- InChI
- InChI=1S/C2H4Br2/c3-1-2-4/h1-2H2
- InChI Key
- PAAZPARNPHGIKF-UHFFFAOYSA-N
- Formula
- C2H4Br2
- SMILES
- BrCCBr
- Molecular Weight1
- 187.86
- CAS
- 106-93-4
- Other Names
-
- 1,2-DIBROMOETHANE
- 1,2-Dibromaethan
- 1,2-Dibromoetano
- 1,2-Dibroomethaan
- 1,2-Ethylene dibromide
- 1,2-dibromoethane (EDB)
- ALPHA,BETA-DIBROMOETHANE
- Aadibroom
- Aethylenbromid
- Bromofume
- Bromuro di etile
- CH2BrCH2Br
- Celmide
- DBE
- Dibromoethane
- Dibromure D'ethylene
- Dowfume 40
- Dowfume W-100
- Dowfume W-8
- Dowfume W-90
- Dowfume W85
- Dowfume edb
- Dwubromoetan
- E-D-Bee
- EDB
- EDB-85
- ENT 15,349
- ETHYLENE DIBROMIDE
- Edabrom
- Ethylene bromide
- Fumo-gas
- Glycol Dibromide
- Iscobrome D
- Kopfume
- NCI-C00522
- Nefis
- Nephis
- Pestmaster edb-85
- Rcra waste number U067
- Sanhyuum
- Soilbrom
- Soilbrom-100
- Soilbrom-40
- Soilbrom-85
- Soilbrom-90
- Soilbrom-90ec
- Soilbrome-85
- Soilfume
- UN 1605
- Unifume
- alpha,omega-dibromoethane
- sym-Dibromoethane
- «alpha»,«beta»-Dibromoethane
- «alpha»,«omega»-Dibromoethane
- «alpha»,«beta»-Dibromoethane
- «alpha»,«omega»-Dibromoethane
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- 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).
- ΔsubH : Enthalpy of sublimation 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).
- n0 : Refractive Index.
- 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).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (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 | 0.7950 | KDB | |
| ΔcH°liquid | [-1240.30; -1215.70] | kJ/mol |
|
| ΔcH°liquid | -1240.30 ± 1.60 | kJ/mol | NIST |
| ΔcH°liquid | -1215.70 | kJ/mol | NIST |
| μ | 1.00 | debye | KDB |
| η | 0.0017330 | Pa×s | Studies... |
| ΔfG° | -10.60 | kJ/mol | KDB |
| ΔfH°gas | -38.94 | kJ/mol | KDB |
| ΔfusH° | 11.51 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [23.70; 42.40] | kJ/mol |
|
| ΔvapH° | 41.74 | kJ/mol | NIST |
| ΔvapH° | 41.70 ± 0.80 | kJ/mol | NIST |
| ΔvapH° | 42.40 | kJ/mol | NIST |
| ΔvapH° | 41.70 ± 0.80 | kJ/mol | NIST |
| ΔvapH° | 41.80 | kJ/mol | NIST |
| ΔvapH° | 41.73 ± 0.02 | kJ/mol | NIST |
| ΔvapH° | Outlier 23.70 ± 0.20 | kJ/mol | NIST |
| IE | [10.20; 10.58] | eV |
|
| IE | 10.35 ± 0.04 | eV | NIST |
| IE | 10.37 | eV | NIST |
| IE | 10.42 | eV | NIST |
| IE | 10.20 | eV | NIST |
| IE | 10.38 | eV | NIST |
| IE | 10.37 | eV | NIST |
| IE | 10.58 ± 0.10 | eV | NIST |
| IE | 10.44 ± 0.10 | eV | NIST |
| IE | 10.57 ± 0.02 | eV | NIST |
| log10WS | -1.68 | Estimat... | |
| logPoct/wat | 1.776 | Crippen Calculated Property | |
| McVol | 74.040 | ml/mol | McGowan Calculated Property |
| Pc | 7200.00 | kPa | KDB |
| Inp | [770.90; 827.00] |
|
|
| Inp | 795.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 791.00 | NIST | |
| Inp | 783.90 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | 770.90 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 811.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 774.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 823.00 | NIST | |
