- InChI
- InChI=1S/C6H4Cl2/c7-5-1-2-6(8)4-3-5/h1-4H
- InChI Key
- OCJBOOLMMGQPQU-UHFFFAOYSA-N
- Formula
- C6H4Cl2
- SMILES
- Clc1ccc(Cl)cc1
- Molecular Weight1
- 147.00
- CAS
- 106-46-7
- Other Names
-
- 1,4-Dichloorbenzeen
- 1,4-Dichlor-benzol
- 1,4-Diclorobenzene
- 1,4-chlorobenzene
- 1,4-dichlorobenzene
- Benzene, p-dichloro-
- Di-chloricide
- Dichlorobenzene
- Dichlorobenzene, p-
- Dichlorobenzene, para
- Dichlorocide
- Evola
- Globol
- Kaydox
- NCI-C54955
- NSC 36935
- PDB
- Paracide
- Paradi
- Paradichlorbenzol
- Paradichlorobenzol
- Paradow
- Paramoth
- Paranuggets
- Parazene
- Persia-Perazol
- Rcra waste number U070
- Rcra waste number U071
- Rcra waste number U072
- Santochlor
- UN 1592
- p-Chlorophenyl chloride
- p-Dichloorbenzeen
- p-Dichlorbenzene
- p-Dichlorbenzol
- p-Dichlorobenzol
- p-Diclorobenzene
- p-dichlorobenzene
- para crystals
- para-Dichlorobenzene
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- ΔcH°solid : Standard solid 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).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°(+) ion : Enthalpy of formation of positive ion at standard conditions (kJ/mol).
- ΔfH(+) ion,0K : Enthalpy of formation of positive ion at 0K (kJ/mol).
- ΔfH°solid : Solid 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).
- ΔsubH° : Enthalpy of sublimation at standard conditions (kJ/mol).
- ΔsubH : Enthalpy of sublimation 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).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- γ : Surface Tension (N/m).
- S°solid,1 bar : Solid phase molar entropy at standard conditions (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- 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 | [0.2700; 0.2846] |
|
|
| ω | 0.2700 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.2846 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°liquid | -2937.00 ± 4.00 | kJ/mol | NIST |
| ΔcH°solid | [-2939.90; -2934.10] | kJ/mol |
|
| ΔcH°solid | -2939.90 | kJ/mol | NIST |
| ΔcH°solid | -2934.10 ± 1.00 | kJ/mol | NIST |
| μ | 0.00 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | 76.70 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | [22.50; 24.60] | kJ/mol |
|
| ΔfH°gas | 22.50 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | 24.60 | kJ/mol | NIST |
| ΔfH°(+) ion | 883.20 | kJ/mol | NIST |
| ΔfH(+) ion,0K | 895.80 | kJ/mol | NIST |
| ΔfH°solid | -42.30 ± 1.00 | kJ/mol | NIST |
| ΔfusH° | 17.91 | kJ/mol | Low-Temperature Heat Capacities and Derived Thermodynamic Functions of 1,4 Dichlorobenzene, 1,4 Dibromobenzene, 1,3,5 Trichlorobenzene, and 1,3,5 Tribromobenzene |
| ΔsubH° | [64.75; 65.20] | kJ/mol |
|
| ΔsubH° | 64.75 ± 0.15 | kJ/mol | NIST |
| ΔsubH° | 65.20 ± 2.00 | kJ/mol | NIST |
| ΔvapH° | [47.80; 54.80] | kJ/mol |
|
| ΔvapH° | 54.80 | kJ/mol | NIST |
| ΔvapH° | 47.80 | kJ/mol | NIST |
| IE | [8.89; 9.00] | eV |
|
| IE | 8.92 ± 0.03 | eV | NIST |
| IE | 8.95 | eV | NIST |
| IE | 8.92 ± 0.02 | eV | NIST |
| IE | 8.97 ± 0.03 | eV | NIST |
| IE | 8.94 | eV | NIST |
| IE | 8.98 ± 0.02 | eV | NIST |
| IE | 8.89 ± 0.01 | eV | NIST |
| IE | 8.94 ± 0.01 | eV | NIST |
| IE | 8.95 | eV | NIST |
| IE | 8.99 | eV | NIST |
| IE | 9.00 | eV | NIST |
| log10WS | [-3.29; -3.27] |
|
|
| log10WS | -3.29 | Aq. Solubility Prediction | |
| log10WS | -3.27 | Estimated Solubility | |
| logPoct/wat | 2.993 | Crippen Calculated Property | |
