- InChI
- InChI=1S/C2H5ClO/c3-1-2-4/h4H,1-2H2
- InChI Key
- SZIFAVKTNFCBPC-UHFFFAOYSA-N
- Formula
- C2H5ClO
- SMILES
- OCCCl
- Molecular Weight1
- 80.51
- CAS
- 107-07-3
- Other Names
-
- 1-chloro-2-hydroxyethane
- 2-Chloorethanol
- 2-Chloraethanol
- 2-Chlorethanol
- 2-Chloro-1-ethanol
- 2-Chloro-1-hydroxyethane
- 2-Chloroethyl alcohol
- 2-Cloroetanolo
- 2-Hydroxyethyl chloride
- 2-Monochloroethanol
- Aethylenechlorhydrin
- CH2ClCH2OH
- Chloroethanol
- Ethanol, 2-chloro-
- Ethene, chlorohydrin
- Ethylchlorohydrin
- Ethyleen-chloorhydrine
- Ethylene chlorhydrin
- Glicol monocloridrina
- Glycol chlorohydrin
- Glycol monochlorohydrin
- Glycolmonochloorhydrine
- Glycomonochlorhydrin
- NCI-C50135
- NSC 122289
- UN 1135
- Z-Chloroethanol
- ethane, 1-chloro-2-hydroxy-
- ethylene chlorohydrin
- ethylene glycol, chlorohydrin
- «beta»-Chloroethanol
- «beta»-Chloroethyl alcohol
- «beta»-Hydroxyethyl chloride
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (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.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | 766.10 | kJ/mol | NIST |
| BasG | 735.70 | kJ/mol | NIST |
| ΔcH°liquid | -1191.40 | kJ/mol | NIST |
| ΔfG° | -182.79 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -252.58 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 9.22 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [41.40; 48.30] | kJ/mol |
|
| ΔvapH° | 48.30 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 41.40 ± 0.03 | kJ/mol | NIST |
| IE | [10.50; 10.95] | eV |
|
| IE | Outlier 10.50 | eV | NIST |
| IE | 10.66 | eV | NIST |
| IE | 10.90 | eV | NIST |
| IE | 10.90 | eV | NIST |
| IE | 10.91 | eV | NIST |
| IE | 10.95 | eV | NIST |
| IE | 10.91 | eV | NIST |
| IE | 10.90 | eV | NIST |
| log10WS | -0.08 | Crippen Calculated Property | |
| logPoct/wat | 0.218 | Crippen Calculated Property | |
| McVol | 57.150 | ml/mol | McGowan Calculated Property |
| Pc | 5446.55 | kPa | Joback Calculated Property |
| Inp | [600.00; 680.00] |
|
|
| Inp | 633.00 | NIST | |
| Inp | 635.00 | NIST | |
| Inp | Outlier 680.00 | NIST | |
| Inp | 614.00 | NIST | |
| Inp | 633.00 | NIST | |
| Inp | 623.00 | NIST | |
| Inp | 638.00 | NIST | |
| Inp | 606.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 607.00 | NIST | |
| Inp | 629.00 | NIST | |
| Inp | 640.00 | NIST | |
| Inp | 653.00 | NIST | |
| Inp | 640.00 | NIST | |
| Inp | 643.00 | NIST | |
| Inp | 643.00 | NIST | |
| Inp | 638.00 | NIST | |
| Inp | 629.00 | NIST | |
| Inp | 640.00 | NIST | |
| Inp | 633.00 | NIST | |
| I | [1329.00; 1400.00] |
|
|
| I | 1369.00 | NIST | |
| I | 1400.00 | NIST | |
| I | 1386.00 | NIST | |
| I | 1372.00 | NIST | |
| I | 1378.00 | NIST | |
| I | 1385.00 | NIST | |
| I | 1394.00 | NIST | |
| I | 1396.00 | NIST | |
| I | 1379.00 | NIST | |
| I | 1329.00 | NIST | |
| I | 1357.00 | NIST | |
| I | 1329.00 | NIST | |
| I | 1358.00 | NIST | |
| I | 1369.00 | NIST | |
| Tboil | [401.15; 405.15] | K |
|
| Tboil | 401.20 | K | NIST |
| Tboil | 401.85 | K | NIST |
| Tboil | 401.80 ± 0.60 | K | NIST |
| Tboil | 401.75 ± 0.30 | K | NIST |
