- Name
- Carbon dioxide
- InChI
- InChI=1S/CO2/c2-1-3
- InChI Key
- CURLTUGMZLYLDI-UHFFFAOYSA-N
- Formula
- CO2
- SMILES
- O=C=O
- Mol. Weight (g/mol)
- 44.01
- CAS
- 124-38-9
- Name
- Octadecane
- InChI
- InChI=1S/C18H38/c1-3-5-7-9-11-13-15-17-18-16-14-12-10-8-6-4-2/h3-18H2,1-2H3
- InChI Key
- RZJRJXONCZWCBN-UHFFFAOYSA-N
- Formula
- C18H38
- SMILES
- CCCCCCCCCCCCCCCCCC
- Mol. Weight (g/mol)
- 254.50
- CAS
- 593-45-3
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Datasets
Mole fraction of Carbon dioxide (1) [ref]
Operational condition: Temperature, K = 323.1 (Liquid)
| Pressure, kPa - Liquid | Mole fraction of Carbon dioxide (1) - Liquid |
|---|---|
| 990.00 | 0.1030 |
| 2020.00 | 0.2040 |
| 3020.00 | 0.2940 |
| 4000.00 | 0.3660 |
| 4960.00 | 0.4420 |
| 5960.00 | 0.4920 |
Mole fraction of Carbon dioxide (1) [ref]
Operational condition: Temperature, K = 323.1 (Liquid)
| Pressure, kPa - Liquid | Mole fraction of Carbon dioxide (1) - Liquid |
|---|---|
| 990.00 | 0.1030 |
| 2020.00 | 0.2040 |
| 3020.00 | 0.2940 |
| 4000.00 | 0.3660 |
| 4960.00 | 0.4420 |
| 5960.00 | 0.4920 |
Viscosity, Pa*s [ref]
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Mole fraction of Carbon dioxide (1) - Liquid | Viscosity, Pa*s - Liquid |
| 950.00 | 0.0820 | 0.0010 |
| 2010.00 | 0.1520 | 0.0009 |
| 3080.00 | 0.2190 | 0.0008 |
| 4050.00 | 0.2780 | 0.0008 |
| 5080.00 | 0.3380 | 0.0007 |
| 5990.00 | 0.3780 | 0.0006 |
Viscosity, Pa*s [ref]
Operational condition: Temperature, K = 323.1 (Liquid)
| Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
|---|---|
| 990.00 | 0.0019 |
| 2020.00 | 0.0017 |
| 3020.00 | 0.0015 |
| 4000.00 | 0.0014 |
| 4960.00 | 0.0011 |
| 5960.00 | 0.0010 |
Viscosity, Pa*s [ref]
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Mole fraction of Carbon dioxide (1) - Liquid | Viscosity, Pa*s - Liquid |
| 950.00 | 0.0820 | 0.0010 |
| 2010.00 | 0.1520 | 0.0009 |
| 3080.00 | 0.2190 | 0.0008 |
| 4050.00 | 0.2780 | 0.0008 |
| 5080.00 | 0.3380 | 0.0007 |
| 5990.00 | 0.3780 | 0.0006 |
Viscosity, Pa*s [ref]
Operational condition: Temperature, K = 323.1 (Liquid)
| Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
|---|---|
| 990.00 | 0.0019 |
| 2020.00 | 0.0017 |
| 3020.00 | 0.0015 |
| 4000.00 | 0.0014 |
| 4960.00 | 0.0011 |
| 5960.00 | 0.0010 |
Interfacial tension, N/m [ref]
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Interfacial tension, N/m - Liquid |
| 323.15 | 410.00 | 0.0233 |
| 323.15 | 1300.00 | 0.0212 |
| 323.15 | 2000.00 | 0.0185 |
| 323.15 | 2670.00 | 0.0171 |
| 323.15 | 3200.00 | 0.0156 |
| 323.15 | 4000.00 | 0.0141 |
| 323.15 | 5100.00 | 0.0119 |
| 323.15 | 6250.00 | 0.0098 |
| 323.15 | 7000.00 | 0.0086 |
| 323.15 | 8150.00 | 0.0051 |
| 323.15 | 9100.00 | 0.0032 |
| 323.15 | 10100.00 | 0.0018 |
| 353.15 | 400.00 | 0.0200 |
| 353.15 | 1100.00 | 0.0192 |
| 353.15 | 2200.00 | 0.0177 |
| 353.15 | 3300.00 | 0.0162 |
| 353.15 | 4180.00 | 0.0151 |
