- InChI
- InChI=1S/C2H4BrCl/c3-1-2-4/h1-2H2
- InChI Key
- IBYHHJPAARCAIE-UHFFFAOYSA-N
- Formula
- C2H4BrCl
- SMILES
- ClCCBr
- Molecular Weight1
- 143.41
- CAS
- 107-04-0
- Other Names
-
- 1,2-Bromochloroethane
- 1,2-Chlorobromoethane
- 1-Bromo-2-chloroethane
- 1-Chloro-2-bromoethane
- 1-bromo-2-chloroethyne
- 2-Bromo-1-chloroethane
- 2-Bromoethyl chloride
- 2-Chloroethyl bromide
- CH2BrCH2Cl
- Ethylene chlorobromide
- NSC 60186
- s-Chlorobromoethane
- sym-Chlorobromoethane
- «beta»-Chloroethyl bromide
- «beta»-Chloroethyl bromide
- 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).
- ΔfusH : Enthalpy of fusion at a given temperature (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).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- 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.
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° | -31.65 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -74.02 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 10.42 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 38.13 ± 0.04 | kJ/mol | NIST |
| IE | [10.50; 10.70] | eV |
|
| IE | 10.57 ± 0.05 | eV | NIST |
| IE | 10.55 | eV | NIST |
| IE | 10.52 | eV | NIST |
| IE | 10.63 ± 0.03 | eV | NIST |
| IE | 10.63 | eV | NIST |
| IE | 10.50 ± 0.10 | eV | NIST |
| IE | 10.70 ± 0.10 | eV | NIST |
| IE | 10.65 ± 0.01 | eV | NIST |
| log10WS | [-1.32; -1.32] |
|
|
| log10WS | -1.32 | Aq. Sol... | |
| log10WS | -1.32 | Estimat... | |
| logPoct/wat | 1.620 | Crippen Calculated Property | |
| McVol | 68.780 | ml/mol | McGowan Calculated Property |
| Pc | 5266.25 | kPa | Joback Calculated Property |
| Inp | [681.00; 729.00] |
|
|
| Inp | 716.00 | NIST | |
| Inp | 723.00 | NIST | |
| Inp | 708.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 698.00 | NIST | |
| Inp | 729.00 | NIST | |
| Inp | 704.00 | NIST | |
| Inp | 725.20 | NIST | |
| I | [1174.97; 1192.67] |
|
|
| I | 1186.26 | NIST | |
| I | 1192.67 | NIST | |
| I | 1174.97 | NIST | |
| I | 1186.26 | NIST | |
| Tboil | 348.75 | K | Joback Calculated Property |
| Tc | 545.22 | K | Joback Calculated Property |
| Tfus | [198.80; 256.50] | K |
|
| Tfus | 255.92 | K | Aq. Sol... |
| Tfus | 256.40 | K | NIST |
| Tfus | 256.50 ± 0.20 | K | NIST |
| Tfus | 198.80 ± 0.40 | K | NIST |
| Vc | 0.259 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [86.29; 108.82] | J/mol×K | [348.75; 545.22] |
|
| Cp,gas | 86.29 | J/mol×K | 348.75 | Joback Calculated Property |
| Cp,gas | 90.61 | J/mol×K | 381.50 | Joback Calculated Property |
| Cp,gas | 94.69 | J/mol×K | 414.24 | Joback Calculated Property |
| Cp,gas | 98.54 | J/mol×K | 446.99 | Joback Calculated Property |
| Cp,gas | 102.17 | J/mol×K | 479.73 | Joback Calculated Property |
| Cp,gas | 105.59 | J/mol×K | 512.48 | Joback Calculated Property |
| Cp,gas | 108.82 | J/mol×K | 545.22 | Joback Calculated Property |
