- InChI
- InChI=1S/C6H5Br/c7-6-4-2-1-3-5-6/h1-5H
- InChI Key
- QARVLSVVCXYDNA-UHFFFAOYSA-N
- Formula
- C6H5Br
- SMILES
- Brc1ccccc1
- Molecular Weight1
- 157.01
- CAS
- 108-86-1
- Other Names
-
- 1-Bromobenzene
- Bromobenzene
- MONOBROMOBENZENE
- NCI-C55492
- PHENYL BROMIDE
- UN 2514
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- BasG : Gas basicity (kJ/mol).
- 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).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase 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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- 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).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboil : Boiling point at given pressure (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Tfus : Melting point (K).
- Ttriple : Triple Point Temperature (K).
- 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 | 0.2510 | KDB | |
| PAff | 754.10 | kJ/mol | NIST |
| Tig | 838.15 | K | KDB |
| BasG | 725.80 | kJ/mol | NIST |
| ΔcH°liquid | -3111.90 ± 0.67 | kJ/mol | NIST |
| μ | 1.50 | debye | KDB |
| Tflash,oc | 324.26 | K | KDB |
| ΔfG° | 138.60 | kJ/mol | KDB |
| ΔfH°gas | 105.10 | kJ/mol | KDB |
| ΔfH°liquid | [58.60; 60.90] | kJ/mol |
|
| ΔfH°liquid | 58.60 | kJ/mol | NIST |
| ΔfH°liquid | 60.90 ± 4.10 | kJ/mol | NIST |
| ΔfusH° | 10.62 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [37.90; 44.80] | kJ/mol |
|
| ΔvapH° | 44.54 | kJ/mol | NIST |
| ΔvapH° | 44.80 | kJ/mol | NIST |
| ΔvapH° | 44.50 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 44.54 ± 0.04 | kJ/mol | NIST |
| ΔvapH° | 37.90 ± 0.03 | kJ/mol | NIST |
| IE | [8.95; 9.45] | eV |
|
| IE | 9.00 ± 0.03 | eV | NIST |
| IE | 9.00 | eV | NIST |
| IE | 9.00 | eV | NIST |
| IE | 9.02 | eV | NIST |
| IE | 9.05 ± 0.02 | eV | NIST |
| IE | 8.98 ± 0.02 | eV | NIST |
| IE | 8.98 | eV | NIST |
| IE | Outlier 9.45 | eV | NIST |
| IE | 8.97 ± 0.02 | eV | NIST |
| IE | 8.99 | eV | NIST |
| IE | 9.03 ± 0.01 | eV | NIST |
| IE | 8.98 ± 0.03 | eV | NIST |
| IE | 8.95 | eV | NIST |
| IE | 8.98 ± 0.02 | eV | NIST |
| IE | 8.99 | eV | NIST |
| IE | 9.04 | eV | NIST |
| IE | 9.05 | eV | NIST |
| IE | 8.99 ± 0.03 | eV | NIST |
| IE | 9.00 | eV | NIST |
| log10WS | [-2.55; -2.55] |
|
|
| log10WS | -2.55 | Aq. Sol... | |
| log10WS | -2.55 | Estimat... | |
| logPoct/wat | 2.449 | Crippen Calculated Property | |
| McVol | 89.140 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | 4520.00 | kPa | KDB |
| Inp | [150.00; 983.00] |
|
|
| Inp | 960.00 | NIST | |
| Inp | 952.20 | NIST | |
| Inp | 931.71 | NIST | |
| Inp | 941.36 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 914.70 | NIST | |
| Inp | 923.70 | NIST | |
| Inp | 934.80 | NIST | |
| Inp | 959.60 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | 925.80 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 979.60 | NIST | |
| Inp | 941.00 | NIST | |
