- InChI
- InChI=1S/C19H40/c1-4-7-10-13-16-19(17-14-11-8-5-2)18-15-12-9-6-3/h19H,4-18H2,1-3H3
- InChI Key
- PLHNETQGLPOKGV-UHFFFAOYSA-N
- Formula
- C19H40
- SMILES
- CCCCCCC(CCCCCC)CCCCCC
- Molecular Weight1
- 268.52
- CAS
- 7225-66-3
- Other Names
-
- 7-Hexyltridecane
- ω : Acentric Factor.
- 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).
- 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 |
|---|---|---|---|
| ω | 0.7668 | Relay (1.0) Calculated Property | |
| ΔfG° | 106.66 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -433.99 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 41.44 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 83.84 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.50 | eV | Relay (1.0) Calculated Property |
| log10WS | -8.25 | Relay (1.0) Calculated Property | |
| logPoct/wat | 7.514 | Crippen Calculated Property | |
| McVol | 278.570 | ml/mol | McGowan Calculated Property |
| Pc | 1086.35 | kPa | Joback Calculated Property |
| Tboil | 570.82 | K | Relay (1.0) Calculated Property |
| Tc | 734.23 | K | Relay (1.0) Calculated Property |
| Tfus | [244.85; 244.90] | K |
|
| Tfus | 244.85 ± 0.50 | K | NIST |
| Tfus | 244.90 ± 0.60 | K | NIST |
| Vc | 1.072 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 75.20 | kJ/mol | 427.50 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [408.23; 1000.09] | 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 | -1.60650e+01 | |||
| Coefficient B | 1.81476e+00 | |||
| Coefficient C | -1.01300e-03 | |||
| Coefficient D | 2.14400e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 408.23 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 508.66 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 598.85 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 679.46 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 751.18 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 814.68 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 870.65 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 919.75 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 962.68 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 1000.09 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0215816; 0.0001626] | Pa×s | [244.88; 556.65] |
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 | -1.25640e+01 | |||
| Coefficient B | 2.13730e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 244.88 | |||
| Temperature range, max. | 556.65 | |||
| η | 0.0215816 | Pa×s | 244.88 | Calculated Property |
| η | 0.0073165 | Pa×s | 279.52 | Calculated Property |
| η | 0.0031487 | Pa×s | 314.16 | Calculated Property |
| η | 0.0016021 | Pa×s | 348.80 | Calculated Property |
| η | 0.0009210 | Pa×s | 383.44 | Calculated Property |
| η | 0.0005803 | Pa×s | 418.08 | Calculated Property |
| η | 0.0003925 | Pa×s | 452.72 | Calculated Property |
| η | 0.0002806 | Pa×s | 487.36 | Calculated Property |
| η | 0.0002097 | Pa×s | 522.01 | Calculated Property |
| η | 0.0001626 | Pa×s | 556.65 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [453.71; 613.56] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.62470e+01 | |||
| Coefficient B | -5.55297e+03 | |||
| Coefficient C | -1.05764e+02 | |||
| Temperature range, min. | 453.71 | |||
| Temperature range, max. | 613.56 | |||
| Pvap | 1.33 | kPa | 453.71 | Calculated Property |
| Pvap | 2.89 | kPa | 471.47 | Calculated Property |
| Pvap | 5.85 | kPa | 489.23 | Calculated Property |
| Pvap | 11.10 | kPa | 506.99 | Calculated Property |
| Pvap | 19.96 | kPa | 524.75 | Calculated Property |
| Pvap | 34.22 | kPa | 542.52 | Calculated Property |
| Pvap | 56.23 | kPa | 560.28 | Calculated Property |
| Pvap | 89.03 | kPa | 578.04 | Calculated Property |
| Pvap | 136.34 | kPa | 595.80 | Calculated Property |
| Pvap | 202.66 | kPa | 613.56 | Calculated Property |
Similar Compounds
Find more compounds similar to Tridecane, 7-hexyl-.
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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