Mixture of Carbon dioxide + 2H-Azepin-2-one, hexahydro-1-methyl-
Datasets
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
Vapor or sublimation pressure, kPa (2)
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
323.15 |
0.3640 |
5690.00 |
323.15 |
0.4730 |
7330.00 |
323.15 |
0.5280 |
7590.00 |
323.15 |
0.5670 |
8290.00 |
323.15 |
0.5860 |
8410.00 |
323.15 |
0.6300 |
9040.00 |
323.15 |
0.7050 |
9550.00 |
323.15 |
0.7620 |
10620.00 |
323.15 |
0.8120 |
11440.00 |
323.15 |
0.8220 |
11580.00 |
323.15 |
0.8470 |
11840.00 |
323.15 |
0.8710 |
11950.00 |
323.15 |
0.8720 |
11990.00 |
323.15 |
0.8800 |
12120.00 |
333.15 |
0.3640 |
6180.00 |
333.15 |
0.4730 |
8160.00 |
333.15 |
0.5230 |
8590.00 |
333.15 |
0.5280 |
8720.00 |
333.15 |
0.5670 |
9450.00 |
333.15 |
0.5860 |
9710.00 |
333.15 |
0.6300 |
10530.00 |
333.15 |
0.7050 |
11480.00 |
333.15 |
0.7620 |
12980.00 |
333.15 |
0.8120 |
14130.00 |
333.15 |
0.8220 |
14330.00 |
333.15 |
0.8470 |
14620.00 |
333.15 |
0.8710 |
14750.00 |
333.15 |
0.8800 |
14980.00 |
343.15 |
0.3640 |
6940.00 |
343.15 |
0.4730 |
9040.00 |
343.15 |
0.5230 |
9660.00 |
343.15 |
0.5280 |
9710.00 |
343.15 |
0.5860 |
11050.00 |
343.15 |
0.6300 |
11780.00 |
343.15 |
0.7050 |
13500.00 |
343.15 |
0.7620 |
15370.00 |
343.15 |
0.8120 |
16740.00 |
343.15 |
0.8220 |
16950.00 |
343.15 |
0.8710 |
17330.00 |
343.15 |
0.8800 |
17460.00 |
353.15 |
0.3640 |
7350.00 |
353.15 |
0.4730 |
9700.00 |
353.15 |
0.5230 |
10480.00 |
353.15 |
0.5280 |
10710.00 |
353.15 |
0.5860 |
12340.00 |
353.15 |
0.6300 |
13350.00 |
353.15 |
0.7050 |
15550.00 |
353.15 |
0.7620 |
17660.00 |
353.15 |
0.8120 |
19160.00 |
353.15 |
0.8220 |
19240.00 |
353.15 |
0.8710 |
19510.00 |
353.15 |
0.8800 |
19630.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
323.15 |
0.3640 |
5690.00 |
323.15 |
0.4730 |
7330.00 |
323.15 |
0.5280 |
7590.00 |
323.15 |
0.5670 |
8290.00 |
323.15 |
0.5860 |
8410.00 |
323.15 |
0.6300 |
9040.00 |
323.15 |
0.7050 |
9550.00 |
323.15 |
0.7620 |
10620.00 |
323.15 |
0.8120 |
11440.00 |
323.15 |
0.8220 |
11580.00 |
323.15 |
0.8470 |
11840.00 |
323.15 |
0.8710 |
11950.00 |
323.15 |
0.8720 |
11990.00 |
323.15 |
0.8800 |
12120.00 |
333.15 |
0.3640 |
6180.00 |
333.15 |
0.4730 |
8160.00 |
333.15 |
0.5230 |
8590.00 |
333.15 |
0.5280 |
8720.00 |
333.15 |
0.5670 |
9450.00 |
333.15 |
0.5860 |
9710.00 |
333.15 |
0.6300 |
10530.00 |
333.15 |
0.7050 |
11480.00 |
333.15 |
0.7620 |
12980.00 |
333.15 |
0.8120 |
14130.00 |
333.15 |
0.8220 |
14330.00 |
333.15 |
0.8470 |
14620.00 |
333.15 |
0.8710 |
14750.00 |
333.15 |
0.8800 |
14980.00 |
343.15 |
0.3640 |
6940.00 |
343.15 |
0.4730 |
9040.00 |
343.15 |
0.5230 |
9660.00 |
343.15 |
0.5280 |
9710.00 |
343.15 |
0.5860 |
11050.00 |
343.15 |
0.6300 |
11780.00 |
343.15 |
0.7050 |
13500.00 |
343.15 |
0.7620 |
15370.00 |
343.15 |
0.8120 |
16740.00 |
343.15 |
0.8220 |
16950.00 |
343.15 |
0.8710 |
17330.00 |
343.15 |
0.8800 |
17460.00 |
353.15 |
0.3640 |
7350.00 |
353.15 |
0.4730 |
9700.00 |
353.15 |
0.5230 |
10480.00 |
353.15 |
0.5280 |
10710.00 |
353.15 |
0.5860 |
12340.00 |
353.15 |
0.6300 |
13350.00 |
353.15 |
0.7050 |
15550.00 |
353.15 |
0.7620 |
17660.00 |
353.15 |
0.8120 |
19160.00 |
353.15 |
0.8220 |
19240.00 |
353.15 |
0.8710 |
19510.00 |
353.15 |
0.8800 |
19630.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of Carbon dioxide (1) - Gas |
Vapor or sublimation pressure, kPa - Gas |
323.15 |
0.9040 |
11920.00 |
323.15 |
0.9150 |
11810.00 |
333.15 |
0.9040 |
14710.00 |
333.15 |
0.9150 |
14370.00 |
343.15 |
0.9040 |
17230.00 |
343.15 |
0.9150 |
17010.00 |
353.15 |
0.9040 |
19500.00 |
353.15 |
0.9150 |
19340.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of Carbon dioxide (1) - Gas |
Vapor or sublimation pressure, kPa - Gas |
323.15 |
0.9040 |
11920.00 |
323.15 |
0.9150 |
11810.00 |
333.15 |
0.9040 |
14710.00 |
333.15 |
0.9150 |
14370.00 |
343.15 |
0.9040 |
17230.00 |
343.15 |
0.9150 |
17010.00 |
353.15 |
0.9040 |
19500.00 |
353.15 |
0.9150 |
19340.00 |
Sources