- InChI
- InChI=1S/CHCl3/c2-1(3)4/h1H
- InChI Key
- HEDRZPFGACZZDS-UHFFFAOYSA-N
- Formula
- CHCl3
- SMILES
- ClC(Cl)Cl
- Molecular Weight1
- 119.38
- CAS
- 67-66-3
- Other Names
-
- CHCl3
- Chloroform
- Chloroforme
- Cloroformio
- F 20
- Formyl trichloride
- Freon 20
- Methane trichloride
- Methane, trichloro-
- Methenyl trichloride
- Methyl trichloride
- NCI-C02686
- NSC 77361
- R 20
- R 20 (refrigerant)
- R-20
- Rcra waste number U044
- Trichloormethaan
- Trichlormethan
- Trichloroform
- Triclorometano
- UN 1888
- 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).
- 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).
- ν : Kinematic viscosity (m2/s).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- 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.
- 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).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Vm : Molar Volume (m3/mol).
- 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.
Contents
- Physical Properties
- Temperature Dependent Properties
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.2180 | KDB | |
| ΔcH°liquid | [-474.00; -473.21] | kJ/mol |
|
| ΔcH°liquid | -473.21 | kJ/mol | NIST |
| ΔcH°liquid | -474.00 ± 8.40 | kJ/mol | NIST |
| μ | 1.10 | debye | KDB |
| EA | [0.62; 1.76] | eV |
|
| EA | 0.62 ± 0.16 | eV | NIST |
| EA | 1.76 ± 0.05 | eV | NIST |
| ΔfG° | -68.58 | kJ/mol | KDB |
| Rg | 3.1780 | KDB | |
| ΔfH°gas | [-102.90; -101.30] | kJ/mol |
|
| ΔfH°gas | -101.30 | kJ/mol | KDB |
| ΔfH°gas | -102.90 ± 2.50 | kJ/mol | NIST |
| ΔfH°liquid | [-134.30; -134.10] | kJ/mol |
|
| ΔfH°liquid | -134.10 ± 2.50 | kJ/mol | NIST |
| ΔfH°liquid | -134.30 | kJ/mol | NIST |
| ΔfusH° | 7.41 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [30.50; 31.40] | kJ/mol |
|
| ΔvapH° | 31.40 | kJ/mol | NIST |
| ΔvapH° | 31.32 ± 0.08 | kJ/mol | NIST |
| ΔvapH° | 31.10 | kJ/mol | NIST |
| ΔvapH° | 30.50 ± 0.42 | kJ/mol | NIST |
| IE | [11.30; 11.50] | eV |
|
| IE | 11.37 ± 0.02 | eV | NIST |
| IE | 11.41 ± 0.02 | eV | NIST |
| IE | 11.30 | eV | NIST |
| IE | 11.48 | eV | NIST |
| IE | 11.37 ± 0.02 | eV | NIST |
| IE | 11.40 | eV | NIST |
| IE | 11.50 | eV | NIST |
| IE | 11.42 ± 0.03 | eV | NIST |
| IE | 11.50 | eV | NIST |
| IE | 11.48 | eV | NIST |
| log10WS | [-1.17; -1.17] |
|
|
| log10WS | -1.17 | Estimat... | |
| log10WS | -1.17 | Aq. Sol... | |
| logPoct/wat | 1.986 | Crippen Calculated Property | |
| McVol | 61.670 | ml/mol | McGowan Calculated Property |
| NFPA Health | 2 | KDB | |
| Pc | [5328.68; 5470.00] | kPa |
|
| Pc | 5470.00 | kPa | KDB |
| Pc | 5328.68 ± 10.13 | kPa | NIST |
| Pc | 5328.68 ± 6.07 | kPa | NIST |
| ρc | [458.41; 495.42] | kg/m3 |
|
| ρc | 490.64 ± 3.58 | kg/m3 | NIST |
| ρc | 458.41 ± 2.39 | kg/m3 | NIST |
| ρc | 495.42 ± 2.39 | kg/m3 | NIST |
| Inp | [561.00; 630.00] |
|
|
| Inp | 617.20 | NIST | |
| Inp | 619.00 | NIST | |
| Inp | 628.40 | NIST | |
| Inp | 625.80 | NIST | |
| Inp | 621.10 | NIST | |
| Inp | 618.20 | NIST | |
| Inp | 614.80 | NIST | |
| Inp | 607.90 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 606.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 606.80 | NIST | |
| Inp | 610.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 608.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 582.00 | NIST | |
| Inp | 609.00 | NIST | |
| Inp | Outlier 568.00 | NIST | |
| Inp | 595.20 | NIST | |
| Inp | 616.00 | NIST | |
| Inp | 610.00 | NIST | |
| Inp | 587.00 | NIST | |
| Inp | 622.00 | NIST | |
| Inp | 622.00 | NIST | |
| Inp | 613.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 616.00 | NIST | |
| Inp | 615.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 621.70 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 590.00 | NIST | |
| Inp | 618.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | Outlier 561.00 | NIST | |
| Inp | Outlier 569.00 | NIST | |
| Inp | 630.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 615.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 615.00 | NIST | |
| Inp | 618.00 | NIST | |
| Inp | 618.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 588.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 616.00 | NIST | |
| Inp | 609.00 | NIST | |
| Inp | 617.00 | NIST | |
| Inp | 609.00 | NIST | |
| Inp | 609.00 | NIST | |
| Inp | 611.00 | NIST | |
| Inp | 629.00 | NIST | |
| Inp | 609.00 | NIST | |
| Inp | 603.00 | NIST | |
| Inp | 620.00 | NIST | |
| Inp | 618.00 | NIST | |
| Inp | 609.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 603.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 620.00 | NIST | |
| Inp | 609.00 | NIST | |
| Inp | 611.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 606.00 | NIST | |
| Inp | 603.00 | NIST | |
| Inp | 609.00 | NIST | |
| Inp | 616.00 | NIST | |
| Inp | 595.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 598.00 | NIST | |
| I | [992.00; 1045.00] |
|
|
| I | 1037.00 | NIST | |
| I | 1037.00 | NIST | |
| I | 1034.00 | NIST | |
| I | 1030.11 | NIST | |