| Inp | 814.90 | NIST | |
| I | [1226.00; 1299.71] |
|
|
| I | 1247.00 | NIST | |
| I | 1265.00 | NIST | |
| I | 1286.00 | NIST | |
| I | 1299.71 | NIST | |
| I | 1267.79 | NIST | |
| I | 1226.00 | NIST | |
| I | 1265.00 | NIST | |
| I | 1247.00 | NIST | |
| S°liquid | 223.30 | J/mol×K | NIST |
| Tboil | [323.70; 464.39] | K |
|
| Tboil | 404.70 | K | KDB |
| Tboil | 404.65 | K | Excess ... |
| Tboil | 404.50 | K | NIST |
| Tboil | 404.80 | K | NIST |
| Tboil | 402.65 ± 0.60 | K | NIST |
| Tboil | 404.00 ± 2.00 | K | NIST |
| Tboil | 402.00 ± 3.00 | K | NIST |
| Tboil | 405.00 ± 3.00 | K | NIST |
| Tboil | 398.00 ± 20.00 | K | NIST |
| Tboil | 404.90 ± 0.80 | K | NIST |
| Tboil | 404.90 ± 1.00 | K | NIST |
| Tboil | 402.65 ± 1.50 | K | NIST |
| Tboil | 404.30 ± 0.60 | K | NIST |
| Tboil | 404.56 ± 0.07 | K | NIST |
| Tboil | 403.70 ± 1.50 | K | NIST |
| Tboil | 404.80 ± 0.50 | K | NIST |
| Tboil | 385.70 ± 20.00 | K | NIST |
| Tboil | 404.80 ± 0.30 | K | NIST |
| Tboil | 404.90 ± 1.00 | K | NIST |
| Tboil | 404.90 ± 1.00 | K | NIST |
| Tboil | 404.80 ± 0.40 | K | NIST |
| Tboil | 404.80 ± 0.50 | K | NIST |
| Tboil | Outlier 464.39 ± 0.20 | K | NIST |
| Tboil | 404.80 ± 0.50 | K | NIST |
| Tboil | 404.80 ± 0.40 | K | NIST |
| Tboil | 404.80 ± 0.50 | K | NIST |
| Tboil | 404.60 ± 0.50 | K | NIST |
| Tboil | 404.85 ± 0.30 | K | NIST |
| Tboil | 404.85 ± 0.30 | K | NIST |
| Tboil | 403.00 ± 2.00 | K | NIST |
| Tboil | 404.80 ± 0.30 | K | NIST |
| Tboil | 404.45 ± 0.40 | K | NIST |
| Tboil | 405.80 ± 0.80 | K | NIST |
| Tboil | 404.30 ± 0.50 | K | NIST |
| Tboil | Outlier 323.70 ± 1.00 | K | NIST |
| Tboil | 404.20 ± 1.50 | K | NIST |
| Tboil | 402.00 ± 1.50 | K | NIST |
| Tboil | 404.70 ± 1.50 | K | NIST |
| Tboil | 402.15 ± 1.50 | K | NIST |
| Tc | 583.00 | K | KDB |
| Tfus | 283.08 | K | KDB |
| Ttriple | [282.90; 283.00] | K |
|
| Ttriple | 282.90 | K | KDB |
| Ttriple | 283.00 ± 0.20 | K | NIST |
| Vc | 0.272 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [91.33; 113.99] | J/mol×K | [377.48; 587.98] |
|
| Cp,gas | 91.33 | J/mol×K | 377.48 | Joback Calculated Property |
| Cp,gas | 95.83 | J/mol×K | 412.56 | Joback Calculated Property |
| Cp,gas | 100.01 | J/mol×K | 447.65 | Joback Calculated Property |
| Cp,gas | 103.89 | J/mol×K | 482.73 | Joback Calculated Property |
| Cp,gas | 107.50 | J/mol×K | 517.81 | Joback Calculated Property |
| Cp,gas | 110.86 | J/mol×K | 552.89 | Joback Calculated Property |
| Cp,gas | 113.99 | J/mol×K | 587.98 | Joback Calculated Property |
| Cp,liquid | [129.50; 140.91] | J/mol×K | [285.15; 398.00] |
|
| 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 | 134.80 | J/mol×K | 293.00 | NIST |
| Cp,liquid | 136.87 | J/mol×K | 293.15 | Thermop... |
| Cp,liquid | 136.90 | J/mol×K | 294.15 | Thermop... |
