Mixture of Propane, 2-methoxy-2-methyl- + 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 |
| 274.83 |
0.3711 |
8.18 |
| 274.85 |
0.6712 |
5.83 |
| 274.86 |
0.6712 |
5.84 |
| 274.86 |
0.8694 |
4.34 |
| 274.86 |
0.8694 |
4.34 |
| 274.88 |
0.5324 |
6.87 |
| 274.88 |
0.5324 |
6.86 |
| 275.00 |
0.1662 |
10.01 |
| 284.78 |
0.3711 |
13.43 |
| 284.81 |
0.3711 |
13.43 |
| 284.81 |
0.8694 |
7.35 |
| 284.81 |
0.8694 |
7.35 |
| 284.83 |
0.5324 |
11.38 |
| 284.83 |
0.6712 |
9.75 |
| 284.84 |
0.5324 |
11.38 |
| 284.84 |
0.6712 |
9.76 |
| 284.96 |
0.1662 |
16.23 |
| 294.75 |
0.3711 |
21.18 |
| 294.77 |
0.8694 |
11.97 |
| 294.78 |
0.8694 |
11.97 |
| 294.79 |
0.5324 |
18.14 |
| 294.80 |
0.5324 |
18.13 |
| 294.81 |
0.6712 |
15.64 |
| 294.82 |
0.6712 |
15.64 |
| 294.91 |
0.1662 |
25.31 |
| 304.73 |
0.3711 |
32.51 |
| 304.73 |
0.3711 |
32.49 |
| 304.74 |
0.8694 |
18.78 |
| 304.74 |
0.8694 |
18.79 |
| 304.76 |
0.5324 |
27.89 |
| 304.77 |
0.5324 |
27.90 |
| 304.79 |
0.6712 |
24.23 |
| 304.88 |
0.1662 |
38.20 |
| 314.71 |
0.3711 |
48.02 |
| 314.73 |
0.6712 |
36.34 |
| 314.73 |
0.8694 |
28.54 |
| 314.73 |
0.8694 |
28.55 |
| 314.74 |
0.5324 |
41.58 |
| 314.74 |
0.6712 |
36.33 |
| 314.74 |
0.5324 |
41.57 |
| 314.86 |
0.1662 |
55.94 |
| 324.69 |
0.3711 |
68.93 |
| 324.72 |
0.3711 |
69.06 |
| 324.74 |
0.5324 |
60.20 |
| 324.74 |
0.5324 |
60.21 |
| 324.82 |
0.6712 |
53.19 |
| 324.82 |
0.8694 |
42.30 |
| 324.83 |
0.6712 |
53.18 |
| 324.83 |
0.8694 |
42.31 |
| 324.84 |
0.3711 |
69.20 |
| 324.97 |
0.1662 |
80.05 |
| 334.73 |
0.5324 |
84.97 |
| 334.74 |
0.5324 |
84.98 |
| 334.79 |
0.8694 |
60.64 |
| 334.79 |
0.8694 |
60.64 |
| 334.79 |
0.8694 |
60.65 |
| 334.80 |
0.8694 |
60.65 |
| 334.81 |
0.6712 |
75.41 |
| 334.82 |
0.3711 |
96.80 |
| 334.93 |
0.1662 |
111.23 |
| 344.73 |
0.5324 |
117.26 |
| 344.74 |
0.5324 |
117.29 |
| 344.78 |
0.8694 |
84.89 |
| 344.79 |
0.6712 |
104.59 |
| 344.79 |
0.8694 |
84.87 |
| 344.79 |
0.8694 |
84.72 |
| 344.80 |
0.3711 |
132.57 |
| 344.80 |
0.6712 |
104.53 |
| 344.80 |
0.8694 |
84.83 |
| 344.80 |
0.3711 |
132.60 |
| 344.90 |
0.1662 |
151.04 |
| 354.73 |
0.5324 |
157.69 |
| 354.76 |
0.6712 |
141.99 |
| 354.78 |
0.8694 |
116.31 |
| 354.79 |
0.8694 |
116.34 |
| 354.79 |
0.8694 |
116.33 |
| 354.89 |
