- Name
- Cyclohexanol
- InChI
- InChI=1S/C6H12O/c7-6-4-2-1-3-5-6/h6-7H,1-5H2
- InChI Key
- HPXRVTGHNJAIIH-UHFFFAOYSA-N
- Formula
- C6H12O
- SMILES
- OC1CCCCC1
- Mol. Weight (g/mol)
- 100.16
- CAS
- 108-93-0
- 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
- Cyclohexane
- InChI
- InChI=1S/C6H12/c1-2-4-6-5-3-1/h1-6H2
- InChI Key
- XDTMQSROBMDMFD-UHFFFAOYSA-N
- Formula
- C6H12
- SMILES
- C1CCCCC1
- Mol. Weight (g/mol)
- 84.16
- CAS
- 110-82-7
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Datasets
Vapor or sublimation pressure, kPa [ref]
Operational condition: Solvent: Mole fraction = 0.5 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Vapor or sublimation pressure, kPa - Liquid mixture 1 |
|---|---|
| 293.00 | 5120.00 |
| 293.00 | 4880.00 |
| 293.00 | 5100.00 |
| 293.00 | 4890.00 |
| 293.00 | 4830.00 |
| 293.00 | 5040.00 |
| 293.00 | 4950.00 |
| 303.00 | 6310.00 |
| 303.00 | 6390.00 |
| 303.00 | 5980.00 |
| 303.00 | 6290.00 |
| 303.00 | 6250.00 |
| 313.00 | 7610.00 |
| 313.00 | 7700.00 |
| 313.00 | 7680.00 |
| 313.00 | 7340.00 |
| 313.00 | 7510.00 |
| 323.00 | 8990.00 |
| 323.00 | 8990.00 |
| 323.00 | 8890.00 |
Vapor or sublimation pressure, kPa [ref]
Operational condition: Solvent: Mole fraction = 0.5 (Liquid mixture 1)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Carbon dioxide (2) - Liquid mixture 1 | Temperature, K - Liquid mixture 1 | Vapor or sublimation pressure, kPa - Liquid mixture 1 |
| 0.7577 | 293.00 | 6390.00 |
| 0.7802 | 293.00 | 8080.00 |
| 0.8290 | 293.00 | 12030.00 |
| 0.8290 | 303.00 | 7750.00 |
| 0.8290 | 313.00 | 7480.00 |
| 0.8622 | 293.00 | 14270.00 |
| 0.8622 | 303.00 | 9190.00 |
| 0.8622 | 313.00 | 8640.00 |
| 0.8622 | 323.00 | 9580.00 |
| 0.8926 | 293.00 | 11920.00 |
| 0.8926 | 303.00 | 8850.00 |
| 0.8926 | 313.00 | 8850.00 |
| 0.8926 | 323.00 | 9940.00 |
| 0.9219 | 293.00 | 9900.00 |
| 0.9219 | 303.00 | 8010.00 |
| 0.9219 | 313.00 | 8690.00 |
| 0.9219 | 323.00 | 10000.00 |
| 0.9494 | 293.00 | 6040.00 |
| 0.9494 | 303.00 | 6570.00 |
| 0.9494 | 313.00 | 8100.00 |
Vapor or sublimation pressure, kPa [ref]
Operational condition: Solvent: Mole fraction = 0.5 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Carbon dioxide (2) - Liquid | Temperature, K - Liquid | Vapor or sublimation pressure, kPa - Liquid |
| 0.4730 | 293.00 | 4450.00 |
| 0.4730 | 303.00 | 5260.00 |
| 0.4730 | 313.00 | 6090.00 |
| 0.4730 | 323.00 | 6880.00 |
| 0.4730 | 333.00 | 7630.00 |
| 0.4730 | 343.00 | 8360.00 |
| 0.6750 | 293.00 | 4770.00 |
| 0.6750 | 303.00 | 5910.00 |
| 0.6750 | 313.00 | 6930.00 |
| 0.6750 | 323.00 | 8140.00 |
| 0.6750 | 333.00 | 9440.00 |
| 0.6750 | 343.00 | 10440.00 |
| 0.7577 | 303.00 | 5990.00 |
| 0.7577 | 313.00 | 7160.00 |
| 0.7577 | 323.00 | 8430.00 |
| 0.7577 | 333.00 | 9770.00 |
| 0.7577 | 343.00 | 11150.00 |
| 0.7802 | 303.00 | 6030.00 |
| 0.7802 | 313.00 | 7270.00 |
| 0.7802 | 323.00 | 8610.00 |
| 0.7802 | 333.00 | 10000.00 |
| 0.7802 | 343.00 | 11440.00 |
| 0.8290 | 323.00 | 8590.00 |
| 0.8290 | 333.00 | 10180.00 |
| 0.8290 | 343.00 | 11690.00 |
| 0.9754 | 293.00 | 5370.00 |
| 0.9754 | 303.00 | 6700.00 |
| 0.9754 | 313.00 | 8060.00 |
Vapor or sublimation pressure, kPa [ref]
Operational condition: Solvent: Mole fraction = 0.5 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Vapor or sublimation pressure, kPa - Liquid mixture 1 |
|---|---|
| 293.00 | 5120.00 |
| 293.00 | 4880.00 |
| 293.00 | 5100.00 |
| 293.00 | 4890.00 |
| 293.00 | 4830.00 |
| 293.00 | 5040.00 |
| 293.00 | 4950.00 |
