Mixture of Tetrahydropyran + Ethane, 1,2-dichloro-
Datasets
-
Pvap - Vapor or sublimation pressure, kPa (2)
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
273.37 |
0.1496 |
2.60 |
285.32 |
0.1496 |
4.85 |
295.24 |
0.1496 |
7.93 |
305.17 |
0.1496 |
12.36 |
315.17 |
0.1496 |
19.12 |
325.27 |
0.1496 |
28.91 |
335.21 |
0.1496 |
42.33 |
345.25 |
0.1496 |
60.75 |
355.36 |
0.1496 |
85.43 |
275.41 |
0.3610 |
2.62 |
285.35 |
0.3610 |
4.56 |
295.27 |
0.3610 |
7.58 |
305.63 |
0.3610 |
12.27 |
315.71 |
0.3610 |
19.28 |
325.86 |
0.3610 |
29.19 |
335.65 |
0.3610 |
42.42 |
345.54 |
0.3610 |
60.30 |
355.43 |
0.3610 |
83.06 |
275.46 |
0.4993 |
2.68 |
285.40 |
0.4993 |
4.67 |
295.32 |
0.4993 |
7.77 |
305.17 |
0.4993 |
12.46 |
315.26 |
0.4993 |
19.36 |
325.39 |
0.4993 |
29.38 |
335.37 |
0.4993 |
43.10 |
345.07 |
0.4993 |
61.22 |
355.01 |
0.4993 |
84.89 |
275.10 |
0.6479 |
2.75 |
285.05 |
0.6479 |
4.79 |
294.97 |
0.6479 |
7.98 |
304.86 |
0.6479 |
12.73 |
314.91 |
0.6479 |
19.87 |
325.04 |
0.6479 |
30.20 |
335.03 |
0.6479 |
44.23 |
344.98 |
0.6479 |
63.28 |
354.70 |
0.6479 |
87.25 |
274.97 |
0.8961 |
2.95 |
284.89 |
0.8961 |
5.14 |
294.80 |
0.8961 |
8.53 |
304.76 |
0.8961 |
13.76 |
314.74 |
0.8961 |
21.34 |
324.88 |
0.8961 |
32.51 |
334.87 |
0.8961 |
47.44 |
344.85 |
0.8961 |
67.37 |
354.79 |
0.8961 |
93.83 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
273.37 |
0.1496 |
2.60 |
285.32 |
0.1496 |
4.85 |
295.24 |
0.1496 |
7.93 |
305.17 |
0.1496 |
12.36 |
315.17 |
0.1496 |
19.12 |
325.27 |
0.1496 |
28.91 |
335.21 |
0.1496 |
42.33 |
345.25 |
0.1496 |
60.75 |
355.36 |
0.1496 |
85.43 |
275.41 |
0.3610 |
2.62 |
285.35 |
0.3610 |
4.56 |
295.27 |
0.3610 |
7.58 |
305.63 |
0.3610 |
12.27 |
315.71 |
0.3610 |
19.28 |
325.86 |
0.3610 |
29.19 |
335.65 |
0.3610 |
42.42 |
345.54 |
0.3610 |
60.30 |
355.43 |
0.3610 |
83.06 |
275.46 |
0.4993 |
2.68 |
285.40 |
0.4993 |
4.67 |
295.32 |
0.4993 |
7.77 |
305.17 |
0.4993 |
12.46 |
315.26 |
0.4993 |
19.36 |
325.39 |
0.4993 |
29.38 |
335.37 |
0.4993 |
43.10 |
345.07 |
0.4993 |
61.22 |
355.01 |
0.4993 |
84.89 |
275.10 |
0.6479 |
2.75 |
285.05 |
0.6479 |
4.79 |
294.97 |
0.6479 |
7.98 |
304.86 |
0.6479 |
12.73 |
314.91 |
0.6479 |
19.87 |
325.04 |
0.6479 |
30.20 |
335.03 |
0.6479 |
44.23 |
344.98 |
0.6479 |
63.28 |
354.70 |
0.6479 |
87.25 |
274.97 |
0.8961 |
2.95 |
284.89 |
0.8961 |
5.14 |
294.80 |
0.8961 |
8.53 |
304.76 |
0.8961 |
13.76 |
314.74 |
0.8961 |
21.34 |
324.88 |
0.8961 |
32.51 |
334.87 |
0.8961 |
47.44 |
344.85 |
0.8961 |
67.37 |
354.79 |
0.8961 |
93.83 |
Sources