- InChI
- InChI=1S/C2H7NO/c3-1-2-4/h4H,1-3H2
- InChI Key
- HZAXFHJVJLSVMW-UHFFFAOYSA-N
- Formula
- C2H7NO
- SMILES
- NCCO
- Molecular Weight1
- 61.08
- CAS
- 141-43-5
- Other Names
-
- 1-Amino-2-hydroxyethane
- 2-Amino-1-Ethanol
- 2-Aminoaethanol
- 2-Aminoetanolo
- 2-Aminoethan-1-ol
- 2-Aminoethanol
- 2-Aminoethyl alcohol
- 2-Ethanolamine
- 2-Hydroxyethanamine
- 2-Hydroxyethylamine
- Aethanolamin
- Aminoethanol
- Colamine
- Etanolamina
- Ethanol, 2-amino-
- Ethanolamine
- Ethylolamine
- Glycinol
- Kolamin
- MEA
- Monoaethanolamin
- NH2CH2CH2OH
- Olamine
- Thiofaco M-50
- UN 2491
- USAF EK-1597
- «beta»-Aminoethanol
- «beta»-Aminoethyl alcohol
- «beta»-Ethanolamine
- «beta»-Hydroxyethylamine
- «beta»-Aminoethanol
- «beta»-Aminoethyl alcohol
- «beta»-Ethanolamine
- «beta»-Hydroxyethylamine
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- 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).
- ΔfH°liquid : Liquid phase 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).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- 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.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | 930.30 | kJ/mol | NIST |
| BasG | 896.80 | kJ/mol | NIST |
| ΔfG° | -104.41 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -203.05 | kJ/mol | Joback Calculated Property |
| ΔfH°liquid | -507.50 | kJ/mol | NIST |
| ΔfusH° | 10.22 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 47.37 | kJ/mol | Joback Calculated Property |
| IE | [8.90; 9.88] | eV |
|
| IE | 8.96 | eV | NIST |
| IE | 8.90 | eV | NIST |
| IE | 8.96 | eV | NIST |
| IE | 8.96 | eV | NIST |
| IE | 9.88 | eV | NIST |
| IE | 9.88 | eV | NIST |
| IE | 9.87 ± 0.06 | eV | NIST |
| log10WS | 0.64 | Crippen Calculated Property | |
| logPoct/wat | -1.063 | Crippen Calculated Property | |
| McVol | 54.890 | ml/mol | McGowan Calculated Property |
| Pc | 8030.00 ± 40.00 | kPa | NIST |
| Inp | [643.00; 698.00] |
|
|
| Inp | 698.00 | NIST | |
| Inp | 643.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 643.00 | NIST | |
| I | [1402.00; 1470.00] |
|
|
| I | 1402.00 | NIST | |
| I | 1470.00 | NIST | |
| I | 1450.00 | NIST | |
| I | 1411.00 | NIST | |
| I | 1413.00 | NIST | |
| I | 1427.00 | NIST | |
| I | 1402.00 | NIST | |
| I | 1427.00 | NIST | |
| Tboil | [443.20; 444.15] | K |
|
| Tboil | 443.20 | K | NIST |
| Tboil | 444.00 | K | NIST |
| Tboil | 444.15 ± 1.50 | K | NIST |
| Tboil | 443.55 | K | NIST |
| Tboil | 444.00 ± 0.50 | K | NIST |
| Tc | [670.00; 671.40] | K |
|
| Tc | 671.40 ± 1.50 | K | NIST |
| Tc | 670.00 ± 50.00 | K | NIST |
| Tfus | [283.45; 283.70] | K |
|
| Tfus | 283.45 | K | NIST |
| Tfus | 283.46 ± 0.05 | K | NIST |
| Tfus | 283.70 ± 0.60 | K | NIST |
| Vc | 0.196 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [107.21; 135.10] | J/mol×K | [409.87; 588.15] |
|
| Cp,gas | 107.21 | J/mol×K | 409.87 | Joback Calculated Property |
| Cp,gas | 112.35 | J/mol×K | 439.58 | Joback Calculated Property |
| Cp,gas | 117.29 | J/mol×K | 469.30 | Joback Calculated Property |
| Cp,gas | 122.02 | J/mol×K | 499.01 | Joback Calculated Property |
| Cp,gas | 126.57 | J/mol×K | 528.72 | Joback Calculated Property |
| Cp,gas | 130.93 | J/mol×K | 558.43 | Joback Calculated Property |
| Cp,gas | 135.10 | J/mol×K | 588.15 | Joback Calculated Property |
| Cp,liquid | [163.70; 182.00] | J/mol×K | [303.15; 353.15] |
|
| Cp,liquid | 168.00 | J/mol×K | 303.15 | Molar H... |
| Cp,liquid | 163.70 | J/mol×K | 303.15 | Density... |
| Cp,liquid | 169.00 | J/mol×K | 308.15 | Molar H... |
| Cp,liquid | 169.00 | J/mol×K | 313.15 | Molar H... |