| Inp | 903.90 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 909.50 | NIST | |
| Inp | 919.67 | NIST | |
| Inp | 921.35 | NIST | |
| Inp | 926.64 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 918.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 930.00 | NIST | |
| Inp | 921.00 | NIST | |
| Inp | 935.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 936.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 983.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 936.00 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | 930.00 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | Outlier 150.00 | NIST | |
| I | [1330.00; 1391.00] |
|
|
| I | 1351.00 | NIST | |
| I | 1338.00 | NIST | |
| I | 1330.00 | NIST | |
| I | 1381.03 | NIST | |
| I | 1373.68 | NIST | |
| I | 1358.59 | NIST | |
| I | 1348.92 | NIST | |
| I | 1391.00 | NIST | |
| I | 1338.00 | NIST | |
| I | 1365.00 | NIST | |
| S°liquid | [207.90; 21922.00] | J/mol×K |
|
| S°liquid | 21922.00 | J/mol×K | NIST |
| S°liquid | 207.90 | J/mol×K | NIST |
| Tboil | 429.21 | K | KDB |
| Tc | 670.00 | K | KDB |
| Tfus | [242.25; 242.50] | K |
|
| Tfus | 242.50 | K | KDB |
| Tfus | 242.25 | K | Aq. Sol... |
| Ttriple | [242.40; 242.42] | K |
|
| Ttriple | 242.40 | K | KDB |
| Ttriple | 242.42 ± 0.02 | K | NIST |
| Ttriple | 242.40 ± 0.01 | K | NIST |
| Ttriple | 242.40 ± 0.20 | K | NIST |
| Vc | 0.324 | m3/kmol | KDB |
| Zc | 0.2628890 | KDB | |
| Zra | 0.26 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [135.44; 182.34] | J/mol×K | [429.52; 665.41] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 140 150 160 170 180 500 600 | ||||
| Cp,gas | 135.44 | J/mol×K | 429.52 | Joback Calculated Property |
| Cp,gas | 144.94 | J/mol×K | 468.84 | Joback Calculated Property |
| Cp,gas | 153.71 | J/mol×K | 508.15 | Joback Calculated Property |
| Cp,gas | 161.79 | J/mol×K | 547.47 | Joback Calculated Property |
| Cp,gas | 169.22 | J/mol×K | 586.78 | Joback Calculated Property |
| Cp,gas | 176.06 | J/mol×K | 626.10 | Joback Calculated Property |
| Cp,gas | 182.34 | J/mol×K | 665.41 | Joback Calculated Property |
| Cp,liquid | [127.60; 167.15] | J/mol×K | [231.70; 353.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 130 140 150 160 170 250 300 350 | ||||
| Cp,liquid | 127.60 | J/mol×K | 231.70 | NIST |
| Cp,liquid | 151.63 | J/mol×K | 283.15 | Heat Ca... |
| Cp,liquid | 151.99 | J/mol×K | 285.15 | Heat Ca... |
| Cp,liquid | 152.37 | J/mol×K | 287.15 | Heat Ca... |
| Cp,liquid | 152.75 | J/mol×K | 289.15 | Heat Ca... |
| Cp,liquid | 153.14 | J/mol×K | 291.15 | Heat Ca... |
| Cp,liquid | 153.54 | J/mol×K | 293.15 | Heat Ca... |
| Cp,liquid | 151.50 | J/mol×K | 293.20 | NIST |
| Cp,liquid | 153.94 | J/mol×K | 295.15 | Heat Ca... |
| Cp,liquid | 154.35 | J/mol×K | 297.15 | Heat Ca... |
| Cp,liquid | 151.00 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 155.39 | J/mol×K | 298.10 | NIST |
