Mixture of 1,3-Dioxolane + 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 |
| 274.94 |
0.1408 |
3.59 |
| 284.89 |
0.1408 |
6.27 |
| 294.80 |
0.1408 |
10.60 |
| 304.69 |
0.1408 |
17.02 |
| 314.72 |
0.1408 |
26.57 |
| 324.83 |
0.1408 |
40.35 |
| 334.85 |
0.1408 |
59.19 |
| 344.80 |
0.1408 |
84.27 |
| 351.77 |
0.1408 |
106.34 |
| 274.94 |
0.3357 |
3.32 |
| 284.87 |
0.3357 |
5.80 |
| 294.77 |
0.3357 |
9.92 |
| 304.66 |
0.3357 |
15.77 |
| 314.69 |
0.3357 |
24.76 |
| 324.83 |
0.3357 |
37.49 |
| 334.80 |
0.3357 |
55.00 |
| 344.80 |
0.3357 |
78.50 |
| 354.72 |
0.3357 |
109.41 |
| 275.02 |
0.5042 |
3.16 |
| 284.94 |
0.5042 |
5.53 |
| 294.85 |
0.5042 |
9.25 |
| 304.76 |
0.5042 |
15.06 |
| 314.79 |
0.5042 |
23.54 |
| 324.90 |
0.5042 |
35.81 |
| 334.85 |
0.5042 |
52.52 |
| 344.80 |
0.5042 |
74.86 |
| 354.74 |
0.5042 |
104.54 |
| 274.94 |
0.6326 |
3.06 |
| 284.87 |
0.6326 |
5.35 |
| 294.80 |
0.6326 |
8.94 |
| 304.74 |
0.6326 |
14.56 |
| 314.69 |
0.6326 |
22.72 |
| 324.85 |
0.6326 |
34.56 |
| 334.85 |
0.6326 |
50.70 |
| 344.78 |
0.6326 |
72.47 |
| 354.76 |
0.6326 |
101.09 |
| 274.92 |
0.8927 |
2.99 |
| 284.82 |
0.8927 |
5.21 |
| 294.77 |
0.8927 |
8.67 |
| 304.71 |
0.8927 |
14.20 |
| 314.67 |
0.8927 |
21.94 |
| 324.81 |
0.8927 |
33.33 |
| 334.83 |
0.8927 |
48.87 |
| 344.80 |
0.8927 |
69.71 |
| 354.72 |
0.8927 |
96.88 |
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 |
| 274.94 |
0.1408 |
3.59 |
| 284.89 |
0.1408 |
6.27 |
| 294.80 |
0.1408 |
10.60 |
| 304.69 |
0.1408 |
17.02 |
| 314.72 |
0.1408 |
26.57 |
| 324.83 |
0.1408 |
40.35 |
| 334.85 |
0.1408 |
59.19 |
| 344.80 |
0.1408 |
84.27 |
| 351.77 |
0.1408 |
106.34 |
| 274.94 |
0.3357 |
3.32 |
| 284.87 |
0.3357 |
5.80 |
| 294.77 |
0.3357 |
9.92 |
| 304.66 |
0.3357 |
15.77 |
| 314.69 |
0.3357 |
24.76 |
| 324.83 |
0.3357 |
37.49 |
| 334.80 |
0.3357 |
55.00 |
| 344.80 |
0.3357 |
78.50 |
| 354.72 |
0.3357 |
109.41 |
| 275.02 |
0.5042 |
3.16 |
| 284.94 |
0.5042 |
5.53 |
| 294.85 |
0.5042 |
9.25 |
| 304.76 |
0.5042 |
15.06 |
| 314.79 |
0.5042 |
23.54 |
| 324.90 |
0.5042 |
35.81 |
| 334.85 |
0.5042 |
52.52 |
| 344.80 |
0.5042 |
74.86 |
| 354.74 |
0.5042 |
104.54 |
| 274.94 |
0.6326 |
3.06 |
| 284.87 |
0.6326 |
5.35 |
| 294.80 |
0.6326 |
8.94 |
| 304.74 |
0.6326 |
14.56 |
| 314.69 |
0.6326 |
22.72 |
| 324.85 |
0.6326 |
34.56 |
| 334.85 |
0.6326 |
50.70 |
| 344.78 |
0.6326 |
72.47 |
| 354.76 |
0.6326 |
101.09 |
| 274.92 |
0.8927 |
2.99 |
| 284.82 |
0.8927 |
5.21 |
| 294.77 |
0.8927 |
8.67 |
| 304.71 |
0.8927 |
14.20 |
| 314.67 |
0.8927 |
21.94 |
| 324.81 |
0.8927 |
33.33 |
| 334.83 |
0.8927 |
48.87 |
| 344.80 |
0.8927 |
69.71 |
| 354.72 |
0.8927 |
96.88 |
Sources