- InChI
- InChI=1S/C10H22O3/c1-2-3-4-5-7-12-9-10-13-8-6-11/h11H,2-10H2,1H3
- InChI Key
- GZMAAYIALGURDQ-UHFFFAOYSA-N
- Formula
- C10H22O3
- SMILES
- CCCCCCOCCOCCO
- Molecular Weight1
- 190.28
- CAS
- 112-59-4
- Other Names
-
- 2-(2-hexyloxyethoxy)ethanol
- 2-(2-n-hexyloxyethoxy)ethanol
- 3,6-dioxa-1-dodecanol
- 3,6-dioxadodecanol-1
- Diethylene glycol mono-n-hexyl ether
- Ethanol, 2-[2-(hexyloxy)ethoxy]-
- Hexol carbitol
- Hexylkarbitol
- NSC 403666
- Ucar Filmer EHC
- diethylene glycol monohexyl ether
- diethylene glycol n-hexyl ether
- ethanol, 2-(2-hexyloxyethoxy)-
- hexyl carbitol
- n-Hexyl Carbitol
- n-hexoxyethoxyethanol
- 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.
- csound,fluid : Speed of sound in fluid (m/s).
- 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° | -313.50 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -666.40 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 28.12 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 86.50 | kJ/mol | NIST |
| log10WS | -1.45 | Crippen Calculated Property | |
| logPoct/wat | 1.592 | Crippen Calculated Property | |
| McVol | 169.370 | ml/mol | McGowan Calculated Property |
| Pc | 2224.99 | kPa | Joback Calculated Property |
| Inp | [1363.00; 1363.00] |
|
|
| Inp | 1363.00 | NIST | |
| Inp | 1363.00 | NIST | |
| Tboil | 533.20 | K | NIST |
| Tc | 724.20 | K | Joback Calculated Property |
| Tfus | 307.74 | K | Joback Calculated Property |
| Vc | 0.650 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [433.45; 504.63] | J/mol×K | [565.22; 724.20] |
|
| Cp,gas | 433.45 | J/mol×K | 565.22 | Joback Calculated Property |
| Cp,gas | 446.41 | J/mol×K | 591.72 | Joback Calculated Property |
| Cp,gas | 458.93 | J/mol×K | 618.21 | Joback Calculated Property |
| Cp,gas | 471.02 | J/mol×K | 644.71 | Joback Calculated Property |
| Cp,gas | 482.66 | J/mol×K | 671.20 | Joback Calculated Property |
| Cp,gas | 493.86 | J/mol×K | 697.70 | Joback Calculated Property |
| Cp,gas | 504.63 | J/mol×K | 724.20 | Joback Calculated Property |
| Cp,liquid | [411.20; 441.20] | J/mol×K | [275.15; 339.15] |
|
| Cp,liquid | 411.20 | J/mol×K | 275.15 | Measure... |
| Cp,liquid | 412.00 | J/mol×K | 277.15 | Measure... |
| Cp,liquid | 412.80 | J/mol×K | 279.15 | Measure... |
| Cp,liquid | 413.60 | J/mol×K | 281.15 | Measure... |
| Cp,liquid | 414.40 | J/mol×K | 283.15 | Measure... |
| Cp,liquid | 415.30 | J/mol×K | 285.15 | Measure... |
| Cp,liquid | 416.10 | J/mol×K | 287.15 | Measure... |
| Cp,liquid | 417.00 | J/mol×K | 289.15 | Measure... |
| Cp,liquid | 417.90 | J/mol×K | 291.15 | Measure... |
| Cp,liquid | 418.70 | J/mol×K | 293.15 | Measure... |
| Cp,liquid | 419.60 | J/mol×K | 295.15 | Measure... |
| Cp,liquid | 420.50 | J/mol×K | 297.15 | Measure... |
| Cp,liquid | 421.00 | J/mol×K | 298.15 | Measure... |
| Cp,liquid | 421.40 | J/mol×K | 299.15 | Measure... |
| Cp,liquid | 422.30 | J/mol×K | 301.15 | Measure... |
| Cp,liquid | 423.20 | J/mol×K | 303.15 | Measure... |
| Cp,liquid | 424.20 | J/mol×K | 305.15 | Measure... |
| Cp,liquid | 425.10 | J/mol×K | 307.15 | Measure... |
| Cp,liquid | 426.00 | J/mol×K | 309.15 | Measure... |
| Cp,liquid | 427.00 | J/mol×K | 311.15 | Measure... |
| Cp,liquid | 428.00 | J/mol×K | 313.15 | Measure... |
| Cp,liquid | 428.90 | J/mol×K | 315.15 | Measure... |
| Cp,liquid | 429.90 | J/mol×K | 317.15 | Measure... |
| Cp,liquid | 430.90 | J/mol×K | 319.15 | Measure... |
| Cp,liquid | 431.90 | J/mol×K | 321.15 | Measure... |
| Cp,liquid | 432.90 | J/mol×K | 323.15 | Measure... |
| Cp,liquid | 433.90 | J/mol×K | 325.15 | Measure... |
| Cp,liquid | 434.90 | J/mol×K | 327.15 | Measure... |
| Cp,liquid | 436.00 | J/mol×K | 329.15 | Measure... |
| Cp,liquid | 437.00 | J/mol×K | 331.15 | Measure... |
| Cp,liquid | 438.00 | J/mol×K | 333.15 | Measure... |
| Cp,liquid | 439.10 | J/mol×K | 335.15 | Measure... |
| Cp,liquid | 440.20 | J/mol×K | 337.15 | Measure... |
| Cp,liquid | 441.20 | J/mol×K | 339.15 | Measure... |
| η | [0.0000675; 0.0078855] | Pa×s | [307.74; 565.22] |
|
