- InChI
- InChI=1S/Br2/c1-2
- InChI Key
- GDTBXPJZTBHREO-UHFFFAOYSA-N
- Formula
- Br2
- SMILES
- BrBr
- Molecular Weight1
- 159.81
- CAS
- 7726-95-6
- Other Names
-
- Br2
- Brom
- Brome
- Bromo
- Broom
- Dibromine
- UN 1744
- ω : Acentric Factor.
- 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).
- EA : Electron affinity (eV).
- 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 a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- S°gas,1 bar : Molar entropy at standard conditions (1 bar) (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.1290; 0.1320] |
|
|
| ω | 0.1320 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.1290 | ChemSep v8.3 pure component data Compiled value | |
| μ | 0.00 | debye | ChemSep v8.3 pure component data Compiled value |
| EA | [1.47; 2.87] | eV |
|
| EA | 2.42 | eV | NIST |
| EA | 2.60 ± 0.20 | eV | NIST |
| EA | 2.62 ± 0.20 | eV | NIST |
| EA | 2.55 ± 0.10 | eV | NIST |
| EA | 2.51 ± 0.10 | eV | NIST |
| EA | 2.87 ± 0.14 | eV | NIST |
| EA | Outlier 1.47 ± 0.05 | eV | NIST |
| ΔfG° | 3.14 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | [30.88; 30.91] | kJ/mol |
|
| ΔfH°gas | 30.88 ± 0.12 | kJ/mol | Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value |
| ΔfH°gas | 30.91 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | 30.91 ± 0.11 | kJ/mol | NIST |
| ΔfusH° | 6.33 | kJ/mol | Joback Calculated Property |
| IE | [10.50; 10.92] | eV |
|
| IE | 10.52 ± 0.00 | eV | NIST |
| IE | 10.52 ± 0.00 | eV | NIST |
| IE | 10.52 ± 0.01 | eV | NIST |
| IE | 10.51 ± 0.02 | eV | NIST |
| IE | 10.50 ± 0.30 | eV | NIST |
| IE | 10.52 ± 0.01 | eV | NIST |
| IE | 10.55 | eV | NIST |
| IE | 10.52 | eV | NIST |
| IE | 10.80 ± 0.20 | eV | NIST |
| IE | 10.51 ± 0.01 | eV | NIST |
| IE | 10.70 ± 0.10 | eV | NIST |
| IE | 10.51 | eV | NIST |
| IE | 10.52 ± 0.01 | eV | NIST |
| IE | 10.56 ± 0.01 | eV | NIST |
| IE | 10.51 | eV | NIST |
| IE | 10.57 | eV | NIST |
| IE | Outlier 10.92 | eV | NIST |
| logPoct/wat | 1.691 | Crippen Calculated Property | |
| McVol | 45.860 | ml/mol | McGowan Calculated Property |
| Pc | [10300.00; 10335.15] | kPa |
|
| Pc | 10335.15 | kPa | Mathews (1972), critical constants of inorganic substances Compiled value |
| Pc | 10335.15 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 10300.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 5.85 | kPa | ChemSep v8.3 pure component data Compiled value |
| S°gas,1 bar | 245.47 ± 0.01 | J/mol×K | NIST |
| S°liquid | 152.21 ± 0.30 | J/mol×K | NIST |
| Tboil | 331.90 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | [584.00; 584.15] | K |
|
| Tc | 584.00 | K | Mathews (1972), critical constants of inorganic substances Compiled value |
| Tc | 584.00 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 584.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [254.15; 266.00] | K |
|
| Tfus | 265.90 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 266.00 ± 0.30 | K | NIST |
| Tfus | 254.15 ± 10.00 | K | NIST |
| Ttriple | 265.85 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 1.67 | ChemSep v8.3 pure component data Compiled value | |
| URi | 1.90 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.127; 0.135] | m3/kmol |