| I | 1028.95 | NIST | |
| I | 1027.69 | NIST | |
| I | 1026.00 | NIST | |
| I | 1026.00 | NIST | |
| I | 1024.00 | NIST | |
| I | 1021.00 | NIST | |
| I | 1020.00 | NIST | |
| I | 1022.00 | NIST | |
| I | 1026.00 | NIST | |
| I | 1026.00 | NIST | |
| I | 1013.00 | NIST | |
| I | 1028.00 | NIST | |
| I | 1010.00 | NIST | |
| I | 1020.00 | NIST | |
| I | 1021.00 | NIST | |
| I | 1022.00 | NIST | |
| I | 1022.00 | NIST | |
| I | 1018.00 | NIST | |
| I | 1020.00 | NIST | |
| I | 1023.00 | NIST | |
| I | 1022.00 | NIST | |
| I | Outlier 999.00 | NIST | |
| I | 1038.00 | NIST | |
| I | 1010.00 | NIST | |
| I | Outlier 1045.00 | NIST | |
| I | 1007.00 | NIST | |
| I | 1037.00 | NIST | |
| I | 1037.00 | NIST | |
| I | 1017.00 | NIST | |
| I | 1025.00 | NIST | |
| I | 1015.00 | NIST | |
| I | 1016.00 | NIST | |
| I | 1037.00 | NIST | |
| I | 1037.00 | NIST | |
| I | 1018.00 | NIST | |
| I | 1020.00 | NIST | |
| I | Outlier 992.00 | NIST | |
| I | 1014.00 | NIST | |
| I | 1014.00 | NIST | |
| I | 1000.00 | NIST | |
| I | 1000.00 | NIST | |
| I | 1024.00 | NIST | |
| I | 1037.00 | NIST | |
| I | 1027.69 | NIST | |
| I | 1010.00 | NIST | |
| I | 1024.00 | NIST | |
| Tboil | [333.95; 335.00] | K |
|
| Tboil | 334.32 | K | KDB |
| Tboil | Outlier 335.00 | K | The rol... |
| Tboil | 334.10 | K | Phase d... |
| Tboil | 334.35 | K | Separat... |
| Tboil | 334.12 | K | Isobari... |
| Tboil | 334.30 | K | NIST |
| Tboil | 334.37 ± 0.15 | K | NIST |
| Tboil | 334.45 ± 0.50 | K | NIST |
| Tboil | 334.10 ± 0.30 | K | NIST |
| Tboil | 334.35 ± 0.06 | K | NIST |
| Tboil | 334.34 ± 0.25 | K | NIST |
| Tboil | 334.39 ± 0.30 | K | NIST |
| Tboil | 334.30 ± 0.20 | K | NIST |
| Tboil | 334.35 ± 0.10 | K | NIST |
| Tboil | 334.24 ± 0.15 | K | NIST |
| Tboil | Outlier 333.95 ± 0.40 | K | NIST |
| Tboil | 334.42 ± 0.35 | K | NIST |
| Tboil | 334.42 ± 0.30 | K | NIST |
| Tboil | 334.35 ± 0.30 | K | NIST |
| Tboil | 334.35 ± 0.30 | K | NIST |
| Tboil | 334.35 ± 0.30 | K | NIST |
| Tboil | 334.30 ± 0.20 | K | NIST |
| Tboil | 334.30 ± 0.50 | K | NIST |
| Tboil | 334.45 ± 0.50 | K | NIST |
| Tboil | 334.20 ± 1.00 | K | NIST |
| Tboil | 334.50 ± 0.20 | K | NIST |
| Tboil | 334.22 ± 0.50 | K | NIST |
| Tboil | 334.27 ± 0.30 | K | NIST |
| Tboil | 334.30 ± 0.25 | K | NIST |
| Tboil | 334.30 ± 0.50 | K | NIST |
| Tboil | 334.23 ± 0.06 | K | NIST |
| Tboil | 334.30 ± 0.30 | K | NIST |
| Tboil | 334.40 ± 0.50 | K | NIST |
| Tboil | 334.37 ± 0.20 | K | NIST |
| Tboil | 334.20 ± 0.30 | K | NIST |
| Tboil | 334.22 ± 0.20 | K | NIST |
| Tboil | 334.35 ± 0.30 | K | NIST |
| Tboil | 334.30 ± 0.50 | K | NIST |
| Tboil | 334.15 ± 0.50 | K | NIST |
| Tboil | 334.40 ± 0.30 | K | NIST |
| Tboil | 334.35 ± 0.20 | K | NIST |
| Tboil | 334.45 ± 0.60 | K | NIST |
| Tc | 536.40 | K | KDB |
| Tfus | [209.50; 212.15] | K |
|
| Tfus | 209.50 | K | KDB |
| Tfus | 209.95 | K | Aq. Sol... |
| Tfus | 209.73 ± 0.01 | K | NIST |
| Tfus | 209.64 ± 0.10 | K | NIST |
| Tfus | 210.15 ± 1.00 | K | NIST |
| Tfus | 209.61 ± 0.08 | K | NIST |
| Tfus | 209.65 ± 0.20 | K | NIST |
| Tfus | 211.05 ± 0.30 | K | NIST |
| Tfus | 209.50 ± 0.70 | K | NIST |
| Tfus | 210.00 ± 2.00 | K | NIST |
| Tfus | 209.65 ± 0.20 | K | NIST |
| Tfus | 211.59 ± 0.50 | K | NIST |
| Tfus | 209.90 ± 0.30 | K | NIST |
| Tfus | Outlier 212.15 ± 1.00 | K | NIST |
| Tfus | 210.46 ± 0.20 | K | NIST |
| Tfus | 210.00 ± 2.00 | K | NIST |
| Ttriple | 209.61 ± 0.20 | K | NIST |
| Vc | 0.239 | m3/kmol | KDB |
| Vm | 8.07e-05 | m3/mol | Excess ... |
| Zc | 0.2931300 | KDB | |
| Zra | 0.28 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [71.18; 82.74] | J/mol×K | [334.13; 532.11] |
|
| Cp,gas | 71.18 | J/mol×K | 334.13 | Joback Calculated Property |
| Cp,gas | 73.44 | J/mol×K | 367.13 | Joback Calculated Property |
| Cp,gas | 75.56 | J/mol×K | 400.12 | Joback Calculated Property |
| Cp,gas | 77.54 | J/mol×K | 433.12 | Joback Calculated Property |
| Cp,gas | 79.40 | J/mol×K | 466.12 | Joback Calculated Property |
| Cp,gas | 81.13 | J/mol×K | 499.12 | Joback Calculated Property |
| Cp,gas | 82.74 | J/mol×K | 532.11 | Joback Calculated Property |
| Cp,liquid | [113.00; 139.70] | J/mol×K | [293.00; 303.60] |
|
| Cp,liquid | 116.20 | J/mol×K | 293.00 | NIST |
| Cp,liquid | 115.50 | J/mol×K | 293.20 | NIST |
| Cp,liquid | 117.10 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 114.18 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 113.00 | J/mol×K | 298.10 | NIST |
| Cp,liquid | 114.25 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 115.50 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 113.73 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 114.26 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 113.85 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 115.50 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 114.35 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 114.32 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 113.20 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 113.40 | J/mol×K | 300.00 | NIST |
