- InChI
- InChI=1S/C8H18O3/c1-3-9-5-7-11-8-6-10-4-2/h3-8H2,1-2H3
- InChI Key
- RRQYJINTUHWNHW-UHFFFAOYSA-N
- Formula
- C8H18O3
- SMILES
- CCOCCOCCOCC
- Molecular Weight1
- 162.23
- CAS
- 112-36-7
- Other Names
-
- .beta.,.beta.'-diethoxy diethyl ether
- 1,1'-oxybis[2-ethoxyethane]
- 1-Ethoxy-2-(«beta»-ethoxyethoxy)ethane
- 1-Ethoxy-2-(«beta»-ethoxyethoxy)ethane
- 2-(2-Ethoxyethoxy)-1-ethoxyethane
- 2-Ethoxyethyl ether
- 3,6,9-Trioxaundecane
- 3-oxa-1,5-pentanediol, diethyl ether
- Bis(2-ethoxyethyl) ether
- Diethyldiethylene glycol
- Diethylene glycol diethyl ether
- Diethylether diethylenglykolu
- Ethane, 1,1'-oxybis[2-ethoxy-
- Ethanol, 2,2'-oxybis-, diethyl ether
- Ether, bis(2-ethoxyethyl)
- Ethyl diglyme
- 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).
- 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.
- γ : Surface Tension (N/m).
- 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 |
|---|---|---|---|
| ΔfG° | -298.52 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -605.11 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 20.04 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [56.40; 58.40] | kJ/mol |
|
| ΔvapH° | 56.40 ± 1.40 | kJ/mol | NIST |
| ΔvapH° | 58.40 ± 0.04 | kJ/mol | NIST |
| log10WS | -0.43 | Crippen Calculated Property | |
| logPoct/wat | 1.076 | Crippen Calculated Property | |
| McVol | 141.190 | ml/mol | McGowan Calculated Property |
| Pc | 2410.00 | kPa | Joback Calculated Property |
| Inp | [174.83; 1081.40] |
|
|
| Inp | 1081.00 | NIST | |
| Inp | 1081.40 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 174.83 | NIST | |
| Inp | 179.46 | NIST | |
| Inp | 1081.40 | NIST | |
| Inp | 1058.00 | NIST | |
| Tboil | [458.20; 462.15] | K |
|
| Tboil | 458.20 | K | NIST |
| Tboil | 462.15 | K | NIST |
| Tboil | 462.15 | K | NIST |
| Tc | 614.00 | K | Joback Calculated Property |
| Tfus | [228.00; 228.85] | K |
|
| Tfus | 228.85 | K | NIST |
| Tfus | 228.85 | K | NIST |
| Tfus | 228.00 ± 2.00 | K | NIST |
| Vc | 0.537 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [307.19; 376.53] | J/mol×K | [449.70; 614.00] |
|
| Cp,gas | 307.19 | J/mol×K | 449.70 | Joback Calculated Property |
| Cp,gas | 319.50 | J/mol×K | 477.08 | Joback Calculated Property |
| Cp,gas | 331.53 | J/mol×K | 504.47 | Joback Calculated Property |
| Cp,gas | 343.25 | J/mol×K | 531.85 | Joback Calculated Property |
| Cp,gas | 354.67 | J/mol×K | 559.23 | Joback Calculated Property |
| Cp,gas | 365.76 | J/mol×K | 586.61 | Joback Calculated Property |
| Cp,gas | 376.53 | J/mol×K | 614.00 | Joback Calculated Property |
| Cp,liquid | [347.50; 384.80] | J/mol×K | [298.10; 421.48] |
|
| Cp,liquid | 347.50 | J/mol×K | 298.10 | NIST |
| Cp,liquid | 349.11 | J/mol×K | 312.57 | Liquid ... |