| Cp,liquid | 167.98 | J/mol×K | 313.15 | Density... |
| Cp,liquid | 171.00 | J/mol×K | 318.15 | Molar H... |
| Cp,liquid | 173.00 | J/mol×K | 323.15 | Molar H... |
| Cp,liquid | 172.25 | J/mol×K | 323.15 | Density... |
| Cp,liquid | 174.00 | J/mol×K | 328.15 | Molar H... |
| Cp,liquid | 175.00 | J/mol×K | 333.15 | Molar H... |
| Cp,liquid | 178.00 | J/mol×K | 338.15 | Molar H... |
| Cp,liquid | 179.00 | J/mol×K | 343.15 | Molar H... |
| Cp,liquid | 180.00 | J/mol×K | 348.15 | Molar H... |
| Cp,liquid | 182.00 | J/mol×K | 353.15 | Molar H... |
| η | [0.0013760; 0.0199000] | Pa×s | [298.15; 393.15] |
|
| η | 0.0199000 | Pa×s | 298.15 | Density... |
| η | 0.0144230 | Pa×s | 303.15 | Viscome... |
| η | 0.0096100 | Pa×s | 313.15 | Density... |
| η | 0.0095620 | Pa×s | 313.15 | Viscome... |
| η | 0.0066650 | Pa×s | 323.15 | Viscome... |
| η | 0.0067200 | Pa×s | 323.15 | Density... |
| η | 0.0048140 | Pa×s | 333.15 | Viscome... |
| η | 0.0035510 | Pa×s | 343.15 | Viscome... |
| η | 0.0036900 | Pa×s | 343.15 | Density... |
| η | 0.0028500 | Pa×s | 353.15 | Density... |
| η | 0.0027640 | Pa×s | 353.15 | Viscome... |
| η | 0.0023370 | Pa×s | 363.15 | Viscome... |
| η | 0.0019010 | Pa×s | 373.15 | Viscome... |
| η | 0.0015880 | Pa×s | 383.15 | Viscome... |
| η | 0.0013760 | Pa×s | 393.15 | Viscome... |
| ΔvapH | [54.70; 61.70] | kJ/mol | [377.00; 411.00] |
|
| ΔvapH | 61.70 | kJ/mol | 377.00 | NIST |
| ΔvapH | 58.90 | kJ/mol | 390.50 | NIST |
| ΔvapH | 55.90 | kJ/mol | 396.00 | NIST |
| ΔvapH | 54.70 | kJ/mol | 411.00 | NIST |
| Pvap | [8.48e-03; 97.50] | kPa | [279.00; 442.28] |
|
| Pvap | 8.48e-03 | kPa | 279.00 | Vapor P... |
| Pvap | 0.01 | kPa | 281.10 | Vapor P... |
| Pvap | 0.02 | kPa | 283.34 | Isother... |
| Pvap | 0.03 | kPa | 288.34 | Isother... |
| Pvap | 0.04 | kPa | 293.34 | Isother... |
| Pvap | 0.03 | kPa | 294.00 | Vapor P... |
| Pvap | 0.04 | kPa | 297.20 | Vapor P... |
| Pvap | 0.06 | kPa | 298.34 | Isother... |
| Pvap | 0.05 | kPa | 300.20 | Vapor P... |
| Pvap | 0.06 | kPa | 303.20 | Vapor P... |
| Pvap | 0.09 | kPa | 303.34 | Isother... |
| Pvap | 0.08 | kPa | 306.30 | Vapor P... |
| Pvap | 0.13 | kPa | 308.34 | Isother... |
| Pvap | 0.11 | kPa | 309.40 | Vapor P... |
| Pvap | 0.13 | kPa | 312.40 | Vapor P... |
| Pvap | 0.19 | kPa | 313.34 | Isother... |
| Pvap | 0.17 | kPa | 315.40 | Vapor P... |
| Pvap | 0.27 | kPa | 318.34 | Isother... |
| Pvap | 0.20 | kPa | 318.40 | Vapor P... |
| Pvap | 0.26 | kPa | 321.40 | Vapor P... |
| Pvap | 0.38 | kPa | 323.34 | Isother... |
| Pvap | 0.31 | kPa | 324.50 | Vapor P... |
| Pvap | 0.53 | kPa | 328.34 | Isother... |
| Pvap | 0.74 | kPa | 333.34 | Isother... |
| Pvap | 1.01 | kPa | 338.34 | Isother... |
| Pvap | 1.36 | kPa | 343.34 | Isother... |
| Pvap | 1.83 | kPa | 348.34 | Isother... |
| Pvap | 2.43 | kPa | 353.34 | Isother... |
| Pvap | 2.98 | kPa | 357.46 | Ebullio... |
| Pvap | 3.19 | kPa | 358.34 | Isother... |
| Pvap | 3.02 | kPa | 358.60 | Vapor P... |
| Pvap | 3.98 | kPa | 362.99 | Ebullio... |
| Pvap | 4.11 | kPa | 363.09 | Isother... |
| Pvap | 5.48 | kPa | 369.33 | Ebullio... |
| Pvap | 6.40 | kPa | 373.00 | Vapor P... |
| Pvap | 6.17 | kPa | 373.15 | Vapor L... |
| Pvap | 6.64 | kPa | 373.15 | Vapor L... |
| Pvap | 6.16 | kPa | 373.15 | Vapor L... |
| Pvap | 6.98 | kPa | 374.29 | Ebullio... |
| Pvap | 8.47 | kPa | 378.41 | Ebullio... |
| Pvap | 10.97 | kPa | 384.07 | Ebullio... |
| Pvap | 11.70 | kPa | 385.70 | Vapor P... |
| Pvap | 14.96 | kPa | 391.14 | Ebullio... |
| Pvap | 19.97 | kPa | 398.01 | Ebullio... |
| Pvap | 24.97 | kPa | 403.43 | Ebullio... |
| Pvap | 24.90 | kPa | 403.60 | Vapor P... |
