- InChI
- InChI=1S/C11H22Br2/c12-10-8-6-4-2-1-3-5-7-9-11-13/h1-11H2
- InChI Key
- SIBVHGAPHVRHMJ-UHFFFAOYSA-N
- Formula
- C11H22Br2
- SMILES
- BrCCCCCCCCCCCBr
- Molecular Weight1
- 314.10
- CAS
- 16696-65-4
- Other Names
-
- Undecamethylene dibromide
- Undecane, 1,11-dibromo-
- 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).
- 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° | 70.38 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -217.71 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 34.82 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 52.95 | kJ/mol | Joback Calculated Property |
| log10WS | -5.29 | Crippen Calculated Property | |
| logPoct/wat | 5.287 | Crippen Calculated Property | |
| McVol | 200.850 | ml/mol | McGowan Calculated Property |
| Pc | 2191.78 | kPa | Joback Calculated Property |
| Tboil | 583.40 | K | Joback Calculated Property |
| Tc | 772.41 | K | Joback Calculated Property |
| Tfus | 333.33 | K | Joback Calculated Property |
| Vc | 0.775 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [458.85; 536.96] | J/mol×K | [583.40; 772.41] | 
|
| Cp,gas | 458.85 | J/mol×K | 583.40 | Joback Calculated Property |
| Cp,gas | 473.59 | J/mol×K | 614.90 | Joback Calculated Property |
| Cp,gas | 487.60 | J/mol×K | 646.40 | Joback Calculated Property |
| Cp,gas | 500.90 | J/mol×K | 677.90 | Joback Calculated Property |
| Cp,gas | 513.54 | J/mol×K | 709.40 | Joback Calculated Property |
| Cp,gas | 525.55 | J/mol×K | 740.91 | Joback Calculated Property |
| Cp,gas | 536.96 | J/mol×K | 772.41 | Joback Calculated Property |
| Cp,liquid | [389.40; 425.41] | J/mol×K | [285.15; 355.15] |
|
| Cp,liquid | 389.40 | J/mol×K | 285.15 | Heat Ca... |
| Cp,liquid | 389.99 | J/mol×K | 286.65 | Heat Ca... |
| Cp,liquid | 390.59 | J/mol×K | 288.15 | Heat Ca... |
| Cp,liquid | 391.20 | J/mol×K | 289.65 | Heat Ca... |
| Cp,liquid | 391.83 | J/mol×K | 291.15 | Heat Ca... |
| Cp,liquid | 392.47 | J/mol×K | 292.65 | Heat Ca... |
| Cp,liquid | 393.12 | J/mol×K | 294.15 | Heat Ca... |
| Cp,liquid | 393.79 | J/mol×K | 295.65 | Heat Ca... |
| Cp,liquid | 394.47 | J/mol×K | 297.15 | Heat Ca... |
| Cp,liquid | 394.92 | J/mol×K | 298.15 | Heat Ca... |
| Cp,liquid | 395.16 | J/mol×K | 298.65 | Heat Ca... |
| Cp,liquid | 395.85 | J/mol×K | 300.15 | Heat Ca... |
| Cp,liquid | 396.56 | J/mol×K | 301.65 | Heat Ca... |
| Cp,liquid | 397.28 | J/mol×K | 303.15 | Heat Ca... |
| Cp,liquid | 398.01 | J/mol×K | 304.65 | Heat Ca... |
| Cp,liquid | 398.75 | J/mol×K | 306.15 | Heat Ca... |
| Cp,liquid | 399.50 | J/mol×K | 307.65 | Heat Ca... |
| Cp,liquid | 400.25 | J/mol×K | 309.15 | Heat Ca... |
| Cp,liquid | 401.02 | J/mol×K | 310.65 | Heat Ca... |
| Cp,liquid | 401.79 | J/mol×K | 312.15 | Heat Ca... |
| Cp,liquid | 402.57 | J/mol×K | 313.65 | Heat Ca... |
| Cp,liquid | 403.35 | J/mol×K | 315.15 | Heat Ca... |
| Cp,liquid | 404.15 | J/mol×K | 316.65 | Heat Ca... |
| Cp,liquid | 404.94 | J/mol×K | 318.15 | Heat Ca... |