| Cp,liquid | [130.10; 140.91] | J/mol×K | [285.15; 355.15] |
|
| Cp,liquid | 136.31 | J/mol×K | 285.15 | Heat Ca... |
| Cp,liquid | 136.37 | J/mol×K | 286.65 | Heat Ca... |
| Cp,liquid | 136.43 | J/mol×K | 288.15 | Heat Ca... |
| Cp,liquid | 136.50 | J/mol×K | 289.65 | Heat Ca... |
| Cp,liquid | 136.56 | J/mol×K | 291.15 | Heat Ca... |
| Cp,liquid | 136.63 | J/mol×K | 292.65 | Heat Ca... |
| Cp,liquid | 136.70 | J/mol×K | 294.15 | Heat Ca... |
| Cp,liquid | 136.77 | J/mol×K | 295.65 | Heat Ca... |
| Cp,liquid | 136.84 | J/mol×K | 297.15 | Heat Ca... |
| Cp,liquid | 136.89 | J/mol×K | 298.15 | Heat Ca... |
| Cp,liquid | 136.92 | J/mol×K | 298.65 | Heat Ca... |
| Cp,liquid | 130.10 | J/mol×K | 300.00 | NIST |
| Cp,liquid | 136.99 | J/mol×K | 300.15 | Heat Ca... |
| Cp,liquid | 137.07 | J/mol×K | 301.65 | Heat Ca... |
| Cp,liquid | 137.15 | J/mol×K | 303.15 | Heat Ca... |
| Cp,liquid | 137.23 | J/mol×K | 304.65 | Heat Ca... |
| Cp,liquid | 137.31 | J/mol×K | 306.15 | Heat Ca... |
| Cp,liquid | 137.39 | J/mol×K | 307.65 | Heat Ca... |
| Cp,liquid | 137.48 | J/mol×K | 309.15 | Heat Ca... |
| Cp,liquid | 137.57 | J/mol×K | 310.65 | Heat Ca... |
| Cp,liquid | 137.66 | J/mol×K | 312.15 | Heat Ca... |
| Cp,liquid | 137.75 | J/mol×K | 313.65 | Heat Ca... |
| Cp,liquid | 137.84 | J/mol×K | 315.15 | Heat Ca... |
| Cp,liquid | 137.93 | J/mol×K | 316.65 | Heat Ca... |
| Cp,liquid | 138.03 | J/mol×K | 318.15 | Heat Ca... |
| Cp,liquid | 138.13 | J/mol×K | 319.65 | Heat Ca... |
| Cp,liquid | 138.22 | J/mol×K | 321.15 | Heat Ca... |
| Cp,liquid | 138.33 | J/mol×K | 322.65 | Heat Ca... |
| Cp,liquid | 138.43 | J/mol×K | 324.15 | Heat Ca... |
| Cp,liquid | 138.53 | J/mol×K | 325.65 | Heat Ca... |
| Cp,liquid | 138.64 | J/mol×K | 327.15 | Heat Ca... |
| Cp,liquid | 138.74 | J/mol×K | 328.65 | Heat Ca... |
| Cp,liquid | 138.85 | J/mol×K | 330.15 | Heat Ca... |
| Cp,liquid | 138.96 | J/mol×K | 331.65 | Heat Ca... |
| Cp,liquid | 139.07 | J/mol×K | 333.15 | Heat Ca... |
| Cp,liquid | 139.19 | J/mol×K | 334.65 | Heat Ca... |
| Cp,liquid | 139.30 | J/mol×K | 336.15 | Heat Ca... |
| Cp,liquid | 139.42 | J/mol×K | 337.65 | Heat Ca... |
| Cp,liquid | 139.54 | J/mol×K | 339.15 | Heat Ca... |
| Cp,liquid | 139.66 | J/mol×K | 340.65 | Heat Ca... |
| Cp,liquid | 139.78 | J/mol×K | 342.15 | Heat Ca... |
| Cp,liquid | 139.90 | J/mol×K | 343.65 | Heat Ca... |
| Cp,liquid | 140.03 | J/mol×K | 345.15 | Heat Ca... |
| Cp,liquid | 140.16 | J/mol×K | 346.65 | Heat Ca... |
| Cp,liquid | 140.29 | J/mol×K | 348.15 | Heat Ca... |
| Cp,liquid | 140.42 | J/mol×K | 349.65 | Heat Ca... |
| Cp,liquid | 140.55 | J/mol×K | 351.15 | Heat Ca... |
| Cp,liquid | 140.68 | J/mol×K | 352.65 | Heat Ca... |
| Cp,liquid | 140.82 | J/mol×K | 354.15 | Heat Ca... |
| Cp,liquid | 140.91 | J/mol×K | 355.15 | Heat Ca... |
| η | [0.0004315; 0.0031520] | Pa×s | [202.02; 348.75] |