| Pvap | 29.97 | kPa | 408.19 | Ebullio... |
| Pvap | 39.98 | kPa | 415.78 | Ebullio... |
| Pvap | 39.95 | kPa | 415.81 | Ebullio... |
| Pvap | 51.10 | kPa | 422.70 | Vapor P... |
| Pvap | 50.62 | kPa | 423.15 | Vapor L... |
| Pvap | 52.71 | kPa | 423.15 | Vapor L... |
| Pvap | 51.97 | kPa | 423.15 | Vapor L... |
| Pvap | 54.95 | kPa | 424.61 | Ebullio... |
| Pvap | 64.95 | kPa | 429.44 | Ebullio... |
| Pvap | 69.95 | kPa | 431.61 | Ebullio... |
| Pvap | 71.80 | kPa | 432.60 | Vapor P... |
| Pvap | 79.95 | kPa | 435.61 | Ebullio... |
| Pvap | 97.50 | kPa | 441.90 | Vapor P... |
| Pvap | 95.30 | kPa | 442.28 | Activit... |
| n0 | [1.43472; 1.45601] | [293.15; 353.15] |
|
|
| n0 | 1.45601 | 293.15 | Densiti... | |
| n0 | 1.45250 | 293.15 | Density... | |
| n0 | 1.45420 | 293.15 | Experim... | |
| n0 | 1.45432 | 298.15 | Densiti... | |
| n0 | 1.45250 | 298.15 | Vapor-L... | |
| n0 | 1.44880 | 303.15 | Density... | |
| n0 | 1.45273 | 303.15 | Densiti... | |
| n0 | 1.44490 | 313.15 | Density... | |
| n0 | 1.44913 | 313.15 | Densiti... | |
| n0 | 1.44170 | 323.15 | Density... | |
| n0 | 1.44561 | 323.15 | Densiti... | |
| n0 | 1.44213 | 333.15 | Densiti... | |
| n0 | 1.43862 | 343.15 | Densiti... | |
| n0 | 1.43472 | 353.15 | Densiti... | |
| ρl | [959.54; 1025.55] | kg/m3 | [281.15; 363.15] |
|
| ρl | 1025.55 | kg/m3 | 281.15 | Volumet... |
| ρl | 1023.99 | kg/m3 | 283.15 | Volumet... |
| ρl | 1024.11 | kg/m3 | 283.15 | Densiti... |
| ρl | 1022.42 | kg/m3 | 285.15 | Volumet... |
| ρl | 1020.84 | kg/m3 | 287.15 | Volumet... |
| ρl | 1019.87 | kg/m3 | 288.15 | Excess ... |
| ρl | 1019.26 | kg/m3 | 289.15 | Volumet... |
| ρl | 1017.68 | kg/m3 | 291.15 | Volumet... |
| ρl | 1016.90 | kg/m3 | 293.15 | Volumet... |
| ρl | 1016.10 | kg/m3 | 293.15 | Density... |
| ρl | 1016.70 | kg/m3 | 293.15 | Monoeth... |
| ρl | 1016.47 | kg/m3 | 293.15 | Volumet... |
| ρl | 1015.50 | kg/m3 | 293.15 | Volumet... |
| ρl | 1016.30 | kg/m3 | 293.15 | Volumet... |
| ρl | 1015.96 | kg/m3 | 293.15 | Solubil... |
| ρl | 1016.23 | kg/m3 | 293.15 | Densiti... |
| ρl | 1012.10 | kg/m3 | 293.15 | Viscosi... |
| ρl | 1017.90 | kg/m3 | 293.15 | Experim... |
| ρl | 1016.00 | kg/m3 | 293.15 | Volumet... |
| ρl | 1016.10 | kg/m3 | 293.15 | Volumet... |
| ρl | 1016.34 | kg/m3 | 293.16 | Volumet... |
| ρl | 1014.52 | kg/m3 | 295.15 | Volumet... |
| ρl | 1012.94 | kg/m3 | 297.15 | Volumet... |
| ρl | 1012.94 | kg/m3 | 297.15 | Volumet... |
| ρl | 1012.40 | kg/m3 | 298.15 | Thermod... |
| ρl | 1012.53 | kg/m3 | 298.15 | Volumet... |
| ρl | 1011.98 | kg/m3 | 298.15 | Density... |
| ρl | 1011.79 | kg/m3 | 298.15 | Hydroge... |
| ρl | 1011.98 | kg/m3 | 298.15 | Density... |
| ρl | 1012.38 | kg/m3 | 298.15 | Physico... |
| ρl | 1012.40 | kg/m3 | 298.15 | Thermod... |
| ρl | 1012.00 | kg/m3 | 298.15 | Volumet... |
| ρl | 1012.12 | kg/m3 | 298.15 | Excess ... |
| ρl | 1012.80 | kg/m3 | 298.15 | Monoeth... |
| ρl | 1011.35 | kg/m3 | 299.15 | Volumet... |
| ρl | 1009.76 | kg/m3 | 301.15 | Volumet... |
| ρl | 1008.40 | kg/m3 | 303.14 | Volumet... |
| ρl | 1008.32 | kg/m3 | 303.15 | Densiti... |
| ρl | 1008.72 | kg/m3 | 303.15 | Volumet... |
| ρl | 1010.67 | kg/m3 | 303.15 | Densiti... |
| ρl | 1009.50 | kg/m3 | 303.15 | Volumet... |
| ρl | 1008.80 | kg/m3 | 303.15 | Monoeth... |
| ρl | 1007.90 | kg/m3 | 303.15 | Densiti... |
| ρl | 1008.00 | kg/m3 | 303.15 | Volumet... |
| ρl | 1007.60 | kg/m3 | 303.15 | Volumet... |
| ρl | 1008.40 | kg/m3 | 303.15 | Thermod... |
| ρl | 1008.40 | kg/m3 | 303.15 | Thermod... |
| ρl | 1008.40 | kg/m3 | 303.15 | Density... |
| ρl | 1008.80 | kg/m3 | 303.15 | Solubil... |
