- 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
- ω : Acentric Factor.
- 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.
- Ip : 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 |
|---|---|---|---|
| ω | 0.5490 | Relay (1.0) Calculated Property | |
| ΔfG° | 19.86 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -117.17 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfH°liquid | -163.00 | kJ/mol | NIST |
| ΔfusH° | 19.28 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 56.69 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 10.23 | eV | NIST |
| log10WS | -3.68 | Relay (1.0) 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 | 1178.00 | NIST | |
| Inp | 1208.00 | NIST | |
| Ip | [1662.00; 1712.00] |
|
|
| Ip | 1673.00 | NIST | |
| Ip | 1712.00 | NIST | |
| Ip | 1662.00 | NIST | |
| Ip | 1673.00 | NIST | |
| Tboil | 495.50 | K | NIST |
| Tc | 670.15 | K | Relay (1.0) Calculated Property |
| Tfus | [233.20; 233.65] | K |
|
| Tfus | 233.65 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 233.20 ± 0.40 | K | NIST |
| Vc | 0.426 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
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 |
|---|---|---|---|---|
| Cp,gas | [139.52; 295.43] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 1.47250e+01 | |||
| Coefficient B | 5.55200e-01 | |||
| Coefficient C | -3.91000e-04 | |||
| Coefficient D | 1.16500e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 139.52 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 167.36 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 191.71 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 212.94 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 231.42 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 247.52 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 261.60 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 274.03 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 285.18 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 295.43 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0064202; 0.0003827] | Pa×s | [233.43; 455.30] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.08352e+01 | |||
| Coefficient B | 1.35080e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 233.43 | |||
| Temperature range, max. | 455.30 | |||
| η | 0.0064202 | Pa×s | 233.43 | Calculated Property |
| η | 0.0036939 | Pa×s | 258.08 | Calculated Property |
| η | 0.0023403 | Pa×s | 282.73 | Calculated Property |
| η | 0.0015954 | Pa×s | 307.38 | Calculated Property |
| η | 0.0011512 | Pa×s | 332.04 | Calculated Property |
| η | 0.0008691 | Pa×s | 356.69 | Calculated Property |
| η | 0.0006803 | Pa×s | 381.34 | Calculated Property |
| η | 0.0005487 | Pa×s | 405.99 | Calculated Property |
| η | 0.0004535 | Pa×s | 430.65 | Calculated Property |
| η | 0.0003827 | Pa×s | 455.30 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [376.36; 524.03] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| 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
- 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-
- 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
Sources
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Cheméo Relay (1.0)
- 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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