Mixture of Carbon dioxide + Ethylene glycol monoisobutyl ether
Datasets
-
Mole fraction (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
0.0500 |
333.15 |
0.9920 |
0.0510 |
313.15 |
0.9980 |
0.0630 |
323.15 |
0.9950 |
0.1360 |
313.15 |
0.9980 |
0.1510 |
323.15 |
0.9970 |
0.1530 |
333.15 |
0.9960 |
0.2050 |
333.15 |
0.9970 |
0.2120 |
323.15 |
0.9980 |
0.2230 |
313.15 |
0.9980 |
0.2750 |
333.15 |
0.9980 |
0.3090 |
323.15 |
0.9980 |
0.3420 |
313.15 |
0.9990 |
0.3730 |
333.15 |
0.9980 |
0.3930 |
323.15 |
0.9980 |
0.4190 |
313.15 |
0.9990 |
0.4460 |
323.15 |
0.9980 |
0.4810 |
313.15 |
0.9990 |
0.5060 |
323.15 |
0.9980 |
0.5070 |
333.15 |
0.9980 |
0.5720 |
333.15 |
0.9970 |
0.5890 |
313.15 |
0.9990 |
0.5890 |
323.15 |
0.9980 |
0.6310 |
323.15 |
0.9980 |
0.6660 |
333.15 |
0.9970 |
0.6740 |
313.15 |
0.9990 |
0.7130 |
323.15 |
0.9980 |
0.7670 |
313.15 |
0.9990 |
0.7780 |
333.15 |
0.9960 |
0.7880 |
323.15 |
0.9980 |
0.8480 |
323.15 |
0.9980 |
0.8510 |
333.15 |
0.9950 |
0.8780 |
313.15 |
0.9980 |
0.9030 |
323.15 |
0.9970 |
0.9030 |
333.15 |
0.9960 |
0.9080 |
333.15 |
0.9920 |
0.9310 |
333.15 |
0.9900 |
0.9480 |
313.15 |
0.9950 |
0.9520 |
323.15 |
0.9950 |
0.9520 |
333.15 |
0.9940 |
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
0.0500 |
333.15 |
0.9920 |
0.0510 |
313.15 |
0.9980 |
0.0630 |
323.15 |
0.9950 |
0.1360 |
313.15 |
0.9980 |
0.1510 |
323.15 |
0.9970 |
0.1530 |
333.15 |
0.9960 |
0.2050 |
333.15 |
0.9970 |
0.2120 |
323.15 |
0.9980 |
0.2230 |
313.15 |
0.9980 |
0.2750 |
333.15 |
0.9980 |
0.3090 |
323.15 |
0.9980 |
0.3420 |
313.15 |
0.9990 |
0.3730 |
333.15 |
0.9980 |
0.3930 |
323.15 |
0.9980 |
0.4190 |
313.15 |
0.9990 |
0.4460 |
323.15 |
0.9980 |
0.4810 |
313.15 |
0.9990 |
0.5060 |
323.15 |
0.9980 |
0.5070 |
333.15 |
0.9980 |
0.5720 |
333.15 |
0.9970 |
0.5890 |
313.15 |
0.9990 |
0.5890 |
323.15 |
0.9980 |
0.6310 |
323.15 |
0.9980 |
0.6660 |
333.15 |
0.9970 |
0.6740 |
313.15 |
0.9990 |
0.7130 |
323.15 |
0.9980 |
0.7670 |
313.15 |
0.9990 |
0.7780 |
333.15 |
0.9960 |
0.7880 |
323.15 |
0.9980 |
0.8480 |
323.15 |
0.9980 |
0.8510 |
333.15 |
0.9950 |
0.8780 |
313.15 |
0.9980 |
0.9030 |
323.15 |
0.9970 |
0.9030 |
333.15 |
0.9960 |
0.9080 |
333.15 |
0.9920 |
0.9310 |
333.15 |
0.9900 |
0.9480 |