| Cp,liquid | 136.70 | J/mol×K | 294.15 | Heat Ca... |
| Cp,liquid | 136.95 | J/mol×K | 295.15 | Thermop... |
| Cp,liquid | 136.77 | J/mol×K | 295.65 | Heat Ca... |
| Cp,liquid | 136.99 | J/mol×K | 296.15 | Thermop... |
| Cp,liquid | 137.02 | J/mol×K | 297.15 | Thermop... |
| Cp,liquid | 136.84 | J/mol×K | 297.15 | Heat Ca... |
| Cp,liquid | 136.89 | J/mol×K | 298.15 | Heat Ca... |
| Cp,liquid | 134.70 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 136.00 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 135.00 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 137.04 | J/mol×K | 298.15 | Thermop... |
| Cp,liquid | 136.92 | J/mol×K | 298.65 | Heat Ca... |
| Cp,liquid | 137.09 | J/mol×K | 299.15 | Thermop... |
| Cp,liquid | 136.40 | J/mol×K | 300.00 | NIST |
| Cp,liquid | 129.50 | J/mol×K | 300.00 | NIST |
| Cp,liquid | 136.99 | J/mol×K | 300.15 | Heat Ca... |
| Cp,liquid | 137.11 | J/mol×K | 300.15 | Thermop... |
| Cp,liquid | 137.15 | J/mol×K | 301.15 | Thermop... |
| Cp,liquid | 137.07 | J/mol×K | 301.65 | Heat Ca... |
| Cp,liquid | 137.20 | J/mol×K | 302.15 | Thermop... |
| Cp,liquid | 137.15 | J/mol×K | 303.15 | Heat Ca... |
| Cp,liquid | 137.25 | J/mol×K | 303.15 | Thermop... |
| Cp,liquid | 137.29 | J/mol×K | 304.15 | Thermop... |
| Cp,liquid | 137.23 | J/mol×K | 304.65 | Heat Ca... |
| Cp,liquid | 137.32 | J/mol×K | 305.15 | Thermop... |
| Cp,liquid | 137.31 | J/mol×K | 306.15 | Heat Ca... |
| Cp,liquid | 137.39 | J/mol×K | 306.15 | Thermop... |
| Cp,liquid | 137.42 | J/mol×K | 307.15 | Thermop... |
| Cp,liquid | 137.39 | J/mol×K | 307.65 | Heat Ca... |
| Cp,liquid | 137.49 | J/mol×K | 308.15 | Thermop... |
| Cp,liquid | 137.48 | J/mol×K | 309.15 | Heat Ca... |
| Cp,liquid | 137.53 | J/mol×K | 309.15 | Thermop... |
| Cp,liquid | 135.14 | J/mol×K | 310.00 | NIST |
| Cp,liquid | 137.60 | J/mol×K | 310.15 | Thermop... |
| Cp,liquid | 137.57 | J/mol×K | 310.65 | Heat Ca... |
| Cp,liquid | 137.65 | J/mol×K | 311.15 | Thermop... |
| Cp,liquid | 137.66 | J/mol×K | 312.15 | Heat Ca... |
| Cp,liquid | 137.71 | J/mol×K | 312.15 | Thermop... |
| Cp,liquid | 137.77 | J/mol×K | 313.15 | Thermop... |
| 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... |
| Cp,liquid | 134.70 | J/mol×K | 398.00 | NIST |
| η | [0.0004954; 0.0029279] | Pa×s | [231.90; 377.48] |
|
| η | 0.0029279 | Pa×s | 231.90 | Joback Calculated Property |
| η | 0.0018926 | Pa×s | 256.16 | Joback Calculated Property |
| η | 0.0013193 | Pa×s | 280.43 | Joback Calculated Property |
| η | 0.0009741 | Pa×s | 304.69 | Joback Calculated Property |
| η | 0.0007521 | Pa×s | 328.95 | Joback Calculated Property |
| η | 0.0006017 | Pa×s | 353.22 | Joback Calculated Property |
| η | 0.0004954 | Pa×s | 377.48 | Joback Calculated Property |
| ΔfusH | [1.94; 10.94] | kJ/mol | [249.50; 283.00] |
|
| ΔfusH | 1.94 | kJ/mol | 249.50 | NIST |
| ΔfusH | 10.94 | kJ/mol | 283.00 | NIST |
| ΔsubH | [49.80; 54.80] | kJ/mol | [238.50; 266.00] |