| ρl | 1008.02 | kg/m3 | 303.15 | Volumet... |
| ρl | 1009.35 | kg/m3 | 303.15 | Physico... |
| ρl | 1008.05 | kg/m3 | 303.15 | Solubil... |
| ρl | 1008.17 | kg/m3 | 303.15 | Volumet... |
| ρl | 1008.47 | kg/m3 | 303.15 | Volumet... |
| ρl | 1006.58 | kg/m3 | 305.15 | Volumet... |
| ρl | 1004.99 | kg/m3 | 307.15 | Volumet... |
| ρl | 1004.50 | kg/m3 | 308.15 | Thermod... |
| ρl | 1004.90 | kg/m3 | 308.15 | Monoeth... |
| ρl | 1004.20 | kg/m3 | 308.15 | Densiti... |
| ρl | 1006.80 | kg/m3 | 308.15 | Liquid-... |
| ρl | 1004.68 | kg/m3 | 308.15 | Hydroge... |
| ρl | 1004.49 | kg/m3 | 308.15 | Volumet... |
| ρl | 1004.50 | kg/m3 | 308.15 | Thermod... |
| ρl | 1004.65 | kg/m3 | 308.15 | Volumet... |
| ρl | 1003.40 | kg/m3 | 309.15 | Volumet... |
| ρl | 1001.80 | kg/m3 | 311.15 | Volumet... |
| ρl | 1000.41 | kg/m3 | 313.14 | Volumet... |
| ρl | 1000.90 | kg/m3 | 313.15 | Solubil... |
| ρl | 999.98 | kg/m3 | 313.15 | Volumet... |
| ρl | 1000.09 | kg/m3 | 313.15 | Solubil... |
| ρl | 1000.37 | kg/m3 | 313.15 | Densiti... |
| ρl | 1002.77 | kg/m3 | 313.15 | Densiti... |
| ρl | 1000.90 | kg/m3 | 313.15 | Monoeth... |
| ρl | 1002.16 | kg/m3 | 313.15 | Physico... |
| ρl | 1000.21 | kg/m3 | 313.15 | Volumet... |
| ρl | 1000.00 | kg/m3 | 313.15 | Volumet... |
| ρl | 1001.10 | kg/m3 | 313.15 | Volumet... |
| ρl | 1000.10 | kg/m3 | 313.15 | Density... |
| ρl | 999.70 | kg/m3 | 313.15 | Volumet... |
| ρl | 1000.50 | kg/m3 | 313.15 | Volumet... |
| ρl | 1000.74 | kg/m3 | 313.15 | Volumet... |
| ρl | 1000.50 | kg/m3 | 313.15 | Densiti... |
| ρl | 998.60 | kg/m3 | 315.15 | Volumet... |
| ρl | 997.00 | kg/m3 | 317.15 | Volumet... |
| ρl | 998.15 | kg/m3 | 318.15 | Hydroge... |
| ρl | 996.39 | kg/m3 | 318.15 | Volumet... |
| ρl | 996.20 | kg/m3 | 318.15 | Densiti... |
| ρl | 996.90 | kg/m3 | 318.15 | Monoeth... |
| ρl | 996.04 | kg/m3 | 318.15 | Volumet... |
| ρl | 995.40 | kg/m3 | 319.15 | Volumet... |
| ρl | 993.79 | kg/m3 | 321.15 | Volumet... |
| ρl | 992.38 | kg/m3 | 323.15 | Volumet... |
| ρl | 992.36 | kg/m3 | 323.15 | Densiti... |
| ρl | 992.70 | kg/m3 | 323.15 | Densiti... |
| ρl | 991.97 | kg/m3 | 323.15 | Volumet... |
| ρl | 992.19 | kg/m3 | 323.15 | Volumet... |
| ρl | 992.00 | kg/m3 | 323.15 | Volumet... |
| ρl | 992.07 | kg/m3 | 323.15 | Solubil... |
| ρl | 992.90 | kg/m3 | 323.15 | Monoeth... |
| ρl | 991.90 | kg/m3 | 323.15 | Density... |
| ρl | 992.70 | kg/m3 | 323.15 | Volumet... |
| ρl | 994.40 | kg/m3 | 323.15 | Physico... |
| ρl | 991.70 | kg/m3 | 323.15 | Volumet... |
| ρl | 992.41 | kg/m3 | 323.15 | Volumet... |
| ρl | 994.80 | kg/m3 | 323.15 | Densiti... |
| ρl | 990.58 | kg/m3 | 325.15 | Volumet... |
| ρl | 988.96 | kg/m3 | 327.15 | Volumet... |
| ρl | 988.70 | kg/m3 | 328.15 | Densiti... |
| ρl | 988.80 | kg/m3 | 328.15 | Monoeth... |
| ρl | 987.34 | kg/m3 | 329.15 | Volumet... |
| ρl | 985.72 | kg/m3 | 331.15 | Volumet... |
| ρl | 984.30 | kg/m3 | 333.14 | Volumet... |
| ρl | 983.60 | kg/m3 | 333.15 | Density... |
| ρl | 984.30 | kg/m3 | 333.15 | Densiti... |
| ρl | 983.98 | kg/m3 | 333.15 | Solubil... |
| ρl | 986.24 | kg/m3 | 333.15 | Physico... |
| ρl | 984.30 | kg/m3 | 333.15 | Volumet... |
| ρl | 983.60 | kg/m3 | 333.15 | Volumet... |
| ρl | 984.80 | kg/m3 | 333.15 | Monoeth... |
| ρl | 986.75 | kg/m3 | 333.15 | Densiti... |
| ρl | 984.10 | kg/m3 | 333.15 | Volumet... |
| ρl | 982.48 | kg/m3 | 335.15 | Volumet... |
| ρl | 980.85 | kg/m3 | 337.15 | Volumet... |
| ρl | 980.70 | kg/m3 | 338.15 | Monoeth... |
| ρl | 979.21 | kg/m3 | 339.15 | Volumet... |
| ρl | 977.58 | kg/m3 | 341.15 | Volumet... |
| ρl | 976.14 | kg/m3 | 343.14 | Volumet... |
