- 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
- Chlorobenzene, mono-
- Chlorobenzenu
- Chlorobenzol
- Clorobenzene
- IP Carrier T 40
- MCB
- MONOCHLOROBENZENE
- Monochloorbenzeen
- Monochlorbenzene
- Monochlorbenzol
- Monoclorobenzene
- NCI-C54886
- NSC 8433
- PHENYL CHLORIDE
- Tetrosin SP
- UN 1134
- 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.
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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. Sol... | |
| log10WS | -2.38 | Estimat... | |
| 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 | Outlier 877.90 | NIST | |
| Inp | 839.00 | 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 | |
| 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 | 1209.00 | NIST | |
| I | 1257.10 | NIST | |
| I | 1257.00 | NIST | |
| I | 1238.00 | NIST | |
| S°liquid | 197.50 | J/mol×K | NIST |
| Tboil | [402.15; 444.85] | K |
|
| Tboil | 404.87 | K | KDB |
| Tboil | 404.80 | K | Isobari... |
| 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. Sol... |
| 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 ± 0.20 | K | NIST |
| Vc | 0.308 | m3/kmol | KDB |
| Zc | 0.2647650 | KDB | |
| Zra | 0.27 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [126.70; 174.43] | J/mol×K | [400.79; 623.15] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 130 140 150 160 170 400 500 600 | ||||
| Cp,gas | 126.70 | J/mol×K | 400.79 | Joback Calculated Property |
| Cp,gas | 136.13 | J/mol×K | 437.85 | Joback Calculated Property |
| Cp,gas | 144.94 | J/mol×K | 474.91 | Joback Calculated Property |
| Cp,gas | 153.14 | J/mol×K | 511.97 | Joback Calculated Property |
| Cp,gas | 160.77 | J/mol×K | 549.03 | Joback Calculated Property |
| Cp,gas | 167.86 | J/mol×K | 586.09 | Joback Calculated Property |
| Cp,gas | 174.43 | J/mol×K | 623.15 | Joback Calculated Property |
| Cp,liquid | [141.00; 164.34] | J/mol×K | [283.15; 353.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 140 145 150 155 160 165 300 320 340 | ||||
| Cp,liquid | 147.73 | J/mol×K | 283.15 | Heat Ca... |
| Cp,liquid | 148.14 | J/mol×K | 285.15 | Heat Ca... |
| Cp,liquid | 148.56 | J/mol×K | 287.15 | Heat Ca... |
| Cp,liquid | 148.99 | J/mol×K | 289.15 | Heat Ca... |
| Cp,liquid | 149.41 | J/mol×K | 291.15 | Heat Ca... |
| Cp,liquid | 149.85 | J/mol×K | 293.15 | Heat Ca... |
| Cp,liquid | 145.60 | J/mol×K | 293.20 | NIST |
| Cp,liquid | 150.29 | J/mol×K | 295.15 | Heat Ca... |
| Cp,liquid | 150.73 | J/mol×K | 297.15 | Heat Ca... |
| Cp,liquid | 147.70 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 141.00 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 150.08 | J/mol×K | 298.10 | NIST |
| Cp,liquid | 153.78 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 152.10 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 150.79 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 151.18 | J/mol×K | 299.15 | Heat Ca... |
