Experimental Data, Property Prediction
Introduction
Carbon dioxide (CO2) is one of the most important technically used components and by far the
chemical that has the highest production. Most of the carbon dioxide is not produced in the chemical industry but comes from
the combustion of mineral fuels in engines, power stations, and heating installations.
Carbon dioxide has become known even in the public in the last years because of the green house effect
carbon dioxide creates in higher layers of the atmosphere.
Carbon dioxide is also a product and by-product of several chemical and biological processes and
sometimes but rarely a reagent.
Carbon dioxide is a supercritical gas at normal conditions. Some of the basic properties are
| Property |
Value |
| Critical Temperature |
304 K |
| Critical Pressure |
7376 kPa |
| Critical Volume |
94 cm³/mol |
| Melting Temperature |
216 K |
| Normal Boiling Temperature |
185 K (Sublimation) |
| Molar Mass |
44.01 g/mol |
Carbon Dioxide is a component frequently measured. In the DDB it holds place 3 in the data
sets list behind water and benzene and place 2 in the data points list. For water the DDB contains more than 86000 data
sets and for carbon dioxide more than 18500 sets.
Overview
|
Databank |
Sets |
Points |
References |
| Adsorbent/adsorptive equilibria |
405 |
4135 |
47 |
| Activity coefficients at infinite dilution (binary systems) |
11 |
11 |
1 |
| Azeotropic/zeotropic information |
804 |
804 |
177 |
| Critical data of mixtures |
445 |
3743 |
163 |
| Gas solubilities (electrolyte containing systems) |
370 |
2060 |
34 |
| Vapor-liquid equilibria for systems containing solved salts |
40 |
416 |
4 |
| Salt solubilities |
83 |
775 |
20 |
| Gas solubilities |
2471 |
13657 |
422 |
| Heats of mixing |
887 |
12653 |
69 |
| Vapor-liquid equilibria |
9098 |
78571 |
1195 |
| Liquid-liquid equilibria |
382 |
2285 |
69 |
| Pure component properties |
1660 |
16992 |
419 |
| Thermophysical data for polymer mixtures |
625 |
9137 |
111 |
| Solid-liquid equilibria for systems without salts |
249 |
2206 |
58 |
| Densities and (excess) volumes of mixtures |
479 |
2875 |
28 |
| Different thermodynamic properties |
685 |
13734 |
63 |
| Sum |
18694 |
164054 |
(2880) |
The Dortmund Data Bank contains all data from the GPA reports and other technical publications.
Single Data Banks
Vapor-liquid equilibria
This data bank is by far the biggest. It
contains more than 9000 data sets for 1455 different mixtures
with carbon dixoide. This data bank contains pressure,
temperature, liquid and vapor compositions. Several data sets
are not complete (the vapor composition is missing) due to the
used measurement methods.
|
|
Azeotropic/zeotropic information
Most of the available data sets (90%) describe a zeotropic systems several of them telling that the
system is supercritical at a specific condition. Only 90 data sets are describing azeotropes for nine different systems.
|
|
Activity coefficients at infinite dilution (binary systems)
Activity coefficients at infinite dilutions are not an important property for carbons
dioxide since dioxide is supercritical at normal conditions. The DDB only contains therefore very few data points.
|
|
Gas solubilities
This data bank contains 463 different mixtures with carbon dioxide. 386 different solvents are
available. A lot of these data sets describe the solubility of carbon dioxide in amine solutions and some other alkaline
solvents. These data are of great importance in the gas sweetening processes in the natural gas processing industry,
refineries, and petrochemical plants. A new field of interest are CO2 reduced power plants.
|
|
Gas solubilities (electrolyte containing systems)
This data bank contains 51 different mixtures all with carbon dioxide and water but with different
electrolytes like sodium hydroxyde, ammonium chloride, potassium carbonate, and others.
|
|
Vapor-liquid equilibria for systems containing electrolytes
In this data bank sets for seven different
mixtures are available.
|
|
Liquid-liquid equilibria
This data banks contains information about miscibility gaps for 196 different mixtures.
|
|
Excess Enthalpies
This data bank contains data for 52 different systems mainly at elevated pressures.
|
|
Salt solubilities
This data bank contains data for 34 different
systems with solved carbon dioxide at elevated pressures and
mainly solubilities of carbonates.
|
|
Critical data of mixtures
This data bank contains data for 203 systems with carbon dioxide.
|
|
Adsorbent/adsorptive equilibria
The AAE data bank contains data about the amount of carbon dioxide adsorbed on zeolites, activated
carbons, silica gels, and other materials with microporous structures. Many data sets also contain a second or third
adsorptive.