| ρl | 976.60 | kg/m3 | 343.15 | Monoeth... |
| ρl | 975.94 | kg/m3 | 343.15 | Volumet... |
| ρl | 978.62 | kg/m3 | 343.15 | Densiti... |
| ρl | 976.15 | kg/m3 | 343.15 | Densiti... |
| ρl | 974.30 | kg/m3 | 345.15 | Volumet... |
| ρl | 972.65 | kg/m3 | 347.15 | Volumet... |
| ρl | 972.50 | kg/m3 | 348.15 | Monoeth... |
| ρl | 970.99 | kg/m3 | 349.15 | Volumet... |
| ρl | 969.34 | kg/m3 | 351.15 | Volumet... |
| ρl | 967.89 | kg/m3 | 353.14 | Volumet... |
| ρl | 968.40 | kg/m3 | 353.15 | Monoeth... |
| ρl | 967.68 | kg/m3 | 353.15 | Volumet... |
| ρl | 970.40 | kg/m3 | 353.15 | Densiti... |
| ρl | 968.33 | kg/m3 | 353.15 | Excess ... |
| ρl | 959.54 | kg/m3 | 363.15 | Volumet... |
| csound,fluid | [1637.20; 1735.46] | m/s | [293.15; 323.15] |
|
| csound,fluid | 1734.40 | m/s | 293.15 | Density... |
| csound,fluid | 1735.46 | m/s | 293.15 | Density... |
| csound,fluid | 1719.23 | m/s | 298.15 | Density... |
| csound,fluid | 1702.10 | m/s | 303.15 | Density... |
| csound,fluid | 1703.09 | m/s | 303.15 | Density... |
| csound,fluid | 1686.79 | m/s | 308.15 | Density... |
| csound,fluid | 1670.10 | m/s | 313.15 | Density... |
| csound,fluid | 1670.54 | m/s | 313.15 | Density... |
| csound,fluid | 1654.19 | m/s | 318.15 | Density... |
| csound,fluid | 1637.20 | m/s | 323.15 | Density... |
| csound,fluid | 1637.86 | m/s | 323.15 | Density... |
| γ | [0.04; 0.05] | N/m | [293.15; 333.15] |
|
| γ | 0.05 | N/m | 293.15 | Densiti... |
| γ | 0.05 | N/m | 293.15 | Density... |
| γ | 0.05 | N/m | 303.15 | Densiti... |
| γ | 0.05 | N/m | 303.15 | Density... |
| γ | 0.05 | N/m | 303.15 | Density... |
| γ | 0.05 | N/m | 303.20 | Investi... |
| γ | 0.05 | N/m | 313.15 | Densiti... |
| γ | 0.05 | N/m | 313.15 | Density... |
| γ | 0.05 | N/m | 313.15 | Density... |
| γ | 0.05 | N/m | 313.20 | Investi... |
| γ | 0.05 | N/m | 323.15 | Density... |
| γ | 0.04 | N/m | 323.20 | Investi... |
| γ | 0.04 | N/m | 333.15 | Density... |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 100.00 | 0.0187 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 1012.0 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.01; 6609.81] | kPa | [283.65; 638.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.62291e+02 | |||
| Coefficient B | -1.33605e+04 | |||
| Coefficient C | -2.13543e+01 | |||
| Coefficient D | 1.31668e-05 | |||
| Temperature range, min. | 283.65 | |||
| Temperature range, max. | 638.00 | |||
| Pvap | 0.01 | kPa | 283.65 | Calculated Property |
| Pvap | 0.34 | kPa | 323.02 | Calculated Property |
| Pvap | 3.74 | kPa | 362.39 | Calculated Property |
| Pvap | 22.75 | kPa | 401.77 | Calculated Property |
| Pvap | 93.06 | kPa | 441.14 | Calculated Property |
| Pvap | 289.19 | kPa | 480.51 | Calculated Property |
| Pvap | 742.24 | kPa | 519.88 | Calculated Property |
| Pvap | 1668.11 | kPa | 559.26 | Calculated Property |
| Pvap | 3422.56 | kPa | 598.63 | Calculated Property |
| Pvap | 6609.81 | kPa | 638.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Monoethanolamine.
Mixtures
- Monoethanolamine + 2-Pyrrolidinone, 1-methyl-
- Monoethanolamine + Thiophene, tetrahydro-, 1,1-dioxide
- Monoethanolamine + Methyldiethanolamine + Water
- Monoethanolamine + Carbon dioxide + Water
- Naphthalene, 2-methyl- + Monoethanolamine + Indole
- Monoethanolamine + 1,4-Dioxane
- Monoethanolamine + 1,2-Ethanediamine, N-(2-aminoethyl)-
- Monoethanolamine + Ethanol, 2-[(2-aminoethyl)amino]-
- Monoethanolamine + Water
- Monoethanolamine + Dimethyl Sulfoxide
- Monoethanolamine + m-Chloroaniline
- Monoethanolamine + Estrone
- Monoethanolamine + N,N-Diethyl-2-aminoethanol + Water