| McVol | 96.120 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | [3951.68; 4070.00] | kPa |
|
| Pc | 3951.68 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 4070.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 1.23 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [162.00; 1057.00] |
|
|
| Inp | 1023.15 | NIST | |
| Inp | 1023.18 | NIST | |
| Inp | 1032.51 | NIST | |
| Inp | 1032.76 | NIST | |
| Inp | 1016.00 | NIST | |
| Inp | 1037.40 | NIST | |
| Inp | 1037.40 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1012.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 1016.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 1015.00 | NIST | |
| Inp | 1016.00 | NIST | |
| Inp | 1016.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 1021.24 | NIST | |
| Inp | 1021.56 | NIST | |
| Inp | 1024.00 | NIST | |
| Inp | 1025.03 | NIST | |
| Inp | 1014.90 | NIST | |
| Inp | 991.21 | NIST | |
| Inp | 990.60 | NIST | |
| Inp | 989.50 | NIST | |
| Inp | 1014.00 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 996.00 | NIST | |
| Inp | 991.00 | NIST | |
| Inp | 987.00 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 1024.00 | NIST | |
| Inp | 1010.00 | NIST | |
| Inp | 998.00 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 1004.00 | NIST | |
| Inp | 1004.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 1008.00 | NIST | |
| Inp | 1015.00 | NIST | |
| Inp | 1024.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1014.00 | NIST | |
| Inp | 1016.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 989.00 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 1050.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 988.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 987.00 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 988.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 1023.00 | NIST | |
| Inp | Outlier 163.00 | NIST | |
| Inp | Outlier 162.00 | NIST | |
| Inp | Outlier 163.15 | NIST | |
| Inp | Outlier 164.81 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 974.00 | NIST | |
| Ip | [1420.00; 1495.00] |
|
|
| Ip | 1483.20 | NIST | |
| Ip | 1438.00 | NIST | |
| Ip | 1438.00 | NIST | |
| Ip | 1471.00 | NIST | |
| Ip | 1438.00 | NIST | |
| Ip | 1449.00 | NIST | |
| Ip | 1449.00 | NIST | |
| Ip | 1450.00 | NIST | |
| Ip | 1446.09 | NIST | |
| Ip | 1450.00 | NIST | |
| Ip | 1446.00 | NIST | |
| Ip | 1453.00 | NIST | |
| Ip | 1420.00 | NIST | |
| Ip | 1434.00 | NIST | |
| Ip | 1436.00 | NIST | |
| Ip | 1436.00 | NIST | |
| Ip | Outlier 1495.00 | NIST | |
| Ip | 1420.00 | NIST | |
| S°solid,1 bar | 175.41 | J/mol×K | NIST |
| Tboil | [446.85; 447.75] | K |
|
| Tboil | 447.21 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 446.85 | K | KDB |
| Tboil | 447.20 | K | NIST |
| Tboil | 447.27 ± 0.07 | K | NIST |
| Tboil | 447.60 ± 0.50 | K | NIST |
| Tboil | 447.75 ± 0.30 | K | NIST |
| Tboil | 447.30 ± 0.50 | K | NIST |
| Tboil | 446.85 ± 0.70 | K | NIST |
| Tc | [684.75; 685.00] | K |
|
| Tc | 685.00 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 684.75 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [325.00; 327.15] | K |
|
| Tfus | 326.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 326.14 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 326.35 | K | KDB |
| Tfus | 326.41 | K | Aq. Solubility Prediction |
| Tfus | 326.56 ± 0.20 | K | NIST |