| 303.00 | 6310.00 |
| 303.00 | 6390.00 |
| 303.00 | 5980.00 |
| 303.00 | 6290.00 |
| 303.00 | 6250.00 |
| 313.00 | 7610.00 |
| 313.00 | 7700.00 |
| 313.00 | 7680.00 |
| 313.00 | 7340.00 |
| 313.00 | 7510.00 |
| 323.00 | 8990.00 |
| 323.00 | 8990.00 |
| 323.00 | 8890.00 |
Vapor or sublimation pressure, kPa [ref]
Operational condition: Solvent: Mole fraction = 0.5 (Liquid mixture 1)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Carbon dioxide (2) - Liquid mixture 1 | Temperature, K - Liquid mixture 1 | Vapor or sublimation pressure, kPa - Liquid mixture 1 |
| 0.7577 | 293.00 | 6390.00 |
| 0.7802 | 293.00 | 8080.00 |
| 0.8290 | 293.00 | 12030.00 |
| 0.8290 | 303.00 | 7750.00 |
| 0.8290 | 313.00 | 7480.00 |
| 0.8622 | 293.00 | 14270.00 |
| 0.8622 | 303.00 | 9190.00 |
| 0.8622 | 313.00 | 8640.00 |
| 0.8622 | 323.00 | 9580.00 |
| 0.8926 | 293.00 | 11920.00 |
| 0.8926 | 303.00 | 8850.00 |
| 0.8926 | 313.00 | 8850.00 |
| 0.8926 | 323.00 | 9940.00 |
| 0.9219 | 293.00 | 9900.00 |
| 0.9219 | 303.00 | 8010.00 |
| 0.9219 | 313.00 | 8690.00 |
| 0.9219 | 323.00 | 10000.00 |
| 0.9494 | 293.00 | 6040.00 |
| 0.9494 | 303.00 | 6570.00 |
| 0.9494 | 313.00 | 8100.00 |
Vapor or sublimation pressure, kPa [ref]
Operational condition: Solvent: Mole fraction = 0.5 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Carbon dioxide (2) - Liquid | Temperature, K - Liquid | Vapor or sublimation pressure, kPa - Liquid |
| 0.4730 | 293.00 | 4450.00 |
| 0.4730 | 303.00 | 5260.00 |
| 0.4730 | 313.00 | 6090.00 |
| 0.4730 | 323.00 | 6880.00 |
| 0.4730 | 333.00 | 7630.00 |
| 0.4730 | 343.00 | 8360.00 |
| 0.6750 | 293.00 | 4770.00 |
| 0.6750 | 303.00 | 5910.00 |
| 0.6750 | 313.00 | 6930.00 |
| 0.6750 | 323.00 | 8140.00 |
| 0.6750 | 333.00 | 9440.00 |
| 0.6750 | 343.00 | 10440.00 |
| 0.7577 | 303.00 | 5990.00 |
| 0.7577 | 313.00 | 7160.00 |
| 0.7577 | 323.00 | 8430.00 |
| 0.7577 | 333.00 | 9770.00 |
| 0.7577 | 343.00 | 11150.00 |
| 0.7802 | 303.00 | 6030.00 |
| 0.7802 | 313.00 | 7270.00 |
| 0.7802 | 323.00 | 8610.00 |
| 0.7802 | 333.00 | 10000.00 |
| 0.7802 | 343.00 | 11440.00 |
| 0.8290 | 323.00 | 8590.00 |
| 0.8290 | 333.00 | 10180.00 |
| 0.8290 | 343.00 | 11690.00 |
| 0.9754 | 293.00 | 5370.00 |
| 0.9754 | 303.00 | 6700.00 |
| 0.9754 | 313.00 | 8060.00 |
Vapor or sublimation pressure, kPa [ref]
Operational condition: Solvent: Mole fraction = 0.5 (Gas)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Carbon dioxide (2) - Gas | Temperature, K - Gas | Vapor or sublimation pressure, kPa - Gas |
| 0.8622 | 333.00 | 10890.00 |
| 0.8622 | 343.00 | 12280.00 |
| 0.8926 | 333.00 | 11350.00 |
| 0.8926 | 343.00 | 12690.00 |
| 0.9219 | 333.00 | 11480.00 |
| 0.9219 | 343.00 | 12820.00 |
| 0.9494 | 323.00 | 9790.00 |
| 0.9494 | 333.00 | 11320.00 |
| 0.9494 | 343.00 | 12560.00 |
| 0.9754 | 323.00 | 9700.00 |
| 0.9754 | 333.00 | 11040.00 |
| 0.9754 | 343.00 | 12020.00 |
Vapor or sublimation pressure, kPa [ref]
Operational condition: Solvent: Mole fraction = 0.5 (Gas)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Carbon dioxide (2) - Gas | Temperature, K - Gas | Vapor or sublimation pressure, kPa - Gas |
| 0.8622 | 333.00 | 10890.00 |
| 0.8622 | 343.00 | 12280.00 |
| 0.8926 | 333.00 | 11350.00 |
| 0.8926 | 343.00 | 12690.00 |
| 0.9219 | 333.00 | 11480.00 |
| 0.9219 | 343.00 | 12820.00 |
| 0.9494 | 323.00 | 9790.00 |
| 0.9494 | 333.00 | 11320.00 |
| 0.9494 | 343.00 | 12560.00 |
| 0.9754 | 323.00 | 9700.00 |
| 0.9754 | 333.00 | 11040.00 |
| 0.9754 | 343.00 | 12020.00 |