- InChI
- InChI=1S/C5H10Br2/c6-4-2-1-3-5-7/h1-5H2
- InChI Key
- IBODDUNKEPPBKW-UHFFFAOYSA-N
- Formula
- C5H10Br2
- SMILES
- BrCCCCCBr
- Molecular Weight1
- 229.94
- CAS
- 111-24-0
- Other Names
-
- 1,5-Dibromopentane
- Br(CH2)5Br
- Dibromo-1,5 pentane
- Pentamethylene bromide
- Pentamethylene 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).
- ΔfH°liquid : Liquid phase 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).
- ΔvapH : Enthalpy of vaporization at a given temperature (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).
- n0 : Refractive Index.
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- 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° | 19.86 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -93.87 | kJ/mol | Joback Calculated Property |
| ΔfH°liquid | -163.00 | kJ/mol | NIST |
| ΔfusH° | 19.28 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 39.59 | kJ/mol | Joback Calculated Property |
| IE | 10.23 | eV | NIST |
| log10WS | -2.78 | Crippen Calculated Property | |
| logPoct/wat | 2.947 | Crippen Calculated Property | |
| McVol | 116.310 | ml/mol | McGowan Calculated Property |
| Pc | 4109.14 | kPa | Joback Calculated Property |
| Inp | [1170.00; 1208.00] |
|
|
| Inp | 1208.00 | NIST | |
| Inp | 1178.00 | NIST | |
| Inp | 1178.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1208.00 | NIST | |
| Inp | 1178.00 | NIST | |
| I | [1662.00; 1712.00] |
|
|
| I | 1673.00 | NIST | |
| I | 1712.00 | NIST | |
| I | 1662.00 | NIST | |
| I | 1673.00 | NIST | |
| Tboil | 495.50 | K | NIST |
| Tc | 650.13 | K | Joback Calculated Property |
| Tfus | 233.20 ± 0.40 | K | NIST |
| Vc | 0.440 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [194.94; 242.43] | J/mol×K | [446.12; 650.13] |
|
| Cp,gas | 194.94 | J/mol×K | 446.12 | Joback Calculated Property |
| Cp,gas | 204.05 | J/mol×K | 480.12 | Joback Calculated Property |
| Cp,gas | 212.65 | J/mol×K | 514.12 | Joback Calculated Property |
| Cp,gas | 220.76 | J/mol×K | 548.13 | Joback Calculated Property |
| Cp,gas | 228.41 | J/mol×K | 582.13 | Joback Calculated Property |
| Cp,gas | 235.62 | J/mol×K | 616.13 | Joback Calculated Property |
| Cp,gas | 242.43 | J/mol×K | 650.13 | Joback Calculated Property |
| Cp,liquid | [217.95; 234.28] | J/mol×K | [285.15; 355.15] |
|
| Cp,liquid | 217.95 | J/mol×K | 285.15 | Heat Ca... |
| Cp,liquid | 218.27 | J/mol×K | 286.65 | Heat Ca... |
| Cp,liquid | 218.58 | J/mol×K | 288.15 | Heat Ca... |
| Cp,liquid | 218.90 | J/mol×K | 289.65 | Heat Ca... |
| Cp,liquid | 219.22 | J/mol×K | 291.15 | Heat Ca... |
| Cp,liquid | 219.54 | J/mol×K | 292.65 | Heat Ca... |
| Cp,liquid | 219.76 | J/mol×K | 293.15 | Heat Ca... |
| Cp,liquid | 219.86 | J/mol×K | 294.15 | Heat Ca... |
| Cp,liquid | 219.98 | J/mol×K | 294.15 | Heat Ca... |
