- InChI
- InChI=1S/C4H11NO/c1-5(2)3-4-6/h6H,3-4H2,1-2H3
- InChI Key
- UEEJHVSXFDXPFK-UHFFFAOYSA-N
- Formula
- C4H11NO
- SMILES
- CN(C)CCO
- Molecular Weight1
- 89.14
- CAS
- 108-01-0
- Other Names
-
- (2-Hydroxyethyl)dimethylamine
- (CH3)2NCH2CH2OH
- (Dimethylamino)ethanol
- (N,N-dimethylamino)ethanol
- .beta.-(dimethylamino)ethanol
- .beta.-dimethylaminoethyl alcohol
- .beta.-hydroxyethyldimethylamine
- 2-(Dimethylamino)-1-ethanol
- 2-(Dimethylamino)ethanol
- 2-(N,N-Dimethylamino)ethanol
- 2-(dimethylamino)ethyl alcohol
- 2-dimethylaminoethanol
- 67-48-1
- Amietol M 21
- Bimanol
- DMAE
- DMEA
- Dabco DMEA
- Deanol
- Dimethyl(2-hydroxyethyl)amine
- Dimethyl(hydroxyethyl)amine
- Dimethylaethanolamin
- Dimethylaminoaethanol
- Dimethylethanolamine
- Dimethylmonoethanolamine
- Ethanol, 2-(dimethylamino)-
- Kalpur P
- Liparon
- N,N'-Dimethylethanolamine
- N,N-Dimethyl(2-hydroxyethyl)amine
- N,N-Dimethyl-2-aminoethanol
- N,N-Dimethyl-N-(2-hydroxyethyl)amine
- N,N-Dimethyl-N-(«beta»-hydroxyethyl)amine
- N,N-Dimethyl-N-(«beta»-hydroxyethyl)amine
- N,N-Dimethyl-«beta»-hydroxyethylamine
- N,N-Dimethyl-«beta»-hydroxyethylamine
- N,N-Dimethylethanolamine
- N,N-dimethyl-.beta.-hydroxyethylamine
- N,N-dimethyl-2-hydroxyethylamine
- N,N-dimethyl-N-(.beta.-hydroxyethyl)amine
- N-(2-Hydroxyethyl)dimethylamine
- N-(Dimethylamino)ethanol
- NSC 2652
- Norcholine
- Propamine A
- Tegoamin DMEA
- Texacat DME
- UN 2051
- Varesal
- ethanolamine, N,N-dimethyl-
- «beta»-(Dimethylamino)ethanol
- «beta»-(Dimethylamino)ethyl alcohol
- «beta»-Hydroxyethyldimethylamine
- «beta»-(Dimethylamino)ethanol
- «beta»-(Dimethylamino)ethyl alcohol
- «beta»-Hydroxyethyldimethylamine
- 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).
- 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.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- Vm : Molar Volume (m3/mol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfG° | -43.24 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -210.59 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 13.22 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [46.50; 47.90] | kJ/mol |
|
| ΔvapH° | 46.50 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 47.90 | kJ/mol | NIST |
| ΔvapH° | 47.60 | kJ/mol | NIST |
| IE | [8.80; 8.85] | eV |
|
| IE | 8.80 | eV | NIST |
| IE | 8.82 | eV | NIST |
| IE | 8.85 ± 0.04 | eV | NIST |
| log10WS | 0.67 | Crippen Calculated Property | |
| logPoct/wat | -0.460 | Crippen Calculated Property | |
| McVol | 83.070 | ml/mol | McGowan Calculated Property |
| Pc | 4374.18 | kPa | Joback Calculated Property |
| Inp | [706.00; 710.00] |
|
|
| Inp | 710.00 | NIST | |
| Inp | 706.00 | NIST | |
| Inp | 708.00 | NIST | |
| Inp | 710.00 | NIST | |