|
| Vc | 0.127 | m3/kmol | Mathews (1972), critical constants of inorganic substances Compiled value |
| Vc | 0.127 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.135 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | [0.2700000; 0.2860000] |
|
|
| Zc | 0.2700000 | Mathews (1972), critical constants of inorganic substances Compiled value | |
| Zc | 0.2860000 | ChemSep v8.3 pure component data Compiled value | |
| Zra | 0.28 | ChemSep v8.3 pure component data Compiled value |
Cheméo can also estimate Enthalpy of vaporization at standard conditions, Log10 of Water solubility in mol/l for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [17.60; 31.30] | kJ/mol | [206.00; 363.00] |
|
| ΔvapH | 17.60 | kJ/mol | 206.00 | NIST |
| ΔvapH | 31.30 | kJ/mol | 343.00 | NIST |
| ΔvapH | 29.80 | kJ/mol | 363.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [35.00; 37.88] | J/mol×K | [50.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 3.50000e+01 | |||
| Coefficient B | -4.10000e+02 | |||
| Coefficient C | 1.59224e+00 | |||
| Coefficient D | -1.60000e-04 | |||
| Coefficient E | -1.00000e-08 | |||
| Temperature range, min. | 50.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 35.00 | J/mol×K | 50.00 | Calculated Property |
| Cp,gas | 35.68 | J/mol×K | 211.11 | Calculated Property |
| Cp,gas | 36.54 | J/mol×K | 372.22 | Calculated Property |
| Cp,gas | 37.09 | J/mol×K | 533.33 | Calculated Property |
| Cp,gas | 37.43 | J/mol×K | 694.44 | Calculated Property |
| Cp,gas | 37.63 | J/mol×K | 855.56 | Calculated Property |
| Cp,gas | 37.76 | J/mol×K | 1016.67 | Calculated Property |
| Cp,gas | 37.83 | J/mol×K | 1177.78 | Calculated Property |
| Cp,gas | 37.87 | J/mol×K | 1338.89 | Calculated Property |
| Cp,gas | 37.88 | J/mol×K | 1500.00 | Calculated Property |
| Cp,gas | [36.35; 41.63] | J/mol×K | [332.50; 3400.00] |
NIST
|
| Equation | Y = A + B·t + C·t² + D·t³ + E/t², t = T/1000 Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 3.85272e+01 | |||
| Coefficient B | -1.97683e+00 | |||
| Coefficient C | 1.52611e+00 | |||
| Coefficient D | -1.98398e-01 | |||
| Coefficient E | -1.85815e-01 | |||
| Reference | Chase, 1998 | |||
| Comment | F=18.87620, G=291.4863, H=30.91001; Data last reviewed in June, 1982 | |||
| Temperature range, min. | 332.50 | |||
| Temperature range, max. | 3400.00 | |||
| Cp,gas | 36.35 | J/mol×K | 332.50 | Calculated Property |
| Cp,gas | 37.42 | J/mol×K | 673.34 | Calculated Property |
| Cp,gas | 37.70 | J/mol×K | 1014.17 | Calculated Property |
| Cp,gas | 38.06 | J/mol×K | 1355.00 | Calculated Property |
| Cp,gas | 38.53 | J/mol×K | 1695.83 | Calculated Property |
| Cp,gas | 39.11 | J/mol×K | 2036.67 | Calculated Property |
| Cp,gas | 39.75 | J/mol×K | 2377.50 | Calculated Property |
| Cp,gas | 40.42 | J/mol×K | 2718.33 | Calculated Property |
| Cp,gas | 41.06 | J/mol×K | 3059.17 | Calculated Property |
| Cp,gas | 41.63 | J/mol×K | 3400.00 | Calculated Property |
| Cp,gas | [41.49; 37.63] | J/mol×K | [3400.00; 6000.00] |
NIST
|
| Equation | Y = A + B·t + C·t² + D·t³ + E/t², t = T/1000 Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 3.49929e+01 | |||
