- InChI
- InChI=1S/C6H5Cl/c7-6-4-2-1-3-5-6/h1-5H
- InChI Key
- MVPPADPHJFYWMZ-UHFFFAOYSA-N
- Formula
- C6H5Cl
- SMILES
- Clc1ccccc1
- Molecular Weight1
- 112.56
- CAS
- 108-90-7
- Other Names
-
- Abluton T30
- Benzene chloride
- CP 27
- Chloorbenzeen
- Chlorbenzene
- Chlorbenzol
- Chlorobenzen
- Chlorobenzene, mono-
- Chlorobenzenu
- Chlorobenzol
- Clorobenzene
- IP Carrier T 40
- MCB
- Monochloorbenzeen
- Monochlorbenzene
- Monochlorbenzol
- Monoclorobenzene
- NCI-C54886
- NSC 8433
- Tetrosin SP
- UN 1134
- chlorobenzene
- monochlorobenzene
- phenyl chloride
- 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).
- Cp,solid : Solid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- LFL : Lower Flammability Limit (% in Air).
- UFL : Upper Flammability Limit (% in Air).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Rg : Radius of Gyration.
- 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.
- ρc : Critical density (kg/m3).
- 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).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboil : Boiling point at given 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.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.2490 | KDB | |
| PAff | 753.10 | kJ/mol | NIST |
| Tig | 913.15 | K | KDB |
| BasG | 724.60 | kJ/mol | NIST |
| ΔcH°liquid | [-3112.70; -3108.90] | kJ/mol |
|
| ΔcH°liquid | -3112.70 ± 0.90 | kJ/mol | NIST |
| ΔcH°liquid | -3110.70 ± 1.00 | kJ/mol | NIST |
| ΔcH°liquid | -3108.90 ± 0.79 | kJ/mol | NIST |
| ΔcH°liquid | -3111.60 ± 8.40 | kJ/mol | NIST |
| μ | 1.60 | debye | KDB |
| LFL | 1.30 | % in Air | KDB |
| UFL | 7.10 | % in Air | KDB |
| Tflash,cc | 309.26 | K | KDB |
| Tflash,oc | 302.04 | K | KDB |
| ΔfG° | 99.23 | kJ/mol | KDB |
| Rg | 3.5680 | KDB | |
| ΔfH°gas | [51.87; 54.42] | kJ/mol |
|
| ΔfH°gas | 51.87 | kJ/mol | KDB |
| ΔfH°gas | 54.42 | kJ/mol | NIST |
| ΔfH°liquid | [10.70; 11.50] | kJ/mol |
|
| ΔfH°liquid | 11.50 ± 1.00 | kJ/mol | NIST |
| ΔfH°liquid | 10.70 ± 0.79 | kJ/mol | NIST |
| ΔfusH° | 9.53 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [36.60; 43.90] | kJ/mol |
|
| ΔvapH° | 41.00 | kJ/mol | NIST |
| ΔvapH° | 40.30 | kJ/mol | NIST |
| ΔvapH° | 43.90 | kJ/mol | NIST |
| ΔvapH° | 41.00 | kJ/mol | NIST |
| ΔvapH° | 41.00 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 40.97 ± 0.06 | kJ/mol | NIST |
| ΔvapH° | Outlier 36.60 ± 0.04 | kJ/mol | NIST |
| IE | [8.80; 9.55] | eV |
|
| IE | 9.07 ± 0.02 | eV | NIST |
| IE | 9.08 | eV | NIST |
| IE | Outlier 8.80 | eV | NIST |
| IE | 9.07 ± 0.03 | eV | NIST |
| IE | 9.10 | eV | NIST |
| IE | 9.10 ± 0.02 | eV | NIST |
| IE | 9.10 ± 0.02 | eV | NIST |
| IE | 9.06 ± 0.01 | eV | NIST |
| IE | 9.09 | eV | NIST |
| IE | Outlier 9.55 | eV | NIST |
| IE | 9.07 ± 0.02 | eV | NIST |
| IE | 9.10 ± 0.10 | eV | NIST |
| IE | 8.99 | eV | NIST |
| IE | 9.08 ± 0.01 | eV | NIST |
| IE | 9.04 | eV | NIST |
| IE | 9.05 | eV | NIST |
| IE | 9.07 | eV | NIST |
| IE | 9.07 ± 0.02 | eV | NIST |
| IE | 9.07 | eV | NIST |
| IE | 9.07 | eV | NIST |
| IE | 9.08 | eV | NIST |
| IE | 9.07 | eV | NIST |
| IE | 9.09 | eV | NIST |
| log10WS | [-2.39; -2.38] |
|
|
| log10WS | -2.39 | Aq. Solubility Prediction | |
| log10WS | -2.38 | Estimated Solubility | |
| logPoct/wat | 2.340 | Crippen Calculated Property | |
