- InChI
- InChI=1S/C4H11NO/c1-2-5-3-4-6/h5-6H,2-4H2,1H3
- InChI Key
- MIJDSYMOBYNHOT-UHFFFAOYSA-N
- Formula
- C4H11NO
- SMILES
- CCNCCO
- Molecular Weight1
- 89.14
- CAS
- 110-73-6
- Other Names
-
- (2-Hydroxyethyl)ethylamine
- 2-(Ethylamino)ethanol
- 2-(N-Ethylamino)ethanol
- 2-Ethylamino-1-ethanol
- 2-N-Monoethylaminoethanol
- 2-ethylaminoethanol
- Ethyl-2-hydroxyethylamine
- Ethylaminoethanol
- Monoethylaminoethanol
- N-Ethyl-2-aminoethanol
- N-Ethyl-2-hydroxyethylamine
- N-Ethyl-N-(2-hydroxyethyl)amine
- N-Ethyl-N-(«beta»-hydroxyethyl)amine
- N-Ethyl-N-(«beta»-hydroxyethyl)amine
- N-Ethylethanolamine
- N-Ethylmonoethanolamine
- 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).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (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.
- 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.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfG° | -64.63 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -224.65 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 15.30 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 61.00 ± 0.40 | kJ/mol | NIST |
| log10WS | 0.05 | Crippen Calculated Property | |
| logPoct/wat | -0.412 | Crippen Calculated Property | |
| McVol | 83.070 | ml/mol | McGowan Calculated Property |
| Pc | 4462.28 | kPa | Joback Calculated Property |
| Inp | [786.00; 786.00] |
|
|
| Inp | 786.00 | NIST | |
| Inp | 786.00 | NIST | |
| Tboil | 442.70 | K | NIST |
| Tc | 600.20 | K | Joback Calculated Property |
| Tfus | 248.32 | K | Joback Calculated Property |
| Vc | 0.314 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [170.78; 213.83] | J/mol×K | [433.27; 600.20] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 170 180 190 200 210 450 500 550 600 | ||||
| Cp,gas | 170.78 | J/mol×K | 433.27 | Joback Calculated Property |
| Cp,gas | 178.68 | J/mol×K | 461.09 | Joback Calculated Property |
| Cp,gas | 186.28 | J/mol×K | 488.91 | Joback Calculated Property |
| Cp,gas | 193.59 | J/mol×K | 516.73 | Joback Calculated Property |
| Cp,gas | 200.61 | J/mol×K | 544.55 | Joback Calculated Property |
| Cp,gas | 207.36 | J/mol×K | 572.38 | Joback Calculated Property |
| Cp,gas | 213.83 | J/mol×K | 600.20 | Joback Calculated Property |
| Pvap | [0.02; 0.37] | kPa | [282.50; 321.30] |
|
|
T(K) Vapor pressure (kPa) 0 0.05 0.1 0.15 0.2 0.25 0.3 0.35 0.4 290 300 310 320 | ||||
| Pvap | 0.02 | kPa | 282.50 | Vapor P... |
| Pvap | 0.02 | kPa | 284.50 | Vapor P... |
| Pvap | 0.03 | kPa | 287.30 | Vapor P... |
| Pvap | 0.03 | kPa | 290.30 | Vapor P... |
| Pvap | 0.04 | kPa | 293.20 | Vapor P... |
| Pvap | 0.06 | kPa | 296.30 | Vapor P... |
| Pvap | 0.08 | kPa | 299.30 | Vapor P... |
| Pvap | 0.09 | kPa | 302.30 | Vapor P... |
| Pvap | 0.12 | kPa | 305.50 | Vapor P... |
| Pvap | 0.12 | kPa | 306.20 | Vapor P... |
| Pvap | 0.15 | kPa | 308.50 | Vapor P... |
| Pvap | 0.16 | kPa | 309.20 | Vapor P... |
| Pvap | 0.19 | kPa | 311.50 | Vapor P... |
| Pvap | 0.21 | kPa | 312.20 | Vapor P... |
| Pvap | 0.25 | kPa | 315.30 | Vapor P... |
| Pvap | 0.30 | kPa | 318.30 | Vapor P... |
| Pvap | 0.37 | kPa | 321.30 | Vapor P... |
| ρl | [887.20; 917.79] | kg/m3 | [293.15; 333.15] |
|
|
T(K) Liquid Density (kg/m3) 885 890 895 900 905 910 915 920 300 310 320 330 | ||||
| ρl | 917.79 | kg/m3 | 293.15 | Density... |
| ρl | 916.80 | kg/m3 | 293.15 | Density... |
| ρl | 913.39 | kg/m3 | 298.15 | Densiti... |
| ρl | 909.40 | kg/m3 | 303.15 | Densiti... |
| ρl | 909.70 | kg/m3 | 303.15 | Density... |
| ρl | 909.82 | kg/m3 | 303.15 | Density... |
| ρl | 905.40 | kg/m3 | 308.15 | Densiti... |
| ρl | 901.79 | kg/m3 | 313.15 | Density... |
| ρl | 901.39 | kg/m3 | 313.15 | Densiti... |
