- 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
- Caryophyllene
- InChI
- InChI=1S/C15H24/c1-11-6-5-7-12(2)13-10-15(3,4)14(13)9-8-11/h6,13-14H,2,5,7-10H2,1,3-4H3/b11-6+/t13-,14-/m0/s1
- InChI Key
- NPNUFJAVOOONJE-IOMPXFEGSA-N
- Formula
- C15H24
- SMILES
- C=C1CCC=C(C)CCC2C1CC2(C)C
- Mol. Weight (g/mol)
- 204.35
- CAS
- 87-44-5
- Name
- Humulene
- InChI
- InChI=1S/C15H24/c1-13-7-5-8-14(2)10-12-15(3,4)11-6-9-13/h6-7,10-11H,5,8-9,12H2,1-4H3/b11-6+,13-7+,14-10+
- InChI Key
- FAMPSKZZVDUYOS-HRGUGZIWSA-N
- Formula
- C15H24
- SMILES
- CC1=CCCC(C)=CCC(C)(C)C=CC1
- Mol. Weight (g/mol)
- 204.35
- CAS
- 6753-98-6
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Datasets
Vapor or sublimation pressure, kPa [ref]
Operational conditions:
- Temperature, K = 303 (Liquid mixture 1)
- Solvent: Mass ratio of component to other component of binary solvent = 2.4 (Liquid mixture 1)
| Vapor or sublimation pressure, kPa - Liquid mixture 1 |
|---|
| 6600.00 |
| 6600.00 |
| 6700.00 |
| 6900.00 |
Vapor or sublimation pressure, kPa [ref]
Operational conditions:
- Temperature, K = 303 (Liquid mixture 1)
- Solvent: Mass ratio of component to other component of binary solvent = 2.4 (Liquid mixture 1)
| Mole fraction of Carbon dioxide (1) - Liquid mixture 1 | Vapor or sublimation pressure, kPa - Liquid mixture 1 |
|---|---|
| 0.8740 | 10000.00 |
| 0.9120 | 10100.00 |
| 0.9490 | 9900.00 |
| 0.9760 | 7000.00 |
Vapor or sublimation pressure, kPa [ref]
Operational condition: Solvent: Mass ratio of component to other component of binary solvent = 2.4 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Carbon dioxide (1) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
| 313.00 | 0.8740 | 12100.00 |
| 313.00 | 0.9120 | 12200.00 |
| 313.00 | 0.9490 | 11500.00 |
| 313.00 | 0.9760 | 9600.00 |
| 323.00 | 0.8740 | 14200.00 |
| 323.00 | 0.9120 | 14300.00 |
| 323.00 | 0.9490 | 13600.00 |
| 323.00 | 0.9760 | 12500.00 |
| 333.00 | 0.8740 | 16400.00 |
| 333.00 | 0.9120 | 16600.00 |
| 333.00 | 0.9490 | 16000.00 |
| 333.00 | 0.9760 | 14700.00 |
| 343.00 | 0.8740 | 18500.00 |
| 343.00 | 0.9120 | 19000.00 |
| 343.00 | 0.9490 | 18400.00 |
| 343.00 | 0.9760 | 16600.00 |
Vapor or sublimation pressure, kPa [ref]
Operational conditions:
- Temperature, K = 303 (Liquid mixture 1)
- Solvent: Mass ratio of component to other component of binary solvent = 2.4 (Liquid mixture 1)
| Vapor or sublimation pressure, kPa - Liquid mixture 1 |
|---|
| 6600.00 |
| 6600.00 |
| 6700.00 |
| 6900.00 |
Vapor or sublimation pressure, kPa [ref]
Operational conditions:
- Temperature, K = 303 (Liquid mixture 1)
- Solvent: Mass ratio of component to other component of binary solvent = 2.4 (Liquid mixture 1)
| Mole fraction of Carbon dioxide (1) - Liquid mixture 1 | Vapor or sublimation pressure, kPa - Liquid mixture 1 |
|---|---|
| 0.8740 | 10000.00 |
| 0.9120 | 10100.00 |
| 0.9490 | 9900.00 |
| 0.9760 | 7000.00 |
Vapor or sublimation pressure, kPa [ref]
Operational condition: Solvent: Mass ratio of component to other component of binary solvent = 2.4 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Carbon dioxide (1) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
| 313.00 | 0.8740 | 12100.00 |
| 313.00 | 0.9120 | 12200.00 |
| 313.00 | 0.9490 | 11500.00 |
| 313.00 | 0.9760 | 9600.00 |
| 323.00 | 0.8740 | 14200.00 |
| 323.00 | 0.9120 | 14300.00 |
| 323.00 | 0.9490 | 13600.00 |
| 323.00 | 0.9760 | 12500.00 |
| 333.00 | 0.8740 | 16400.00 |
| 333.00 | 0.9120 | 16600.00 |
| 333.00 | 0.9490 | 16000.00 |
| 333.00 | 0.9760 | 14700.00 |
| 343.00 | 0.8740 | 18500.00 |
| 343.00 | 0.9120 | 19000.00 |
| 343.00 | 0.9490 | 18400.00 |
| 343.00 | 0.9760 | 16600.00 |