- InChI
- InChI=1S/C2Cl4/c3-1(4)2(5)6
- InChI Key
- CYTYCFOTNPOANT-UHFFFAOYSA-N
- Formula
- C2Cl4
- SMILES
- ClC(Cl)=C(Cl)Cl
- Molecular Weight1
- 165.83
- CAS
- 127-18-4
- Other Names
-
- 1,1,2,2-Tetrachloroethene
- 1,1,2,2-Tetrachloroethylene
- Ankilostin
- Antisal 1
- Antisol 1
- C2Cl4
- Carbon bichloride
- Carbon dichloride
- Czterochloroetylen
- Didakene
- Dilatin PT
- Dow-per
- ENT 1,860
- ETHYLENE TETRACHLORIDE
- Ethene, tetrachloro-
- Ethylene, tetrachloro-
- F 1110
- Fedal-Un
- Freon 1110
- NCI-C04580
- Nema
- Nema, veterinary
- PERC
- PERK
- PerSec
- Perawin
- Perchloorethyleen, per
- Perchlor
- Perchloraethylen, per
- Perchlorethylene
- Perchlorethylene, per
- Perchloroethene
- Perchloroethylene
- Perclene
- Perclene D
- Perclene TG
- Percloroetilene
- Percosolve
- Perklone
- RCRA Waste Number U210
- TETLEN
- TETRACHLOROETHENE
- Tetracap
- Tetrachlooretheen
- Tetrachloraethen
- Tetrachlorethylene
- Tetracloroetene
- Tetraguer
- Tetraleno
- Tetralex
- Tetravec
- Tetroguer
- Tetropil
- UN 1897
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- EA : Electron affinity (eV).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- 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.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | -830.00 ± 10.00 | kJ/mol | NIST |
| μ | 0.00 | debye | KDB |
| η | [0.0008474; 0.0008900] | Pa×s |
|
| η | 0.0008474 | Pa×s | Densiti... |
| η | 0.0008900 | Pa×s | Studies... |
| EA | [0.50; 0.64] | eV |
|
| EA | 0.64 ± 0.03 | eV | NIST |
| EA | 0.50 | eV | NIST |
| ΔfG° | 22.61 | kJ/mol | KDB |
| ΔfH°gas | [-24.00; -12.14] | kJ/mol |
|
| ΔfH°gas | -12.14 | kJ/mol | KDB |
| ΔfH°gas | -24.00 ± 4.00 | kJ/mol | NIST |
| ΔfH°gas | -15.00 | kJ/mol | NIST |
| ΔfH°liquid | [-64.00; -54.40] | kJ/mol |
|
| ΔfH°liquid | -64.00 ± 4.00 | kJ/mol | NIST |
| ΔfH°liquid | -54.40 | kJ/mol | NIST |
| ΔfusH° | 15.31 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [39.70; 39.72] | kJ/mol |
|
| ΔvapH° | 39.72 | kJ/mol | NIST |
| ΔvapH° | 39.72 ± 0.05 | kJ/mol | NIST |
| ΔvapH° | 39.70 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 39.70 ± 0.84 | kJ/mol | NIST |
| IE | [9.32; 9.51] | eV |
|
| IE | 9.33 ± 0.00 | eV | NIST |
| IE | 9.33 ± 0.00 | eV | NIST |
| IE | 9.51 | eV | NIST |
| IE | 9.34 | eV | NIST |
| IE | 9.32 ± 0.01 | eV | NIST |
| IE | 9.32 | eV | NIST |
| IE | 9.50 | eV | NIST |
| log10WS | [-2.60; -2.54] |
|
|
| log10WS | -2.60 | Aq. Sol... | |
| log10WS | -2.54 | Estimat... | |
| logPoct/wat | 3.068 | Crippen Calculated Property | |
| McVol | 83.700 | ml/mol | McGowan Calculated Property |
| Pc | 4760.00 | kPa | KDB |
| Inp | [785.00; 832.30] |
|
|
| Inp | 825.59 | NIST | |
