Chemical Properties of Ethanol, 2-(methylamino)- (CAS 109-83-1)

Ethanol, 2-(methylamino)-

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-(N-Methylamino)ethanol
  • 2-(N-Monomethylamino)ethanol
  • 2-(methylamino)ethanol
  • 2-Hydroxy-N-methylethylamine
  • 2-Hydroxyethyl-N-methylamine
  • 2-Methylamino-1-ethanol
  • 2-Methylaminoethanol
  • 2-N-Monomethylaminoethanol
  • Amietol M 11
  • Methyl(2-hydroxyethyl)amine
  • Methyl(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-hydroxyethylamine
  • N-Methylmonoethanolamine
  • N-Monomethylaminoethanol
  • N-Monomethylethanolamine
  • N-methylaminoethanol
  • N-methylethanolamine
  • NSC 62776
  • USAF DO-50
  • ethanolamine, N-methyl-
  • «beta»-(Methylamino)ethanol
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Physical Properties

Property Value Unit Source
ω [0.6022; 0.6040]   Show Hide
ω 0.6022 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω 0.6040 ChemSep v8.3 pure component data Compiled value
μ 2.16 debye ChemSep v8.3 pure component data Compiled value
Tflash,cc 345.15 K NCMS SOLV-DB
ΔfG° -61.10 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas -198.00 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfusH° 12.71 kJ/mol Joback Calculated Property
ΔvapH° [57.00; 57.90] kJ/mol Show Hide
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
logPoct/wat -0.991 NCMS SOLV-DB
McVol 68.980 ml/mol McGowan Calculated Property
NFPA Fire 2 NCMS SOLV-DB
NFPA Health 2 NCMS SOLV-DB
NFPA Safety 0 NCMS SOLV-DB
Pc [5300.00; 5300.00] kPa Show Hide
Pc 5300.00 kPa PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc 5300.00 kPa ChemSep v8.3 pure component data Compiled value
Pc 5300.00 ± 500.00 kPa NIST
Ptriple 0.01 kPa ChemSep v8.3 pure component data Compiled value
ρc 289.92 ± 20.28 kg/m3 NIST
Tboil [428.50; 432.75] K Show Hide
Tboil 431.20 K 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
Tboil 432.39 K ChemSep v8.3 pure component data Compiled value
Tboil 432.15 K NCMS SOLV-DB
Tboil 431.20 K NIST
Tboil Outlier 428.50 ± 0.50 K NIST
Tboil 432.75 K NIST
Tc [630.00; 630.00] K Show Hide
Tc 630.00 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc 630.00 K ChemSep v8.3 pure component data Compiled value
Tc 630.00 ± 10.00 K NIST
Tfus [268.65; 268.65] K Show Hide
Tfus 268.65 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 268.65 K ChemSep v8.3 pure component data Compiled value
Tfus 268.65 K NCMS SOLV-DB
Tfus 268.65 K NIST
Ttriple 268.65 K ChemSep v8.3 pure component data Compiled value
UQi 3.52 ChemSep v8.3 pure component data Compiled value
URi 3.78 ChemSep v8.3 pure component data Compiled value
Vc [0.255; 0.259] m3/kmol Show Hide
Vc 0.255 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc 0.259 m3/kmol ChemSep v8.3 pure component data Compiled value
Zc 0.2620000 ChemSep v8.3 pure component data Compiled value
Zra 0.26 ChemSep v8.3 pure component data Compiled value