| Cp,liquid | 151.64 | J/mol×K | 301.15 | Heat Ca... |
| Cp,liquid | 150.60 | J/mol×K | 303.15 | NIST |
| Cp,liquid | 152.10 | J/mol×K | 303.15 | Heat Ca... |
| Cp,liquid | 152.56 | J/mol×K | 305.15 | Heat Ca... |
| Cp,liquid | 157.30 | J/mol×K | 305.60 | NIST |
| Cp,liquid | 153.03 | J/mol×K | 307.15 | Heat Ca... |
| Cp,liquid | 153.50 | J/mol×K | 309.15 | Heat Ca... |
| Cp,liquid | 153.97 | J/mol×K | 311.15 | Heat Ca... |
| Cp,liquid | 154.45 | J/mol×K | 313.15 | Heat Ca... |
| Cp,liquid | 154.93 | J/mol×K | 315.15 | Heat Ca... |
| Cp,liquid | 155.41 | J/mol×K | 317.15 | Heat Ca... |
| Cp,liquid | 155.90 | J/mol×K | 319.15 | Heat Ca... |
| Cp,liquid | 156.39 | J/mol×K | 321.15 | Heat Ca... |
| Cp,liquid | 156.88 | J/mol×K | 323.15 | Heat Ca... |
| Cp,liquid | 157.37 | J/mol×K | 325.15 | Heat Ca... |
| Cp,liquid | 157.86 | J/mol×K | 327.15 | Heat Ca... |
| Cp,liquid | 158.36 | J/mol×K | 329.15 | Heat Ca... |
| Cp,liquid | 158.86 | J/mol×K | 331.15 | Heat Ca... |
| Cp,liquid | 159.35 | J/mol×K | 333.15 | Heat Ca... |
| Cp,liquid | 159.85 | J/mol×K | 335.15 | Heat Ca... |
| Cp,liquid | 160.35 | J/mol×K | 337.15 | Heat Ca... |
| Cp,liquid | 160.85 | J/mol×K | 339.15 | Heat Ca... |
| Cp,liquid | 161.35 | J/mol×K | 341.15 | Heat Ca... |
| Cp,liquid | 161.85 | J/mol×K | 343.15 | Heat Ca... |
| Cp,liquid | 162.35 | J/mol×K | 345.15 | Heat Ca... |
| Cp,liquid | 162.85 | J/mol×K | 347.15 | Heat Ca... |
| Cp,liquid | 163.34 | J/mol×K | 349.15 | Heat Ca... |
| Cp,liquid | 163.84 | J/mol×K | 351.15 | Heat Ca... |
| Cp,liquid | 164.34 | J/mol×K | 353.15 | Heat Ca... |
| Cp,solid | 106.30 | J/mol×K | 216.80 | NIST |
| η | [0.0004658; 0.0008432] | Pa×s | [293.00; 343.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 5.00e-4 6.00e-4 7.00e-4 8.00e-4 300 320 340 | ||||
| η | 0.0008432 | Pa×s | 293.00 | Thermop... |
| η | 0.0008084 | Pa×s | 293.15 | Excess ... |
| η | 0.0007568 | Pa×s | 298.15 | Thermop... |
| η | 0.0007422 | Pa×s | 298.15 | Excess ... |
| η | 0.0007560 | Pa×s | 298.15 | Densiti... |
| η | 0.0007550 | Pa×s | 298.15 | Thermop... |
| η | 0.0007570 | Pa×s | 298.15 | Acousti... |
| η | 0.0007210 | Pa×s | 303.00 | Thermop... |
| η | 0.0007053 | Pa×s | 303.15 | Excess ... |
| η | 0.0007140 | Pa×s | 303.15 | Densiti... |
| η | 0.0007258 | Pa×s | 303.15 | Thermop... |
| η | 0.0007140 | Pa×s | 303.15 | Acousti... |
| η | 0.0006730 | Pa×s | 308.15 | Densiti... |
| η | 0.0006770 | Pa×s | 308.15 | Thermop... |
| η | 0.0006790 | Pa×s | 308.15 | Thermop... |
| η | 0.0006770 | Pa×s | 308.15 | Acousti... |
| η | 0.0006247 | Pa×s | 313.00 | Thermop... |
| η | 0.0006310 | Pa×s | 313.15 | Excess ... |
| η | 0.0006350 | Pa×s | 313.15 | Densiti... |
| η | 0.0006170 | Pa×s | 313.15 | Acousti... |