| Cp,liquid | 154.29 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 154.77 | J/mol×K | 299.15 | Heat Ca... |
| Cp,liquid | 155.19 | J/mol×K | 301.15 | Heat Ca... |
| Cp,liquid | 145.60 | J/mol×K | 302.60 | NIST |
| Cp,liquid | 145.60 | J/mol×K | 302.60 | NIST |
| Cp,liquid | 155.62 | J/mol×K | 303.15 | Heat Ca... |
| Cp,liquid | 155.90 | J/mol×K | 303.15 | NIST |
| Cp,liquid | 156.05 | J/mol×K | 305.15 | Heat Ca... |
| Cp,liquid | 156.49 | J/mol×K | 307.15 | Heat Ca... |
| Cp,liquid | 156.93 | J/mol×K | 309.15 | Heat Ca... |
| Cp,liquid | 157.38 | J/mol×K | 311.15 | Heat Ca... |
| Cp,liquid | 157.83 | J/mol×K | 313.15 | Heat Ca... |
| Cp,liquid | 158.28 | J/mol×K | 315.15 | Heat Ca... |
| Cp,liquid | 158.74 | J/mol×K | 317.15 | Heat Ca... |
| Cp,liquid | 159.20 | J/mol×K | 319.15 | Heat Ca... |
| Cp,liquid | 159.66 | J/mol×K | 321.15 | Heat Ca... |
| Cp,liquid | 160.13 | J/mol×K | 323.15 | Heat Ca... |
| Cp,liquid | 160.60 | J/mol×K | 325.15 | Heat Ca... |
| Cp,liquid | 161.06 | J/mol×K | 327.15 | Heat Ca... |
| Cp,liquid | 161.53 | J/mol×K | 329.15 | Heat Ca... |
| Cp,liquid | 162.00 | J/mol×K | 331.15 | Heat Ca... |
| Cp,liquid | 162.48 | J/mol×K | 333.15 | Heat Ca... |
| Cp,liquid | 162.95 | J/mol×K | 335.15 | Heat Ca... |
| Cp,liquid | 163.42 | J/mol×K | 337.15 | Heat Ca... |
| Cp,liquid | 163.89 | J/mol×K | 339.15 | Heat Ca... |
| Cp,liquid | 164.36 | J/mol×K | 341.15 | Heat Ca... |
| Cp,liquid | 164.83 | J/mol×K | 343.15 | Heat Ca... |
| Cp,liquid | 165.30 | J/mol×K | 345.15 | Heat Ca... |
| Cp,liquid | 165.76 | J/mol×K | 347.15 | Heat Ca... |
| Cp,liquid | 166.23 | J/mol×K | 349.15 | Heat Ca... |
| Cp,liquid | 166.69 | J/mol×K | 351.15 | Heat Ca... |
| Cp,liquid | 167.15 | J/mol×K | 353.15 | Heat Ca... |
| η | [0.0008780; 0.0011640] | Pa×s | [293.00; 313.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 8.50e-4 9.00e-4 9.50e-4 1.00e-3 1.05e-3 1.10e-3 1.15e-3 295 300 305 310 | ||||
| η | 0.0011640 | Pa×s | 293.00 | Thermop... |
| η | 0.0010410 | Pa×s | 298.15 | Thermop... |
| η | 0.0010820 | Pa×s | 298.15 | Thermop... |
| η | 0.0009844 | Pa×s | 303.00 | Thermop... |
| η | 0.0010146 | Pa×s | 303.15 | Thermop... |
| η | 0.0009640 | Pa×s | 308.15 | Thermop... |
| η | 0.0009540 | Pa×s | 308.15 | Thermop... |
| η | 0.0008786 | Pa×s | 313.00 | Thermop... |
| η | 0.0008780 | Pa×s | 313.15 | Thermop... |
| ΔfusH | [10.63; 10.70] | kJ/mol | [242.40; 242.43] |
|
| ΔfusH | 10.70 | kJ/mol | 242.40 | NIST |
| ΔfusH | 10.70 | kJ/mol | 242.40 | NIST |
| ΔfusH | 10.70 | kJ/mol | 242.40 | NIST |
| ΔfusH | 10.63 | kJ/mol | 242.43 | NIST |
| ΔvapH | [42.30; 44.00] | kJ/mol | [293.00; 429.10] |
|
| ΔvapH | 44.00 | kJ/mol | 293.00 | NIST |
| ΔvapH | 42.40 | kJ/mol | 378.00 | NIST |
| ΔvapH | 42.30 | kJ/mol | 398.00 | NIST |
| ΔvapH | 42.50 | kJ/mol | 429.10 | KDB |
| Pvap | [0.13; 95.30] | kPa | [276.40; 426.85] |
|
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 300 350 400 | ||||
