- InChI
- InChI=1S/C4H11NO2/c6-3-1-5-2-4-7/h5-7H,1-4H2
- InChI Key
- ZBCBWPMODOFKDW-UHFFFAOYSA-N
- Formula
- C4H11NO2
- SMILES
- OCCNCCO
- Molecular Weight1
- 105.14
- CAS
- 111-42-2
- Other Names
-
- 2,2'-Dihydroxydiethylamine
- 2,2'-IMINOBIS-ETHANOL
- 2,2'-Iminobis[ethanol]
- 2,2'-Iminodi-1-ethanol
- 2,2'-Iminodiethanol
- 2,2'-azanediylbis(ethan-1-ol)
- 2-[(2-Hydroxyethyl)amino]ethanol
- Bis(2-hydroxyethyl)amine
- Bis(hydroxyethyl)amine
- DEA
- DIETHYLOLAMINE
- Dabco DEOA-LF
- Di(2-hydroxyethyl)amine
- Diaethanolamin
- Diethanol, 2,2'-imino-
- Diethanolamin
- Diethylamine, 2,2'-dihydroxy-
- Diolamine
- Ethanol, 2,2'-iminobis-
- Ethanol, 2,2'-iminodi-
- Iminodiethanol
- N,N'-Iminodiethanol
- N,N-Bis(2-hydroxyethyl)amine
- N,N-Diethanolamine
- NCI-C55174
- NSC 4959
- Niax DEOA-LF
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,solid : Solid 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°solid : Solid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔsubH° : Enthalpy of sublimation 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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- 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 |
|---|---|---|---|
| PAff | 953.00 | kJ/mol | NIST |
| BasG | 920.00 | kJ/mol | NIST |
| ΔcH°solid | -2652.30 ± 2.50 | kJ/mol | NIST |
| η | 0.5665700 | Pa×s | Densiti... |
| ΔfG° | -201.45 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -397.10 ± 2.90 | kJ/mol | NIST |
| ΔfH°solid | -493.80 ± 2.60 | kJ/mol | NIST |
| ΔfusH° | 19.39 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [96.70; 105.90] | kJ/mol |
|
| ΔsubH° | 96.70 ± 1.20 | kJ/mol | NIST |
| ΔsubH° | 105.90 ± 2.00 | kJ/mol | NIST |
| ΔvapH° | 64.29 | kJ/mol | Joback Calculated Property |
| log10WS | 0.79 | Crippen Calculated Property | |
| logPoct/wat | -1.439 | Crippen Calculated Property | |
| McVol | 88.940 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | 5065.79 | kPa | Joback Calculated Property |
| I | [2141.00; 2200.00] |
|
|
| I | 2200.00 | NIST | |
| I | 2141.00 | NIST | |
| I | 2180.00 | NIST | |
| I | 2200.00 | NIST | |
| Tboil | [541.55; 544.20] | K |
|
| Tboil | 542.46 | K | Experim... |
| Tboil | 544.20 | K | NIST |
| Tboil | 541.55 | K | NIST |
| Tc | 687.52 | K | Joback Calculated Property |
| Tfus | [300.15; 301.20] | K |
|
| Tfus | 300.15 | K | Thermod... |
| Tfus | 301.15 | K | NIST |
| Tfus | 301.10 ± 0.07 | K | NIST |
| Tfus | 301.20 ± 0.60 | K | NIST |
| Vc | 0.333 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [212.00; 249.93] | J/mol×K | [525.45; 687.52] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 210 220 230 240 250 550 600 650 | ||||
| Cp,gas | 212.00 | J/mol×K | 525.45 | Joback Calculated Property |
| Cp,gas | 219.00 | J/mol×K | 552.46 | Joback Calculated Property |
| Cp,gas | 225.71 | J/mol×K | 579.47 | Joback Calculated Property |
| Cp,gas | 232.16 | J/mol×K | 606.48 | Joback Calculated Property |
| Cp,gas | 238.34 | J/mol×K | 633.49 | Joback Calculated Property |
| Cp,gas | 244.26 | J/mol×K | 660.50 | Joback Calculated Property |
| Cp,gas | 249.93 | J/mol×K | 687.52 | Joback Calculated Property |
| Cp,solid | 137.00 | J/mol×K | 298.15 | NIST |