| Cp,liquid | 405.75 | J/mol×K | 319.65 | Heat Ca... |
| Cp,liquid | 406.56 | J/mol×K | 321.15 | Heat Ca... |
| Cp,liquid | 407.37 | J/mol×K | 322.65 | Heat Ca... |
| Cp,liquid | 408.19 | J/mol×K | 324.15 | Heat Ca... |
| Cp,liquid | 409.01 | J/mol×K | 325.65 | Heat Ca... |
| Cp,liquid | 409.84 | J/mol×K | 327.15 | Heat Ca... |
| Cp,liquid | 410.67 | J/mol×K | 328.65 | Heat Ca... |
| Cp,liquid | 411.50 | J/mol×K | 330.15 | Heat Ca... |
| Cp,liquid | 412.33 | J/mol×K | 331.65 | Heat Ca... |
| Cp,liquid | 413.17 | J/mol×K | 333.15 | Heat Ca... |
| Cp,liquid | 414.01 | J/mol×K | 334.65 | Heat Ca... |
| Cp,liquid | 414.84 | J/mol×K | 336.15 | Heat Ca... |
| Cp,liquid | 415.68 | J/mol×K | 337.65 | Heat Ca... |
| Cp,liquid | 416.53 | J/mol×K | 339.15 | Heat Ca... |
| Cp,liquid | 417.37 | J/mol×K | 340.65 | Heat Ca... |
| Cp,liquid | 418.21 | J/mol×K | 342.15 | Heat Ca... |
| Cp,liquid | 419.04 | J/mol×K | 343.65 | Heat Ca... |
| Cp,liquid | 419.88 | J/mol×K | 345.15 | Heat Ca... |
| Cp,liquid | 420.72 | J/mol×K | 346.65 | Heat Ca... |
| Cp,liquid | 421.55 | J/mol×K | 348.15 | Heat Ca... |
| Cp,liquid | 422.38 | J/mol×K | 349.65 | Heat Ca... |
| Cp,liquid | 423.21 | J/mol×K | 351.15 | Heat Ca... |
| Cp,liquid | 424.04 | J/mol×K | 352.65 | Heat Ca... |
| Cp,liquid | 424.86 | J/mol×K | 354.15 | Heat Ca... |
| Cp,liquid | 425.41 | J/mol×K | 355.15 | Heat Ca... |
| η | [0.0002175; 0.0025544] | Pa×s | [333.33; 583.40] |
|
| η | 0.0025544 | Pa×s | 333.33 | Joback Calculated Property |
| η | 0.0013486 | Pa×s | 375.01 | Joback Calculated Property |
| η | 0.0008090 | Pa×s | 416.69 | Joback Calculated Property |
| η | 0.0005326 | Pa×s | 458.37 | Joback Calculated Property |
| η | 0.0003759 | Pa×s | 500.04 | Joback Calculated Property |
| η | 0.0002800 | Pa×s | 541.72 | Joback Calculated Property |
| η | 0.0002175 | Pa×s | 583.40 | Joback Calculated Property |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 464.20 | K | 2.40 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [442.52; 589.90] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.69232e+01 | |||
| Coefficient B | -5.66681e+03 | |||
| Coefficient C | -1.01876e+02 | |||
| Temperature range, min. | 442.52 | |||
| Temperature range, max. | 589.90 | |||
| Pvap | 1.33 | kPa | 442.52 | Calculated Property |
| Pvap | 2.86 | kPa | 458.90 | Calculated Property |
| Pvap | 5.74 | kPa | 475.27 | Calculated Property |
| Pvap | 10.85 | kPa | 491.65 | Calculated Property |
| Pvap | 19.50 | kPa | 508.02 | Calculated Property |
| Pvap | 33.49 | kPa | 524.40 | Calculated Property |
| Pvap | 55.24 | kPa | 540.77 | Calculated Property |
| Pvap | 87.89 | kPa | 557.15 | Calculated Property |
| Pvap | 135.40 | kPa | 573.52 | Calculated Property |
| Pvap | 202.64 | kPa | 589.90 | Calculated Property |
Similar Compounds
Find more compounds similar to 1,11-Dibromoundecane.
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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