| η | 0.0078855 | Pa×s | 307.74 | Joback Calculated Property |
| η | 0.0021950 | Pa×s | 350.65 | Joback Calculated Property |
| η | 0.0008075 | Pa×s | 393.57 | Joback Calculated Property |
| η | 0.0003616 | Pa×s | 436.48 | Joback Calculated Property |
| η | 0.0001870 | Pa×s | 479.39 | Joback Calculated Property |
| η | 0.0001078 | Pa×s | 522.31 | Joback Calculated Property |
| η | 0.0000675 | Pa×s | 565.22 | Joback Calculated Property |
| ΔvapH | 62.70 | kJ/mol | 468.50 | NIST |
| Pvap | [1.11; 19.26] | kPa | [402.96; 473.15] |
|
| Pvap | 1.11 | kPa | 402.96 | Vapor-L... |
| Pvap | 1.12 | kPa | 403.01 | Vapor-L... |
| Pvap | 1.12 | kPa | 403.15 | Vapor-L... |
| Pvap | 1.43 | kPa | 408.02 | Vapor-L... |
| Pvap | 1.83 | kPa | 413.15 | Vapor-L... |
| Pvap | 1.97 | kPa | 413.15 | Vapor P... |
| Pvap | 1.83 | kPa | 413.20 | Vapor-L... |
| Pvap | 2.29 | kPa | 418.17 | Vapor-L... |
| Pvap | 2.83 | kPa | 422.87 | Vapor-L... |
| Pvap | 2.86 | kPa | 423.15 | Vapor-L... |
| Pvap | 3.09 | kPa | 423.15 | Vapor P... |
| Pvap | 4.58 | kPa | 433.15 | Vapor P... |
| Pvap | 6.79 | kPa | 443.15 | Vapor P... |
| Pvap | 9.86 | kPa | 453.15 | Vapor P... |
| Pvap | 11.71 | kPa | 458.15 | Vapor P... |
| Pvap | 13.89 | kPa | 463.15 | Vapor P... |
| Pvap | 16.36 | kPa | 468.15 | Vapor P... |
| Pvap | 19.26 | kPa | 473.15 | Vapor P... |
| ρl | [906.64; 942.09] | kg/m3 | [283.15; 313.15] |
|
| ρl | 942.09 | kg/m3 | 283.15 | Density... |
| ρl | 924.35 | kg/m3 | 288.15 | Thermod... |
| ρl | 938.05 | kg/m3 | 288.15 | Density... |
| ρl | 934.06 | kg/m3 | 293.15 | Density... |
| ρl | 915.52 | kg/m3 | 298.15 | Thermod... |
| ρl | 926.08 | kg/m3 | 303.15 | Density... |
| ρl | 906.64 | kg/m3 | 308.15 | Thermod... |
| ρl | 918.17 | kg/m3 | 313.15 | Density... |
| csound,fluid | [1337.65; 1405.17] | m/s | [288.15; 308.15] |
|
| csound,fluid | 1405.17 | m/s | 288.15 | Densiti... |
| csound,fluid | 1405.17 | m/s | 288.15 | Densiti... |
| csound,fluid | 1388.08 | m/s | 293.15 | Densiti... |
| csound,fluid | 1388.08 | m/s | 293.15 | Densiti... |
| csound,fluid | 1371.14 | m/s | 298.15 | Densiti... |
| csound,fluid | 1371.14 | m/s | 298.15 | Densiti... |
| csound,fluid | 1354.30 | m/s | 303.15 | Densiti... |
| csound,fluid | 1354.30 | m/s | 303.15 | Densiti... |
| csound,fluid | 1337.65 | m/s | 308.15 | Densiti... |
| csound,fluid | 1337.65 | m/s | 308.15 | Densiti... |
Similar Compounds
Find more compounds similar to Diethylene glycol hexyl ether.
Mixtures
- Diethylene glycol hexyl ether + Methyl Alcohol
- 1-Propanol + Diethylene glycol hexyl ether
- 1-Pentanol + Diethylene glycol hexyl ether
- Carbon dioxide + Diethylene glycol hexyl ether
- Propylene Glycol + Diethylene glycol hexyl ether
- 1-Butanamine + Diethylene glycol hexyl ether
- 1-Butanamine, N-butyl- + Diethylene glycol hexyl ether
- Tributylamine + Diethylene glycol hexyl ether
- Diethylene glycol hexyl ether + Water
Sources
- Crippen Method
- Crippen Method
- Thermodynamic properties of mixtures containing alkoxypropanol and n-alkanol
- Densities, excess molar volumes, speeds of sound and isothermal compressibilities for {2-(2-hexyloxyethoxy)ethanol + n-alkanol} systems at temperatures between (288.15 and 308.15) K
- Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
- Solubility Measurement and Thermodynamic Properties Calculation for Several CO2 + Ether Absorbent Systems
- Vapor-Liquid Equilibrium for Propylene Glycol + 2-(2-Hexyloxyethoxy)ethanol and 1-Methyl-2-pyrrolidone + 1-Methoxypropan-2-ol
- Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
- Mutual Solubility and Lower Critical Solution Temperature for Water + Glycol Ether Systems
- Densities, Excess Molar Volumes, Speeds of Sound, and Isothermal Compressibilities for 2-(2-Hexyloxyethoxy)ethanol + n-Alkylamine at Temperatures Between 288.15 K and 308.15 K
- Density, Viscosity, and Refractive Index for Water + 2-Butoxyethanol and + 2-(2-Butoxyethoxy)ethanol at Various Temperatures
- Joback Method
- McGowan Method
- NIST Webbook
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