- InChI
- InChI=1S/C3H9NO/c1-4-2-3-5/h4-5H,2-3H2,1H3
- InChI Key
- OPKOKAMJFNKNAS-UHFFFAOYSA-N
- Formula
- C3H9NO
- SMILES
- CNCCO
- Molecular Weight1
- 75.11
- CAS
- 109-83-1
- Other Names
-
- (2-Hydroxyethyl)methylamine
- (Hydroxyethyl)methylamine
- 2-(Methylamino)ethanol
- 2-(N-Methylamino)ethanol
- 2-(N-Monomethylamino)ethanol
- 2-Hydroxy-N-methylethylamine
- 2-Hydroxyethyl-N-methylamine
- 2-Methylamino-1-ethanol
- Amietol M 11
- Methyl(2-hydroxyethyl)amine
- Methyl(hydroxyethyl)amine
- Methyl(«beta»-hydroxyethyl)amine
- Methyl(«beta»-hydroxyethyl)amine
- Methylaminoethanol
- Methylethanolamine
- Methylethylolamine
- Monomethyl-aminoaethanol
- Monomethylaminoethanol
- Monomethylethanolamine
- Monomethylmonoethanolamine
- N-(2-Hydroxyethyl)methylamine
- N-Methyl-2-aminoethanol
- N-Methyl-2-ethanolamine
- N-Methyl-2-hydroxyethylamine
- N-Methyl-N-(2-hydroxyethyl)amine
- N-Methyl-N-(«beta»-hydroxyethyl)amine
- N-Methyl-N-(«beta»-hydroxyethyl)amine
- N-Methyl-N-hydroxyethylamine
- N-Methylaminoethanol
- N-Methylethanolamine
- N-Methylmonoethanolamine
- N-Monomethylaminoethanol
- N-Monomethylethanolamine
- NSC 62776
- USAF DO-50
- ethanolamine, N-methyl-
- «beta»-(Methylamino)ethanol
- «beta»-(Methylamino)ethanol
- 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).
- 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.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- 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° | -73.05 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -204.01 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 12.71 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [57.00; 57.90] | kJ/mol |
|
| ΔvapH° | 57.80 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 57.90 | kJ/mol | NIST |
| ΔvapH° | 57.00 ± 0.50 | kJ/mol | NIST |
| ΔvapH° | 57.60 | kJ/mol | NIST |
| ΔvapH° | 57.50 | kJ/mol | NIST |
| log10WS | 0.47 | Crippen Calculated Property | |
| logPoct/wat | -0.802 | Crippen Calculated Property | |
| McVol | 68.980 | ml/mol | McGowan Calculated Property |
| Pc | 5300.00 ± 500.00 | kPa | NIST |
| ρc | 289.92 ± 20.28 | kg/m3 | NIST |
| Tboil | [428.50; 432.75] | K |
|
| Tboil | 431.20 | K | Vapor L... |
| Tboil | 431.20 | K | NIST |
| Tboil | 428.50 ± 0.50 | K | NIST |
| Tboil | 432.75 | K | NIST |
| Tc | 630.00 ± 10.00 | K | NIST |
| Tfus | 268.65 | K | NIST |
| Vc | 0.258 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [134.31; 170.58] | J/mol×K | [410.39; 578.11] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 135 140 145 150 155 160 165 170 450 500 550 | ||||
| Cp,gas | 134.31 | J/mol×K | 410.39 | Joback Calculated Property |
| Cp,gas | 140.96 | J/mol×K | 438.34 | Joback Calculated Property |
| Cp,gas | 147.36 | J/mol×K | 466.30 | Joback Calculated Property |
| Cp,gas | 153.52 | J/mol×K | 494.25 | Joback Calculated Property |
| Cp,gas | 159.43 | J/mol×K | 522.21 | Joback Calculated Property |
| Cp,gas | 165.12 | J/mol×K | 550.16 | Joback Calculated Property |
