Mixture of Carbon dioxide + Dodecanoic acid + Methyl Alcohol
Datasets
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
Ttriple - Triple point temperature, K (2)
-
Vapor or sublimation pressure, kPa (6)
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid mixture 1 |
Mole fraction of Methyl Alcohol (3) - Liquid mixture 1 |
Temperature, K - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
0.8248 |
0.1168 |
303.32 |
8140.00 |
0.8590 |
0.0940 |
303.28 |
9040.00 |
0.8886 |
0.0743 |
303.03 |
9790.00 |
0.9194 |
0.0537 |
303.60 |
9060.00 |
0.9642 |
0.0239 |
303.28 |
9050.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid mixture 1 |
Mole fraction of Methyl Alcohol (3) - Liquid mixture 1 |
Temperature, K - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
0.8248 |
0.1168 |
303.32 |
8140.00 |
0.8590 |
0.0940 |
303.28 |
9040.00 |
0.8886 |
0.0743 |
303.03 |
9790.00 |
0.9194 |
0.0537 |
303.60 |
9060.00 |
0.9642 |
0.0239 |
303.28 |
9050.00 |
Triple point temperature, K
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid mixture 1 |
Mole fraction of Methyl Alcohol (3) - Liquid mixture 1 |
Triple point temperature, K - Gas |
0.8248 |
0.1168 |
303.38 |
0.8590 |
0.0940 |
303.55 |
0.8886 |
0.0743 |
303.18 |
0.9194 |
0.0537 |
303.48 |
0.9642 |
0.0239 |
303.02 |
Triple point temperature, K
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid mixture 1 |
Mole fraction of Methyl Alcohol (3) - Liquid mixture 1 |
Triple point temperature, K - Gas |
0.8248 |
0.1168 |
303.38 |
0.8590 |
0.0940 |
303.55 |
0.8886 |
0.0743 |
303.18 |
0.9194 |
0.0537 |
303.48 |
0.9642 |
0.0239 |
303.02 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid mixture 1 |
Mole fraction of Methyl Alcohol (3) - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Gas |
0.8248 |
0.1168 |
6420.00 |
0.8590 |
0.0940 |
6360.00 |
0.8886 |
0.0743 |
6630.00 |
0.9194 |
0.0537 |
6320.00 |
0.9642 |
0.0239 |
6250.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Methyl Alcohol (3) - Liquid |
Temperature, K - Gas |
Vapor or sublimation pressure, kPa - Gas |
0.3414 |
0.5488 |
313.45 |
5690.00 |
0.3414 |
0.5488 |
323.35 |
6590.00 |
0.3414 |
0.5488 |
333.05 |
7500.00 |
0.3414 |
0.5488 |
343.15 |
8530.00 |
0.5598 |
0.3668 |
303.55 |
5960.00 |
0.5598 |
0.3668 |
313.22 |
7330.00 |
0.5598 |
0.3668 |
323.42 |
8820.00 |
0.5598 |
0.3668 |
333.15 |
10400.00 |
0.5598 |
0.3668 |
343.12 |
12030.00 |
0.7474 |
0.2105 |
303.58 |
6540.00 |
0.7474 |
0.2105 |
313.32 |
8110.00 |
0.7474 |
0.2105 |
323.18 |
10520.00 |
0.7474 |
0.2105 |
332.95 |
12700.00 |
0.7474 |
0.2105 |
343.08 |
14760.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Methyl Alcohol (3) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Gas |