| η | [0.0025220; 0.3805000] | Pa×s | [303.15; 423.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 0.05 0.1 0.15 0.2 0.25 0.3 0.35 0.4 350 400 | ||||
| η | 0.3805000 | Pa×s | 303.15 | Viscome... |
| η | 0.1835000 | Pa×s | 313.15 | Viscome... |
| η | 0.1006000 | Pa×s | 323.15 | Viscome... |
| η | 0.0613600 | Pa×s | 333.15 | Viscome... |
| η | 0.0337900 | Pa×s | 343.15 | Viscome... |
| η | 0.0231350 | Pa×s | 353.15 | Viscome... |
| η | 0.0148080 | Pa×s | 363.15 | Viscome... |
| η | 0.0104110 | Pa×s | 373.15 | Viscome... |
| η | 0.0080110 | Pa×s | 383.15 | Viscome... |
| η | 0.0059850 | Pa×s | 393.15 | Viscome... |
| η | 0.0045840 | Pa×s | 403.15 | Viscome... |
| η | 0.0036090 | Pa×s | 413.15 | Viscome... |
| η | 0.0025220 | Pa×s | 423.15 | Viscome... |
| ΔvapH | [69.00; 77.00] | kJ/mol | [415.00; 522.50] |
|
| ΔvapH | 77.00 | kJ/mol | 415.00 | NIST |
| ΔvapH | 74.40 | kJ/mol | 482.50 | NIST |
| ΔvapH | 70.60 | kJ/mol | 490.00 | NIST |
| ΔvapH | 69.00 | kJ/mol | 522.50 | NIST |
| Pvap | [1.44; 4.94] | kPa | [427.50; 452.40] |
|
|
T(K) Vapor pressure (kPa) 1.5 2 2.5 3 3.5 4 4.5 5 430 440 450 | ||||
| Pvap | 1.44 | kPa | 427.50 | Vapor P... |
| Pvap | 1.94 | kPa | 433.00 | Vapor P... |
| Pvap | 2.94 | kPa | 441.40 | Vapor P... |
| Pvap | 3.94 | kPa | 447.40 | Vapor P... |
| Pvap | 4.94 | kPa | 452.40 | Vapor P... |
| ρl | [1050.24; 1107.05] | kg/m3 | [278.14; 363.15] |
|
|
T(K) Liquid Density (kg/m3) 1050 1060 1070 1080 1090 1100 1110 300 350 | ||||
| ρl | 1107.05 | kg/m3 | 278.14 | Densiti... |
| ρl | 1103.88 | kg/m3 | 283.14 | Densiti... |
| ρl | 1097.51 | kg/m3 | 293.15 | Densiti... |
| ρl | 1096.10 | kg/m3 | 293.15 | Density... |
| ρl | 1097.40 | kg/m3 | 293.15 | Volumet... |
| ρl | 1097.61 | kg/m3 | 293.15 | Volumet... |
| ρl | 1094.02 | kg/m3 | 298.15 | Densiti... |
| ρl | 1091.06 | kg/m3 | 303.14 | Densiti... |
| ρl | 1089.80 | kg/m3 | 303.15 | Density... |
| ρl | 1090.79 | kg/m3 | 303.15 | Densiti... |
| ρl | 1090.50 | kg/m3 | 303.15 | Volumet... |
| ρl | 1091.17 | kg/m3 | 303.15 | Volumet... |
| ρl | 1087.51 | kg/m3 | 308.15 | Densiti... |
| ρl | 1084.49 | kg/m3 | 313.14 | Densiti... |
| ρl | 1084.60 | kg/m3 | 313.15 | Volumet... |
| ρl | 1083.90 | kg/m3 | 313.15 | Volumet... |
| ρl | 1084.20 | kg/m3 | 313.15 | Densiti... |
| ρl | 1083.70 | kg/m3 | 313.15 | Density... |
| ρl | 1084.70 | kg/m3 | 313.15 | Density... |
| ρl | 1080.86 | kg/m3 | 318.15 | Densiti... |
| ρl | 1077.78 | kg/m3 | 323.14 | Densiti... |
| ρl | 1077.88 | kg/m3 | 323.15 | Volumet... |
| ρl | 1077.40 | kg/m3 | 323.15 | Density... |
| ρl | 1077.10 | kg/m3 | 323.15 | Volumet... |
| ρl | 1077.40 | kg/m3 | 323.15 | Density... |
| ρl | 1077.49 | kg/m3 | 323.15 | Densiti... |
| ρl | 1071.00 | kg/m3 | 333.14 | Densiti... |
| ρl | 1071.11 | kg/m3 | 333.14 | Volumet... |
| ρl | 1070.30 | kg/m3 | 333.15 | Density... |
| ρl | 1070.30 | kg/m3 | 333.15 | Volumet... |
| ρl | 1070.70 | kg/m3 | 333.15 | Density... |
| ρl | 1064.14 | kg/m3 | 343.14 | Densiti... |
| ρl | 1064.25 | kg/m3 | 343.14 | Volumet... |
| ρl | 1063.50 | kg/m3 | 343.15 | Volumet... |
| ρl | 1060.68 | kg/m3 | 348.14 | Densiti... |
| ρl | 1057.31 | kg/m3 | 353.14 | Volumet... |
| ρl | 1056.83 | kg/m3 | 353.15 | Densiti... |