| Cp,liquid | 116.70 | J/mol×K | 303.00 | NIST |
| Cp,liquid | 114.00 | J/mol×K | 303.20 | NIST |
| Cp,liquid | 139.70 | J/mol×K | 303.60 | NIST |
| η | [0.0004710; 0.0007130] | Pa×s | [273.15; 318.15] |
|
| η | 0.0007130 | Pa×s | 273.15 | Density... |
| η | 0.0006510 | Pa×s | 283.15 | Density... |
| η | 0.0006000 | Pa×s | 293.15 | Density... |
| η | 0.0005560 | Pa×s | 298.15 | Densiti... |
| η | 0.0005760 | Pa×s | 298.15 | Density... |
| η | 0.0005340 | Pa×s | 303.15 | Densiti... |
| η | 0.0005340 | Pa×s | 303.15 | Densiti... |
| η | 0.0005200 | Pa×s | 303.15 | Studies... |
| η | 0.0005520 | Pa×s | 303.15 | Density... |
| η | 0.0005130 | Pa×s | 308.15 | Densiti... |
| η | 0.0004910 | Pa×s | 313.15 | Densiti... |
| η | 0.0004910 | Pa×s | 313.15 | Densiti... |
| η | 0.0004710 | Pa×s | 313.15 | Studies... |
| η | 0.0005090 | Pa×s | 313.15 | Density... |
| η | 0.0004910 | Pa×s | 318.15 | Density... |
| ΔfusH | [8.80; 8.80] | kJ/mol | [209.60; 209.60] |
|
| ΔfusH | 8.80 | kJ/mol | 209.60 | NIST |
| ΔfusH | 8.80 | kJ/mol | 209.60 | NIST |
| ΔvapH | [28.90; 35.00] | kJ/mol | [248.00; 501.00] |
|
| ΔvapH | 31.80 | kJ/mol | 248.00 | NIST |
| ΔvapH | 35.00 | kJ/mol | 274.50 | NIST |
| ΔvapH | 32.50 | kJ/mol | 296.50 | NIST |
| ΔvapH | 30.90 | kJ/mol | 320.50 | NIST |
| ΔvapH | 29.71 | kJ/mol | 334.30 | KDB |
| ΔvapH | 29.24 | kJ/mol | 334.30 | NIST |
| ΔvapH | 30.80 | kJ/mol | 366.50 | NIST |
| ΔvapH | 30.40 | kJ/mol | 374.50 | NIST |
| ΔvapH | 28.90 | kJ/mol | 445.50 | NIST |
| ΔvapH | 30.10 | kJ/mol | 501.00 | NIST |
| ν | [0.0000003; 0.0000004] | m2/s | [303.15; 313.15] |
|
| ν | 0.0000004 | m2/s | 303.15 | Densiti... |
| ν | 0.0000003 | m2/s | 313.15 | Densiti... |
| Pvap | [32.19; 129.28] | kPa | [303.15; 342.00] |
|
| Pvap | 32.19 | kPa | 303.15 | Density... |
| Pvap | 32.41 | kPa | 303.15 | Total V... |
| Pvap | 32.19 | kPa | 303.15 | Density... |
| Pvap | 34.81 | kPa | 305.00 | Isobari... |
| Pvap | 42.47 | kPa | 310.00 | Isobari... |
| Pvap | 51.43 | kPa | 315.00 | Isobari... |
| Pvap | 61.85 | kPa | 320.00 | Isobari... |
| Pvap | 73.88 | kPa | 325.00 | Isobari... |
| Pvap | 87.71 | kPa | 330.00 | Isobari... |
| Pvap | 101.30 | kPa | 334.12 | Isobari... |
| Pvap | 101.30 | kPa | 334.35 | Separat... |
| Pvap | 103.50 | kPa | 335.00 | Isobari... |
| Pvap | 121.45 | kPa | 340.00 | Isobari... |
| Pvap | 129.28 | kPa | 342.00 | Isobari... |
| n0 | [1.44100; 1.45000] | [283.15; 303.15] |
|
|
| n0 | 1.45000 | 283.15 | Partial... | |
| n0 | 1.44710 | 288.15 | Partial... | |
| n0 | 1.44760 | 293.15 | Solubil... | |
| n0 | 1.44390 | 293.15 | Partial... | |
| n0 | 1.44280 | 298.15 | Vapour ... | |
| n0 | 1.44300 | 298.15 | Liquid-... | |
| n0 | 1.44200 | 298.15 | Partial... | |
| n0 | 1.44290 | 298.15 | Study o... | |
| n0 | 1.44100 | 303.15 | Densiti... | |
| ρl | [1429.89; 1498.14] | kg/m3 | [288.15; 323.15] |
|
| ρl | 1498.08 | kg/m3 | 288.15 | Volumet... |
| ρl | 1498.08 | kg/m3 | 288.15 | Tempera... |
| ρl | 1491.86 | kg/m3 | 288.15 | Densiti... |
| ρl | 1498.08 | kg/m3 | 288.15 | Densiti... |
| ρl | 1498.08 | kg/m3 | 288.15 | Volumet... |
| ρl | 1498.14 | kg/m3 | 288.15 | Volumet... |
| ρl | 1492.31 | kg/m3 | 288.15 | Densiti... |
| ρl | 1489.00 | kg/m3 | 293.00 | KDB |
| ρl | 1488.70 | kg/m3 | 293.15 | Excess ... |
| ρl | 1488.64 | kg/m3 | 293.15 | Volumet... |
| ρl | 1488.64 | kg/m3 | 293.15 | Densiti... |
| ρl | 1488.64 | kg/m3 | 293.15 | Volumet... |
| ρl | 1488.70 | kg/m3 | 293.15 | Volumet... |
| ρl | 1488.64 | kg/m3 | 293.15 | Tempera... |
| ρl | 1487.63 | kg/m3 | 293.15 | Speed o... |
| ρl | 1483.02 | kg/m3 | 293.20 | Isobari... |
| ρl | 1478.16 | kg/m3 | 298.15 | Speed o... |
| ρl | 1478.75 | kg/m3 | 298.15 | Densiti... |
| ρl | 1473.42 | kg/m3 | 298.15 | Volumet... |
| ρl | 1479.15 | kg/m3 | 298.15 | Volumet... |
| ρl | 1473.43 | kg/m3 | 298.15 | Densiti... |
| ρl | 1479.15 | kg/m3 | 298.15 | Tempera... |
| ρl | 1479.21 | kg/m3 | 298.15 | Volumet... |
| ρl | 1473.16 | kg/m3 | 298.15 | Densiti... |
| ρl | 1479.15 | kg/m3 | 298.15 | Densiti... |
| ρl | 1479.15 | kg/m3 | 298.15 | Volumet... |
| ρl | 1480.34 | kg/m3 | 298.20 | The cho... |
| ρl | 1475.30 | kg/m3 | 303.00 | Thermo-... |
| ρl | 1475.30 | kg/m3 | 303.00 | Thermo-... |
| ρl | 1468.61 | kg/m3 | 303.15 | Speed o... |
| ρl | 1469.63 | kg/m3 | 303.15 | Volumet... |
| ρl | 1469.61 | kg/m3 | 303.15 | Densiti... |
| ρl | 1469.61 | kg/m3 | 303.15 | Volumet... |
| ρl | 1469.61 | kg/m3 | 303.15 | Volumet... |
| ρl | 1470.50 | kg/m3 | 303.15 | Viscosi... |
| ρl | 1469.61 | kg/m3 | 303.15 | Tempera... |
| ρl | 1469.16 | kg/m3 | 303.15 | Densiti... |
| ρl | 1469.69 | kg/m3 | 303.15 | Excess ... |
| ρl | 1470.80 | kg/m3 | 308.00 | Thermo-... |
| ρl | 1470.80 | kg/m3 | 308.00 | Thermo-... |
| ρl | 1459.00 | kg/m3 | 308.15 | Speed o... |
| ρl | 1460.01 | kg/m3 | 308.15 | Densiti... |
| ρl | 1454.33 | kg/m3 | 308.15 | Volumet... |
| ρl | 1454.33 | kg/m3 | 308.15 | Densiti... |
