- InChI
- InChI=1S/C2H5ClO/c3-1-2-4/h4H,1-2H2
- InChI Key
- SZIFAVKTNFCBPC-UHFFFAOYSA-N
- Formula
- C2H5ClO
- SMILES
- OCCCl
- Molecular Weight1
- 80.51
- 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
- 2-chloroethanol
- Aethylenechlorhydrin
- CH2ClCH2OH
- Chloroethanol
- 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
- ω : Acentric Factor.
- 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).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- 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).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.6578; 0.6776] |
|
|
| ω | 0.6776 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.6578 | ChemSep v8.3 pure component data Compiled value | |
| PAff | 766.10 | kJ/mol | NIST |
| BasG | 735.70 | kJ/mol | NIST |
| ΔcH°liquid | -1191.40 | kJ/mol | NIST |
| μ | 1.78 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -193.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | [-266.76; -258.00] | kJ/mol |
|
| ΔfH°gas | -266.76 ± 0.61 | kJ/mol | Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value |
| ΔfH°gas | -258.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| 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 | 0.75 | Relay (1.0) Calculated Property | |
| logPoct/wat | 0.218 | Crippen Calculated Property | |
| McVol | 57.150 | ml/mol | McGowan Calculated Property |
| Pc | [5799.84; 5920.00] | kPa |
|
| Pc | 5799.84 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 5920.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 2.12e-04 | kPa | ChemSep v8.3 pure component data Compiled value |
| 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 | |
| Ip | [1329.00; 1400.00] |
|
|
| Ip | 1369.00 | NIST | |
| Ip | 1400.00 | NIST | |
| Ip | 1386.00 | NIST | |
| Ip | 1372.00 | NIST | |
| Ip | 1378.00 | NIST | |
| Ip | 1385.00 | NIST | |
| Ip | 1394.00 | NIST | |
| Ip | 1396.00 | NIST | |
| Ip | 1379.00 | NIST | |
| Ip | 1329.00 | NIST | |
| Ip | 1357.00 | NIST | |
| Ip | 1329.00 | NIST | |
| Ip | 1358.00 | NIST | |
| Ip | 1369.00 | NIST | |
| Tboil | [401.15; 405.15] | K |
|
| Tboil | 401.95 | K | ChemSep v8.3 pure component data Compiled value |
| 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 | [582.00; 585.00] | K |
|
| Tc | 582.00 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 585.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [204.15; 210.55] | K |
|
| Tfus | 205.90 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 204.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | Outlier 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 |
| Ttriple | 205.65 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 3.00 | ChemSep v8.3 pure component data Compiled value | |
| URi | 3.14 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.212; 0.212] | m3/kmol |
|
| Vc | 0.212 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.212 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2580000 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [67.28; 167.79] | J/mol×K | [255.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 4.27149e+01 | |||
| Coefficient B | -5.00000e+02 | |||
| Coefficient C | 5.16224e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 255.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 67.28 | J/mol×K | 255.00 | Calculated Property |
| Cp,gas | 91.68 | J/mol×K | 393.33 | Calculated Property |
| Cp,gas | 110.87 | J/mol×K | 531.67 | Calculated Property |
| Cp,gas | 125.48 | J/mol×K | 670.00 | Calculated Property |
| Cp,gas | 136.75 | J/mol×K | 808.33 | Calculated Property |
| Cp,gas | 145.65 | J/mol×K | 946.67 | Calculated Property |
| Cp,gas | 152.82 | J/mol×K | 1085.00 | Calculated Property |
| Cp,gas | 158.71 | J/mol×K | 1223.33 | Calculated Property |
| Cp,gas | 163.63 | J/mol×K | 1361.67 | Calculated Property |
| Cp,gas | 167.79 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [108.90; 137.82] | J/mol×K | [292.50; 432.50] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 4.84700e+01 | |||
| Coefficient B | 2.06600e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 292.50 | |||
| Temperature range, max. | 432.50 | |||
| Cp,liquid | 108.90 | J/mol×K | 292.50 | Calculated Property |