| Tboil | [406.88; 407.75] | K |
|
| Tboil | 407.20 | K | NIST |
| Tboil | 406.88 ± 0.20 | K | NIST |
| Tboil | 407.75 | K | NIST |
| Tc | 556.43 | K | Joback Calculated Property |
| Tfus | 214.15 | K | NIST |
| Vc | 0.296 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [160.61; 205.42] | J/mol×K | [395.54; 556.43] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 160 170 180 190 200 400 450 500 550 | ||||
| Cp,gas | 160.61 | J/mol×K | 395.54 | Joback Calculated Property |
| Cp,gas | 168.88 | J/mol×K | 422.35 | Joback Calculated Property |
| Cp,gas | 176.81 | J/mol×K | 449.17 | Joback Calculated Property |
| Cp,gas | 184.42 | J/mol×K | 475.98 | Joback Calculated Property |
| Cp,gas | 191.72 | J/mol×K | 502.80 | Joback Calculated Property |
| Cp,gas | 198.71 | J/mol×K | 529.61 | Joback Calculated Property |
| Cp,gas | 205.42 | J/mol×K | 556.43 | Joback Calculated Property |
| Cp,liquid | [213.00; 226.00] | J/mol×K | [303.15; 353.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 212 214 216 218 220 222 224 226 320 340 | ||||
| Cp,liquid | 213.00 | J/mol×K | 303.15 | Molar H... |
| Cp,liquid | 215.00 | J/mol×K | 308.15 | Molar H... |
| Cp,liquid | 217.00 | J/mol×K | 313.15 | Molar H... |
| Cp,liquid | 219.00 | J/mol×K | 318.15 | Molar H... |
| Cp,liquid | 221.00 | J/mol×K | 323.15 | Molar H... |
| Cp,liquid | 222.00 | J/mol×K | 328.15 | Molar H... |
| Cp,liquid | 223.00 | J/mol×K | 333.15 | Molar H... |
| Cp,liquid | 223.00 | J/mol×K | 338.15 | Molar H... |
| Cp,liquid | 223.00 | J/mol×K | 343.15 | Molar H... |
| Cp,liquid | 224.00 | J/mol×K | 348.15 | Molar H... |
| Cp,liquid | 226.00 | J/mol×K | 353.15 | Molar H... |
| η | [0.0009630; 0.0022380] | Pa×s | [313.15; 353.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 1.00e-3 1.20e-3 1.40e-3 1.60e-3 1.80e-3 2.00e-3 2.20e-3 320 330 340 350 | ||||
| η | 0.0022380 | Pa×s | 313.15 | Density... |
| η | 0.0017560 | Pa×s | 323.15 | Density... |
| η | 0.0014130 | Pa×s | 333.15 | Density... |
| η | 0.0011560 | Pa×s | 343.15 | Density... |
| η | 0.0009630 | Pa×s | 353.15 | Density... |
| ΔvapH | [42.70; 43.20] | kJ/mol | [365.50; 368.50] |
|
| ΔvapH | 42.70 | kJ/mol | 365.50 | NIST |
| ΔvapH | 43.20 | kJ/mol | 368.50 | NIST |
| Pvap | [0.14; 300.20] | kPa | [273.15; 447.80] |
|
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 300 350 400 450 | ||||
| Pvap | 0.14 | kPa | 273.15 | Measure... |
| Pvap | 0.15 | kPa | 273.86 | Measure... |
| Pvap | 0.19 | kPa | 277.90 | Vapor P... |
| Pvap | 0.19 | kPa | 278.30 | Vapor P... |
| Pvap | 0.19 | kPa | 278.60 | Vapor P... |
| Pvap | 0.22 | kPa | 280.20 | Vapor P... |
| Pvap | 0.23 | kPa | 280.70 | Vapor P... |
| Pvap | 0.24 | kPa | 281.80 | Vapor P... |
| Pvap | 0.29 | kPa | 282.97 | Measure... |
