- 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.
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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] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 85 90 95 100 105 110 350 400 450 500 | ||||
| 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] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 130 132 134 136 138 140 300 320 340 | ||||
| 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] |
|
|
T(K) Dynamic viscosity (Pa×s) 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 200 250 300 350 | ||||
| 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] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 36.5 37 37.5 38 38.5 39 39.5 320 340 360 380 | ||||
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
| 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
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