Mixture of Carbon dioxide + Dodecanoic acid, ethyl ester
Datasets
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
Vapor or sublimation pressure, kPa (2)
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Dodecanoic acid, ethyl ester (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.2610 |
308.40 |
6090.00 |
0.2610 |
318.10 |
7160.00 |
0.2610 |
328.70 |
8420.00 |
0.2610 |
338.70 |
9620.00 |
0.2610 |
348.70 |
10840.00 |
0.2610 |
358.70 |
12080.00 |
0.1950 |
308.50 |
6740.00 |
0.1950 |
318.40 |
8070.00 |
0.1950 |
328.60 |
9590.00 |
0.1950 |
338.60 |
11110.00 |
0.1950 |
348.70 |
12620.00 |
0.1950 |
358.70 |
14050.00 |
0.1450 |
308.50 |
7250.00 |
0.1450 |
318.50 |
8850.00 |
0.1450 |
328.60 |
10620.00 |
0.1450 |
338.60 |
12400.00 |
0.1450 |
348.50 |
14160.00 |
0.1450 |
358.70 |
15900.00 |
0.1070 |
308.50 |
7540.00 |
0.1070 |
318.50 |
9330.00 |
0.1070 |
328.70 |
11380.00 |
0.1070 |
338.90 |
13480.00 |
0.1070 |
348.70 |
15370.00 |
0.1070 |
358.70 |
17110.00 |
0.0800 |
308.50 |
7610.00 |
0.0800 |
318.50 |
9550.00 |
0.0800 |
328.60 |
11820.00 |
0.0800 |
338.40 |
14000.00 |
0.0800 |
349.00 |
16130.00 |
0.0550 |
308.60 |
7870.00 |
0.0550 |
318.60 |
9850.00 |
0.0440 |
308.70 |
7970.00 |
0.0260 |
308.50 |
7850.00 |
0.0180 |
308.40 |
7830.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Dodecanoic acid, ethyl ester (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.2610 |
308.40 |
6090.00 |
0.2610 |
318.10 |
7160.00 |
0.2610 |
328.70 |
8420.00 |
0.2610 |
338.70 |
9620.00 |
0.2610 |
348.70 |
10840.00 |
0.2610 |
358.70 |
12080.00 |
0.1950 |
308.50 |
6740.00 |
0.1950 |
318.40 |
8070.00 |
0.1950 |
328.60 |
9590.00 |
0.1950 |
338.60 |
11110.00 |
0.1950 |
348.70 |
12620.00 |
0.1950 |
358.70 |
14050.00 |
0.1450 |
308.50 |
7250.00 |
0.1450 |
318.50 |
8850.00 |
0.1450 |
328.60 |
10620.00 |
0.1450 |
338.60 |
12400.00 |
0.1450 |
348.50 |
14160.00 |
0.1450 |
358.70 |
15900.00 |
0.1070 |
308.50 |
7540.00 |
0.1070 |
318.50 |
9330.00 |
0.1070 |
328.70 |
11380.00 |
0.1070 |
338.90 |
13480.00 |
0.1070 |
348.70 |
15370.00 |
0.1070 |
358.70 |
17110.00 |
0.0800 |
308.50 |
7610.00 |
0.0800 |
318.50 |
9550.00 |
0.0800 |
328.60 |
11820.00 |
0.0800 |
338.40 |
14000.00 |
0.0800 |
349.00 |
16130.00 |
0.0550 |
308.60 |
7870.00 |
0.0550 |
318.60 |
9850.00 |
0.0440 |
308.70 |
7970.00 |
0.0260 |
308.50 |
7850.00 |
0.0180 |
308.40 |
7830.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Dodecanoic acid, ethyl ester (2) - Gas |