| ρl | 1460.03 | kg/m3 | 308.15 | Tempera... |
| ρl | 1460.03 | kg/m3 | 308.15 | Volumet... |
| ρl | 1460.03 | kg/m3 | 308.15 | Densiti... |
| ρl | 1454.07 | kg/m3 | 308.15 | Densiti... |
| ρl | 1460.03 | kg/m3 | 308.15 | Volumet... |
| ρl | 1465.80 | kg/m3 | 313.00 | Thermo-... |
| ρl | 1465.80 | kg/m3 | 313.00 | Thermo-... |
| ρl | 1450.39 | kg/m3 | 313.15 | Excess ... |
| ρl | 1450.41 | kg/m3 | 313.15 | Volumet... |
| ρl | 1450.41 | kg/m3 | 313.15 | Densiti... |
| ρl | 1450.41 | kg/m3 | 313.15 | Volumet... |
| ρl | 1450.41 | kg/m3 | 313.15 | Tempera... |
| ρl | 1450.39 | kg/m3 | 313.15 | Densiti... |
| ρl | 1434.72 | kg/m3 | 318.15 | Densiti... |
| ρl | 1440.03 | kg/m3 | 318.15 | Densiti... |
| ρl | 1434.97 | kg/m3 | 318.15 | Densiti... |
| ρl | 1434.98 | kg/m3 | 318.15 | Volumet... |
| ρl | 1429.89 | kg/m3 | 323.15 | Excess ... |
| csound,fluid | [916.63; 984.42] | m/s | [298.15; 318.15] |
|
| csound,fluid | 984.42 | m/s | 298.15 | Speeds ... |
| csound,fluid | 950.45 | m/s | 308.15 | Speeds ... |
| csound,fluid | 916.63 | m/s | 318.15 | Speeds ... |
| γ | [0.03; 0.03] | N/m | [293.15; 298.20] |
|
| γ | 0.03 | N/m | 293.15 | Investi... |
| γ | 0.03 | N/m | 298.20 | KDB |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | 334.25 | K | 96.60 | Low cos... |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 101.30 | 0.0005 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 101.30 | 0.0005 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 5482.48] | kPa | [244.65; 536.40] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.43630e+01 | |||
| Coefficient B | -2.83926e+03 | |||
| Coefficient C | -4.29370e+01 | |||
| Temperature range, min. | 244.65 | |||
| Temperature range, max. | 536.40 | |||
| Pvap | 1.33 | kPa | 244.65 | Calculated Property |
| Pvap | 9.36 | kPa | 277.07 | Calculated Property |
| Pvap | 40.90 | kPa | 309.48 | Calculated Property |
| Pvap | 129.81 | kPa | 341.90 | Calculated Property |
| Pvap | 328.67 | kPa | 374.32 | Calculated Property |
| Pvap | 705.23 | kPa | 406.73 | Calculated Property |
| Pvap | 1335.51 | kPa | 439.15 | Calculated Property |
| Pvap | 2296.22 | kPa | 471.57 | Calculated Property |
| Pvap | 3658.33 | kPa | 503.98 | Calculated Property |
| Pvap | 5482.48 | kPa | 536.40 | Calculated Property |
| Pvap | [0.08; 5628.11] | kPa | [209.63; 536.40] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.11439e+01 | |||
| Coefficient B | -6.35114e+03 | |||
| Coefficient C | -1.00709e+01 | |||
| Coefficient D | 9.12761e-06 | |||
| Temperature range, min. | 209.63 | |||
| Temperature range, max. | 536.40 | |||
| Pvap | 0.08 | kPa | 209.63 | Calculated Property |
| Pvap | 1.54 | kPa | 245.94 | Calculated Property |
| Pvap | 12.69 | kPa | 282.25 | Calculated Property |
| Pvap | 59.51 | kPa | 318.55 | Calculated Property |
| Pvap | 192.92 | kPa | 354.86 | Calculated Property |
| Pvap | 487.71 | kPa | 391.17 | Calculated Property |
| Pvap | 1039.15 | kPa | 427.48 | Calculated Property |
| Pvap | 1965.80 | kPa | 463.78 | Calculated Property |
| Pvap | 3422.90 | kPa | 500.09 | Calculated Property |
| Pvap | 5628.11 | kPa | 536.40 | Calculated Property |
Similar Compounds
Find more compounds similar to Trichloromethane.
Mixtures
- Trichloromethane + 1-Butanol
- Benzene + Trichloromethane + 1-Butanol
- Trichloromethane + Ethane, 1,2-dibromo-
- Trichloromethane + Ethanol
- Benzene + Trichloromethane
- Benzene + Trichloromethane + Ethanol
- Betulin + Trichloromethane
- Betulin + Trichloromethane + Methyl Alcohol
- Trichloromethane + Cyclopentanone
- Trichloromethane + Cyclohexanone
- Trichloromethane + Tetrahydrofuran
- Trichloromethane + Cyclohexane
- Trichloromethane + Tetrahydrofuran + Cyclohexane
- Trichloromethane + Aziridine, 2-methyl- + Water
- Trichloromethane + Ethanol + Thiophene, tetrabromo-
- Trichloromethane + Thiophene, tetrabromo-
- Trichloromethane + Methane, nitro-
- Trichloromethane + Water
- Trichloromethane + Phosphoramidic acid, phenyl-, diphenyl ester
- Trichloromethane + 2-Propanone, 1-hydroxy- + Water
Find more mixtures with Trichloromethane.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Dortmund Data Bank Vapor-Liquid Equilibrium Data
- Temperature Dependence of Densities and Excess Molar Volumes of the Ternary Mixture (1-Butanol + Chloroform + Benzene) and its Binary Constituents (1-Butanol + Chloroform and 1-Butanol + Benzene)
- Isobaric vapour liquid equilibria for binary mixtures of 1,2-dibromoethane with 1,2-dichloroethane, trichloromethane, and 1,1,2,2-tetrachloroethane at atmospheric pressure
- Liquid liquid equilibria for the system (water + carboxylic acid + chloroform): Thermodynamic modeling
- Volumetric properties of the ternary system ethanol + chloroform + benzene at temperature range (288.15 313.15) K: Experimental data, correlation and prediction by cubic EOS
- Solubility of naproxen in several organic solvents at different temperatures
- Hydrogen substitution effect on the solubility of perhalogenated compounds in ionic liquid [bmim][PF6]