| Cp,liquid | 351.22 | J/mol×K | 322.47 | Liquid ... |
| Cp,liquid | 353.33 | J/mol×K | 332.37 | Liquid ... |
| Cp,liquid | 355.44 | J/mol×K | 342.27 | Liquid ... |
| Cp,liquid | 358.68 | J/mol×K | 352.18 | Liquid ... |
| Cp,liquid | 360.79 | J/mol×K | 362.08 | Liquid ... |
| Cp,liquid | 364.85 | J/mol×K | 371.98 | Liquid ... |
| Cp,liquid | 368.90 | J/mol×K | 381.88 | Liquid ... |
| Cp,liquid | 372.15 | J/mol×K | 391.78 | Liquid ... |
| Cp,liquid | 377.01 | J/mol×K | 401.68 | Liquid ... |
| Cp,liquid | 380.75 | J/mol×K | 411.58 | Liquid ... |
| Cp,liquid | 384.80 | J/mol×K | 421.48 | Liquid ... |
| η | [0.0001628; 0.0022330] | Pa×s | [246.61; 449.70] |
|
| η | 0.0022330 | Pa×s | 246.61 | Joback Calculated Property |
| η | 0.0011091 | Pa×s | 280.46 | Joback Calculated Property |
| η | 0.0006405 | Pa×s | 314.31 | Joback Calculated Property |
| η | 0.0004115 | Pa×s | 348.15 | Joback Calculated Property |
| η | 0.0002860 | Pa×s | 382.00 | Joback Calculated Property |
| η | 0.0002109 | Pa×s | 415.85 | Joback Calculated Property |
| η | 0.0001628 | Pa×s | 449.70 | Joback Calculated Property |
| ΔvapH | [43.18; 48.30] | kJ/mol | [273.00; 395.50] |
|
| ΔvapH | 43.18 | kJ/mol | 273.00 | NIST |
| ΔvapH | 48.30 | kJ/mol | 395.50 | NIST |
| Pvap | [2.61; 84.21] | kPa | [363.15; 453.15] |
|
| Pvap | 2.61 | kPa | 363.15 | Vapor P... |
| Pvap | 4.29 | kPa | 373.15 | Vapor P... |
| Pvap | 6.69 | kPa | 383.15 | Vapor P... |
| Pvap | 10.08 | kPa | 393.15 | Vapor P... |
| Pvap | 15.08 | kPa | 403.15 | Vapor P... |
| Pvap | 22.08 | kPa | 413.15 | Vapor P... |
| Pvap | 31.51 | kPa | 423.15 | Vapor P... |
| Pvap | 37.58 | kPa | 428.15 | Vapor P... |
| Pvap | 44.45 | kPa | 433.15 | Vapor P... |
| Pvap | 52.47 | kPa | 438.15 | Vapor P... |
| Pvap | 61.68 | kPa | 443.15 | Vapor P... |
| Pvap | 72.21 | kPa | 448.15 | Vapor P... |
| Pvap | 84.21 | kPa | 453.15 | Vapor P... |
| ρl | [831.60; 926.40] | kg/m3 | [273.15; 373.15] |
|
| ρl | 926.40 | kg/m3 | 273.15 | Below t... |
| ρl | 916.36 | kg/m3 | 283.15 | Volumet... |
| ρl | 916.30 | kg/m3 | 283.15 | Below t... |
| ρl | 917.00 | kg/m3 | 283.15 | Thermop... |
| ρl | 915.39 | kg/m3 | 284.15 | Volumet... |
| ρl | 914.43 | kg/m3 | 285.15 | Volumet... |
| ρl | 913.46 | kg/m3 | 286.15 | Volumet... |
| ρl | 912.50 | kg/m3 | 287.15 | Volumet... |
| ρl | 914.40 | kg/m3 | 288.15 | Thermop... |
| ρl | 911.53 | kg/m3 | 288.15 | Volumet... |
| ρl | 912.20 | kg/m3 | 288.15 | Thermop... |
| ρl | 910.57 | kg/m3 | 289.15 | Volumet... |
| ρl | 909.60 | kg/m3 | 290.15 | Volumet... |
| ρl | 908.63 | kg/m3 | 291.15 | Volumet... |
| ρl | 907.67 | kg/m3 | 292.15 | Volumet... |
| ρl | 906.73 | kg/m3 | 293.15 | Thermod... |
| ρl | 907.40 | kg/m3 | 293.15 | Thermop... |
