- InChI
- InChI=1S/C6H14O2/c1-3-7-5-6-8-4-2/h3-6H2,1-2H3
- InChI Key
- LZDKZFUFMNSQCJ-UHFFFAOYSA-N
- Formula
- C6H14O2
- SMILES
- CCOCCOCC
- Molecular Weight1
- 118.17
- CAS
- 629-14-1
- Other Names
-
- 1,2-DIETHOXYETHANE
- 1,2-ethanediol, diethyl ether
- 2-Ethoxyethyl ethyl ether
- 3,6-Dioxaoctane
- Diethyl cellosolve
- Diethylether ethylenglykolu
- ETHYL GLYME
- Ethylene glycol diethyl ether
- Glyme-1
- Hisolve EME
- UN 1153
- ethylene glycol, diethyl ether
- 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).
- η : Dynamic viscosity (Pa×s).
- 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).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- 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).
- ρl : Liquid Density (kg/m3).
- Inp : Non-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 |
|---|---|---|---|
| ΔcH°liquid | [-3910.43; -3908.40] | kJ/mol |
|
| ΔcH°liquid | -3908.40 ± 0.60 | kJ/mol | NIST |
| ΔcH°liquid | -3910.43 ± 0.92 | kJ/mol | NIST |
| ΔfG° | -210.36 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-410.30; -408.23] | kJ/mol |
|
| ΔfH°gas | -410.30 | kJ/mol | NIST |
| ΔfH°gas | -408.23 ± 0.97 | kJ/mol | NIST |
| ΔfH°liquid | [-453.50; -451.43] | kJ/mol |
|
| ΔfH°liquid | -453.50 ± 0.60 | kJ/mol | NIST |
| ΔfH°liquid | -451.43 ± 0.93 | kJ/mol | NIST |
| ΔfusH° | 13.67 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [43.20; 43.27] | kJ/mol |
|
| ΔvapH° | Outlier 43.27 | kJ/mol | NIST |
| ΔvapH° | 43.20 ± 0.04 | kJ/mol | NIST |
| ΔvapH° | 43.20 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 43.20 ± 0.12 | kJ/mol | NIST |
| ΔvapH° | 43.20 | kJ/mol | NIST |
| log10WS | [-0.77; -0.77] |
|
|
| log10WS | -0.77 | Aq. Sol... | |
| log10WS | -0.77 | Estimat... | |
| logPoct/wat | 1.059 | Crippen Calculated Property | |
| McVol | 107.140 | ml/mol | McGowan Calculated Property |
| Pc | 2992.59 | kPa | Joback Calculated Property |
| Inp | [744.80; 787.00] |
|
|
| Inp | 787.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 771.00 | NIST | |
| Inp | 773.00 | NIST | |
| Inp | 744.80 | NIST | |
| Inp | 754.40 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 754.40 | NIST | |
| Tboil | 381.52 | K | Joback Calculated Property |
| Tc | 546.82 | K | Joback Calculated Property |
| Tfus | 199.15 | K | NIST |
| Vc | 0.407 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [204.67; 260.92] | J/mol×K | [381.52; 546.82] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 200 210 220 230 240 250 260 400 450 500 550 | ||||
| Cp,gas | 204.67 | J/mol×K | 381.52 | Joback Calculated Property |
| Cp,gas | 214.60 | J/mol×K | 409.07 | Joback Calculated Property |
| Cp,gas | 224.32 | J/mol×K | 436.62 | Joback Calculated Property |
| Cp,gas | 233.82 | J/mol×K | 464.17 | Joback Calculated Property |
| Cp,gas | 243.09 | J/mol×K | 491.72 | Joback Calculated Property |
| Cp,gas | 252.13 | J/mol×K | 519.27 | Joback Calculated Property |
| Cp,gas | 260.92 | J/mol×K | 546.82 | Joback Calculated Property |
| Cp,liquid | [254.50; 296.97] | J/mol×K | [288.15; 421.48] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 260 270 280 290 300 300 350 400 | ||||
| Cp,liquid | 254.50 | J/mol×K | 288.15 | Thermop... |
| Cp,liquid | 255.30 | J/mol×K | 293.15 | Thermop... |
| Cp,liquid | 257.50 | J/mol×K | 298.15 | Thermop... |
| Cp,liquid | 261.08 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 259.40 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 257.90 | J/mol×K | 303.15 | Thermop... |
| Cp,liquid | 258.70 | J/mol×K | 308.15 | Thermop... |
| Cp,liquid | 264.59 | J/mol×K | 312.57 | Liquid ... |
| Cp,liquid | 259.50 | J/mol×K | 313.15 | Thermop... |
| Cp,liquid | 261.20 | J/mol×K | 318.15 | Thermop... |
| Cp,liquid | 265.54 | J/mol×K | 322.47 | Liquid ... |
| Cp,liquid | 262.90 | J/mol×K | 323.15 | Thermop... |
| Cp,liquid | 268.37 | J/mol×K | 332.37 | Liquid ... |
