Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 104.81 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 68.48 | kJ/mol | Joback Calculated Property |
ΔfusH° | 14.43 | kJ/mol | Joback Calculated Property |
ΔvapH° | 42.71 | kJ/mol | Joback Calculated Property |
log10WS | [-3.19; -3.19] |
![]() |
|
log10WS | -3.19 | Aq. Sol... | |
log10WS | -3.19 | Estimat... | |
logPoct/wat | 3.103 | Crippen Calculated Property | |
McVol | 101.380 | ml/mol | McGowan Calculated Property |
Pc | 4782.59 | kPa | Joback Calculated Property |
Inp | [188.00; 1137.48] |
![]() |
|
Inp | 1137.48 | NIST | |
Inp | 1111.54 | NIST | |
Inp | 1123.72 | NIST | |
Inp | 1097.60 | NIST | |
Inp | 1097.60 | NIST | |
Inp | 1105.74 | NIST | |
Inp | 1110.94 | NIST | |
Inp | 1116.38 | NIST | |
Inp | 1120.00 | NIST | |
Inp | 1111.00 | NIST | |
Inp | 1100.00 | NIST | |
Inp | 1094.00 | NIST | |
Inp | Outlier 188.00 | NIST | |
Inp | 1137.48 | NIST | |
Inp | Outlier 188.00 | NIST | |
Inp | 1097.60 | NIST | |
Inp | 1120.00 | NIST | |
I | [1633.76; 1665.31] |
![]() |
|
I | 1665.31 | NIST | |
I | 1653.05 | NIST | |
I | 1650.41 | NIST | |
I | 1633.76 | NIST | |
Tboil | [468.00; 477.20] | K |
![]() |
Tboil | 477.20 | K | NIST |
Tboil | 468.00 | K | NIST |
Tc | 716.18 | K | Joback Calculated Property |
Tfus | [260.50; 261.00] | K |
![]() |
Tfus | 260.50 | K | Aq. Sol... |
Tfus | 261.00 | K | NIST |
Tfus | 260.55 ± 0.20 | K | NIST |
Vc | 0.374 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [156.69; 197.22] | J/mol×K | [471.93; 716.18] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 160 170 180 190 200 500 600 700 | ||||
Cp,gas | 156.69 | J/mol×K | 471.93 | Joback Calculated Property |
Cp,gas | 164.95 | J/mol×K | 512.64 | Joback Calculated Property |
Cp,gas | 172.55 | J/mol×K | 553.35 | Joback Calculated Property |
Cp,gas | 179.54 | J/mol×K | 594.05 | Joback Calculated Property |
Cp,gas | 185.95 | J/mol×K | 634.76 | Joback Calculated Property |
Cp,gas | 191.83 | J/mol×K | 675.47 | Joback Calculated Property |
Cp,gas | 197.22 | J/mol×K | 716.18 | Joback Calculated Property |
Cp,liquid | [172.25; 186.53] | J/mol×K | [283.15; 353.15] | ![]() |
T(K) Liquid phase heat capacity (J/mol×K) 172 174 176 178 180 182 184 186 300 320 340 | ||||
Cp,liquid | 172.25 | J/mol×K | 283.15 | Heat Ca... |
Cp,liquid | 172.59 | J/mol×K | 285.15 | Heat Ca... |
Cp,liquid | 172.94 | J/mol×K | 287.15 | Heat Ca... |
Cp,liquid | 173.29 | J/mol×K | 289.15 | Heat Ca... |
Cp,liquid | 173.65 | J/mol×K | 291.15 | Heat Ca... |
Cp,liquid | 174.02 | J/mol×K | 293.15 | Heat Ca... |
Cp,liquid | 174.39 | J/mol×K | 295.15 | Heat Ca... |
Cp,liquid | 174.78 | J/mol×K | 297.15 | Heat Ca... |
Cp,liquid | 176.90 | J/mol×K | 298.15 | NIST |
Cp,liquid | 175.17 | J/mol×K | 299.15 | Heat Ca... |
Cp,liquid | 175.56 | J/mol×K | 301.15 | Heat Ca... |
Cp,liquid | 175.96 | J/mol×K | 303.15 | Heat Ca... |
Cp,liquid | 176.36 | J/mol×K | 305.15 | Heat Ca... |
Cp,liquid | 176.77 | J/mol×K | 307.15 | Heat Ca... |
Cp,liquid | 177.19 | J/mol×K | 309.15 | Heat Ca... |
Cp,liquid | 177.61 | J/mol×K | 311.15 | Heat Ca... |
Cp,liquid | 178.03 | J/mol×K | 313.15 | Heat Ca... |
Cp,liquid | 178.45 | J/mol×K | 315.15 | Heat Ca... |
Cp,liquid | 178.88 | J/mol×K | 317.15 | Heat Ca... |
Cp,liquid | 179.31 | J/mol×K | 319.15 | Heat Ca... |
Cp,liquid | 179.74 | J/mol×K | 321.15 | Heat Ca... |
Cp,liquid | 180.17 | J/mol×K | 323.15 | Heat Ca... |
Cp,liquid | 180.60 | J/mol×K | 325.15 | Heat Ca... |
Cp,liquid | 181.03 | J/mol×K | 327.15 | Heat Ca... |
Cp,liquid | 181.47 | J/mol×K | 329.15 | Heat Ca... |
Cp,liquid | 181.90 | J/mol×K | 331.15 | Heat Ca... |
Cp,liquid | 182.33 | J/mol×K | 333.15 | Heat Ca... |
Cp,liquid | 182.77 | J/mol×K | 335.15 | Heat Ca... |
Cp,liquid | 183.20 | J/mol×K | 337.15 | Heat Ca... |
Cp,liquid | 183.62 | J/mol×K | 339.15 | Heat Ca... |
Cp,liquid | 184.05 | J/mol×K | 341.15 | Heat Ca... |
Cp,liquid | 184.47 | J/mol×K | 343.15 | Heat Ca... |
Cp,liquid | 184.89 | J/mol×K | 345.15 | Heat Ca... |
Cp,liquid | 185.31 | J/mol×K | 347.15 | Heat Ca... |
Cp,liquid | 185.72 | J/mol×K | 349.15 | Heat Ca... |
Cp,liquid | 186.13 | J/mol×K | 351.15 | Heat Ca... |
Cp,liquid | 186.53 | J/mol×K | 353.15 | Heat Ca... |
η | [0.0003355; 0.0020482] | Pa×s | [286.04; 471.93] | ![]() |
T(K) Dynamic viscosity (Pa×s) 5.00e-4 1.00e-3 1.50e-3 2.00e-3 300 350 400 450 | ||||
η | 0.0020482 | Pa×s | 286.04 | Joback Calculated Property |
η | 0.0013076 | Pa×s | 317.02 | Joback Calculated Property |
η | 0.0009042 | Pa×s | 348.00 | Joback Calculated Property |
η | 0.0006641 | Pa×s | 378.99 | Joback Calculated Property |
η | 0.0005111 | Pa×s | 409.97 | Joback Calculated Property |
η | 0.0004080 | Pa×s | 440.95 | Joback Calculated Property |
η | 0.0003355 | Pa×s | 471.93 | Joback Calculated Property |
ΔfusH | [12.37; 12.37] | kJ/mol | [260.55; 260.60] | ![]() |
ΔfusH | 12.37 | kJ/mol | 260.55 | NIST |
ΔfusH | 12.37 | kJ/mol | 260.60 | NIST |
ΔfusS | 47.50 | J/mol×K | 260.55 | NIST |
Find more compounds similar to Benzene, 1-bromo-2-chloro-.
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.