- Solubilities of betulin in chloroform + methanol mixed solvents at T = (278.2, 288.2, 293.2, 298.2, 308.2 and 313.2) K
- Vapour pressure and excess Gibbs energy of binary 1,2-dichloroethane + cyclohexanone, chloroform + cyclopentanone and chloroform + cyclohexanone mixtures at temperatures from 298.15 to 318.15 K
- Experimental measurements and correlations of vapor liquid equilibrium data for the binary system of chloroform +N,N-dimethylformamide at 101.3 kPa
- Determination of vapour-liquid and vapour-liquid-liquid equilibrium of the chloroform-water and trichloroethylene-water binary mixtures
- Excess Gibbs energies and volumes of the ternary system chloroform + tetrahydrofuran + cyclohexane at 298.15 K
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Thermodynamics of the solubility of lomefloxacin in methanol, ethanol, 1-propanol, 2-propanol, acetone, and chloroform from 293.15 to 323.15 K
- Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
- The choice of solvent and liquid liquid equilibrium for ternary water + 2-methylaziridine + chloroform system: Experimental data and modeling
- Solubility of 1, 3, 2-dioxaphosphorinane-5,5-dimethyl -2- (2,4,6-tribromophenoxy)-2-oxide in selected solvents
- Solubility and solution thermodynamics of 2,3,4,5-tetrabromothiophene in (ethanol + trichloromethane) binary solvent mixtures
- Thermostabilities and solubilities of flame retardant bisphenol S-bis (5,5-dimethyl-1,3-dioxaphosphorinanyl-2-oxy phosphate ester) as a function of temperature
- Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
- Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
- Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
- The role of organic diluents in the aspects of equilibrium, kinetics and thermodynamic model for silver ion extraction using an extractant D2EHPA
- Solid-liquid equilibrium of diphenyl anilinophosphonate in the different organic solvents
- Measurement and correlation of solid-liquid equilibria for three binaries, ethanol-antipyrine, chloroform-antipyrine, and dimethyl ether-antipyrine
- Liquid-liquid equilibria and COSMO-SAC modeling of organic solvent/ ionic liquid - hydroxyacetone - water mixtures
- Isobaric vapor-liquid equilibrium for chloroform + isopropanol + 1,3-dimethylimidazolium dimethylphosphate at 101.3 kPa
- Isobaric vapor-liquid equilibrium for chloroform + ethanol + 1,3- dimethylimidazolium dimethylphosphate at 101.3 kPa
- Densities, viscosities, and refractive indices of binary and ternary mixtures of methanol, acetone, and chloroform at temperatures from (298.15-318.15) K and ambient pressure
- Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
- Densities, viscosities, and ultrasonic velocity studies of binary mixtures of trichloromethane with methanol, ethanol, propan-1-ol, and butan-1-ol at T=(298.15 and 308.15) K
- Density, viscosity, isothermal (vapour + liquid) equilibrium, excess molar volume, viscosity deviation, and their correlations for chloroform + methyl isobutyl ketone binary system
- Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
- Phase diagrams of (vapour + liquid) equilibrium for binary mixtures of a,a,a-trifluorotoluene with ethanol, or benzene, or chloroform at pressure 101.4 kPa
- Volumetric behaviour of binary mixtures of (trichloromethane + amines) at temperatures between T = (288.15 and 303.15) K at p = 0.1 MPa
- Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- Measurement and correlation of the solubility of 2,3,4,5-tetrabromothiophene in different solvents
- Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
- Henry s constants and activity coefficients of some organic solutes in 1-butyl,3-methylimidazolium hydrogen sulfate and in 1-methyl,3-trimethylsilylmethylimidazolium chloride
- Thermo-physical properties of 1,3,4-oxadiazole derivatives in pure solvents
- Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
- Solubilities of evodiamine in twelve organic solvents from T = (283.2 to 323.2) K
- Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
- Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
- Thermo-acoustical studies of 1,3,4-oxadiazole as binary mixture at three different temperatures
- 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
- Measurement, correlation and dissolution thermodynamics of biological active chalcone in organic solvents at different temperatures
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium methyl sulfate
- Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
- Solubility of daidzin in different organic solvents and (ethyl alcohol + water) mixed solvents
- Measurement and correlation of the solubility of genistin in eleven organic solvents from T = (283.2 to 323.2) K
- Solubility measurement and modelling of 1,8-dinitronaphthalene in nine organic solvents from T = (273.15 to 308.15) K and mixing properties of solutions