| ρl | 1050.24 | kg/m3 | 363.15 | Volumet... |
| csound,fluid | [1660.36; 1739.20] | m/s | [293.15; 323.15] |
|
|
T(K) Speed of sound in fluid (m/s) 1660 1680 1700 1720 1740 300 310 320 | ||||
| csound,fluid | 1739.20 | m/s | 293.15 | Density... |
| csound,fluid | 1736.54 | m/s | 293.15 | Density... |
| csound,fluid | 1723.96 | m/s | 298.15 | Density... |
| csound,fluid | 1711.30 | m/s | 303.15 | Density... |
| csound,fluid | 1711.55 | m/s | 303.15 | Density... |
| csound,fluid | 1698.70 | m/s | 308.15 | Density... |
| csound,fluid | 1685.90 | m/s | 313.15 | Density... |
| csound,fluid | 1686.13 | m/s | 313.15 | Density... |
| csound,fluid | 1673.76 | m/s | 318.15 | Density... |
| csound,fluid | 1661.10 | m/s | 323.15 | Density... |
| csound,fluid | 1660.36 | m/s | 323.15 | Density... |
| γ | [0.04; 0.05] | N/m | [293.15; 323.20] |
|
|
T(K) Surface Tension (N/m) 0.04 0.04 0.05 0.05 0.05 300 310 320 | ||||
| γ | 0.05 | N/m | 293.15 | Density... |
| γ | 0.05 | N/m | 298.15 | Density... |
| γ | 0.05 | N/m | 303.15 | Density... |
| γ | 0.05 | N/m | 303.20 | Investi... |
| γ | 0.05 | N/m | 313.15 | Density... |
| γ | 0.04 | N/m | 313.20 | Investi... |
| γ | 0.05 | N/m | 323.15 | Density... |
| γ | 0.04 | N/m | 323.20 | Investi... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [427.70; 490.20] | K | [1.30; 20.00] |
|
| Tboilr | 427.70 | K | 1.30 | NIST |
| Tboilr | 490.20 | K | 20.00 | NIST |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 298.15 | 1093.6 |
| 100.00 | 303.15 | 1090.4 |
| 100.00 | 308.15 | 1087.1 |
| 100.00 | 313.15 | 1083.8 |
| 100.00 | 318.15 | 1080.6 |
| 100.00 | 323.15 | 1077.4 |
| 100.00 | 328.15 | 1074.1 |
| 100.00 | 333.15 | 1070.8 |
| 100.00 | 338.15 | 1067.4 |
| 100.00 | 343.15 | 1064.0 |
| 100.00 | 348.15 | 1060.6 |
| 100.00 | 353.15 | 1057.2 |
| 100.00 | 358.15 | 1053.7 |
| 100.00 | 363.15 | 1050.1 |
| 700.00 | 373.15 | 1043.3 |
| 700.00 | 383.15 | 1035.5 |
| 700.00 | 393.15 | 1028.1 |
| 700.00 | 403.15 | 1020.5 |
| 700.00 | 413.15 | 1012.9 |
| 700.00 | 423.15 | 1004.8 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [425.18; 567.97] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.72949e+01 | |||
| Coefficient B | -5.79247e+03 | |||
| Coefficient C | -8.45980e+01 | |||
| Temperature range, min. | 425.18 | |||
| Temperature range, max. | 567.97 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 | ||||
| Pvap | 1.33 | kPa | 425.18 | Calculated Property |
| Pvap | 2.84 | kPa | 441.05 | Calculated Property |
| Pvap | 5.68 | kPa | 456.91 | Calculated Property |
| Pvap | 10.73 | kPa | 472.78 | Calculated Property |
| Pvap | 19.27 | kPa | 488.64 | Calculated Property |
| Pvap | 33.13 | kPa | 504.51 | Calculated Property |
| Pvap | 54.74 | kPa | 520.37 | Calculated Property |
| Pvap | 87.32 | kPa | 536.24 | Calculated Property |
| Pvap | 134.93 | kPa | 552.10 | Calculated Property |
| Pvap | 202.65 | kPa | 567.97 | Calculated Property |
| Pvap | [7.74e-05; 102.80] | kPa | [301.15; 542.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 2.16769e+02 | |||
| Coefficient B | -1.89915e+04 | |||
| Coefficient C | -2.88239e+01 | |||
| Coefficient D | 1.48221e-05 | |||
| Temperature range, min. | 301.15 | |||