- Diosgenin + Monoethanolamine
- Estriol + Monoethanolamine
- Monoethanolamine + 2-Propanol, 1-(dimethylamino)- + Water
- Monoethanolamine + Methyl Alcohol + Water
- Monoethanolamine + Carbon dioxide + Ethanol, 2-methoxy-
- Monoethanolamine + Ethanol, 2-methoxy-
- Monoethanolamine + Ethanol
Find more mixtures with Monoethanolamine.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Vapor Liquid Equilibrium for Binary Mixtures of 1,4-Diazabicyclo[2.2.2]octane with Ethylenediamine, Ethanolamine, and Ethylene Glycol
- Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
- High pressure solubility of carbon dioxide (CO2) in aqueous piperazine solutions
- Experiment and model for the viscosity of carbonated MDEA - MEA aqueous solutions
- Experiment and model for the surface tension of carbonated MEA-MDEA aqueous solutions
- Solubility of CO2 in aqueous mixtures of monoethanolamine and dicyanamide-based ionic liquids
- CO2 solubility measurement and thermodynamic modeling for 1-methylpiperazine/water/CO2
- Liquid-liquid phase equilibrium for ternary mixtures of formamide (or ethylene glycol, or monoethanolamine) + indole + 2-methylnaphthalene at 308.15 K
- Vapor-liquid equilibrium measurement and ENRTL Modeling of CO2 absorption in aqueous hexamethylenediamine
- Hydrogen bond interactions in the blends of 1,4-dioxane with some 1, 2- disubstituted ethanes at T = (298.15, 308.15 and 318.15) K
- Monoethanolamine-based deep eutectic solvents, their synthesis and characterization
- Thermodynamic properties and CO2 solubility of monoethanolamine + diethylenetriamine/aminoethylethanolamine mixtures: Experimental measurements and thermodynamic modeling
- Effective extraction of benzene and thiophene by novel deep eutectic solvents from hexane / aromatic mixture at different temperatures
- Viscosity of aqueous solutions of 2-methoxyethanol, 2-ethoxyethanol, and ethanolamine
- Solubility data for toluene in various aqueous alkanolamine solutions
- Volumetric properties of binary mixtures of dimethyl sulfoxide with amines from (293.15 to 363.15) K
- Equilibrium solubility of carbon dioxide in aqueous solutions of (diethylenetriamine + piperazine)
- Experiment and model for the surface tension of MEA-PEG400 and DEA-PEG400 aqueous solutions
- Experiment and model for the surface tension of amine - ionic liquids aqueous solutions
- Experiment and model for the viscosities of MEA-PEG400, DEA-PEG400 and MDEA-PEG400 aqueous solutions
- Carbon dioxide solubility in aqueous potassium salt solutions of L-proline and DL-.alpha.-aminobutyric acid at high pressures
- Volumetric, acoustic and spectroscopic properties of 3-chloroaniline with substituted ethanols at various temperatures
- Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
- Viscosity and density measurements of aqueous amines at high pressures: MDEA-water and MEA-water mixtures for CO2 capture
- Volumetric and viscometric properties of binary and ternary mixtures of 1-butyl-3-methylimidazolium tetrafluoroborate, monoethanolamine and water
- Experiments and model for the surface tension of DEAE-PZ and DEAE-MEA aqueous solutions
- Experimental solubility of diosgenin and estriol in various solvents between T = (293.2-328.2) K
- Surface thermodynamics of DMA2P, DMA2P-MEA and DMA2P-PZ aqueous solutions
- CO2 solubility in aqueous potassium lysinate solutions at absorber conditions
- Absorption performance of (CO2 + N2) gas mixtures in amino acid ionic liquids promoted N-methyldiethanolamine aqueous solutions
- CO2 absorption using aqueous potassium lysinate solutions: Vapor - liquid equilibrium data and modelling