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-hexyl-2,3-dimethylimidazolium bis(trifluoromethylsulfonyl)imide
- Thermodynamic modelling for solubility of 5-chloro-1-methyl-4-nitroimidazole in eleven organic solvents from T = (283.15 to 318.15) K
- Thermodynamic study of solubility for 2-amino-4-chloro-6-methoxypyrimidine in twelve organic solvents at temperatures from 273.15 K to 323.15 K
- Determination and correlation of solubility of 11alpha,17alpha-dihydroxy-4-pregnene-3,20-dione in different solvents
- Thermodynamic functions for solubility of 2-mercaptobenzothiazole in eleven pure organic solvents at temperatures from 273.15 K to 318.15 K and mixing properties of solutions
- Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
- Separation of azeotrope (2,2,3,3-tetrafluoro-1-propanol + water): Isobaric vapour-liquid phase equilibrium measurements and azeotropic distillation
- Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
- Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
- Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
- Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
- Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
- Liquid-liquid equilibrium study for ternary systems of water + propargyl alcohol + solvents at 308.2 K: Measurement and thermodynamic modelling
- Speeds of sound, isentropic compressibilities, viscosities, and excess molar volumes of binary mixtures of alkanoates with tetra- and trichloromethanes at 303.15 K
- Densities, speeds of sound, isentropic compressibilities, refractive indexes, and viscosities of tetrahydrofuran with haloalkane or alkyl ethanoate at T = 303.15 K
- Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
- Topological and thermodynamic investigations of molecular interactions of aniline and o-toluidine with chloroform
- Excess volumes, Viscosities, and Excess Gibbs Energy of Activation for Viscous Flow, for binary and ternary mixtures 1- propanol + N-N dimethylformamid + chloroform at different temperatures
- Low cost apparatus for rapid boiling point determination of small air sensitive samples under inert atmosphere
- Solubilities of Phosphoramidic Acid, N-(phenylmethyl)-, Diphenyl Ester in Selected Solvents
- Dissociation Constants and Solubilities of Dalbergin and Nordalbergin in Different Solvents
- Investigation of Surface and Solubility Properties of N-Vinylimidazolium Tetrahalogenidoferrate(III) Magnetic Ionic Liquids Using Density Functional Theory
- Comparing Composition- and Temperature-Dependent Viscosities of Binary Systems Involving Ionic Liquids
- Measurement and Correlation of the Solubility for Camptothecine in Different Organic Solvents
- Solubility Measurement and Thermodynamic Modeling of 4-Nitrophthalimide in Twelve Pure Solvents at Elevated Temperatures Ranging from (273.15 to 323.15) K
- Solubility Measurement and Correlation for e-2,4,6,8,10,12-Hexanitro-2,4,6,8,10,12-hexaazaisowurtzitane in Five Organic Solvents at Temperatures between 283.15 and 333.15 K and Different Chloralkane + Ethyl Acetate Binary Solvents at Temperatures between 283.15 and 323.15 K
- Measurement and Correlation of the Solubility of e-CL-20 in 12 Organic Solvents at Temperatures Ranging from 278.15 to 318.15 K
- Measurements and Thermodynamic Models for the Separation of 2-Methoxyethanol and Water Azeotropic Mixtures via Different Solvents
- Measurement and Thermodynamic Modeling of Ternary (Liquid + Liquid) Equilibrium for Extraction of N,N-Dimethylacetamide from Aqueous Solution with Different Solvents
- Solid Liquid Phase Equilibrium of N,N'-Piperazinebis(neopentylglycol)phosphoramidate in Selected Solvents from T = (293.15 to 333.15) K
- Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
- Synthesis and Solubility of 5,5-Dimethyl-2-(phenyl(phenylamino)methyl)-1,3,2-dioxaphosphinane 2-oxide in Selected Solvents between 278.15 K and 347.15 K
- Measurement and Correlation of Solubility of Resorcinol Bis(cyclic 2,2-dimethyl-1,3-propanediol phosphate) in Selected Solvents from T = 293.15 to 333.15 K
- Measurement and Correlation of the Dissolution Equilibria of o-Iodoaniline and p-Iodoaniline in Pure Solvents
- Determination, Correlation, and Application of Sodium l-Ascorbate Solubility in Nine Pure Solvents and Two Binary Solvents at Temperatures from 278.15 to 323.15 K
- Determination and Thermodynamic Analysis of the Solubility of Limonin in Eight Organic Solvents and Ethyl Acetate + 2-Propanol Binary Solvents from 283.2 to 323.2 K
- Solubility Measurement and Thermodynamic Modeling of Benzoic Acid in Monosolvents and Binary Mixtures
- Determination of Activity Coefficients at Infinite Dilution of Organic Solutes in the Ionic Liquid 1-(2-Hydroxyethyl)-3-methylimidazolium Nonafluoro-1-butanesulfonate Using Gas-Liquid Chromatography
- Solubilities of Organic Semiconductors and Nonsteroidal Anti-inflammatory Drugs in Pure and Mixed Organic Solvents: Measurement and Modeling with Hansen Solubility Parameter
- Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