0.1662 |
201.17 |
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 |
| 274.83 |
0.3711 |
8.18 |
| 274.85 |
0.6712 |
5.83 |
| 274.86 |
0.6712 |
5.84 |
| 274.86 |
0.8694 |
4.34 |
| 274.86 |
0.8694 |
4.34 |
| 274.88 |
0.5324 |
6.87 |
| 274.88 |
0.5324 |
6.86 |
| 275.00 |
0.1662 |
10.01 |
| 284.78 |
0.3711 |
13.43 |
| 284.81 |
0.3711 |
13.43 |
| 284.81 |
0.8694 |
7.35 |
| 284.81 |
0.8694 |
7.35 |
| 284.83 |
0.5324 |
11.38 |
| 284.83 |
0.6712 |
9.75 |
| 284.84 |
0.5324 |
11.38 |
| 284.84 |
0.6712 |
9.76 |
| 284.96 |
0.1662 |
16.23 |
| 294.75 |
0.3711 |
21.18 |
| 294.77 |
0.8694 |
11.97 |
| 294.78 |
0.8694 |
11.97 |
| 294.79 |
0.5324 |
18.14 |
| 294.80 |
0.5324 |
18.13 |
| 294.81 |
0.6712 |
15.64 |
| 294.82 |
0.6712 |
15.64 |
| 294.91 |
0.1662 |
25.31 |
| 304.73 |
0.3711 |
32.51 |
| 304.73 |
0.3711 |
32.49 |
| 304.74 |
0.8694 |
18.78 |
| 304.74 |
0.8694 |
18.79 |
| 304.76 |
0.5324 |
27.89 |
| 304.77 |
0.5324 |
27.90 |
| 304.79 |
0.6712 |
24.23 |
| 304.88 |
0.1662 |
38.20 |
| 314.71 |
0.3711 |
48.02 |
| 314.73 |
0.6712 |
36.34 |
| 314.73 |
0.8694 |
28.54 |
| 314.73 |
0.8694 |
28.55 |
| 314.74 |
0.5324 |
41.58 |
| 314.74 |
0.6712 |
36.33 |
| 314.74 |
0.5324 |
41.57 |
| 314.86 |
0.1662 |
55.94 |
| 324.69 |
0.3711 |
68.93 |
| 324.72 |
0.3711 |
69.06 |
| 324.74 |
0.5324 |
60.20 |
| 324.74 |
0.5324 |
60.21 |
| 324.82 |
0.6712 |
53.19 |
| 324.82 |
0.8694 |
42.30 |
| 324.83 |
0.6712 |
53.18 |
| 324.83 |
0.8694 |
42.31 |
| 324.84 |
0.3711 |
69.20 |
| 324.97 |
0.1662 |
80.05 |
| 334.73 |
0.5324 |
84.97 |
| 334.74 |
0.5324 |
84.98 |
| 334.79 |
0.8694 |
60.64 |
| 334.79 |
0.8694 |
60.64 |
| 334.79 |
0.8694 |
60.65 |
| 334.80 |
0.8694 |
60.65 |
| 334.81 |
0.6712 |
75.41 |
| 334.82 |
0.3711 |
96.80 |
| 334.93 |
0.1662 |
111.23 |
| 344.73 |
0.5324 |
117.26 |
| 344.74 |
0.5324 |
117.29 |
| 344.78 |
0.8694 |
84.89 |
| 344.79 |
0.6712 |
104.59 |
| 344.79 |
0.8694 |
84.87 |
| 344.79 |
0.8694 |
84.72 |
| 344.80 |
0.3711 |
132.57 |
| 344.80 |
0.6712 |
104.53 |
| 344.80 |
0.8694 |
84.83 |
| 344.80 |
0.3711 |
132.60 |
| 344.90 |
0.1662 |
151.04 |
| 354.73 |
0.5324 |
157.69 |
| 354.76 |
0.6712 |
141.99 |
| 354.78 |
0.8694 |
116.31 |
| 354.79 |
0.8694 |
116.34 |
| 354.79 |
0.8694 |
116.33 |
| 354.89 |
0.1662 |
201.17 |
Sources