- InChI
- InChI=1S/C10H16/c1-8(2)10-6-4-9(3)5-7-10/h4,10H,1,5-7H2,2-3H3/t10-/m1/s1
- InChI Key
- XMGQYMWWDOXHJM-SNVBAGLBSA-N
- Formula
- C10H16
- SMILES
- C=C(C)C1CC=C(C)CC1
- Molecular Weight1
- 136.23
- CAS
- 5989-27-5
- Other Names
-
- (+)-(4R)-Limonene
- (+)-(R)-Limonene
- (+)-Dipentene
- (+)-Limonene
- (+)-p-Mentha-1,8-diene
- (-)-(S)-limonene
- (-)-.alpha.-limonene
- (-)-limonene
- (4R)-(+)-Limonene
- (4R)-Limonene
- (R)-(+)-Limonene
- (R)-(+)-p-Mentha-1,8-diene
- (R)-1-methyl-4-(1-methylethenyl)cyclohexene
- (R)-4-Isopropenyl-1-methyl-1-cyclohexene
- (R)-Limonene
- (R)-p-Mentha-1,8-diene
- (S)-(-)-limonene
- (S)-1-methyl-4-(1-methylethenyl)cyclohexene
- (S)-4-isopropenyl-1-methyl-1-cyclohexene
- (S)-limonene
- .beta.-limonene
- 4-Isopropenyl-1-methyl-1-cyclohexene-, (R)-
- Biogenic SE 374
- Carvene
- Cyclohexene, 1-methyl-4-(1-methylethenyl)-, (4R)-
- Cyclohexene, 1-methyl-4-(1-methylethenyl)-, (R)-
- D-(+)-Limonene
- Dextro-limonene
- EC 7
- Glidesafe
- Glidsafe
- L-limonene
- Limonene, (+)-
- Limonene, (D)-
- Refchole
- cyclohexene, 1-methyl-4-(1-methylethenyl)-, (S)-,
- p-Mentha-1,8-diene, (R)-(+)-
- p-mentha-1,8-diene, (S)-(-)-
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- 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).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pvap : Vapor pressure (kPa).
- Tboil : Normal Boiling Point Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- 1: Molecular weight from the IUPAC atomic weights tables.
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.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | -6167.20 ± 2.10 | kJ/mol | NIST |
| ΔfH°gas | 39.83 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 11.73 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [48.90; 49.90] | kJ/mol |
|
| ΔvapH° | 49.50 | kJ/mol | NIST |
| ΔvapH° | 49.60 | kJ/mol | NIST |
| ΔvapH° | 49.90 | kJ/mol | NIST |
| ΔvapH° | 49.60 | kJ/mol | NIST |
| ΔvapH° | 48.90 ± 0.10 | kJ/mol | NIST |
| IE | 8.54 | eV | Relay (1.0) Calculated Property |
| log10WS | -4.26 | Estimated Solubility | |
| logPoct/wat | 3.309 | Crippen Calculated Property | |
| McVol | 132.300 | ml/mol | McGowan Calculated Property |
| Tboil | [448.00; 452.00] | K |
|
| Tboil | 450.34 | K | Measurement and Correlation of Vapor-Liquid Equilibrium Data for ss-Pinene + p-Cymene + (S)-(-)-Limonene at Atmospheric Pressure |
| Tboil | 449.00 | K | NIST |
| Tboil | 451.00 | K | NIST |
| Tboil | 449.40 ± 2.00 | K | NIST |
| Tboil | 448.00 ± 4.00 | K | NIST |
| Tboil | 451.00 ± 0.50 | K | NIST |
| Tboil | 451.00 ± 0.50 | K | NIST |
| Tboil | 451.00 ± 1.00 | K | NIST |
| Tboil | 449.40 ± 3.00 | K | NIST |
| Tboil | 451.00 ± 3.00 | K | NIST |
| Tboil | 449.00 ± 3.00 | K | NIST |
| Tboil | 451.00 ± 2.00 | K | NIST |
| Tboil | 449.90 ± 3.00 | K | NIST |
| Tboil | 449.70 ± 3.00 | K | NIST |
| Tboil | 449.50 ± 3.00 | K | NIST |
| Tboil | 452.00 ± 3.00 | K | NIST |
| Tboil | 449.00 ± 6.00 | K | NIST |
| Tboil | 448.00 ± 4.00 | K | NIST |
| Tboil | 449.00 ± 4.00 | K | NIST |
| Tfus | 198.65 ± 0.15 | K | NIST |
Cheméo can also estimate Critical Temperature, Critical Pressure, Critical Volume, Standard Gibbs free energy of formation, Acentric Factor for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [269.91; 362.47] | J/mol×K | [448.65; 657.45] |
|
| Cp,gas | 269.91 | J/mol×K | 448.65 | Joback Calculated Property |
| Cp,gas | 287.53 | J/mol×K | 483.45 | Joback Calculated Property |
| Cp,gas | 304.24 | J/mol×K | 518.25 | Joback Calculated Property |
| Cp,gas | 320.05 | J/mol×K | 553.05 | Joback Calculated Property |
| Cp,gas | 335.01 | J/mol×K | 587.85 | Joback Calculated Property |
| Cp,gas | 349.14 | J/mol×K | 622.65 | Joback Calculated Property |
| Cp,gas | 362.47 | J/mol×K | 657.45 | Joback Calculated Property |
| ΔfusH | 11.38 | kJ/mol | 199.20 | NIST |