| Tfus | 326.70 ± 0.20 | K | NIST |
| Tfus | 326.70 ± 0.30 | K | NIST |
| Tfus | 326.15 ± 0.20 | K | NIST |
| Tfus | 325.90 ± 0.10 | K | NIST |
| Tfus | 326.00 ± 1.00 | K | NIST |
| Tfus | 326.28 ± 0.05 | K | NIST |
| Tfus | 326.14 ± 0.05 | K | NIST |
| Tfus | 326.15 ± 1.00 | K | NIST |
| Tfus | 326.00 ± 3.00 | K | NIST |
| Tfus | 326.00 ± 1.00 | K | NIST |
| Tfus | 326.00 ± 2.00 | K | NIST |
| Tfus | 326.14 ± 0.05 | K | NIST |
| Tfus | 326.00 ± 0.50 | K | NIST |
| Tfus | 326.30 ± 0.20 | K | NIST |
| Tfus | 326.00 ± 1.50 | K | NIST |
| Tfus | 326.35 ± 0.30 | K | NIST |
| Tfus | 325.99 ± 0.05 | K | NIST |
| Tfus | Outlier 327.15 ± 1.00 | K | NIST |
| Tfus | 326.10 ± 0.50 | K | NIST |
| Tfus | Outlier 325.25 ± 0.35 | K | NIST |
| Tfus | 326.25 ± 1.50 | K | NIST |
| Tfus | 326.15 ± 1.00 | K | NIST |
| Tfus | Outlier 325.00 ± 2.00 | K | NIST |
| Tfus | 326.35 ± 0.50 | K | NIST |
| Tfus | 325.65 ± 0.50 | K | NIST |
| Ttriple | [326.14; 326.16] | K |
|
| Ttriple | 326.14 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 326.16 | K | KDB |
| Ttriple | 326.15 ± 0.01 | K | NIST |
| Ttriple | 326.15 ± 0.01 | K | NIST |
| UQi | 3.29 | ChemSep v8.3 pure component data Compiled value | |
| URi | 4.44 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.351; 0.372] | m3/kmol |
|
| Vc | 0.372 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.351 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2510000 | ChemSep v8.3 pure component data Compiled value | |
| Zra | 0.26 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [177.09; 183.21] | J/mol×K | [327.15; 353.15] |
|
| Cp,liquid | 177.09 | J/mol×K | 327.15 | Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes |
| Cp,liquid | 177.53 | J/mol×K | 329.15 | Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes |
| Cp,liquid | 177.98 | J/mol×K | 331.15 | Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes |
| Cp,liquid | 178.43 | J/mol×K | 333.15 | Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes |
| Cp,liquid | 178.89 | J/mol×K | 335.15 | Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes |
| Cp,liquid | 179.35 | J/mol×K | 337.15 | Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes |
| Cp,liquid | 179.81 | J/mol×K | 339.15 | Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes |
| Cp,liquid | 180.28 | J/mol×K | 341.15 | Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes |
| Cp,liquid | 180.76 | J/mol×K | 343.15 | Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes |
| Cp,liquid | 181.24 | J/mol×K | 345.15 | Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes |
| Cp,liquid | 181.73 | J/mol×K | 347.15 | Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes |
| Cp,liquid | 182.22 | J/mol×K | 349.15 | Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes |
| Cp,liquid | 182.71 | J/mol×K | 351.15 | Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes |
| Cp,liquid | 183.21 | J/mol×K | 353.15 | Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes |
| Cp,solid | [98.00; 172.00] | J/mol×K | [180.00; 299.80] |
|
| Cp,solid | 98.00 | J/mol×K | 180.00 | NIST |
| Cp,solid | 147.60 | J/mol×K | 298.00 | NIST |
| Cp,solid | 147.76 | J/mol×K | 298.15 | NIST |
| Cp,solid | 142.70 | J/mol×K | 298.15 | NIST |
| Cp,solid | 172.00 | J/mol×K | 299.80 | NIST |
| ΔfusH | [17.91; 18.19] | kJ/mol | [192.50; 326.20] |
|
| ΔfusH | 17.91 | kJ/mol | 192.50 | NIST |