| Cp,liquid | 220.19 | J/mol×K | 295.15 | Heat Ca... |
| Cp,liquid | 220.18 | J/mol×K | 295.65 | Heat Ca... |
| Cp,liquid | 220.41 | J/mol×K | 296.15 | Heat Ca... |
| Cp,liquid | 220.66 | J/mol×K | 297.15 | Heat Ca... |
| Cp,liquid | 220.50 | J/mol×K | 297.15 | Heat Ca... |
| Cp,liquid | 220.72 | J/mol×K | 298.15 | Heat Ca... |
| Cp,liquid | 220.84 | J/mol×K | 298.15 | Heat Ca... |
| Cp,liquid | 220.83 | J/mol×K | 298.65 | Heat Ca... |
| Cp,liquid | 221.10 | J/mol×K | 299.15 | Heat Ca... |
| Cp,liquid | 221.16 | J/mol×K | 300.15 | Heat Ca... |
| Cp,liquid | 221.28 | J/mol×K | 300.15 | Heat Ca... |
| Cp,liquid | 221.49 | J/mol×K | 301.15 | Heat Ca... |
| Cp,liquid | 221.49 | J/mol×K | 301.65 | Heat Ca... |
| Cp,liquid | 221.73 | J/mol×K | 302.15 | Heat Ca... |
| Cp,liquid | 221.95 | J/mol×K | 303.15 | Heat Ca... |
| Cp,liquid | 221.82 | J/mol×K | 303.15 | Heat Ca... |
| Cp,liquid | 222.17 | J/mol×K | 304.15 | Heat Ca... |
| Cp,liquid | 222.15 | J/mol×K | 304.65 | Heat Ca... |
| Cp,liquid | 222.41 | J/mol×K | 305.15 | Heat Ca... |
| Cp,liquid | 222.48 | J/mol×K | 306.15 | Heat Ca... |
| Cp,liquid | 222.63 | J/mol×K | 306.15 | Heat Ca... |
| Cp,liquid | 222.85 | J/mol×K | 307.15 | Heat Ca... |
| Cp,liquid | 222.82 | J/mol×K | 307.65 | Heat Ca... |
| Cp,liquid | 223.09 | J/mol×K | 308.15 | Heat Ca... |
| Cp,liquid | 223.31 | J/mol×K | 309.15 | Heat Ca... |
| Cp,liquid | 223.16 | J/mol×K | 309.15 | Heat Ca... |
| Cp,liquid | 223.56 | J/mol×K | 310.15 | Heat Ca... |
| Cp,liquid | 223.50 | J/mol×K | 310.65 | Heat Ca... |
| Cp,liquid | 223.78 | J/mol×K | 311.15 | Heat Ca... |
| Cp,liquid | 224.03 | J/mol×K | 312.15 | Heat Ca... |
| Cp,liquid | 223.84 | J/mol×K | 312.15 | Heat Ca... |
| Cp,liquid | 224.26 | J/mol×K | 313.15 | Heat Ca... |
| Cp,liquid | 224.18 | J/mol×K | 313.65 | Heat Ca... |
| Cp,liquid | 224.52 | J/mol×K | 315.15 | Heat Ca... |
| Cp,liquid | 224.87 | J/mol×K | 316.65 | Heat Ca... |
| Cp,liquid | 225.21 | J/mol×K | 318.15 | Heat Ca... |
| Cp,liquid | 225.56 | J/mol×K | 319.65 | Heat Ca... |
| Cp,liquid | 225.91 | J/mol×K | 321.15 | Heat Ca... |
| Cp,liquid | 226.26 | J/mol×K | 322.65 | Heat Ca... |
| Cp,liquid | 226.62 | J/mol×K | 324.15 | Heat Ca... |
| Cp,liquid | 226.97 | J/mol×K | 325.65 | Heat Ca... |
| Cp,liquid | 227.33 | J/mol×K | 327.15 | Heat Ca... |
| Cp,liquid | 227.69 | J/mol×K | 328.65 | Heat Ca... |
| Cp,liquid | 228.05 | J/mol×K | 330.15 | Heat Ca... |
| Cp,liquid | 228.41 | J/mol×K | 331.65 | Heat Ca... |
| Cp,liquid | 228.77 | J/mol×K | 333.15 | Heat Ca... |
| Cp,liquid | 229.13 | J/mol×K | 334.65 | Heat Ca... |
| Cp,liquid | 229.50 | J/mol×K | 336.15 | Heat Ca... |
| Cp,liquid | 229.87 | J/mol×K | 337.65 | Heat Ca... |
| Cp,liquid | 230.24 | J/mol×K | 339.15 | Heat Ca... |
| Cp,liquid | 230.61 | J/mol×K | 340.65 | Heat Ca... |