| Cp,liquid | 112.11 | J/mol×K | 308.06 | Calculated Property |
| Cp,liquid | 115.33 | J/mol×K | 323.61 | Calculated Property |
| Cp,liquid | 118.54 | J/mol×K | 339.17 | Calculated Property |
| Cp,liquid | 121.76 | J/mol×K | 354.72 | Calculated Property |
| Cp,liquid | 124.97 | J/mol×K | 370.28 | Calculated Property |
| Cp,liquid | 128.18 | J/mol×K | 385.83 | Calculated Property |
| Cp,liquid | 131.40 | J/mol×K | 401.39 | Calculated Property |
| Cp,liquid | 134.61 | J/mol×K | 416.94 | Calculated Property |
| Cp,liquid | 137.82 | J/mol×K | 432.50 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0146160; 0.0004755] | Pa×s | [250.00; 401.75] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -4.42940e+01 | |||
| Coefficient B | 3.70330e+03 | |||
| Coefficient C | 4.57400e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 250.00 | |||
| Temperature range, max. | 401.75 | |||
| η | 0.0146160 | Pa×s | 250.00 | Calculated Property |
| η | 0.0077269 | Pa×s | 266.86 | Calculated Property |
| η | 0.0044828 | Pa×s | 283.72 | Calculated Property |
| η | 0.0028070 | Pa×s | 300.58 | Calculated Property |
| η | 0.0018727 | Pa×s | 317.44 | Calculated Property |
| η | 0.0013174 | Pa×s | 334.31 | Calculated Property |
| η | 0.0009693 | Pa×s | 351.17 | Calculated Property |
| η | 0.0007410 | Pa×s | 368.03 | Calculated Property |
| η | 0.0005853 | Pa×s | 384.89 | Calculated Property |
| η | 0.0004755 | Pa×s | 401.75 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [48.67; 0.00] | kJ/mol | [205.65; 585.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 5.34000e+01 | |||
| Coefficient B | 2.13900e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 5.85000e+02 | |||
| Temperature range, min. | 205.65 | |||
| Temperature range, max. | 585.00 | |||
| ΔvapH | 48.67 | kJ/mol | 205.65 | Calculated Property |
| ΔvapH | 47.46 | kJ/mol | 247.80 | Calculated Property |
| ΔvapH | 46.13 | kJ/mol | 289.95 | Calculated Property |
| ΔvapH | 44.63 | kJ/mol | 332.10 | Calculated Property |
| ΔvapH | 42.92 | kJ/mol | 374.25 | Calculated Property |
| ΔvapH | 40.92 | kJ/mol | 416.40 | Calculated Property |
| ΔvapH | 38.48 | kJ/mol | 458.55 | Calculated Property |
| ΔvapH | 35.28 | kJ/mol | 500.70 | Calculated Property |
| ΔvapH | 30.42 | kJ/mol | 542.85 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 585.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [2.12e-04; 5919.48] | kPa | [205.65; 585.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 3.14592e+01 | |||
| Coefficient B | -6.06010e+03 | |||
| Coefficient C | -1.96210e+00 | |||
| Coefficient D | 2.18670e-18 | |||
| Coefficient E | 6.00000e+00 | |||
| Temperature range, min. | 205.65 | |||
| Temperature range, max. | 585.00 | |||
| Pvap | 2.12e-04 | kPa | 205.65 | Calculated Property |
| Pvap | 0.02 | kPa | 247.80 | Calculated Property |
| Pvap | 0.57 | kPa | 289.95 | Calculated Property |
| Pvap | 6.19 | kPa | 332.10 | Calculated Property |
| Pvap | 38.37 | kPa | 374.25 | Calculated Property |
| Pvap | 161.16 | kPa | 416.40 | Calculated Property |
| Pvap | 512.81 | kPa | 458.55 | Calculated Property |
| Pvap | 1331.44 | kPa | 500.70 | Calculated Property |
| Pvap | 2971.13 | kPa | 542.85 | Calculated Property |
| Pvap | 5919.48 | kPa | 585.00 | Calculated Property |
| Pvap | [0.13; 101.78] | kPa | [269.00; 402.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.71351e+01 | |||
| Coefficient B | -4.79413e+03 | |||
| Coefficient C | -1.88440e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 269.00 | |||
| Temperature range, max. | 402.00 | |||
| Pvap | 0.13 | kPa | 269.00 | Calculated Property |
| Pvap | 0.38 | kPa | 283.78 | Calculated Property |
| Pvap | 1.00 | kPa | 298.56 | Calculated Property |
| Pvap | 2.35 | kPa | 313.33 | Calculated Property |
| Pvap | 5.12 | kPa | 328.11 | Calculated Property |
| Pvap | 10.39 | kPa | 342.89 | Calculated Property |
| Pvap | 19.80 | kPa | 357.67 | Calculated Property |
| Pvap | 35.77 | kPa | 372.44 | Calculated Property |
| Pvap | 61.62 | kPa | 387.22 | Calculated Property |
| Pvap | 101.78 | kPa | 402.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1285.94; 379.79] | kg/m3 | [205.65; 585.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 9.93537e+01 | |||
| Coefficient B | 2.61600e-01 | |||