|
| ΔsubH | 54.80 | kJ/mol | 238.50 | NIST |
| ΔsubH | 49.80 | kJ/mol | 266.00 | NIST |
| ΔvapH | [31.10; 49.60] | kJ/mol | [291.50; 491.00] |
|
| ΔvapH | 49.60 | kJ/mol | 291.50 | NIST |
| ΔvapH | 41.80 | kJ/mol | 300.00 | NIST |
| ΔvapH | 41.70 ± 0.10 | kJ/mol | 308.00 | NIST |
| ΔvapH | 41.70 ± 0.10 | kJ/mol | 315.00 | NIST |
| ΔvapH | 41.60 ± 0.10 | kJ/mol | 323.00 | NIST |
| ΔvapH | 31.10 | kJ/mol | 325.00 | NIST |
| ΔvapH | 41.50 ± 0.10 | kJ/mol | 330.00 | NIST |
| ΔvapH | 41.40 ± 0.10 | kJ/mol | 338.00 | NIST |
| ΔvapH | 39.60 | kJ/mol | 364.50 | NIST |
| ΔvapH | 40.00 | kJ/mol | 402.00 | NIST |
| ΔvapH | 36.36 | kJ/mol | 404.60 | KDB |
| ΔvapH | 41.78 | kJ/mol | 404.70 | NIST |
| ΔvapH | 34.77 | kJ/mol | 404.80 | NIST |
| ΔvapH | 37.40 | kJ/mol | 491.00 | NIST |
| n0 | 1.53570 | 298.15 | Thermod... | |
| ρl | [2179.24; 2180.01] | kg/m3 | [293.00; 293.20] |
|
| ρl | 2180.01 | kg/m3 | 293.00 | KDB |
| ρl | 2179.60 | kg/m3 | 293.15 | Thermop... |
| ρl | 2179.24 | kg/m3 | 293.20 | Isobari... |
| ρl | 2179.24 | kg/m3 | 293.20 | Isobari... |
| ΔfusS | [7.78; 38.66] | J/mol×K | [249.50; 283.00] |
|
| ΔfusS | 7.78 | J/mol×K | 249.50 | NIST |
| ΔfusS | 38.66 | J/mol×K | 283.00 | NIST |
| csound,fluid | [994.27; 1007.04] | m/s | [293.15; 298.15] |
|
| csound,fluid | 1007.04 | m/s | 293.15 | Densiti... |
| csound,fluid | 994.27 | m/s | 298.15 | Densiti... |
| γ | [0.04; 0.04] | N/m | [293.15; 313.15] |
|
| γ | 0.04 | N/m | 293.15 | The add... |
| γ | 0.04 | N/m | 293.20 | KDB |
| 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... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.76; 5624.74] | kPa | [282.94; 650.15] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.46602e+01 | |||
| Coefficient B | -3.70799e+03 | |||
| Coefficient C | -3.47480e+01 | |||
| Temperature range, min. | 282.94 | |||
| Temperature range, max. | 650.15 | |||
| Pvap | 0.76 | kPa | 282.94 | Calculated Property |
| Pvap | 6.23 | kPa | 323.74 | Calculated Property |
| Pvap | 30.47 | kPa | 364.54 | Calculated Property |
| Pvap | 105.08 | kPa | 405.34 | Calculated Property |
| Pvap | 283.46 | kPa | 446.14 | Calculated Property |
| Pvap | 639.26 | kPa | 486.95 | Calculated Property |
| Pvap | 1260.10 | kPa | 527.75 | Calculated Property |
| Pvap | 2239.12 | kPa | 568.55 | Calculated Property |
| Pvap | 3666.84 | kPa | 609.35 | Calculated Property |
| Pvap | 5624.74 | kPa | 650.15 | Calculated Property |
| Pvap | [0.75; 5365.44] | kPa | [282.94; 650.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 3.51685e+01 | |||
| Coefficient B | -5.52047e+03 | |||
| Coefficient C | -2.83216e+00 | |||
| Coefficient D | 6.02747e-07 | |||
| Temperature range, min. | 282.94 | |||
| Temperature range, max. | 650.15 | |||
| Pvap | 0.75 | kPa | 282.94 | Calculated Property |
| Pvap | 6.11 | kPa | 323.74 | Calculated Property |
| Pvap | 29.94 | kPa | 364.54 | Calculated Property |
