- InChI
- InChI=1S/C6H15NO/c1-3-7(4-2)5-6-8/h8H,3-6H2,1-2H3
- InChI Key
- BFSVOASYOCHEOV-UHFFFAOYSA-N
- Formula
- C6H15NO
- SMILES
- CCN(CC)CCO
- Molecular Weight1
- 117.19
- CAS
- 100-37-8
- Other Names
-
- (2-Hydroxyethyl)diethylamine
- (diethylamino)ethanol
- 2-(Diethylamino)ethyl alcohol
- 2-(N,N-Diethylamino)ethanol
- 2-(diethylamino)ethanol
- 2-Hydroxytriethylamine
- 2-diethylaminoethanol
- A 22
- DEAE
- Diaethylaminoaethanol
- Diethyl(2-hydroxyethyl)amine
- Diethylethanolamine
- Diethylmonoethanolamine
- Ethanol, 2-(diethylamino)-
- N,N-Diethyl-2-hydroxyethylamine
- N,N-Diethyl-N-(«beta»-Hydroxyethyl)amine
- N,N-Diethylaminoethanol
- N,N-Diethylmonoethanolamine
- N,N-diethylethanolamine
- N-(Diethylamino)ethanol
- NSC 8759
- Pennad 150
- UN 2686
- ethanolamine, N,N-diethyl-
- «beta»-(Diethylamino)ethanol
- «beta»-(Diethylamino)ethyl alcohol
- «beta»-Hydroxytriethylamine
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°solid : Solid 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).
- 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).
- 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 |
|---|---|---|---|
| ΔcH°solid | -4195.30 ± 0.54 | kJ/mol | NIST |
| ΔfG° | -26.40 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -251.87 | kJ/mol | Joback Calculated Property |
| ΔfH°solid | -310.00 ± 0.54 | kJ/mol | NIST |
| ΔfusH° | 18.41 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [52.50; 58.50] | kJ/mol |
|
| ΔvapH° | 52.50 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 58.50 ± 1.30 | kJ/mol | NIST |
| IE | 8.58 ± 0.03 | eV | NIST |
| log10WS | -0.17 | Crippen Calculated Property | |
| logPoct/wat | 0.321 | Crippen Calculated Property | |
| McVol | 111.250 | ml/mol | McGowan Calculated Property |
| Pc | 3443.98 | kPa | Joback Calculated Property |
| Inp | [873.00; 894.00] |
|
|
| Inp | 894.00 | NIST | |
| Inp | 873.00 | NIST | |
| Inp | 873.00 | NIST | |
| Tboil | [162.10; 436.20] | K |
|
| Tboil | 435.94 | K | Isobari... |
| Tboil | 435.85 | K | Isobari... |
| Tboil | 434.20 | K | NIST |
| Tboil | 436.20 | K | NIST |
| Tboil | 436.00 | K | NIST |
| Tboil | Outlier 162.10 | K | NIST |
| Tc | 601.20 | K | Joback Calculated Property |
| Tfus | 250.67 | K | Joback Calculated Property |
| Vc | 0.408 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [237.40; 294.23] | J/mol×K | [441.30; 601.20] |
|
| Cp,gas | 237.40 | J/mol×K | 441.30 | Joback Calculated Property |
| Cp,gas | 247.88 | J/mol×K | 467.95 | Joback Calculated Property |
| Cp,gas | 257.94 | J/mol×K | 494.60 | Joback Calculated Property |
| Cp,gas | 267.59 | J/mol×K | 521.25 | Joback Calculated Property |
| Cp,gas | 276.85 | J/mol×K | 547.90 | Joback Calculated Property |
| Cp,gas | 285.73 | J/mol×K | 574.55 | Joback Calculated Property |
| Cp,gas | 294.23 | J/mol×K | 601.20 | Joback Calculated Property |
| ΔvapH | [37.80; 48.50] | kJ/mol | [380.50; 403.50] |
|
| ΔvapH | 48.50 | kJ/mol | 380.50 | NIST |
| ΔvapH | 48.50 ± 0.20 | kJ/mol | 403.50 | NIST |
| ΔvapH | 45.00 ± 0.20 | kJ/mol | 403.50 | NIST |
| ΔvapH | 41.60 ± 0.40 | kJ/mol | 403.50 | NIST |
| ΔvapH | 37.80 ± 0.70 | kJ/mol | 403.50 | NIST |
| Pvap | [0.05; 150.00] | kPa | [278.20; 449.50] |
|
| Pvap | 0.05 | kPa | 278.20 | Vapor P... |
| Pvap | 0.05 | kPa | 278.60 | Vapor P... |
| Pvap | 0.06 | kPa | 279.80 | Vapor P... |
| Pvap | 0.06 | kPa | 281.20 | Vapor P... |
| Pvap | 0.07 | kPa | 282.70 | Vapor P... |
| Pvap | 0.08 | kPa | 284.20 | Vapor P... |
| Pvap | 0.09 | kPa | 285.10 | Vapor P... |
| Pvap | 0.09 | kPa | 285.30 | Vapor P... |
| Pvap | 0.10 | kPa | 287.30 | Vapor P... |
