- InChI
- InChI=1S/C9H18Br2/c10-8-6-4-2-1-3-5-7-9-11/h1-9H2
- InChI Key
- WGAXVZXBFBHLMC-UHFFFAOYSA-N
- Formula
- C9H18Br2
- SMILES
- BrCCCCCCCCCBr
- Molecular Weight1
- 286.05
- CAS
- 4549-33-1
- Other Names
-
- 1,9-Dibromononane
- NONAMETHYLENE 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).
- 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° | 53.54 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -176.43 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 29.64 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 48.50 | kJ/mol | Joback Calculated Property |
| log10WS | -4.45 | Crippen Calculated Property | |
| logPoct/wat | 4.507 | Crippen Calculated Property | |
| McVol | 172.670 | ml/mol | McGowan Calculated Property |
| Pc | 2646.11 | kPa | Joback Calculated Property |
| Inp | 1607.00 | NIST | |
| Tboil | [559.00; 559.70] | K |
|
| Tboil | 559.70 | K | NIST |
| Tboil | 559.00 | K | NIST |
| Tc | 731.36 | K | Joback Calculated Property |
| Tfus | 310.79 | K | Joback Calculated Property |
| Vc | 0.663 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [363.47; 433.72] | J/mol×K | [537.64; 731.36] |
|
| Cp,gas | 363.47 | J/mol×K | 537.64 | Joback Calculated Property |
| Cp,gas | 376.78 | J/mol×K | 569.93 | Joback Calculated Property |
| Cp,gas | 389.40 | J/mol×K | 602.21 | Joback Calculated Property |
| Cp,gas | 401.38 | J/mol×K | 634.50 | Joback Calculated Property |
| Cp,gas | 412.73 | J/mol×K | 666.79 | Joback Calculated Property |
| Cp,gas | 423.50 | J/mol×K | 699.07 | Joback Calculated Property |
| Cp,gas | 433.72 | J/mol×K | 731.36 | Joback Calculated Property |
| Cp,liquid | [330.90; 360.95] | J/mol×K | [286.65; 355.15] |
|
| Cp,liquid | 330.90 | J/mol×K | 286.65 | Heat Ca... |
| Cp,liquid | 331.44 | J/mol×K | 288.15 | Heat Ca... |
| Cp,liquid | 332.00 | J/mol×K | 289.65 | Heat Ca... |
| Cp,liquid | 332.56 | J/mol×K | 291.15 | Heat Ca... |
| Cp,liquid | 333.14 | J/mol×K | 292.65 | Heat Ca... |
| Cp,liquid | 333.72 | J/mol×K | 294.15 | Heat Ca... |
| Cp,liquid | 334.30 | J/mol×K | 295.65 | Heat Ca... |
| Cp,liquid | 334.90 | J/mol×K | 297.15 | Heat Ca... |
| Cp,liquid | 335.29 | J/mol×K | 298.15 | Heat Ca... |
| Cp,liquid | 335.50 | J/mol×K | 298.65 | Heat Ca... |
| Cp,liquid | 336.10 | J/mol×K | 300.15 | Heat Ca... |
| Cp,liquid | 336.72 | J/mol×K | 301.65 | Heat Ca... |
| Cp,liquid | 337.34 | J/mol×K | 303.15 | Heat Ca... |
| Cp,liquid | 337.96 | J/mol×K | 304.65 | Heat Ca... |
| Cp,liquid | 338.59 | J/mol×K | 306.15 | Heat Ca... |
| Cp,liquid | 339.23 | J/mol×K | 307.65 | Heat Ca... |
| Cp,liquid | 339.87 | J/mol×K | 309.15 | Heat Ca... |
| Cp,liquid | 340.52 | J/mol×K | 310.65 | Heat Ca... |
| Cp,liquid | 341.17 | J/mol×K | 312.15 | Heat Ca... |
| Cp,liquid | 341.83 | J/mol×K | 313.65 | Heat Ca... |
| Cp,liquid | 342.49 | J/mol×K | 315.15 | Heat Ca... |
| Cp,liquid | 343.16 | J/mol×K | 316.65 | Heat Ca... |
| Cp,liquid | 343.83 | J/mol×K | 318.15 | Heat Ca... |
