![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] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 220 230 240 250 260 550 600 650 | ||||
| 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] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 280 285 290 295 320 340 | ||||
| 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] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 0.02 0.04 0.06 0.08 0.1 0.12 0.14 0.16 300 310 320 330 | ||||
| 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] |
|
|
T(K) Vapor pressure (kPa) 0 0.05 0.1 0.15 0.2 0.25 340 360 | ||||
| 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] |
|
|
|
T(K) Refractive Index 1.47 1.47 1.47 1.48 1.48 1.48 1.48 1.48 300 310 320 330 | ||||
| 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] |
|
|
T(K) Liquid Density (kg/m3) 1005 1010 1015 1020 1025 1030 300 310 320 | ||||
| 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
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