- InChI
- InChI=1S/C4H8BrCl/c5-3-1-2-4-6/h1-4H2
- InChI Key
- NIDSRGCVYOEDFW-UHFFFAOYSA-N
- Formula
- C4H8BrCl
- SMILES
- ClCCCCBr
- Molecular Weight1
- 171.46
- CAS
- 6940-78-9
- Other Names
-
- 1-Bromo-4-chlorobutane
- 1-Chloro-4-bromobutane
- 4-Bromo-1-chlorobutane
- Tetramethylene chlorobromide
- 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).
- Inp : Non-polar retention indices.
- 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° | -14.81 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -115.30 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 15.60 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 35.32 | kJ/mol | Joback Calculated Property |
| log10WS | -2.08 | Crippen Calculated Property | |
| logPoct/wat | 2.400 | Crippen Calculated Property | |
| McVol | 96.960 | ml/mol | McGowan Calculated Property |
| Pc | 4056.96 | kPa | Joback Calculated Property |
| Inp | [986.30; 991.90] |
|
|
| Inp | 991.90 | NIST | |
| Inp | 986.30 | NIST | |
| Inp | 991.90 | NIST | |
| Tboil | 394.51 | K | Joback Calculated Property |
| Tc | 588.79 | K | Joback Calculated Property |
| Tfus | 224.56 | K | Joback Calculated Property |
| Vc | 0.370 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [149.93; 190.02] | J/mol×K | [394.51; 588.79] |
|
| Cp,gas | 149.93 | J/mol×K | 394.51 | Joback Calculated Property |
| Cp,gas | 157.52 | J/mol×K | 426.89 | Joback Calculated Property |
| Cp,gas | 164.73 | J/mol×K | 459.27 | Joback Calculated Property |
| Cp,gas | 171.57 | J/mol×K | 491.65 | Joback Calculated Property |
| Cp,gas | 178.05 | J/mol×K | 524.03 | Joback Calculated Property |
| Cp,gas | 184.20 | J/mol×K | 556.41 | Joback Calculated Property |
| Cp,gas | 190.02 | J/mol×K | 588.79 | Joback Calculated Property |
| Cp,liquid | [189.62; 202.14] | J/mol×K | [285.15; 355.15] |
|
| Cp,liquid | 189.62 | J/mol×K | 285.15 | Heat Ca... |
| Cp,liquid | 189.85 | J/mol×K | 286.65 | Heat Ca... |
| Cp,liquid | 190.08 | J/mol×K | 288.15 | Heat Ca... |
| Cp,liquid | 190.32 | J/mol×K | 289.65 | Heat Ca... |
| Cp,liquid | 190.55 | J/mol×K | 291.15 | Heat Ca... |
| Cp,liquid | 190.79 | J/mol×K | 292.65 | Heat Ca... |
| Cp,liquid | 191.03 | J/mol×K | 294.15 | Heat Ca... |
| Cp,liquid | 191.27 | J/mol×K | 295.65 | Heat Ca... |
| Cp,liquid | 191.52 | J/mol×K | 297.15 | Heat Ca... |
| Cp,liquid | 191.68 | J/mol×K | 298.15 | Heat Ca... |
| Cp,liquid | 191.76 | J/mol×K | 298.65 | Heat Ca... |
| Cp,liquid | 192.01 | J/mol×K | 300.15 | Heat Ca... |
| Cp,liquid | 192.26 | J/mol×K | 301.65 | Heat Ca... |
| Cp,liquid | 192.51 | J/mol×K | 303.15 | Heat Ca... |
| Cp,liquid | 192.76 | J/mol×K | 304.65 | Heat Ca... |
| Cp,liquid | 193.01 | J/mol×K | 306.15 | Heat Ca... |
