Mixture of Ethane + Ethanol, 2,2'-oxybis-
Datasets
-
Mole fraction (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
Mole fraction of Ethane (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethane (1) - Liquid |
| 298.15 |
30.00 |
0.0005 |
| 298.15 |
116.00 |
0.0020 |
| 298.15 |
312.00 |
0.0053 |
| 298.15 |
544.00 |
0.0091 |
| 298.15 |
890.00 |
0.0151 |
| 298.15 |
1740.00 |
0.0270 |
| 298.15 |
2630.00 |
0.0389 |
| 298.15 |
3750.00 |
0.0510 |
| 298.15 |
4220.00 |
0.0551 |
| 298.15 |
5460.00 |
0.0561 |
| 298.15 |
7720.00 |
0.0572 |
| 298.15 |
9680.00 |
0.0597 |
| 298.15 |
11840.00 |
0.0602 |
| 298.15 |
14700.00 |
0.0609 |
| 298.15 |
17460.00 |
0.0616 |
| 298.15 |
20450.00 |
0.0611 |
| 323.15 |
25.00 |
0.0003 |
| 323.15 |
125.00 |
0.0016 |
| 323.15 |
242.00 |
0.0031 |
| 323.15 |
636.00 |
0.0082 |
| 323.15 |
1620.00 |
0.0204 |
| 323.15 |
3120.00 |
0.0351 |
| 323.15 |
5540.00 |
0.0539 |
| 323.15 |
6650.00 |
0.0564 |
| 323.15 |
9150.00 |
0.0604 |
| 323.15 |
11930.00 |
0.0637 |
| 323.15 |
14590.00 |
0.0655 |
| 323.15 |
17050.00 |
0.0676 |
| 323.15 |
19580.00 |
0.0698 |
| 348.15 |
39.00 |
0.0004 |
| 348.15 |
126.00 |
0.0014 |
| 348.15 |
167.00 |
0.0018 |
| 348.15 |
263.00 |
0.0028 |
| 348.15 |
672.00 |
0.0071 |
| 348.15 |
1640.00 |
0.0170 |
| 348.15 |
2790.00 |
0.0272 |
| 348.15 |
3450.00 |
0.0327 |
| 348.15 |
4490.00 |
0.0411 |
| 348.15 |
6380.00 |
0.0518 |
| 348.15 |
8160.00 |
0.0580 |
| 348.15 |
10580.00 |
0.0646 |
| 348.15 |
12680.00 |
0.0674 |
| 348.15 |
14780.00 |
0.0706 |
| 348.15 |
17370.00 |
0.0732 |
| 348.15 |
20040.00 |
0.0769 |
| 373.15 |
43.00 |
0.0004 |
| 373.15 |
116.00 |
0.0011 |
| 373.15 |
220.00 |
0.0021 |
| 373.15 |
256.00 |
0.0024 |
| 373.15 |
338.00 |
0.0031 |
| 373.15 |
643.00 |
0.0059 |
| 373.15 |
2170.00 |
0.0190 |
| 373.15 |
3790.00 |
0.0326 |
| 373.15 |
4130.00 |
0.0344 |
| 373.15 |
6500.00 |
0.0496 |
| 373.15 |
8930.00 |
0.0591 |
| 373.15 |
11650.00 |
0.0683 |
| 373.15 |
14300.00 |
0.0741 |
| 373.15 |
16980.00 |
0.0784 |
| 373.15 |
19480.00 |
0.0825 |
| 398.15 |
29.00 |
0.0003 |
| 398.15 |
125.00 |
0.0011 |
| 398.15 |
284.00 |
0.0025 |
| 398.15 |
814.00 |
0.0068 |
| 398.15 |
1380.00 |
0.0117 |
| 398.15 |
2340.00 |
0.0190 |
| 398.15 |
3870.00 |
0.0302 |
| 398.15 |
4450.00 |
0.0346 |
| 398.15 |
6570.00 |
0.0468 |
| 398.15 |
8980.00 |
0.0580 |
| 398.15 |
11400.00 |
0.0689 |
| 398.15 |
13970.00 |
0.0770 |
| 398.15 |
16350.00 |
0.0844 |
| 398.15 |
18890.00 |
0.0877 |
Mole fraction of Ethane (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethane (1) - Liquid |