| McVol | 83.880 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | [4519.10; 4520.00] | kPa |
|
| Pc | 4520.00 | kPa | KDB |
| Pc | 4519.10 ± 30.39 | kPa | NIST |
| ρc | 364.68 ± 4.50 | kg/m3 | NIST |
| Inp | [811.00; 885.00] |
|
|
| Inp | 859.30 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 853.80 | NIST | |
| Inp | Outlier 877.50 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 830.32 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 866.47 | NIST | |
| Inp | 850.16 | NIST | |
| Inp | 857.29 | NIST | |
| Inp | 842.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 836.00 | NIST | |
| Inp | 838.80 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 850.30 | NIST | |
| Inp | 864.50 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 840.00 | NIST | |
| Inp | Outlier 880.00 | NIST | |
| Inp | Outlier 880.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 849.60 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 854.60 | NIST | |
| Inp | 857.40 | NIST | |
| Inp | 860.30 | NIST | |
| Inp | 863.30 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 836.00 | NIST | |
| Inp | 840.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 838.40 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 818.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 826.30 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 817.00 | NIST | |
| Inp | 821.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 820.00 | NIST | |
| Inp | 826.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 819.00 | NIST | |
| Inp | 833.00 | NIST | |
| Inp | 822.00 | NIST | |
| Inp | 826.00 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 819.00 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 819.00 | NIST | |
| Inp | 825.00 | NIST | |
| Inp | 822.00 | NIST | |
| Inp | 811.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 817.00 | NIST | |
| Inp | 822.00 | NIST | |
| Inp | Outlier 885.00 | NIST | |
| Inp | 833.00 | NIST | |
| Inp | Outlier 877.90 | NIST | |
| Inp | 831.20 | NIST | |
| Inp | 821.20 | NIST | |
| Inp | 852.40 | NIST | |
| Inp | 826.50 | NIST | |
| Inp | 836.42 | NIST | |
| Inp | 837.68 | NIST | |
| Inp | 840.15 | NIST | |
| Inp | 825.30 | NIST | |
| Inp | 833.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 825.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 842.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 828.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 833.00 | NIST | |
| Inp | Outlier 880.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 841.00 | NIST | |
| Inp | 842.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | Outlier 880.00 | NIST | |
| Inp | 824.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 836.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 820.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 859.30 | NIST | |
| Inp | 830.32 | NIST | |
| Inp | 842.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 840.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 860.30 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 838.40 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 820.00 | NIST | |
| Inp | 822.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 825.00 | NIST | |