| ρl | 909.60 | kg/m3 | 293.15 | Thermop... |
| ρl | 906.71 | kg/m3 | 293.15 | Volumet... |
| ρl | 905.75 | kg/m3 | 294.15 | Volumet... |
| ρl | 904.78 | kg/m3 | 295.15 | Volumet... |
| ρl | 903.81 | kg/m3 | 296.15 | Volumet... |
| ρl | 902.85 | kg/m3 | 297.15 | Volumet... |
| ρl | 904.70 | kg/m3 | 298.15 | Thermop... |
| ρl | 902.88 | kg/m3 | 298.15 | Thermod... |
| ρl | 902.76 | kg/m3 | 298.15 | Speeds ... |
| ρl | 901.88 | kg/m3 | 298.15 | Volumet... |
| ρl | 902.60 | kg/m3 | 298.15 | Thermop... |
| ρl | 900.92 | kg/m3 | 299.15 | Volumet... |
| ρl | 899.95 | kg/m3 | 300.15 | Volumet... |
| ρl | 898.98 | kg/m3 | 301.15 | Volumet... |
| ρl | 898.02 | kg/m3 | 302.15 | Volumet... |
| ρl | 897.22 | kg/m3 | 303.15 | Thermod... |
| ρl | 897.05 | kg/m3 | 303.15 | Volumet... |
| ρl | 899.80 | kg/m3 | 303.15 | Thermop... |
| ρl | 897.70 | kg/m3 | 303.15 | Thermop... |
| ρl | 896.08 | kg/m3 | 304.15 | Volumet... |
| ρl | 895.12 | kg/m3 | 305.15 | Volumet... |
| ρl | 894.15 | kg/m3 | 306.15 | Volumet... |
| ρl | 893.18 | kg/m3 | 307.15 | Volumet... |
| ρl | 892.21 | kg/m3 | 308.15 | Volumet... |
| ρl | 892.90 | kg/m3 | 308.15 | Thermop... |
| ρl | 895.00 | kg/m3 | 308.15 | Thermop... |
| ρl | 893.08 | kg/m3 | 308.50 | Excess ... |
| ρl | 891.25 | kg/m3 | 309.15 | Volumet... |
| ρl | 890.28 | kg/m3 | 310.15 | Volumet... |
| ρl | 889.31 | kg/m3 | 311.15 | Volumet... |
| ρl | 888.34 | kg/m3 | 312.15 | Volumet... |
| ρl | 888.10 | kg/m3 | 313.15 | Thermop... |
| ρl | 887.37 | kg/m3 | 313.15 | Volumet... |
| ρl | 890.10 | kg/m3 | 313.15 | Thermop... |
| ρl | 886.40 | kg/m3 | 314.15 | Volumet... |
| ρl | 885.43 | kg/m3 | 315.15 | Volumet... |
| ρl | 884.46 | kg/m3 | 316.15 | Volumet... |
| ρl | 883.48 | kg/m3 | 317.15 | Volumet... |
| ρl | 882.51 | kg/m3 | 318.15 | Volumet... |
| ρl | 885.30 | kg/m3 | 318.15 | Thermop... |
| ρl | 881.54 | kg/m3 | 319.15 | Volumet... |
| ρl | 880.57 | kg/m3 | 320.15 | Volumet... |
| ρl | 879.60 | kg/m3 | 321.15 | Volumet... |
| ρl | 878.63 | kg/m3 | 322.15 | Volumet... |
| ρl | 878.40 | kg/m3 | 323.15 | Thermop... |
| ρl | 880.40 | kg/m3 | 323.15 | Thermop... |
| ρl | 877.66 | kg/m3 | 323.15 | Volumet... |
| ρl | 876.70 | kg/m3 | 324.15 | Volumet... |
| ρl | 875.73 | kg/m3 | 325.15 | Volumet... |
| ρl | 874.75 | kg/m3 | 326.15 | Volumet... |
| ρl | 873.78 | kg/m3 | 327.15 | Volumet... |
| ρl | 872.81 | kg/m3 | 328.15 | Volumet... |
| ρl | 875.60 | kg/m3 | 328.15 | Thermop... |
| ρl | 871.84 | kg/m3 | 329.15 | Volumet... |
| ρl | 870.87 | kg/m3 | 330.15 | Volumet... |
| ρl | 869.89 | kg/m3 | 331.15 | Volumet... |
| ρl | 868.92 | kg/m3 | 332.15 | Volumet... |
| ρl | 867.94 | kg/m3 | 333.15 | Volumet... |
| ρl | 868.70 | kg/m3 | 333.15 | Thermop... |
| ρl | 870.70 | kg/m3 | 333.15 | Thermop... |