| Pvap | 0.13 | kPa | 276.40 | Thermoc... |
| Pvap | 0.15 | kPa | 278.30 | Thermoc... |
| Pvap | 0.20 | kPa | 282.20 | Thermoc... |
| Pvap | 0.21 | kPa | 283.10 | Thermoc... |
| Pvap | 0.25 | kPa | 285.40 | Thermoc... |
| Pvap | 0.25 | kPa | 286.20 | Thermoc... |
| Pvap | 0.30 | kPa | 288.30 | Thermoc... |
| Pvap | 0.32 | kPa | 289.30 | Thermoc... |
| Pvap | 0.35 | kPa | 291.40 | Thermoc... |
| Pvap | 0.38 | kPa | 292.40 | Thermoc... |
| Pvap | 0.40 | kPa | 293.20 | Thermoc... |
| Pvap | 0.44 | kPa | 294.40 | Thermoc... |
| Pvap | 0.46 | kPa | 295.50 | Thermoc... |
| Pvap | 0.52 | kPa | 297.40 | Thermoc... |
| Pvap | 0.64 | kPa | 300.40 | Thermoc... |
| Pvap | 0.76 | kPa | 303.40 | Thermoc... |
| Pvap | 95.30 | kPa | 426.85 | Vapor-l... |
| n0 | [1.54970; 1.55770] | [293.15; 313.15] |
|
|
|
T(K) Refractive Index 1.55 1.55 1.55 1.56 1.56 295 300 305 310 | ||||
| n0 | 1.55710 | 293.15 | Excess ... | |
| n0 | 1.55710 | 298.15 | Activit... | |
| n0 | 1.55710 | 298.15 | (Vapor ... | |
| n0 | 1.55770 | 298.15 | Density... | |
| n0 | 1.55610 | 303.15 | Refract... | |
| n0 | 1.55460 | 303.15 | Excess ... | |
| n0 | 1.55420 | 303.15 | Density... | |
| n0 | 1.55140 | 308.15 | Density... | |
| n0 | 1.55340 | 308.15 | Refract... | |
| n0 | 1.54970 | 313.15 | Refract... | |
| ρl | [1441.22; 1495.52] | kg/m3 | [293.00; 333.15] |
|
|
T(K) Liquid Density (kg/m3) 1440 1450 1460 1470 1480 1490 1500 300 310 320 330 | ||||
| ρl | 1495.00 | kg/m3 | 293.00 | KDB |
| ρl | 1495.52 | kg/m3 | 293.15 | Theoret... |
| ρl | 1495.28 | kg/m3 | 293.20 | Isobari... |
| ρl | 1495.23 | kg/m3 | 293.20 | Isobari... |
| ρl | 1488.12 | kg/m3 | 298.15 | Densiti... |
| ρl | 1481.52 | kg/m3 | 303.15 | Studies... |
| ρl | 1481.40 | kg/m3 | 303.15 | Densiti... |
| ρl | 1481.97 | kg/m3 | 303.15 | Theoret... |
| ρl | 1474.58 | kg/m3 | 308.15 | Densiti... |
| ρl | 1475.36 | kg/m3 | 308.15 | Studies... |
| ρl | 1468.41 | kg/m3 | 313.15 | Theoret... |
| ρl | 1468.02 | kg/m3 | 313.15 | Studies... |
| ρl | 1461.36 | kg/m3 | 318.15 | Studies... |
| ρl | 1454.85 | kg/m3 | 323.15 | Theoret... |
| ρl | 1441.22 | kg/m3 | 333.15 | Theoret... |
| ΔfusS | [43.84; 44.15] | J/mol×K | [242.40; 242.43] |
|
| ΔfusS | 44.15 | J/mol×K | 242.40 | NIST |
| ΔfusS | 43.84 | J/mol×K | 242.43 | NIST |
| γ | 0.04 | N/m | 293.20 | KDB |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | 427.85 | K | 95.30 | Excess ... |
| Tboilr | 300.90 | K | 0.70 | NIST |
| Tfus | [259.05; 587.21] | K | [100000.00; 3500000.00] |
|
|
P(kPa) Melting point (K) 250 300 350 400 450 500 550 600 1000000 2000000 3000000 | ||||
| Tfus | 259.05 | K | 100000.00 | Fusion ... |
| Tfus | 276.45 | K | 200000.00 | Fusion ... |
| Tfus | 292.45 | K | 300000.00 | Fusion ... |
| Tfus | 310.05 | K | 400000.00 | Fusion ... |
| Tfus | 322.55 | K | 500000.00 | Fusion ... |
| Tfus | 336.15 | K | 600000.00 | Fusion ... |
| Tfus | 349.25 | K | 700000.00 | Fusion ... |