| Coefficient B | 9.25225e+00 | |||
| Coefficient C | -2.36159e+00 | |||
| Coefficient D | 1.54336e-01 | |||
| Coefficient E | -4.30764e+01 | |||
| Reference | Chase, 1998 | |||
| Comment | F=-7.467771, G=273.6303, H=30.91001; Data last reviewed in June, 1982 | |||
| Temperature range, min. | 3400.00 | |||
| Temperature range, max. | 6000.00 | |||
| Cp,gas | 41.49 | J/mol×K | 3400.00 | Calculated Property |
| Cp,gas | 41.57 | J/mol×K | 3688.89 | Calculated Property |
| Cp,gas | 41.42 | J/mol×K | 3977.78 | Calculated Property |
| Cp,gas | 41.10 | J/mol×K | 4266.67 | Calculated Property |
| Cp,gas | 40.65 | J/mol×K | 4555.56 | Calculated Property |
| Cp,gas | 40.10 | J/mol×K | 4844.44 | Calculated Property |
| Cp,gas | 39.50 | J/mol×K | 5133.33 | Calculated Property |
| Cp,gas | 38.87 | J/mol×K | 5422.22 | Calculated Property |
| Cp,gas | 38.23 | J/mol×K | 5711.11 | Calculated Property |
| Cp,gas | 37.63 | J/mol×K | 6000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [75.35; 75.35] | J/mol×K | [265.90; 331.90] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 7.53510e+01 | |||
| Coefficient B | -4.87000e+07 | |||
| Coefficient C | 5.40261e+04 | |||
| Coefficient D | 1.02730e+02 | |||
| Coefficient E | 4.37750e-01 | |||
| Temperature range, min. | 265.90 | |||
| Temperature range, max. | 331.90 | |||
| Cp,liquid | 75.35 | J/mol×K | 265.90 | Calculated Property |
| Cp,liquid | 75.35 | J/mol×K | 273.23 | Calculated Property |
| Cp,liquid | 75.35 | J/mol×K | 280.57 | Calculated Property |
| Cp,liquid | 75.35 | J/mol×K | 287.90 | Calculated Property |
| Cp,liquid | 75.35 | J/mol×K | 295.23 | Calculated Property |
| Cp,liquid | 75.35 | J/mol×K | 302.57 | Calculated Property |
| Cp,liquid | 75.35 | J/mol×K | 309.90 | Calculated Property |
| Cp,liquid | 75.35 | J/mol×K | 317.23 | Calculated Property |
| Cp,liquid | 75.35 | J/mol×K | 324.57 | Calculated Property |
| Cp,liquid | 75.35 | J/mol×K | 331.90 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0013548; 0.0006007] | Pa×s | [265.85; 350.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -5.98130e+00 | |||
| Coefficient B | 4.10550e+02 | |||
| Coefficient C | -3.00360e-01 | |||
| Coefficient D | -6.93600e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 265.85 | |||
| Temperature range, max. | 350.00 | |||
| η | 0.0013548 | Pa×s | 265.85 | Calculated Property |
| η | 0.0012284 | Pa×s | 275.20 | Calculated Property |
| η | 0.0011167 | Pa×s | 284.55 | Calculated Property |
| η | 0.0010174 | Pa×s | 293.90 | Calculated Property |
| η | 0.0009287 | Pa×s | 303.25 | Calculated Property |
| η | 0.0008491 | Pa×s | 312.60 | Calculated Property |
| η | 0.0007775 | Pa×s | 321.95 | Calculated Property |
| η | 0.0007127 | Pa×s | 331.30 | Calculated Property |
| η | 0.0006540 | Pa×s | 340.65 | Calculated Property |
| η | 0.0006007 | Pa×s | 350.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [32.59; 0.00] | kJ/mol | [265.85; 584.15] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 3.84190e+01 | |||
| Coefficient B | -2.62820e-01 | |||
| Coefficient C | 2.18080e+00 | |||
| Coefficient D | -2.75290e+00 | |||
| Coefficient E | 1.18230e+00 | |||
