- InChI
- InChI=1S/C15H30/c1-2-3-4-5-6-7-9-12-15-13-10-8-11-14-15/h15H,2-14H2,1H3
- InChI Key
- CLMFECCMAVQYQA-UHFFFAOYSA-N
- Formula
- C15H30
- SMILES
- CCCCCCCCCC1CCCCC1
- Molecular Weight1
- 210.40
- CAS
- 2883-02-5
- Other Names
-
- 1-cyclohexylnonane
- Cyclohexane, nonyl-
- Nonylcyclohexane
- Nonylcylohexane
- nonane, 1-cyclohexyl-
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- 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).
- 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).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Tboil : Normal Boiling Point Temperature (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 |
|---|---|---|---|
| ΔcH°liquid | -9874.10 ± 2.10 | kJ/mol | NIST |
| ΔfG° | 99.87 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -316.20 ± 2.30 | kJ/mol | NIST |
| ΔfusH° | 26.44 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 74.70 | kJ/mol | NIST |
| log10WS | -5.75 | Crippen Calculated Property | |
| logPoct/wat | 5.707 | Crippen Calculated Property | |
| McVol | 211.350 | ml/mol | McGowan Calculated Property |
| Pc | 1661.90 | kPa | Joback Calculated Property |
| Inp | [1535.00; 1559.54] |
|
|
| Inp | 1546.00 | NIST | |
| Inp | 1543.00 | NIST | |
| Inp | 1543.00 | NIST | |
| Inp | 1556.00 | NIST | |
| Inp | 1549.60 | NIST | |
| Inp | 1551.20 | NIST | |
| Inp | 1536.00 | NIST | |
| Inp | 1544.32 | NIST | |
| Inp | 1549.04 | NIST | |
| Inp | 1552.36 | NIST | |
| Inp | 1551.07 | NIST | |
| Inp | 1556.36 | NIST | |
| Inp | 1559.54 | NIST | |
| Inp | 1535.00 | NIST | |
| Inp | 1556.00 | NIST | |
| Inp | 1543.00 | NIST | |
| Inp | 1535.00 | NIST | |
| Inp | 1549.60 | NIST | |
| Inp | 1552.36 | NIST | |
| Inp | 1546.00 | NIST | |
| Tboil | [545.00; 554.70] | K |
|
| Tboil | 545.00 ± 3.00 | K | NIST |
| Tboil | 554.70 ± 0.60 | K | NIST |
| Tc | 747.76 | K | Joback Calculated Property |
| Tfus | 266.19 | K | Joback Calculated Property |
| Vc | 0.808 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [550.98; 669.08] | J/mol×K | [562.15; 747.76] |
|
| Cp,gas | 550.98 | J/mol×K | 562.15 | Joback Calculated Property |
| Cp,gas | 573.23 | J/mol×K | 593.08 | Joback Calculated Property |
| Cp,gas | 594.41 | J/mol×K | 624.02 | Joback Calculated Property |
| Cp,gas | 614.56 | J/mol×K | 654.95 | Joback Calculated Property |
| Cp,gas | 633.70 | J/mol×K | 685.89 | Joback Calculated Property |
| Cp,gas | 651.86 | J/mol×K | 716.82 | Joback Calculated Property |
| Cp,gas | 669.08 | J/mol×K | 747.76 | Joback Calculated Property |
| η | [0.0001810; 0.0069856] | Pa×s | [266.19; 562.15] |
|
| η | 0.0069856 | Pa×s | 266.19 | Joback Calculated Property |
| η | 0.0023609 | Pa×s | 315.52 | Joback Calculated Property |
| η | 0.0010699 | Pa×s | 364.84 | Joback Calculated Property |
| η | 0.0005854 | Pa×s | 414.17 | Joback Calculated Property |
| η | 0.0003642 | Pa×s | 463.50 | Joback Calculated Property |
| η | 0.0002482 | Pa×s | 512.82 | Joback Calculated Property |
| η | 0.0001810 | Pa×s | 562.15 | Joback Calculated Property |
| ρl | [761.60; 816.41] | kg/m3 | [293.15; 373.15] |
|
| ρl | 816.41 | kg/m3 | 293.15 | Densiti... |
| ρl | 809.57 | kg/m3 | 303.15 | Densiti... |
| ρl | 802.74 | kg/m3 | 313.15 | Densiti... |
| ρl | 795.80 | kg/m3 | 323.15 | Densiti... |
| ρl | 789.05 | kg/m3 | 333.15 | Densiti... |
| ρl | 782.20 | kg/m3 | 343.15 | Densiti... |
| ρl | 775.40 | kg/m3 | 353.15 | Densiti... |
| ρl | 768.50 | kg/m3 | 363.15 | Densiti... |
| ρl | 761.60 | kg/m3 | 373.15 | Densiti... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [414.70; 576.57] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.50882e+01 | |||
| Coefficient B | -4.66235e+03 | |||
| Coefficient C | -9.96870e+01 | |||
| Temperature range, min. | 414.70 | |||
| Temperature range, max. | 576.57 | |||
| Pvap | 1.33 | kPa | 414.70 | Calculated Property |
| Pvap | 2.97 | kPa | 432.69 | Calculated Property |
| Pvap | 6.08 | kPa | 450.67 | Calculated Property |
| Pvap | 11.61 | kPa | 468.66 | Calculated Property |
| Pvap | 20.89 | kPa | 486.64 | Calculated Property |
| Pvap | 35.68 | kPa | 504.63 | Calculated Property |
| Pvap | 58.21 | kPa | 522.61 | Calculated Property |
| Pvap | 91.27 | kPa | 540.60 | Calculated Property |
| Pvap | 138.14 | kPa | 558.58 | Calculated Property |
| Pvap | 202.64 | kPa | 576.57 | Calculated Property |
Similar Compounds
Find more compounds similar to n-Nonylcyclohexane.
Mixtures
Sources
- Crippen Method
- Crippen Method
- Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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