- InChI
- InChI=1S/C14H28/c1-2-3-4-5-6-7-8-11-14-12-9-10-13-14/h14H,2-13H2,1H3
- InChI Key
- GDCYEUOAZVKNHT-UHFFFAOYSA-N
- Formula
- C14H28
- SMILES
- CCCCCCCCCC1CCCC1
- Molecular Weight1
- 196.37
- CAS
- 2882-98-6
- Other Names
-
- n-Nonylcyclopentane
- nonylcyclopentane
- 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).
- ΔfusH° : Enthalpy of fusion at standard conditions (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).
- 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).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.5660; 0.6101] |
|
|
| ω | 0.6101 | Passut and Danner (1973), critical constants and acentric factors Compiled value | |
| ω | 0.5660 | KDB | |
| ΔcH°liquid | -9239.60 ± 1.90 | kJ/mol | NIST |
| ΔfG° | 103.50 | kJ/mol | KDB |
| ΔfH°gas | [-271.50; -271.30] | kJ/mol |
|
| ΔfH°gas | -271.50 | kJ/mol | KDB |
| ΔfH°gas | -271.30 ± 2.10 | kJ/mol | NIST |
| ΔfusH° | 25.95 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 70.70 | kJ/mol | NIST |
| IE | 9.72 | eV | Relay (1.0) Calculated Property |
| log10WS | -6.81 | Relay (1.0) Calculated Property | |
| logPoct/wat | 5.317 | Crippen Calculated Property | |
| McVol | 197.260 | ml/mol | McGowan Calculated Property |
| Pc | [1654.74; 1760.00] | kPa |
|
| Pc | 1654.74 | kPa | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Pc | 1760.00 | kPa | KDB |
| Inp | [1438.00; 1451.00] |
|
|
| Inp | 1438.00 | NIST | |
| Inp | 1451.00 | NIST | |
| Inp | 1451.00 | NIST | |
| Inp | 1438.00 | NIST | |
| Tboil | 535.30 | K | KDB |
| Tc | [710.54; 717.00] | K |
|
| Tc | 710.54 | K | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Tc | 717.00 | K | KDB |
| Tfus | [244.00; 244.15] | K |
|
| Tfus | 244.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 244.00 | K | KDB |
| Vc | 0.760 | m3/kmol | KDB |
| Zc | 0.2245210 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 47.24 | kJ/mol | 535.30 | KDB |
| ρl | 808.00 | kg/m3 | 293.00 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [269.25; 724.90] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | -7.03220e+01 | |||
| Coefficient B | 1.46552e+00 | |||
| Coefficient C | -8.65200e-04 | |||
| Coefficient D | 1.94900e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 269.25 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 348.49 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 419.14 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 481.81 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 537.13 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 585.70 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 628.15 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 665.09 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 697.13 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 724.90 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0077030; 0.0003058] | Pa×s | [244.07; 499.64] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.11740e+01 | |||
| Coefficient B | 1.53958e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 244.07 | |||
| Temperature range, max. | 499.64 | |||
| η | 0.0077030 | Pa×s | 244.07 | Calculated Property |
| η | 0.0039918 | Pa×s | 272.47 | Calculated Property |
| η | 0.0023419 | Pa×s | 300.87 | Calculated Property |
| η | 0.0015063 | Pa×s | 329.26 | Calculated Property |
| η | 0.0010391 | Pa×s | 357.66 | Calculated Property |
| η | 0.0007571 | Pa×s | 386.05 | Calculated Property |
| η | 0.0005761 | Pa×s | 414.45 | Calculated Property |
| η | 0.0004540 | Pa×s | 442.85 | Calculated Property |
| η | 0.0003682 | Pa×s | 471.24 | Calculated Property |
| η | 0.0003058 | Pa×s | 499.64 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [402.71; 549.36] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.60257e+01 | |||
| Coefficient B | -4.92219e+03 | |||
| Coefficient C | -8.99520e+01 | |||
| Temperature range, min. | 402.71 | |||
| Temperature range, max. | 549.36 | |||
| Pvap | 1.33 | kPa | 402.71 | Calculated Property |
| Pvap | 2.91 | kPa | 419.00 | Calculated Property |
| Pvap | 5.89 | kPa | 435.30 | Calculated Property |
| Pvap | 11.19 | kPa | 451.59 | Calculated Property |
| Pvap | 20.12 | kPa | 467.89 | Calculated Property |
| Pvap | 34.47 | kPa | 484.18 | Calculated Property |
| Pvap | 56.58 | kPa | 500.48 | Calculated Property |
| Pvap | 89.43 | kPa | 516.77 | Calculated Property |
| Pvap | 136.67 | kPa | 533.07 | Calculated Property |
| Pvap | 202.66 | kPa | 549.36 | Calculated Property |
| Pvap | [1.35; 201.21] | kPa | [400.00; 569.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.46646e+02 | |||
| Coefficient B | -1.39168e+04 | |||
| Coefficient C | -1.88310e+01 | |||
| Coefficient D | 7.96535e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 400.00 | |||
| Temperature range, max. | 569.00 | |||
| Pvap | 1.35 | kPa | 400.00 | Calculated Property |
| Pvap | 3.07 | kPa | 418.78 | Calculated Property |
| Pvap | 6.36 | kPa | 437.56 | Calculated Property |
| Pvap | 12.19 | kPa | 456.33 | Calculated Property |
| Pvap | 21.89 | kPa | 475.11 | Calculated Property |
| Pvap | 37.14 | kPa | 493.89 | Calculated Property |
| Pvap | 60.02 | kPa | 512.67 | Calculated Property |
| Pvap | 93.00 | kPa | 531.44 | Calculated Property |
| Pvap | 138.96 | kPa | 550.22 | Calculated Property |
| Pvap | 201.21 | kPa | 569.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Cyclopentane, nonyl-.
Sources
- KDB Vapor Pressure Data
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Passut and Danner (1973), critical constants and acentric factors ChEDL chemicals 1.5.2, from Passut, C. A.; Danner, R. P. Acentric Factor. A Valuable Correlating Parameter for the Properties of Hydrocarbons. Ind. Eng. Chem. Process Des. Dev. 1973, 12, 365-368.
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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