- InChI
- InChI=1S/C6H4Cl2/c7-5-3-1-2-4-6(5)8/h1-4H
- InChI Key
- RFFLAFLAYFXFSW-UHFFFAOYSA-N
- Formula
- C6H4Cl2
- SMILES
- Clc1ccccc1Cl
- Molecular Weight1
- 147.00
- CAS
- 95-50-1
- Other Names
-
- 1,2-DICHLOROBENZENE
- 1,2-Dichlorbenzene
- Benzene, o-dichloro-
- CHLOROBEN
- Chloroden
- Cloroben
- DCB
- Dichlorobenzene, o-
- Dichlorobenzene, ortho
- Dilantin DB
- Dilatin db
- Dizene
- Dowtherm E
- NCI-C54944
- NSC 60644
- O-DICHLOROBENZENE
- ODB
- ODCB
- Orthodichlorobenzol
- Special termite fluid
- Termitkil
- UN 1591
- o-Dichlorbenzene
- o-Dichlorbenzol
- o-Dichlorobenzol
- ortho-Dichlorobenzene
- ω : Acentric Factor.
- 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).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- EA : Electron affinity (eV).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase 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).
- 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.
- 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).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.2720 | KDB | |
| ΔcH°liquid | [-2964.70; -2957.80] | kJ/mol |
|
| ΔcH°liquid | -2964.70 | kJ/mol | NIST |
| ΔcH°liquid | -2962.60 ± 1.30 | kJ/mol | NIST |
| ΔcH°liquid | -2963.00 ± 2.00 | kJ/mol | NIST |
| ΔcH°liquid | -2958.60 ± 0.71 | kJ/mol | NIST |
| ΔcH°liquid | -2963.90 ± 2.50 | kJ/mol | NIST |
| ΔcH°liquid | -2957.80 ± 1.20 | kJ/mol | NIST |
| μ | 2.30 | debye | KDB |
| EA | 0.09 | eV | NIST |
| ΔfG° | 82.73 | kJ/mol | KDB |
| ΔfH°gas | [30.00; 33.00] | kJ/mol |
|
| ΔfH°gas | 30.00 | kJ/mol | KDB |
| ΔfH°gas | 33.00 | kJ/mol | NIST |
| ΔfH°liquid | [-17.60; -16.00] | kJ/mol |
|
| ΔfH°liquid | -17.40 ± 1.30 | kJ/mol | NIST |
| ΔfH°liquid | -16.00 ± 2.00 | kJ/mol | NIST |
| ΔfH°liquid | -17.60 ± 0.71 | kJ/mol | NIST |
| ΔfH°(+) ion | 904.20 | kJ/mol | NIST |
| ΔfH(+) ion,0K | 916.70 | kJ/mol | NIST |
| ΔfusH° | 13.34 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [48.50; 50.90] | kJ/mol |
|
| ΔvapH° | 50.90 | kJ/mol | NIST |
| ΔvapH° | 48.50 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 49.90 | kJ/mol | NIST |
| IE | [9.06; 9.24] | eV |
|
| IE | 9.06 ± 0.02 | eV | NIST |
| IE | 9.06 ± 0.02 | eV | NIST |
| IE | 9.08 ± 0.03 | eV | NIST |
| IE | 9.06 ± 0.02 | eV | NIST |
| IE | 9.08 ± 0.01 | eV | NIST |
| IE | 9.07 ± 0.01 | eV | NIST |
| IE | 9.06 | eV | NIST |
| IE | Outlier 9.24 | eV | NIST |
| IE | 9.23 | eV | NIST |
| IE | 9.08 | eV | NIST |
| log10WS | [-3.05; -3.03] |
|
|
| log10WS | -3.03 | Aq. Sol... | |
| log10WS | -3.05 | Estimat... | |
| logPoct/wat | 2.993 | Crippen Calculated Property | |
| McVol | 96.120 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | 4100.00 | kPa | KDB |
| Inp | [167.40; 1076.00] |
|
|
| Inp | 1046.17 | NIST | |
| Inp | 1046.22 | NIST | |
| Inp | 1056.93 | NIST | |
| Inp | 1057.07 | NIST | |
| Inp | 1050.00 | NIST | |
| Inp | 1063.80 | NIST | |
| Inp | 1063.80 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1052.48 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1040.29 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1050.00 | NIST | |
| Inp | 1045.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1038.00 | NIST | |
| Inp | 1050.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 1024.00 | NIST | |