| Pvap | 0.29 | kPa | 282.97 | Measure... |
| Pvap | 0.30 | kPa | 283.15 | Measure... |
| Pvap | 0.28 | kPa | 283.20 | Vapor P... |
| Pvap | 0.28 | kPa | 284.30 | Vapor P... |
| Pvap | 0.34 | kPa | 286.20 | Vapor P... |
| Pvap | 0.32 | kPa | 286.50 | Vapor P... |
| Pvap | 0.42 | kPa | 289.20 | Vapor P... |
| Pvap | 0.40 | kPa | 289.40 | Vapor P... |
| Pvap | 0.43 | kPa | 290.60 | Vapor P... |
| Pvap | 0.50 | kPa | 292.20 | Vapor P... |
| Pvap | 0.48 | kPa | 292.40 | Vapor P... |
| Pvap | 0.58 | kPa | 292.89 | Measure... |
| Pvap | 0.58 | kPa | 292.91 | Measure... |
| Pvap | 0.58 | kPa | 292.91 | Measure... |
| Pvap | 0.59 | kPa | 293.15 | Measure... |
| Pvap | 0.55 | kPa | 294.10 | Vapor P... |
| Pvap | 0.58 | kPa | 295.00 | Vapor P... |
| Pvap | 0.61 | kPa | 295.20 | Vapor P... |
| Pvap | 0.69 | kPa | 298.00 | Vapor P... |
| Pvap | 0.74 | kPa | 298.20 | Vapor P... |
| Pvap | 0.83 | kPa | 301.10 | Vapor P... |
| Pvap | 0.88 | kPa | 301.20 | Vapor P... |
| Pvap | 1.09 | kPa | 302.89 | Measure... |
| Pvap | 1.10 | kPa | 302.89 | Measure... |
| Pvap | 1.11 | kPa | 303.15 | Measure... |
| Pvap | 1.02 | kPa | 304.20 | Vapor P... |
| Pvap | 1.06 | kPa | 304.20 | Vapor P... |
| Pvap | 1.24 | kPa | 307.20 | Vapor P... |
| Pvap | 1.27 | kPa | 307.20 | Vapor P... |
| Pvap | 1.44 | kPa | 309.50 | Vapor P... |
| Pvap | 1.53 | kPa | 310.20 | Vapor P... |
| Pvap | 1.96 | kPa | 312.86 | Measure... |
| Pvap | 1.96 | kPa | 312.86 | Measure... |
| Pvap | 1.99 | kPa | 313.15 | Measure... |
| Pvap | 1.87 | kPa | 313.30 | Vapor P... |
| Pvap | 2.21 | kPa | 316.30 | Vapor P... |
| Pvap | 2.94 | kPa | 320.80 | Vapor P... |
| Pvap | 3.39 | kPa | 323.03 | Measure... |
| Pvap | 3.44 | kPa | 323.15 | Measure... |
| Pvap | 4.94 | kPa | 330.40 | Vapor P... |
| Pvap | 5.63 | kPa | 333.06 | Measure... |
| Pvap | 5.71 | kPa | 333.15 | Measure... |
| Pvap | 7.44 | kPa | 338.50 | Vapor P... |
| Pvap | 9.05 | kPa | 343.05 | Measure... |
| Pvap | 9.16 | kPa | 343.15 | Measure... |
| Pvap | 9.94 | kPa | 344.70 | Vapor P... |
| Pvap | 14.45 | kPa | 353.04 | Measure... |
| Pvap | 14.29 | kPa | 353.15 | Measure... |
| Pvap | 19.90 | kPa | 360.90 | Vapor P... |
| Pvap | 21.59 | kPa | 363.10 | Measure... |
| Pvap | 21.66 | kPa | 363.15 | Measure... |
| Pvap | 29.90 | kPa | 371.20 | Vapor P... |
| Pvap | 49.90 | kPa | 385.30 | Vapor P... |
| Pvap | 75.00 | kPa | 397.60 | Vapor P... |
| Pvap | 100.00 | kPa | 406.80 | Vapor P... |
| Pvap | 120.00 | kPa | 413.10 | Vapor P... |
| Pvap | 150.00 | kPa | 420.90 | Vapor P... |
| Pvap | 200.00 | kPa | 431.60 | Vapor P... |
| Pvap | 250.10 | kPa | 440.40 | Vapor P... |
| Pvap | 300.20 | kPa | 447.80 | Vapor P... |
| ρl | [823.75; 894.96] | kg/m3 | [283.15; 363.15] |
|
|