| Inp | Outlier 832.30 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 799.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 809.00 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 825.00 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 815.45 | NIST | |
| Inp | 817.10 | NIST | |
| Inp | 815.90 | NIST | |
| Inp | 794.80 | NIST | |
| Inp | 809.30 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 796.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 807.00 | NIST | |
| Inp | 796.52 | NIST | |
| Inp | 819.00 | NIST | |
| Inp | 823.00 | NIST | |
| Inp | 794.00 | NIST | |
| Inp | 808.00 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 808.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 794.51 | NIST | |
| Inp | 794.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 811.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 793.00 | NIST | |
| Inp | 793.00 | NIST | |
| Inp | 811.00 | NIST | |
| Inp | 797.00 | NIST | |
| Inp | 816.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 797.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 796.00 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 794.00 | NIST | |
| Inp | 793.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 796.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 823.00 | NIST | |
| I | [1012.00; 1059.96] |
|
|
| I | 1044.00 | NIST | |
| I | 1038.00 | NIST | |
| I | 1050.23 | NIST | |
| I | Outlier 1059.96 | NIST | |
| I | 1036.20 | NIST | |
| I | 1030.00 | NIST | |
| I | 1024.00 | NIST | |
| I | 1022.00 | NIST | |
| I | 1022.00 | NIST | |
| I | 1021.00 | NIST | |
| I | 1026.00 | NIST | |
| I | 1045.00 | NIST | |
| I | 1012.00 | NIST | |
| I | 1012.00 | NIST | |
| I | 1018.00 | NIST | |
| I | 1021.00 | NIST | |
| I | 1024.00 | NIST | |
| I | 1044.00 | NIST | |
| I | 1030.00 | NIST | |
| S°liquid | 240.60 | J/mol×K | NIST |
| Tboil | [394.15; 394.45] | K |
|
| Tboil | 394.40 | K | KDB |
| Tboil | 394.45 | K | Excess ... |
| Tboil | 394.15 | K | Excess ... |
| Tboil | 394.15 | K | Vapor-L... |
| Tboil | 394.15 | K | Isobari... |
| Tc | [620.00; 620.20] | K |
|
| Tc | 620.20 | K | KDB |
| Tc | 620.00 | K | NIST |
| Tfus | [250.60; 251.00] | K |
|
| Tfus | 250.80 | K | KDB |
| Tfus | 251.00 | K | Aq. Sol... |
| Tfus | 250.97 ± 0.05 | K | NIST |
| Tfus | 250.60 ± 0.60 | K | NIST |
| Ttriple | 250.81 ± 0.02 | K | NIST |
| Vc | 0.326 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [100.86; 114.10] | J/mol×K | [398.80; 620.38] |
|
| Cp,gas | 100.86 | J/mol×K | 398.80 | Joback Calculated Property |
| Cp,gas | 103.82 | J/mol×K | 435.73 | Joback Calculated Property |
| Cp,gas | 106.43 | J/mol×K | 472.66 | Joback Calculated Property |
| Cp,gas | 108.74 | J/mol×K | 509.59 | Joback Calculated Property |
| Cp,gas | 110.77 | J/mol×K | 546.52 | Joback Calculated Property |
