Datasets
-
Pvap - Vapor or sublimation pressure, kPa (6)
-
Vapor or sublimation pressure, kPa (2)
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
303 (Liquid mixture 1)
| Vapor or sublimation pressure, kPa - Liquid mixture 1 |
| 7410.00 |
| 7420.00 |
| 6980.00 |
| 7810.00 |
| 6940.00 |
| 7680.00 |
| 6860.00 |
| 7580.00 |
| 6940.00 |
| 7670.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
303 (Liquid mixture 1)
| Mole fraction of Carbon dioxide (1) - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
| 0.8293 |
7540.00 |
| 0.8293 |
9450.00 |
| 0.8574 |
7860.00 |
| 0.8574 |
9660.00 |
| 0.9112 |
8060.00 |
| 0.9112 |
9920.00 |
| 0.9584 |
7640.00 |
| 0.9584 |
9080.00 |
| 0.9696 |
8110.00 |
| 0.9801 |
7660.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Carbon dioxide (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 0.2299 |
303.00 |
3460.00 |
| 0.2299 |
313.00 |
3850.00 |
| 0.2299 |
318.00 |
3990.00 |
| 0.2299 |
323.00 |
4300.00 |
| 0.2299 |
328.00 |
4530.00 |
| 0.2299 |
333.00 |
4720.00 |
| 0.2299 |
338.00 |
4940.00 |
| 0.2299 |
343.00 |
5160.00 |
| 0.2299 |
303.00 |
3630.00 |
| 0.5268 |
303.00 |
6140.00 |
| 0.5268 |
313.00 |
7330.00 |
| 0.5268 |
318.00 |
7940.00 |
| 0.5268 |
323.00 |
8760.00 |
| 0.5268 |
328.00 |
9370.00 |
| 0.5268 |
333.00 |
10120.00 |
| 0.5268 |
338.00 |
10910.00 |
| 0.5268 |
343.00 |
11780.00 |
| 0.5268 |
303.00 |
6810.00 |
| 0.6485 |
303.00 |
6730.00 |
| 0.6485 |
313.00 |
8270.00 |
| 0.6485 |
323.00 |
10210.00 |
| 0.6485 |
333.00 |
12340.00 |
| 0.6485 |
343.00 |
14970.00 |
| 0.7217 |
303.00 |
7430.00 |
| 0.7217 |
313.00 |
9310.00 |
| 0.7217 |
318.00 |
10600.00 |
| 0.7217 |
323.00 |
12120.00 |
| 0.7217 |
328.00 |
13480.00 |
| 0.7217 |
333.00 |
15050.00 |
| 0.7217 |
338.00 |
16490.00 |
| 0.7217 |
343.00 |
17880.00 |
| 0.7217 |
303.00 |
8290.00 |
| 0.7413 |
303.00 |
7130.00 |
| 0.7413 |
313.00 |
9460.00 |
| 0.7413 |
323.00 |
12650.00 |
| 0.7413 |
333.00 |
15890.00 |
| 0.7413 |
343.00 |
18820.00 |
| 0.8293 |
313.00 |
11320.00 |
| 0.8293 |
323.00 |
14810.00 |
| 0.8293 |
333.00 |
17850.00 |
| 0.8293 |
343.00 |
20730.00 |
| 0.8574 |
313.00 |
11490.00 |
| 0.8574 |
318.00 |
13330.00 |
| 0.8574 |
323.00 |
15050.00 |
| 0.8574 |
328.00 |
16660.00 |
| 0.8574 |
333.00 |
18040.00 |
| 0.8574 |
338.00 |
19580.00 |
| 0.8574 |
343.00 |
20830.00 |
| 0.9696 |
303.00 |
6670.00 |
| 0.9801 |
303.00 |
6720.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
303 (Liquid mixture 1)
| Vapor or sublimation pressure, kPa - Liquid mixture 1 |
| 7410.00 |
| 7420.00 |
| 6980.00 |
| 7810.00 |
| 6940.00 |
| 7680.00 |
| 6860.00 |
| 7580.00 |
| 6940.00 |
| 7670.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
303 (Liquid mixture 1)
| Mole fraction of Carbon dioxide (1) - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
| 0.8293 |
7540.00 |
| 0.8293 |
9450.00 |
| 0.8574 |
7860.00 |
| 0.8574 |
9660.00 |
| 0.9112 |
8060.00 |
| 0.9112 |
9920.00 |
| 0.9584 |
7640.00 |
| 0.9584 |
9080.00 |
| 0.9696 |
8110.00 |
| 0.9801 |
7660.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Carbon dioxide (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 0.2299 |
303.00 |
3460.00 |