T(K) Liquid Density (kg/m3) 820 840 860 880 900 300 320 340 360 | ||||
| ρl | 894.96 | kg/m3 | 283.15 | Volumet... |
| ρl | 888.20 | kg/m3 | 293.15 | Densiti... |
| ρl | 886.56 | kg/m3 | 293.15 | Volumet... |
| ρl | 883.34 | kg/m3 | 298.15 | Study o... |
| ρl | 884.00 | kg/m3 | 298.15 | Densiti... |
| ρl | 883.83 | kg/m3 | 298.15 | Density... |
| ρl | 879.57 | kg/m3 | 303.15 | Density... |
| ρl | 879.80 | kg/m3 | 303.15 | Densiti... |
| ρl | 878.06 | kg/m3 | 303.15 | Volumet... |
| ρl | 874.99 | kg/m3 | 308.15 | Study o... |
| ρl | 875.50 | kg/m3 | 308.15 | Densiti... |
| ρl | 869.43 | kg/m3 | 313.15 | Volumet... |
| ρl | 870.95 | kg/m3 | 313.15 | Density... |
| ρl | 871.20 | kg/m3 | 313.15 | Densiti... |
| ρl | 866.37 | kg/m3 | 318.15 | Study o... |
| ρl | 866.80 | kg/m3 | 318.15 | Densiti... |
| ρl | 862.40 | kg/m3 | 323.15 | Densiti... |
| ρl | 860.65 | kg/m3 | 323.15 | Volumet... |
| ρl | 862.20 | kg/m3 | 323.15 | Density... |
| ρl | 858.00 | kg/m3 | 328.15 | Densiti... |
| ρl | 853.50 | kg/m3 | 333.15 | Densiti... |
| ρl | 851.72 | kg/m3 | 333.15 | Volumet... |
| ρl | 853.29 | kg/m3 | 333.15 | Density... |
| ρl | 849.00 | kg/m3 | 338.15 | Densiti... |
| ρl | 844.20 | kg/m3 | 343.15 | Density... |
| ρl | 844.40 | kg/m3 | 343.15 | Densiti... |
| ρl | 842.60 | kg/m3 | 343.15 | Volumet... |
| ρl | 834.93 | kg/m3 | 353.15 | Density... |
| ρl | 833.29 | kg/m3 | 353.15 | Volumet... |
| ρl | 823.75 | kg/m3 | 363.15 | Volumet... |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 100.00 | 0.0037 |
| Reference | ||
Molar volume, m3/mol
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Molar volume, m3/mol - Liquid |
| 298.15 | 100.00 | 0.0001 |
| 298.15 | 10000.00 | 0.0001 |
| 313.15 | 100.00 | 0.0001 |
| 313.15 | 10000.00 | 0.0001 |
| 328.15 | 100.00 | 0.0001 |
| 328.15 | 10000.00 | 0.0001 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.68] | kPa | [310.72; 429.82] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.61267e+01 | |||
| Coefficient B | -4.06085e+03 | |||
| Coefficient C | -5.43380e+01 | |||
| Temperature range, min. | 310.72 | |||
| Temperature range, max. | 429.82 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 | ||||
| Pvap | 1.33 | kPa | 310.72 | Calculated Property |
| Pvap | 2.90 | kPa | 323.95 | Calculated Property |
| Pvap | 5.87 | kPa | 337.19 | Calculated Property |
| Pvap | 11.15 | kPa | 350.42 | Calculated Property |
| Pvap | 20.05 | kPa | 363.65 | Calculated Property |
| Pvap | 34.36 | kPa | 376.89 | Calculated Property |
| Pvap | 56.43 | kPa | 390.12 | Calculated Property |
| Pvap | 89.25 | kPa | 403.35 | Calculated Property |
| Pvap | 136.53 | kPa | 416.59 | Calculated Property |
| Pvap | 202.68 | kPa | 429.82 | Calculated Property |
Similar Compounds