| Tfus | 361.85 | K | 800000.00 | Fusion ... |
| Tfus | 374.75 | K | 900000.00 | Fusion ... |
| Tfus | 382.85 | K | 1000000.00 | Fusion ... |
| Tfus | 430.05 | K | 1500000.00 | Fusion ... |
| Tfus | 473.67 | K | 2000000.00 | Fusion ... |
| Tfus | 514.22 | K | 2500000.00 | Fusion ... |
| Tfus | 553.94 | K | 3000000.00 | Fusion ... |
| Tfus | 587.21 | K | 3500000.00 | Fusion ... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 248.15 | 99.70 | 1554.489 |
| 248.15 | 1231.41 | 1555.368 |
| 248.15 | 2075.45 | 1556.036 |
| 248.15 | 4196.22 | 1557.697 |
| 248.15 | 5950.98 | 1559.054 |
| 248.15 | 8068.32 | 1560.666 |
| 248.15 | 10015.40 | 1562.113 |
| 248.15 | 11951.60 | 1563.577 |
| 248.15 | 13994.80 | 1565.093 |
| 248.15 | 15940.30 | 1566.527 |
| 248.15 | 18145.00 | 1568.122 |
| 248.15 | 19946.50 | 1569.417 |
| 248.15 | 21965.00 | 1570.861 |
| 248.15 | 24135.90 | 1572.41 |
| 248.15 | 25864.70 | 1573.623 |
| 248.15 | 27917.30 | 1575.05 |
| 248.15 | 29850.30 | 1576.387 |
| 273.15 | 100.51 | 1520.557 |
| 273.15 | 1116.26 | 1521.447 |
| 273.15 | 2128.10 | 1522.34 |
| 273.15 | 4045.82 | 1524.026 |
| 273.15 | 5967.30 | 1525.66 |
| 273.15 | 8142.83 | 1527.515 |
| 273.15 | 10020.30 | 1529.109 |
| 273.15 | 11896.10 | 1530.677 |
| 273.15 | 13922.00 | 1532.353 |
| 273.15 | 16083.00 | 1534.134 |
| 273.15 | 18195.20 | 1535.834 |
| 273.15 | 20035.10 | 1537.31 |
| 273.15 | 21829.30 | 1538.747 |
| 273.15 | 23856.50 | 1540.342 |
| 273.15 | 25976.20 | 1542.017 |
| 273.15 | 28097.70 | 1543.651 |
| 273.15 | 29947.00 | 1545.093 |
| 293.15 | 101.93 | 1493.557 |
| 293.15 | 1239.69 | 1494.684 |
| 293.15 | 2010.73 | 1495.408 |
| 293.15 | 4059.70 | 1497.371 |
| 293.15 | 6007.85 | 1499.218 |
| 293.15 | 8079.77 | 1501.16 |
| 293.15 | 10000.80 | 1502.944 |
| 293.15 | 11960.00 | 1504.732 |
| 293.15 | 14168.60 | 1506.732 |
| 293.15 | 15878.80 | 1508.265 |
| 293.15 | 17960.30 | 1510.109 |
| 293.15 | 19999.40 | 1511.901 |
| 293.15 | 21880.00 | 1513.531 |
| 293.15 | 24122.20 | 1515.458 |
| 293.15 | 26141.00 | 1517.174 |
| 293.15 | 28060.50 | 1518.79 |
| 293.15 | 29992.70 | 1520.418 |
| 313.15 | 102.54 | 1466.553 |
| 313.15 | 2000.76 | 1468.587 |
| 313.15 | 4010.97 | 1470.712 |
| 313.15 | 6189.56 | 1473.0 |
| 313.15 | 7991.64 | 1474.858 |
| 313.15 | 10089.40 | 1477.007 |
| 313.15 | 12142.80 | 1479.063 |
| 313.15 | 14014.60 | 1480.929 |
| 313.15 | 16087.30 | 1482.944 |
| 313.15 | 18046.60 | 1484.852 |
| 313.15 | 20004.20 | 1486.73 |
| 313.15 | 22154.30 | 1488.763 |
| 313.15 | 23944.20 | 1490.446 |
| 313.15 | 26099.80 | 1492.424 |
| 313.15 | 28042.50 | 1494.215 |
| 313.15 | 29905.50 | 1495.902 |
| 333.15 | 100.42 | 1439.385 |
| 333.15 | 1115.03 | 1440.596 |
| 333.15 | 1943.37 | 1441.571 |
| 333.15 | 4094.54 | 1444.097 |
| 333.15 | 6114.22 | 1446.439 |
| 333.15 | 7927.80 | 1448.512 |
| 333.15 | 10021.70 | 1450.842 |
| 333.15 | 11958.50 | 1453.001 |
| 333.15 | 13999.00 | 1455.239 |
| 333.15 | 16048.70 | 1457.443 |