| η | 0.0006240 | Pa×s | 313.15 | Thermop... |
| η | 0.0005677 | Pa×s | 323.15 | Excess ... |
| η | 0.0005069 | Pa×s | 333.15 | Excess ... |
| η | 0.0004658 | Pa×s | 343.15 | Excess ... |
| ΔfusH | [9.55; 9.56] | kJ/mol | [227.89; 227.90] |
|
| ΔfusH | 9.56 | kJ/mol | 227.89 | NIST |
| ΔfusH | 9.55 | kJ/mol | 227.90 | NIST |
| ΔfusH | 9.55 | kJ/mol | 227.90 | NIST |
| ΔvapH | [35.19; 48.10] | kJ/mol | [278.00; 501.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 34 36 38 40 42 44 46 48 300 400 500 | ||||
| ΔvapH | 37.30 | kJ/mol | 278.00 | NIST |
| ΔvapH | 48.10 | kJ/mol | 285.50 | NIST |
| ΔvapH | 38.80 | kJ/mol | 369.00 | NIST |
| ΔvapH | 35.19 | kJ/mol | 404.90 | NIST |
| ΔvapH | 36.55 | kJ/mol | 405.10 | KDB |
| ΔvapH | 35.40 | kJ/mol | 501.00 | NIST |
| Pvap | [0.37; 101.33] | kPa | [274.50; 404.80] |
|
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 300 350 400 | ||||
| Pvap | 0.37 | kPa | 274.50 | Vaporiz... |
| Pvap | 0.44 | kPa | 277.30 | Vaporiz... |
| Pvap | 0.53 | kPa | 280.30 | Vaporiz... |
| Pvap | 0.65 | kPa | 283.30 | Vaporiz... |
| Pvap | 0.79 | kPa | 286.30 | Vaporiz... |
| Pvap | 0.95 | kPa | 289.30 | Vaporiz... |
| Pvap | 1.12 | kPa | 292.20 | Vaporiz... |
| Pvap | 1.30 | kPa | 295.20 | Vaporiz... |
| Pvap | 1.54 | kPa | 298.20 | Vaporiz... |
| Pvap | 1.87 | kPa | 301.20 | Vaporiz... |
| Pvap | 2.17 | kPa | 304.20 | Vaporiz... |
| Pvap | 2.61 | kPa | 307.20 | Vaporiz... |
| Pvap | 7.92 | kPa | 330.50 | Vapor P... |
| Pvap | 10.59 | kPa | 337.40 | Vapor P... |
| Pvap | 28.33 | kPa | 363.15 | Vapor-L... |
| Pvap | 95.30 | kPa | 402.35 | Vapor-l... |
| Pvap | 95.50 | kPa | 402.85 | Vapor-l... |
| Pvap | 101.33 | kPa | 404.80 | Isobari... |
| n0 | [1.51072; 1.52480] | [293.15; 318.15] |
|
|
|
T(K) Refractive Index 1.51 1.52 1.52 1.53 300 310 | ||||
| n0 | 1.52480 | 293.15 | Bubble ... | |
| n0 | 1.52440 | 293.20 | Phase E... | |
| n0 | 1.52180 | 298.15 | Liquid-... | |
| n0 | 1.52230 | 298.15 | Density... | |
| n0 | 1.52190 | 298.15 | (Vapor ... | |
| n0 | 1.52176 | 298.15 | Azeotro... | |
| n0 | 1.52180 | 298.15 | Bubble ... | |
| n0 | 1.52168 | 298.15 | Volumet... | |
| n0 | 1.52180 | 298.15 | Activit... | |
| n0 | 1.52176 | 298.15 | Thermop... | |
| n0 | 1.51950 | 303.15 | Density... | |
| n0 | 1.51893 | 303.15 | Volumet... | |
| n0 | 1.51600 | 303.15 | Refract... | |
| n0 | 1.51910 | 303.15 | Excess ... | |
| n0 | 1.51629 | 308.15 | Volumet... | |
| n0 | 1.51660 | 308.15 | Density... | |
| n0 | 1.51500 | 308.15 | Refract... | |
| n0 | 1.51430 | 313.15 | Refract... | |
| n0 | 1.51348 | 313.15 | Volumet... | |
| n0 | 1.51072 | 318.15 | Volumet... | |
| ρl | [1062.80; 1117.29] | kg/m3 | [283.15; 333.15] |
|
|
T(K) Liquid Density (kg/m3) 1060 1070 1080 1090 1100 1110 1120 300 320 | ||||
| ρl | 1117.29 | kg/m3 | 283.15 | The den... |
| ρl | 1111.81 | kg/m3 | 288.15 | Effect ... |
