- InChI
- InChI=1S/C18H36/c1-2-3-4-5-6-7-8-9-10-11-12-15-18-16-13-14-17-18/h18H,2-17H2,1H3
- InChI Key
- NYZHNJGPFXHHNR-UHFFFAOYSA-N
- Formula
- C18H36
- SMILES
- CCCCCCCCCCCCCC1CCCC1
- Molecular Weight1
- 252.49
- CAS
- 6006-34-4
- Other Names
-
- n-Tridecylcyclopentane
- 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.
- γ : Surface Tension (N/m).
- 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 | [0.6970; 0.7546] |
|
|
| ω | 0.7546 | Passut and Danner (1973), critical constants and acentric factors Compiled value | |
| ω | 0.6970 | KDB | |
| ΔcH°liquid | -11874.60 ± 2.70 | kJ/mol | NIST |
| ΔfG° | 137.10 | kJ/mol | KDB |
| ΔfH°gas | [-354.00; -353.80] | kJ/mol |
|
| ΔfH°gas | -354.00 | kJ/mol | KDB |
| ΔfH°gas | -353.80 ± 2.90 | kJ/mol | NIST |
| ΔfusH° | 36.31 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 90.50 | kJ/mol | NIST |
| IE | 9.83 | eV | Relay (1.0) Calculated Property |
| log10WS | -7.91 | Relay (1.0) Calculated Property | |
| logPoct/wat | 6.878 | Crippen Calculated Property | |
| McVol | 253.620 | ml/mol | McGowan Calculated Property |
| Pc | [1206.58; 1310.00] | kPa |
|
| Pc | 1206.58 | kPa | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Pc | 1310.00 | kPa | KDB |
| Inp | 1862.00 | NIST | |
| Tboil | 598.60 | K | KDB |
| Tc | [761.37; 766.50] | K |
|
| Tc | 761.37 | K | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Tc | 766.50 | K | KDB |
| Tfus | 278.00 | K | KDB |
| Vc | 0.985 | m3/kmol | KDB |
| Zc | 0.2023660 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [54.31; 70.90] | kJ/mol | [548.50; 598.60] |
|
| ΔvapH | 70.90 | kJ/mol | 548.50 | NIST |
| ΔvapH | 54.31 | kJ/mol | 598.60 | KDB |
| ρl | 818.00 | kg/m3 | 293.00 | KDB |
| γ | 0.03 | N/m | 298.20 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [354.10; 931.26] | 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 | -7.39580e+01 | |||
| Coefficient B | 1.84552e+00 | |||
| Coefficient C | -1.08280e-03 | |||
| Coefficient D | 2.42500e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 354.10 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 454.16 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 543.45 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 622.73 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 692.77 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 754.35 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 808.21 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 855.15 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 895.91 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 931.26 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0080204; 0.0002930] | Pa×s | [278.00; 534.76] |
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 | -1.17186e+01 | |||
| Coefficient B | 1.91622e+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. | 278.00 | |||
| Temperature range, max. | 534.76 | |||
| η | 0.0080204 | Pa×s | 278.00 | Calculated Property |
| η | 0.0042227 | Pa×s | 306.53 | Calculated Property |
| η | 0.0024799 | Pa×s | 335.06 | Calculated Property |
| η | 0.0015832 | Pa×s | 363.59 | Calculated Property |
| η | 0.0010790 | Pa×s | 392.11 | Calculated Property |
| η | 0.0007746 | Pa×s | 420.64 | Calculated Property |
| η | 0.0005800 | Pa×s | 449.17 | Calculated Property |
| η | 0.0004495 | Pa×s | 477.70 | Calculated Property |
| η | 0.0003586 | Pa×s | 506.23 | Calculated Property |
| η | 0.0002930 | Pa×s | 534.76 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [453.35; 614.42] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.60970e+01 | |||
| Coefficient B | -5.46688e+03 | |||
| Coefficient C | -1.07550e+02 | |||
| Temperature range, min. | 453.35 | |||
| Temperature range, max. | 614.42 | |||
| Pvap | 1.33 | kPa | 453.35 | Calculated Property |
| Pvap | 2.90 | kPa | 471.25 | Calculated Property |
| Pvap | 5.87 | kPa | 489.14 | Calculated Property |
| Pvap | 11.16 | kPa | 507.04 | Calculated Property |
| Pvap | 20.07 | kPa | 524.94 | Calculated Property |
| Pvap | 34.39 | kPa | 542.83 | Calculated Property |
| Pvap | 56.47 | kPa | 560.73 | Calculated Property |
| Pvap | 89.30 | kPa | 578.63 | Calculated Property |
| Pvap | 136.55 | kPa | 596.52 | Calculated Property |
| Pvap | 202.65 | kPa | 614.42 | Calculated Property |
| Pvap | [1.32; 199.30] | kPa | [453.00; 634.00] |
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 | 1.85922e+02 | |||
| Coefficient B | -1.82187e+04 | |||
| Coefficient C | -2.40551e+01 | |||
| Coefficient D | 8.24385e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 453.00 | |||
| Temperature range, max. | 634.00 | |||
| Pvap | 1.32 | kPa | 453.00 | Calculated Property |
| Pvap | 2.99 | kPa | 473.11 | Calculated Property |
| Pvap | 6.20 | kPa | 493.22 | Calculated Property |
| Pvap | 11.91 | kPa | 513.33 | Calculated Property |
| Pvap | 21.42 | kPa | 533.44 | Calculated Property |
| Pvap | 36.42 | kPa | 553.56 | Calculated Property |
| Pvap | 59.00 | kPa | 573.67 | Calculated Property |
| Pvap | 91.63 | kPa | 593.78 | Calculated Property |
| Pvap | 137.27 | kPa | 613.89 | Calculated Property |
| Pvap | 199.30 | kPa | 634.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Tridecylcyclopentane.
Sources
- KDB Vapor Pressure Data
- 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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