| Pvap | 0.11 | kPa | 288.00 | Vapor P... |
| Pvap | 0.11 | kPa | 288.30 | Vapor P... |
| Pvap | 0.13 | kPa | 290.20 | Vapor P... |
| Pvap | 0.14 | kPa | 291.00 | Vapor P... |
| Pvap | 0.15 | kPa | 292.30 | Vapor P... |
| Pvap | 0.16 | kPa | 293.30 | Vapor P... |
| Pvap | 0.19 | kPa | 295.30 | Vapor P... |
| Pvap | 0.20 | kPa | 296.00 | Vapor P... |
| Pvap | 0.20 | kPa | 296.30 | Vapor P... |
| Pvap | 0.20 | kPa | 296.30 | Vapor P... |
| Pvap | 0.22 | kPa | 297.30 | Vapor P... |
| Pvap | 0.23 | kPa | 298.20 | Vapor P... |
| Pvap | 0.25 | kPa | 299.20 | Vapor P... |
| Pvap | 0.29 | kPa | 301.20 | Vapor P... |
| Pvap | 0.31 | kPa | 302.20 | Vapor P... |
| Pvap | 0.30 | kPa | 302.20 | Vapor P... |
| Pvap | 0.35 | kPa | 304.20 | Vapor P... |
| Pvap | 0.43 | kPa | 307.20 | Vapor P... |
| Pvap | 0.52 | kPa | 310.20 | Vapor P... |
| Pvap | 0.63 | kPa | 313.20 | Vapor P... |
| Pvap | 0.77 | kPa | 316.30 | Vapor P... |
| Pvap | 0.88 | kPa | 318.30 | Vapor P... |
| Pvap | 1.94 | kPa | 333.20 | Vapor P... |
| Pvap | 2.94 | kPa | 340.70 | Vapor P... |
| Pvap | 4.94 | kPa | 351.00 | Vapor P... |
| Pvap | 7.44 | kPa | 359.80 | Vapor P... |
| Pvap | 9.94 | kPa | 366.50 | Vapor P... |
| Pvap | 19.90 | kPa | 383.90 | Vapor P... |
| Pvap | 29.90 | kPa | 395.10 | Vapor P... |
| Pvap | 49.90 | kPa | 410.50 | Vapor P... |
| Pvap | 60.00 | kPa | 418.34 | Isobari... |
| Pvap | 75.00 | kPa | 423.90 | Vapor P... |
| Pvap | 100.00 | kPa | 434.00 | Vapor P... |
| Pvap | 101.30 | kPa | 435.94 | Isobari... |
| Pvap | 120.00 | kPa | 440.90 | Vapor P... |
| Pvap | 130.00 | kPa | 443.90 | Vapor P... |
| Pvap | 150.00 | kPa | 449.50 | Vapor P... |
| ρl | [818.60; 894.42] | kg/m3 | [283.15; 363.15] |
|
| ρl | 894.42 | kg/m3 | 283.15 | Volumet... |
| ρl | 883.50 | kg/m3 | 293.15 | Density... |
| ρl | 884.14 | kg/m3 | 293.15 | Changes... |
| ρl | 885.36 | kg/m3 | 293.15 | Volumet... |
| ρl | 891.20 | kg/m3 | 293.15 | Volumet... |
| ρl | 884.37 | kg/m3 | 293.15 | Intermo... |
| ρl | 880.00 | kg/m3 | 298.15 | Study o... |
| ρl | 880.37 | kg/m3 | 298.15 | Density... |
| ρl | 879.50 | kg/m3 | 298.15 | Changes... |
| ρl | 875.10 | kg/m3 | 303.15 | Density... |
| ρl | 874.93 | kg/m3 | 303.15 | Intermo... |
| ρl | 876.15 | kg/m3 | 303.15 | Volumet... |
| ρl | 875.75 | kg/m3 | 303.15 | Density... |
| ρl | 874.40 | kg/m3 | 303.15 | Volumet... |
| ρl | 866.20 | kg/m3 | 313.15 | Density... |
| ρl | 866.83 | kg/m3 | 313.15 | Volumet... |
| ρl | 866.41 | kg/m3 | 313.15 | Density... |
| ρl | 865.62 | kg/m3 | 313.15 | Intermo... |
| ρl | 865.40 | kg/m3 | 313.15 | Volumet... |
| ρl | 856.40 | kg/m3 | 323.15 | Volumet... |
| ρl | 857.50 | kg/m3 | 323.15 | Density... |
| ρl | 857.39 | kg/m3 | 323.15 | Volumet... |
| ρl | 856.95 | kg/m3 | 323.15 | Density... |
| ρl | 845.60 | kg/m3 | 333.15 | Volumet... |
| ρl | 849.20 | kg/m3 | 333.15 | Density... |
| ρl | 847.38 | kg/m3 | 333.15 | Density... |
| ρl | 847.84 | kg/m3 | 333.15 | Volumet... |
| ρl | 838.16 | kg/m3 | 343.15 | Volumet... |
| ρl | 837.74 | kg/m3 | 343.15 | Density... |
| ρl | 828.49 | kg/m3 | 353.15 | Volumet... |
| ρl | 828.02 | kg/m3 | 353.15 | Density... |
| ρl | 818.60 | kg/m3 | 363.15 | Volumet... |
| γ | [0.03; 0.03] | N/m | [283.20; 323.20] |
|
| γ | 0.03 | N/m | 283.20 | Experim... |
| γ | 0.03 | N/m | 293.20 | Experim... |
| γ | 0.03 | N/m | 303.20 | Experim... |
| γ | 0.03 | N/m | 313.20 | Experim... |
| γ | 0.03 | N/m | 323.20 | Experim... |
Similar Compounds
![Ethanol, 2,2'-[(1-methylethyl)imino]bis-.](data:image/png;base64,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)
Find more compounds similar to N,N-Diethyl-2-aminoethanol.