- Investigation of surface tension and viscosity for aqueous solutions of MEA-MeOH and DEA-MeOH
- Volumetric, acoustic and transport properties of mixtures containing dimethyl sulfoxide and some amines or alkanolamines: Measurement and correlation
- Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
- Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
- Volumetric and viscometric properties of ternary solution of (N-methyldiethanolamine + monoethanolamine + ethanol)
- Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
- Vapour-liquid equilibrium study of tertiary amines, single and in blend with 3-(methylamino)propylamine, for post-combustion CO2 capture
- Volumetric and viscometric properties of binary and ternary mixtures of monoethanolamine, 2-(diethylamino) ethanol and water from (293.15 to 333.15) K
- Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
- Low-temperature thermal properties of the aqueous solutions of simple aminoalcohols: Finding of peculiarities in 1-amino-2-propanol solutions
- CO2 Solubility in Hybrid Solvents Containing 1-Butyl-3- methylimidazolium tetrafluoroborate and Mixtures of Alkanolamines
- 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
- Effect of the Presence of MEA on the CO2 Capture Ability of Superbase Ionic Liquids
- Specific Heat Capacities of Two Functional Ionic Liquids and Two Functional Deep Eutectic Solvents for the Absorption of SO2
- Characteristics of Potassium Prolinate + Water + Ethanol Solution as a Phase Changing Absorbent for CO2 Capture
- Density, Viscosity, Refractive Index, and Electrical Conductivity of Degraded Monoethanolamine Solutions at Standard Temperatures
- Density, Viscosity, and N2O Solubility of Aqueous Solutions of MEA, BmimBF4, and Their Mixtures from 293.15 to 333.15 K
- Investigation of Thermodynamic Properties on CO2 Absorbents Blended with Ammonia, Amino Acids, and Corrosion Inhibitors at 313.15, 333.15, and 353.15 K
- Viscosity, Density, and Volatility of Binary Mixtures of Imidazole, 2-Methylimidazole, 2,4,5-Trimethylimidazole, and 1,2,4,5-Tetramethylimidazole with Water
- Liquid-Liquid Equilibrium Measurements and Correlation for Ternary Systems (Butyl Acetate + 1-Butanol + Ethylene Glycol/1,3-Propanediol/Ethanolamine) at 298.15 K
- Liquid-Liquid Equilibria for Benzene/Thiophene + Cyclohexane/Hexadecane + Deep Eutectic Solvents: Data and Correlation
- Density and Viscosity of Aqueous Solutions of (N-Methyldiethanolamine + Monoethanolamine), (N-Methyldiethanolamine + Diethanolamine), (2-Amino-2-methyl-1-propanol + Monoethanolamine) and (2-Amino-2-methyl-1-propanol + Diethanolamine
- Volumetric Properties of Water + Monoethanolamine + Methanol Mixtures at Atmospheric Pressure from 283.15 to 353.15 K
- Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
- Solubility of Ethane in Aqueous Solutions of Monoethanolamine and Diethanolamine
- Density and Viscosity of Aqueous Solutions of 2-Piperidineethanol, (2-Piperidineethanol + Monoethanolamine), and (2-Piperidineethanol + Diethanolamine) from (288 to 333) K
- Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
- Density, Viscosity, and Performances of Carbon Dioxide Capture in 16 Absorbents of Amine + Ionic Liquid + H2O, Ionic Liquid + H2O, and Amine + H2O Systems
- Densities and Excess Molar Volumes of Binary Mixtures of Bis(2-hydroxyethyl)ammonium Acetate + Water and Monoethanolamine + Bis(2-hydroxyethyl)ammonium Acetate at Temperatures from (303.15 to 353.15) K
- Density, Speed of Sound, Viscosity, Refractive Index, and Excess Volume of N-Methyl-2-pyrrolidone + Ethanol (or Water or Ethanolamine) from T = (293.15 to 323.15) K
