- InChI
- InChI=1S/C16H32/c1-2-3-4-5-6-7-8-10-13-16-14-11-9-12-15-16/h16H,2-15H2,1H3
- InChI Key
- STWFZICHPLEOIC-UHFFFAOYSA-N
- Formula
- C16H32
- SMILES
- CCCCCCCCCCC1CCCCC1
- Molecular Weight1
- 224.43
- CAS
- 1795-16-0
- Other Names
-
- 1-CYCLOHEXYLDECANE
- 1-DECYLCYCLOHEXANE
- Cyclohexane, n-decyl-
- DECYLCYCLOHEXANE
- Decane, 1-cyclohexyl-
- n-Decylcyclohexane
- ω : Acentric Factor.
- 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).
- ΔfH°liquid : Liquid phase 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).
- 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.
- S°gas : Molar entropy at standard conditions (J/mol×K).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Tfus : Melting point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.6130 | KDB | |
| ΔcH°liquid | [-10532.80; -10451.10] | kJ/mol |
|
| ΔcH°liquid | -10451.10 ± 3.30 | kJ/mol | NIST |
| ΔcH°liquid | -10451.20 ± 1.80 | kJ/mol | NIST |
| ΔcH°liquid | -10532.80 ± 2.20 | kJ/mol | NIST |
| ΔfG° | 108.29 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -336.90 ± 2.40 | kJ/mol | NIST |
| ΔfH°liquid | -418.40 ± 2.10 | kJ/mol | NIST |
| ΔfusH° | 29.03 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [78.70; 79.70] | kJ/mol |
|
| ΔvapH° | 78.70 ± 0.80 | kJ/mol | NIST |
| ΔvapH° | 79.70 | kJ/mol | NIST |
| ΔvapH° | 78.76 | kJ/mol | NIST |
| log10WS | -6.17 | Crippen Calculated Property | |
| logPoct/wat | 6.098 | Crippen Calculated Property | |
| McVol | 225.440 | ml/mol | McGowan Calculated Property |
| Pc | 1540.00 | kPa | KDB |
| Inp | [1638.00; 1679.00] |
|
|
| Inp | 1658.00 | NIST | |
| Inp | Outlier 1679.00 | NIST | |
| Inp | 1638.00 | NIST | |
| Inp | 1640.00 | NIST | |
| Inp | 1642.00 | NIST | |
| Inp | 1656.00 | NIST | |
| Inp | 1656.20 | NIST | |
| Inp | 1655.90 | NIST | |
| Inp | 1650.70 | NIST | |
| Inp | 1656.20 | NIST | |
| Inp | 1658.40 | NIST | |
| Inp | 1650.70 | NIST | |
| Inp | 1656.20 | NIST | |
| Inp | 1658.40 | NIST | |
| Inp | 1656.20 | NIST | |
| Inp | 1655.90 | NIST | |
| Inp | 1648.54 | NIST | |
| Inp | 1653.53 | NIST | |
| Inp | 1656.86 | NIST | |
| Inp | 1655.41 | NIST | |
| Inp | 1660.95 | NIST | |
| Inp | 1664.11 | NIST | |
| Inp | 1640.00 | NIST | |
| S°gas | 694.42 | J/mol×K | NIST |
| Tboil | [560.00; 570.80] | K |
|
| Tboil | 570.80 | K | KDB |
| Tboil | 560.00 ± 3.00 | K | NIST |
| Tc | 750.00 | K | KDB |
| Tfus | [271.00; 271.45] | K |
|
| Tfus | 271.00 | K | KDB |
| Tfus | 271.45 ± 0.50 | K | NIST |
| Tfus | 271.40 ± 0.04 | K | NIST |
| Tfus | 271.40 ± 0.04 | K | NIST |
| Tfus | 271.43 ± 0.03 | K | NIST |
| Tfus | 271.14 ± 0.40 | K | NIST |
| Ttriple | [271.42; 271.44] | K |
|
| Ttriple | 271.43 ± 0.02 | K | NIST |
| Ttriple | 271.42 ± 0.05 | K | NIST |
| Ttriple | 271.44 ± 0.02 | K | NIST |
| Vc | 0.865 | m3/kmol | KDB |
| Zc | 0.2134950 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [605.97; 725.60] | J/mol×K | [585.03; 768.70] |
|
| Cp,gas | 605.97 | J/mol×K | 585.03 | Joback Calculated Property |
| Cp,gas | 628.52 | J/mol×K | 615.64 | Joback Calculated Property |
| Cp,gas | 649.97 | J/mol×K | 646.25 | Joback Calculated Property |
| Cp,gas | 670.38 | J/mol×K | 676.87 | Joback Calculated Property |
| Cp,gas | 689.76 | J/mol×K | 707.48 | Joback Calculated Property |
| Cp,gas | 708.16 | J/mol×K | 738.09 | Joback Calculated Property |
| Cp,gas | 725.60 | J/mol×K | 768.70 | Joback Calculated Property |
| η | [0.0001634; 0.0064682] | Pa×s | [277.46; 585.03] |
|
| η | 0.0064682 | Pa×s | 277.46 | Joback Calculated Property |
| η | 0.0021724 | Pa×s | 328.72 | Joback Calculated Property |
| η | 0.0009794 | Pa×s | 379.98 | Joback Calculated Property |
| η | 0.0005336 | Pa×s | 431.25 | Joback Calculated Property |
| η | 0.0003308 | Pa×s | 482.51 | Joback Calculated Property |