| Inp | 1045.72 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1049.02 | NIST | |
| Inp | 1049.74 | NIST | |
| Inp | 1002.80 | NIST | |
| Inp | 1022.40 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1012.20 | NIST | |
| Inp | 1021.95 | NIST | |
| Inp | 1025.52 | NIST | |
| Inp | 1029.19 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1016.00 | NIST | |
| Inp | 1016.00 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1015.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1012.00 | NIST | |
| Inp | 1010.00 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 1014.40 | NIST | |
| Inp | 1003.00 | NIST | |
| Inp | 1027.00 | NIST | |
| Inp | 992.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 984.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1006.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1008.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1055.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | Outlier 168.00 | NIST | |
| Inp | Outlier 167.40 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | Outlier 168.00 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1008.00 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 1015.00 | NIST | |
| Inp | 995.00 | NIST | |
| I | [1445.00; 1529.80] |
|
|
| I | 1529.80 | NIST | |
| I | 1445.00 | NIST | |
| I | 1447.00 | NIST | |
| I | 1514.00 | NIST | |
| I | 1486.00 | NIST | |
| I | 1455.00 | NIST | |
| I | 1459.00 | NIST | |
| I | 1492.00 | NIST | |
| I | 1492.00 | NIST | |
| I | 1519.77 | NIST | |
| I | 1511.85 | NIST | |
| I | 1488.07 | NIST | |
| I | 1495.00 | NIST | |
| I | 1497.00 | NIST | |
| I | 1452.00 | NIST | |
| I | 1452.00 | NIST | |
| I | 1452.00 | NIST | |
| I | 1529.80 | NIST | |
| I | 1492.00 | NIST | |
| I | 1495.00 | NIST | |
| I | 1486.00 | NIST | |
| Tboil | [452.65; 453.70] | K |
|
| Tboil | 453.60 | K | KDB |
| Tboil | 453.70 | K | NIST |
| Tboil | 453.40 ± 0.50 | K | NIST |
| Tboil | 453.00 ± 1.50 | K | NIST |
| Tboil | 453.63 ± 0.07 | K | NIST |
| Tboil | 452.65 ± 0.35 | K | NIST |
| Tc | [698.80; 729.00] | K |
|
| Tc | 729.00 | K | KDB |
| Tc | 698.80 | K | The Cri... |
| Tfus | [255.20; 256.15] | K |
|
| Tfus | 256.10 | K | KDB |
| Tfus | 255.92 | K | Aq. Sol... |
| Tfus | Outlier 255.20 ± 0.20 | K | NIST |
| Tfus | 256.15 ± 0.05 | K | NIST |
| Tfus | 256.00 ± 0.10 | K | NIST |
| Tfus | 256.13 ± 0.10 | K | NIST |
| Tfus | 256.14 ± 0.05 | K | NIST |
| Tfus | 256.12 ± 0.05 | K | NIST |
| Tfus | 256.00 ± 2.00 | K | NIST |
| Tfus | 256.00 ± 0.50 | K | NIST |
| Vc | 0.360 | m3/kmol | KDB |
| Zc | 0.2435130 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [149.05; 190.77] | J/mol×K | [443.20; 674.86] |
|
| Cp,gas | 149.05 | J/mol×K | 443.20 | Joback Calculated Property |
| Cp,gas | 157.36 | J/mol×K | 481.81 | Joback Calculated Property |
| Cp,gas | 165.09 | J/mol×K | 520.42 | Joback Calculated Property |
| Cp,gas | 172.26 | J/mol×K | 559.03 | Joback Calculated Property |
| Cp,gas | 178.92 | J/mol×K | 597.64 | Joback Calculated Property |
| Cp,gas | 185.08 | J/mol×K | 636.25 | Joback Calculated Property |
| Cp,gas | 190.77 | J/mol×K | 674.86 | Joback Calculated Property |
| Cp,liquid | [167.68; 183.28] | J/mol×K | [283.15; 353.15] |
|
