- InChI
- InChI=1S/C14H28Br2/c15-13-11-9-7-5-3-1-2-4-6-8-10-12-14-16/h1-14H2
- InChI Key
- SDENLXLNLFKRAR-UHFFFAOYSA-N
- Formula
- C14H28Br2
- SMILES
- BrCCCCCCCCCCCCCCBr
- Molecular Weight1
- 356.19
- CAS
- 37688-96-3
- 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).
- 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 | 0.8639 | Relay (1.0) Calculated Property | |
| ΔfG° | 95.64 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -318.89 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 42.59 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 99.50 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.94 | eV | Relay (1.0) Calculated Property |
| log10WS | -7.43 | Relay (1.0) Calculated Property | |
| logPoct/wat | 6.457 | Crippen Calculated Property | |
| McVol | 243.120 | ml/mol | McGowan Calculated Property |
| Pc | 1701.90 | kPa | Joback Calculated Property |
| Tboil | 587.38 | K | Relay (1.0) Calculated Property |
| Tc | 770.12 | K | Relay (1.0) Calculated Property |
| Tfus | 319.45 | K | Relay (1.0) Calculated Property |
| Vc | 0.937 | m3/kmol | Relay (1.0) Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [330.45; 759.74] | 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 | 6.54400e+00 | |||
| Coefficient B | 1.41020e+00 | |||
| Coefficient C | -8.80600e-04 | |||
| Coefficient D | 2.23600e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 330.45 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 405.13 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 471.41 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 530.01 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 581.62 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 626.97 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 666.74 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 701.66 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 732.42 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 759.74 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0020272; 0.0002178] | Pa×s | [367.14; 585.19] |
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 | -1.21885e+01 | |||
| Coefficient B | 2.19824e+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. | 367.14 | |||
| Temperature range, max. | 585.19 | |||
| η | 0.0020272 | Pa×s | 367.14 | Calculated Property |
| η | 0.0013994 | Pa×s | 391.37 | Calculated Property |
| η | 0.0010086 | Pa×s | 415.59 | Calculated Property |
| η | 0.0007537 | Pa×s | 439.82 | Calculated Property |
| η | 0.0005806 | Pa×s | 464.05 | Calculated Property |
| η | 0.0004590 | Pa×s | 488.28 | Calculated Property |
| η | 0.0003710 | Pa×s | 512.50 | Calculated Property |
| η | 0.0003057 | Pa×s | 536.73 | Calculated Property |
| η | 0.0002561 | Pa×s | 560.96 | Calculated Property |
| η | 0.0002178 | Pa×s | 585.19 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [481.72; 633.59] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.74259e+01 | |||
| Coefficient B | -6.27642e+03 | |||
| Coefficient C | -1.15498e+02 | |||
| Temperature range, min. | 481.72 | |||
| Temperature range, max. | 633.59 | |||
| Pvap | 1.33 | kPa | 481.72 | Calculated Property |
| Pvap | 2.84 | kPa | 498.59 | Calculated Property |
| Pvap | 5.66 | kPa | 515.47 | Calculated Property |
| Pvap | 10.69 | kPa | 532.34 | Calculated Property |
| Pvap | 19.20 | kPa | 549.22 | Calculated Property |
| Pvap | 33.01 | kPa | 566.09 | Calculated Property |
| Pvap | 54.57 | kPa | 582.97 | Calculated Property |
| Pvap | 87.12 | kPa | 599.84 | Calculated Property |
| Pvap | 134.76 | kPa | 616.72 | Calculated Property |
| Pvap | 202.63 | kPa | 633.59 | Calculated Property |
Similar Compounds
Find more compounds similar to 1,14-dibromotetradecane.
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- The Yaws Handbook of Vapor Pressure
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