- InChI
- InChI=1S/C8H9Br/c1-6-4-3-5-7(2)8(6)9/h3-5H,1-2H3
- InChI Key
- MYMYVYZLMUEVED-UHFFFAOYSA-N
- Formula
- C8H9Br
- SMILES
- Cc1cccc(C)c1Br
- Molecular Weight1
- 185.06
- CAS
- 576-22-7
- Other Names
-
- 1-Bromo-2,6-dimethylbenzene
- 2,6-Dimethylbromobenzene
- 2-Bromo-1,3-dimethylbenzene
- 2-Bromo-m-xylene
- 2-Bromo-meta-xylene
- m-Xylene, 2-bromo-
- 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).
- 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).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (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° | 123.95 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 31.47 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 15.02 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 43.44 | kJ/mol | Joback Calculated Property |
| log10WS | -3.59 | Crippen Calculated Property | |
| logPoct/wat | 3.066 | Crippen Calculated Property | |
| McVol | 117.320 | ml/mol | McGowan Calculated Property |
| Pc | 3829.28 | kPa | Joback Calculated Property |
| Tboil | [479.00; 479.20] | K |
|
| Tboil | 479.20 | K | NIST |
| Tboil | 479.00 | K | NIST |
| Tc | 716.43 | K | Joback Calculated Property |
| Tfus | 291.18 | K | Joback Calculated Property |
| Vc | 0.438 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [212.91; 270.81] | J/mol×K | [485.24; 716.43] |
|
| Cp,gas | 212.91 | J/mol×K | 485.24 | Joback Calculated Property |
| Cp,gas | 224.18 | J/mol×K | 523.77 | Joback Calculated Property |
| Cp,gas | 234.76 | J/mol×K | 562.30 | Joback Calculated Property |
| Cp,gas | 244.68 | J/mol×K | 600.83 | Joback Calculated Property |
| Cp,gas | 253.98 | J/mol×K | 639.37 | Joback Calculated Property |
| Cp,gas | 262.68 | J/mol×K | 677.90 | Joback Calculated Property |
| Cp,gas | 270.81 | J/mol×K | 716.43 | Joback Calculated Property |
| η | [0.0002772; 0.0016069] | Pa×s | [291.18; 485.24] |
|
| η | 0.0016069 | Pa×s | 291.18 | Joback Calculated Property |
| η | 0.0010357 | Pa×s | 323.52 | Joback Calculated Property |
| η | 0.0007230 | Pa×s | 355.87 | Joback Calculated Property |
| η | 0.0005358 | Pa×s | 388.21 | Joback Calculated Property |
| η | 0.0004159 | Pa×s | 420.55 | Joback Calculated Property |
| η | 0.0003347 | Pa×s | 452.90 | Joback Calculated Property |
| η | 0.0002772 | Pa×s | 485.24 | Joback Calculated Property |
| Pvap | [6.95e-03; 0.08] | kPa | [274.20; 305.30] |
|
| Pvap | 6.95e-03 | kPa | 274.20 | Thermoc... |
| Pvap | 8.40e-03 | kPa | 276.20 | Thermoc... |
| Pvap | 0.01 | kPa | 278.30 | Thermoc... |
| Pvap | 0.01 | kPa | 281.20 | Thermoc... |
| Pvap | 0.02 | kPa | 284.20 | Thermoc... |
| Pvap | 0.02 | kPa | 287.20 | Thermoc... |
| Pvap | 0.03 | kPa | 290.20 | Thermoc... |
| Pvap | 0.03 | kPa | 293.30 | Thermoc... |
| Pvap | 0.03 | kPa | 293.30 | Thermoc... |
| Pvap | 0.03 | kPa | 293.40 | Thermoc... |
| Pvap | 0.04 | kPa | 296.30 | Thermoc... |
| Pvap | 0.05 | kPa | 299.30 | Thermoc... |
| Pvap | 0.06 | kPa | 302.20 | Thermoc... |
| Pvap | 0.08 | kPa | 305.30 | Thermoc... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 315.00 | K | 0.10 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [350.32; 511.87] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.39149e+01 | |||
| Coefficient B | -3.77016e+03 | |||
| Coefficient C | -7.36590e+01 | |||
| Temperature range, min. | 350.32 | |||
| Temperature range, max. | 511.87 | |||
| Pvap | 1.33 | kPa | 350.32 | Calculated Property |
| Pvap | 3.06 | kPa | 368.27 | Calculated Property |
| Pvap | 6.38 | kPa | 386.22 | Calculated Property |
| Pvap | 12.28 | kPa | 404.17 | Calculated Property |
| Pvap | 22.10 | kPa | 422.12 | Calculated Property |
| Pvap | 37.54 | kPa | 440.07 | Calculated Property |
| Pvap | 60.71 | kPa | 458.02 | Calculated Property |
| Pvap | 94.04 | kPa | 475.97 | Calculated Property |
| Pvap | 140.32 | kPa | 493.92 | Calculated Property |
| Pvap | 202.64 | kPa | 511.87 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, 2-bromo-1,3-dimethyl-.
Sources
- Crippen Method
- Crippen Method
- Thermochemistry of Halogen-Substituted Methylbenzenes
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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