Mixture of Propane, 2-methoxy-2-methyl- + 1-Hexyne
Datasets
-
Excess molar enthalpy (molar enthalpy (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of 1-Hexyne (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.1111 |
-0.1390 |
| 0.2113 |
-0.2680 |
| 0.3134 |
-0.3700 |
| 0.3890 |
-0.4200 |
| 0.4482 |
-0.4360 |
| 0.5204 |
-0.4250 |
| 0.6206 |
-0.3770 |
| 0.7263 |
-0.2980 |
| 0.8179 |
-0.2200 |
| 0.9011 |
-0.1420 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of 1-Hexyne (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.1111 |
-0.1390 |
| 0.2113 |
-0.2680 |
| 0.3134 |
-0.3700 |
| 0.3890 |
-0.4200 |
| 0.4482 |
-0.4360 |
| 0.5204 |
-0.4250 |
| 0.6206 |
-0.3770 |
| 0.7263 |
-0.2980 |
| 0.8179 |
-0.2200 |
| 0.9011 |
-0.1420 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 1-Hexyne (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 263.15 |
0.1567 |
5.59 |
| 263.15 |
0.2670 |
5.14 |
| 263.15 |
0.3528 |
4.78 |
| 263.15 |
0.4802 |
4.31 |
| 263.15 |
0.5725 |
3.96 |
| 263.15 |
0.6692 |
3.64 |
| 263.15 |
0.7626 |
3.33 |
| 263.15 |
0.8653 |
3.04 |
| 273.15 |
0.1567 |
9.57 |
| 273.15 |
0.2670 |
8.85 |
| 273.15 |
0.3528 |
8.27 |
| 273.15 |
0.4802 |
7.50 |
| 273.15 |
0.5725 |
6.95 |
| 273.15 |
0.6692 |
6.43 |
| 273.15 |
0.7626 |
5.92 |
| 273.15 |
0.8653 |
5.44 |
| 283.15 |
0.1567 |
15.66 |
| 283.15 |
0.2670 |
14.55 |
| 283.15 |
0.3528 |
13.67 |
| 283.15 |
0.4802 |
12.45 |
| 283.15 |
0.5725 |
11.63 |
| 283.15 |
0.6692 |
10.80 |
| 283.15 |
0.7626 |
10.00 |
| 283.15 |
0.8653 |
9.25 |
| 293.15 |
0.1567 |
24.62 |
| 293.15 |
0.2670 |
22.97 |
| 293.15 |
0.3528 |
21.67 |
| 293.15 |
0.4802 |
19.84 |
| 293.15 |
0.5725 |
18.65 |
| 293.15 |
0.6692 |
17.39 |
| 293.15 |
0.7626 |
16.19 |
| 293.15 |
0.8653 |
15.05 |
| 298.15 |
0.1567 |
30.45 |
| 298.15 |
0.2670 |
28.47 |
| 298.15 |
0.3528 |
26.91 |
| 298.15 |
0.4802 |
24.70 |
| 298.15 |
0.5725 |
23.27 |
| 298.15 |
0.6692 |
21.74 |
| 298.15 |
0.7626 |
20.30 |
| 298.15 |
0.8653 |
18.91 |
| 303.15 |
0.1567 |
37.35 |
| 303.15 |
0.2670 |
34.99 |
| 303.15 |
0.3528 |
33.13 |
| 303.15 |
0.4802 |
30.49 |
| 303.15 |
0.5725 |
28.80 |
| 303.15 |
0.6692 |
26.95 |
| 303.15 |
0.7626 |
25.22 |
| 303.15 |
0.8653 |
23.55 |
| 313.15 |
0.1567 |
54.92 |
| 313.15 |
0.2670 |
51.64 |
| 313.15 |
0.3528 |
49.05 |
| 313.15 |
0.4802 |
45.38 |
| 313.15 |
0.5725 |
43.01 |
| 313.15 |
0.6692 |
40.39 |
| 313.15 |
0.7626 |
37.98 |
| 313.15 |
0.8653 |
35.62 |
| 323.15 |
0.1567 |
78.53 |
| 323.15 |
0.2670 |
74.09 |
| 323.15 |
0.3528 |
70.56 |
| 323.15 |
0.4802 |
65.60 |
| 323.15 |
0.5725 |
62.37 |
| 323.15 |
0.6692 |
58.77 |
| 323.15 |
0.7626 |
55.52 |
| 323.15 |
0.8653 |
52.25 |
| 333.15 |
0.1567 |
109.50 |
| 333.15 |
0.2670 |
103.64 |
| 333.15 |
0.3528 |
98.93 |