| Cp,liquid | 193.26 | J/mol×K | 307.65 | Heat Ca... |
| Cp,liquid | 193.52 | J/mol×K | 309.15 | Heat Ca... |
| Cp,liquid | 193.78 | J/mol×K | 310.65 | Heat Ca... |
| Cp,liquid | 194.04 | J/mol×K | 312.15 | Heat Ca... |
| Cp,liquid | 194.30 | J/mol×K | 313.65 | Heat Ca... |
| Cp,liquid | 194.56 | J/mol×K | 315.15 | Heat Ca... |
| Cp,liquid | 194.82 | J/mol×K | 316.65 | Heat Ca... |
| Cp,liquid | 195.09 | J/mol×K | 318.15 | Heat Ca... |
| Cp,liquid | 195.35 | J/mol×K | 319.65 | Heat Ca... |
| Cp,liquid | 195.62 | J/mol×K | 321.15 | Heat Ca... |
| Cp,liquid | 195.89 | J/mol×K | 322.65 | Heat Ca... |
| Cp,liquid | 196.16 | J/mol×K | 324.15 | Heat Ca... |
| Cp,liquid | 196.44 | J/mol×K | 325.65 | Heat Ca... |
| Cp,liquid | 196.71 | J/mol×K | 327.15 | Heat Ca... |
| Cp,liquid | 196.99 | J/mol×K | 328.65 | Heat Ca... |
| Cp,liquid | 197.27 | J/mol×K | 330.15 | Heat Ca... |
| Cp,liquid | 197.55 | J/mol×K | 331.65 | Heat Ca... |
| Cp,liquid | 197.83 | J/mol×K | 333.15 | Heat Ca... |
| Cp,liquid | 198.11 | J/mol×K | 334.65 | Heat Ca... |
| Cp,liquid | 198.40 | J/mol×K | 336.15 | Heat Ca... |
| Cp,liquid | 198.68 | J/mol×K | 337.65 | Heat Ca... |
| Cp,liquid | 198.97 | J/mol×K | 339.15 | Heat Ca... |
| Cp,liquid | 199.26 | J/mol×K | 340.65 | Heat Ca... |
| Cp,liquid | 199.55 | J/mol×K | 342.15 | Heat Ca... |
| Cp,liquid | 199.84 | J/mol×K | 343.65 | Heat Ca... |
| Cp,liquid | 200.14 | J/mol×K | 345.15 | Heat Ca... |
| Cp,liquid | 200.43 | J/mol×K | 346.65 | Heat Ca... |
| Cp,liquid | 200.73 | J/mol×K | 348.15 | Heat Ca... |
| Cp,liquid | 201.03 | J/mol×K | 349.65 | Heat Ca... |
| Cp,liquid | 201.33 | J/mol×K | 351.15 | Heat Ca... |
| Cp,liquid | 201.63 | J/mol×K | 352.65 | Heat Ca... |
| Cp,liquid | 201.93 | J/mol×K | 354.15 | Heat Ca... |
| Cp,liquid | 202.14 | J/mol×K | 355.15 | Heat Ca... |
| η | [0.0004065; 0.0036433] | Pa×s | [224.56; 394.51] |
|
| η | 0.0036433 | Pa×s | 224.56 | Joback Calculated Property |
| η | 0.0020600 | Pa×s | 252.88 | Joback Calculated Property |
| η | 0.0013065 | Pa×s | 281.21 | Joback Calculated Property |
| η | 0.0009006 | Pa×s | 309.53 | Joback Calculated Property |
| η | 0.0006608 | Pa×s | 337.86 | Joback Calculated Property |
| η | 0.0005086 | Pa×s | 366.19 | Joback Calculated Property |
| η | 0.0004065 | Pa×s | 394.51 | Joback Calculated Property |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [354.00; 354.20] | K | [4.00; 4.00] |
|
| Tboilr | 354.20 | K | 4.00 | NIST |
| Tboilr | 354.00 | K | 4.00 | NIST |
| Tboilr | 354.00 ± 1.00 | K | 4.00 | NIST |
Similar Compounds
Find more compounds similar to Butane, 1-bromo-4-chloro-.
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
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