- Isobaric Vapor-Liquid Phase Equilibrium Measurements for Allyl Alcohol with Chloroform, Ethyl Acetate, and Methyl Propionate at 101.3 kPa
- Liquid-Liquid Equilibrium for the Ternary System of 3-Mercaptopropionic Acid + Water + Trichloromethane
- Measurement and Correlation of the Solubility of 2-Cyanoacetamide in 14 Pure Solvents and the Mixing Properties of Solutions
- Equilibrium Solubility, Model Correlation, and Solvent Effect of Indole-3-acetic Acid in Twelve Pure Solvents
- Thermodynamic Studies of Solubility for Naphthalene in 12 Solvents from 279 to 330 K
- Solubility and Thermodynamic Modeling of Dimethyl Terephthalate in Pure Solvents and the Evaluation of the Mixing Properties of the Solutions
- Viscosity and Density for Binary Mixtures of Carbon Tetrachloride + Chloroform, Carbon Tetrachloride + Dichloromethane, and Chloroform + Dichloromethane and One Ternary Mixture of Chloroform + 1:1 (Carbon Tetrachloride + Dichloromethane) at 303.15 K
- Measurement of Activity Coefficients of Solutes at Infinite Dilution in (Dimethyl Sulfoxide + Acetamide, or Formamide, or Urea) Using Gas Liquid Chromatography at the Temperature 298.15 K
- Total Vapor Pressure Measurements for 2-Ethoxyethanol with Carbon Tetrachloride, Chloroform, and Dichloromethane at 303.15 K
- Density, Viscosity, and Excess Properties of Binary Liquid Mixtures of Propylene Carbonate with Polar and Nonpolar Solvents
- Phase Separation in Binary Mixtures Containing Linear Perfluoroalkanes
- Solid-Liquid Equilibria for Benzoic Acid + p-Toluic Acid + Chloroform, Benzoic Acid + p-Toluic Acid + Acetic Acid, and Terephthalic Acid + Isophthalic Acid + N,N-Dimethylformamide
- Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Propan-1-ol and Butan-1-ol at (303.15 and 313.15) K
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
- Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Pentan-1-ol, Hexan-1-ol, and Heptan-1-ol at (303.15 and 313.15) K
- Solubility of Erythromycin A Dihydrate in Different Pure Solvents and Acetone + Water Binary Mixtures between 293 K and 323 K
- Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
- Thermodynamic Properties of Mixtures Containing Ionic Liquids: Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Propyl Boronic Acid-3-Alkylimidazolium Bromide and 1-Propenyl-3-alkylimidazolium Bromide Using Inverse Gas Chromatography
- Density, Viscosity, Vapor-Liquid Equilibrium, Excess Molar Volume, Viscosity Deviation, and Their Correlations for the Chloroform + 2-Butanone Binary System
- Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Octan-1-ol and Decan-1-ol at (303.15 and 313.15) K
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Volumetric Properties of the Binary Methanol + Chloroform and Ternary Methanol + Chloroform + Benzene Mixtures at (288.15, 293.15, 298.15, 303.15, 308.15, and 313.15) K
- Solubility of Physalin D in Ethanol, Methanol, Propanone, Trichloromethane, Ethyl Ethanoate, and Water at Temperatures from (283.2 to 313.2) K
- Solubilities of Phosphorus-Containing Compounds in Selected Solvents
- Partial Molar Volumes of N,N'-1,2-Ethyl-bis(salicyladimine) Schiff Base (Salen) in Organic Solvents at T = (283.15 to 318.15) K
- Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
- Solubility and Crystal Size of Sirolimus in Different Organic Solvents
- Solubility of Benzoic Acid in Pure Solvents and Binary Mixtures
- Liquid-Liquid Equilibrium, Solid-Liquid Equilibrium, Densities, and Refractivity of a Water, Chloroform, and Acetylacetone Mixture
- Solubilities of N-[(4-Bromo-3,5-difluorine)-phenyl]maleimide in Pyridine, Acetone, Tetrahydrofuran, Ethanol, Trichloromethane, and Acetonitrile at Temperature between (285.00 and 350.15) K
- Density, Viscosity, Vapor-Liquid Equilibrium, and Excess Molar Enthalpy of [Chloroform + Methyl tert-Butyl Ether]
- Solubilities of Phenylphosphinic Acid, Methylphenylphosphinic Acid, Hexachlorocyclotriphosphazene, and Hexaphenoxycyclotriphosphazene in Selected Solvents
- Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
- Measurement and Correlation of the Solubility of Prednisone Acetate in Different Solvents
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Butyl-3-methylimidazolium Nitrate Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
- Solubilities of Tris(o-phenylenedioxy)cyclotriphosphazene in Selected Solvents
- Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
- Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
- Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
- Solubilities of 3-Methoxy-N-phenylaniline and 3-(Methylthio)-N-phenylaniline in Five Organic Solvents (285 K to 333.75 K)
- Crystal Structures, Reaction Rates, and Selected Physical Properties of Halo-Boronsubphthalocyanines (Halo = Fluoride, Chloride, and Bromide)
- Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Solubilities of 4,4'-Dichlorodiphenyl Disulfide in Six Organic Solvents between (303.15 and 333.15) K
- Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