Cheméo can also estimate Ionization energy, Log10 of Water solubility in mol/l for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,liquid [194.00; 212.00] J/mol×K [303.15; 353.15] Show Hide
Cp,liquid 194.00 J/mol×K 303.15 Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid 199.00 J/mol×K 308.15 Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid 200.00 J/mol×K 313.15 Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid 202.00 J/mol×K 318.15 Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid 203.00 J/mol×K 323.15 Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid 205.00 J/mol×K 328.15 Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid 206.00 J/mol×K 333.15 Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid 207.00 J/mol×K 338.15 Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid 208.00 J/mol×K 343.15 Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid 210.00 J/mol×K 348.15 Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid 212.00 J/mol×K 353.15 Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
η [0.0024200; 0.0131200] Pa×s [293.15; 333.15] Show Hide
η 0.0131200 Pa×s 293.15 Experimental Data and Modeling for Viscosity and Refractive Index of Aqueous Mixtures with 2-(Methylamino)ethanol (MAE) and Aminoethylethanolamine (AEEA)
η 0.0102800 Pa×s 298.15 Experimental Data and Modeling for Viscosity and Refractive Index of Aqueous Mixtures with 2-(Methylamino)ethanol (MAE) and Aminoethylethanolamine (AEEA)
η 0.0130000 Pa×s 298.15 NCMS SOLV-DB
η 0.0084200 Pa×s 303.15 Experimental Data and Modeling for Viscosity and Refractive Index of Aqueous Mixtures with 2-(Methylamino)ethanol (MAE) and Aminoethylethanolamine (AEEA)
η 0.0067800 Pa×s 308.15 Experimental Data and Modeling for Viscosity and Refractive Index of Aqueous Mixtures with 2-(Methylamino)ethanol (MAE) and Aminoethylethanolamine (AEEA)
η 0.0055400 Pa×s 313.15 Experimental Data and Modeling for Viscosity and Refractive Index of Aqueous Mixtures with 2-(Methylamino)ethanol (MAE) and Aminoethylethanolamine (AEEA)
η 0.0046100 Pa×s 318.15 Experimental Data and Modeling for Viscosity and Refractive Index of Aqueous Mixtures with 2-(Methylamino)ethanol (MAE) and Aminoethylethanolamine (AEEA)
η 0.0038200 Pa×s 323.15 Experimental Data and Modeling for Viscosity and Refractive Index of Aqueous Mixtures with 2-(Methylamino)ethanol (MAE) and Aminoethylethanolamine (AEEA)
η 0.0031300 Pa×s 328.15 Experimental Data and Modeling for Viscosity and Refractive Index of Aqueous Mixtures with 2-(Methylamino)ethanol (MAE) and Aminoethylethanolamine (AEEA)
η 0.0024200 Pa×s 333.15 Experimental Data and Modeling for Viscosity and Refractive Index of Aqueous Mixtures with 2-(Methylamino)ethanol (MAE) and Aminoethylethanolamine (AEEA)
Pvap [0.01; 180.00] kPa [274.90; 451.10] Show Hide
Pvap 0.01 kPa 274.90 Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap 0.02 kPa 277.90 Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap 0.03 kPa 282.10 Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap 0.04 kPa 285.10 Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap 0.05 kPa 288.20 Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap 0.06 kPa 291.10 Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap 0.06 kPa 291.20 Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap 0.07 kPa 293.15 NCMS SOLV-DB
Pvap 0.07 kPa 293.20 Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap 0.09 kPa 296.30 Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap 0.11 kPa 299.20 Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap 0.14 kPa 302.30 Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap 0.23 kPa 308.40 Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap 0.28 kPa 311.40 Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap 0.35 kPa 314.30 Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap 0.42 kPa 317.20 Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap 0.51 kPa 320.20 Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap 1.94 kPa 341.80 Vapor Pressures of Several Commercially Used Alkanolamines
Pvap 2.94 kPa 347.90 Vapor Pressures of Several Commercially Used Alkanolamines
Pvap 4.94 kPa 357.50 Vapor Pressures of Several Commercially Used Alkanolamines
Pvap 7.44 kPa 365.70 Vapor Pressures of Several Commercially Used Alkanolamines
Pvap 9.94 kPa 371.60 Vapor Pressures of Several Commercially Used Alkanolamines
Pvap 19.90 kPa 387.40 Vapor Pressures of Several Commercially Used Alkanolamines
Pvap 29.90 kPa 397.30 Vapor Pressures of Several Commercially Used Alkanolamines
Pvap 39.90 kPa 404.80 Vapor Pressures of Several Commercially Used Alkanolamines
Pvap 49.90 kPa 411.00 Vapor Pressures of Several Commercially Used Alkanolamines
Pvap 75.00 kPa 422.70 Vapor Pressures of Several Commercially Used Alkanolamines
Pvap 100.00 kPa 431.40 Vapor Pressures of Several Commercially Used Alkanolamines
Pvap 120.00 kPa 437.30 Vapor Pressures of Several Commercially Used Alkanolamines
Pvap 140.00 kPa 442.50 Vapor Pressures of Several Commercially Used Alkanolamines
Pvap 150.00 kPa 444.80 Vapor Pressures of Several Commercially Used Alkanolamines
Pvap 170.00 kPa 449.10 Vapor Pressures of Several Commercially Used Alkanolamines
Pvap 180.00 kPa 451.10 Vapor Pressures of Several Commercially Used Alkanolamines
n0 [1.42780; 1.43930]   [293.15; 323.15] Show Hide
n0 1.43930 293.15 Volumetric Properties, Viscosities, and Refractive Indices for Aqueous 2-(Methylamino)ethanol Solutions from (298.15 to 343.15) K
n0 1.43750 298.15 Volumetric Properties, Viscosities, and Refractive Indices for Aqueous 2-(Methylamino)ethanol Solutions from (298.15 to 343.15) K
n0 1.43900 298.15 NCMS SOLV-DB
n0 1.43560 303.15 Volumetric Properties, Viscosities, and Refractive Indices for Aqueous 2-(Methylamino)ethanol Solutions from (298.15 to 343.15) K
n0 1.43390 308.15 Volumetric Properties, Viscosities, and Refractive Indices for Aqueous 2-(Methylamino)ethanol Solutions from (298.15 to 343.15) K
n0 1.43180 313.15 Volumetric Properties, Viscosities, and Refractive Indices for Aqueous 2-(Methylamino)ethanol Solutions from (298.15 to 343.15) K
n0 1.42980 318.15 Volumetric Properties, Viscosities, and Refractive Indices for Aqueous 2-(Methylamino)ethanol Solutions from (298.15 to 343.15) K
n0 1.42780 323.15 Volumetric Properties, Viscosities, and Refractive Indices for Aqueous 2-(Methylamino)ethanol Solutions from (298.15 to 343.15) K
ρl [892.10; 941.79] kg/m3 [293.15; 353.15] Show Hide
ρl 940.10 kg/m3 293.15 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
ρl 941.79 kg/m3 293.15 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
ρl 936.18 kg/m3 298.15 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
ρl 937.68 kg/m3 298.15 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
ρl 936.20 kg/m3 298.15 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
ρl 932.30 kg/m3 303.15 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
ρl 933.79 kg/m3 303.15 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
ρl 934.02 kg/m3 303.15 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
ρl 932.26 kg/m3 303.15 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
ρl 928.40 kg/m3 308.15 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
ρl 929.88 kg/m3 308.15 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
ρl 924.42 kg/m3 313.15 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
ρl 926.18 kg/m3 313.15 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
ρl 924.50 kg/m3 313.15 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
ρl 925.95 kg/m3 313.15 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
ρl 922.00 kg/m3 318.15 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
ρl 920.50 kg/m3 318.15 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
ρl 918.02 kg/m3 323.15 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
ρl 916.48 kg/m3 323.15 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
ρl 916.50 kg/m3 323.15 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
ρl 918.25 kg/m3 323.15 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
ρl 912.50 kg/m3 328.15 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
ρl 908.50 kg/m3 333.15 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
ρl 904.40 kg/m3 338.15 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
ρl 900.30 kg/m3 343.15 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
ρl 896.20 kg/m3 348.15 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
ρl 892.10 kg/m3 353.15 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

