Dortmund Data Bank
Excess Enthalpy 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.
Enthalpy of Mixing Data Set 12722
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
Miscibility gap: No
Constant Value
| Temperature |
293.150 |
K |
| Pressure |
5.070 |
bar |
Data Table
| hE [J/mol] |
x1 [mol/mol] |
| 17.900 |
0.25300 |
| 25.630 |
0.47700 |
| 26.390 |
0.50100 |
| 18.450 |
0.81600 |
(hE - excess enthalpy, x - liquid mole fraction)
Reference
| Source |
| Barry A.O.; Kaliaguine S.C.; Ramalho R.S.: Direct Determination of Enthalpy of Mixing for the Binary Gaseous System Methane-Carbon Dioxide by an Isothermal Flow Calorimeter. J.Chem.Eng.Data 27 (1982) 258-264 |
Enthalpy of Mixing Data Set 12723
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
Miscibility gap: No
Constant Value
| Temperature |
293.150 |
K |
| Pressure |
11.140 |
bar |
Data Table
| hE [J/mol] |
x1 [mol/mol] |
| 29.300 |
0.16900 |
| 46.980 |
0.31700 |
| 48.210 |
0.39300 |
| 47.720 |
0.44500 |
| 42.780 |
0.70700 |
| 21.950 |
0.88300 |
(hE - excess enthalpy, x - liquid mole fraction)
Reference
| Source |
| Barry A.O.; Kaliaguine S.C.; Ramalho R.S.: Direct Determination of Enthalpy of Mixing for the Binary Gaseous System Methane-Carbon Dioxide by an Isothermal Flow Calorimeter. J.Chem.Eng.Data 27 (1982) 258-264 |
Enthalpy of Mixing Data Set 12724
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
Miscibility gap: No
Constant Value
| Temperature |
293.150 |
K |
| Pressure |
15.200 |
bar |
Data Table
| hE [J/mol] |
x1 [mol/mol] |
| 36.820 |
0.16500 |
| 61.050 |
0.35800 |
| 62.540 |
0.50000 |
| 50.480 |
0.68900 |
| 33.780 |
0.82900 |
(hE - excess enthalpy, x - liquid mole fraction)
Reference
| Source |
| Barry A.O.; Kaliaguine S.C.; Ramalho R.S.: Direct Determination of Enthalpy of Mixing for the Binary Gaseous System Methane-Carbon Dioxide by an Isothermal Flow Calorimeter. J.Chem.Eng.Data 27 (1982) 258-264 |
Diagrams
List of All References
| Source |
| Barry A.O.; Kaliaguine S.C.; Ramalho R.S.: Direct Determination of Enthalpy of Mixing for the Binary Gaseous System Methane-Carbon Dioxide by an Isothermal Flow Calorimeter. J.Chem.Eng.Data 27 (1982) 258-264 |
Excess Enthalpy Data Overview
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