Mixtures
- N,N-Diethyl-2-aminoethanol + Water
- Monoethanolamine + N,N-Diethyl-2-aminoethanol + Water
- Piperazine + N,N-Diethyl-2-aminoethanol + Water
- 1-Propanol + N,N-Diethyl-2-aminoethanol
- 1-Butanol + N,N-Diethyl-2-aminoethanol
- Monoethanolamine + N,N-Diethyl-2-aminoethanol
- Ethanol, 2-(ethylamino)- + N,N-Diethyl-2-aminoethanol
- Carbon dioxide + N,N-Diethyl-2-aminoethanol + Water
- N,N-Diethyl-2-aminoethanol + Methyl Alcohol
- Ethanamine, N-ethyl- + N,N-Diethyl-2-aminoethanol
- 1,3-Propanediamine, N-methyl- + N,N-Diethyl-2-aminoethanol
- Ethanol + N,N-Diethyl-2-aminoethanol
- 1,3-Propanediamine, N-methyl- + N,N-Diethyl-2-aminoethanol + Water
- 1,4-Butanediamine + N,N-Diethyl-2-aminoethanol + Water
- Nitrous oxide + N,N-Diethyl-2-aminoethanol + Water
Sources
- Crippen Method
- Crippen Method
- Excess molar enthalpies for binary mixtures of different amines with water
- Absorption capacity and viscosity for CO2 capture process using high concentrated PZ-DEAE aqueous solution
- Experiments and model for the surface tension of DEAE-PZ and DEAE-MEA aqueous solutions
- CO2 absorption with aqueous tertiary amine solutions: Equilibrium solubility and thermodynamic modeling
- Intermolecular interactions in binary mixtures of 2-diethylethanolamine with 1-propanol and 1-butanol at different temperatures
- Volumetric and viscometric properties of binary and ternary mixtures of monoethanolamine, 2-(diethylamino) ethanol and water from (293.15 to 333.15) K
- Density and viscosity of monoethylethanolamine + H2O and monoethylethanolamine + diethylethanolamine solutions for CO2 capture
- Density and Viscosity of Partially Carbonated Aqueous Tertiary Alkanolamine Solutions at Temperatures between (298.15 and 353.15) K
- Vapor Liquid Equilibrium and Physicochemical Properties of Novel Aqueous Blends of (2-Diethylaminoethanol + Piperazine) for CO2 Appropriation
- Study of CO2 Absorption into Phase Change Solvents MAPA and DEEA
- Density and Viscosity of Partially Carbonated Aqueous Solutions Containing a Tertiary Alkanolamine and Piperazine at Temperatures between 298.15 and 353.15 K
- Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
- Vapor Pressures of Several Commercially Used Alkanolamines
- Isobaric Vapor Liquid Equilibrium for the Binary Systems of Methanol, Diethylamine, and N,N-Diethylethanolamine at p = (60.0 and 101.3) kPa
- Freezing Point Depressions of Phase Change CO2 Solvents
- Solubility of N2O in Density and Viscosity of Aqueous Solutions of 1,4-Butanediamine, 2-(Diethylamino)-ethanol, and Their Mixtures from (298.15 to 333.15) K
- Volumetric Properties of Binary Mixtures of 3-(Methylamino)propylamine with Water, N-Methyldiethanolamine, N,N-Dimethylethanolamine, and N,N-Diethylethanolamine from (283.15 to 363.15) K
- Isobaric Vapor Liquid Equilibrium for the Binary Systems (Diethylamine + Ethanol), (Ethanol + N,N-Diethylethanolamine), and (Diethylamine + N,N-Diethylethanolamine) at p = (80.0 and 40.0) kPa
- Equilibrium Total Pressure and CO2 Solubility in Binary and Ternary Aqueous Solutions of 2-(Diethylamino)ethanol (DEEA) and 3-(Methylamino)propylamine (MAPA)
- Changes in Aggregation Patterns Detected by Diffusion, Viscosity, and Surface Tension in Water + 2-(Diethylamino)Ethanol Mixtures at Different Temperatures
- Joback Method
- McGowan Method
- NIST Webbook
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