| Inp | 817.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 841.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | Outlier 877.90 | NIST | |
| I | [1188.00; 1279.10] |
|
|
| I | 1257.10 | NIST | |
| I | 1279.10 | NIST | |
| I | 1224.00 | NIST | |
| I | 1257.00 | NIST | |
| I | 1231.00 | NIST | |
| I | 1257.00 | NIST | |
| I | 1270.00 | NIST | |
| I | 1270.00 | NIST | |
| I | 1219.00 | NIST | |
| I | 1213.00 | NIST | |
| I | 1243.90 | NIST | |
| I | 1240.38 | NIST | |
| I | 1226.05 | NIST | |
| I | 1220.51 | NIST | |
| I | 1241.00 | NIST | |
| I | 1234.00 | NIST | |
| I | 1202.00 | NIST | |
| I | 1233.00 | NIST | |
| I | 1238.00 | NIST | |
| I | 1238.00 | NIST | |
| I | 1209.00 | NIST | |
| I | Outlier 1188.00 | NIST | |
| I | 1205.00 | NIST | |
| I | 1241.00 | NIST | |
| I | 1200.00 | NIST | |
| I | 1238.00 | NIST | |
| I | 1209.00 | NIST | |
| I | 1257.10 | NIST | |
| I | 1257.00 | NIST | |
| S°liquid | 197.50 | J/mol×K | NIST |
| Tboil | [402.15; 444.85] | K |
|
| Tboil | 404.80 | K | Isobaric Vapor-Liquid Equilibrium for Binary and Ternary Systems of tert-Butanol + tert-Butyl Acetate + Chlorobenzene at 101.33 kPa |
| Tboil | 404.87 | K | KDB |
| Tboil | 404.60 ± 0.40 | K | NIST |
| Tboil | 405.20 ± 0.50 | K | NIST |
| Tboil | 404.80 ± 0.50 | K | NIST |
| Tboil | 404.90 ± 0.50 | K | NIST |
| Tboil | 404.85 ± 0.40 | K | NIST |
| Tboil | 405.20 | K | NIST |
| Tboil | 404.95 ± 0.30 | K | NIST |
| Tboil | 404.15 ± 1.00 | K | NIST |
| Tboil | 404.90 | K | NIST |
| Tboil | 404.82 ± 0.40 | K | NIST |
| Tboil | 405.65 ± 0.40 | K | NIST |
| Tboil | 405.20 ± 0.60 | K | NIST |
| Tboil | 404.80 ± 0.70 | K | NIST |
| Tboil | 404.87 ± 0.25 | K | NIST |
| Tboil | 404.65 ± 0.30 | K | NIST |
| Tboil | 404.98 ± 0.25 | K | NIST |
| Tboil | 404.75 ± 0.30 | K | NIST |
| Tboil | 404.40 ± 0.40 | K | NIST |
| Tboil | 404.90 ± 0.40 | K | NIST |
| Tboil | 405.15 ± 1.50 | K | NIST |
| Tboil | 405.20 ± 0.40 | K | NIST |
| Tboil | Outlier 444.85 ± 0.20 | K | NIST |
| Tboil | 404.70 ± 0.50 | K | NIST |
| Tboil | 404.90 ± 0.50 | K | NIST |
| Tboil | 404.95 ± 0.30 | K | NIST |
| Tboil | 404.20 ± 1.00 | K | NIST |
| Tboil | 405.11 ± 0.30 | K | NIST |
| Tboil | 405.15 ± 0.20 | K | NIST |
| Tboil | 405.00 ± 3.00 | K | NIST |
| Tboil | 404.60 ± 0.50 | K | NIST |
| Tboil | 404.70 ± 0.30 | K | NIST |
| Tboil | 404.45 ± 0.50 | K | NIST |
| Tboil | 404.82 ± 0.20 | K | NIST |
| Tboil | 404.90 ± 0.50 | K | NIST |
| Tboil | 405.15 ± 0.60 | K | NIST |
| Tboil | 404.90 ± 0.30 | K | NIST |
| Tboil | 404.90 ± 0.30 | K | NIST |
| Tboil | 404.80 ± 1.00 | K | NIST |
| Tboil | 404.98 ± 0.10 | K | NIST |
| Tboil | 405.15 ± 0.40 | K | NIST |
| Tboil | 404.83 ± 0.10 | K | NIST |
| Tboil | 405.20 ± 0.50 | K | NIST |
| Tboil | 405.20 ± 0.50 | K | NIST |
| Tboil | 404.85 ± 0.50 | K | NIST |
| Tboil | 405.15 ± 0.04 | K | NIST |
| Tboil | 405.12 ± 0.30 | K | NIST |
| Tboil | 404.15 ± 1.50 | K | NIST |
| Tboil | 405.15 ± 0.40 | K | NIST |
| Tboil | 405.15 ± 0.04 | K | NIST |
| Tboil | 405.15 ± 0.20 | K | NIST |
| Tboil | 405.15 ± 0.40 | K | NIST |
| Tboil | 405.15 ± 0.05 | K | NIST |
| Tboil | 404.65 ± 0.50 | K | NIST |
| Tboil | 402.15 ± 1.50 | K | NIST |
| Tboil | 405.50 ± 0.80 | K | NIST |
| Tc | [632.35; 635.35] | K |
|
| Tc | 632.40 | K | KDB |
| Tc | 632.35 ± 0.30 | K | NIST |