| Cp,gas | 112.54 | J/mol×K | 583.45 | Joback Calculated Property |
| Cp,gas | 114.10 | J/mol×K | 620.38 | Joback Calculated Property |
| Cp,liquid | [139.70; 157.90] | J/mol×K | [298.00; 298.15] |
|
| Cp,liquid | 139.70 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 146.90 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 147.16 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 157.90 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 146.50 | J/mol×K | 298.15 | NIST |
| ΔfusH | [0.82; 10.88] | kJ/mol | [210.00; 250.81] |
|
| ΔfusH | 0.82 | kJ/mol | 210.00 | NIST |
| ΔfusH | 10.88 | kJ/mol | 250.80 | NIST |
| ΔfusH | 10.88 | kJ/mol | 250.80 | NIST |
| ΔfusH | 10.88 | kJ/mol | 250.81 | NIST |
| ΔvapH | [34.68; 38.90] | kJ/mol | [340.00; 394.20] |
|
| ΔvapH | 38.90 | kJ/mol | 340.00 | NIST |
| ΔvapH | 38.40 | kJ/mol | 350.00 | NIST |
| ΔvapH | 38.70 | kJ/mol | 351.50 | NIST |
| ΔvapH | 37.60 | kJ/mol | 353.00 | NIST |
| ΔvapH | 34.68 | kJ/mol | 394.10 | NIST |
| ΔvapH | 34.73 | kJ/mol | 394.20 | KDB |
| Pvap | [1.02; 8.29] | kPa | [283.15; 323.15] |
|
| Pvap | 1.02 | kPa | 283.15 | Isother... |
| Pvap | 1.02 | kPa | 283.15 | Total v... |
| Pvap | 1.02 | kPa | 283.15 | Total v... |
| Pvap | 1.40 | kPa | 288.15 | Total v... |
| Pvap | 1.40 | kPa | 288.15 | Total v... |
| Pvap | 1.40 | kPa | 288.15 | Isother... |
| Pvap | 1.86 | kPa | 293.15 | Total v... |
| Pvap | 1.86 | kPa | 293.15 | Total v... |
| Pvap | 1.86 | kPa | 293.15 | Isother... |
| Pvap | 2.46 | kPa | 298.15 | Isother... |
| Pvap | 2.46 | kPa | 298.15 | Total v... |
| Pvap | 2.46 | kPa | 298.15 | Total v... |
| Pvap | 3.21 | kPa | 303.15 | Total v... |
| Pvap | 3.21 | kPa | 303.15 | Isother... |
| Pvap | 3.21 | kPa | 303.15 | Total v... |
| Pvap | 4.12 | kPa | 308.15 | Total v... |
| Pvap | 4.12 | kPa | 308.15 | Isother... |
| Pvap | 4.12 | kPa | 308.15 | Total v... |
| Pvap | 5.25 | kPa | 313.15 | Total v... |
| Pvap | 5.25 | kPa | 313.15 | Total v... |
| Pvap | 5.25 | kPa | 313.15 | Isother... |
| Pvap | 6.62 | kPa | 318.15 | Isother... |
| Pvap | 6.62 | kPa | 318.15 | Total v... |
| Pvap | 6.62 | kPa | 318.15 | Total v... |
| Pvap | 8.29 | kPa | 323.15 | Total v... |
| Pvap | 8.29 | kPa | 323.15 | Total v... |
| Pvap | 8.29 | kPa | 323.15 | Isother... |
| n0 | [1.49780; 1.50580] | [293.15; 308.15] |
|
|
| n0 | 1.50500 | 293.15 | Activit... | |
| n0 | 1.50580 | 293.15 | Excess ... | |
| n0 | 1.50500 | 293.15 | Bubble ... | |
| n0 | 1.50580 | 293.15 | Vapor-L... | |
| n0 | 1.50500 | 298.15 | Bubble ... | |
| n0 | 1.50320 | 298.15 | Bubble-... | |
| n0 | 1.50500 | 298.15 | Bubble ... | |
| n0 | 1.50360 | 298.15 | Density... | |
| n0 | 1.50360 | 298.15 | Density... | |
| n0 | 1.50050 | 303.15 | Density... | |
