![Ethanol, 2-[(2-aminoethyl)amino]-](/cid/36-714-9/Ethanol-2-2-aminoethyl-amino.png "Ethanol, 2-[(2-aminoethyl)amino]-")
- InChI
- InChI=1S/C4H12N2O/c5-1-2-6-3-4-7/h6-7H,1-5H2
- InChI Key
- LHIJANUOQQMGNT-UHFFFAOYSA-N
- Formula
- C4H12N2O
- SMILES
- NCCNCCO
- Molecular Weight1
- 104.15
- CAS
- 111-41-1
- Other Names
-
- (2-Aminoethyl)ethanolamine
- (2-Hydroxyethyl)ethylenediamine
- («beta»-Hydroxyethyl)ethylenediamine
- 1-Aminoethyl ethanolamine
- 1-[2-(Hydroxyethyl)amino]-2-aminoethane
- 2-(2-Hydroxyethylamino)ethylamine
- 2-(2-aminoethylamino)ethanol
- 2-Amino-2'-hydroxydiethylamine
- 2-[(2-Aminoethyl)amino]ethanol
- Aminoethylethanolamine
- Ethanolethylene diamine
- Monoethanolethylenediamine
- N-(2'-Hydroxyethyl)ethylenediamine
- N-(2-Hydroxyethyl)-1,2-ethanediamine
- N-(2-Hydroxyethyl)ethylenediamine
- N-(2-aminoethyl)ethanolamine
- N-(Aminoethyl)ethanolamine
- N-(Hydroxyethyl)ethylenediamine
- N-(«beta»-Aminoethyl)ethanolamine
- N-(«beta»-Hydroxyethyl)ethylenediamine
- N-Hydroxyethyl-1,2-ethanediamine
- NSC 461
- ethanolamine, N-(2-aminoethyl)-
- ethylenediamine, N-.beta.-hydroxyethyl-
- «beta»-Aminoethyl-«beta»-hydroxyethylamine
- 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).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (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° | 1.82 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -190.86 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 20.50 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 58.25 | kJ/mol | Joback Calculated Property |
| log10WS | 0.62 | Crippen Calculated Property | |
| logPoct/wat | -1.473 | Crippen Calculated Property | |
| McVol | 93.050 | ml/mol | McGowan Calculated Property |
| Pc | 4822.53 | kPa | Joback Calculated Property |
| Inp | 1072.00 | NIST | |
| I | [1920.00; 1965.00] |
|
|
| I | 1965.00 | NIST | |
| I | 1920.00 | NIST | |
| I | 1955.00 | NIST | |
| Tboil | [512.00; 516.95] | K |
|
| Tboil | 512.00 ± 1.00 | K | NIST |
| Tboil | 516.95 | K | NIST |
| Tc | 684.47 | K | Joback Calculated Property |
| Tfus | 331.58 | K | Joback Calculated Property |
| Vc | 0.343 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [218.86; 263.89] | J/mol×K | [505.80; 684.47] |
|
| Cp,gas | 218.86 | J/mol×K | 505.80 | Joback Calculated Property |
| Cp,gas | 227.25 | J/mol×K | 535.58 | Joback Calculated Property |
| Cp,gas | 235.27 | J/mol×K | 565.36 | Joback Calculated Property |
| Cp,gas | 242.94 | J/mol×K | 595.14 | Joback Calculated Property |
| Cp,gas | 250.25 | J/mol×K | 624.91 | Joback Calculated Property |
| Cp,gas | 257.23 | J/mol×K | 654.69 | Joback Calculated Property |
| Cp,gas | 263.89 | J/mol×K | 684.47 | Joback Calculated Property |
| Cp,liquid | [279.00; 296.00] | J/mol×K | [303.15; 353.15] |
|
| Cp,liquid | 279.00 | J/mol×K | 303.15 | Molar H... |
| Cp,liquid | 284.00 | J/mol×K | 308.15 | Molar H... |
| Cp,liquid | 285.00 | J/mol×K | 313.15 | Molar H... |
| Cp,liquid | 286.00 | J/mol×K | 318.15 | Molar H... |