| Tc | 632.65 ± 6.00 | K | NIST |
| Tc | 635.35 ± 2.00 | K | NIST |
| Tfus | [227.57; 228.25] | K |
|
| Tfus | 227.90 | K | KDB |
| Tfus | 227.82 | K | Aq. Solubility Prediction |
| Tfus | 227.83 ± 0.06 | K | NIST |
| Tfus | 228.15 ± 1.00 | K | NIST |
| Tfus | Outlier 227.57 ± 0.20 | K | NIST |
| Tfus | 228.00 ± 1.50 | K | NIST |
| Tfus | 228.15 ± 0.40 | K | NIST |
| Tfus | 227.95 ± 0.06 | K | NIST |
| Tfus | 227.95 ± 0.10 | K | NIST |
| Tfus | 227.92 ± 0.10 | K | NIST |
| Tfus | 227.80 ± 0.15 | K | NIST |
| Tfus | 228.05 ± 0.20 | K | NIST |
| Tfus | 227.95 ± 0.20 | K | NIST |
| Tfus | 227.95 ± 0.50 | K | NIST |
| Tfus | Outlier 227.57 ± 0.10 | K | NIST |
| Tfus | 227.95 ± 0.50 | K | NIST |
| Tfus | 228.15 ± 0.30 | K | NIST |
| Tfus | 228.15 ± 0.30 | K | NIST |
| Tfus | 228.15 ± 0.25 | K | NIST |
| Tfus | 228.15 ± 2.00 | K | NIST |
| Tfus | 228.25 ± 0.50 | K | NIST |
| Ttriple | [227.90; 227.90] | K |
|
| Ttriple | 227.90 ± 0.20 | K | NIST |
| Ttriple | 227.90 ± 0.20 | K | NIST |
| Vc | 0.308 | m3/kmol | KDB |
| Zc | 0.2647650 | KDB | |
| Zra | 0.27 | KDB |
Temperature Dependent Properties
Pressure Dependent Properties
Datasets
Speed of sound, m/s
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Frequency, MHz - Liquid | Speed of sound, m/s - Liquid |
| 303.15 | 100.00 | 2.0 | 1251.8 |
| Reference | |||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [88.91; 218.62] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | -2.35800e+01 | |||
| Coefficient B | 5.01700e-01 | |||
| Coefficient C | -3.54200e-04 | |||
| Coefficient D | 9.47000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 88.91 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 113.77 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 135.32 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 153.86 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 169.68 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 183.10 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 194.40 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 203.89 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 211.86 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 218.62 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [293.56; 432.78] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.45006e+01 | |||
| Coefficient B | -3.61917e+03 | |||
| Coefficient C | -3.89210e+01 | |||
| Temperature range, min. | 293.56 | |||
| Temperature range, max. | 432.78 | |||
| Pvap | 1.33 | kPa | 293.56 | Calculated Property |
| Pvap | 3.01 | kPa | 309.03 | Calculated Property |
| Pvap | 6.22 | kPa | 324.50 | Calculated Property |
| Pvap | 11.92 | kPa | 339.97 | Calculated Property |
| Pvap | 21.46 | kPa | 355.44 | Calculated Property |
| Pvap | 36.56 | kPa | 370.90 | Calculated Property |
| Pvap | 59.40 | kPa | 386.37 | Calculated Property |
| Pvap | 92.60 | kPa | 401.84 | Calculated Property |
| Pvap | 139.20 | kPa | 417.31 | Calculated Property |
| Pvap | 202.67 | kPa | 432.78 | Calculated Property |
| Pvap | [9.25e-03; 4404.58] | kPa | [227.95; 632.35] |
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 | 5.24220e+01 | |||
| Coefficient B | -6.32735e+03 | |||
| Coefficient C | -5.42919e+00 | |||
| Coefficient D | 2.47507e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 227.95 | |||