| 333.15 | 18155.70 | 1459.682 |
| 333.15 | 20007.80 | 1461.631 |
| 333.15 | 22157.50 | 1463.842 |
| 333.15 | 24129.60 | 1465.857 |
| 333.15 | 26094.50 | 1467.846 |
| 333.15 | 28018.50 | 1469.764 |
| 333.15 | 29890.30 | 1471.607 |
| 353.15 | 99.80 | 1411.936 |
| 353.15 | 1173.75 | 1413.368 |
| 353.15 | 1944.34 | 1414.39 |
| 353.15 | 3949.81 | 1417.013 |
| 353.15 | 5968.93 | 1419.612 |
| 353.15 | 7990.46 | 1422.164 |
| 353.15 | 9916.05 | 1424.555 |
| 353.15 | 11986.60 | 1427.088 |
| 353.15 | 14134.60 | 1429.674 |
| 353.15 | 15921.30 | 1431.797 |
| 353.15 | 18146.30 | 1434.386 |
| 353.15 | 19873.50 | 1436.374 |
| 353.15 | 22180.00 | 1438.986 |
| 353.15 | 23963.50 | 1440.977 |
| 353.15 | 26085.20 | 1443.316 |
| 353.15 | 28122.10 | 1445.529 |
| 353.15 | 29956.10 | 1447.501 |
| 373.15 | 98.54 | 1384.068 |
| 373.15 | 1150.11 | 1385.641 |
| 373.15 | 2174.39 | 1387.16 |
| 373.15 | 3917.65 | 1389.708 |
| 373.15 | 6182.40 | 1392.956 |
| 373.15 | 8042.69 | 1395.57 |
| 373.15 | 10003.40 | 1398.276 |
| 373.15 | 12007.70 | 1400.991 |
| 373.15 | 14086.40 | 1403.757 |
| 373.15 | 15912.60 | 1406.155 |
| 373.15 | 18065.60 | 1408.912 |
| 373.15 | 19882.10 | 1411.213 |
| 373.15 | 22174.10 | 1414.047 |
| 373.15 | 24052.60 | 1416.329 |
| 373.15 | 25897.20 | 1418.541 |
| 373.15 | 27711.00 | 1420.705 |
| 373.15 | 29530.80 | 1422.851 |
| 393.15 | 97.33 | 1355.66 |
| 393.15 | 1226.04 | 1357.559 |
| 393.15 | 2181.20 | 1359.152 |
| 393.15 | 3965.26 | 1362.078 |
| 393.15 | 6075.43 | 1365.466 |
| 393.15 | 8146.91 | 1368.751 |
| 393.15 | 9937.30 | 1371.465 |
| 393.15 | 11969.70 | 1374.529 |
| 393.15 | 14177.00 | 1377.777 |
| 393.15 | 15955.80 | 1380.344 |
| 393.15 | 18163.70 | 1383.473 |
| 393.15 | 20146.90 | 1386.231 |
| 393.15 | 22175.70 | 1388.998 |
| 393.15 | 23981.50 | 1391.424 |
| 393.15 | 26169.90 | 1394.302 |
| 393.15 | 28005.40 | 1396.697 |
| 393.15 | 29541.50 | 1398.685 |
| 413.15 | 99.45 | 1326.547 |
| 413.15 | 1202.85 | 1328.655 |
| 413.15 | 2177.13 | 1330.512 |
| 413.15 | 3915.54 | 1333.735 |
| 413.15 | 6185.52 | 1337.833 |
| 413.15 | 8176.14 | 1341.325 |
| 413.15 | 10032.40 | 1344.48 |
| 413.15 | 12103.60 | 1348.01 |
| 413.15 | 13991.80 | 1351.03 |
| 413.15 | 15890.50 | 1354.115 |
| 413.15 | 18162.20 | 1357.681 |
| 413.15 | 19933.00 | 1360.414 |
| 413.15 | 22150.20 | 1363.736 |
| 413.15 | 24133.10 | 1366.656 |
| 413.15 | 26038.90 | 1369.413 |
| 413.15 | 27898.50 | 1372.058 |
| 413.15 | 29858.00 | 1374.805 |
| 433.15 | 1243.75 | 1299.092 |
| 433.15 | 1973.28 | 1300.66 |
| 433.15 | 4075.91 | 1305.09 |
| 433.15 | 6197.75 | 1309.427 |
| 433.15 | 7981.47 | 1312.955 |
| 433.15 | 10019.80 | 1316.907 |
| 433.15 | 12072.60 | 1320.75 |
| 433.15 | 14033.50 | 1324.335 |
| 433.15 | 15960.20 | 1327.765 |
| 433.15 | 17921.10 | 1331.186 |
| 433.15 | 19992.20 | 1334.752 |
| 433.15 | 21950.20 | 1337.95 |
| 433.15 | 24017.90 | 1341.307 |
| 433.15 | 26143.40 | 1344.678 |
| 433.15 | 28052.40 | 1347.64 |
