- InChI
- InChI=1S/C10H14O/c1-7(2)9-5-4-8(3)10(11)6-9/h4,9H,1,5-6H2,2-3H3/t9-/m1/s1
- InChI Key
- ULDHMXUKGWMISQ-SECBINFHSA-N
- Formula
- C10H14O
- SMILES
- C=C(C)C1CC=C(C)C(=O)C1
- Molecular Weight1
- 150.22
- CAS
- 2244-16-8
- Other Names
-
- (+)-Carvon
- (+)-carvone
- (S)-(+)-carvone
- (S)-(+)-p-Mentha-6,8-dien-2-one
- (S)-2-methyl-5-(1-methylethenyl)-2-cyclohexen-1-one
- (S)-2-methyl-5-(1-methylvinyl)cyclohex-2-en-1-one
- (S)-carvone
- 2-Cyclohexen-1-one, 2-methyl-5-(1-methylethenyl)-, (5S)-
- 2-cyclohexen-1-one, 2-methyl-5-(1-methylethenyl), (5R)-
- 2-cyclohexen-1-one, 2-methyl-5-(1-methylethenyl)-, (S)-
- 5-Isopropenyl-2-methyl-2-cyclohexen-1-one, (S)-
- D-(+)-carvone
- R-(-)-1-methyl-4-isopropenyl-6-cyclohexen-2-one
- carvone, (+)-
- d-1-Methyl-4-isopropenyl-6-cyclohexen-2-one
- d-p-Mentha-6,8(9)-dien-2-one
- l-1-methyl-4-isopropenyl-6-cyclohexen-2-one
- l-carvone
- p-mentha-6,8-dien-2-one
- p-mentha-6,8-dien-2-one, (S)-(+)-
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfG° | 34.80 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -171.16 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 11.24 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 58.20 | kJ/mol | NIST |
| log10WS | -2.65 | Crippen Calculated Property | |
| logPoct/wat | 2.488 | Crippen Calculated Property | |
| McVol | 133.870 | ml/mol | McGowan Calculated Property |
| Pc | 2859.68 | kPa | Joback Calculated Property |
| Inp | [1194.54; 1270.00] |
|
|
| Inp | 1212.83 | NIST | |
| Inp | 1216.93 | NIST | |
| Inp | 1221.14 | NIST | |
| Inp | 1225.42 | NIST | |
| Inp | 1229.89 | NIST | |
| Inp | 1234.47 | NIST | |
| Inp | 1239.00 | NIST | |
| Inp | 1194.54 | NIST | |
| Inp | 1197.94 | NIST | |
| Inp | 1201.12 | NIST | |
| Inp | 1205.05 | NIST | |
| Inp | 1208.89 | NIST | |
| Inp | 1223.00 | NIST | |
| Inp | 1238.00 | NIST | |
| Inp | 1242.00 | NIST | |
| Inp | 1254.00 | NIST | |
| Inp | 1256.00 | NIST | |
| Inp | 1240.00 | NIST | |
| Inp | 1257.00 | NIST | |
| Inp | 1246.00 | NIST | |
| Inp | 1234.00 | NIST | |
| Inp | 1249.00 | NIST | |
| Inp | 1245.00 | NIST | |
| Inp | 1242.00 | NIST | |
| Inp | 1222.00 | NIST | |
| Inp | 1263.00 | NIST | |
| Inp | 1231.00 | NIST | |
| Inp | 1270.00 | NIST | |
| Inp | 1228.00 | NIST | |
| Inp | 1249.00 | NIST | |
| Inp | 1210.00 | NIST | |
| Inp | 1210.00 | NIST | |
| Inp | 1212.83 | NIST | |
| Inp | 1234.47 | NIST | |
| Inp | 1205.05 | NIST | |
| Inp | 1245.00 | NIST | |
| Inp | 1270.00 | NIST | |
| Inp | 1238.00 | NIST | |
| I | [1714.00; 1752.00] |
|
|
| I | 1752.00 | NIST | |
| I | 1740.00 | NIST | |
| I | 1747.00 | NIST | |
| I | 1751.00 | NIST | |
| I | 1744.00 | NIST | |
| I | 1714.00 | NIST | |
| I | 1718.00 | NIST | |
| I | 1717.00 | NIST | |
| I | 1719.00 | NIST | |
| I | 1745.00 | NIST | |
| I | 1749.00 | NIST | |
| I | 1751.00 | NIST | |
| I | 1748.00 | NIST | |
| I | 1728.00 | NIST | |
| I | 1741.00 | NIST | |
| I | 1721.00 | NIST | |
| I | 1729.00 | NIST | |
| I | 1715.00 | NIST | |
| I | 1752.00 | NIST | |
| I | 1714.00 | NIST | |
| Tboil | 504.20 | K | NIST |
| Tc | 742.23 | K | Joback Calculated Property |
| Tfus | 275.62 | K | Joback Calculated Property |
| Vc | 0.503 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [302.34; 391.51] | J/mol×K | [516.27; 742.23] |
|
| Cp,gas | 302.34 | J/mol×K | 516.27 | Joback Calculated Property |
| Cp,gas | 319.31 | J/mol×K | 553.93 | Joback Calculated Property |
| Cp,gas | 335.43 | J/mol×K | 591.59 | Joback Calculated Property |
| Cp,gas | 350.72 | J/mol×K | 629.25 | Joback Calculated Property |
| Cp,gas | 365.16 | J/mol×K | 666.91 | Joback Calculated Property |
| Cp,gas | 378.76 | J/mol×K | 704.57 | Joback Calculated Property |
| Cp,gas | 391.51 | J/mol×K | 742.23 | Joback Calculated Property |
| ΔfusH | 1.50 | kJ/mol | 221.60 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 372.20 | K | 1.30 | NIST |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 101.80 | 298.15 | 958.79 |
| Reference | ||
Similar Compounds
Find more compounds similar to D-Carvone.
Mixtures
Sources
- Crippen Method
- Crippen Method
- Viscosities and densities of systems involved in the deterpenation of essential oils by liquid-liquid extraction: New UNIFAC-VISCO parameters
- High Pressure Phase Equilibria of the Related Substances in the Limonene Oxidation in Supercritical CO2
- Joback Method
- McGowan Method
- NIST Webbook
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