- 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.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
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] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 200 210 220 230 240 500 600 | ||||
| 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] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 220 225 230 235 300 320 340 | ||||
| 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] |
|
|
T(K) Dynamic viscosity (Pa×s) 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 300 350 400 450 | ||||
| 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] |
|
|
T(K) Surface Tension (N/m) 0.04 0.04 0.04 0.04 0.04 295 300 305 310 | ||||
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
| 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
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.