| Cp,liquid | 230.98 | J/mol×K | 342.15 | Heat Ca... |
| Cp,liquid | 231.36 | J/mol×K | 343.65 | Heat Ca... |
| Cp,liquid | 231.73 | J/mol×K | 345.15 | Heat Ca... |
| Cp,liquid | 232.11 | J/mol×K | 346.65 | Heat Ca... |
| Cp,liquid | 232.49 | J/mol×K | 348.15 | Heat Ca... |
| Cp,liquid | 232.87 | J/mol×K | 349.65 | Heat Ca... |
| Cp,liquid | 233.25 | J/mol×K | 351.15 | Heat Ca... |
| Cp,liquid | 233.63 | J/mol×K | 352.65 | Heat Ca... |
| Cp,liquid | 234.02 | J/mol×K | 354.15 | Heat Ca... |
| Cp,liquid | 234.28 | J/mol×K | 355.15 | Heat Ca... |
| η | [0.0004068; 0.0031782] | Pa×s | [265.71; 446.12] |
|
| η | 0.0031782 | Pa×s | 265.71 | Joback Calculated Property |
| η | 0.0018956 | Pa×s | 295.78 | Joback Calculated Property |
| η | 0.0012437 | Pa×s | 325.85 | Joback Calculated Property |
| η | 0.0008762 | Pa×s | 355.91 | Joback Calculated Property |
| η | 0.0006520 | Pa×s | 385.98 | Joback Calculated Property |
| η | 0.0005063 | Pa×s | 416.05 | Joback Calculated Property |
| η | 0.0004068 | Pa×s | 446.12 | Joback Calculated Property |
| ΔvapH | 54.40 | kJ/mol | 472.50 | NIST |
| n0 | 1.50990 | 298.15 | Thermod... | |
| γ | [0.04; 0.04] | N/m | [293.15; 313.15] |
|
| γ | 0.04 | N/m | 293.15 | The add... |
| γ | 0.04 | N/m | 298.15 | The add... |
| γ | 0.04 | N/m | 303.15 | The add... |
| γ | 0.04 | N/m | 308.15 | The add... |
| γ | 0.04 | N/m | 313.15 | The add... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [383.00; 383.20] | K | [2.00; 2.00] |
|
| Tboilr | 383.20 | K | 2.00 | NIST |
| Tboilr | 383.00 | K | 2.00 | NIST |
Datasets
Speed of sound, m/s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Speed of sound, m/s - Liquid |
| 292.38 | 100.00 | 1149.48 |
| 292.47 | 91200.00 | 1353.98 |
| 292.48 | 30400.00 | 1226.21 |
| 292.50 | 45600.00 | 1260.76 |
| 292.52 | 60800.00 | 1293.37 |
| 292.53 | 15210.00 | 1189.09 |
| 292.57 | 101320.00 | 1372.23 |
| 292.59 | 76010.00 | 1324.36 |
| 298.00 | 60800.00 | 1281.15 |
| 298.00 | 91200.00 | 1342.44 |
| 298.00 | 101330.00 | 1361.63 |
| 298.01 | 45600.00 | 1247.97 |
| 298.02 | 30410.00 | 1212.72 |
| 298.03 | 15210.00 | 1174.79 |
| 298.05 | 76000.00 | 1312.6 |
| 298.37 | 100.00 | 1133.01 |
| 303.00 | 76000.00 | 1301.95 |
| 303.01 | 15200.00 | 1162.07 |
| 303.01 | 30400.00 | 1200.58 |
| 303.01 | 60790.00 | 1270.04 |
| 303.01 | 91200.00 | 1331.8 |
| 303.01 | 101340.00 | 1350.72 |
| 303.02 | 45600.00 | 1236.47 |
| 303.40 | 100.00 | 1119.29 |
| 308.03 | 15210.00 | 1148.74 |
| 308.03 | 30410.00 | 1187.74 |
| 308.03 | 45590.00 | 1223.97 |
| 308.05 | 101330.00 | 1340.01 |
| 308.06 | 60790.00 | 1257.88 |
| 308.06 | 76000.00 | 1290.08 |
| 308.06 | 91200.00 | 1320.46 |
| 308.38 | 100.00 | 1105.79 |
| 313.14 | 76030.00 | 1279.29 |
| 313.16 | 91210.00 | 1310.12 |
| 313.16 | 101330.00 | 1329.99 |
| 313.17 | 45610.00 | 1212.35 |
| 313.18 | 60800.00 | 1246.82 |
