- 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.
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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] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 72 74 76 78 80 82 350 400 450 500 | ||||
| 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] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 115 120 125 130 135 140 295 300 | ||||
| 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] |
|
|
T(K) Dynamic viscosity (Pa×s) 4.50e-4 5.00e-4 5.50e-4 6.00e-4 6.50e-4 7.00e-4 280 290 300 310 | ||||
| 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] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 29 30 31 32 33 34 35 300 400 500 | ||||
| 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] |
|
|
T(K) Vapor pressure (kPa) 40 60 80 100 120 310 320 330 340 | ||||
| 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] |
|
|
|
T(K) Refractive Index 1.44 1.44 1.45 1.45 1.45 285 290 295 300 | ||||
| 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] |
|
|
T(K) Liquid Density (kg/m3) 1430 1440 1450 1460 1470 1480 1490 1500 290 300 310 320 | ||||
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 300 400 500 | ||||
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 300 400 500 | ||||
| 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
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