| Cp,liquid | 270.86 | J/mol×K | 342.27 | Liquid ... |
| Cp,liquid | 273.57 | J/mol×K | 352.18 | Liquid ... |
| Cp,liquid | 276.17 | J/mol×K | 362.08 | Liquid ... |
| Cp,liquid | 280.31 | J/mol×K | 371.98 | Liquid ... |
| Cp,liquid | 283.03 | J/mol×K | 381.88 | Liquid ... |
| Cp,liquid | 286.22 | J/mol×K | 391.78 | Liquid ... |
| Cp,liquid | 289.88 | J/mol×K | 401.68 | Liquid ... |
| Cp,liquid | 293.43 | J/mol×K | 411.58 | Liquid ... |
| Cp,liquid | 296.97 | J/mol×K | 421.48 | Liquid ... |
| η | [0.0002032; 0.0027699] | Pa×s | [201.84; 381.52] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 200 250 300 350 | ||||
| η | 0.0027699 | Pa×s | 201.84 | Joback Calculated Property |
| η | 0.0013528 | Pa×s | 231.79 | Joback Calculated Property |
| η | 0.0007784 | Pa×s | 261.73 | Joback Calculated Property |
| η | 0.0005017 | Pa×s | 291.68 | Joback Calculated Property |
| η | 0.0003510 | Pa×s | 321.63 | Joback Calculated Property |
| η | 0.0002609 | Pa×s | 351.57 | Joback Calculated Property |
| η | 0.0002032 | Pa×s | 381.52 | Joback Calculated Property |
| ΔvapH | [36.28; 39.30] | kJ/mol | [316.00; 392.50] |
|
| ΔvapH | 37.90 | kJ/mol | 316.00 | NIST |
| ΔvapH | 39.30 | kJ/mol | 360.50 | NIST |
| ΔvapH | 36.28 | kJ/mol | 392.50 | NIST |
| ρl | 826.22 | kg/m3 | 308.50 | Excess ... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [301.30; 415.60] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.63266e+01 | |||
| Coefficient B | -4.01967e+03 | |||
| Coefficient C | -5.06820e+01 | |||
| Temperature range, min. | 301.30 | |||
| Temperature range, max. | 415.60 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
| Pvap | 1.33 | kPa | 301.30 | Calculated Property |
| Pvap | 2.89 | kPa | 314.00 | Calculated Property |
| Pvap | 5.83 | kPa | 326.70 | Calculated Property |
| Pvap | 11.07 | kPa | 339.40 | Calculated Property |
| Pvap | 19.90 | kPa | 352.10 | Calculated Property |
| Pvap | 34.12 | kPa | 364.80 | Calculated Property |
| Pvap | 56.11 | kPa | 377.50 | Calculated Property |
| Pvap | 88.88 | kPa | 390.20 | Calculated Property |
| Pvap | 136.21 | kPa | 402.90 | Calculated Property |
| Pvap | 202.63 | kPa | 415.60 | Calculated Property |
| Pvap | [14.75; 73.39] | kPa | [339.15; 383.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.39789e+02 | |||
| Coefficient B | -1.01431e+04 | |||
| Coefficient C | -1.86755e+01 | |||
| Coefficient D | 1.41020e-05 | |||
| Temperature range, min. | 339.15 | |||
| Temperature range, max. | 383.15 | |||
|
T(K) Vapor pressure (kPa) 10 20 30 40 50 60 70 340 360 380 | ||||
| Pvap | 14.75 | kPa | 339.15 | Calculated Property |
| Pvap | 18.10 | kPa | 344.04 | Calculated Property |
| Pvap | 22.05 | kPa | 348.93 | Calculated Property |
| Pvap | 26.67 | kPa | 353.82 | Calculated Property |
| Pvap | 32.05 | kPa | 358.71 | Calculated Property |
| Pvap | 38.26 | kPa | 363.59 | Calculated Property |
| Pvap | 45.40 | kPa | 368.48 | Calculated Property |
| Pvap | 53.57 | kPa | 373.37 | Calculated Property |
| Pvap | 62.86 | kPa | 378.26 | Calculated Property |
| Pvap | 73.39 | kPa | 383.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Ethane, 1,2-diethoxy-.
Mixtures
- Ethane, 1,2-diethoxy- + Dimethyl Sulfoxide
- Ethane, 1,2-diethoxy- + Benzyl alcohol
- Ethane, 1,2-diethoxy- + Terephthalic acid
- Ethane, 1,2-diethoxy- + 1,2-Benzenedicarboxylic acid
- Isophthalic acid + Ethane, 1,2-diethoxy-
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
- Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
- Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Ethers and Benzyl Alcohol at 308.15 K and Atmospheric Pressure
- Solubilities of Terephthalic Acid, Phthalic Acid, and Isophthalic Acid in Tetrahydrofuran, Cyclohexanone, 1,2-Diethoxyethane, and Acetophenone
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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