Datasets
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Tboil - Boiling temperature at pressure P, K (2)
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Vapor or sublimation pressure, kPa (2)
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
94.6 (Liquid)
Mole fraction of Tetrahydrofuran (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
369.35 |
0.1411 |
362.05 |
0.3301 |
354.05 |
0.4508 |
349.95 |
0.6002 |
345.35 |
0.7831 |
340.95 |
0.9002 |
338.75 |
1.0000 |
337.15 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
94.6 (Liquid)
Mole fraction of Tetrahydrofuran (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
369.35 |
0.1411 |
362.05 |
0.3301 |
354.05 |
0.4508 |
349.95 |
0.6002 |
345.35 |
0.7831 |
340.95 |
0.9002 |
338.75 |
1.0000 |
337.15 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of Heptane (1) - Liquid |
Vapor or sublimation pressure, kPa - Gas |
303.20 |
0.0000 |
26.60 |
303.20 |
0.1090 |
25.50 |
303.20 |
0.1240 |
25.20 |
303.20 |
0.2410 |
24.00 |
303.20 |
0.3220 |
22.80 |
303.20 |
0.3550 |
22.40 |
303.20 |
0.4640 |
20.70 |
303.20 |
0.4720 |
20.70 |
303.20 |
0.5640 |
19.00 |
303.20 |
0.5980 |
18.40 |
303.20 |
0.6680 |
17.00 |
303.20 |
0.6780 |
16.80 |
303.20 |
0.7750 |
14.60 |
303.20 |
0.7800 |
14.30 |
303.10 |
0.8520 |
12.40 |
303.10 |
0.8640 |
12.30 |
303.10 |
0.9210 |
10.60 |
303.20 |
0.9340 |
9.90 |
303.20 |
0.9830 |
8.60 |
303.20 |
1.0000 |
7.70 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of Heptane (1) - Liquid |
Vapor or sublimation pressure, kPa - Gas |
303.20 |
0.0000 |
26.60 |
303.20 |
0.1090 |
25.50 |
303.20 |
0.1240 |
25.20 |
303.20 |
0.2410 |
24.00 |
303.20 |
0.3220 |
22.80 |
303.20 |
0.3550 |
22.40 |
303.20 |
0.4640 |
20.70 |
303.20 |
0.4720 |
20.70 |
303.20 |
0.5640 |
19.00 |
303.20 |
0.5980 |
18.40 |
303.20 |
0.6680 |
17.00 |
303.20 |
0.6780 |
16.80 |
303.20 |
0.7750 |
14.60 |
303.20 |
0.7800 |
14.30 |
303.10 |
0.8520 |
12.40 |
303.10 |
0.8640 |
12.30 |
303.10 |
0.9210 |
10.60 |
303.20 |
0.9340 |
9.90 |
303.20 |
0.9830 |
8.60 |
303.20 |
1.0000 |
7.70 |
Sources