Dortmund Data Bank
Solid-Liquid Equilibrium Data
The experimental data shown in these pages are freely available and have been published already in the DDB Explorer Edition. The data represent a small sub list of all available data in the Dortmund Data Bank. For more data or any further information please search the DDB or contact DDBST.
Solid-Liquid Equilibrium Data Set 414
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4 |
16.043 |
74-82-8 |
Methane |
| 2 |
CO2 |
44.010 |
124-38-9 |
Carbon dioxide |
Search the DDB for all data of this mixture
Data Table
| T [K] |
P [bar] |
xL1 [mol/mol] |
| 210.15 |
42.2 |
0.30620 |
| 203.15 |
48.26 |
0.73070 |
| 193.15 |
42.885 |
0.88530 |
| 183.15 |
33.6 |
0.93500 |
| 173.15 |
24.662 |
0.95070 |
| 153.15 |
11.687 |
0.99192 |
(P - pressure, T - temperature, xl - liquid mole fraction)
Reference
| Source |
| Mraw S.C.; Hwang S.-C.; Kobayashi R.: The Vapor-Liquid Equilibrium of the CH4-CO2 System at Low Temperatures. GPA Research Rep. (1977) 1-18 |
Comment: SVLE
Solid-Liquid Equilibrium Data Set 418
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4 |
16.043 |
74-82-8 |
Methane |
| 2 |
CO2 |
44.010 |
124-38-9 |
Carbon dioxide |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
xL1 [mol/mol] |
| 129.65 |
0.99840 |
| 135.21 |
0.99750 |
| 139.43 |
0.99630 |
| 144.54 |
0.99420 |
| 150.37 |
0.99070 |
| 162.04 |
0.98170 |
| 169.87 |
0.97060 |
| 182.15 |
0.94150 |
| 189.26 |
0.89920 |
| 196.93 |
0.84610 |
| 201.26 |
0.79500 |
(P - pressure, T - temperature, xl - liquid mole fraction)
Reference
| Source |
| Davis J.A.; Rodewald N.; Kurata F.: Solid-Liquid-Vapor Phase Behavior of the Methane-Carbon Dioxide System. AIChE J. 8 (1962) 537-539 |
Solid-Liquid Equilibrium Data Set 437
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CO2 |
44.010 |
124-38-9 |
Carbon dioxide |
| 2 |
CH4 |
16.043 |
74-82-8 |
Methane |
Search the DDB for all data of this mixture
Data Table
| T [K] |
xL1 [mol/mol] |
| 126.40 |
0.000732 |
| 137.50 |
0.002366 |
(P - pressure, T - temperature, xl - liquid mole fraction)
Reference
| Source |
| Preston G.T.; Funk E.W.; Prausnitz J.M.: Solubilities of Hydrocarbons and Carbon Dioxide in Liquid Methane and in Liquid Argon. J.Phys.Chem. 75 (1971) 2345-2352 |
Diagrams
Solid-Liquid Equilibrium Data Overview
© DDBST GmbH