| Cp,liquid | 167.68 | J/mol×K | 283.15 | Heat Ca... |
| Cp,liquid | 168.06 | J/mol×K | 285.15 | Heat Ca... |
| Cp,liquid | 168.44 | J/mol×K | 287.15 | Heat Ca... |
| Cp,liquid | 168.83 | J/mol×K | 289.15 | Heat Ca... |
| Cp,liquid | 169.23 | J/mol×K | 291.15 | Heat Ca... |
| Cp,liquid | 169.64 | J/mol×K | 293.15 | Heat Ca... |
| Cp,liquid | 170.05 | J/mol×K | 295.15 | Heat Ca... |
| Cp,liquid | 170.47 | J/mol×K | 297.15 | Heat Ca... |
| Cp,liquid | 170.90 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 170.89 | J/mol×K | 299.15 | Heat Ca... |
| Cp,liquid | 171.32 | J/mol×K | 301.15 | Heat Ca... |
| Cp,liquid | 171.76 | J/mol×K | 303.15 | Heat Ca... |
| Cp,liquid | 172.20 | J/mol×K | 305.15 | Heat Ca... |
| Cp,liquid | 172.64 | J/mol×K | 307.15 | Heat Ca... |
| Cp,liquid | 173.09 | J/mol×K | 309.15 | Heat Ca... |
| Cp,liquid | 173.54 | J/mol×K | 311.15 | Heat Ca... |
| Cp,liquid | 174.00 | J/mol×K | 313.15 | Heat Ca... |
| Cp,liquid | 174.46 | J/mol×K | 315.15 | Heat Ca... |
| Cp,liquid | 174.92 | J/mol×K | 317.15 | Heat Ca... |
| Cp,liquid | 175.38 | J/mol×K | 319.15 | Heat Ca... |
| Cp,liquid | 175.85 | J/mol×K | 321.15 | Heat Ca... |
| Cp,liquid | 176.32 | J/mol×K | 323.15 | Heat Ca... |
| Cp,liquid | 176.79 | J/mol×K | 325.15 | Heat Ca... |
| Cp,liquid | 177.26 | J/mol×K | 327.15 | Heat Ca... |
| Cp,liquid | 177.73 | J/mol×K | 329.15 | Heat Ca... |
| Cp,liquid | 178.20 | J/mol×K | 331.15 | Heat Ca... |
| Cp,liquid | 178.67 | J/mol×K | 333.15 | Heat Ca... |
| Cp,liquid | 179.14 | J/mol×K | 335.15 | Heat Ca... |
| Cp,liquid | 179.61 | J/mol×K | 337.15 | Heat Ca... |
| Cp,liquid | 180.07 | J/mol×K | 339.15 | Heat Ca... |
| Cp,liquid | 180.54 | J/mol×K | 341.15 | Heat Ca... |
| Cp,liquid | 181.00 | J/mol×K | 343.15 | Heat Ca... |
| Cp,liquid | 181.47 | J/mol×K | 345.15 | Heat Ca... |
| Cp,liquid | 181.92 | J/mol×K | 347.15 | Heat Ca... |
| Cp,liquid | 182.38 | J/mol×K | 349.15 | Heat Ca... |
| Cp,liquid | 182.83 | J/mol×K | 351.15 | Heat Ca... |
| Cp,liquid | 183.28 | J/mol×K | 353.15 | Heat Ca... |
| η | [0.0002989; 0.0021588] | Pa×s | [256.16; 443.20] |
|
| η | 0.0021588 | Pa×s | 256.16 | Joback Calculated Property |
| η | 0.0012985 | Pa×s | 287.33 | Joback Calculated Property |
| η | 0.0008628 | Pa×s | 318.51 | Joback Calculated Property |
| η | 0.0006166 | Pa×s | 349.68 | Joback Calculated Property |
| η | 0.0004656 | Pa×s | 380.85 | Joback Calculated Property |
| η | 0.0003668 | Pa×s | 412.03 | Joback Calculated Property |
| η | 0.0002989 | Pa×s | 443.20 | Joback Calculated Property |
| ΔfusH | [12.40; 12.93] | kJ/mol | [255.65; 256.50] |
|
| ΔfusH | 12.92 | kJ/mol | 255.65 | NIST |
| ΔfusH | 12.40 | kJ/mol | 255.90 | NIST |
| ΔfusH | 12.93 | kJ/mol | 256.50 | NIST |
| ΔfusH | 12.93 | kJ/mol | 256.50 | NIST |
| ΔvapH | [39.66; 51.20] | kJ/mol | [256.00; 449.10] |
|
| ΔvapH | 51.20 | kJ/mol | 256.00 | NIST |
| ΔvapH | 50.80 | kJ/mol | 271.50 | NIST |
| ΔvapH | 51.20 | kJ/mol | 285.50 | NIST |
| ΔvapH | 50.00 | kJ/mol | 322.00 | NIST |
| ΔvapH | 44.50 | kJ/mol | 408.50 | NIST |
| ΔvapH | 44.00 | kJ/mol | 413.00 | NIST |
| ΔvapH | 39.66 | kJ/mol | 449.10 | KDB |
| Pvap | [4.86; 98.36] | kPa | [360.41; 452.62] |
|
| Pvap | 4.86 | kPa | 360.41 | Physico... |
| Pvap | 9.95 | kPa | 377.35 | Physico... |