| Cp,liquid | 344.50 | J/mol×K | 319.65 | Heat Ca... |
| Cp,liquid | 345.18 | J/mol×K | 321.15 | Heat Ca... |
| Cp,liquid | 345.86 | J/mol×K | 322.65 | Heat Ca... |
| Cp,liquid | 346.54 | J/mol×K | 324.15 | Heat Ca... |
| Cp,liquid | 347.22 | J/mol×K | 325.65 | Heat Ca... |
| Cp,liquid | 347.91 | J/mol×K | 327.15 | Heat Ca... |
| Cp,liquid | 348.60 | J/mol×K | 328.65 | Heat Ca... |
| Cp,liquid | 349.30 | J/mol×K | 330.15 | Heat Ca... |
| Cp,liquid | 349.99 | J/mol×K | 331.65 | Heat Ca... |
| Cp,liquid | 350.69 | J/mol×K | 333.15 | Heat Ca... |
| Cp,liquid | 351.39 | J/mol×K | 334.65 | Heat Ca... |
| Cp,liquid | 352.08 | J/mol×K | 336.15 | Heat Ca... |
| Cp,liquid | 352.78 | J/mol×K | 337.65 | Heat Ca... |
| Cp,liquid | 353.49 | J/mol×K | 339.15 | Heat Ca... |
| Cp,liquid | 354.19 | J/mol×K | 340.65 | Heat Ca... |
| Cp,liquid | 354.89 | J/mol×K | 342.15 | Heat Ca... |
| Cp,liquid | 355.59 | J/mol×K | 343.65 | Heat Ca... |
| Cp,liquid | 356.29 | J/mol×K | 345.15 | Heat Ca... |
| Cp,liquid | 356.99 | J/mol×K | 346.65 | Heat Ca... |
| Cp,liquid | 357.69 | J/mol×K | 348.15 | Heat Ca... |
| Cp,liquid | 358.39 | J/mol×K | 349.65 | Heat Ca... |
| Cp,liquid | 359.09 | J/mol×K | 351.15 | Heat Ca... |
| Cp,liquid | 359.79 | J/mol×K | 352.65 | Heat Ca... |
| Cp,liquid | 360.49 | J/mol×K | 354.15 | Heat Ca... |
| Cp,liquid | 360.95 | J/mol×K | 355.15 | Heat Ca... |
| η | [0.0002747; 0.0028667] | Pa×s | [310.79; 537.64] |
|
| η | 0.0028667 | Pa×s | 310.79 | Joback Calculated Property |
| η | 0.0015688 | Pa×s | 348.60 | Joback Calculated Property |
| η | 0.0009660 | Pa×s | 386.41 | Joback Calculated Property |
| η | 0.0006486 | Pa×s | 424.21 | Joback Calculated Property |
| η | 0.0004648 | Pa×s | 462.02 | Joback Calculated Property |
| η | 0.0003503 | Pa×s | 499.83 | Joback Calculated Property |
| η | 0.0002747 | Pa×s | 537.64 | Joback Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [414.52; 596.02] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.42348e+01 | |||
| Coefficient B | -4.49622e+03 | |||
| Coefficient C | -9.21460e+01 | |||
| Temperature range, min. | 414.52 | |||
| Temperature range, max. | 596.02 | |||
| Pvap | 1.33 | kPa | 414.52 | Calculated Property |
| Pvap | 3.03 | kPa | 434.69 | Calculated Property |
| Pvap | 6.29 | kPa | 454.85 | Calculated Property |
| Pvap | 12.08 | kPa | 475.02 | Calculated Property |
| Pvap | 21.74 | kPa | 495.19 | Calculated Property |
| Pvap | 36.99 | kPa | 515.35 | Calculated Property |
| Pvap | 59.97 | kPa | 535.52 | Calculated Property |
| Pvap | 93.23 | kPa | 555.69 | Calculated Property |
| Pvap | 139.70 | kPa | 575.85 | Calculated Property |
| Pvap | 202.65 | kPa | 596.02 | Calculated Property |
Similar Compounds
Find more compounds similar to Nonane, 1,9-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
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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