Mixture of Phenanthrene + Toluene + Carbon dioxide
Datasets
-
Pvap - Vapor or sublimation pressure, kPa (4)
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (3) - Liquid |
Mole fraction of Toluene (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
363.20 |
0.6128 |
0.3319 |
9340.00 |
353.40 |
0.6128 |
0.3319 |
8480.00 |
343.60 |
0.6128 |
0.3319 |
7530.00 |
333.90 |
0.6128 |
0.3319 |
6590.00 |
323.70 |
0.6128 |
0.3319 |
5680.00 |
313.50 |
0.6128 |
0.3319 |
4760.00 |
303.70 |
0.6128 |
0.3319 |
3950.00 |
298.90 |
0.6128 |
0.3319 |
3520.00 |
297.70 |
0.6128 |
0.3319 |
3330.00 |
295.90 |
0.6128 |
0.3319 |
3220.00 |
363.00 |
0.7807 |
0.1880 |
11350.00 |
353.30 |
0.7807 |
0.1880 |
10040.00 |
343.40 |
0.7807 |
0.1880 |
8990.00 |
334.00 |
0.7807 |
0.1880 |
7730.00 |
323.70 |
0.7807 |
0.1880 |
6580.00 |
313.70 |
0.7807 |
0.1880 |
5530.00 |
358.50 |
0.9047 |
0.0187 |
15190.00 |
353.40 |
0.9047 |
0.0187 |
13920.00 |
348.60 |
0.9047 |
0.0187 |
13530.00 |
343.70 |
0.9047 |
0.0187 |
12460.00 |
338.90 |
0.9047 |
0.0187 |
11860.00 |
334.10 |
0.9047 |
0.0187 |
11270.00 |
363.20 |
0.5994 |
0.3698 |
8970.00 |
353.40 |
0.5994 |
0.3698 |
8180.00 |
343.60 |
0.5994 |
0.3698 |
7390.00 |
333.50 |
0.5994 |
0.3698 |
6560.00 |
323.70 |
0.5994 |
0.3698 |
5620.00 |
313.50 |
0.5994 |
0.3698 |
4810.00 |
303.70 |
0.5994 |
0.3698 |
4160.00 |
298.70 |
0.5994 |
0.3698 |
3680.00 |
362.70 |
0.7710 |
0.2114 |
11290.00 |
353.20 |
0.7710 |
0.2114 |
10100.00 |
343.60 |
0.7710 |
0.2114 |
8910.00 |
333.80 |
0.7710 |
0.2114 |
7700.00 |
323.40 |
0.7710 |
0.2114 |
6600.00 |
313.60 |
0.7710 |
0.2114 |
5560.00 |
303.50 |
0.7710 |
0.2114 |
4670.00 |
298.60 |
0.7710 |
0.2114 |
4150.00 |
292.80 |
0.7710 |
0.2114 |
3540.00 |
352.50 |
0.8998 |
0.0925 |
13410.00 |
343.30 |
0.8998 |
0.0925 |
12960.00 |
333.50 |
0.8998 |
0.0925 |
11270.00 |
323.60 |
0.8998 |
0.0925 |
9950.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (3) - Liquid |
Mole fraction of Toluene (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
291.80 |
0.6128 |
0.3319 |
4000.00 |
290.80 |
0.6128 |
0.3319 |
5000.00 |
290.00 |
0.6128 |
0.3319 |
6000.00 |
307.60 |
0.7807 |
0.1880 |
6500.00 |
306.40 |
0.7807 |
0.1880 |
7000.00 |
306.40 |
0.7807 |
0.1880 |
8000.00 |
306.00 |
0.7807 |
0.1880 |
9000.00 |
306.00 |
0.7807 |
0.1880 |
10000.00 |
329.50 |
0.9047 |
0.0187 |
11000.00 |
324.90 |
0.9047 |
0.0187 |
13000.00 |
277.30 |
0.5994 |
0.3698 |
4000.00 |
291.40 |
0.7710 |
0.2114 |
4000.00 |
290.60 |
0.7710 |
0.2114 |
5000.00 |
289.40 |
0.7710 |
0.2114 |
6000.00 |
289.00 |
0.7710 |
0.2114 |
7000.00 |
288.80 |
0.7710 |
0.2114 |
8000.00 |
315.20 |
0.8998 |