| ΔfusH | 18.16 | kJ/mol | 326.00 | NIST |
| ΔfusH | 18.16 | kJ/mol | 326.00 | NIST |
| ΔfusH | 18.16 | kJ/mol | 326.00 | NIST |
| ΔfusH | 18.14 | kJ/mol | 326.05 | NIST |
| ΔfusH | 18.05 | kJ/mol | 326.15 | NIST |
| ΔfusH | 18.19 | kJ/mol | 326.20 | NIST |
| ΔsubH | [53.10; 65.40] | kJ/mol | [275.50; 363.00] |
|
| ΔsubH | 56.90 | kJ/mol | 275.50 | NIST |
| ΔsubH | 53.10 | kJ/mol | 285.50 | NIST |
| ΔsubH | 64.80 ± 0.80 | kJ/mol | 302.00 | NIST |
| ΔsubH | 64.80 ± 0.40 | kJ/mol | 303.00 | NIST |
| ΔsubH | 63.00 ± 0.40 | kJ/mol | 318.00 | NIST |
| ΔsubH | 65.40 | kJ/mol | 363.00 | NIST |
| ΔvapH | [44.20; 46.40] | kJ/mol | [326.00; 403.00] |
|
| ΔvapH | 46.40 | kJ/mol | 326.00 | NIST |
| ΔvapH | 45.00 | kJ/mol | 394.50 | NIST |
| ΔvapH | 44.20 | kJ/mol | 403.00 | NIST |
| ΔfusS | [55.30; 55.70] | J/mol×K | [326.00; 326.15] |
|
| ΔfusS | 55.70 | J/mol×K | 326.00 | NIST |
| ΔfusS | 55.60 | J/mol×K | 326.05 | NIST |
| ΔfusS | 55.30 | J/mol×K | 326.15 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [82.00; 251.89] | J/mol×K | [200.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 5.56950e+01 | |||
| Coefficient B | -4.89460e+02 | |||
| Coefficient C | 5.74124e+00 | |||
| Coefficient D | -1.25240e-04 | |||
| Coefficient E | 2.31150e-08 | |||
| Temperature range, min. | 200.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 82.00 | J/mol×K | 200.00 | Calculated Property |
| Cp,gas | 127.92 | J/mol×K | 344.44 | Calculated Property |
| Cp,gas | 163.94 | J/mol×K | 488.89 | Calculated Property |
| Cp,gas | 189.77 | J/mol×K | 633.33 | Calculated Property |
| Cp,gas | 208.40 | J/mol×K | 777.78 | Calculated Property |
| Cp,gas | 222.14 | J/mol×K | 922.22 | Calculated Property |
| Cp,gas | 232.51 | J/mol×K | 1066.67 | Calculated Property |
| Cp,gas | 240.51 | J/mol×K | 1211.11 | Calculated Property |
| Cp,gas | 246.81 | J/mol×K | 1355.56 | Calculated Property |
| Cp,gas | 251.89 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [178.56; 250.36] | J/mol×K | [326.14; 513.56] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 1.55200e+02 | |||
| Coefficient B | 8.55070e+02 | |||
| Coefficient C | -6.02191e+00 | |||
| Coefficient D | 2.48430e-02 | |||
| Coefficient E | -1.45820e-05 | |||
| Temperature range, min. | 326.14 | |||
| Temperature range, max. | 513.56 | |||
| Cp,liquid | 178.56 | J/mol×K | 326.14 | Calculated Property |
| Cp,liquid | 182.50 | J/mol×K | 346.96 | Calculated Property |
| Cp,liquid | 187.26 | J/mol×K | 367.79 | Calculated Property |
| Cp,liquid | 192.93 | J/mol×K | 388.61 | Calculated Property |
| Cp,liquid | 199.62 | J/mol×K | 409.44 | Calculated Property |
| Cp,liquid | 207.39 | J/mol×K | 430.26 | Calculated Property |
| Cp,liquid | 216.32 | J/mol×K | 451.09 | Calculated Property |
| Cp,liquid | 226.46 | J/mol×K | 471.91 | Calculated Property |
| Cp,liquid | 237.81 | J/mol×K | 492.74 | Calculated Property |
| Cp,liquid | 250.36 | J/mol×K | 513.56 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0008580; 0.0003017] | Pa×s | [326.14; 447.21] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.31860e+02 | |||
| Coefficient B | 5.31280e+03 | |||
| Coefficient C | 1.92840e+01 | |||
| Coefficient D | -2.90850e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 326.14 | |||
| Temperature range, max. | 447.21 | |||
| η | 0.0008580 | Pa×s | 326.14 | Calculated Property |
| η | 0.0007561 | Pa×s | 339.59 | Calculated Property |
