- InChI
- InChI=1S/CH2BrCl/c2-1-3/h1H2
- InChI Key
- JPOXNPPZZKNXOV-UHFFFAOYSA-N
- Formula
- CH2BrCl
- SMILES
- ClCBr
- Molecular Weight1
- 129.38
- CAS
- 74-97-5
- Other Names
-
- Bromochloromethane
- CBM
- CH2ClBr
- Chlorobromomethane
- Fluorocarbon 1011
- HALON 1011
- MIL-B-4394-B
- Methylene bromide chloride
- Methylene chlorobromide
- Monochloromonobromomethane
- NSC 7294
- REFRIGERANT-30B1
- UN 1887
- Cp,gas : Ideal gas 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).
- 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.
- csound,fluid : Speed of sound in fluid (m/s).
- 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° | -40.07 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -20.00 ± 7.00 | kJ/mol | NIST |
| ΔfusH° | 7.83 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 28.64 | kJ/mol | Joback Calculated Property |
| IE | [10.75; 10.77] | eV |
|
| IE | 10.77 ± 0.01 | eV | NIST |
| IE | 10.77 | eV | NIST |
| IE | 10.77 ± 0.01 | eV | NIST |
| IE | 10.75 ± 0.05 | eV | NIST |
| log10WS | [-0.89; -0.89] |
|
|
| log10WS | -0.89 | Aq. Sol... | |
| log10WS | -0.89 | Estimat... | |
| logPoct/wat | 1.578 | Crippen Calculated Property | |
| McVol | 54.690 | ml/mol | McGowan Calculated Property |
| Pc | 6084.49 | kPa | Joback Calculated Property |
| Inp | [569.00; 617.00] |
|
|
| Inp | 607.00 | NIST | |
| Inp | 611.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 569.00 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 578.00 | NIST | |
| Inp | 582.00 | NIST | |
| Inp | 617.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | 607.00 | NIST | |
| Inp | 578.00 | NIST | |
| Inp | 598.00 | NIST | |
| I | [1054.00; 1066.29] |
|
|
| I | 1064.58 | NIST | |
| I | 1066.29 | NIST | |
| I | 1057.80 | NIST | |
| I | 1054.00 | NIST | |
| I | 1060.00 | NIST | |
| I | 1054.00 | NIST | |
| Tboil | [341.00; 342.00] | K |
|
| Tboil | 341.00 | K | NIST |
| Tboil | 342.00 | K | NIST |
| Tc | 522.75 | K | Joback Calculated Property |
| Tfus | [185.18; 185.20] | K |
|
| Tfus | 185.18 | K | Aq. Sol... |
| Tfus | 185.20 ± 0.05 | K | NIST |
| Vc | 0.203 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [58.44; 71.04] | J/mol×K | [325.87; 522.75] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 58 60 62 64 66 68 70 72 350 400 450 500 | ||||
| Cp,gas | 58.44 | J/mol×K | 325.87 | Joback Calculated Property |
| Cp,gas | 60.91 | J/mol×K | 358.68 | Joback Calculated Property |
| Cp,gas | 63.23 | J/mol×K | 391.50 | Joback Calculated Property |
| Cp,gas | 65.39 | J/mol×K | 424.31 | Joback Calculated Property |
| Cp,gas | 67.40 | J/mol×K | 457.12 | Joback Calculated Property |
| Cp,gas | 69.28 | J/mol×K | 489.93 | Joback Calculated Property |
| Cp,gas | 71.04 | J/mol×K | 522.75 | Joback Calculated Property |
| η | [0.0004312; 0.0028003] | Pa×s | [190.75; 325.87] |
|
|
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 | ||||
| η | 0.0028003 | Pa×s | 190.75 | Joback Calculated Property |
| η | 0.0017389 | Pa×s | 213.27 | Joback Calculated Property |
| η | 0.0011827 | Pa×s | 235.79 | Joback Calculated Property |
| η | 0.0008603 | Pa×s | 258.31 | Joback Calculated Property |
| η | 0.0006586 | Pa×s | 280.83 | Joback Calculated Property |
| η | 0.0005246 | Pa×s | 303.35 | Joback Calculated Property |
| η | 0.0004312 | Pa×s | 325.87 | Joback Calculated Property |
| ΔvapH | [33.50; 42.00] | kJ/mol | [283.50; 315.00] |
|
| ΔvapH | 42.00 | kJ/mol | 283.50 | NIST |
| ΔvapH | 33.50 | kJ/mol | 315.00 | NIST |
| Pvap | 37.28 | kPa | 313.15 | Isother... |
