- InChI
- InChI=1S/C12H24Br2/c13-11-9-7-5-3-1-2-4-6-8-10-12-14/h1-12H2
- InChI Key
- ZJJATABWMGVVRZ-UHFFFAOYSA-N
- Formula
- C12H24Br2
- SMILES
- BrCCCCCCCCCCCCBr
- Molecular Weight1
- 328.13
- CAS
- 3344-70-5
- Other Names
-
- 1,12-Dibromododecane
- Dodecamethylene dibromide
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase 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).
- 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).
- Tboilr : Boiling point at reduced pressure (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 |
|---|---|---|---|
| ΔfG° | 78.80 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -238.35 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 37.41 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 55.18 | kJ/mol | Joback Calculated Property |
| log10WS | -5.71 | Crippen Calculated Property | |
| logPoct/wat | 5.677 | Crippen Calculated Property | |
| McVol | 214.940 | ml/mol | McGowan Calculated Property |
| Pc | 2007.30 | kPa | Joback Calculated Property |
| Inp | 1946.00 | NIST | |
| Tboil | 606.28 | K | Joback Calculated Property |
| Tc | 793.23 | K | Joback Calculated Property |
| Tfus | 344.60 | K | Joback Calculated Property |
| Vc | 0.832 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [508.98; 590.36] | J/mol×K | [606.28; 793.23] | 
|
| Cp,gas | 508.98 | J/mol×K | 606.28 | Joback Calculated Property |
| Cp,gas | 524.31 | J/mol×K | 637.44 | Joback Calculated Property |
| Cp,gas | 538.89 | J/mol×K | 668.60 | Joback Calculated Property |
| Cp,gas | 552.74 | J/mol×K | 699.75 | Joback Calculated Property |
| Cp,gas | 565.92 | J/mol×K | 730.91 | Joback Calculated Property |
| Cp,gas | 578.44 | J/mol×K | 762.07 | Joback Calculated Property |
| Cp,gas | 590.36 | J/mol×K | 793.23 | Joback Calculated Property |
| Cp,liquid | [432.62; 457.90] | J/mol×K | [310.65; 355.15] |
|
| Cp,liquid | 432.62 | J/mol×K | 310.65 | Heat Ca... |
| Cp,liquid | 433.39 | J/mol×K | 312.15 | Heat Ca... |
| Cp,liquid | 434.17 | J/mol×K | 313.65 | Heat Ca... |
| Cp,liquid | 434.98 | J/mol×K | 315.15 | Heat Ca... |
| Cp,liquid | 435.79 | J/mol×K | 316.65 | Heat Ca... |
| Cp,liquid | 436.62 | J/mol×K | 318.15 | Heat Ca... |
| Cp,liquid | 437.46 | J/mol×K | 319.65 | Heat Ca... |
| Cp,liquid | 438.31 | J/mol×K | 321.15 | Heat Ca... |
| Cp,liquid | 439.17 | J/mol×K | 322.65 | Heat Ca... |
| Cp,liquid | 440.04 | J/mol×K | 324.15 | Heat Ca... |
| Cp,liquid | 440.91 | J/mol×K | 325.65 | Heat Ca... |
| Cp,liquid | 441.80 | J/mol×K | 327.15 | Heat Ca... |
| Cp,liquid | 442.68 | J/mol×K | 328.65 | Heat Ca... |
| Cp,liquid | 443.57 | J/mol×K | 330.15 | Heat Ca... |
| Cp,liquid | 444.47 | J/mol×K | 331.65 | Heat Ca... |
| Cp,liquid | 445.36 | J/mol×K | 333.15 | Heat Ca... |
| Cp,liquid | 446.26 | J/mol×K | 334.65 | Heat Ca... |
| Cp,liquid | 447.15 | J/mol×K | 336.15 | Heat Ca... |
| Cp,liquid | 448.04 | J/mol×K | 337.65 | Heat Ca... |
| Cp,liquid | 448.93 | J/mol×K | 339.15 | Heat Ca... |
| Cp,liquid | 449.82 | J/mol×K | 340.65 | Heat Ca... |
| Cp,liquid | 450.69 | J/mol×K | 342.15 | Heat Ca... |
| Cp,liquid | 451.57 | J/mol×K | 343.65 | Heat Ca... |
| Cp,liquid | 452.43 | J/mol×K | 345.15 | Heat Ca... |
| Cp,liquid | 453.29 | J/mol×K | 346.65 | Heat Ca... |
| Cp,liquid | 454.13 | J/mol×K | 348.15 | Heat Ca... |
| Cp,liquid | 454.96 | J/mol×K | 349.65 | Heat Ca... |
| Cp,liquid | 455.78 | J/mol×K | 351.15 | Heat Ca... |
| Cp,liquid | 456.59 | J/mol×K | 352.65 | Heat Ca... |
| Cp,liquid | 457.38 | J/mol×K | 354.15 | Heat Ca... |
| Cp,liquid | 457.90 | J/mol×K | 355.15 | Heat Ca... |
| η | [0.0001921; 0.0023816] | Pa×s | [344.60; 606.28] |
|
| η | 0.0023816 | Pa×s | 344.60 | Joback Calculated Property |
| η | 0.0012368 | Pa×s | 388.21 | Joback Calculated Property |
| η | 0.0007332 | Pa×s | 431.83 | Joback Calculated Property |
| η | 0.0004784 | Pa×s | 475.44 | Joback Calculated Property |
| η | 0.0003354 | Pa×s | 519.05 | Joback Calculated Property |
| η | 0.0002484 | Pa×s | 562.67 | Joback Calculated Property |
| η | 0.0001921 | Pa×s | 606.28 | Joback Calculated Property |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 488.20 | K | 2.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [456.92; 604.60] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.72197e+01 | |||
| Coefficient B | -5.92693e+03 | |||
| Coefficient C | -1.06880e+02 | |||
| Temperature range, min. | 456.92 | |||
| Temperature range, max. | 604.60 | |||
| Pvap | 1.33 | kPa | 456.92 | Calculated Property |
| Pvap | 2.85 | kPa | 473.33 | Calculated Property |
| Pvap | 5.69 | kPa | 489.74 | Calculated Property |
| Pvap | 10.75 | kPa | 506.15 | Calculated Property |
| Pvap | 19.32 | kPa | 522.56 | Calculated Property |
| Pvap | 33.20 | kPa | 538.96 | Calculated Property |
| Pvap | 54.85 | kPa | 555.37 | Calculated Property |
| Pvap | 87.44 | kPa | 571.78 | Calculated Property |
| Pvap | 135.04 | kPa | 588.19 | Calculated Property |
| Pvap | 202.67 | kPa | 604.60 | Calculated Property |
Similar Compounds
Find more compounds similar to Dodecane, 1,12-dibromo-.
Sources
- Crippen Method
- Crippen Method
- Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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