| Temperature range, max. | 542.15 | |||
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 300 400 500 | ||||
| Pvap | 7.74e-05 | kPa | 301.15 | Calculated Property |
| Pvap | 1.47e-03 | kPa | 327.93 | Calculated Property |
| Pvap | 0.02 | kPa | 354.71 | Calculated Property |
| Pvap | 0.11 | kPa | 381.48 | Calculated Property |
| Pvap | 0.57 | kPa | 408.26 | Calculated Property |
| Pvap | 2.23 | kPa | 435.04 | Calculated Property |
| Pvap | 7.15 | kPa | 461.82 | Calculated Property |
| Pvap | 19.55 | kPa | 488.59 | Calculated Property |
| Pvap | 47.13 | kPa | 515.37 | Calculated Property |
| Pvap | 102.80 | kPa | 542.15 | 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 Diethanolamine.
Mixtures
- Diethanolamine + 2-Pyrrolidinone, 1-methyl-
- Diethanolamine + Thiophene, tetrahydro-, 1,1-dioxide
- Diethanolamine + Water
- Diethanolamine + Dimethyl Sulfoxide
- Diethanolamine + Methyl Alcohol + Water
- p-Cresol + Diethanolamine
- Phenol, 3-methyl- + Diethanolamine
- Diethanolamine + Methyl Alcohol
- Diethanolamine + Ethanol
- Diethanolamine + Ethanol + Water
- Choline chloride + Diethanolamine
- Diethanolamine + Tetra-N-butylammonium bromide
- Carbon dioxide + Diethanolamine + Tetra-N-butylammonium bromide
- Choline chloride + Carbon dioxide + Diethanolamine
- 2-Propanol, 1-amino- + Diethanolamine + Water
- Diethanolamine + 1-Propanol, 3-amino- + Water
- Diethanolamine + Methyldiethanolamine + Water
- Diethanolamine + Ethanol, 2-(methylamino)- + Water
- Ethanol, 2-(ethylamino)- + Diethanolamine + Water
- Diethanolamine + 2-(2-Hydroxyethyl)piperidine + Water
Find more mixtures with Diethanolamine.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
- CO2 solubility measurement and thermodynamic modeling for 1-methylpiperazine/water/CO2
- Effective extraction of benzene and thiophene by novel deep eutectic solvents from hexane / aromatic mixture at different temperatures
- Solubility data for toluene in various aqueous alkanolamine solutions
- Molar excess enthalpy (HEm) for various {alkanolamine (1) + water (2)} systems at T = (298.15, 313.15, and 323.15) K
- Heat capacities of aqueous solutions containing diethanolamine and N-methyldiethanolamine
- (Vapour + liquid) equilibria (VLE) of CO2 in aqueous solutions of 2-amino-2-methyl-1-propanol: New data and modelling using eNRTL-equation
- Volumetric properties of binary mixtures of dimethyl sulfoxide with amines from (293.15 to 363.15) K
- Density, speed of sound, viscosity, refractive index and surface tension of N-methyl-2-pyrrolidone + diethanolamine (or triethanolamine) from T = (293.15 to 323.15) K
- Volumetric and viscometric behaviour of the binary systems of N-methyldiethanolamine and diethanolamine with 1-butyl-3-methylimidazolium acetate at various temperatures
- 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
- Excess molar enthalpies for binary mixtures of different amines with water
- Molar excess enthalpy (Hm E) for systems of aqueous piperazine derivatives
- Density and viscosity measurements of aqueous amines at high pressures: DEA-water, DMAE-water and TEA-water mixtures
- Investigation of surface tension and viscosity for aqueous solutions of MEA-MeOH and DEA-MeOH