|
| η | 0.0031520 | Pa×s | 202.02 | Joback Calculated Property |
| η | 0.0018920 | Pa×s | 226.48 | Joback Calculated Property |
| η | 0.0012545 | Pa×s | 250.93 | Joback Calculated Property |
| η | 0.0008948 | Pa×s | 275.38 | Joback Calculated Property |
| η | 0.0006744 | Pa×s | 299.84 | Joback Calculated Property |
| η | 0.0005304 | Pa×s | 324.30 | Joback Calculated Property |
| η | 0.0004315 | Pa×s | 348.75 | Joback Calculated Property |
| ΔfusH | [3.10; 9.62] | kJ/mol | [182.00; 256.40] |
|
| ΔfusH | 3.10 | kJ/mol | 182.00 | NIST |
| ΔfusH | 9.62 | kJ/mol | 256.40 | NIST |
| ΔfusH | 9.62 | kJ/mol | 256.40 | NIST |
| ΔvapH | [36.40; 39.50] | kJ/mol | [308.00; 379.80] |
|
| ΔvapH | 37.60 ± 0.10 | kJ/mol | 308.00 | NIST |
| ΔvapH | 39.50 | kJ/mol | 311.50 | NIST |
| ΔvapH | 37.30 ± 0.10 | kJ/mol | 315.00 | NIST |
| ΔvapH | 36.90 ± 0.10 | kJ/mol | 323.00 | NIST |
| ΔvapH | 36.60 ± 0.10 | kJ/mol | 330.00 | NIST |
| ΔvapH | 36.40 ± 0.10 | kJ/mol | 338.00 | NIST |
| ΔvapH | 38.06 | kJ/mol | 379.80 | NIST |
| Pvap | 8.91 | kPa | 313.15 | Isother... |
| ρl | 1727.01 | kg/m3 | 298.15 | (Vapor ... |
| ΔfusS | [17.15; 37.53] | J/mol×K | [182.00; 256.40] |
|
| ΔfusS | 17.15 | J/mol×K | 182.00 | NIST |
| ΔfusS | 37.53 | J/mol×K | 256.40 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.00; 202.65] | kPa | [272.75; 407.21] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.31363e+01 | |||
| Coefficient B | -2.60209e+03 | |||
| Coefficient C | -7.46670e+01 | |||
| Temperature range, min. | 272.75 | |||
| Temperature range, max. | 407.21 | |||
| Pvap | 1.00 | kPa | 272.75 | Calculated Property |
| Pvap | 2.51 | kPa | 287.69 | Calculated Property |
| Pvap | 5.59 | kPa | 302.63 | Calculated Property |
| Pvap | 11.29 | kPa | 317.57 | Calculated Property |
| Pvap | 21.00 | kPa | 332.51 | Calculated Property |
| Pvap | 36.50 | kPa | 347.45 | Calculated Property |
| Pvap | 59.89 | kPa | 362.39 | Calculated Property |
| Pvap | 93.59 | kPa | 377.33 | Calculated Property |
| Pvap | 140.24 | kPa | 392.27 | Calculated Property |
| Pvap | 202.65 | kPa | 407.21 | Calculated Property |
Similar Compounds
Find more compounds similar to Ethane, 1-bromo-2-chloro-.
Mixtures
Sources
- Crippen Method
- Temperature and Pressure Dependence of the Volumetric Properties of Binary Liquid Mixtures Containing Dihaloalkanes
- (Vapor + liquid) equilibria for the binary mixtures (1-propanol + dibromomethane, or + bromochloromethane, or + 1,2-dichloroethane or +1-bromo-2-chloroethane) at T = 313.15 K.
- Isothermal Vapor-Liquid Equilibria of ethyl acetate + dibromomethane, or + bromochloromethane or + 1,2-dichloroethane or +1-bromo-2-chloroethane at T = 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
- Aqueous Solubility Prediction Method
- Estimated Solubility 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.