- InChI
- InChI=1S/C16H34/c1-5-6-7-8-9-10-11-12-13-14-15-16(2,3)4/h5-15H2,1-4H3
- InChI Key
- VCAMXEBNASZVEZ-UHFFFAOYSA-N
- Formula
- C16H34
- SMILES
- CCCCCCCCCCCCC(C)(C)C
- Molecular Weight1
- 226.44
- CAS
- 59222-86-5
- Other Names
-
- 2,2-Dimethyltetradecane
- 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).
- 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).
- 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 |
|---|---|---|---|
| ω | 0.6536 | Relay (1.0) Calculated Property | |
| ΔfG° | 86.68 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -395.23 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 29.78 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 74.41 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.56 | eV | Relay (1.0) Calculated Property |
| log10WS | -7.65 | Relay (1.0) Calculated Property | |
| logPoct/wat | 6.344 | Crippen Calculated Property | |
| McVol | 236.300 | ml/mol | McGowan Calculated Property |
| Pc | 1336.86 | kPa | Joback Calculated Property |
| Inp | 1515.00 | NIST | |
| Tboil | 538.09 | K | Relay (1.0) Calculated Property |
| Tc | 699.30 | K | Relay (1.0) Calculated Property |
| Tfus | 260.59 | K | Relay (1.0) Calculated Property |
| Vc | 0.928 | m3/kmol | Relay (1.0) Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [343.44; 846.25] | 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 | -3.61290e+01 | |||
| Coefficient B | 1.64968e+00 | |||
| Coefficient C | -1.01840e-03 | |||
| Coefficient D | 2.51100e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 343.44 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 431.15 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 509.04 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 577.92 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 638.57 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 691.79 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 738.37 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 779.11 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 814.81 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 846.25 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0068269; 0.0002029] | Pa×s | [272.50; 509.94] |
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 | -1.25375e+01 | |||
| Coefficient B | 2.05754e+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. | 272.50 | |||
| Temperature range, max. | 509.94 | |||
| η | 0.0068269 | Pa×s | 272.50 | Calculated Property |
| η | 0.0035056 | Pa×s | 298.88 | Calculated Property |
| η | 0.0020057 | Pa×s | 325.27 | Calculated Property |
| η | 0.0012478 | Pa×s | 351.65 | Calculated Property |
| η | 0.0008295 | Pa×s | 378.03 | Calculated Property |
| η | 0.0005816 | Pa×s | 404.41 | Calculated Property |
| η | 0.0004259 | Pa×s | 430.80 | Calculated Property |
| η | 0.0003233 | Pa×s | 457.18 | Calculated Property |
| η | 0.0002529 | Pa×s | 483.56 | Calculated Property |
| η | 0.0002029 | Pa×s | 509.94 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [412.24; 581.17] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.40409e+01 | |||
| Coefficient B | -4.03710e+03 | |||
| Coefficient C | -1.18700e+02 | |||
| Temperature range, min. | 412.24 | |||
| Temperature range, max. | 581.17 | |||
| Pvap | 1.33 | kPa | 412.24 | Calculated Property |
| Pvap | 3.05 | kPa | 431.01 | Calculated Property |
| Pvap | 6.34 | kPa | 449.78 | Calculated Property |
| Pvap | 12.20 | kPa | 468.55 | Calculated Property |
| Pvap | 21.95 | kPa | 487.32 | Calculated Property |
| Pvap | 37.32 | kPa | 506.09 | Calculated Property |
| Pvap | 60.41 | kPa | 524.86 | Calculated Property |
| Pvap | 93.72 | kPa | 543.63 | Calculated Property |
| Pvap | 140.07 | kPa | 562.40 | Calculated Property |
| Pvap | 202.64 | kPa | 581.17 | Calculated Property |
Similar Compounds
Find more compounds similar to Tetradecane, 2,2-dimethyl-.
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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