![Ethanol, 2,2'-[(1-methylethyl)imino]bis-.](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAPoAAAD6CAIAAAAHjs1qAAAZYElEQVR4nO3de1xUZf4H8A83RRHjIoohlqHDyJCwctHlomVIGema5mUVTbxgm4oDsiaJJsZKJOtamm7WmlTbaqtl5lppbWhe1wuYICCYhXIRuchwHeZyfn8Mq2s/rjNnzjMz5/t++Y9yXuf5yuvDl+ecOed5rDiOAyHiYM26AEKEQ3EnIkJxJyJCcSciQnEnIkJxJyJCcSciQnEnIkJxJyJCcSciQnEnIkJxJyJCcSciYsu6ACJ6HIfSUlRXo1cvuLvD2fnXB2i1UKthZQU7u/bPoNFAo4GNDWxsOh+Kujth55dfsHQpBg+Gpyf8/eHjA1dX+Pvj7behVN4/7KOP0Ls3vLw6PM+SJejdGwsWdDkgdXfCyOHDmDULTU2wsoK/P4YORWsrcnJw+TJWrsSePThyBO7u/I5J3Z2wcPEipk9HUxMmTEBhIbKz8cUX+OorlJbi00/h7IzsbEyeDJWK32Ep7oSF2Fi0tiIkBF99hREj7v+7tTVmzMDXX8PODhcuYPt2foeluBPBnT6NS5cAYOtW9OrVzgHBwVi0CADFnZi/Y8cAwMsLQUEdHhMdDQA//YTr13kcmeJOBJeTAwCjR3d2zG9+A2trAMjO5nFkujNDBFdVBQCDBnV2TN++cHREXR2qq2FvDwC3bsHBof2DW1u7OTLFnQhOl86OPjO6p3dvAFAq2+JuZYU+fdo/UqOBWt2dkSnuRHAPPQQA9fVdHKZQAICTE3RLIXl4oKSk/SMXLsQHH3RnZJq7E8ENHQoAxcWdHVNSgpYWAHj0UR5HprgTwY0dCwDnz6OxscNjsrIAwM4OAQE8jkxxJ4KbOhX29mhsxJ497R+g1bbdcZ8ypcPLU71Q3IngBgxAbCwArF3b9nnTr7z2Gs6fh60t1qzhd2SKO2EhLQ1+fqirw7hxWLcOly+joQGVlTh6FJMnIzUVAFJSEBjI77B0Z4aw0LcvsrKwYAG++AKpqW35vqdfP7zxBpYt431YijthxMkJBw/i9Gl8/jkuXMCdO7C3h4cHnngCc+Y88CGURIIlS+Dq2uGpxo+HrW3bFXCnrGh9dyIeNHcngjt+HJ99xmRk6u5EWCoV/PyQn4+//x1z5gg8OHV3Iqzt25Gfj+HDMX268INTdycCqqnBiBGoqcHhw4iKEn586u5EQGvXoqYGERFMsg7q7kQ4eXnw9weA7Gz4+jIpgbo7EUp8PNRqLF/OKuug7k4Esn8/ZsyAiwuuXevsAyMjo+5OjE+pRFISAPzpTwyzDoo7EUJGBoqLIZNh8WK2hdBkhhhZaSmkUjQ04OhRTJzIthbq7sTIkpLQ0IDp05lnHdTdiXGdPYuQEPTqhdxcDB/Ouhrq7sR4OA5yOTgOiYmmkHVQdydGlJmJBQvg7o7CQvTvz7oagOJOjKWhAd7eKCvDhx9i3jzW1bShyQwxjrQ0lJUhIABz57Iu5T7q7sQIbtyAjw+USpw5gzFjWFdzH3V3YgSJiWhpwbx5JpV1UHcn/Pv+e0yYgH79UFiIhx9mXc0DqLsTPmk0mgu7drWtiGRiWQfFnfDrvffeC9q79+XQUKxaxbqWdtBkhvCmtrZWIpFUVVUdOHBg2rRprMtpB3V3wpuUlJSqqqonn3zSNLMO6u6EL/n5+X5+flqt9uLFi35+fqzLaR91d8KPhIQElUoVGxtrslkHdXfCi8OHD0+ePNnZ2fnatWsDBgxgXU6HqLsTQ7W2tiYmJgJ47bXXTDnroLgTw7399tuFhYVSqfTll19mXUsXaDJDDFJZWSmRSOrq6o4cOTJp0iTW5XSBujsxyNq1a+vq6p577jnTzzqouxND5OTkBAYGWltbX7lyxdvbm3U5XaPuTvQnl8s1Gk1cXJxZZB3U3Yne9u3bN3v27IEDBxYWFjo5ObEup1uouxN9NDc3r1mzBkBqaqq5ZB0Ud6KfzZs3//zzz/7+/gsXLmRdSw/QZIb0WGlpqbe3d2NjY1ZW1vjx41mX0wPU3UmPrV69urGxcebMmeaVdVB3Jz115syZ0NBQe3v7q1evPvroo6zL6Rnq7qQHtFqtXC7nOO6Pf/yj2WUd3enu5eXldXV1UqlUmIJEpbS09OTJky+++CLrQrqL4zgrKys3N7eCggIHBwfW5fQc16msrCxHR8cxY8ZotdrOjyR6mD17tp2dHesI9ExSUtKpU6dYf+f01EV3b2ho8Pb2Lisry8zMnD9/vmDfUzE4ffp0WFiYvb19Tk7O0KFDWZfTXXZ2djY2Nqyr0FeXPxCZmZkABg0aVFdXZ/wfP7HQaDSBgYEANmzYwLoWEek67lqtNjQ0FMCrr74qQEEisWvXLgBDhgxpaGhgXYuIdOtG5MWLF4ODg+3s7HJzc4ebxkLdZq2+vl4ikVRUVOzdu3fWrFmsyxGRbt2IDAgImDt3rlKp1D0mQQy0cePGioqKkJCQmTNnsq5FXLr7MVNFRYW3t7dCoTh69OhEE9hkx3xdv35dJpOpVKqzZ88GBQWxLkdcuvsxk7u7++rVqwHEx8er1WpjlmTh5HK5UqlcuHAhZZ2B7k/zW1padBP3nTt3GutSwtIdO3YMgKOjY1lZGetaxKgHcec4bv/+/QBcXFyqqqqMVJAFU6