| n0 | 1.50100 | 303.15 | Density... | |
| n0 | 1.49780 | 308.15 | Density... | |
| n0 | 1.49800 | 308.15 | Density... | |
| ρl | [1590.60; 1622.39] | kg/m3 | [293.00; 313.15] |
|
| ρl | 1620.00 | kg/m3 | 293.00 | KDB |
| ρl | 1622.39 | kg/m3 | 293.15 | Thermop... |
| ρl | 1614.49 | kg/m3 | 298.15 | Excess ... |
| ρl | 1614.80 | kg/m3 | 298.15 | Excess ... |
| ρl | 1607.20 | kg/m3 | 303.15 | Excess ... |
| ρl | 1597.90 | kg/m3 | 308.15 | Excess ... |
| ρl | 1590.60 | kg/m3 | 313.15 | Excess ... |
| ΔfusS | [3.90; 43.38] | J/mol×K | [210.00; 250.81] |
|
| ΔfusS | 3.90 | J/mol×K | 210.00 | NIST |
| ΔfusS | 43.38 | J/mol×K | 250.80 | NIST |
| ΔfusS | 43.38 | J/mol×K | 250.81 | NIST |
| csound,fluid | [1038.97; 1054.03] | m/s | [293.15; 298.15] |
|
| csound,fluid | 1054.03 | m/s | 293.15 | Densiti... |
| csound,fluid | 1038.97 | m/s | 298.15 | Densiti... |
| γ | 0.03 | N/m | 293.20 | KDB |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 308.15 | 101.00 | 0.0007 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 203.96] | kPa | [286.48; 421.37] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.42797e+01 | |||
| Coefficient B | -3.36251e+03 | |||
| Coefficient C | -4.61640e+01 | |||
| Temperature range, min. | 286.48 | |||
| Temperature range, max. | 421.37 | |||
| Pvap | 1.33 | kPa | 286.48 | Calculated Property |
| Pvap | 3.03 | kPa | 301.47 | Calculated Property |
| Pvap | 6.29 | kPa | 316.46 | Calculated Property |
| Pvap | 12.10 | kPa | 331.44 | Calculated Property |
| Pvap | 21.79 | kPa | 346.43 | Calculated Property |
| Pvap | 37.10 | kPa | 361.42 | Calculated Property |
| Pvap | 60.21 | kPa | 376.41 | Calculated Property |
| Pvap | 93.67 | kPa | 391.39 | Calculated Property |
| Pvap | 140.48 | kPa | 406.38 | Calculated Property |
| Pvap | 203.96 | kPa | 421.37 | Calculated Property |
| Pvap | [0.11; 4603.17] | kPa | [250.80; 620.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.04740e+01 | |||
| Coefficient B | -6.53097e+03 | |||
| Coefficient C | -6.66587e+00 | |||
| Coefficient D | 3.52238e-06 | |||
| Temperature range, min. | 250.80 | |||
| Temperature range, max. | 620.00 | |||
| Pvap | 0.11 | kPa | 250.80 | Calculated Property |
| Pvap | 1.75 | kPa | 291.82 | Calculated Property |
| Pvap | 12.55 | kPa | 332.84 | Calculated Property |
| Pvap | 55.13 | kPa | 373.87 | Calculated Property |
| Pvap | 173.62 | kPa | 414.89 | Calculated Property |
| Pvap | 432.94 | kPa | 455.91 | Calculated Property |
| Pvap | 912.80 | kPa | 496.93 | Calculated Property |
| Pvap | 1701.91 | kPa | 537.96 | Calculated Property |
| Pvap | 2896.38 | kPa | 578.98 | Calculated Property |
| Pvap | 4603.17 | kPa | 620.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Tetrachloroethylene.