| 433.15 | 29864.50 | 1350.426 |
| 453.15 | 1135.36 | 1268.141 |
| 453.15 | 1982.45 | 1270.245 |
| 453.15 | 4017.67 | 1275.165 |
| 453.15 | 6189.02 | 1280.221 |
| 453.15 | 7994.19 | 1284.28 |
| 453.15 | 10138.80 | 1288.978 |
| 453.15 | 12157.20 | 1293.201 |
| 453.15 | 13981.80 | 1296.937 |
| 453.15 | 16133.80 | 1301.214 |
| 453.15 | 18121.60 | 1305.054 |
| 453.15 | 19974.20 | 1308.564 |
| 453.15 | 22140.80 | 1312.522 |
| 453.15 | 24115.40 | 1316.051 |
| 453.15 | 26121.30 | 1319.557 |
| 453.15 | 28034.20 | 1322.825 |
| 453.15 | 29912.10 | 1325.979 |
| 473.15 | 1191.19 | 1236.278 |
| 473.15 | 2175.44 | 1239.118 |
| 473.15 | 4131.48 | 1244.576 |
| 473.15 | 5988.10 | 1249.543 |
| 473.15 | 8161.41 | 1255.135 |
| 473.15 | 10165.40 | 1260.077 |
| 473.15 | 12165.90 | 1264.845 |
| 473.15 | 14162.70 | 1269.434 |
| 473.15 | 16124.70 | 1273.802 |
| 473.15 | 18166.70 | 1278.202 |
| 473.15 | 20146.20 | 1282.345 |
| 473.15 | 22123.10 | 1286.362 |
| 473.15 | 24157.00 | 1290.388 |
| 473.15 | 26074.70 | 1294.08 |
| 473.15 | 28019.90 | 1297.733 |
| 473.15 | 29860.30 | 1301.116 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [312.67; 458.01] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.44191e+01 | |||
| Coefficient B | -3.72354e+03 | |||
| Coefficient C | -4.91780e+01 | |||
| Temperature range, min. | 312.67 | |||
| Temperature range, max. | 458.01 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 312.67 | Calculated Property |
| Pvap | 3.02 | kPa | 328.82 | Calculated Property |
| Pvap | 6.24 | kPa | 344.97 | Calculated Property |
| Pvap | 11.97 | kPa | 361.12 | Calculated Property |
| Pvap | 21.54 | kPa | 377.27 | Calculated Property |
| Pvap | 36.68 | kPa | 393.41 | Calculated Property |
| Pvap | 59.56 | kPa | 409.56 | Calculated Property |
| Pvap | 92.77 | kPa | 425.71 | Calculated Property |
| Pvap | 139.33 | kPa | 441.86 | Calculated Property |
| Pvap | 202.63 | kPa | 458.01 | Calculated Property |
| Pvap | [7.67e-03; 4446.48] | kPa | [242.43; 670.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.92440e+01 | |||
| Coefficient B | -7.92948e+03 | |||
| Coefficient C | -9.41640e+00 | |||
| Coefficient D | 5.04459e-06 | |||
| Temperature range, min. | 242.43 | |||
| Temperature range, max. | 670.15 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 300 400 500 600 | ||||
| Pvap | 7.67e-03 | kPa | 242.43 | Calculated Property |
| Pvap | 0.34 | kPa | 289.95 | Calculated Property |
| Pvap | 4.50 | kPa | 337.48 | Calculated Property |
| Pvap | 28.15 | kPa | 385.00 | Calculated Property |
| Pvap | 110.01 | kPa | 432.53 | Calculated Property |
| Pvap | 315.03 | kPa | 480.05 | Calculated Property |
| Pvap | 730.18 | kPa | 527.58 | Calculated Property |
| Pvap | 1461.92 | kPa | 575.10 | Calculated Property |
| Pvap | 2642.33 | kPa | 622.63 | Calculated Property |
| Pvap | 4446.48 | kPa | 670.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, bromo-.