| η | 0.0006720 | Pa×s | 353.04 | Calculated Property |
| η | 0.0006004 | Pa×s | 366.50 | Calculated Property |
| η | 0.0005377 | Pa×s | 379.95 | Calculated Property |
| η | 0.0004818 | Pa×s | 393.40 | Calculated Property |
| η | 0.0004311 | Pa×s | 406.85 | Calculated Property |
| η | 0.0003845 | Pa×s | 420.31 | Calculated Property |
| η | 0.0003415 | Pa×s | 433.76 | Calculated Property |
| η | 0.0003017 | Pa×s | 447.21 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [48.32; 0.00] | kJ/mol | [298.15; 684.75] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 6.11263e+01 | |||
| Coefficient B | 4.26201e-01 | |||
| Coefficient C | -3.66365e-02 | |||
| Coefficient D | 8.11781e-03 | |||
| Coefficient E | -7.54654e-03 | |||
| Critical temperature, Tc (K) | 6.84750e+02 | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 684.75 | |||
| ΔvapH | 48.32 | kJ/mol | 298.15 | Calculated Property |
| ΔvapH | 46.11 | kJ/mol | 341.11 | Calculated Property |
| ΔvapH | 43.73 | kJ/mol | 384.06 | Calculated Property |
| ΔvapH | 41.16 | kJ/mol | 427.02 | Calculated Property |
| ΔvapH | 38.33 | kJ/mol | 469.97 | Calculated Property |
| ΔvapH | 35.15 | kJ/mol | 512.93 | Calculated Property |
| ΔvapH | 31.45 | kJ/mol | 555.88 | Calculated Property |
| ΔvapH | 26.91 | kJ/mol | 598.84 | Calculated Property |
| ΔvapH | 20.60 | kJ/mol | 641.79 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 684.75 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [323.57; 477.69] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.47073e+01 | |||
| Coefficient B | -4.15642e+03 | |||
| Coefficient C | -3.53240e+01 | |||
| Temperature range, min. | 323.57 | |||
| Temperature range, max. | 477.69 | |||
| Pvap | 1.33 | kPa | 323.57 | Calculated Property |
| Pvap | 2.99 | kPa | 340.69 | Calculated Property |
| Pvap | 6.17 | kPa | 357.82 | Calculated Property |
| Pvap | 11.81 | kPa | 374.94 | Calculated Property |
| Pvap | 21.25 | kPa | 392.07 | Calculated Property |
| Pvap | 36.23 | kPa | 409.19 | Calculated Property |
| Pvap | 58.96 | kPa | 426.32 | Calculated Property |
| Pvap | 92.11 | kPa | 443.44 | Calculated Property |
| Pvap | 138.80 | kPa | 460.57 | Calculated Property |
| Pvap | 202.64 | kPa | 477.69 | Calculated Property |
| Pvap | [0.24; 2309.81] | kPa | [298.15; 684.75] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 3.37291e+01 | |||
| Coefficient B | -6.60772e+03 | |||
| Coefficient C | -2.22118e+00 | |||
| Coefficient D | -3.90747e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 684.75 | |||
| Pvap | 0.24 | kPa | 298.15 | Calculated Property |
| Pvap | 2.58 | kPa | 341.11 | Calculated Property |
| Pvap | 15.33 | kPa | 384.06 | Calculated Property |
| Pvap | 59.69 | kPa | 427.02 | Calculated Property |
| Pvap | 170.72 | kPa | 469.97 | Calculated Property |
| Pvap | 386.93 | kPa | 512.93 | Calculated Property |
| Pvap | 731.93 | kPa | 555.88 | Calculated Property |
| Pvap | 1198.95 | kPa | 598.84 | Calculated Property |
| Pvap | 1746.93 | kPa | 641.79 | Calculated Property |
| Pvap | 2309.81 | kPa | 684.75 | Calculated Property |
| Pvap | [1.25; 4077.90] | kPa | [326.14; 684.75] |
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 | 8.13197e+01 | |||
| Coefficient B | -8.43460e+03 | |||
| Coefficient C | -9.63023e+00 | |||
| Coefficient D | 4.66574e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 326.14 | |||