|
 |
Solid-liquid equilibria
This data bank contains data (melting temperatures) for 84 different mixtures with carbon dioxide.
|
|
Densities and (excess) volumes of mixtures
This data bank contains data for 31 different mixture with carbon dioxide.
|
|
Thermophysical Data for Polymer Systems
The polymer data bank contains data for 163 different systems with carbon dioxide. These include
vapor-liquid and liquid-liquid equilibrium data with different polymers, gas solubilities, P-v-T related data and polymer
swelling data.
|
|
Different thermodynamic properties
This data bank contains 116 different mixtures with carbon dioxide. The list of
properties is very wide-spread since this data bank also contains data type normally found in other data banks but can't
be stored there because of limitations in the data bank formats.
|
|
Pure component properties
The PCP data banks contains a variety of data for the pure carbon dioxide. The most important are listed below:
| Property |
Sets |
Points |
References |
| Dynamic Viscosity |
347 |
2809 |
79 |
| Vapor Pressure |
132 |
1252 |
102 |
| Critical Data |
57 |
57 |
51 |
| Triple Point |
5 |
9 |
5 |
| Kinematic Viscosity |
104 |
120 |
2 |
| Density |
568 |
7948 |
93 |
| Melting Point |
14 |
35 |
14 |
| Molar Heat Capacity (cP) |
165 |
835 |
16 |
| Virial Coefficients |
38 |
201 |
35 |
Thermal Conductivity |
105 |
1309 |
61 |
| Molar Heat Capacity (cV) |
54 |
1073 |
7 |
| Ideal Gas Heat Capacity |
8 |
287 |
8 |
| Dielectric Constant |
3 |
27 |
2 |
| Speed of Sound |
24 |
439 |
4 |
Property Prediction
The state-of-the-art prediction method is the PSRK (Predictive Soave-Redlich-Kwong) method. PSRK
is a combination of the group contribution method UNIFAC with the SRK equation of state. This combination allows the
prediction of systems with supercritical components like carbon dioxide.
Scientific Papers
| 2004 | Experimental Determination of Carbon Dioxide Solubility Data in Aqueous Alkanolamine Solutions | Sidi-Boumedine R., Horstmann S., Fischer K., Provost E., Fuerst W., Gmehling J. | Journal | Fluid Phase Equilib., 218, 1, 85 94 (2004) |
| 2003 | Experimental Determination and Prediction of Gas Solubility Data for CO2 + H2O Mixtures Containing NaNO3 or KNO3 | Kiepe J., Horstmann S., Fischer K., Gmehling J. | Journal | Ind.Eng.Chem.Res., 42, 16, 3851 3856 (2003) |
| 2002 | Compressed Liquid Densities and Excess Volumes for the Binary Systems Carbon Dioxide + 1-Propanol and Carbon Dioxide + 2-Propanol Using a Vibrating Tube Densimeter up to 25 MPa | Zuniga-Moreno A., Galicia-Luna L.A., Horstmann S., Ihmels C., Gmehling J. | Journal | J.Chem.Eng.Data, 47, 6, 1418 1424 (2002) |
| 2002 | Experimental Determination and Prediction of Gas Solubility Data for CO2 + H2O Mixtures Containing NaCl or KCl at Temperatures between 313 and 393 K and Pressures up to 10 MPa | Kiepe J., Horstmann S., Fischer K., Gmehling J. | Journal | Ind.Eng.Chem.Res., 41, 17, 4393 4398 (2002) |
| 2002 | Solubility of H2S and CO2 in N-Octyl-2-pyrrolidone and of H2S in Methanol and Benzene | Fischer K., Chen J., Petri M., Gmehling J. | Journal | AIChE J., 48, 4, 887 893 (2002) |
| 2001 | Densities of Toluene, Carbon Dioxide, Carbonyl Sulfide, and Hydrogen Sulfide over a Wide Temperature and Pressure Range in the Sub- and Supercritical State | Ihmels E.C., Gmehling J. | Journal | Ind.Eng.Chem.Res., 40, 20, 4470 4477 (2001) |
| 2000 | Experimental Determination of the Critical Line for (Carbon Dioxide + Ethane) and Calculation of Various Thermodynamic Properties for (Carbon Dioxide + n-Alkane) using the PSRK Model | Horstmann S., Fischer K., Gmehling J., Kolar P. | Journal | J.Chem.Thermodyn., 32, 7, 451 464 (2000) |
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