313.15 |
0.9950 |
0.9520 |
323.15 |
0.9950 |
0.9520 |
333.15 |
0.9940 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0500 |
333.15 |
485.00 |
0.0510 |
313.15 |
371.00 |
0.0630 |
323.15 |
533.00 |
0.1360 |
313.15 |
995.00 |
0.1510 |
323.15 |
1285.00 |
0.1530 |
333.15 |
1499.00 |
0.2050 |
333.15 |
2027.00 |
0.2120 |
323.15 |
1850.00 |
0.2230 |
313.15 |
1626.00 |
0.2750 |
333.15 |
2690.00 |
0.3090 |
323.15 |
2646.00 |
0.3420 |
313.15 |
2486.00 |
0.3730 |
333.15 |
3669.00 |
0.3930 |
323.15 |
3350.00 |
0.4190 |
313.15 |
3029.00 |
0.4460 |
323.15 |
3782.00 |
0.4810 |
313.15 |
3468.00 |
0.5060 |
323.15 |
4265.00 |
0.5070 |
333.15 |
4923.00 |
0.5720 |
333.15 |
5533.00 |
0.5890 |
313.15 |
4217.00 |
0.5890 |
323.15 |
4870.00 |
0.6310 |
323.15 |
5186.00 |
0.6660 |
333.15 |
6482.00 |
0.6740 |
313.15 |
4791.00 |
0.7130 |
323.15 |
5826.00 |
0.7670 |
313.15 |
5468.00 |
0.7780 |
333.15 |
7532.00 |
0.7880 |
323.15 |
6640.00 |
0.8480 |
323.15 |
7280.00 |
0.8510 |
333.15 |
8532.00 |
0.8780 |
313.15 |
6326.00 |
0.9030 |
323.15 |
8160.00 |
0.9080 |
333.15 |
9386.00 |
0.9310 |
333.15 |
9790.00 |
0.9480 |
313.15 |
7187.00 |
0.9520 |
323.15 |
8820.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0500 |
333.15 |
485.00 |
0.0510 |
313.15 |
371.00 |
0.0630 |
323.15 |
533.00 |
0.1360 |
313.15 |
995.00 |
0.1510 |
323.15 |
1285.00 |
0.1530 |
333.15 |
1499.00 |
0.2050 |
333.15 |
2027.00 |
0.2120 |
323.15 |
1850.00 |
0.2230 |
313.15 |
1626.00 |
0.2750 |
333.15 |
2690.00 |
0.3090 |
323.15 |
2646.00 |
0.3420 |
313.15 |
2486.00 |
0.3730 |
333.15 |
3669.00 |
0.3930 |
323.15 |
3350.00 |
0.4190 |
313.15 |
3029.00 |
0.4460 |
323.15 |
3782.00 |
0.4810 |
313.15 |
3468.00 |
0.5060 |
323.15 |
4265.00 |
0.5070 |
333.15 |
4923.00 |
0.5720 |
333.15 |
5533.00 |
0.5890 |
313.15 |
4217.00 |
0.5890 |
323.15 |
4870.00 |
0.6310 |
323.15 |
5186.00 |
0.6660 |
333.15 |
6482.00 |
0.6740 |
313.15 |
4791.00 |
0.7130 |
323.15 |
5826.00 |
0.7670 |
313.15 |
5468.00 |
0.7780 |
333.15 |
7532.00 |
0.7880 |
323.15 |
6640.00 |
0.8480 |
323.15 |
7280.00 |
0.8510 |
333.15 |
8532.00 |
0.8780 |
313.15 |
6326.00 |
0.9030 |
323.15 |
8160.00 |
0.9080 |
333.15 |
9386.00 |
0.9310 |
333.15 |
9790.00 |
0.9480 |
313.15 |
7187.00 |
0.9520 |
323.15 |
8820.00 |
Sources