| Coefficient C | 5.85000e+02 | |||
| Coefficient D | 2.18930e-01 | |||
| Temperature range, min. | 205.65 | |||
| Temperature range, max. | 585.00 | |||
| ρl | 1285.94 | kg/m3 | 205.65 | Calculated Property |
| ρl | 1246.63 | kg/m3 | 247.80 | Calculated Property |
| ρl | 1204.66 | kg/m3 | 289.95 | Calculated Property |
| ρl | 1159.39 | kg/m3 | 332.10 | Calculated Property |
| ρl | 1109.85 | kg/m3 | 374.25 | Calculated Property |
| ρl | 1054.53 | kg/m3 | 416.40 | Calculated Property |
| ρl | 990.80 | kg/m3 | 458.55 | Calculated Property |
| ρl | 913.30 | kg/m3 | 500.70 | Calculated Property |
| ρl | 807.16 | kg/m3 | 542.85 | Calculated Property |
| ρl | 379.79 | kg/m3 | 585.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.05; 0.00] | N/m | [205.65; 585.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is γ in N/m, T in K | |||
| Coefficient A | 7.50800e-02 | |||
| Coefficient B | 1.01000e+00 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 5.85000e+02 | |||
| Temperature range, min. | 205.65 | |||
| Temperature range, max. | 585.00 | |||
| γ | 0.05 | N/m | 205.65 | Calculated Property |
| γ | 0.04 | N/m | 247.80 | Calculated Property |
| γ | 0.04 | N/m | 289.95 | Calculated Property |
| γ | 0.03 | N/m | 332.10 | Calculated Property |
| γ | 0.03 | N/m | 374.25 | Calculated Property |
| γ | 0.02 | N/m | 416.40 | Calculated Property |
| γ | 0.02 | N/m | 458.55 | Calculated Property |
| γ | 0.01 | N/m | 500.70 | Calculated Property |
| γ | 0.01 | N/m | 542.85 | Calculated Property |
| γ | 0.00 | N/m | 585.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.02; 0.09] | W/m×K | [401.75; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 1.80300e+03 | |||
| Coefficient B | 8.31400e-01 | |||
| Coefficient C | 6.06800e+09 | |||
| Coefficient D | 0.00000e+00 | |||
| Temperature range, min. | 401.75 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.02 | W/m×K | 401.75 | Calculated Property |
| λgas | 0.02 | W/m×K | 468.22 | Calculated Property |
| λgas | 0.03 | W/m×K | 534.69 | Calculated Property |
| λgas | 0.04 | W/m×K | 601.17 | Calculated Property |
| λgas | 0.04 | W/m×K | 667.64 | Calculated Property |
| λgas | 0.05 | W/m×K | 734.11 | Calculated Property |
| λgas | 0.06 | W/m×K | 800.58 | Calculated Property |
| λgas | 0.07 | W/m×K | 867.06 | Calculated Property |
| λgas | 0.08 | W/m×K | 933.53 | Calculated Property |
| λgas | 0.09 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.16; 0.11] | W/m×K | [205.65; 401.75] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λliquid in W/m×K, T in K | |||
| Coefficient A | 2.08640e-01 | |||
| Coefficient B | -2.52900e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 205.65 | |||
| Temperature range, max. | 401.75 | |||
| λliquid | 0.16 | W/m×K | 205.65 | Calculated Property |
| λliquid | 0.15 | W/m×K | 227.44 | Calculated Property |
| λliquid | 0.15 | W/m×K | 249.23 | Calculated Property |
| λliquid | 0.14 | W/m×K | 271.02 | Calculated Property |
| λliquid | 0.13 | W/m×K | 292.81 | Calculated Property |
| λliquid | 0.13 | W/m×K | 314.59 | Calculated Property |
| λliquid | 0.12 | W/m×K | 336.38 | Calculated Property |
| λliquid | 0.12 | W/m×K | 358.17 | Calculated Property |
| λliquid | 0.11 | W/m×K | 379.96 | Calculated Property |
| λliquid | 0.11 | W/m×K | 401.75 | Calculated Property |
Similar Compounds
Find more compounds similar to Ethanol, 2-chloro-.
Mixtures
- Ethanol, 2-chloro- + m-Chloroaniline
- Ethanol, 2-chloro- + Anisole
- Ethanol, 2-chloro- + 1,4-Dioxane
- 2-Pyrrolidinone, 1-methyl- + Ethanol, 2-chloro-
Sources
- Active Thermochemical Tables 1.112, gas-phase enthalpies of formation ChEDL chemicals 1.5.2, from Active Thermochemical Tables (ATcT), version 1.112, Argonne National Laboratory; Ruscic, B. et al. Active Thermochemical Tables: Thermochemistry for the 21st Century. J. Phys.: Conf. Ser. 2005, 16, 561.
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- Cheméo Relay (1.0)
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- 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
- Enthalpies of Solution of 1-Butyl-3-methylimidazolium Tetrafluoroborate in 15 Solvents at 298.15 K
- Joback Method
- McGowan Method
- NIST Webbook
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