| Critical temperature, Tc (K) | 5.84150e+02 | |||
| Temperature range, min. | 265.85 | |||
| Temperature range, max. | 584.15 | |||
| ΔvapH | 32.59 | kJ/mol | 265.85 | Calculated Property |
| ΔvapH | 31.09 | kJ/mol | 301.22 | Calculated Property |
| ΔvapH | 29.54 | kJ/mol | 336.58 | Calculated Property |
| ΔvapH | 27.93 | kJ/mol | 371.95 | Calculated Property |
| ΔvapH | 26.21 | kJ/mol | 407.32 | Calculated Property |
| ΔvapH | 24.29 | kJ/mol | 442.68 | Calculated Property |
| ΔvapH | 22.02 | kJ/mol | 478.05 | Calculated Property |
| ΔvapH | 19.14 | kJ/mol | 513.42 | Calculated Property |
| ΔvapH | 14.95 | kJ/mol | 548.78 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 584.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [5.85; 10296.51] | kPa | [265.85; 584.15] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.47457e+01 | |||
| Coefficient B | -3.04378e+03 | |||
| Coefficient C | -3.13500e+01 | |||
| Temperature range, min. | 265.85 | |||
| Temperature range, max. | 584.15 | |||
| Pvap | 5.85 | kPa | 265.85 | Calculated Property |
| Pvap | 32.04 | kPa | 301.22 | Calculated Property |
| Pvap | 118.36 | kPa | 336.58 | Calculated Property |
| Pvap | 333.34 | kPa | 371.95 | Calculated Property |
| Pvap | 772.63 | kPa | 407.32 | Calculated Property |
| Pvap | 1549.81 | kPa | 442.68 | Calculated Property |
| Pvap | 2784.30 | kPa | 478.05 | Calculated Property |
| Pvap | 4590.08 | kPa | 513.42 | Calculated Property |
| Pvap | 7067.18 | kPa | 548.78 | Calculated Property |
| Pvap | 10296.51 | kPa | 584.15 | Calculated Property |
| Pvap | [6.02; 10272.27] | kPa | [265.15; 584.15] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 5.67492e+01 | |||
| Coefficient B | -5.32160e+03 | |||
| Coefficient C | -6.31990e+00 | |||
| Coefficient D | 5.44120e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 265.15 | |||
| Temperature range, max. | 584.15 | |||
| Pvap | 6.02 | kPa | 265.15 | Calculated Property |
| Pvap | 32.38 | kPa | 300.59 | Calculated Property |
| Pvap | 117.11 | kPa | 336.04 | Calculated Property |
| Pvap | 322.73 | kPa | 371.48 | Calculated Property |
| Pvap | 734.19 | kPa | 406.93 | Calculated Property |
| Pvap | 1454.73 | kPa | 442.37 | Calculated Property |
| Pvap | 2605.28 | kPa | 477.82 | Calculated Property |
| Pvap | 4329.95 | kPa | 513.26 | Calculated Property |
| Pvap | 6807.95 | kPa | 548.71 | Calculated Property |
| Pvap | 10272.27 | kPa | 584.15 | Calculated Property |
| Pvap | [1.37; 200.31] | kPa | [243.15; 354.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 2.30793e+02 | |||
| Coefficient B | -1.11621e+04 | |||
| Coefficient C | -3.41575e+01 | |||
| Coefficient D | 5.20176e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 243.15 | |||
| Temperature range, max. | 354.00 | |||
| Pvap | 1.37 | kPa | 243.15 | Calculated Property |
| Pvap | 3.18 | kPa | 255.47 | Calculated Property |
| Pvap | 6.64 | kPa | 267.78 | Calculated Property |
| Pvap | 12.70 | kPa | 280.10 | Calculated Property |
| Pvap | 22.57 | kPa | 292.42 | Calculated Property |
| Pvap | 37.82 | kPa | 304.73 | Calculated Property |
| Pvap | 60.39 | kPa | 317.05 | Calculated Property |
| Pvap | 92.72 | kPa | 329.37 | Calculated Property |
