Mixture of Squalane + Carbon dioxide + Ethanol
Datasets
-
Pvap - Vapor or sublimation pressure, kPa (4)
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (2) - Liquid |
Mole fraction of Squalane (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.6414 |
0.0100 |
318.15 |
6740.00 |
0.6414 |
0.0100 |
328.15 |
7710.00 |
0.6414 |
0.0100 |
337.95 |
8720.00 |
0.5949 |
0.0504 |
327.65 |
7940.00 |
0.5949 |
0.0504 |
337.85 |
8910.00 |
0.5949 |
0.0504 |
347.90 |
9950.00 |
0.5949 |
0.0504 |
358.15 |
10980.00 |
0.5773 |
0.0952 |
334.35 |
8485.00 |
0.5773 |
0.0952 |
343.55 |
9392.00 |
0.5773 |
0.0952 |
362.43 |
11234.00 |
0.5770 |
0.0952 |
383.15 |
12980.00 |
0.5528 |
0.0997 |
333.15 |
7990.00 |
0.5528 |
0.0997 |
343.25 |
8970.00 |
0.5528 |
0.0997 |
352.65 |
9720.00 |
0.5528 |
0.0997 |
363.05 |
10630.00 |
0.5528 |
0.0997 |
372.75 |
11470.00 |
0.5090 |
0.1489 |
323.23 |
5690.00 |
0.5090 |
0.1489 |
333.45 |
6458.00 |
0.5090 |
0.1489 |
343.31 |
7198.00 |
0.5090 |
0.1489 |
353.27 |
7892.00 |
0.5090 |
0.1489 |
363.21 |
8593.00 |
0.5090 |
0.1489 |
373.32 |
9793.00 |
0.5090 |
0.1489 |
383.25 |
10477.00 |
0.4569 |
0.1964 |
343.40 |
6775.00 |
0.4569 |
0.1964 |
353.31 |
7433.00 |
0.4569 |
0.1964 |
363.07 |
8078.00 |
0.4569 |
0.1964 |
373.11 |
8370.00 |
0.4569 |
0.1964 |
383.29 |
8963.00 |
0.4569 |
0.1964 |
393.25 |
9367.00 |
0.2333 |
0.0510 |
328.12 |
3237.00 |
0.2333 |
0.0510 |
353.08 |
4058.00 |
0.2333 |
0.0510 |
362.48 |
4243.00 |
0.2333 |
0.0510 |
373.48 |
4540.00 |
0.2333 |
0.0510 |
383.55 |
4927.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (2) - Liquid |
Mole fraction of Squalane (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.5011 |
0.1489 |
323.25 |
5680.00 |
0.5011 |
0.1489 |
333.45 |
6450.00 |
0.5011 |
0.1489 |
343.25 |
7220.00 |
0.5011 |
0.1489 |
353.35 |
7790.00 |
0.5773 |
0.0952 |
334.35 |
8470.00 |
0.5773 |
0.0952 |
343.55 |
9390.00 |
0.5773 |
0.0952 |
362.15 |
11180.00 |
0.5773 |
0.0952 |
383.15 |
13140.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (2) - Liquid |
Mole fraction of Squalane (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.6414 |
0.0100 |
318.15 |
6740.00 |
0.6414 |
0.0100 |
328.15 |
7710.00 |
0.6414 |
0.0100 |
337.95 |
8720.00 |
0.5949 |
0.0504 |
327.65 |
7940.00 |
0.5949 |
0.0504 |
337.85 |
8910.00 |
0.5949 |
0.0504 |
347.90 |
9950.00 |
0.5949 |
0.0504 |
358.15 |
10980.00 |
0.5773 |
0.0952 |
334.35 |
8485.00 |
0.5773 |
0.0952 |
343.55 |
9392.00 |
0.5773 |
0.0952 |
362.43 |
11234.00 |
0.5770 |
0.0952 |
383.15 |
12980.00 |
0.5528 |
0.0997 |
333.15 |
7990.00 |
0.5528 |
0.0997 |
343.25 |
8970.00 |
0.5528 |
0.0997 |
352.65 |
9720.00 |
0.5528 |
0.0997 |
363.05 |
10630.00 |
0.5528 |
0.0997 |
372.75 |
11470.00 |
0.5090 |
0.1489 |
323.23 |
5690.00 |
0.5090 |
0.1489 |
333.45 |
6458.00 |
0.5090 |
0.1489 |
343.31 |
7198.00 |
0.5090 |
0.1489 |
353.27 |
7892.00 |
0.5090 |
0.1489 |
363.21 |
8593.00 |
0.5090 |
0.1489 |
373.32 |
9793.00 |
0.5090 |
0.1489 |
383.25 |
10477.00 |
0.4569 |
0.1964 |
343.40 |
6775.00 |
0.4569 |
0.1964 |
353.31 |
7433.00 |
0.4569 |
0.1964 |
363.07 |
8078.00 |
0.4569 |
0.1964 |
373.11 |
8370.00 |
0.4569 |
0.1964 |
383.29 |
8963.00 |
0.4569 |
0.1964 |
393.25 |
9367.00 |
0.2333 |
0.0510 |
328.12 |
3237.00 |
0.2333 |
0.0510 |
353.08 |
4058.00 |
0.2333 |
0.0510 |
362.48 |
4243.00 |
0.2333 |
0.0510 |
373.48 |
4540.00 |
0.2333 |
0.0510 |
383.55 |
4927.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (2) - Liquid |
Mole fraction of Squalane (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.5011 |
0.1489 |
323.25 |
5680.00 |
0.5011 |
0.1489 |
333.45 |
6450.00 |
0.5011 |
0.1489 |
343.25 |
7220.00 |
0.5011 |
0.1489 |
353.35 |
7790.00 |
0.5773 |
0.0952 |
334.35 |
8470.00 |
0.5773 |
0.0952 |
343.55 |
9390.00 |
0.5773 |
0.0952 |
362.15 |
11180.00 |
0.5773 |
0.0952 |
383.15 |
13140.00 |
Sources