| ρl | 1111.81 | kg/m3 | 288.15 | Influen... |
| ρl | 1111.89 | kg/m3 | 288.15 | The den... |
| ρl | 1106.00 | kg/m3 | 293.00 | KDB |
| ρl | 1106.49 | kg/m3 | 293.15 | Theoret... |
| ρl | 1106.43 | kg/m3 | 293.15 | Influen... |
| ρl | 1106.43 | kg/m3 | 293.15 | Effect ... |
| ρl | 1106.55 | kg/m3 | 293.15 | The den... |
| ρl | 1106.00 | kg/m3 | 293.15 | Bubble ... |
| ρl | 1106.07 | kg/m3 | 293.20 | Isobari... |
| ρl | 1101.08 | kg/m3 | 298.00 | Optimiz... |
| ρl | 1101.16 | kg/m3 | 298.15 | The den... |
| ρl | 1100.80 | kg/m3 | 298.15 | Thermod... |
| ρl | 1100.90 | kg/m3 | 298.15 | Binary ... |
| ρl | 1101.04 | kg/m3 | 298.15 | Effect ... |
| ρl | 1101.17 | kg/m3 | 298.15 | Excess ... |
| ρl | 1101.04 | kg/m3 | 298.15 | Influen... |
| ρl | 1101.03 | kg/m3 | 298.15 | Densiti... |
| ρl | 1101.08 | kg/m3 | 298.20 | Optimiz... |
| ρl | 1095.79 | kg/m3 | 303.15 | The den... |
| ρl | 1095.54 | kg/m3 | 303.15 | Studies... |
| ρl | 1095.64 | kg/m3 | 303.15 | Effect ... |
| ρl | 1095.64 | kg/m3 | 303.15 | Influen... |
| ρl | 1095.49 | kg/m3 | 303.15 | Studies... |
| ρl | 1095.70 | kg/m3 | 303.15 | Effect ... |
| ρl | 1086.60 | kg/m3 | 303.15 | Density... |
| ρl | 1095.52 | kg/m3 | 303.15 | Densiti... |
| ρl | 1095.71 | kg/m3 | 303.15 | Theoret... |
| ρl | 1090.23 | kg/m3 | 308.15 | Effect ... |
| ρl | 1085.10 | kg/m3 | 308.15 | Density... |
| ρl | 1089.72 | kg/m3 | 308.15 | Studies... |
| ρl | 1090.20 | kg/m3 | 308.15 | Densiti... |
| ρl | 1090.23 | kg/m3 | 308.15 | Influen... |
| ρl | 1084.82 | kg/m3 | 313.15 | Influen... |
| ρl | 1084.82 | kg/m3 | 313.15 | Effect ... |
| ρl | 1084.80 | kg/m3 | 313.15 | Effect ... |
| ρl | 1081.10 | kg/m3 | 313.15 | Density... |
| ρl | 1084.71 | kg/m3 | 313.15 | Studies... |
| ρl | 1084.86 | kg/m3 | 313.15 | Theoret... |
| ρl | 1079.42 | kg/m3 | 318.15 | Influen... |
| ρl | 1079.45 | kg/m3 | 318.15 | Studies... |
| ρl | 1073.96 | kg/m3 | 323.15 | Theoret... |
| ρl | 1073.97 | kg/m3 | 323.15 | Influen... |
| ρl | 1073.80 | kg/m3 | 323.15 | Effect ... |
| ρl | 1063.01 | kg/m3 | 333.15 | Theoret... |
| ρl | 1062.80 | kg/m3 | 333.15 | Effect ... |
| ΔfusS | 41.93 | J/mol×K | 227.89 | NIST |
| γ | [0.03; 0.03] | N/m | [293.20; 323.15] |
|
| γ | 0.03 | N/m | 293.20 | KDB |
| γ | 0.03 | N/m | 303.15 | Thermop... |
| γ | 0.03 | N/m | 313.15 | Thermop... |
| γ | 0.03 | N/m | 323.15 | Thermop... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | 404.35 | K | 95.30 | Excess ... |
| Tfus | [246.40; 530.87] | K | [100000.00; 3500000.00] |
|
|
P(kPa) Melting point (K) 250 300 350 400 450 500 550 1000000 2000000 3000000 | ||||
| Tfus | 246.40 | K | 100000.00 | Fusion ... |
| Tfus | 263.03 | K | 200000.00 | Fusion ... |
| Tfus | 273.46 | K | 300000.00 | Fusion ... |
| Tfus | 288.44 | K | 400000.00 | Fusion ... |
| Tfus | 301.03 | K | 500000.00 | Fusion ... |