| 313.20 | 15210.00 | 1135.8 |
| 313.20 | 30410.00 | 1175.46 |
| 314.36 | 100.00 | 1089.74 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [376.36; 524.03] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.54315e+01 | |||
| Coefficient B | -4.50494e+03 | |||
| Coefficient C | -7.88850e+01 | |||
| Temperature range, min. | 376.36 | |||
| Temperature range, max. | 524.03 | |||
| Pvap | 1.33 | kPa | 376.36 | Calculated Property |
| Pvap | 2.94 | kPa | 392.77 | Calculated Property |
| Pvap | 6.00 | kPa | 409.18 | Calculated Property |
| Pvap | 11.45 | kPa | 425.58 | Calculated Property |
| Pvap | 20.59 | kPa | 441.99 | Calculated Property |
| Pvap | 35.21 | kPa | 458.40 | Calculated Property |
| Pvap | 57.58 | kPa | 474.81 | Calculated Property |
| Pvap | 90.55 | kPa | 491.21 | Calculated Property |
| Pvap | 137.56 | kPa | 507.62 | Calculated Property |
| Pvap | 202.63 | kPa | 524.03 | Calculated Property |
Similar Compounds
Find more compounds similar to Pentane, 1,5-dibromo-.
Mixtures
- Ethyl formate + Pentane, 1,5-dibromo-
- Pentane, 1,5-dibromo- + Ethyl Acetate
- Propanoic acid, ethyl ester + Pentane, 1,5-dibromo-
- Pentane, 1,5-dibromo- + Butanoic acid, ethyl ester
- Pentanoic acid, ethyl ester + Pentane, 1,5-dibromo-
- Pentane, 1,5-dibromo- + Methyl formate
- Pentane, 1,5-dibromo- + Acetic acid, methyl ester
- Pentane, 1,5-dibromo- + Methyl propionate
- Butanoic acid, methyl ester + Pentane, 1,5-dibromo-
- Pentane, 1,5-dibromo- + Methyl valerate
- Pentane, 1,5-dibromo- + Heptane
- Formic acid, butyl ester + Pentane, 1,5-dibromo-
- Pentane, 1,5-dibromo- + Acetic acid, butyl ester
- Propanoic acid, butyl ester + Pentane, 1,5-dibromo-
- Butanoic acid, butyl ester + Pentane, 1,5-dibromo-
Sources
- Crippen Method
- Crippen Method
- Thermodynamic and Acoustic Properties of 1,3-Dibromopropane and 1,5-Dibromopentane within the Temperature Range From 293K to 313K at Pressures up to 100MPa
- Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) II: HE m and V E m for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1 - x)a,x-BrCH2(CH2)v-2CH2Br}, where u = 1 to 5, a = 1 and v = x = 2 to 6
- Thermodynamic study of (alkyl esters + alpha,omega-alkyl dihalides) IV: Hex and Vex for 25 binary mixtures {xC(u-1)H(2u-1)CO2CH3 + (1-x)alpha,omega-BrCH2(CH2)(v-2)CH2Br}, where u = 1 to 5, alpha = 1 and v = omega = 2 to 6
- Thermodynamic study of (alkyl esters + alpha,beta-alkyl dihalides) VI.H and V for 20 binary mixtures {xCu-1H2u-1CO2(CH2)3CH3 + (1 - x)alpha,omega-BrCH2(CH2)v-2CH2Br}, where u = 1 to 5, alpha = 1, and v = omega = 2 to 6
- The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
- Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
- 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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