| Pvap | 137.98 | kPa | 341.68 | Calculated Property |
| Pvap | 200.31 | kPa | 354.00 | Calculated Property |
| Pvap | [145.17; 432.44] | kPa | [343.00; 383.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.54464e+01 | |||
| Coefficient B | -3.59725e+03 | |||
| Coefficient C | 6.28000e-01 | |||
| Reference | Blair and Ihle, 1973 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 343.00 | |||
| Temperature range, max. | 383.00 | |||
| Pvap | 145.17 | kPa | 343.00 | Calculated Property |
| Pvap | 165.94 | kPa | 347.44 | Calculated Property |
| Pvap | 189.03 | kPa | 351.89 | Calculated Property |
| Pvap | 214.64 | kPa | 356.33 | Calculated Property |
| Pvap | 242.96 | kPa | 360.78 | Calculated Property |
| Pvap | 274.18 | kPa | 365.22 | Calculated Property |
| Pvap | 308.53 | kPa | 369.67 | Calculated Property |
| Pvap | 346.20 | kPa | 374.11 | Calculated Property |
| Pvap | 387.43 | kPa | 378.56 | Calculated Property |
| Pvap | 432.44 | kPa | 383.00 | Calculated Property |
| Pvap | [0.13; 98.60] | kPa | [224.50; 331.40] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.13870e+01 | |||
| Coefficient B | -1.46964e+03 | |||
| Coefficient C | -1.15144e+02 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 224.50 | |||
| Temperature range, max. | 331.40 | |||
| Pvap | 0.13 | kPa | 224.50 | Calculated Property |
| Pvap | 0.48 | kPa | 236.38 | Calculated Property |
| Pvap | 1.41 | kPa | 248.26 | Calculated Property |
| Pvap | 3.49 | kPa | 260.13 | Calculated Property |
| Pvap | 7.53 | kPa | 272.01 | Calculated Property |
| Pvap | 14.55 | kPa | 283.89 | Calculated Property |
| Pvap | 25.80 | kPa | 295.77 | Calculated Property |
| Pvap | 42.63 | kPa | 307.64 | Calculated Property |
| Pvap | 66.43 | kPa | 319.52 | Calculated Property |
| Pvap | 98.60 | kPa | 331.40 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [3210.53; 1136.06] | kg/m3 | [265.85; 584.15] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 3.29252e+02 | |||
| Coefficient B | 2.89820e-01 | |||
| Coefficient C | 5.84150e+02 | |||
| Coefficient D | 2.89480e-01 | |||
| Temperature range, min. | 265.85 | |||
| Temperature range, max. | 584.15 | |||
| ρl | 3210.53 | kg/m3 | 265.85 | Calculated Property |
| ρl | 3100.65 | kg/m3 | 301.22 | Calculated Property |
| ρl | 2984.83 | kg/m3 | 336.58 | Calculated Property |
| ρl | 2861.61 | kg/m3 | 371.95 | Calculated Property |
| ρl | 2728.88 | kg/m3 | 407.32 | Calculated Property |
| ρl | 2583.31 | kg/m3 | 442.68 | Calculated Property |
| ρl | 2419.19 | kg/m3 | 478.05 | Calculated Property |
| ρl | 2224.92 | kg/m3 | 513.42 | Calculated Property |
| ρl | 1968.99 | kg/m3 | 548.78 | Calculated Property |
| ρl | 1136.06 | kg/m3 | 584.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.05; 2.11e-05] | N/m | [265.85; 582.56] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -1.42740e-02 | |||
| Coefficient B | 2.35980e+02 | |||
| Coefficient C | -4.51310e+00 | |||
| Coefficient D | 5.91590e-03 | |||
| Coefficient E | -1.05670e-05 | |||
| Comment | Range stopped where the equation turns negative; ChemSep gives it to 584.15 K. | |||
| Temperature range, min. | 265.85 | |||
| Temperature range, max. | 582.56 | |||