| 353.15 | 5300.00 | 0.0139 |
| 353.15 | 6150.00 | 0.0129 |
| 353.15 | 7200.00 | 0.0118 |
| 353.15 | 8100.00 | 0.0107 |
| 353.15 | 9300.00 | 0.0097 |
| 353.15 | 10100.00 | 0.0089 |
| 353.15 | 11100.00 | 0.0077 |
| 353.15 | 12100.00 | 0.0066 |
| 353.15 | 13000.00 | 0.0057 |
| 353.15 | 14000.00 | 0.0049 |
| 353.15 | 15000.00 | 0.0040 |
| 353.15 | 16300.00 | 0.0031 |
| 353.15 | 17400.00 | 0.0025 |
Interfacial tension, N/m [ref]
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Interfacial tension, N/m - Liquid |
| 323.15 | 410.00 | 0.0233 |
| 323.15 | 1300.00 | 0.0212 |
| 323.15 | 2000.00 | 0.0185 |
| 323.15 | 2670.00 | 0.0171 |
| 323.15 | 3200.00 | 0.0156 |
| 323.15 | 4000.00 | 0.0141 |
| 323.15 | 5100.00 | 0.0119 |
| 323.15 | 6250.00 | 0.0098 |
| 323.15 | 7000.00 | 0.0086 |
| 323.15 | 8150.00 | 0.0051 |
| 323.15 | 9100.00 | 0.0032 |
| 323.15 | 10100.00 | 0.0018 |
| 353.15 | 400.00 | 0.0200 |
| 353.15 | 1100.00 | 0.0192 |
| 353.15 | 2200.00 | 0.0177 |
| 353.15 | 3300.00 | 0.0162 |
| 353.15 | 4180.00 | 0.0151 |
| 353.15 | 5300.00 | 0.0139 |
| 353.15 | 6150.00 | 0.0129 |
| 353.15 | 7200.00 | 0.0118 |
| 353.15 | 8100.00 | 0.0107 |
| 353.15 | 9300.00 | 0.0097 |
| 353.15 | 10100.00 | 0.0089 |
| 353.15 | 11100.00 | 0.0077 |
| 353.15 | 12100.00 | 0.0066 |
| 353.15 | 13000.00 | 0.0057 |
| 353.15 | 14000.00 | 0.0049 |
| 353.15 | 15000.00 | 0.0040 |
| 353.15 | 16300.00 | 0.0031 |
| 353.15 | 17400.00 | 0.0025 |
Mass density, kg/m3 [ref]
Operational condition: Temperature, K = 372.8 (Liquid)
| Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 950.00 | 729.0 |
| 2010.00 | 730.1 |
| 3080.00 | 731.4 |
| 4050.00 | 732.6 |
| 5080.00 | 734.2 |
| 5990.00 | 735.3 |
Mass density, kg/m3 [ref]
Operational condition: Temperature, K = 323.1 (Liquid)
| Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 990.00 | 763.8 |
| 2020.00 | 766.4 |
| 3020.00 | 769.4 |
| 4000.00 | 771.9 |
| 4960.00 | 775.0 |
| 5960.00 | 777.7 |
Mass density, kg/m3 [ref]
Operational condition: Temperature, K = 372.8 (Liquid)
| Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 950.00 | 729.0 |
| 2010.00 | 730.1 |
| 3080.00 | 731.4 |
| 4050.00 | 732.6 |
| 5080.00 | 734.2 |
| 5990.00 | 735.3 |
Mass density, kg/m3 [ref]
Operational condition: Temperature, K = 323.1 (Liquid)
| Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 990.00 | 763.8 |
| 2020.00 | 766.4 |
| 3020.00 | 769.4 |
| 4000.00 | 771.9 |
| 4960.00 | 775.0 |
| 5960.00 | 777.7 |
Sources
- Experimental results and thermodynamic investigation of carbon dioxide solubility in heavy liquid hydrocarbons and corresponding phase properties
- Interfacial Tension Measurement and Calculation of (Carbon Dioxide + n-Alkane) Binary Mixtures
- Equilibrium Properties of (Carbon Dioxide + n-Decane + n-Octadecane) Systems: Experiments and Thermodynamic Modeling
Note: These property values are available through the Cheméo API. A free account gives you an access key.