0.4617 |
0.3589 |
313.38 |
6140.00 |
0.4617 |
0.3589 |
323.25 |
7220.00 |
0.4617 |
0.3589 |
333.02 |
8300.00 |
0.4617 |
0.3589 |
343.05 |
9470.00 |
0.5710 |
0.2860 |
303.48 |
5650.00 |
0.5710 |
0.2860 |
313.58 |
7210.00 |
0.5710 |
0.2860 |
323.45 |
8740.00 |
0.5710 |
0.2860 |
333.22 |
10290.00 |
0.5710 |
0.2860 |
342.92 |
11910.00 |
0.6675 |
0.2217 |
303.55 |
6420.00 |
0.6675 |
0.2217 |
313.38 |
8160.00 |
0.6675 |
0.2217 |
323.25 |
10160.00 |
0.6675 |
0.2217 |
333.32 |
12400.00 |
0.6675 |
0.2217 |
343.05 |
14470.00 |
0.7492 |
0.1672 |
303.40 |
6340.00 |
0.7492 |
0.1672 |
313.42 |
9310.00 |
0.7492 |
0.1672 |
323.18 |
11890.00 |
0.7492 |
0.1672 |
333.25 |
14310.00 |
0.7492 |
0.1672 |
343.25 |
16540.00 |
0.8248 |
0.1168 |
313.28 |
10960.00 |
0.8248 |
0.1168 |
323.12 |
13600.00 |
0.8248 |
0.1168 |
333.28 |
16120.00 |
0.8248 |
0.1168 |
343.15 |
18250.00 |
0.8590 |
0.0940 |
313.55 |
11650.00 |
0.8590 |
0.0940 |
323.22 |
14300.00 |
0.8590 |
0.0940 |
333.05 |
16610.00 |
0.8590 |
0.0940 |
343.22 |
18880.00 |
0.8886 |
0.0743 |
313.28 |
12460.00 |
0.8886 |
0.0743 |
322.88 |
14890.00 |
0.8886 |
0.0743 |
332.82 |
17230.00 |
0.8886 |
0.0743 |
343.02 |
19400.00 |
0.9194 |
0.0537 |
303.48 |
6320.00 |
0.9194 |
0.0537 |
303.60 |
9060.00 |
0.9194 |
0.0537 |
313.08 |
11700.00 |
0.9194 |
0.0537 |
323.75 |
14590.00 |
0.9194 |
0.0537 |
333.08 |
16900.00 |
0.9194 |
0.0537 |
343.08 |
19220.00 |
0.9479 |
0.0347 |
313.15 |
12160.00 |
0.9479 |
0.0347 |
323.15 |
14780.00 |
0.9479 |
0.0347 |
333.15 |
17180.00 |
0.9479 |
0.0347 |
343.15 |
19290.00 |
0.9642 |
0.0239 |
303.02 |
6250.00 |
0.9642 |
0.0239 |
303.28 |
9050.00 |
0.9642 |
0.0239 |
313.15 |
11480.00 |
0.9642 |
0.0239 |
323.15 |
14200.00 |
0.9642 |
0.0239 |
333.15 |
16690.00 |
0.9642 |
0.0239 |
343.15 |
18610.00 |
0.9745 |
0.0170 |
313.15 |
11190.00 |
0.9745 |
0.0170 |
323.15 |
13920.00 |
0.9745 |
0.0170 |
333.15 |
16270.00 |
0.9745 |
0.0170 |
343.15 |
18280.00 |
0.9895 |
0.0070 |
303.02 |
6770.00 |
0.9895 |
0.0070 |
313.25 |
9440.00 |
0.9895 |
0.0070 |
323.05 |
11840.00 |
0.9895 |
0.0070 |
332.88 |
13920.00 |
0.9895 |
0.0070 |
342.85 |
15740.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid mixture 1 |
Mole fraction of Methyl Alcohol (3) - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Gas |
0.8248 |
0.1168 |
6420.00 |
0.8590 |
0.0940 |
6360.00 |
0.8886 |
0.0743 |
6630.00 |
0.9194 |
0.0537 |
6320.00 |
0.9642 |
0.0239 |
6250.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Methyl Alcohol (3) - Liquid |
Temperature, K - Gas |
Vapor or sublimation pressure, kPa - Gas |
0.3414 |
0.5488 |
313.45 |
5690.00 |
0.3414 |
0.5488 |
323.35 |
6590.00 |
0.3414 |
0.5488 |