| 0.2299 |
313.00 |
3850.00 |
| 0.2299 |
318.00 |
3990.00 |
| 0.2299 |
323.00 |
4300.00 |
| 0.2299 |
328.00 |
4530.00 |
| 0.2299 |
333.00 |
4720.00 |
| 0.2299 |
338.00 |
4940.00 |
| 0.2299 |
343.00 |
5160.00 |
| 0.2299 |
303.00 |
3630.00 |
| 0.5268 |
303.00 |
6140.00 |
| 0.5268 |
313.00 |
7330.00 |
| 0.5268 |
318.00 |
7940.00 |
| 0.5268 |
323.00 |
8760.00 |
| 0.5268 |
328.00 |
9370.00 |
| 0.5268 |
333.00 |
10120.00 |
| 0.5268 |
338.00 |
10910.00 |
| 0.5268 |
343.00 |
11780.00 |
| 0.5268 |
303.00 |
6810.00 |
| 0.6485 |
303.00 |
6730.00 |
| 0.6485 |
313.00 |
8270.00 |
| 0.6485 |
323.00 |
10210.00 |
| 0.6485 |
333.00 |
12340.00 |
| 0.6485 |
343.00 |
14970.00 |
| 0.7217 |
303.00 |
7430.00 |
| 0.7217 |
313.00 |
9310.00 |
| 0.7217 |
318.00 |
10600.00 |
| 0.7217 |
323.00 |
12120.00 |
| 0.7217 |
328.00 |
13480.00 |
| 0.7217 |
333.00 |
15050.00 |
| 0.7217 |
338.00 |
16490.00 |
| 0.7217 |
343.00 |
17880.00 |
| 0.7217 |
303.00 |
8290.00 |
| 0.7413 |
303.00 |
7130.00 |
| 0.7413 |
313.00 |
9460.00 |
| 0.7413 |
323.00 |
12650.00 |
| 0.7413 |
333.00 |
15890.00 |
| 0.7413 |
343.00 |
18820.00 |
| 0.8293 |
313.00 |
11320.00 |
| 0.8293 |
323.00 |
14810.00 |
| 0.8293 |
333.00 |
17850.00 |
| 0.8293 |
343.00 |
20730.00 |
| 0.8574 |
313.00 |
11490.00 |
| 0.8574 |
318.00 |
13330.00 |
| 0.8574 |
323.00 |
15050.00 |
| 0.8574 |
328.00 |
16660.00 |
| 0.8574 |
333.00 |
18040.00 |
| 0.8574 |
338.00 |
19580.00 |
| 0.8574 |
343.00 |
20830.00 |
| 0.9696 |
303.00 |
6670.00 |
| 0.9801 |
303.00 |
6720.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Carbon dioxide (1) - Gas |
Temperature, K - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 0.9112 |
313.00 |
11680.00 |
| 0.9112 |
318.00 |
13360.00 |
| 0.9112 |
323.00 |
15060.00 |
| 0.9112 |
328.00 |
16560.00 |
| 0.9112 |
333.00 |
18020.00 |
| 0.9112 |
338.00 |
19430.00 |
| 0.9112 |
343.00 |
20710.00 |
| 0.9584 |
313.00 |
10680.00 |
| 0.9584 |
323.00 |
13850.00 |
| 0.9584 |
333.00 |
16580.00 |
| 0.9584 |
343.00 |
19090.00 |
| 0.9696 |
313.00 |
9580.00 |
| 0.9696 |
323.00 |
12620.00 |
| 0.9696 |
333.00 |
15430.00 |
| 0.9696 |
343.00 |
17960.00 |
| 0.9801 |
313.00 |
9070.00 |
| 0.9801 |
318.00 |
10430.00 |
| 0.9801 |
323.00 |
11870.00 |
| 0.9801 |
328.00 |
13040.00 |
| 0.9801 |
333.00 |
14110.00 |
| 0.9801 |
338.00 |
15280.00 |
| 0.9801 |
343.00 |
15970.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Carbon dioxide (1) - Gas |
Temperature, K - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 0.9112 |
313.00 |
11680.00 |
| 0.9112 |
318.00 |
13360.00 |
| 0.9112 |
323.00 |
15060.00 |
| 0.9112 |
328.00 |
16560.00 |
| 0.9112 |
333.00 |
18020.00 |
| 0.9112 |
338.00 |
19430.00 |
| 0.9112 |
343.00 |
20710.00 |
| 0.9584 |
313.00 |
10680.00 |
| 0.9584 |
323.00 |
13850.00 |
| 0.9584 |
333.00 |
16580.00 |
| 0.9584 |
343.00 |
19090.00 |
| 0.9696 |
313.00 |
9580.00 |
| 0.9696 |
323.00 |
12620.00 |
| 0.9696 |
333.00 |
15430.00 |
| 0.9696 |
343.00 |
17960.00 |
| 0.9801 |
313.00 |
9070.00 |
| 0.9801 |
318.00 |
10430.00 |
| 0.9801 |
323.00 |
11870.00 |
| 0.9801 |
328.00 |
13040.00 |
| 0.9801 |
333.00 |
14110.00 |
| 0.9801 |
338.00 |
15280.00 |
| 0.9801 |
343.00 |
15970.00 |
Sources