| 298.15 |
30.00 |
0.0005 |
| 298.15 |
116.00 |
0.0020 |
| 298.15 |
312.00 |
0.0053 |
| 298.15 |
544.00 |
0.0091 |
| 298.15 |
890.00 |
0.0151 |
| 298.15 |
1740.00 |
0.0270 |
| 298.15 |
2630.00 |
0.0389 |
| 298.15 |
3750.00 |
0.0510 |
| 298.15 |
4220.00 |
0.0551 |
| 298.15 |
5460.00 |
0.0561 |
| 298.15 |
7720.00 |
0.0572 |
| 298.15 |
9680.00 |
0.0597 |
| 298.15 |
11840.00 |
0.0602 |
| 298.15 |
14700.00 |
0.0609 |
| 298.15 |
17460.00 |
0.0616 |
| 298.15 |
20450.00 |
0.0611 |
| 323.15 |
25.00 |
0.0003 |
| 323.15 |
125.00 |
0.0016 |
| 323.15 |
242.00 |
0.0031 |
| 323.15 |
636.00 |
0.0082 |
| 323.15 |
1620.00 |
0.0204 |
| 323.15 |
3120.00 |
0.0351 |
| 323.15 |
5540.00 |
0.0539 |
| 323.15 |
6650.00 |
0.0564 |
| 323.15 |
9150.00 |
0.0604 |
| 323.15 |
11930.00 |
0.0637 |
| 323.15 |
14590.00 |
0.0655 |
| 323.15 |
17050.00 |
0.0676 |
| 323.15 |
19580.00 |
0.0698 |
| 348.15 |
39.00 |
0.0004 |
| 348.15 |
126.00 |
0.0014 |
| 348.15 |
167.00 |
0.0018 |
| 348.15 |
263.00 |
0.0028 |
| 348.15 |
672.00 |
0.0071 |
| 348.15 |
1640.00 |
0.0170 |
| 348.15 |
2790.00 |
0.0272 |
| 348.15 |
3450.00 |
0.0327 |
| 348.15 |
4490.00 |
0.0411 |
| 348.15 |
6380.00 |
0.0518 |
| 348.15 |
8160.00 |
0.0580 |
| 348.15 |
10580.00 |
0.0646 |
| 348.15 |
12680.00 |
0.0674 |
| 348.15 |
14780.00 |
0.0706 |
| 348.15 |
17370.00 |
0.0732 |
| 348.15 |
20040.00 |
0.0769 |
| 373.15 |
43.00 |
0.0004 |
| 373.15 |
116.00 |
0.0011 |
| 373.15 |
220.00 |
0.0021 |
| 373.15 |
256.00 |
0.0024 |
| 373.15 |
338.00 |
0.0031 |
| 373.15 |
643.00 |
0.0059 |
| 373.15 |
2170.00 |
0.0190 |
| 373.15 |
3790.00 |
0.0326 |
| 373.15 |
4130.00 |
0.0344 |
| 373.15 |
6500.00 |
0.0496 |
| 373.15 |
8930.00 |
0.0591 |
| 373.15 |
11650.00 |
0.0683 |
| 373.15 |
14300.00 |
0.0741 |
| 373.15 |
16980.00 |
0.0784 |
| 373.15 |
19480.00 |
0.0825 |
| 398.15 |
29.00 |
0.0003 |
| 398.15 |
125.00 |
0.0011 |
| 398.15 |
284.00 |
0.0025 |
| 398.15 |
814.00 |
0.0068 |
| 398.15 |
1380.00 |
0.0117 |
| 398.15 |
2340.00 |
0.0190 |
| 398.15 |
3870.00 |
0.0302 |
| 398.15 |
4450.00 |
0.0346 |
| 398.15 |
6570.00 |
0.0468 |
| 398.15 |
8980.00 |
0.0580 |
| 398.15 |
11400.00 |
0.0689 |
| 398.15 |
13970.00 |
0.0770 |
| 398.15 |
16350.00 |
0.0844 |
| 398.15 |
18890.00 |
0.0877 |
Vapor or sublimation pressure, kPa
[ref]
| Temperature, K - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
| 298.15 |
4220.00 |
Vapor or sublimation pressure, kPa
[ref]
| Temperature, K - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
| 298.15 |
4220.00 |
Sources
