- InChI
- InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3/i2D
- InChI Key
- LFQSCWFLJHTTHZ-MICDWDOJSA-N
- Formula
- C2H5DO
- SMILES
- [2H]CCO
- Molecular Weight1
- 47.08
- Other Names
-
- ethanol-1-d
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase 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).
- 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).
- ρl : Liquid Density (kg/m3).
- 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 |
|---|---|---|---|
| ω | 0.5303 | Relay (1.0) Calculated Property | |
| ΔfG° | -170.86 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -319.23 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 5.02 | kJ/mol | Joback Calculated Property |
| IE | 10.70 | eV | Relay (1.0) Calculated Property |
| log10WS | 0.89 | Relay (1.0) Calculated Property | |
| logPoct/wat | -0.001 | Crippen Calculated Property | |
| McVol | 44.910 | ml/mol | McGowan Calculated Property |
| Pc | 5756.64 | kPa | Joback Calculated Property |
| Tboil | 395.99 | K | Relay (1.0) Calculated Property |
| Tc | 823.84 | K | Relay (1.0) Calculated Property |
| Tfus | 199.81 | K | Relay (1.0) Calculated Property |
| Vc | 0.176 | m3/kmol | Relay (1.0) Calculated Property |
Cheméo can also estimate Enthalpy of vaporization at standard conditions for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [102.09; 116.23] | J/mol×K | [250.00; 298.00] | 
|
| Cp,liquid | 102.09 | J/mol×K | 250.00 | NIST |
| Cp,liquid | 116.23 | J/mol×K | 298.00 | NIST |
| ρl | [783.63; 818.95] | kg/m3 | [278.15; 318.15] |
|
| ρl | 818.95 | kg/m3 | 278.15 | Volumetric properties of dilute solutions of water in ethanol and water-d2 in ethanol-d1 between T = (278.15 and 318.15) K |
| ρl | 810.32 | kg/m3 | 288.15 | Volumetric properties of dilute solutions of water in ethanol and water-d2 in ethanol-d1 between T = (278.15 and 318.15) K |
| ρl | 801.57 | kg/m3 | 298.15 | Volumetric properties of dilute solutions of water in ethanol and water-d2 in ethanol-d1 between T = (278.15 and 318.15) K |
| ρl | 792.68 | kg/m3 | 308.15 | Volumetric properties of dilute solutions of water in ethanol and water-d2 in ethanol-d1 between T = (278.15 and 318.15) K |
| ρl | 783.63 | kg/m3 | 318.15 | Volumetric properties of dilute solutions of water in ethanol and water-d2 in ethanol-d1 between T = (278.15 and 318.15) K |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [60.41; 141.18] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 6.36100e+00 | |||
| Coefficient B | 2.27820e-01 | |||
| Coefficient C | -1.15400e-04 | |||
| Coefficient D | 2.24000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 60.41 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 73.51 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 85.41 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 96.18 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 105.90 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 114.64 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 122.47 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 129.45 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 135.67 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 141.18 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.2206204; 0.0003424] | Pa×s | [173.12; 349.59] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.43253e+01 | |||
| Coefficient B | 2.21835e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 173.12 | |||
| Temperature range, max. | 349.59 | |||
| η | 0.2206204 | Pa×s | 173.12 | Calculated Property |
| η | 0.0599079 | Pa×s | 192.73 | Calculated Property |
| η | 0.0206958 | Pa×s | 212.33 | Calculated Property |
| η | 0.0085571 | Pa×s | 231.94 | Calculated Property |
| η | 0.0040603 | Pa×s | 251.55 | Calculated Property |
| η | 0.0021459 | Pa×s | 271.16 | Calculated Property |
| η | 0.0012360 | Pa×s | 290.76 | Calculated Property |
| η | 0.0007633 | Pa×s | 310.37 | Calculated Property |
| η | 0.0004992 | Pa×s | 329.98 | Calculated Property |
| η | 0.0003424 | Pa×s | 349.59 | Calculated Property |
Similar Compounds
Find more compounds similar to Ethanol-d1.
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Volumetric properties of dilute solutions of water in ethanol and water-d2 in ethanol-d1 between T = (278.15 and 318.15) K
- Joback Method
- McGowan Method
- NIST Webbook
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