| Cp,gas | 170.58 | J/mol×K | 578.11 | Joback Calculated Property |
| Cp,liquid | [194.00; 212.00] | J/mol×K | [303.15; 353.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 195 200 205 210 320 340 | ||||
| Cp,liquid | 194.00 | J/mol×K | 303.15 | Molar H... |
| Cp,liquid | 199.00 | J/mol×K | 308.15 | Molar H... |
| Cp,liquid | 200.00 | J/mol×K | 313.15 | Molar H... |
| Cp,liquid | 202.00 | J/mol×K | 318.15 | Molar H... |
| Cp,liquid | 203.00 | J/mol×K | 323.15 | Molar H... |
| Cp,liquid | 205.00 | J/mol×K | 328.15 | Molar H... |
| Cp,liquid | 206.00 | J/mol×K | 333.15 | Molar H... |
| Cp,liquid | 207.00 | J/mol×K | 338.15 | Molar H... |
| Cp,liquid | 208.00 | J/mol×K | 343.15 | Molar H... |
| Cp,liquid | 210.00 | J/mol×K | 348.15 | Molar H... |
| Cp,liquid | 212.00 | J/mol×K | 353.15 | Molar H... |
| η | [0.0024200; 0.0131200] | Pa×s | [293.15; 333.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 2.00e-3 4.00e-3 6.00e-3 8.00e-3 0.01 0.01 0.01 300 310 320 330 | ||||
| η | 0.0131200 | Pa×s | 293.15 | Experim... |
| η | 0.0102800 | Pa×s | 298.15 | Experim... |
| η | 0.0084200 | Pa×s | 303.15 | Experim... |
| η | 0.0067800 | Pa×s | 308.15 | Experim... |
| η | 0.0055400 | Pa×s | 313.15 | Experim... |
| η | 0.0046100 | Pa×s | 318.15 | Experim... |
| η | 0.0038200 | Pa×s | 323.15 | Experim... |
| η | 0.0031300 | Pa×s | 328.15 | Experim... |
| η | 0.0024200 | Pa×s | 333.15 | Experim... |
| Pvap | [0.01; 180.00] | kPa | [274.90; 451.10] |
|
|
T(K) Vapor pressure (kPa) 0 50 100 150 300 350 400 450 | ||||
| Pvap | 0.01 | kPa | 274.90 | Vapor P... |
| Pvap | 0.02 | kPa | 277.90 | Vapor P... |
| Pvap | 0.03 | kPa | 282.10 | Vapor P... |
| Pvap | 0.04 | kPa | 285.10 | Vapor P... |
| Pvap | 0.05 | kPa | 288.20 | Vapor P... |
| Pvap | 0.06 | kPa | 291.10 | Vapor P... |
| Pvap | 0.06 | kPa | 291.20 | Vapor P... |
| Pvap | 0.07 | kPa | 293.20 | Vapor P... |
| Pvap | 0.09 | kPa | 296.30 | Vapor P... |
| Pvap | 0.11 | kPa | 299.20 | Vapor P... |
| Pvap | 0.14 | kPa | 302.30 | Vapor P... |
| Pvap | 0.23 | kPa | 308.40 | Vapor P... |
| Pvap | 0.28 | kPa | 311.40 | Vapor P... |
| Pvap | 0.35 | kPa | 314.30 | Vapor P... |
| Pvap | 0.42 | kPa | 317.20 | Vapor P... |
| Pvap | 0.51 | kPa | 320.20 | Vapor P... |
| Pvap | 1.94 | kPa | 341.80 | Vapor P... |
| Pvap | 2.94 | kPa | 347.90 | Vapor P... |
| Pvap | 4.94 | kPa | 357.50 | Vapor P... |
| Pvap | 7.44 | kPa | 365.70 | Vapor P... |
| Pvap | 9.94 | kPa | 371.60 | Vapor P... |
| Pvap | 19.90 | kPa | 387.40 | Vapor P... |
| Pvap | 29.90 | kPa | 397.30 | Vapor P... |
| Pvap | 39.90 | kPa | 404.80 | Vapor P... |
| Pvap | 49.90 | kPa | 411.00 | Vapor P... |
| Pvap | 75.00 | kPa | 422.70 | Vapor P... |
| Pvap | 100.00 | kPa | 431.40 | Vapor P... |
| Pvap | 120.00 | kPa | 437.30 | Vapor P... |
| Pvap | 140.00 | kPa | 442.50 | Vapor P... |
| Pvap | 150.00 | kPa | 444.80 | Vapor P... |
| Pvap | 170.00 | kPa | 449.10 | Vapor P... |
| Pvap | 180.00 | kPa | 451.10 | Vapor P... |
| n0 | [1.42780; 1.43930] | [293.15; 323.15] |