| Temperature range, max. | 684.75 | |||
| Pvap | 1.25 | kPa | 326.14 | Calculated Property |
| Pvap | 7.81 | kPa | 365.99 | Calculated Property |
| Pvap | 32.01 | kPa | 405.83 | Calculated Property |
| Pvap | 97.57 | kPa | 445.68 | Calculated Property |
| Pvap | 240.38 | kPa | 485.52 | Calculated Property |
| Pvap | 506.82 | kPa | 525.37 | Calculated Property |
| Pvap | 952.11 | kPa | 565.21 | Calculated Property |
| Pvap | 1640.81 | kPa | 605.06 | Calculated Property |
| Pvap | 2650.32 | kPa | 644.90 | Calculated Property |
| Pvap | 4077.90 | kPa | 684.75 | Calculated Property |
| Pvap | [2.67; 101.36] | kPa | [341.12; 447.21] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.40987e+01 | |||
| Coefficient B | -3.62682e+03 | |||
| Coefficient C | -6.46370e+01 | |||
| Reference | McDonald, Shrader, et al., 1959 | |||
| Temperature range, min. | 341.12 | |||
| Temperature range, max. | 447.21 | |||
| Pvap | 2.67 | kPa | 341.12 | Calculated Property |
| Pvap | 4.56 | kPa | 352.91 | Calculated Property |
| Pvap | 7.48 | kPa | 364.70 | Calculated Property |
| Pvap | 11.81 | kPa | 376.48 | Calculated Property |
| Pvap | 18.03 | kPa | 388.27 | Calculated Property |
| Pvap | 26.74 | kPa | 400.06 | Calculated Property |
| Pvap | 38.59 | kPa | 411.85 | Calculated Property |
| Pvap | 54.38 | kPa | 423.63 | Calculated Property |
| Pvap | 74.98 | kPa | 435.42 | Calculated Property |
| Pvap | 101.36 | kPa | 447.21 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1252.33; 418.89] | kg/m3 | [326.14; 684.75] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 1.10047e+02 | |||
| Coefficient B | 2.62710e-01 | |||
| Coefficient C | 6.84750e+02 | |||
| Coefficient D | 3.08150e-01 | |||
| Temperature range, min. | 326.14 | |||
| Temperature range, max. | 684.75 | |||
| ρl | 1252.33 | kg/m3 | 326.14 | Calculated Property |
| ρl | 1204.39 | kg/m3 | 365.99 | Calculated Property |
| ρl | 1154.19 | kg/m3 | 405.83 | Calculated Property |
| ρl | 1101.17 | kg/m3 | 445.68 | Calculated Property |
| ρl | 1044.54 | kg/m3 | 485.52 | Calculated Property |
| ρl | 983.00 | kg/m3 | 525.37 | Calculated Property |
| ρl | 914.38 | kg/m3 | 565.21 | Calculated Property |
| ρl | 834.27 | kg/m3 | 605.06 | Calculated Property |
| ρl | 730.74 | kg/m3 | 644.90 | Calculated Property |
| ρl | 418.89 | kg/m3 | 684.75 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 0.02] | N/m | [326.15; 447.25] |
Jasper (1972), surface tension of pure liquid compounds Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K | |||
| Coefficient A | 5.86699e-02 | |||
| Coefficient B | -8.79000e-05 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 326.15 | |||
| Temperature range, max. | 447.25 | |||
| γ | 0.03 | N/m | 326.15 | Calculated Property |
| γ | 0.03 | N/m | 339.61 | Calculated Property |
| γ | 0.03 | N/m | 353.06 | Calculated Property |
| γ | 0.03 | N/m | 366.52 | Calculated Property |
| γ | 0.03 | N/m | 379.97 | Calculated Property |
| γ | 0.02 | N/m | 393.43 | Calculated Property |
| γ | 0.02 | N/m | 406.88 | Calculated Property |
| γ | 0.02 | N/m | 420.34 | Calculated Property |
| γ | 0.02 | N/m | 433.79 | Calculated Property |
| γ | 0.02 | N/m | 447.25 | Calculated Property |
| γ | [0.03; 3.88e-06] | N/m | [326.14; 681.88] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -7.59660e-03 | |||
| Coefficient B | 3.40080e+02 | |||
| Coefficient C | -5.35860e+00 | |||