Temperature, K - Gas |
Vapor or sublimation pressure, kPa - Gas |
0.0800 |
358.80 |
17930.00 |
0.0550 |
328.70 |
12240.00 |
0.0550 |
338.40 |
14380.00 |
0.0550 |
348.50 |
16400.00 |
0.0550 |
358.30 |
18200.00 |
0.0440 |
318.70 |
10140.00 |
0.0440 |
328.70 |
12480.00 |
0.0440 |
338.40 |
14620.00 |
0.0440 |
348.60 |
16680.00 |
0.0440 |
358.30 |
18370.00 |
0.0260 |
318.60 |
10010.00 |
0.0260 |
328.70 |
12340.00 |
0.0260 |
338.40 |
14390.00 |
0.0260 |
348.80 |
16410.00 |
0.0260 |
358.60 |
18110.00 |
0.0180 |
318.50 |
9870.00 |
0.0180 |
328.60 |
12090.00 |
0.0180 |
338.40 |
14110.00 |
0.0180 |
349.00 |
16040.00 |
0.0180 |
358.60 |
17540.00 |
0.0108 |
308.60 |
7890.00 |
0.0108 |
318.20 |
9710.00 |
0.0108 |
328.70 |
11920.00 |
0.0108 |
338.80 |
13820.00 |
0.0108 |
348.40 |
15460.00 |
0.0108 |
358.60 |
16890.00 |
0.0054 |
308.30 |
7870.00 |
0.0054 |
318.20 |
9570.00 |
0.0054 |
328.70 |
11540.00 |
0.0054 |
338.80 |
13150.00 |
0.0054 |
348.40 |
14440.00 |
0.0054 |
358.40 |
15620.00 |
0.0035 |
308.50 |
7890.00 |
0.0035 |
318.50 |
9470.00 |
0.0035 |
328.60 |
11180.00 |
0.0035 |
338.80 |
12660.00 |
0.0035 |
348.60 |
13850.00 |
0.0035 |
358.80 |
14810.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Dodecanoic acid, ethyl ester (2) - Gas |
Temperature, K - Gas |
Vapor or sublimation pressure, kPa - Gas |
0.0800 |
358.80 |
17930.00 |
0.0550 |
328.70 |
12240.00 |
0.0550 |
338.40 |
14380.00 |
0.0550 |
348.50 |
16400.00 |
0.0550 |
358.30 |
18200.00 |
0.0440 |
318.70 |
10140.00 |
0.0440 |
328.70 |
12480.00 |
0.0440 |
338.40 |
14620.00 |
0.0440 |
348.60 |
16680.00 |
0.0440 |
358.30 |
18370.00 |
0.0260 |
318.60 |
10010.00 |
0.0260 |
328.70 |
12340.00 |
0.0260 |
338.40 |
14390.00 |
0.0260 |
348.80 |
16410.00 |
0.0260 |
358.60 |
18110.00 |
0.0180 |
318.50 |
9870.00 |
0.0180 |
328.60 |
12090.00 |
0.0180 |
338.40 |
14110.00 |
0.0180 |
349.00 |
16040.00 |
0.0180 |
358.60 |
17540.00 |
0.0108 |
308.60 |
7890.00 |
0.0108 |
318.20 |
9710.00 |
0.0108 |
328.70 |
11920.00 |
0.0108 |
338.80 |
13820.00 |
0.0108 |
348.40 |
15460.00 |
0.0108 |
358.60 |
16890.00 |
0.0054 |
308.30 |
7870.00 |
0.0054 |
318.20 |
9570.00 |
0.0054 |
328.70 |
11540.00 |
0.0054 |
338.80 |
13150.00 |
0.0054 |
348.40 |
14440.00 |
0.0054 |
358.40 |
15620.00 |
0.0035 |
308.50 |
7890.00 |
0.0035 |
318.50 |
9470.00 |
0.0035 |
328.60 |
11180.00 |
0.0035 |
338.80 |
12660.00 |
0.0035 |
348.60 |
13850.00 |
0.0035 |
358.80 |
14810.00 |
Sources