- Solubilities of 4-Amino-4?-nitrodiphenyl Sulfide in Six Organic Solvents from 287.45 K to 365.55 K
- Solubilities of Rutaecarpine in Twelve Organic Solvents from (283.2 to 323.2) K
- Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
- Solubilities of 1,3,2-Dioxaphosphorinane-2-methanol-a,a-5,5-tetramethyl 2-oxide in Selected Solvents at 273.15 K to 343.15 K
- Isobaric Vapor Liquid Equilibrium for Chloroform + Methanol + 1,3-Dimethylimidazolium Dimethylphosphate at 101.3 kPa
- Solubility of Benzyl Disulfide in Five Organic Solvents between (283.45 and 333.15) K
- Solubilities of Phosphonic Acid, P,P'-(1,4-Piperazinediyl)bis-,P,P,P',P'-tetraphenyl Ester in Selected Solvents
- Solubility of 3,4-Bis(3-nitrofurazan-4-yl)furoxan in Common Solvents at Temperatures between 293.15 K and 313.15 K
- Solubility of 1-Fluoro-4-(methylsulfonyl)benzene in Five Pure Organic Solvents at Temperatures from (288.40 to 331.50) K
- Solubilities of 4-(Hydroxymethyl)-1-oxido-2,6,7-trioxa-1-phosphabicyclo[2.2.2]octane in Organic Solvents
- Thermodynamics of Fluconazole Solubility in Various Solvents at Different Temperatures
- Dissociation Constants and Solubilities of Daidzein and Genistein in Different Solvents
- Solid Liquid Phase Equilibria of N,N'-[1,3-Phenylenebis(methylene)]bis(phosphoramidic acid) P,P,P',P'-Tetraphenyl Ester in 10 Pure Solvents
- Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
- Investigation of Surface Properties and Solubility of 1-Vinyl-3-alkyl/Esterimidazolium Halide Ionic Liquids by Density Functional Methods
- Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
- Solubilities of 1,3,2-Dioxaphosphorinane-2-methanol-a,5,5-trimethyl-a-phenyl-2-oxide in Selected Solvents between 278.15 K and 343.15 K
- Solid Liquid Phase Equilibrium of Phosphoramidic acid, N,N'-1,2-Ethanediylbis-P,P,P',P'-tetraphenyl Ester in Selected Solvents
- Measurement and Correlation of the Solubility for 4,4'-Diaminodiphenylmethane in Different Solvents
- Solubilities of Betulin in Fourteen Organic Solvents at Different Temperatures
- Study of Vapor-Liquid Equilibrium for Binary Mixtures (Chloroform + 2,2,2-Trifluoroethanol) and (r,r,r-Trifluorotoluene + 2,2,2-Trifluoroethanol) at Pressure 102 kPa
- Densities and Excess Molar Volumes of the Binary 1-Propanol + Chloroform and 1-Propanol + Benzene and Ternary 1-Propanol + Chloroform + Benzene Mixtures at (288.15, 293.15, 298.15, 303.15, 308.15, and 313.15) K
- Solubility of Irbesartan (Form A) in Different Solvents between 278 K and 323 K
- Solubility of Imidacloprid in Different Solvents
- Phase Equilibria of Acrylonitrile and p-Bromobenzaldehyde in Carbon Dioxide
- Diffusion Coefficients of Organic Compounds at Infinite Dilution in Mixtures Involving Associating Compounds. Experimental Determination and Modeling by Group Contribution Methods
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas Liquid Chromatography
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas Liquid Chromatography
- Solubility of Rifapentine in Different Organic Solvents
- Densities and Excess Molar Volumes of the Ternary Mixture 2-Butanol + Chloroform + Benzene and Binary Mixtures 2-Butanol + Chloroform, or + Benzene over the Temperature Range (288.15 to 313.15) K
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Solubility of Pyoluteorin in Water, Dichloromethane, Chloroform, and Carbon Tetrachloride from (278.2 to 333.2) K
- Solubility of the Antimicrobial Agent Triclosan in Organic Solvents of Different Hydrogen Bonding Capabilities at Several Temperatures
- Solubility of Artemisinin in Seven Different Pure Solvents from (283.15 to 323.15) K
- Isobaric Vapor-Liquid and Liquid-Liquid Equilibria for Chloroform + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
- Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
- Solubility of Fluorene in Benzene, Chloroform, Acetone, 1-Propanol, Isobutanol, and Methylbenzene from (283 to 323) K
- Solubility of Adipic Acid in Acetone, Chloroform, and Toluene
- Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
- Solubility of 2-Aminopyridine in Acetone, Chloroform, and Ethyl Acetate
- Solubility of Valsartan in Different Organic Solvents and Ethanol + Water Binary Mixtures from (278.15 to 313.15) K
- Solubility of Canthaxanthin in Pure Solvents from (293.15 to 343.15) K
- Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
- Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
- Solubility of Ofloxacin in 1,2-Dichloromethane, Chloroform, Carbon Tetrachloride, and Water from (293.15 to 313.15) K
- Isobaric Vapor-Liquid and Liquid-Liquid Equilibria for Chloroform + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Solubilities of Sulfadiazine in Methanol, Ethanol, 1-Propanol, 2-Propanol, Acetone, and Chloroform from (294.15 to 318.15) K
- Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
- Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
- 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.