| Coefficient D | 6.47410e-03 | |||
| Coefficient E | -9.53680e-06 | |||
| Comment | Range stopped where the equation turns negative; ChemSep gives it to 684.75 K. | |||
| Temperature range, min. | 326.14 | |||
| Temperature range, max. | 681.88 | |||
| γ | 0.03 | N/m | 326.14 | Calculated Property |
| γ | 0.03 | N/m | 365.67 | Calculated Property |
| γ | 0.02 | N/m | 405.19 | Calculated Property |
| γ | 0.02 | N/m | 444.72 | Calculated Property |
| γ | 0.02 | N/m | 484.25 | Calculated Property |
| γ | 0.01 | N/m | 523.77 | Calculated Property |
| γ | 0.01 | N/m | 563.30 | Calculated Property |
| γ | 0.01 | N/m | 602.83 | Calculated Property |
| γ | 0.00 | N/m | 642.35 | Calculated Property |
| γ | 3.88e-06 | N/m | 681.88 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.01; 0.06] | W/m×K | [326.14; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | -2.26970e+03 | |||
| Coefficient B | 6.85980e-01 | |||
| Coefficient C | -3.77400e+09 | |||
| Coefficient D | -2.66550e+11 | |||
| Temperature range, min. | 326.14 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.01 | W/m×K | 326.14 | Calculated Property |
| λgas | 0.01 | W/m×K | 401.01 | Calculated Property |
| λgas | 0.02 | W/m×K | 475.89 | Calculated Property |
| λgas | 0.02 | W/m×K | 550.76 | Calculated Property |
| λgas | 0.03 | W/m×K | 625.63 | Calculated Property |
| λgas | 0.03 | W/m×K | 700.51 | Calculated Property |
| λgas | 0.04 | W/m×K | 775.38 | Calculated Property |
| λgas | 0.05 | W/m×K | 850.25 | Calculated Property |
| λgas | 0.06 | W/m×K | 925.13 | Calculated Property |
| λgas | 0.06 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.13; 0.07] | W/m×K | [208.50; 548.50] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K | |||
| Coefficient A | 2.92700e-02 | |||
| Coefficient B | -2.82870e+01 | |||
| Coefficient C | -2.03190e+00 | |||
| Coefficient D | 7.77640e-05 | |||
| Coefficient E | -3.77970e-06 | |||
| Temperature range, min. | 208.50 | |||
| Temperature range, max. | 548.50 | |||
| λliquid | 0.13 | W/m×K | 208.50 | Calculated Property |
| λliquid | 0.12 | W/m×K | 246.28 | Calculated Property |
| λliquid | 0.12 | W/m×K | 284.06 | Calculated Property |
| λliquid | 0.11 | W/m×K | 321.83 | Calculated Property |
| λliquid | 0.11 | W/m×K | 359.61 | Calculated Property |
| λliquid | 0.10 | W/m×K | 397.39 | Calculated Property |
| λliquid | 0.09 | W/m×K | 435.17 | Calculated Property |
| λliquid | 0.08 | W/m×K | 472.94 | Calculated Property |
| λliquid | 0.08 | W/m×K | 510.72 | Calculated Property |
| λliquid | 0.07 | W/m×K | 548.50 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, 1,4-dichloro-.
Mixtures
Sources
- KDB Vapor Pressure Data
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Crippen Method
- Improving the method of solution calorimetry for evaluation of the enthalpies of phase transitions and condensed state enthalpies of formation
- Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
- 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
- Solution and solvation enthalpies of aromatic derivitives in binary mixtures. Dipole moment and dielectric properties
- Low-Temperature Heat Capacities and Derived Thermodynamic Functions of 1,4 Dichlorobenzene, 1,4 Dibromobenzene, 1,3,5 Trichlorobenzene, and 1,3,5 Tribromobenzene
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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