| Pvap | 103.74 | kPa | 405.34 | Calculated Property |
| Pvap | 280.55 | kPa | 446.14 | Calculated Property |
| Pvap | 631.85 | kPa | 486.95 | Calculated Property |
| Pvap | 1239.17 | kPa | 527.75 | Calculated Property |
| Pvap | 2184.04 | kPa | 568.55 | Calculated Property |
| Pvap | 3539.60 | kPa | 609.35 | Calculated Property |
| Pvap | 5365.44 | kPa | 650.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Ethane, 1,2-dibromo-.
Mixtures
- Ethane, 1,2-dibromo- + 1-Hexanol
- Ethane, 1,2-dibromo- + Ethane, 1,2-dichloro-
- Trichloromethane + Ethane, 1,2-dibromo-
- Ethane, 1,2-dibromo- + Ethane, 1,1,2,2-tetrachloro-
- Ethane, 1,1,1-trichloro- + Ethane, 1,2-dibromo-
- Trichloroethylene + Ethane, 1,2-dibromo-
- Tetrachloroethylene + Ethane, 1,2-dibromo-
- Ethyl formate + Ethane, 1,2-dibromo-
- Ethane, 1,2-dibromo- + Ethyl Acetate
- Propanoic acid, ethyl ester + Ethane, 1,2-dibromo-
- Ethane, 1,2-dibromo- + Butanoic acid, ethyl ester
- Pentanoic acid, ethyl ester + Ethane, 1,2-dibromo-
- Ethane, 1,2-dibromo- + Methyl formate
- Ethane, 1,2-dibromo- + Acetic acid, methyl ester
- Ethane, 1,2-dibromo- + Methyl propionate
- Butanoic acid, methyl ester + Ethane, 1,2-dibromo-
- Ethane, 1,2-dibromo- + Methyl valerate
- Ethane, 1,2-dibromo- + 1-Decanol
- Benzene + Ethane, 1,2-dibromo-
- Toluene + Ethane, 1,2-dibromo-
Find more mixtures with Ethane, 1,2-dibromo-.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Densities, Excess Molar Volumes, Ultrasonic Speeds, and Isentropic Compressibilities of Hexan-1-ol with 1,2-Dichloroethane, 1,2-Dibromoethane, and 1,1,2,2-Tetrachloroethene at (293.15 and 298.15) K
- Isobaric vapour liquid equilibria for binary mixtures of 1,2-dibromoethane with 1,2-dichloroethane, trichloromethane, and 1,1,2,2-tetrachloroethane at atmospheric pressure
- Excess volumes and speeds of sound of mixtures of 1,2-dibromoethane with chlorinated ethanes and ethenes at 303.15 K
- 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
- Studies on thermodynamic properties of binary mixtures of hexan-1-ol with halogenated compounds at T = (308.15 and 313.15) K
- 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
- Thermophysical and sonochemical behaviour of binary mixtures of decan-1-ol with halohydrocarbons at (T = 293.15 and 313.15) K
- The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
- Isobaric Vapor-Liquid Equilibria for Binary Mixtures of 1,2-Dibromoethane with Benzene, Toluene, Fluorobenzene, and Bromobenzene at Atmospheric Pressure
- Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + 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
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Studies on Transport and Thermodynamic Properties of Binary Mixtures of Hexan-1-ol with Halogenated Compounds at 293.15 K
- Joback Method
- KDB
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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