lUvr6+ADZv3sy6FpHqWdw5jtNN3HUPTpAe2bp1KwAvL6+WlhbWtYhUj5+IzMvL8/f3B5Cdna3rVaQ7ampqJBJJdXX1oUOHJk+ezLockerxE5EymWzx4sVqtTo+Pt4YBVmq5OTk6urqp556irLOkD7Pu99rVIcPH46KijJGWRaGfiWaCH2ed3dxcUlOTsZ/76nxXZIF0t29XbZsGWWdMf2m/CqVSiaTAcjIyODzUsISHThwAHQ7yzToGXfuf24hl5eX81iQhVEqlSNGjADwzjvvsK6FcPq/vBcREREVFVVfX79+/XqeftNYoIyMjKKiIh8fn9jYWNa1EMNezS4uLvb19VWpVOfOndM9vU3+1+3btyUSiUKh+OabbyIjI1mXQwx7NXv48OHLli2797ouXzVZjOTkDQqFYurUqZR1U2HgZKiurs7d3R3Avn37eJhbWZBz5zhX1ztPPrmsuLiYdS2kjaELb/Tv3z8lJQVAYmJiU1MTDz9/FoHjsGoVqqsHjB273cvLi3U5pA0P68wsXrw4MDDw5s2bGRkZhp/NMnz8MU6exKBBoPdhTAo/q4idOnUqPDzc3t6+oKDAjF6qN5KmJowciZIS7NkD81lCRhT4WUUsNDT0hRdeaG5ufvXVV3k5oVnbtAklJQgIwLx5rEshD+JtjcibN29KpdLm5ubjx4+Hh4fzck5zdPMmpFI0N+PECYSFsa6GPIi3NSI9PT1XrVrFcZxcLtdqtXyd1uwkJKCpCXPnUtZNEZ8rADc3N0ul0pKSkt27d8fExPB1WjNy8iTGjUOfPsjPh+gvYUwRnysA9+nTZ9OmTQCSkpIUCgWPZzYLWi3kcnAckpIo6yaK5wWv58yZExYWdvv27bS0NH7PbPreew8XL8LTEwkJrEshHeB/O4NLly4FBQXZ2trm5ubqHgYUA4UC3t6oqMCnn2LGDNbVkA7wv53B6NGj58+f39raqluXRiQ2bEBFBUJD8cILrEshHTPKZjX3ngT8+uuvn376ad7Pb2qKiyGTQa3Gf/6DgADW1ZCOGWWzmkGDBiUlJQFISEgQw5JjcXFobcWSJZR1U2esrchaW1t9fX2Lioq2b9++bNkyYwxhIo4dQ2Qk+vdHYSHc3VlXQzplrK3IevXqlZ6eDmDdunXV1dVGGoU5lQorVgDAa69R1s2AEXfee/755yMjI2tra3VPCFukbdtQWIjhw2HRv8Ash3H3Vb169aqfnx/HcdnZ2Y8//rjxBmLizh1IJLh7F//6F559lnU1pBuMu6+qj4/P0qVLNRqNXC436kBMJCfj7l1MnEhZNxtG3zW7trZ2xIgR1dXVX3zxxZQpU4w6lpAuX0ZAAKyskJMDmYx1NaR7jL5rtrOzs25ljoSEBEtacszBARMnYvlyyro5MXp3B6BWq0ePHn3lypX09HQL+6hVrYatLesiSLcJEXcA3333XUREhKOjY2Fh4eDBgwUY0UA7dqC+Hg89hJdeauerp0/jhx8wbBhoKzEzI9iaB7qJ+8KFCwUb0RCenhzAAdyBA+189fXXOYB7+mnByyKGMfrc/Z4tW7b07t17z54958+fF2xQwy1fjro61kUQnggXdy8vr7i4OK1Wu3LlSs5Mlhxzc0N5OTZsYF0H4YlwcQewbt26wYMHnzlzZu/evUKOq7fkZNjaYts2XLrEuhTCB0Hj7ujo+PrrrwNYvXp1Y2OjkEPrRyrFwoXQaPDSSxDx6+aWQ9C4A4iJiQkKCrp169bmzZsFHlo/aWlwdcX589i5k3UpxGBC3zS2trZ+6623QkND33zzzYiICA8PD8PPaWVlzXGPGH4enSFDYGd3/68uLli/HitXYu1aTJsGc7iJSjrG5H5QZGRk3759+fov9Ov3sO6mIS9/fvyR4/57I/KbbziO49Rqzt+fA7jZs9vqpxuRZorBR4Jarfb27dtNTU1ubm4ODg6Gn9DBYRCPFwK9ev36X2xs8M47CAvD3r1YtAgREbyNRQTGIO4ffPDB5cuXhwwZUlBQwEvcBRASgpgY7N6NuDhcvsy6GqIvoS9V6+vr161bB+DNN980l6zrpKfD1RX5+Xj3XdalEH0JHffU1NTy8vLf/va3s2fPFnhoAw0YgE2bAGD9etTWsq6G6EXQuF+/fv2tt96ytrbeunWrlZWVkEPzYvFijBmD2lrs3s26FKIXQeOue+R9wYIFwcHBQo7LF2tr7NgBGxvcvcu6FKIX4eL+3XffHTp0yNHRMTU1VbBBeTd6dPuPBBOzIFDcNRpNfHw8gOTkZLN43r0TmzbRh03mSqDXO7Zt2xYXF/fYY49dvXq1d+/eAoxooCtX0NqKESPQv387X/3lF1RVoX9/iGbJVwshRNzvvZ198ODB3/3ud8YeTjB1dWhoAB+PQRCBCDGZ0S0kNmHCBEvK+okTkEgQG8u6DtITRu/ulrqyEq2pZI6M3t3j4+PVavXLL79sSVkH4OaGdesAYOVKtLayroZ0j3G7+8GDB59//nlnZ+eioiJXV1fjDcSESoXHH0dhIbZsQXw862pINxixu9/bwGPjxo2Wl3UAdnb485+B/27dQUyfEeO+ZcuWoqIi3TKRxhuFragoTJoEhYJe3zYPxprMiGe/moICjBoFjYZ2qjEDxurua9asUSgUU6dOteysA5BKsWzZ/U1ViSkzSncX216Td+9CIsGdO/jnP2nnPZPGf3fnOE4ul2u12vj4eDFkHYCTEzZuBICEBDQ1sa6GdIz/uH/yySc//PDDvc33RCI2FgEBuHkTW7awLoV0jOfJTHNzs1QqLSkp2b17d0xMDI9nNn0nT2LcOPTpg/x8DB3KuhrSHp67e1paWklJyejRo1988UV+z2z6wsIwbRqampCczLoU0gE+u/vNmzelUmlzc/Px48fDw8P5Oq0ZKSnByJFobsaJEwgLY10N+X/47O6JiYlNTU2///3vxZl1AEOHIj4eHAe5nNaUNEW8dfdTp06Fh4fb29vn5+c/8ghvS9iZnaYmjByJkhLs2QPxTehMHT/dXavVyuVyjuPWrFkj5qwD6NsXundxX3kFCgXrasiD+In7+++/f+HCBU9Pz8TERF5OaNaioxEaitu3kZ7OuhTyIB4mM/X19RKJpKKiYt++fTNpby4AwMWLCA6GrS1yc+l9VhPCQ3dPSUmpqKgICQmZMWOG4WezDAEBiI5GayuSkuiK1YQY2t2Li4t9fX1VKtW5c+cCAwP5KssClJVhxox/V1bGvfvu2xMmTGBdDgEM7+5yuVypVC5atIiy/isPP4yoqLPFxXkrVqxQq9WsyyEADNvO4NixYwAcHR3Ly8sNOY+lUiqVw4cPB7Bjxw7WtRCO4zj9465SqWQyGYCMjAweC7Iw+/fvB+Di4lJVVcW6FmJA3P/yl78A8PLyamlp4bEgyzNx4kQAut1kCVt6XqrW1NRIJJLq6uovv/zyueee43FyZXny8vL8/f0BZGdn+/r6si5H1PS8VF27dm11dXVERARlvUsymWzJkiVqtVoul7OuRez06e7UrnqKfhmaCH26u25hsOXLl1PWu8nFxUW3I5Xuvi3rckSsp5N9utWgH5VKpesOmzdvZl2LePUs7i0tLbobyTt37jRSQRbs3scUZWVlrGsRqZ5NZjIyMoqLi2Uy2eLFi43wm8bC6a7s6+vr169fz7oWkerBpWpFRYW3t7dCoTh69KjuXjLpqevXr8tkMpVKdfbs2aCgINbliE4Puvvq1asVCsX06dMp63rz8vJasWLFvbdhWJcjOt3t7hcvXgwODrazs8vNzdVN34l+7r0esHfv3lmzZrEuR1y61d05jlu5cqVWq121ahVl3UCOjo4bN24EkJiY2NjYyLockenO9WxmZiaAQYMG1dXVGfO6WSw0Go3ueekNGzawrkVcup7MNDQ0eHt7l5WVZWZmzp8/X4gfQRE4ffp0WFgYLdwgsK4nM2lpaWVlZQEBAdHR0QIUJBIhISEzZ85sbm4W1UqazHXR3W/cuOHj46NUKk+cOBFG62Lx6tatW1KptLGxMT09XffmgFmQSqVeXl6sq9BX53OdvLy8sWPHRkdHCzGxEp/169eb3UwmOjp6+/btrL9zeup67s5xXFNTk4ODgzDfTVFpaWkpKipas2YN60K6q76+/uTJk+Z7ySHEJvHEksydO/eTTz6ZOXPmvn37WNfSYxR30jOlpaXe3t6NjY1ZWVnjx49nXU7PGH3XbGJhPDw8dNvlyuVyjUbDupyeoe5Oeqy5udnHx+fnn3/etWvXkiVLWJfTAxR3oo99+/bNnj174MCBhYWFTk5OrMvpLprMEH3MmjVr/PjxlZWVqbrlvc0EdXeip5ycnMDAQBsbmx9//NHb25t1Od1C3Z3oyd/fPyYmprW11YwW9afuTvRXWVkpkUjq6uqOHDkyadIk1uV0jbo70d/AgQOTk5MBJCQkqFQq1uV0jeJODBIXFyeRSAoKCnbs2MG6lq7RZIYY6ssvv5wyZYqzs/O1a9cGDBjAupzOUHcnhpo8efIzzzxTW1tr+guKUHcnPMjPz/fz89NqtZcuXRo1ahTrcjpE3Z3wYOTIkX/4wx80Go2Jr3JM3Z3wo7a2ViKRVFVVHThwYNq0aazLaR91d8IPZ2fnlJQUAImJiS0tLazLaR/FnfBm6dKlo0aNunHjhm4jIxNEcSe8sbGx0QW99tAhlJezLqcdNHcnPPtpxYrHtm/H/PnIzGRdy69R3AnffvoJMhmUSpw5gzFjWFfzAJrMEL499hji48FxkMthYs2UujsxgoYGeHujrAwffoh581hXcx91d2IE/fph0yYASEpCQwPrau6juBPjmD8fwcEoLUV6OutS7qPJDDGas2cREoJevZCbC9PYFoC6OzGasWMxdy6USpjMKsfU3YkxlZZCKkVDA44ehQls6UXdnRiThwdeeQUA4uOhVrOuhuJOjC0xEcOGIS8Pf/sb61JoMkMEsH8/ZsyAiwuKiuDiwrAQ6u7E+F54AU88gZoasF5yjLo7EUReHvz9ASAnB+x25qHuTgQhk2HRIqjVYPp2H3V3IpSaGowYgZoaHD6MqCgmJVB3J0JxcUFyMgDI5VAqmZRAcScCWrECMhmKi/HOO0zGp8kMEdaxY4iMRP/+KCyEu7vAg1N3J8KaOBHPPguFAn/9q/CDU3cngissRFYWFi+GjY3AI1PciYjYsi6AiNvx4/j8c1y6hOpq9OoFDw+Eh2POHHh6PnDMtm1wc8POne2fZMcO/PvfGD8eK1Z0MZyQO9ITcl9lJTdxIge088fenktN5bTatiP37OEAztOzw1PFxHAAFx3d5Zh0qUpYUCgwbhyOHUP//khJQW4uGhpw5w6+/RZTp6KlBcnJbU8O84riTlhISEBBAVxdcfo01q+HTAYHBwwYgKeewuefY+NGAMjIwPff8zssxZ0IrrQUH34IAJs3t/+4WHIywsLAcXjjDX5HprgTwR08CJUKTk6YM6f9A6