- Experimental and predicted vapor-liquid equilibrium for binary systems with diethanolamine, m-cresol and p-cresol at 20.0 kPa
- Densities and Excess Molar Volumes for Binary Mixtures of Diethanolamine with Water, Methanol, Ethanol and Ternary Solutions of Diethanolamine + Water with Methanol, Ethanol at Atmospheric Pressure from 278.15 to 353.15 K
- Estimation of CO2 Absorption Capacity via Correlating Measured Electrical Conductivity in a Diethanolamine Solvent System Compared to Monoethanolamine Solvent Systems
- Thermodynamic and Kinetic Studies of CO2 Capture by Glycol and Amine-Based Deep Eutectic Solvents
- Experimental Mutual Solubility Data for Cyclohexane and Water in Aqueous Solutions of Diethanolamine
- Liquid-Liquid Equilibria for Benzene/Thiophene + Cyclohexane/Hexadecane + Deep Eutectic Solvents: Data and Correlation
- Surface Tension of aqueous vinary mixtures of 1-amino-2-propanol and 3-amino-1-propanol, and aqueous ternary mixtures of these amines with diethanolamine, triethanolamine, and 2-amino-2-methyl-1-propanol from (298.15 to 323.15) K
- 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
- Physical Solubility and Diffusivity of N2O and CO2 into Aqueous Solutions of (2-Amino-2-methyl-1-propanol + Diethanolamine) and (N-Methyldiethanolamine + Diethanolamine)
- Densities of Water + Diethanolamine + Methanol and Water + N-Methyldiethanolamine + Methanol at Temperatures Ranging from (283.15 to 353.15) K
- Density and Viscosity of Aqueous Blends of Three Alkanolamines: N-Methyldiethanolamine, Diethanolamine, and 2-Amino-2-methyl-1-propanol in the Range of (303 to 343) K
- 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
- 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
- Vapor Pressures of Several Commercially Used Alkanolamines
- Absorption Data for Carbon Dioxide in Aqueous Blends of Methyl-Diethanolamine (MDEA) and Diethanol Amine (DEA): 25% MDEA + 25% DEA and 30 % MDEA + 20% DEA
- Density of Water (1) + Diethanolamine (2) + CO2 (3) and Water (1) + N-Methyldiethanolamine (2) + CO2 (3) from (298.15 to 423.15) K
- Densities of Partially Carbonated Aqueous Diethanolamine and Methyldiethanolamine Solutions
- Densities, Viscosities, and Refractive Indices of Aqueous Alkanolamine Solutions as Potential Carbon Dioxide Removal Reagents
- 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
- Density and Viscosity for Binary Mixtures of Diethylene Glycol Monobutyl Ether with Monoethanolamine, Diethanolamine, and Triethanolamine from (293.15 to 333.15) K
- New Vapor Liquid Liquid Equilibrium Data for Ethane and Propane in Alkanolamine Aqueous Solutions
- New Vapor Liquid Liquid Equilibrium Solubility Data for iso-Butane, n-Butane, n-Pentane, and n-Hexane in Alkanolamine Aqueous Solutions
- Bubble Point Determination for CO2 + Ethanol + Alkanolamines (Monoethanolamine, Diethanolamine, or Triethanolamine) at High Pressures
- Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of Binary Mixtures of 1-Amino-2-propanol or 3-Amino-1-propanol with 2-Amino-2-methyl-1-propanol, Diethanolamine, or Triethanolamine from (293.15 to 323.15) K
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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