- Freezing Point Depressions of Aqueous MEA, MDEA, and MEA-MDEA Measured with a New Apparatus
- Density, Viscosity, Heat Capacity, Surface Tension, and Solubility of CO2 in Aqueous Solutions of Potassium Serinate
- CO2 Absorption Rate into Concentrated Aqueous Monoethanolamine and Piperazine
- Vapor Pressures of Several Commercially Used Alkanolamines
- Densities, Refractive Indices and Excess Properties of Binary Mixtures of 1-Butyl-3-Methylimidazolium Tetraflouroborate with Water and Monoethanolamine
- Density of Water (1) + Monoethanolamine (2) + CO2 (3) from (298.15 to 413.15) K and Surface Tension of Water (1) + Monoethanolamine (2) from (303.15 to 333.15) K
- Activity Coefficients and Excess Gibbs Energies for Binary Mixtures of N-Methyl-2-pyrrolidone with Some Substituted Ethanols
- Density, Speed of Sound, and Viscosity of N-Methyl-2-pyrrolidone + Ethanolamine + Water from T = (293.15 to 323.15) K
- Densities, Viscosities and Excess Properties of Binary Mixtures of 1,1,3,3-Tetramethylguanidinium Lactate + Water at T = (303.15 to 328.15) K
- Density and Surface Tension Measurements of Partially Carbonated Aqueous Monoethanolamine Solutions
- Solubility of Carbon Dioxide in Aqueous Solutions of Monoethanolamine in the Low and High Gas Loading Regions
- Oxygen Solubility Measurements in a MEA/H2O/CO2 Mixture
- Density, Speed of Sound, Viscosity, Surface Tension, and Excess Volume of N-Ethyl-2-pyrrolidone + Ethanolamine (or Diethanolamine or Triethanolamine) from T = (293.15 to 323.15) K
- Densities and Surface Tensions of CO2 Loaded Aqueous Monoethanolamine Solutions with r = (0.2 to 0.7) at T = (303.15 to 333.15) K
- Densities and Excess Properties of Primary Amines in Alcoholic Solutions
- Solubility of N2O in Density and Viscosity of Aqueous Solutions of 1,4-Butanediamine, 2-(Diethylamino)-ethanol, and Their Mixtures from (298.15 to 333.15) K
- Density and Viscosity for Binary Mixtures of Diethylene Glycol Monobutyl Ether with Monoethanolamine, Diethanolamine, and Triethanolamine from (293.15 to 333.15) K
- Excess Enthalpy and Excess Volume for Pyridine + Methyldiethanolamine and Pyridine + Ethanolamine Mixtures
- Density, Speed of Sound, and Viscosity of Monoethanolamine + Water + N-Ethyl-2-pyrrolidone from T = (293.15 to 323.15) K
- Physicochemical Properties of Aqueous Solutions of Sodium l-Prolinate as an Absorbent for CO2 Removal
- Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
- Equilibrium Total Pressure and CO2 Solubility in Binary and Ternary Aqueous Solutions of 2-(Diethylamino)ethanol (DEEA) and 3-(Methylamino)propylamine (MAPA)
- Physical Properties of Partially CO2 Loaded Aqueous Monoethanolamine (MEA)
- Bubble Point Determination for CO2 + Ethanol + Alkanolamines (Monoethanolamine, Diethanolamine, or Triethanolamine) at High Pressures
- Vapor-Liquid Equilibrium and Excess Gibbs Energies of Hexane + N,N-Dimethyl Formamide, 2-Methylpropan-2-ol + 2-Aminophenol, N,N-Dimethyl Formamide, and 2-Propanol + Diisopropyl Amine at 94.4 kPa
- Ebulliometric Determination of Vapor
- Isothermal Vapor-Liquid Equilibria of (Monoethanolamine + Water) and (4-Methylmorpholine + Water) Binary Systems at Several Temperatures
- Density and Viscosity of Monoethanolamine + Water + Carbon Dioxide from (25 to 80) deg C
- Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of (Monoethanolamine + 2-Amino-2-methyl-1-propanol), (Monoethanolamine + Triethanolamine), and (Monoethanolamine + N-Methyldiethanolamine) at Temperatures from (293.15 to 323.15) K
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
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