| Cp,liquid | 287.00 | J/mol×K | 323.15 | Molar H... |
| Cp,liquid | 289.00 | J/mol×K | 328.15 | Molar H... |
| Cp,liquid | 290.00 | J/mol×K | 333.15 | Molar H... |
| Cp,liquid | 292.00 | J/mol×K | 338.15 | Molar H... |
| Cp,liquid | 293.00 | J/mol×K | 343.15 | Molar H... |
| Cp,liquid | 295.00 | J/mol×K | 348.15 | Molar H... |
| Cp,liquid | 296.00 | J/mol×K | 353.15 | Molar H... |
| η | [0.0127400; 0.1536200] | Pa×s | [293.15; 333.15] |
|
| η | 0.1536200 | Pa×s | 293.15 | Experim... |
| η | 0.0992700 | Pa×s | 298.15 | Experim... |
| η | 0.0713100 | Pa×s | 303.15 | Experim... |
| η | 0.0529400 | Pa×s | 308.15 | Experim... |
| η | 0.0376700 | Pa×s | 313.15 | Experim... |
| η | 0.0282300 | Pa×s | 318.15 | Experim... |
| η | 0.0215500 | Pa×s | 323.15 | Experim... |
| η | 0.0164300 | Pa×s | 328.15 | Experim... |
| η | 0.0127400 | Pa×s | 333.15 | Experim... |
| ΔvapH | 62.80 | kJ/mol | 450.00 | NIST |
| Pvap | [6.47e-03; 0.24] | kPa | [323.20; 374.20] |
|
| Pvap | 6.47e-03 | kPa | 323.20 | Vapor P... |
| Pvap | 6.52e-03 | kPa | 323.20 | Vapor P... |
| Pvap | 6.81e-03 | kPa | 324.20 | Vapor P... |
| Pvap | 7.11e-03 | kPa | 324.20 | Vapor P... |
| Pvap | 8.20e-03 | kPa | 326.10 | Vapor P... |
| Pvap | 8.09e-03 | kPa | 326.20 | Vapor P... |
| Pvap | 0.01 | kPa | 329.20 | Vapor P... |
| Pvap | 0.01 | kPa | 329.20 | Vapor P... |
| Pvap | 0.01 | kPa | 332.10 | Vapor P... |
| Pvap | 0.01 | kPa | 332.20 | Vapor P... |
| Pvap | 0.02 | kPa | 335.10 | Vapor P... |
| Pvap | 0.02 | kPa | 335.20 | Vapor P... |
| Pvap | 0.02 | kPa | 335.20 | Vapor P... |
| Pvap | 0.02 | kPa | 336.90 | Vapor P... |
| Pvap | 0.02 | kPa | 338.10 | Vapor P... |
| Pvap | 0.02 | kPa | 338.10 | Vapor P... |
| Pvap | 0.03 | kPa | 341.20 | Vapor P... |
| Pvap | 0.03 | kPa | 341.20 | Vapor P... |
| Pvap | 0.03 | kPa | 344.20 | Vapor P... |
| Pvap | 0.03 | kPa | 344.20 | Vapor P... |
| Pvap | 0.04 | kPa | 345.20 | Vapor P... |
| Pvap | 0.04 | kPa | 347.20 | Vapor P... |
| Pvap | 0.05 | kPa | 350.20 | Vapor P... |
| Pvap | 0.06 | kPa | 353.20 | Vapor P... |
| Pvap | 0.08 | kPa | 356.20 | Vapor P... |
| Pvap | 0.09 | kPa | 359.20 | Vapor P... |
| Pvap | 0.10 | kPa | 359.20 | Vapor P... |
| Pvap | 0.11 | kPa | 362.20 | Vapor P... |
| Pvap | 0.14 | kPa | 365.20 | Vapor P... |
| Pvap | 0.17 | kPa | 368.20 | Vapor P... |
| Pvap | 0.20 | kPa | 371.20 | Vapor P... |
| Pvap | 0.23 | kPa | 373.20 | Vapor P... |
| Pvap | 0.24 | kPa | 374.20 | Vapor P... |
| n0 | [1.47128; 1.48454] | [298.15; 333.15] |
|
|
| n0 | 1.48454 | 298.15 | Volumet... | |
| n0 | 1.48269 | 303.15 | Volumet... | |
| n0 | 1.47884 | 313.15 | Volumet... | |
| n0 | 1.47516 | 323.15 | Volumet... | |
| n0 | 1.47128 | 333.15 | Volumet... | |
| ρl | [1006.54; 1029.14] | kg/m3 | [293.15; 323.15] |
|
| ρl | 1029.14 | kg/m3 | 293.15 | Volumet... |
| ρl | 1025.80 | kg/m3 | 298.15 | Thermod... |
| ρl | 1021.30 | kg/m3 | 303.15 | Thermod... |
| ρl | 1021.45 | kg/m3 | 303.15 | Volumet... |