333.05 |
7500.00 |
0.3414 |
0.5488 |
343.15 |
8530.00 |
0.5598 |
0.3668 |
303.55 |
5960.00 |
0.5598 |
0.3668 |
313.22 |
7330.00 |
0.5598 |
0.3668 |
323.42 |
8820.00 |
0.5598 |
0.3668 |
333.15 |
10400.00 |
0.5598 |
0.3668 |
343.12 |
12030.00 |
0.7474 |
0.2105 |
303.58 |
6540.00 |
0.7474 |
0.2105 |
313.32 |
8110.00 |
0.7474 |
0.2105 |
323.18 |
10520.00 |
0.7474 |
0.2105 |
332.95 |
12700.00 |
0.7474 |
0.2105 |
343.08 |
14760.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Methyl Alcohol (3) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Gas |
0.4617 |
0.3589 |
313.38 |
6140.00 |
0.4617 |
0.3589 |
323.25 |
7220.00 |
0.4617 |
0.3589 |
333.02 |
8300.00 |
0.4617 |
0.3589 |
343.05 |
9470.00 |
0.5710 |
0.2860 |
303.48 |
5650.00 |
0.5710 |
0.2860 |
313.58 |
7210.00 |
0.5710 |
0.2860 |
323.45 |
8740.00 |
0.5710 |
0.2860 |
333.22 |
10290.00 |
0.5710 |
0.2860 |
342.92 |
11910.00 |
0.6675 |
0.2217 |
303.55 |
6420.00 |
0.6675 |
0.2217 |
313.38 |
8160.00 |
0.6675 |
0.2217 |
323.25 |
10160.00 |
0.6675 |
0.2217 |
333.32 |
12400.00 |
0.6675 |
0.2217 |
343.05 |
14470.00 |
0.7492 |
0.1672 |
303.40 |
6340.00 |
0.7492 |
0.1672 |
313.42 |
9310.00 |
0.7492 |
0.1672 |
323.18 |
11890.00 |
0.7492 |
0.1672 |
333.25 |
14310.00 |
0.7492 |
0.1672 |
343.25 |
16540.00 |
0.8248 |
0.1168 |
313.28 |
10960.00 |
0.8248 |
0.1168 |
323.12 |
13600.00 |
0.8248 |
0.1168 |
333.28 |
16120.00 |
0.8248 |
0.1168 |
343.15 |
18250.00 |
0.8590 |
0.0940 |
313.55 |
11650.00 |
0.8590 |
0.0940 |
323.22 |
14300.00 |
0.8590 |
0.0940 |
333.05 |
16610.00 |
0.8590 |
0.0940 |
343.22 |
18880.00 |
0.8886 |
0.0743 |
313.28 |
12460.00 |
0.8886 |
0.0743 |
322.88 |
14890.00 |
0.8886 |
0.0743 |
332.82 |
17230.00 |
0.8886 |
0.0743 |
343.02 |
19400.00 |
0.9194 |
0.0537 |
303.48 |
6320.00 |
0.9194 |
0.0537 |
303.60 |
9060.00 |
0.9194 |
0.0537 |
313.08 |
11700.00 |
0.9194 |
0.0537 |
323.75 |
14590.00 |
0.9194 |
0.0537 |
333.08 |
16900.00 |
0.9194 |
0.0537 |
343.08 |
19220.00 |
0.9479 |
0.0347 |
313.15 |
12160.00 |
0.9479 |
0.0347 |
323.15 |
14780.00 |
0.9479 |
0.0347 |
333.15 |
17180.00 |
0.9479 |
0.0347 |
343.15 |
19290.00 |
0.9642 |
0.0239 |
303.02 |
6250.00 |
0.9642 |
0.0239 |
303.28 |
9050.00 |
0.9642 |
0.0239 |
313.15 |
11480.00 |
0.9642 |
0.0239 |
323.15 |
14200.00 |
0.9642 |
0.0239 |
333.15 |
16690.00 |
0.9642 |
0.0239 |
343.15 |
18610.00 |
0.9745 |
0.0170 |
313.15 |
11190.00 |
0.9745 |
0.0170 |
323.15 |
13920.00 |
0.9745 |
0.0170 |
333.15 |
16270.00 |
0.9745 |
0.0170 |
343.15 |
18280.00 |
0.9895 |
0.0070 |
303.02 |
6770.00 |
0.9895 |
0.0070 |
313.25 |
9440.00 |
0.9895 |
0.0070 |
323.05 |
11840.00 |
0.9895 |
0.0070 |
332.88 |
13920.00 |
0.9895 |
0.0070 |
342.85 |
15740.00 |
Sources