| ρl | 901.30 | kg/m3 | 313.15 | Density... |
| ρl | 897.34 | kg/m3 | 318.15 | Densiti... |
| ρl | 893.27 | kg/m3 | 323.15 | Densiti... |
| ρl | 894.70 | kg/m3 | 323.15 | Density... |
| ρl | 893.68 | kg/m3 | 323.15 | Density... |
| ρl | 887.20 | kg/m3 | 333.15 | Density... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [339.12; 466.99] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.61126e+01 | |||
| Coefficient B | -4.35050e+03 | |||
| Coefficient C | -6.42070e+01 | |||
| Temperature range, min. | 339.12 | |||
| Temperature range, max. | 466.99 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 339.12 | Calculated Property |
| Pvap | 2.90 | kPa | 353.33 | Calculated Property |
| Pvap | 5.87 | kPa | 367.54 | Calculated Property |
| Pvap | 11.15 | kPa | 381.74 | Calculated Property |
| Pvap | 20.06 | kPa | 395.95 | Calculated Property |
| Pvap | 34.37 | kPa | 410.16 | Calculated Property |
| Pvap | 56.44 | kPa | 424.37 | Calculated Property |
| Pvap | 89.27 | kPa | 438.57 | Calculated Property |
| Pvap | 136.53 | kPa | 452.78 | Calculated Property |
| Pvap | 202.65 | kPa | 466.99 | Calculated Property |
Similar Compounds
![Ethanol, 2-[(1-methylethyl)amino]-.](data:image/png;base64,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)
![2-((2-[(2-Hydroxyethyl)amino]ethyl)amino)ethanol.](data:image/png;base64,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)
![Ethanol, 2-[(2-aminoethyl)amino]-.](data:image/png;base64,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)
Find more compounds similar to Ethanol, 2-(ethylamino)-.
Mixtures
- Ethanol, 2-(ethylamino)- + N,N-Diethyl-2-aminoethanol
- Ethanol, 2-(ethylamino)- + Water
- Ethanol, 2-(ethylamino)- + Diethanolamine + Water
- Ethanol, 2-(ethylamino)- + Triethanolamine + Water
- Ethanol, 2-(ethylamino)- + Water + 1-Propanol, 2-amino-2-methyl-
- Ethanol, 2-(ethylamino)- + Methyldiethanolamine + Water
- Ethanol, 2-(ethylamino)- + 1-Ethyl-2-pyrrolidinone
- Ethanol, 2-(ethylamino)- + 1-Propanol, 3-(dimethylamino)- + Water
- Ethanol, 2-(ethylamino)- + Nitrous oxide
- Ethanol, 2-(ethylamino)- + Nitrous oxide + Water
- Ethanol, 2-(ethylamino)- + Carbon dioxide + Water
Sources
- Crippen Method
- Crippen Method
- Experiment and model for the viscosity of carbonated 3-(dimethylamino)propan-1-ol and 2-(ethylamino)ethanol blended aqueous solutions
- An experimental and modeling study of physical N2O solubility in 2-(ethylamino)ethanol
- Density and viscosity of monoethylethanolamine + H2O and monoethylethanolamine + diethylethanolamine solutions for CO2 capture
- Solubility of Carbon Dioxide in Aqueous Solutions of Three Secondary Amines: 2-(Butylamino)ethanol, 2-(Isopropylamino)ethanol, and 2-(Ethylamino)ethanol Secondary Alkanolamine Solutions
- Density, Viscosity, and Refractive Index of Aqueous CO2-Loaded and -Unloaded Ethylaminoethanol (EAE) Solutions from 293.15 to 323.15 K for Post Combustion CO2 Capture
- Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
- Densities and Viscosities of Aqueous Ternary Mixtures of 2-(Methylamino)ethanol and 2-(Ethylamino)ethanol with Diethanolamine, Triethanolamine, N-Methyldiethanolamine, or 2-Amino-1-methyl-1-propanol from 298.15 to 323.15 K
- Density, Speed of Sound, Viscosity, and Excess Properties of N-Ethyl-2-pyrrolidone + 2-(Methylamino)ethanol [or 2-(Ethylamino)ethanol] from T = (293.15 to 323.15) K
- Surface Tension of Aqueous Binary Mixtures of 2-(Methylamino)ethanol and 2-(Ethylamino)ethanol and Aqueous Ternary Mixtures of These Amines with Triethanolamine or N-Methyldiethanolamine from (293.15 to 323.15) K
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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.