| ρl | 865.90 | kg/m3 | 338.15 | Thermop... |
| ρl | 861.00 | kg/m3 | 343.15 | Thermop... |
| ρl | 858.90 | kg/m3 | 343.15 | Thermop... |
| ρl | 856.10 | kg/m3 | 348.15 | Thermop... |
| ρl | 851.20 | kg/m3 | 353.15 | Thermop... |
| ρl | 846.30 | kg/m3 | 358.15 | Thermop... |
| ρl | 841.40 | kg/m3 | 363.15 | Thermop... |
| ρl | 836.50 | kg/m3 | 368.15 | Thermop... |
| ρl | 831.60 | kg/m3 | 373.15 | Thermop... |
| γ | 0.03 | N/m | 293.15 | Physica... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [342.30; 489.93] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.65189e+01 | |||
| Coefficient B | -5.34545e+03 | |||
| Coefficient C | -1.29720e+01 | |||
| Temperature range, min. | 342.30 | |||
| Temperature range, max. | 489.93 | |||
| Pvap | 1.33 | kPa | 342.30 | Calculated Property |
| Pvap | 2.88 | kPa | 358.70 | Calculated Property |
| Pvap | 5.80 | kPa | 375.11 | Calculated Property |
| Pvap | 11.00 | kPa | 391.51 | Calculated Property |
| Pvap | 19.77 | kPa | 407.91 | Calculated Property |
| Pvap | 33.91 | kPa | 424.32 | Calculated Property |
| Pvap | 55.82 | kPa | 440.72 | Calculated Property |
| Pvap | 88.56 | kPa | 457.12 | Calculated Property |
| Pvap | 135.95 | kPa | 473.53 | Calculated Property |
| Pvap | 202.65 | kPa | 489.93 | Calculated Property |
Similar Compounds
Find more compounds similar to Diethyl carbitol.
Mixtures
- Propylamine + Diethyl carbitol
- Carbon dioxide + Diethyl carbitol
- Diethyl carbitol + Methyl Alcohol
- Diethyl carbitol + 1-Butanol
- Diethyl carbitol + 1-Decanol
- Diethyl carbitol + Water
- Benzyl alcohol + Diethyl carbitol
- Diethyl carbitol + Ethane, 1,2-dichloro-
Sources
- Crippen Method
- Crippen Method
- Speeds of Sound and Isentropic Compressibilities of n-Alkoxyethanols and Polyethers with Propylamine at 298.15K
- Solubilities of CO2 capture absorbents 2-ethoxyethyl ether, 2-butoxyethyl acetate and 2-(2-ethoxyethoxy)ethyl acetate
- Thermodynamics of 1-alkanol + linear polyether mixtures
- Below the room temperature measurements of CO2 solubilities in six physical absorbents
- Thermophysical properties of glycols and glymes
- Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
- Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
- Physical-Chemical Properties and Liquid-Liquid Equilibria for Binary Mixture of Diethylene Glycol Diethyl Ether with Water
- Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Ethers and Benzyl Alcohol at 308.15 K and Atmospheric Pressure
- Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
- Fast Determination of Binary Vapor Liquid Equilibrium of CO2-Based Mixtures at Elevated Pressures
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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