| 333.15 |
0.4802 |
92.43 |
| 333.15 |
0.5725 |
88.09 |
| 333.15 |
0.6692 |
83.27 |
| 333.15 |
0.7626 |
78.99 |
| 333.15 |
0.8653 |
74.58 |
| 343.15 |
0.1567 |
149.28 |
| 343.15 |
0.2670 |
141.73 |
| 343.15 |
0.3528 |
135.55 |
| 343.15 |
0.4802 |
127.26 |
| 343.15 |
0.5725 |
121.49 |
| 343.15 |
0.6692 |
115.19 |
| 343.15 |
0.7626 |
109.51 |
| 343.15 |
0.8653 |
103.90 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 1-Hexyne (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 263.15 |
0.1567 |
5.59 |
| 263.15 |
0.2670 |
5.14 |
| 263.15 |
0.3528 |
4.78 |
| 263.15 |
0.4802 |
4.31 |
| 263.15 |
0.5725 |
3.96 |
| 263.15 |
0.6692 |
3.64 |
| 263.15 |
0.7626 |
3.33 |
| 263.15 |
0.8653 |
3.04 |
| 273.15 |
0.1567 |
9.57 |
| 273.15 |
0.2670 |
8.85 |
| 273.15 |
0.3528 |
8.27 |
| 273.15 |
0.4802 |
7.50 |
| 273.15 |
0.5725 |
6.95 |
| 273.15 |
0.6692 |
6.43 |
| 273.15 |
0.7626 |
5.92 |
| 273.15 |
0.8653 |
5.44 |
| 283.15 |
0.1567 |
15.66 |
| 283.15 |
0.2670 |
14.55 |
| 283.15 |
0.3528 |
13.67 |
| 283.15 |
0.4802 |
12.45 |
| 283.15 |
0.5725 |
11.63 |
| 283.15 |
0.6692 |
10.80 |
| 283.15 |
0.7626 |
10.00 |
| 283.15 |
0.8653 |
9.25 |
| 293.15 |
0.1567 |
24.62 |
| 293.15 |
0.2670 |
22.97 |
| 293.15 |
0.3528 |
21.67 |
| 293.15 |
0.4802 |
19.84 |
| 293.15 |
0.5725 |
18.65 |
| 293.15 |
0.6692 |
17.39 |
| 293.15 |
0.7626 |
16.19 |
| 293.15 |
0.8653 |
15.05 |
| 298.15 |
0.1567 |
30.45 |
| 298.15 |
0.2670 |
28.47 |
| 298.15 |
0.3528 |
26.91 |
| 298.15 |
0.4802 |
24.70 |
| 298.15 |
0.5725 |
23.27 |
| 298.15 |
0.6692 |
21.74 |
| 298.15 |
0.7626 |
20.30 |
| 298.15 |
0.8653 |
18.91 |
| 303.15 |
0.1567 |
37.35 |
| 303.15 |
0.2670 |
34.99 |
| 303.15 |
0.3528 |
33.13 |
| 303.15 |
0.4802 |
30.49 |
| 303.15 |
0.5725 |
28.80 |
| 303.15 |
0.6692 |
26.95 |
| 303.15 |
0.7626 |
25.22 |
| 303.15 |
0.8653 |
23.55 |
| 313.15 |
0.1567 |
54.92 |
| 313.15 |
0.2670 |
51.64 |
| 313.15 |
0.3528 |
49.05 |
| 313.15 |
0.4802 |
45.38 |
| 313.15 |
0.5725 |
43.01 |
| 313.15 |
0.6692 |
40.39 |
| 313.15 |
0.7626 |
37.98 |
| 313.15 |
0.8653 |
35.62 |
| 323.15 |
0.1567 |
78.53 |
| 323.15 |
0.2670 |
74.09 |
| 323.15 |
0.3528 |
70.56 |
| 323.15 |
0.4802 |
65.60 |
| 323.15 |
0.5725 |
62.37 |
| 323.15 |
0.6692 |
58.77 |
| 323.15 |
0.7626 |
55.52 |
| 323.15 |
0.8653 |
52.25 |
| 333.15 |
0.1567 |
109.50 |
| 333.15 |
0.2670 |
103.64 |
| 333.15 |
0.3528 |
98.93 |
| 333.15 |
0.4802 |
92.43 |
| 333.15 |
0.5725 |
88.09 |
| 333.15 |
0.6692 |
83.27 |
| 333.15 |
0.7626 |
78.99 |
| 333.15 |
0.8653 |
74.58 |
| 343.15 |
0.1567 |
149.28 |
| 343.15 |
0.2670 |
141.73 |
| 343.15 |
0.3528 |
135.55 |
| 343.15 |
0.4802 |
127.26 |
| 343.15 |
0.5725 |
121.49 |
| 343.15 |
0.6692 |
115.19 |
| 343.15 |
0.7626 |
109.51 |
| 343.15 |
0.8653 |
103.90 |
Sources