| Pvap | 14.98 | kPa | 388.41 | Physico... |
| Pvap | 20.04 | kPa | 396.96 | Physico... |
| Pvap | 24.99 | kPa | 403.40 | Physico... |
| Pvap | 30.00 | kPa | 408.91 | Physico... |
| Pvap | 35.02 | kPa | 414.16 | Physico... |
| Pvap | 40.02 | kPa | 418.75 | Physico... |
| Pvap | 45.05 | kPa | 422.87 | Physico... |
| Pvap | 55.03 | kPa | 429.99 | Physico... |
| Pvap | 59.97 | kPa | 433.29 | Physico... |
| Pvap | 69.93 | kPa | 438.87 | Physico... |
| Pvap | 79.98 | kPa | 443.92 | Physico... |
| Pvap | 90.20 | kPa | 448.94 | Physico... |
| Pvap | 95.11 | kPa | 451.11 | Physico... |
| Pvap | 98.36 | kPa | 452.62 | Physico... |
| n0 | [1.53320; 1.55230] | [288.20; 328.20] |
|
|
| n0 | 1.55230 | 288.20 | Mass Di... | |
| n0 | 1.54600 | 298.15 | Densiti... | |
| n0 | 1.54910 | 298.15 | Liquid-... | |
| n0 | 1.54990 | 298.15 | Density... | |
| n0 | 1.54890 | 298.20 | Mass Di... | |
| n0 | 1.54400 | 303.15 | Densiti... | |
| n0 | 1.54760 | 303.15 | Density... | |
| n0 | 1.54500 | 308.15 | Density... | |
| n0 | 1.54100 | 308.15 | Densiti... | |
| n0 | 1.54380 | 308.20 | Mass Di... | |
| n0 | 1.53860 | 318.20 | Mass Di... | |
| n0 | 1.53320 | 328.20 | Mass Di... | |
| ρl | [1299.20; 1306.00] | kg/m3 | [293.00; 303.15] |
|
| ρl | 1306.00 | kg/m3 | 293.00 | KDB |
| ρl | 1299.20 | kg/m3 | 303.15 | Effect ... |
| ΔfusS | 50.50 | J/mol×K | 255.65 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 451.20 | K | 102.00 | NIST |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
| 101.00 | 303.15 | 0.0013 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [330.74; 484.72] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.40308e+01 | |||
| Coefficient B | -3.67273e+03 | |||
| Coefficient C | -6.35030e+01 | |||
| Temperature range, min. | 330.74 | |||
| Temperature range, max. | 484.72 | |||
| Pvap | 1.33 | kPa | 330.74 | Calculated Property |
| Pvap | 3.05 | kPa | 347.85 | Calculated Property |
| Pvap | 6.34 | kPa | 364.96 | Calculated Property |
| Pvap | 12.20 | kPa | 382.07 | Calculated Property |
| Pvap | 21.96 | kPa | 399.18 | Calculated Property |
| Pvap | 37.34 | kPa | 416.28 | Calculated Property |
| Pvap | 60.44 | kPa | 433.39 | Calculated Property |
| Pvap | 93.74 | kPa | 450.50 | Calculated Property |
| Pvap | 140.10 | kPa | 467.61 | Calculated Property |
| Pvap | 202.66 | kPa | 484.72 | Calculated Property |
| Pvap | [6.43e-03; 4105.80] | kPa | [256.15; 729.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.74184e+01 | |||
| Coefficient B | -8.04769e+03 | |||
| Coefficient C | -7.42072e+00 | |||
| Coefficient D | 1.61077e-06 | |||
| Temperature range, min. | 256.15 | |||
| Temperature range, max. | 729.00 | |||
| Pvap | 6.43e-03 | kPa | 256.15 | Calculated Property |
| Pvap | 0.35 | kPa | 308.69 | Calculated Property |
| Pvap | 5.18 | kPa | 361.23 | Calculated Property |
| Pvap | 34.20 | kPa | 413.77 | Calculated Property |
| Pvap | 135.79 | kPa | 466.31 | Calculated Property |
| Pvap | 383.70 | kPa | 518.84 | Calculated Property |
| Pvap | 856.26 | kPa | 571.38 | Calculated Property |
| Pvap | 1614.84 | kPa | 623.92 | Calculated Property |
| Pvap | 2694.26 | kPa | 676.46 | Calculated Property |
| Pvap | 4105.80 | kPa | 729.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, 1,2-dichloro-.
