- 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
- Glycerin
- InChI
- InChI=1S/C3H8O3/c4-1-3(6)2-5/h3-6H,1-2H2
- InChI Key
- PEDCQBHIVMGVHV-UHFFFAOYSA-N
- Formula
- C3H8O3
- SMILES
- OCC(O)CO
- Mol. Weight (g/mol)
- 92.09
- CAS
- 56-81-5
- Name
- 1-Hexanol, 2-ethyl-
- InChI
- InChI=1S/C8H18O/c1-3-5-6-8(4-2)7-9/h8-9H,3-7H2,1-2H3
- InChI Key
- YIWUKEYIRIRTPP-UHFFFAOYSA-N
- Formula
- C8H18O
- SMILES
- CCCCC(CC)CO
- Mol. Weight (g/mol)
- 130.23
- CAS
- 104-76-7
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Datasets
Vapor or sublimation pressure, kPa [ref]
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Mole fraction of Carbon dioxide (1) - Liquid | Mole fraction of 1-Hexanol, 2-ethyl- (3) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
| 343.00 | 0.5010 | 0.4940 | 9100.00 |
| 343.00 | 0.6020 | 0.3940 | 11480.00 |
| 343.00 | 0.7000 | 0.2970 | 13360.00 |
| 343.00 | 0.8010 | 0.1960 | 14900.00 |
| 353.00 | 0.5010 | 0.4940 | 9820.00 |
| 353.00 | 0.6020 | 0.3940 | 12580.00 |
| 353.00 | 0.7000 | 0.2970 | 14260.00 |
| 353.00 | 0.8010 | 0.1960 | 16170.00 |
| 368.00 | 0.5010 | 0.4940 | 10550.00 |
| 368.00 | 0.6020 | 0.3940 | 13680.00 |
| 368.00 | 0.7000 | 0.2970 | 15500.00 |
| 368.00 | 0.8010 | 0.1960 | 17500.00 |
| 383.00 | 0.5010 | 0.4940 | 11260.00 |
| 383.00 | 0.6020 | 0.3940 | 14420.00 |
| 383.00 | 0.7000 | 0.2970 | 16740.00 |
| 383.00 | 0.8010 | 0.1960 | 18500.00 |
| 393.00 | 0.5010 | 0.4940 | 11920.00 |
| 393.00 | 0.6020 | 0.3940 | 14960.00 |
| 393.00 | 0.7000 | 0.2970 | 17690.00 |
| 393.00 | 0.8010 | 0.1960 | 19000.00 |
Vapor or sublimation pressure, kPa [ref]
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Mole fraction of Carbon dioxide (1) - Liquid | Mole fraction of 1-Hexanol, 2-ethyl- (3) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
| 343.00 | 0.5010 | 0.4940 | 9100.00 |
| 343.00 | 0.6020 | 0.3940 | 11480.00 |
| 343.00 | 0.7000 | 0.2970 | 13360.00 |
| 343.00 | 0.8010 | 0.1960 | 14900.00 |
| 353.00 | 0.5010 | 0.4940 | 9820.00 |
| 353.00 | 0.6020 | 0.3940 | 12580.00 |
| 353.00 | 0.7000 | 0.2970 | 14260.00 |
| 353.00 | 0.8010 | 0.1960 | 16170.00 |
| 368.00 | 0.5010 | 0.4940 | 10550.00 |
| 368.00 | 0.6020 | 0.3940 | 13680.00 |
| 368.00 | 0.7000 | 0.2970 | 15500.00 |
| 368.00 | 0.8010 | 0.1960 | 17500.00 |
| 383.00 | 0.5010 | 0.4940 | 11260.00 |
| 383.00 | 0.6020 | 0.3940 | 14420.00 |
| 383.00 | 0.7000 | 0.2970 | 16740.00 |
| 383.00 | 0.8010 | 0.1960 | 18500.00 |
| 393.00 | 0.5010 | 0.4940 | 11920.00 |
| 393.00 | 0.6020 | 0.3940 | 14960.00 |
| 393.00 | 0.7000 | 0.2970 | 17690.00 |
| 393.00 | 0.8010 | 0.1960 | 19000.00 |
Vapor or sublimation pressure, kPa [ref]
Operational conditions:
- Mole fraction = 0.899 (Gas)
- Mole fraction = 0.099 (Gas)
| Temperature, K - Gas | Vapor or sublimation pressure, kPa - Gas |
|---|---|
| 343.00 | 15230.00 |
| 353.00 | 16570.00 |
| 368.00 | 17910.00 |
| 383.00 | 19070.00 |
| 393.00 | 20000.00 |
Vapor or sublimation pressure, kPa [ref]
Operational conditions:
- Mole fraction = 0.899 (Gas)
- Mole fraction = 0.099 (Gas)
| Temperature, K - Gas | Vapor or sublimation pressure, kPa - Gas |
|---|---|
| 343.00 | 15230.00 |
| 353.00 | 16570.00 |
| 368.00 | 17910.00 |
| 383.00 | 19070.00 |
| 393.00 | 20000.00 |