| Temperature range, max. | 632.35 | |||
| Pvap | 9.25e-03 | kPa | 227.95 | Calculated Property |
| Pvap | 0.36 | kPa | 272.88 | Calculated Property |
| Pvap | 4.41 | kPa | 317.82 | Calculated Property |
| Pvap | 27.30 | kPa | 362.75 | Calculated Property |
| Pvap | 107.88 | kPa | 407.68 | Calculated Property |
| Pvap | 314.15 | kPa | 452.62 | Calculated Property |
| Pvap | 738.14 | kPa | 497.55 | Calculated Property |
| Pvap | 1485.81 | kPa | 542.48 | Calculated Property |
| Pvap | 2669.18 | kPa | 587.42 | Calculated Property |
| Pvap | 4404.58 | kPa | 632.35 | Calculated Property |
| Pvap | [9.65; 101.40] | kPa | [335.19; 404.88] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.40707e+01 | |||
| Coefficient B | -3.30576e+03 | |||
| Coefficient C | -5.51240e+01 | |||
| Reference | Brown, 1952, 2 | |||
| Temperature range, min. | 335.19 | |||
| Temperature range, max. | 404.88 | |||
| Pvap | 9.65 | kPa | 335.19 | Calculated Property |
| Pvap | 13.26 | kPa | 342.93 | Calculated Property |
| Pvap | 17.92 | kPa | 350.68 | Calculated Property |
| Pvap | 23.84 | kPa | 358.42 | Calculated Property |
| Pvap | 31.27 | kPa | 366.16 | Calculated Property |
| Pvap | 40.48 | kPa | 373.91 | Calculated Property |
| Pvap | 51.76 | kPa | 381.65 | Calculated Property |
| Pvap | 65.44 | kPa | 389.39 | Calculated Property |
| Pvap | 81.87 | kPa | 397.14 | Calculated Property |
| Pvap | 101.40 | kPa | 404.88 | Calculated Property |
| Pvap | [9.65; 101.40] | kPa | [335.19; 404.88] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.40707e+01 | |||
| Coefficient B | -3.30576e+03 | |||
| Coefficient C | -5.51240e+01 | |||
| Reference | Brown, 1952 | |||
| Temperature range, min. | 335.19 | |||
| Temperature range, max. | 404.88 | |||
| Pvap | 9.65 | kPa | 335.19 | Calculated Property |
| Pvap | 13.26 | kPa | 342.93 | Calculated Property |
| Pvap | 17.92 | kPa | 350.68 | Calculated Property |
| Pvap | 23.84 | kPa | 358.42 | Calculated Property |
| Pvap | 31.27 | kPa | 366.16 | Calculated Property |
| Pvap | 40.48 | kPa | 373.91 | Calculated Property |
| Pvap | 51.76 | kPa | 381.65 | Calculated Property |
| Pvap | 65.44 | kPa | 389.39 | Calculated Property |
| Pvap | 81.87 | kPa | 397.14 | Calculated Property |
| Pvap | 101.40 | kPa | 404.88 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, chloro-.
Mixtures
- 1,2-Ethanediol + Benzene, chloro-
- Benzene, chloro- + Pentanoic acid + Water
- Benzene, chloro- + 2,2',4,4',6,6'-Hexanitrobiphenyl
- Benzene, chloro- + Methyl Alcohol
- Ethanol + Benzene, chloro-
- Benzene, chloro- + Pentane, 2,2,4-trimethyl-
- Benzene, chloro- + Bis(2-ethylhexyl)hydrogen phosphate
- Benzenamine, 4-methyl-2-nitro- + Benzene, chloro-
- Benzene, chloro- + 1-Hexanol
- Benzene, chloro- + Triethylamine
- Benzene, chloro- + Furan, tetrahydro-2-methyl-
- Benzene + Benzene, chloro- + Cyclohexane
- Formamide, N,N-dimethyl- + Benzene, chloro-
- Benzene, bromo- + Benzene, chloro-
- Benzene, nitro- + Benzene, chloro-
- Benzene, bromo- + Benzene, chloro- + Ethane, 1,2-dichloro-
- Benzene, nitro- + Benzene, chloro- + Ethane, 1,2-dichloro-
- Benzene, chloro- + Benzene, ethyl-
- Benzene, chloro- + Dimethyl Sulfoxide
- Benzene, chloro- + m-Chloroaniline
Find more mixtures with Benzene, chloro-.
