Mixture of Carbon dioxide + Ethanol + Butanedioic acid, diethyl ester
Datasets
-
Pvap - Vapor or sublimation pressure, kPa (2)
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Solvent: Mole fraction of Butanedioic acid, diethyl ester (3) - Liquid |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.4960 |
303.28 |
0.4475 |
3480.00 |
0.4960 |
303.28 |
0.5547 |
4020.00 |
0.4960 |
303.28 |
0.6529 |
4470.00 |
0.4960 |
313.17 |
0.4475 |
4100.00 |
0.4960 |
313.17 |
0.5547 |
4810.00 |
0.4960 |
313.17 |
0.6529 |
5500.00 |
0.4960 |
323.21 |
0.4475 |
4700.00 |
0.4960 |
323.21 |
0.5547 |
5600.00 |
0.4960 |
323.21 |
0.6529 |
6220.00 |
0.4960 |
333.17 |
0.4475 |
5290.00 |
0.4960 |
333.17 |
0.5547 |
6830.00 |
0.4960 |
333.17 |
0.6529 |
7270.00 |
0.4960 |
343.16 |
0.4475 |
5930.00 |
0.4960 |
343.16 |
0.5547 |
7630.00 |
0.4960 |
343.16 |
0.6529 |
8520.00 |
0.3240 |
303.28 |
0.4506 |
3860.00 |
0.3240 |
303.28 |
0.5505 |
4440.00 |
0.3240 |
313.15 |
0.4506 |
4460.00 |
0.3240 |
313.15 |
0.5505 |
5320.00 |
0.3240 |
323.13 |
0.4506 |
5250.00 |
0.3240 |
323.13 |
0.5505 |
6230.00 |
0.3240 |
333.15 |
0.4506 |
6020.00 |
0.3240 |
333.15 |
0.5505 |
7330.00 |
0.3240 |
343.14 |
0.4506 |
6850.00 |
0.3240 |
343.14 |
0.5505 |
8010.00 |
0.4960 |
303.28 |
0.7594 |
5160.00 |
0.4960 |
303.28 |
0.8501 |
6020.00 |
0.4960 |
303.28 |
0.9509 |
6520.00 |
0.4960 |
313.17 |
0.7594 |
6400.00 |
0.4960 |
313.17 |
0.8501 |
7180.00 |
0.4960 |
313.17 |
0.9509 |
7870.00 |
0.4960 |
323.21 |
0.7594 |
7430.00 |
0.4960 |
323.21 |
0.8501 |
8520.00 |
0.4960 |
323.21 |
0.9509 |
9400.00 |
0.4960 |
333.17 |
0.7594 |
8880.00 |
0.4960 |
333.17 |
0.8501 |
10090.00 |
0.4960 |
333.17 |
0.9509 |
11450.00 |
0.4960 |
343.16 |
0.7594 |
10280.00 |
0.4960 |
343.16 |
0.8501 |
11660.00 |
0.4960 |
343.16 |
0.9509 |
12840.00 |
0.3240 |
303.28 |
0.7506 |
5590.00 |
0.3240 |
303.28 |
0.9011 |
5960.00 |
0.3240 |
313.15 |
0.7506 |
6690.00 |
0.3240 |
313.15 |
0.9011 |
7370.00 |
0.3240 |
323.13 |
0.7506 |
7890.00 |
0.3240 |
323.13 |
0.9011 |
8950.00 |
0.3240 |
333.15 |
0.7506 |
9330.00 |
0.3240 |
333.15 |
0.9011 |
10570.00 |
0.3240 |
343.14 |
0.7506 |
10820.00 |
0.3240 |
343.14 |
0.9011 |
12240.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Solvent: Mole fraction of Butanedioic acid, diethyl ester (3) - Liquid |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.4960 |
303.28 |
0.4475 |
3480.00 |
0.4960 |
303.28 |
0.5547 |
4020.00 |
0.4960 |
303.28 |
0.6529 |
4470.00 |
0.4960 |
313.17 |
0.4475 |
4100.00 |
0.4960 |
313.17 |
0.5547 |
4810.00 |
0.4960 |
313.17 |
0.6529 |
5500.00 |
0.4960 |
323.21 |
0.4475 |
4700.00 |
0.4960 |
323.21 |
0.5547 |
5600.00 |
0.4960 |
323.21 |
0.6529 |
6220.00 |
0.4960 |
333.17 |
0.4475 |
5290.00 |
0.4960 |
333.17 |
0.5547 |
6830.00 |
0.4960 |
333.17 |
0.6529 |
7270.00 |
0.4960 |
343.16 |
0.4475 |
5930.00 |
0.4960 |
343.16 |
0.5547 |
7630.00 |
0.4960 |
343.16 |
0.6529 |
8520.00 |
0.3240 |
303.28 |
0.4506 |
3860.00 |
0.3240 |
303.28 |
0.5505 |
4440.00 |
0.3240 |
313.15 |
0.4506 |
4460.00 |
0.3240 |
313.15 |
0.5505 |
5320.00 |
0.3240 |
323.13 |
0.4506 |
5250.00 |
0.3240 |
323.13 |
0.5505 |
6230.00 |
0.3240 |
333.15 |
0.4506 |
6020.00 |
0.3240 |
333.15 |
0.5505 |
7330.00 |
0.3240 |
343.14 |
0.4506 |
6850.00 |
0.3240 |
343.14 |
0.5505 |
8010.00 |
0.4960 |
303.28 |
0.7594 |
5160.00 |
0.4960 |
303.28 |
0.8501 |
6020.00 |
0.4960 |
303.28 |
0.9509 |
6520.00 |
0.4960 |
313.17 |
0.7594 |
6400.00 |
0.4960 |
313.17 |
0.8501 |
7180.00 |
0.4960 |
313.17 |
0.9509 |
7870.00 |
0.4960 |
323.21 |
0.7594 |
7430.00 |
0.4960 |
323.21 |
0.8501 |
8520.00 |
0.4960 |
323.21 |
0.9509 |
9400.00 |
0.4960 |
333.17 |
0.7594 |
8880.00 |
0.4960 |
333.17 |
0.8501 |
10090.00 |
0.4960 |
333.17 |
0.9509 |
11450.00 |
0.4960 |
343.16 |
0.7594 |
10280.00 |
0.4960 |
343.16 |
0.8501 |
11660.00 |
0.4960 |
343.16 |
0.9509 |
12840.00 |
0.3240 |
303.28 |
0.7506 |
5590.00 |
0.3240 |
303.28 |
0.9011 |
5960.00 |
0.3240 |
313.15 |
0.7506 |
6690.00 |
0.3240 |
313.15 |
0.9011 |
7370.00 |
0.3240 |
323.13 |
0.7506 |
7890.00 |
0.3240 |
323.13 |
0.9011 |
8950.00 |
0.3240 |
333.15 |
0.7506 |
9330.00 |
0.3240 |
333.15 |
0.9011 |
10570.00 |
0.3240 |
343.14 |
0.7506 |
10820.00 |
0.3240 |
343.14 |
0.9011 |
12240.00 |
Sources