Mixture of Carbon dioxide + Ethanol + Dimethyl ether
Datasets
-
Temperature, K x Pressure, kPa x Mole fraction (2)
Temperature, K x Pressure, kPa x Mole fraction
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Dimethyl ether (3) - Liquid |
Mole fraction of Dimethyl ether (3) - Gas |
Mole fraction of Carbon dioxide (1) - Gas |
298.15 |
420.00 |
0.0000 |
0.5601 |
0.9883 |
0.0000 |
298.15 |
1120.00 |
0.1153 |
0.4991 |
0.3542 |
0.6411 |
298.15 |
1760.00 |
0.2242 |
0.4387 |
0.2120 |
0.7846 |
298.15 |
2170.00 |
0.2915 |
0.3974 |
0.1701 |
0.8269 |
298.15 |
2550.00 |
0.3521 |
0.3698 |
0.1381 |
0.8591 |
298.15 |
3180.00 |
0.4538 |
0.3132 |
0.1068 |
0.8904 |
308.15 |
530.00 |
0.0000 |
0.5319 |
0.9846 |
0.0000 |
308.15 |
1070.00 |
0.0722 |
0.4921 |
0.4811 |
0.5100 |
308.15 |
1620.00 |
0.1490 |
0.4558 |
0.3050 |
0.6901 |
308.15 |
2170.00 |
0.2235 |
0.4162 |
0.2239 |
0.7712 |
308.15 |
2650.00 |
0.2876 |
0.3832 |
0.1761 |
0.8202 |
308.15 |
3110.00 |
0.3509 |
0.3504 |
0.1452 |
0.8517 |
308.15 |
3570.00 |
0.4103 |
0.3181 |
0.1256 |
0.8711 |
318.15 |
610.00 |
0.0000 |
0.4715 |
0.9863 |
0.0000 |
318.15 |
1150.00 |
0.0551 |
0.4435 |
0.5243 |
0.4675 |
318.15 |
1580.00 |
0.1032 |
0.4231 |
0.3744 |
0.6197 |
318.15 |
2140.00 |
0.1638 |
0.3965 |
0.2719 |
0.7226 |
318.15 |
2630.00 |
0.2168 |
0.3700 |
0.2198 |
0.7755 |
318.15 |
3130.00 |
0.2708 |
0.3473 |
0.1793 |
0.8168 |
318.15 |
3800.00 |
0.3486 |
0.3133 |
0.1441 |
0.8521 |
Temperature, K x Pressure, kPa x Mole fraction
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Dimethyl ether (3) - Liquid |
Mole fraction of Dimethyl ether (3) - Gas |
Mole fraction of Carbon dioxide (1) - Gas |
298.15 |
420.00 |
0.0000 |
0.5601 |
0.9883 |
0.0000 |
298.15 |
1120.00 |
0.1153 |
0.4991 |
0.3542 |
0.6411 |
298.15 |
1760.00 |
0.2242 |
0.4387 |
0.2120 |
0.7846 |
298.15 |
2170.00 |
0.2915 |
0.3974 |
0.1701 |
0.8269 |
298.15 |
2550.00 |
0.3521 |
0.3698 |
0.1381 |
0.8591 |
298.15 |
3180.00 |
0.4538 |
0.3132 |
0.1068 |
0.8904 |
308.15 |
530.00 |
0.0000 |
0.5319 |
0.9846 |
0.0000 |
308.15 |
1070.00 |
0.0722 |
0.4921 |
0.4811 |
0.5100 |
308.15 |
1620.00 |
0.1490 |
0.4558 |
0.3050 |
0.6901 |
308.15 |
2170.00 |
0.2235 |
0.4162 |
0.2239 |
0.7712 |
308.15 |
2650.00 |
0.2876 |
0.3832 |
0.1761 |
0.8202 |
308.15 |
3110.00 |
0.3509 |
0.3504 |
0.1452 |
0.8517 |
308.15 |
3570.00 |
0.4103 |
0.3181 |
0.1256 |
0.8711 |
318.15 |
610.00 |
0.0000 |
0.4715 |
0.9863 |
0.0000 |
318.15 |
1150.00 |
0.0551 |
0.4435 |
0.5243 |
0.4675 |
318.15 |
1580.00 |
0.1032 |
0.4231 |
0.3744 |
0.6197 |
318.15 |
2140.00 |
0.1638 |
0.3965 |
0.2719 |
0.7226 |
318.15 |
2630.00 |
0.2168 |
0.3700 |
0.2198 |
0.7755 |
318.15 |
3130.00 |
0.2708 |
0.3473 |
0.1793 |
0.8168 |
318.15 |
3800.00 |
0.3486 |
0.3133 |
0.1441 |
0.8521 |
Sources