|
|
|
T(K) Refractive Index 1.43 1.43 1.43 1.43 1.44 1.44 1.44 300 310 320 | ||||
| n0 | 1.43930 | 293.15 | Volumet... | |
| n0 | 1.43750 | 298.15 | Volumet... | |
| n0 | 1.43560 | 303.15 | Volumet... | |
| n0 | 1.43390 | 308.15 | Volumet... | |
| n0 | 1.43180 | 313.15 | Volumet... | |
| n0 | 1.42980 | 318.15 | Volumet... | |
| n0 | 1.42780 | 323.15 | Volumet... | |
| ρl | [892.10; 941.79] | kg/m3 | [293.15; 353.15] |
|
|
T(K) Liquid Density (kg/m3) 890 900 910 920 930 940 300 320 340 | ||||
| ρl | 940.10 | kg/m3 | 293.15 | Density... |
| ρl | 941.79 | kg/m3 | 293.15 | Density... |
| ρl | 936.20 | kg/m3 | 298.15 | Density... |
| ρl | 936.18 | kg/m3 | 298.15 | Density... |
| ρl | 937.68 | kg/m3 | 298.15 | Densiti... |
| ρl | 934.02 | kg/m3 | 303.15 | Density... |
| ρl | 932.30 | kg/m3 | 303.15 | Density... |
| ρl | 932.26 | kg/m3 | 303.15 | Density... |
| ρl | 933.79 | kg/m3 | 303.15 | Densiti... |
| ρl | 928.40 | kg/m3 | 308.15 | Density... |
| ρl | 929.88 | kg/m3 | 308.15 | Densiti... |
| ρl | 926.18 | kg/m3 | 313.15 | Density... |
| ρl | 925.95 | kg/m3 | 313.15 | Densiti... |
| ρl | 924.50 | kg/m3 | 313.15 | Density... |
| ρl | 924.42 | kg/m3 | 313.15 | Density... |
| ρl | 922.00 | kg/m3 | 318.15 | Densiti... |
| ρl | 920.50 | kg/m3 | 318.15 | Density... |
| ρl | 918.02 | kg/m3 | 323.15 | Densiti... |
| ρl | 916.50 | kg/m3 | 323.15 | Density... |
| ρl | 918.25 | kg/m3 | 323.15 | Density... |
| ρl | 916.48 | kg/m3 | 323.15 | Density... |
| ρl | 912.50 | kg/m3 | 328.15 | Density... |
| ρl | 908.50 | kg/m3 | 333.15 | Density... |
| ρl | 904.40 | kg/m3 | 338.15 | Density... |
| ρl | 900.30 | kg/m3 | 343.15 | Density... |
| ρl | 896.20 | kg/m3 | 348.15 | Density... |
| ρl | 892.10 | kg/m3 | 353.15 | Density... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 389.50 ± 1.50 | K | 0.70 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [329.98; 455.24] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.56909e+01 | |||
| Coefficient B | -3.98645e+03 | |||
| Coefficient C | -7.11700e+01 | |||
| Temperature range, min. | 329.98 | |||
| Temperature range, max. | 455.24 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 329.98 | Calculated Property |
| Pvap | 2.93 | kPa | 343.90 | Calculated Property |
| Pvap | 5.95 | kPa | 357.82 | Calculated Property |
| Pvap | 11.33 | kPa | 371.73 | Calculated Property |
| Pvap | 20.38 | kPa | 385.65 | Calculated Property |
| Pvap | 34.88 | kPa | 399.57 | Calculated Property |
| Pvap | 57.13 | kPa | 413.49 | Calculated Property |
| Pvap | 90.05 | kPa | 427.40 | Calculated Property |
| Pvap | 137.16 | kPa | 441.32 | Calculated Property |
| Pvap | 202.63 | kPa | 455.24 | Calculated Property |
Similar Compounds
![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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)
![Ethanol, 2-[(1-methylethyl)amino]-.](data:image/png;base64,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)
Find more compounds similar to Ethanol, 2-(methylamino)-.