| γ | 0.05 | N/m | 265.85 | Calculated Property |
| γ | 0.04 | N/m | 301.04 | Calculated Property |
| γ | 0.03 | N/m | 336.23 | Calculated Property |
| γ | 0.03 | N/m | 371.42 | Calculated Property |
| γ | 0.02 | N/m | 406.61 | Calculated Property |
| γ | 0.02 | N/m | 441.80 | Calculated Property |
| γ | 0.01 | N/m | 476.99 | Calculated Property |
| γ | 0.01 | N/m | 512.18 | Calculated Property |
| γ | 0.00 | N/m | 547.37 | Calculated Property |
| γ | 2.11e-05 | N/m | 582.56 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.00; 0.01] | W/m×K | [265.85; 520.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 6.56480e-06 | |||
| Coefficient B | 1.47850e+00 | |||
| Coefficient C | 4.50560e+03 | |||
| Coefficient D | -8.70500e+05 | |||
| Temperature range, min. | 265.85 | |||
| Temperature range, max. | 520.00 | |||
| λgas | 0.00 | W/m×K | 265.85 | Calculated Property |
| λgas | 0.00 | W/m×K | 294.09 | Calculated Property |
| λgas | 0.01 | W/m×K | 322.33 | Calculated Property |
| λgas | 0.01 | W/m×K | 350.57 | Calculated Property |
| λgas | 0.01 | W/m×K | 378.81 | Calculated Property |
| λgas | 0.01 | W/m×K | 407.04 | Calculated Property |
| λgas | 0.01 | W/m×K | 435.28 | Calculated Property |
| λgas | 0.01 | W/m×K | 463.52 | Calculated Property |
| λgas | 0.01 | W/m×K | 491.76 | Calculated Property |
| λgas | 0.01 | W/m×K | 520.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.13; 0.04] | W/m×K | [260.00; 584.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K | |||
| Coefficient A | -6.91830e-01 | |||
| Coefficient B | 2.77750e+01 | |||
| Coefficient C | -3.89660e-01 | |||
| Coefficient D | 5.71030e-04 | |||
| Coefficient E | -8.84620e-07 | |||
| Temperature range, min. | 260.00 | |||
| Temperature range, max. | 584.00 | |||
| λliquid | 0.13 | W/m×K | 260.00 | Calculated Property |
| λliquid | 0.12 | W/m×K | 296.00 | Calculated Property |
| λliquid | 0.12 | W/m×K | 332.00 | Calculated Property |
| λliquid | 0.11 | W/m×K | 368.00 | Calculated Property |
| λliquid | 0.10 | W/m×K | 404.00 | Calculated Property |
| λliquid | 0.09 | W/m×K | 440.00 | Calculated Property |
| λliquid | 0.08 | W/m×K | 476.00 | Calculated Property |
| λliquid | 0.07 | W/m×K | 512.00 | Calculated Property |
| λliquid | 0.06 | W/m×K | 548.00 | Calculated Property |
| λliquid | 0.04 | W/m×K | 584.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Bromine.
Sources
- KDB Vapor Pressure Data
- Active Thermochemical Tables 1.112, gas-phase enthalpies of formation ChEDL chemicals 1.5.2, from Active Thermochemical Tables (ATcT), version 1.112, Argonne National Laboratory; Ruscic, B. et al. Active Thermochemical Tables: Thermochemistry for the 21st Century. J. Phys.: Conf. Ser. 2005, 16, 561.
- Mathews (1972), critical constants of inorganic substances ChEDL chemicals 1.5.2, from Mathews, J. F. Critical Constants of Inorganic Substances. Chem. Rev. 1972, 72, 71-100.
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Crippen Method
- Crippen Method
- Standard molar enthalpies of formation of hydroxy-, chlor-, and bromapatite
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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