| Tfus | 315.62 | K | 600000.00 | Fusion ... |
| Tfus | 325.56 | K | 700000.00 | Fusion ... |
| Tfus | 336.87 | K | 800000.00 | Fusion ... |
| Tfus | 348.81 | K | 900000.00 | Fusion ... |
| Tfus | 354.76 | K | 1000000.00 | Fusion ... |
| Tfus | 403.44 | K | 1500000.00 | Fusion ... |
| Tfus | 440.81 | K | 2000000.00 | Fusion ... |
| Tfus | 473.28 | K | 2500000.00 | Fusion ... |
| Tfus | 503.63 | K | 3000000.00 | Fusion ... |
| Tfus | 530.87 | K | 3500000.00 | Fusion ... |
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 |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [293.56; 432.78] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
| 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 Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 5.24220e+01 | |||
| Coefficient B | -6.32735e+03 | |||
| Coefficient C | -5.42919e+00 | |||
| Coefficient D | 2.47507e-06 | |||
| Temperature range, min. | 227.95 | |||
| Temperature range, max. | 632.35 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 300 400 500 600 | ||||
| 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 |
Similar Compounds
Find more compounds similar to Benzene, chloro-.
Mixtures
- Benzene, chloro- + Triethylene glycol
- Benzene, chloro- + Methyl Alcohol
- Benzene, chloro- + Benzaldehyde
- Benzene, chloro- + 1-Hexanol, 2-ethyl-
- Ethanol + Benzene, chloro-
- Benzene, chloro- + Heptane
- 1,2-Ethanediol + Benzene, chloro-
- Benzene, chloro- + Dimethyl Sulfoxide
- 1-Propanol + Benzene, chloro-
- Benzene, chloro- + 1-Butanol
- Benzene, chloro- + 1-Pentanol
- 2-Propanol, 2-methyl- + Benzene, chloro-
- 2-Propenenitrile + Benzene, chloro-
- Formamide, N,N-dimethyl- + Benzene, chloro-
- Benzene, chloro- + 1-Hexanol
- Benzene, chloro- + N-Formylmorpholine
- Benzene, chloro- + Pentanoic acid + Water
- Benzene, chloro- + Pentane, 2,2,4-trimethyl-
- Benzene + Benzene, chloro- + Cyclohexane
- Benzene, chloro- + Ethylbenzene
Find more mixtures with Benzene, chloro-.
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
- 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
- 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
- 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
- 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
- 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
- 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
- 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
- Determination and Correlation of Solubility of 3,4-Dinitro-1H-pyrazole in Different Pure Solvents from 298.15 K to 338.15 K
- 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
- 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
- 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
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Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.