Mixtures
- Ethanol, 2-(methylamino)- + Water
- Ethanol, 2-[(2-aminoethyl)amino]- + Ethanol, 2-(methylamino)- + Water
- Ethanol, 2-methoxy- + Ethanol, 2-(methylamino)-
- Ethanol, 2-ethoxy- + Ethanol, 2-(methylamino)-
- Ethanol, 2-butoxy- + Ethanol, 2-(methylamino)-
- Diethanolamine + Ethanol, 2-(methylamino)- + Water
- Triethanolamine + Ethanol, 2-(methylamino)- + Water
- Ethanol, 2-(methylamino)- + Water + 1-Propanol, 2-amino-2-methyl-
- Methyldiethanolamine + Ethanol, 2-(methylamino)- + Water
- Methyldiethanolamine + Ethanol, 2-(methylamino)-
- 1,2-Ethanediol + Ethanol, 2-(methylamino)-
- 1-Ethyl-2-pyrrolidinone + Ethanol, 2-(methylamino)-
- Carbon dioxide + Ethanol, 2-(methylamino)-
- Carbon dioxide + Ethanol, 2-(methylamino)- + Water
- Nitrous oxide + Ethanol, 2-(methylamino)-
- Nitrous oxide + Ethanol, 2-(methylamino)- + Water
Sources
- Crippen Method
- Crippen Method
- CO2 Solubility in Physicochemical Absorbent: Dibutyl Ether/N-Methylethanolamine/Ethanol
- Equilibrium solubility of carbon dioxide in 2(methylamino)ethanol
- Molar excess enthalpy (HEm) for various {alkanolamine (1) + water (2)} systems at T = (298.15, 313.15, and 323.15) K
- Density, Viscosity and N2O solubility of Aqueous 2- (methylamino)ethanol Solution
- Experimental Data and Modeling for Viscosity and Refractive Index of Aqueous Mixtures with 2-(Methylamino)ethanol (MAE) and Aminoethylethanolamine (AEEA)
- Density, Viscosity, and Excess Properties of Binary Mixtures of 2-(Methylamino)ethanol with 2-Methoxyethanol, 2-Ethoxyethanol, and 2-Butoxyethanol from 293.15 to 353.15 K
- 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
- Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
- Volumetric Properties, Viscosities, and Refractive Indices for Aqueous 2-(Methylamino)ethanol Solutions from (298.15 to 343.15) K
- Density and Surface Tension of Aqueous Solutions of (2-(Methylamino)-ethanol +2-Amino-2-methyl-1-propanol) and (2-(Methylamino)-ethanol + N-Methyl-diethanolamine) from (298.15 to 323.15) K
- Vapor Pressures of Several Commercially Used Alkanolamines
- Vapor Liquid Equilibria for Three Binary Systems of N-Methylethanolamine, N-Methyldiethanolamine, and Ethylene Glycol at P = (40.0, 30.0, and 20.0) kPa
- 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
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