Mixtures
- Benzene, 1,2-dichloro- + N,N-Dimethylacetamide
- Benzene, 1,2-dichloro- + Dimethyl Sulfoxide
- Benzene, 1,2-dichloro- + Buckminsterfullerene
- Benzene, 1,2-dichloro- + Pentane, 2,2,4-trimethyl-
- Benzene, 1,2-dichloro- + Cyclooctane
- Benzene, 1,2-dichloro- + Octane
- Benzene, 1,2-dichloro- + Pentanenitrile
- Azacyclotridecan-2-one + Benzene, 1,2-dichloro-
- Benzene, 1,2-dichloro- + Naphthalene
- n-Hexane + Benzene, 1,2-dichloro- + Furfural
- Benzene, 1,2-dichloro- + Furfural + Hexadecane
- Benzene, 1,2-dichloro- + 1,4-Dioxane
- Benzene, 1,2-dichloro- + Tetrahydrofuran
- Benzene, 1,2-dichloro- + 1,2-Ethanediol
- Benzene, 1,2-dichloro- + Propylene Glycol
- Benzene, 1,2-dichloro- + Cyclic octaatomic sulfur + Benzene, chloro-
- Benzene + Benzene, 1,2-dichloro- + Hexane, 1-chloro-
- Benzene, 1,2-dichloro- + Water
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Octanol with Chlorobenzenes
- Densities and ultrasonic studies for binary mixtures of tetrahydrofuran with chlorobenzenes, chlorotoluenes and nitrotoluenes at 298.15 K
- Liquid-liquid equilibrium data for binary systems containing o-dichlorobenzene and nitrobenzene
- Effect of various substituents on benzene ring and their impact on volumetric, acoustic and transport properties of binary liquid mixtures with dimethylacetamide
- Solubility of 1-methyl-4-nitropyrazole in seventeen pure solvents at temperatures from 283.15 K to 323.15 K
- Volumetric, ultrasonic and viscometric studies of binary mixtures of dimethyl sulphoxide with chloro and nitro substituted aromatic hydrocarbons at T = 303.15 K
- S6 Isomer of C60(CF3)12: Synthesis, properties and thermodynamic functions
- Phase behavior of ionic liquids 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imides with halogenated benzenes
- Mass Diffusion Coefficient and Soret Coefficient of o-Dichlorobenzene Solutions of PCBM and [60]Fullerene by the Soret Forced Rayleigh Scattering Method
- 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
- Physico-Chemical Properties of LiFSI Solutions I. LiFSI with Valeronitrile, Dichloromethane, 1,2-Dichloroethane, and 1,2-Dichlorobenzene
- Solid-Liquid Equilibrium of Azacyclotridecan-2-one in 15 Pure Solvents from T = 273.15 to 323.15 K: Experimental Determination and Thermodynamic Modeling
- Thermodynamic Studies of Solubility for Naphthalene in 12 Solvents from 279 to 330 K
- Liquid-Liquid Equilibria for Mixtures of (Furfural + a Chlorinated Aromatic Compound + an Alkane) at T = 298.15 K
- Excess Molar Enthalpies and Excess Molar Volumes of the Ternary System 1,2-Dichlorobenzene + Benzene +1-Chlorohexane at 298.15 K
- The Effects of Temperature and Inorganic Salts on the Aqueous Solubility of Selected Chlorobenzenes
- Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of 1,4-Dioxane with Different Organic Liquids at (298.15, 303.15, and 308.15) K
- 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
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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