Sources
- 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
- Density, Viscosity, Sound Speed, and Thermoacoustical Parameters of Benzaldehyde with Chlorobenzene or Nitrobenzene at 303.15 K, 308.15 K, and 313.15 K
- Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Ethyl-1-hexanol with Benzene and Halobenzenes
- Effect of temperature on the excess molar volumes of some alcohol + aromatic mixtures and modelling by cubic EOS mixing rules
- Solubility of chlorobutane, ethyl methacrylate and trifluoroethyl acrylate in supercritical carbon dioxide
- Isobaric vapour liquid equilibria for binary mixtures of n-heptane with bromobenzene, chlorobenzene and fluorobenzene at atmospheric pressure
- Binary liquid liquid equilibrium in the systems containing monofunctional benzene derivates and 1,2-ethanediol
- Vapor-liquid equilibrium for the binary mixtures of dimethylsulfoxide with substituted benzenes
- Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
- Excess enthalpies of dimethylsulfoxide with substituted benzenes at 298.15K
- Vapor-liquid equilibrium and excess Gibbs energies of some binary mixtures of acrylonitrile at 95.5 kPa
- Activity coefficients and excess Gibbs energy of binary mixtures of N,N-dimethyl formamide with selected compounds at 95.5 kPa
- Ionic liquid structural effects on solute partitioning in biphasic ionic liquid and supercritical carbon dioxide systems
- Bubble point measurements of binary mixtures formed by 1-hexanol with selected nitro-compounds and substituted benzenes at 95.6 kPa
- Solubility of elemental sulfur in pure organic solvents and organic solvent-ionic liquid mixtures from 293.15 to 353.15 K
- Enthalpies and Gibbs free energies of solvation in ethylene glycol at298 K: Influence of the solvophobic effect
- Vaporization enthalpies of a series of the fluoro- and chloro-substituted methylbenzenes
- 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
- Phase equilibrium for ternary liquid systems of water + di-(2- ethylhexyl)phosphoric acid + organic diluents: Thermodynamic study
- Measurement of infinite dilution partition coefficients of isomeric benzene derivatives in [bmim][Tf2N]-CO2 biphasic system and correlation with the ePC-SAFT equation of state
- Optimization of liquid-liquid equilibria of the type 2 ternary systems (water + valeric acid + aromatic solvent): Modeling through SERLAS
- Effect of polarity and temperature on the binary interaction between D2EHPA extractant and organic solvents (kerosene, n-heptane, chlorobenzene and 1-octanol): Experimental and thermodynamics
- Determination and correlation of solubility of 2,2',4,4',6,6 '-hexanitro-1,1'-biphenyl and 2,2',2" ,4,4',4" ,6,6',6" -Nonanitro-1,1 ':3',1"-terphenyl in six pure solvents
- Measurement and modeling of infinite dilution activity coefficients of organic compounds in an equimolar ionic liquid mixture of [Bmim]Cl and [Bmim][Tf2N]
- (Vapor + liquid) equilibria of binary mixtures formed by iso-octane with a variety of compounds at 95.8 kPa
- Phase equilibria for ternary liquid systems of (water + tetrahydrofuran + nonprotic aromatic solvent) at T = 298.2 K
- Azeotropic behaviour of (benzene + cyclohexane + chlorobenzene) ternary mixture using chlorobenzene as entrainer at 101.3 kPa
- Bubble points of the binary mixtures formed by ethylbenzene with some chloroaliphatics and substituted benzenes at p = 94.7 kPa
- Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
- Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
- Thermodynamics of solvation and solvophobic effect in formamide
- Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
- Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
- The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
- Thermodynamics of solvation in propylene glycol and methyl cellosolve
- Phase behavior of ionic liquids 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imides with halogenated benzenes
- Optimization and modeling of extraction equilibria of the type 2 ternary systems containing (water + isovaleric acid + solvent)
- Ultrasonic and 31P NMR investigations of an acidic nuclear extractant with some monosubstituted 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
- Solubility of 4-methyl-2-nitroaniline in fourteen organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
- Improving the method of solution calorimetry for evaluation of the enthalpies of phase transitions and condensed state enthalpies of formation
- Volumetric and refractive properties of 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane with methoxybenzene, chlorobenzene, tert-butylbenzene and nitrobenzene at T = (298.15-318.15) K
- Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
- Thermophysical properties of the binary mixtures of 2-methyl-tetrahydrofuran with benzene and halobenzenes
- Calorimetric study of solvation of low polar solutes in propylene glycol and methyl cellosolve at 298 K
- Effect of halogen substitution on the enthalpies of solvation and hydrogen bonding of organic solutes in chlorobenzene and 1,2-dichlorobenzene derived using multi-parameter correlations
- Standard molar Gibbs free energy and enthalpy of solvation of lowpolar solutes in formamide derivatives at 298 K
- 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
- Enthalpies of solution and enthalpies of solvation of chloro- and nitro-substituted benzenes in 1-butyl-3-methyl imidazolium based ionic liquids at 298.15 K: Additivity of group contributions
- Determination and Correlation of Solubility of 3,4-Dinitro-1H-pyrazole in Different Pure Solvents from 298.15 K to 338.15 K
- Dilute Vapor Absorption: A New Accurate Technique for Measurement of the Limiting Activity Coefficient of Water in Hydrophobic Solvents of Lower Volatility
- The Critical Temperatures of a Number of (i) (Chloroalkane (C3 C4) + Hydrocarbon (C6 C7)) Binary Mixtures and (ii) (Aromatic Halocarbon (Chlorobenzene, Fluorobenzene, 1,2-Dichlorobenzene, or 1,3-Dichlorobenzene) + Alkane (C8)) Binary Mixtures
- Measurement and Correlation of the Solubilities of Sulfur S8 in 10 Solvents
- Isobaric Vapor-Liquid Equilibrium for Binary and Ternary Systems of tert-Butanol + tert-Butyl Acetate + Chlorobenzene at 101.33 kPa
- Solubilities of Organic Semiconductors and Nonsteroidal Anti-inflammatory Drugs in Pure and Mixed Organic Solvents: Measurement and Modeling with Hansen Solubility Parameter
- Liquid-Liquid Equilibria for Mixtures of (Furfural + a Chlorinated Aromatic Compound + an Alkane) at T = 298.15 K
- Vapor-Liquid Equilibria for Four Binary Systems at 363.15 K: N-Methylformamide + Hexane, + Benzene, + Chlorobenzene, and + Acetonitrile
- 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
- Thermodynamics of Ternary Liquid Mixtures Containing Toluene, Ethylbenzene, and Chlorobenzene
- Bubble Temperature Measurements on the Binary Mixtures of n-Heptane or Nitrobenzene or Chlorobenzene with Some Chloroethanes and Chloroethylenes at (94.6 to 95.8) kPa
- Densities, Viscosities, and Thermodynamic Properties of (N,N-Dimethylformamide + Benzene + Chlorobenzene) Ternary Mixtures at (298.15, 303.15, 308.15, and 313.15) K
- Partition Coefficients of Organic Solutes between Supercritical Carbon Dioxide and Water: Experimental Measurements and Empirical Correlations
- Pressure-Density-Temperature Behavior of CO2/Acetone, CO2/Toluene, and CO2/Monochlorobenzene Mixtures in the Near-Critical Region
- Phase Equilibria for the Ternary Liquid Systems of (Water + Tetrahydrofurfuryl Alcohol + Cyclic Solvent) at 298.2 K
- Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
- Solubilities of 2-(2-Hydroxyphenyl)phenylphosphonic Acid in Chlorobenzene and in Water and Partition Coefficient between Water + Chlorobenzene Mixtures
- Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
- Vapor Pressure Measurements for 2-Chloromethylbenzoxazole and Vapor-Liquid Equilibrium Measurements for the Chlorobenzene + 2-Chloromethylbenzoxazole System
- Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Binary Mixtures at 298.15 K
- Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
- 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
- Crystal Structures, Reaction Rates, and Selected Physical Properties of Halo-Boronsubphthalocyanines (Halo = Fluoride, Chloride, and Bromide)
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Solubilities of 4-Amino-4?-nitrodiphenyl Sulfide in Six Organic Solvents from 287.45 K to 365.55 K
- Solubility of Hydrofluorocarbons in Halobenzene Solvents
- Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
- Measurement and Correlation of Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Alkane and Cycloalkane Solvents
- 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
- Excess Enthalpies of Chloroalkylbenzene + Alkylbenzene Mixtures
- Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
- Thermophysical Properties of para-Anisaldehyde (1) + Chlorobenzene (2) at Temperatures of (303.15, 313.15, and 323.15) K and a Pressure of 0.1 MPa
- Solubility of Bis(benzoxazolyl-2-methyl) Sulfide in Different Pure Solvents and Ethanol + Water Binary Mixtures between (273.25 and 325.25) K
- 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
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.
These property values are available through the Cheméo API. A free account gives you an access key.