15 |
2.78 |
0.5278 |
283.15 |
4.88 |
0.5278 |
293.15 |
8.19 |
0.5278 |
298.15 |
10.45 |
0.5278 |
303.15 |
13.19 |
0.5278 |
313.15 |
20.48 |
0.5278 |
323.15 |
30.78 |
0.5278 |
333.15 |
44.94 |
0.5278 |
343.15 |
63.94 |
0.5278 |
353.15 |
88.87 |
0.5278 |
363.15 |
120.94 |
0.6405 |
273.15 |
2.33 |
0.6405 |
283.15 |
4.15 |
0.6405 |
293.15 |
7.03 |
0.6405 |
298.15 |
9.00 |
0.6405 |
303.15 |
11.42 |
0.6405 |
313.15 |
17.87 |
0.6405 |
323.15 |
27.06 |
0.6405 |
333.15 |
39.77 |
0.6405 |
343.15 |
56.93 |
0.6405 |
353.15 |
79.56 |
0.6405 |
363.15 |
108.83 |
0.7766 |
273.15 |
1.81 |
0.7766 |
283.15 |
3.27 |
0.7766 |
293.15 |
5.63 |
0.7766 |
298.15 |
7.27 |
0.7766 |
303.15 |
9.28 |
0.7766 |
313.15 |
14.71 |
0.7766 |
323.15 |
22.53 |
0.7766 |
333.15 |
33.47 |
0.7766 |
343.15 |
48.38 |
0.7766 |
353.15 |
68.23 |
0.7766 |
363.15 |
94.11 |
0.9044 |
273.15 |
1.34 |
0.9044 |
283.15 |
2.48 |
0.9044 |
293.15 |
4.35 |
0.9044 |
298.15 |
5.66 |
0.9044 |
303.15 |
7.30 |
0.9044 |
313.15 |
11.76 |
0.9044 |
323.15 |
18.30 |
0.9044 |
333.15 |
27.57 |
0.9044 |
343.15 |
40.39 |
0.9044 |
353.15 |
57.66 |
0.9044 |
363.15 |
80.43 |
1.0000 |
273.15 |
1.01 |
1.0000 |
283.15 |
1.91 |
1.0000 |
293.15 |
3.43 |
1.0000 |
298.15 |
4.51 |
1.0000 |
303.15 |
5.87 |
1.0000 |
313.15 |
9.64 |
1.0000 |
323.15 |
15.25 |
1.0000 |
333.15 |
23.33 |
1.0000 |
343.15 |
34.64 |
1.0000 |
353.15 |
50.07 |
1.0000 |
363.15 |
70.64 |
Sources