| ρl | 1016.30 | kg/m3 | 308.15 | Thermod... |
| ρl | 1014.18 | kg/m3 | 313.15 | Volumet... |
| ρl | 1006.54 | kg/m3 | 323.15 | Volumet... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [376.80; 512.20] | K | [1.30; 100.00] |
|
| Tboilr | 376.80 | K | 1.30 | NIST |
| Tboilr | 512.20 | K | 100.00 | NIST |
Similar Compounds
![2-((2-[(2-Hydroxyethyl)amino]ethyl)amino)ethanol.](data:image/png;base64,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)
![Ethanol, 2-[(1-methylethyl)amino]-.](data:image/png;base64,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)
![N-[2-(1-piperazinyl)ethyl]ethylenediamine.](data:image/png;base64,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)
Find more compounds similar to Ethanol, 2-[(2-aminoethyl)amino]-.
Mixtures
- Monoethanolamine + Ethanol, 2-[(2-aminoethyl)amino]-
- Ethanol + Ethanol, 2-[(2-aminoethyl)amino]-
- Ethanol, 2-[(2-aminoethyl)amino]- + Water
- Ethanol, 2-[(2-aminoethyl)amino]- + Ethanol, 2-(methylamino)- + Water
- Carbon dioxide + Ethanol, 2-[(2-aminoethyl)amino]- + Water
- Ethanol, 2-[(2-aminoethyl)amino]- + Methyldiethanolamine + Water
- Ethanol, 2-[(2-aminoethyl)amino]- + Hydrogen sulfide + Water
- Carbon dioxide + Benzyl alcohol + Ethanol, 2-[(2-aminoethyl)amino]-
- Carbon dioxide + Ethanol, 2-[(2-aminoethyl)amino]- + Ethanol, 2,2'-oxybis-
- Carbon dioxide + Ethanol, 2-[(2-aminoethyl)amino]- + Triethylene glycol
Sources
- Crippen Method
- Crippen Method
- Thermodynamic properties and CO2 solubility of monoethanolamine + diethylenetriamine/aminoethylethanolamine mixtures: Experimental measurements and thermodynamic modeling
- Molar excess enthalpy (HEm) for various {alkanolamine (1) + water (2)} systems at T = (298.15, 313.15, and 323.15) K
- Equilibrium solubility of carbon dioxide in aqueous 2-((2-aminoethyl)amino)ethanol and N-methyldiethanolamine solution and modeling by electrolyte mPR-CPA EoS
- Measuring solubility of carbon dioxide in aqueous blends of N-methyldiethanolamine and 2-((2-aminoethyl)amino)ethanol at low CO2 loadings and modelling by electrolyte SAFT-HR EoS
- Excess molar enthalpies for binary mixtures of different amines with water
- Measuring and correlating solubility of hydrogen sulfide in aqueous solution of 2-((2 aminoethyl)amino)ethanol
- Volumetric and Viscometric Properties of Alcohol Amines + Ethanol Binary Mixtures
- Experimental Data and Modeling for Viscosity and Refractive Index of Aqueous Mixtures with 2-(Methylamino)ethanol (MAE) and Aminoethylethanolamine (AEEA)
- Volumetric Properties, Viscosities, and Refractive Indices for Aqueous 2-((2-Aminoethyl)amino)ethanol Solutions from (298.15 to 343.15) K
- Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
- Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
- Solubility of CO2 in Nonaqueous Absorption System of 2-(2-Aminoethylamine)ethanol + Benzyl Alcohol
- Joback Method
- McGowan Method
- NIST Webbook
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.