0.0925 |
9000.00 |
309.80 |
0.8998 |
0.0925 |
11000.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (3) - Liquid |
Mole fraction of Toluene (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
363.20 |
0.6128 |
0.3319 |
9340.00 |
353.40 |
0.6128 |
0.3319 |
8480.00 |
343.60 |
0.6128 |
0.3319 |
7530.00 |
333.90 |
0.6128 |
0.3319 |
6590.00 |
323.70 |
0.6128 |
0.3319 |
5680.00 |
313.50 |
0.6128 |
0.3319 |
4760.00 |
303.70 |
0.6128 |
0.3319 |
3950.00 |
298.90 |
0.6128 |
0.3319 |
3520.00 |
297.70 |
0.6128 |
0.3319 |
3330.00 |
295.90 |
0.6128 |
0.3319 |
3220.00 |
363.00 |
0.7807 |
0.1880 |
11350.00 |
353.30 |
0.7807 |
0.1880 |
10040.00 |
343.40 |
0.7807 |
0.1880 |
8990.00 |
334.00 |
0.7807 |
0.1880 |
7730.00 |
323.70 |
0.7807 |
0.1880 |
6580.00 |
313.70 |
0.7807 |
0.1880 |
5530.00 |
358.50 |
0.9047 |
0.0187 |
15190.00 |
353.40 |
0.9047 |
0.0187 |
13920.00 |
348.60 |
0.9047 |
0.0187 |
13530.00 |
343.70 |
0.9047 |
0.0187 |
12460.00 |
338.90 |
0.9047 |
0.0187 |
11860.00 |
334.10 |
0.9047 |
0.0187 |
11270.00 |
363.20 |
0.5994 |
0.3698 |
8970.00 |
353.40 |
0.5994 |
0.3698 |
8180.00 |
343.60 |
0.5994 |
0.3698 |
7390.00 |
333.50 |
0.5994 |
0.3698 |
6560.00 |
323.70 |
0.5994 |
0.3698 |
5620.00 |
313.50 |
0.5994 |
0.3698 |
4810.00 |
303.70 |
0.5994 |
0.3698 |
4160.00 |
298.70 |
0.5994 |
0.3698 |
3680.00 |
362.70 |
0.7710 |
0.2114 |
11290.00 |
353.20 |
0.7710 |
0.2114 |
10100.00 |
343.60 |
0.7710 |
0.2114 |
8910.00 |
333.80 |
0.7710 |
0.2114 |
7700.00 |
323.40 |
0.7710 |
0.2114 |
6600.00 |
313.60 |
0.7710 |
0.2114 |
5560.00 |
303.50 |
0.7710 |
0.2114 |
4670.00 |
298.60 |
0.7710 |
0.2114 |
4150.00 |
292.80 |
0.7710 |
0.2114 |
3540.00 |
352.50 |
0.8998 |
0.0925 |
13410.00 |
343.30 |
0.8998 |
0.0925 |
12960.00 |
333.50 |
0.8998 |
0.0925 |
11270.00 |
323.60 |
0.8998 |
0.0925 |
9950.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (3) - Liquid |
Mole fraction of Toluene (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
291.80 |
0.6128 |
0.3319 |
4000.00 |
290.80 |
0.6128 |
0.3319 |
5000.00 |
290.00 |
0.6128 |
0.3319 |
6000.00 |
307.60 |
0.7807 |
0.1880 |
6500.00 |
306.40 |
0.7807 |
0.1880 |
7000.00 |
306.40 |
0.7807 |
0.1880 |
8000.00 |
306.00 |
0.7807 |
0.1880 |
9000.00 |
306.00 |
0.7807 |
0.1880 |
10000.00 |
329.50 |
0.9047 |
0.0187 |
11000.00 |
324.90 |
0.9047 |
0.0187 |
13000.00 |
277.30 |
0.5994 |
0.3698 |
4000.00 |
291.40 |
0.7710 |
0.2114 |
4000.00 |
290.60 |
0.7710 |
0.2114 |
5000.00 |
289.40 |
0.7710 |
0.2114 |
6000.00 |
289.00 |
0.7710 |
0.2114 |
7000.00 |
288.80 |
0.7710 |
0.2114 |
8000.00 |
315.20 |
0.8998 |
0.0925 |
9000.00 |
309.80 |
0.8998 |
0.0925 |
11000.00 |
Sources