Mixtures
- Tetrachloroethylene + 1-Hexanol
- Benzene + Tetrachloroethylene
- Tetrachloroethylene + Carbon Tetrachloride
- Phenol, 2-methyl- + Tetrachloroethylene
- Tetrachloroethylene + Formamide, N,N-dimethyl-
- Tetrachloroethylene + Ethane, 1,2-dibromo-
- Tetrachloroethylene + Tetrahydrofuran
- Tetrachloroethylene + Ethylbenzene
- Tetrachloroethylene + Acetamide, N-methyl-
- Tetrachloroethylene + Cyclohexane, methyl-
- p-Cresol + Tetrachloroethylene
- Tetrachloroethylene + 1-Decanol
- Tetrachloroethylene + Dimethyl Sulfoxide
- Tetrachloroethylene + 2-Pyrrolidinone, 1-methyl-
- Tetrachloroethylene + Heptane
- Benzene, nitro- + Tetrachloroethylene
- Tetrachloroethylene + Benzene, chloro-
- Tetrachloroethylene + Tributylamine
- Tetrachloroethylene + Methyl Alcohol
- Tetrachloroethylene + Ethanol
Find more mixtures with Tetrachloroethylene.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Densities, Excess Molar Volumes, Ultrasonic Speeds, and Isentropic Compressibilities of Hexan-1-ol with 1,2-Dichloroethane, 1,2-Dibromoethane, and 1,1,2,2-Tetrachloroethene at (293.15 and 298.15) K
- Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachlorethane or tetrachloroethene with benzene at nine temperatures
- Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
- Bubble points of some binary mixtures formed by o-cresol at 95.75 kPa
- Excess Gibbs energies of selected binary mixtures formed by N,N-dimethyl formamide at 95.5 kPa
- Excess volumes and speeds of sound of mixtures of 1,2-dibromoethane with chlorinated ethanes and ethenes at 303.15 K
- Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
- Bubble points of the binary mixtures formed by ethylbenzene with some chloroaliphatics and substituted benzenes at p = 94.7 kPa
- Densities and viscosities of binary liquid mixtures of N-methylacetamide with some chloroethanes and chloroethenes at T = 308.15 K
- Excess molar volumes, viscosities, and speeds of sound of the ternary mixture {1-heptanol (1) + trichloroethylene (2) + methylcyclohexane (3)} at T = 298.15 K
- Activity coefficients and excess Gibbs free energy of some binary mixtures formed by p-cresol at 95.23 kPa
- Thermophysical and sonochemical behaviour of binary mixtures of decan-1-ol with halohydrocarbons at (T = 293.15 and 313.15) K
- Relation between characteristic molecular volume and hydrophobicity of nonpolar molecules
- Excess molar enthalpies of dimethylsulfoxide with chloroethanes and chloroethenes at 298.15K
- Vapor-Liquid Equilibria and Excess Molar Enthalpies for N-Methyl-2-pyrrolidone with Chloroethanes and Chloroethenes
- Bubble Temperature Measurements on the Binary Mixtures of n-Heptane or Nitrobenzene or Chlorobenzene with Some Chloroethanes and Chloroethylenes at (94.6 to 95.8) kPa
- Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
- Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Tri-n-butylamine + Triethylamine, + Tetrahydrofuran, + Tetradecane, + Tetrachloroethylene, + Pyridine, or + Trichloroethylene at (298.15, 303.15, and 308.15) K
- Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
- Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of Anisole with 2-Chloroethanol, 1,4-Dioxane, Tetrachloroethylene, Tetrachloroethane, DMF, DMSO, and Diethyl Oxalate at (298.15, 303.15, and 308.15) K
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Isobaric Vapor Liquid Equilibrium for Dimethylsulfoxide with Chloroethanes and Chloroethenes
- Vapor-Liquid Equilibria of Binary Mixtures Formed by Hexan-1-ol with Chloroethanes and Chloroethenes at 95.6 kPa
- Studies on Transport and Thermodynamic Properties of Binary Mixtures of Hexan-1-ol with Halogenated Compounds at 293.15 K
- Excess Molar Volumes and Sound Speed in (Phenylacetonitrile + 1,2-Dichloroethane), (Phenylacetonitrile + 1,1,2-Trichloroethane), (Phenylacetonitrile + 1,1,2,2-Tetrachloroethane), (Phenylacetonitrile + Trichloroethene), and (Phenylacetonitrile + Tetrachloroethene) at Temperatures of (303.15, 308.15, and 313.15) 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.