Mixtures
- Benzene, bromo- + Triethylene glycol
- Benzene, bromo- + Methyl Alcohol
- Benzene, bromo- + 1-Hexanol, 2-ethyl-
- Benzene, bromo- + Heptane
- Benzene, nitro- + Benzene, bromo-
- Benzene, bromo- + Dimethyl Sulfoxide
- Benzene, bromo- + Formamide, N,N-dimethyl-
- Benzene, bromo- + N-Formylmorpholine
- Acetonitrile + Benzene, bromo-
- Benzene, bromo- + Ethane, 1,2-dichloro-
- Benzene, bromo- + m-Chloroaniline
- Acetic acid, pentyl ester + Benzene, bromo-
- Acetic acid, chloro-, ethyl ester + Benzene, bromo-
- Ethane, 1,2-dibromo- + Benzene, bromo-
- Benzene, bromo- + Methyl formate
- Ethyl formate + Benzene, bromo-
- Formic acid, propyl ester + Benzene, bromo-
- Acetic acid, phenylmethyl ester + Benzene, bromo-
- Benzene, bromo- + Ethanol, 2-methoxy-
- Benzene, bromo- + Benzene, chloro-
Find more mixtures with Benzene, bromo-.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Thermophysical Properties For Diethylene Glycol + Nitrobenzene and Triethylene Glycol + (Chloro-, Bromo-, Nitro-) Benzene Systems at Different Temperatures
- Thermophysical Properties of Binary Mixtures of Methanol with Chlorobenzene and Bromobenzene from 293K to 313K
- Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Ethyl-1-hexanol with Benzene and Halobenzenes
- Isobaric vapour liquid equilibria for binary mixtures of n-heptane with bromobenzene, chlorobenzene and fluorobenzene at atmospheric pressure
- Excess Gibbs energies of binary mixtures formed by nitrobenzene with selected compounds at 94.95 kPa
- Vapor-liquid equilibrium for the binary mixtures of dimethylsulfoxide with substituted benzenes
- Excess enthalpies of dimethylsulfoxide with substituted benzenes at 298.15K
- Activity coefficients and excess Gibbs energy of binary mixtures of N,N-dimethyl formamide with selected compounds at 95.5 kPa
- Refractive properties, speed of sound and FT-IR study of binary mixtures of N-formylmorpholine with some halobenzenes at 303.15, 308.15 and 313.15 K
- (Vapor + liquid) equilibrium of the binary mixtures formed by acetonitrile with selected compounds at 95.5 kPa
- Measurement and correlation of the (p, ?, T) relation of liquid n-heptane, n-nonane, 2,4-dichlorotoluene, and bromobenzene in the temperature range from (233.15 to 473.15) K at pressures up to 30 MPa for use as density reference liquids
- Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
- Thermodynamics of solvation in propylene glycol and methyl cellosolve
- Phase behavior of ionic liquids 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imides with halogenated benzenes
- Theoretical and experimental study on volumetric and electromagnetic properties of binary systems consisting of 1,2-dichloroethane with benzene and its derivatives at T = (293.15 to 333.15) K
- Studies on the importance of nature of substituent on the thermodynamic and transport properties of liquid mixtures at various temperatures
- Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
- Volumetric and electromagnetic properties of binary mixtures consist of benzene derivatives at different temperature and ternary mixtures with 1,2-dichloroethane at T = 293.15 K with application of the Prigogine-Flory-Patterson theory and PC-SAFT
- Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Ethyl Chloroacetate + Cyclohexanone, + Chlorobenzene, + Bromobenzene, or + Benzyl Alcohol at (298.15, 303.15, and 308.15) K
- Solubilities of p-Tolylboronic Acid, Bromobenzene and 4-Phenyltoluene in Carbon Dioxide at Elevated Pressures
- Isobaric Vapor-Liquid Equilibria for Binary Mixtures of 1,2-Dibromoethane with Benzene, Toluene, Fluorobenzene, and Bromobenzene at Atmospheric Pressure
- Thermophysical properties of the binary mixtures of 1,2-Dichloroethane with Chlorobenzene and Bromobenzene from 298.15 to 313.15 K
- Measuring the Aqueous Henry's Law Constant at Elevated Temperatures Using an Extended EPICS Technique
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Solubility of Hydrofluorocarbons in Halobenzene Solvents
- Thermochemistry of Halogen-Substituted Methylbenzenes
- Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
- Excess Volumes of Binary Solutions of Methyl Formate, Ethyl Formate, Propyl Formate, and Benzyl Acetate with Bromo-, Chloro-, and Nitrobenzenes at (303.15, 308.15, and 313.15) K
- Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
- Liquid-Liquid Equilibria in Binary Mixtures Containing Chlorobenzene, Bromobenzene, and Iodobenzene with Ionic Liquid 1-Ethyl-3-methylimidazolim Bis(trifluoromethylsulfonyl)imide
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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