| Tboil | 401.75 ± 0.30 | K | NIST |
| Tboil | 401.75 ± 0.30 | K | NIST |
| Tboil | 401.80 ± 0.50 | K | NIST |
| Tboil | 401.15 ± 0.30 | K | NIST |
| Tboil | Outlier 405.15 ± 0.50 | K | NIST |
| Tc | 545.41 | K | Joback Calculated Property |
| Tfus | [204.15; 210.55] | K |
|
| Tfus | 210.55 | K | NIST |
| Tfus | 205.65 ± 0.40 | K | NIST |
| Tfus | 204.20 ± 1.50 | K | NIST |
| Tfus | 204.15 ± 0.50 | K | NIST |
| Vc | 0.215 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [89.75; 111.90] | J/mol×K | [374.77; 545.41] |
|
| Cp,gas | 89.75 | J/mol×K | 374.77 | Joback Calculated Property |
| Cp,gas | 93.83 | J/mol×K | 403.21 | Joback Calculated Property |
| Cp,gas | 97.74 | J/mol×K | 431.65 | Joback Calculated Property |
| Cp,gas | 101.50 | J/mol×K | 460.09 | Joback Calculated Property |
| Cp,gas | 105.11 | J/mol×K | 488.53 | Joback Calculated Property |
| Cp,gas | 108.58 | J/mol×K | 516.97 | Joback Calculated Property |
| Cp,gas | 111.90 | J/mol×K | 545.41 | Joback Calculated Property |
| η | [0.0004500; 0.0989526] | Pa×s | [203.04; 374.77] |
|
| η | 0.0989526 | Pa×s | 203.04 | Joback Calculated Property |
| η | 0.0231161 | Pa×s | 231.66 | Joback Calculated Property |
| η | 0.0074352 | Pa×s | 260.28 | Joback Calculated Property |
| η | 0.0029941 | Pa×s | 288.90 | Joback Calculated Property |
| η | 0.0014206 | Pa×s | 317.53 | Joback Calculated Property |
| η | 0.0007625 | Pa×s | 346.15 | Joback Calculated Property |
| η | 0.0004500 | Pa×s | 374.77 | Joback Calculated Property |
| ΔvapH | [39.10; 46.90] | kJ/mol | [335.00; 383.00] |
|
| ΔvapH | 45.70 | kJ/mol | 335.00 | NIST |
| ΔvapH | 46.90 | kJ/mol | 343.00 | NIST |
| ΔvapH | 43.30 | kJ/mol | 364.50 | NIST |
| ΔvapH | 39.10 | kJ/mol | 383.00 | NIST |
| Pvap | 95.30 | kPa | 399.89 | Activit... |
| n0 | [1.43260; 1.44110] | [298.15; 308.15] |
|
|
| n0 | 1.44110 | 298.15 | Density... | |
| n0 | 1.44110 | 298.15 | Density... | |
| n0 | 1.43800 | 303.15 | Density... | |
| n0 | 1.43800 | 303.15 | Density... | |
| n0 | 1.43260 | 308.15 | Density... | |
| n0 | 1.43260 | 308.15 | Density... | |
| ρl | [1170.87; 1192.12] | kg/m3 | [303.15; 318.15] |
|
| ρl | 1192.12 | kg/m3 | 303.15 | Volumet... |
| ρl | 1186.63 | kg/m3 | 308.15 | Volumet... |
| ρl | 1178.05 | kg/m3 | 313.15 | Volumet... |
| ρl | 1170.87 | kg/m3 | 318.15 | Volumet... |
Similar Compounds
Find more compounds similar to 2-Chloroethanol.
Mixtures
- 2-Chloroethanol + m-Chloroaniline
- 2-Chloroethanol + 1,4-Dioxane
- 2-Chloroethanol + Anisole
- 2-Pyrrolidinone, 1-methyl- + 2-Chloroethanol
Sources
- Crippen Method
- Crippen Method
- Volumetric, acoustic and spectroscopic properties of 3-chloroaniline with substituted ethanols at various temperatures
- Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of 1,4-Dioxane with Different Organic Liquids at (298.15, 303.15, and 308.15) K
- 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
- Activity Coefficients and Excess Gibbs Energies for Binary Mixtures of N-Methyl-2-pyrrolidone with Some Substituted Ethanols
- Joback Method
- McGowan Method
- NIST Webbook
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