| ρl | [1921.71; 1924.55] | kg/m3 | [298.15; 298.15] |
|
| ρl | 1921.71 | kg/m3 | 298.15 | Vapour ... |
| ρl | 1924.55 | kg/m3 | 298.15 | (Vapor ... |
| csound,fluid | [940.80; 1001.20] | m/s | [293.15; 313.15] |
|
|
T(K) Speed of sound in fluid (m/s) 940 950 960 970 980 990 1000 295 300 305 310 | ||||
| csound,fluid | 1001.20 | m/s | 293.15 | Excess ... |
| csound,fluid | 986.10 | m/s | 298.15 | Excess ... |
| csound,fluid | 971.00 | m/s | 303.15 | Excess ... |
| csound,fluid | 955.90 | m/s | 308.15 | Excess ... |
| csound,fluid | 940.80 | m/s | 313.15 | Excess ... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [249.72; 363.59] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.48065e+01 | |||
| Coefficient B | -3.12475e+03 | |||
| Coefficient C | -3.44960e+01 | |||
| Temperature range, min. | 249.72 | |||
| Temperature range, max. | 363.59 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 350 | ||||
| Pvap | 1.33 | kPa | 249.72 | Calculated Property |
| Pvap | 2.99 | kPa | 262.37 | Calculated Property |
| Pvap | 6.14 | kPa | 275.02 | Calculated Property |
| Pvap | 11.76 | kPa | 287.68 | Calculated Property |
| Pvap | 21.16 | kPa | 300.33 | Calculated Property |
| Pvap | 36.09 | kPa | 312.98 | Calculated Property |
| Pvap | 58.77 | kPa | 325.63 | Calculated Property |
| Pvap | 91.89 | kPa | 338.29 | Calculated Property |
| Pvap | 138.64 | kPa | 350.94 | Calculated Property |
| Pvap | 202.65 | kPa | 363.59 | Calculated Property |
| Pvap | [2.57e-03; 6774.22] | kPa | [185.20; 557.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.51479e+01 | |||
| Coefficient B | -5.95434e+03 | |||
| Coefficient C | -7.49956e+00 | |||
| Coefficient D | 5.73549e-06 | |||
| Temperature range, min. | 185.20 | |||
| Temperature range, max. | 557.00 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 7000 200 300 400 500 | ||||
| Pvap | 2.57e-03 | kPa | 185.20 | Calculated Property |
| Pvap | 0.22 | kPa | 226.51 | Calculated Property |
| Pvap | 4.06 | kPa | 267.82 | Calculated Property |
| Pvap | 31.00 | kPa | 309.13 | Calculated Property |
| Pvap | 137.01 | kPa | 350.44 | Calculated Property |
| Pvap | 424.91 | kPa | 391.76 | Calculated Property |
| Pvap | 1038.30 | kPa | 433.07 | Calculated Property |
| Pvap | 2152.52 | kPa | 474.38 | Calculated Property |
| Pvap | 3977.00 | kPa | 515.69 | Calculated Property |
| Pvap | 6774.22 | kPa | 557.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Methane, bromochloro-.
Mixtures
- Methane, bromochloro- + Ethyl Acetate
- Methane, bromotrichloro- + Methane, bromochloro-
- Methane, dibromo- + Methane, bromochloro-
- 1-Propanol + Methane, bromochloro-
- Methane, bromochloro- + Water
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Temperature and Pressure Dependence of the Volumetric Properties of Binary Liquid Mixtures Containing Dihaloalkanes
- Vapour liquid equilibrium at T = 308.15 K for binary systems: Dibromomethane + n-heptane, bromotrichloromethane + n-heptane, bromotrichloromethane + dibromomethane, bromotrichloromethane + bromochloromethane and dibromomethane + bromochloromethane. Experimental data and modelling
- (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
- Excess Molar Volumes and Speed of Sound in Bromotrichloromethane + n-Heptane, Dibromomethane + n-Heptane, Bromotrichloromethane + Dibromomethane, and Bromotrichloromethane + Bromochloromethane at Temperatures from (293.15 to 313.15) K
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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