| η | 0.0002248 | Pa×s | 533.77 | Joback Calculated Property |
| η | 0.0001634 | Pa×s | 585.03 | Joback Calculated Property |
| ΔfusH | [38.62; 38.62] | kJ/mol | [271.40; 271.40] |
|
| ΔfusH | 38.62 | kJ/mol | 271.40 | NIST |
| ΔfusH | 38.62 | kJ/mol | 271.40 | NIST |
| ΔvapH | [50.38; 76.70] | kJ/mol | [398.00; 570.80] |
|
| ΔvapH | 76.70 | kJ/mol | 398.00 | NIST |
| ΔvapH | 61.60 | kJ/mol | 520.00 | NIST |
| ΔvapH | 50.38 | kJ/mol | 570.80 | KDB |
| ρl | [764.40; 821.93] | kg/m3 | [288.15; 373.15] |
|
| ρl | 821.93 | kg/m3 | 288.15 | Thermop... |
| ρl | 819.00 | kg/m3 | 293.00 | KDB |
| ρl | 818.55 | kg/m3 | 293.15 | Densiti... |
| ρl | 818.54 | kg/m3 | 293.15 | Thermop... |
| ρl | 815.16 | kg/m3 | 298.15 | Thermop... |
| ρl | 811.78 | kg/m3 | 303.15 | Thermop... |
| ρl | 811.78 | kg/m3 | 303.15 | Densiti... |
| ρl | 805.02 | kg/m3 | 313.15 | Thermop... |
| ρl | 805.02 | kg/m3 | 313.15 | Densiti... |
| ρl | 798.27 | kg/m3 | 323.15 | Densiti... |
| ρl | 798.26 | kg/m3 | 323.15 | Thermop... |
| ρl | 791.49 | kg/m3 | 333.15 | Thermop... |
| ρl | 791.50 | kg/m3 | 333.15 | Densiti... |
| ρl | 784.80 | kg/m3 | 343.15 | Densiti... |
| ρl | 778.00 | kg/m3 | 353.15 | Densiti... |
| ρl | 771.20 | kg/m3 | 363.15 | Densiti... |
| ρl | 764.40 | kg/m3 | 373.15 | Densiti... |
| γ | 0.03 | N/m | 298.20 | KDB |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tfus | [271.30; 293.90] | K | [100.00; 100100.00] |
|
| Tfus | 271.30 | K | 100.00 | Solid-L... |
| Tfus | 276.00 | K | 20000.00 | Solid-L... |
| Tfus | 280.50 | K | 40100.00 | Solid-L... |
| Tfus | 284.80 | K | 59900.00 | Solid-L... |
| Tfus | 289.20 | K | 80100.00 | Solid-L... |
| Tfus | 293.90 | K | 100100.00 | Solid-L... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [427.81; 591.43] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.56565e+01 | |||
| Coefficient B | -5.17811e+03 | |||
| Coefficient C | -9.08880e+01 | |||
| Temperature range, min. | 427.81 | |||
| Temperature range, max. | 591.43 | |||
| Pvap | 1.33 | kPa | 427.81 | Calculated Property |
| Pvap | 2.93 | kPa | 445.99 | Calculated Property |
| Pvap | 5.96 | kPa | 464.17 | Calculated Property |
| Pvap | 11.35 | kPa | 482.35 | Calculated Property |
| Pvap | 20.41 | kPa | 500.53 | Calculated Property |
| Pvap | 34.92 | kPa | 518.71 | Calculated Property |
| Pvap | 57.19 | kPa | 536.89 | Calculated Property |
| Pvap | 90.12 | kPa | 555.07 | Calculated Property |
| Pvap | 137.22 | kPa | 573.25 | Calculated Property |
| Pvap | 202.64 | kPa | 591.43 | Calculated Property |
| Pvap | [4.71e-06; 1704.43] | kPa | [271.42; 751.25] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.83202e+02 | |||
| Coefficient B | -1.66574e+04 | |||
| Coefficient C | -2.40646e+01 | |||
| Coefficient D | 1.02076e-05 | |||
| Temperature range, min. | 271.42 | |||
| Temperature range, max. | 751.25 | |||
| Pvap | 4.71e-06 | kPa | 271.42 | Calculated Property |
| Pvap | 2.07e-03 | kPa | 324.73 | Calculated Property |
| Pvap | 0.11 | kPa | 378.05 | Calculated Property |
| Pvap | 1.63 | kPa | 431.36 | Calculated Property |
| Pvap | 11.35 | kPa | 484.68 | Calculated Property |
| Pvap | 48.44 | kPa | 537.99 | Calculated Property |
| Pvap | 150.31 | kPa | 591.31 | Calculated Property |
| Pvap | 379.07 | kPa | 644.62 | Calculated Property |
| Pvap | 837.15 | kPa | 697.94 | Calculated Property |
| Pvap | 1704.43 | kPa | 751.25 | Calculated Property |
Similar Compounds
Find more compounds similar to Cyclohexane, decyl-.
Mixtures
Sources
- KDB Vapor Pressure Data
- 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
- Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
- Solid-Liquid Equilibria under High Pressure of Eight Pure n-Alkylcyclohexanes
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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