| ΔvapH | [37.90; 49.20] | kJ/mol | [305.50; 417.00] |
|
| ΔvapH | 47.70 | kJ/mol | 305.50 | NIST |
| ΔvapH | 49.20 | kJ/mol | 342.00 | NIST |
| ΔvapH | 44.50 | kJ/mol | 367.50 | NIST |
| ΔvapH | 46.10 ± 0.20 | kJ/mol | 417.00 | NIST |
| ΔvapH | 43.50 ± 0.20 | kJ/mol | 417.00 | NIST |
| ΔvapH | 40.90 ± 0.30 | kJ/mol | 417.00 | NIST |
| ΔvapH | 37.90 ± 0.60 | kJ/mol | 417.00 | NIST |
| Pvap | [0.03; 0.36] | kPa | [273.65; 308.15] |
|
| Pvap | 0.03 | kPa | 273.65 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.03 | kPa | 273.65 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.03 | kPa | 273.65 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.04 | kPa | 278.15 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.04 | kPa | 278.15 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.04 | kPa | 278.15 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.06 | kPa | 283.15 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.06 | kPa | 283.15 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.06 | kPa | 283.15 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.09 | kPa | 288.15 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.09 | kPa | 288.15 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.09 | kPa | 288.15 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.13 | kPa | 293.15 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.13 | kPa | 293.15 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.13 | kPa | 293.15 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.19 | kPa | 298.15 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.19 | kPa | 298.15 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.19 | kPa | 298.15 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.26 | kPa | 303.15 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.26 | kPa | 303.15 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.26 | kPa | 303.15 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.36 | kPa | 308.15 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.36 | kPa | 308.15 | Thermodynamic study of selected monoterpenes III |
| Pvap | 0.36 | kPa | 308.15 | Thermodynamic study of selected monoterpenes III |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [324.43; 480.94] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.42584e+01 | |||
| Coefficient B | -3.89401e+03 | |||
| Coefficient C | -4.57090e+01 | |||
| Temperature range, min. | 324.43 | |||
| Temperature range, max. | 480.94 | |||
| Pvap | 1.33 | kPa | 324.43 | Calculated Property |
| Pvap | 3.03 | kPa | 341.82 | Calculated Property |
| Pvap | 6.28 | kPa | 359.21 | Calculated Property |
| Pvap | 12.06 | kPa | 376.60 | Calculated Property |
| Pvap | 21.71 | kPa | 393.99 | Calculated Property |
| Pvap | 36.95 | kPa | 411.38 | Calculated Property |
| Pvap | 59.91 | kPa | 428.77 | Calculated Property |
| Pvap | 93.16 | kPa | 446.16 | Calculated Property |
| Pvap | 139.63 | kPa | 463.55 | Calculated Property |
| Pvap | 202.63 | kPa | 480.94 | Calculated Property |
Similar Compounds
Find more compounds similar to D-Limonene.
Mixtures
Sources
- Cheméo Relay (1.0)
- Cheméo Relay (1.0, beta) Beta: served but experimental, data-limited and below our cross-validation release bar; the Joback value is recommended where available.
- Crippen Method
- Measurement and correlation of (vapor + liquid) equilibrium data for {alpha-pinene + p-cymene + (S)-(-)-limonene} ternary system at atmospheric pressure
- Thermodynamic study of selected monoterpenes III
- Measurement and Correlation of Vapor-Liquid Equilibrium Data for ss-Pinene + p-Cymene + (S)-(-)-Limonene at Atmospheric Pressure
- Joback Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
These property values are available through the Cheméo API. A free account gives you an access key.