ys2i46v/0WtbU8jkxxJ4I7dw4AgoPRu3eHx4wbBwBaLc6f53FkuhFJBFdWBgDDhnV2jLs7HBzQ2IjSUlhbA0BNDZYsaf/gU6e6OTLFnQhOoQAAB4cuDuvXD42NUCjg5AQAjY14/30DR6a4E8Hpgt7lDh9NTQDQr1/bX93c8PHH7R+5ZQu++aY7I1PcieB0e6/qpjQdUSjaFpd0c2u7WrW3R2Rk+wfv3dvNkelSlQguIAAALlzobDnse1/VHcwTijsR3DPPAMCtW/jhhw6P+egjABg1Ch4ePI5McSeC8/dHeDgAxMejubmdA06daov7ypX8jkxxJyzs3Al7e1y6hMhI5Off/3etFv/4B6KioNHgiSewYAG/w9KlKmFBJsPhw5g2DSdPwscHvr4YNgwtLcjJwZ07ABAejs8+a7vjzh+KO2HkqadQUIBNm/DZZ8jNRW4uAFhbIygIsbGIibn/rpOdHRwcOrtPb28PBwfY23c5Jr3NRExAeTnu3Gl7vcPR0XjjUNyJiNClKhERijsREYo7ERGKOxERijsREYo7ERGKOxERijsREYo7ERGKOxERijsREYo7ERGKOxGR/wMPebeKfM3UHAAAAABJRU5ErkJggg==)
Find more compounds similar to N,N-Dimethylaminoethanol.
Mixtures
- N,N-Dimethylaminoethanol + Water
- N,N-Dimethylaminoethanol + Methyl Alcohol
- Ethanol + N,N-Dimethylaminoethanol
- Carbon dioxide + N,N-Dimethylaminoethanol + Water
- 1,3-Propanediamine, N-methyl- + N,N-Dimethylaminoethanol
- 1-Propanol + N,N-Dimethylaminoethanol
- Isopropyl Alcohol + N,N-Dimethylaminoethanol
- Piperazine + N,N-Dimethylaminoethanol + Water
Sources
- Crippen Method
- Crippen Method
- Density and viscosity of aqueous solutions of N,N-dimethylethanolamine at p = 0.1 MPa from T = (293.15 to 363.15) K
- Molar excess enthalpy (HEm) for various {alkanolamine (1) + water (2)} systems at T = (298.15, 313.15, and 323.15) K
- Measurement and correlation of the (vapor + liquid) equilibria of pure 4-ethylmorpholine, 1,2-dimethylisopropylamine and N,N-dimethylethanolamine, and their binary aqueous solutions
- Density and viscosity measurements of aqueous amines at high pressures: DEA-water, DMAE-water and TEA-water mixtures
- CO2 absorption with aqueous tertiary amine solutions: Equilibrium solubility and thermodynamic modeling
- Study of intermolecular interactions in binary mixtures of 2-(dimethylamino)ethanol with methanol and ethanol at various temperatures
- Density and Viscosity of Partially Carbonated Aqueous Tertiary Alkanolamine Solutions at Temperatures between (298.15 and 353.15) K
- Density, Speed of Sound, Viscosity, and Surface Tension of Dimethylethylenediamine + Water and (Ethanolamine + Dimethylethanolamine) + Water from T = (293.15 to 323.15) K
- Densities of Aqueous 2-Dimethylaminoethanol Solutions at Temperatures of (293.15 to 343.15) K
- 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
- Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
- Vapor Pressures of Several Commercially Used Alkanolamines
- 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
- Excess Molar Enthalpies of N,N-Dimethylethanolamine with (Methanol, Ethanol, 1-Propanol, and 2-Propanol) at T ) (298.2, 313.2, and 328.2) K and p ) (0.1 and 10.0) MPa
- 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.