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
Cp,gas [96.01; 246.10] J/mol×K [273.00; 1200.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,gas in J/mol×K, T in K
Coefficient A5.03510e+01
Coefficient B-4.64920e+02
Coefficient C5.44524e+00
Coefficient D3.20780e-04
Coefficient E-1.15210e-07
Temperature range, min.273.00
Temperature range, max.1200.00
Cp,gas 96.01 J/mol×K 273.00 Calculated Property
Cp,gas 125.02 J/mol×K 376.00 Calculated Property
Cp,gas 150.02 J/mol×K 479.00 Calculated Property
Cp,gas 171.14 J/mol×K 582.00 Calculated Property
Cp,gas 189.04 J/mol×K 685.00 Calculated Property
Cp,gas 204.28 J/mol×K 788.00 Calculated Property
Cp,gas 217.32 J/mol×K 891.00 Calculated Property
Cp,gas 228.49 J/mol×K 994.00 Calculated Property
Cp,gas 238.02 J/mol×K 1097.00 Calculated Property
Cp,gas 246.10 J/mol×K 1200.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [169.63; 258.87] J/mol×K [250.00; 465.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + B·T + C·T² + D·T³ + E·T⁴
Y is Cp,liquid in J/mol×K, T in K
Coefficient A6.58799e+01
Coefficient B4.15001e-01
Coefficient C4.58300e-08
Coefficient D2.10900e-12
Coefficient E0.00000e+00
Temperature range, min.250.00
Temperature range, max.465.00
Cp,liquid 169.63 J/mol×K 250.00 Calculated Property
Cp,liquid 179.55 J/mol×K 273.89 Calculated Property
Cp,liquid 189.46 J/mol×K 297.78 Calculated Property
Cp,liquid 199.38 J/mol×K 321.67 Calculated Property
Cp,liquid 209.29 J/mol×K 345.56 Calculated Property
Cp,liquid 219.21 J/mol×K 369.44 Calculated Property
Cp,liquid 229.12 J/mol×K 393.33 Calculated Property
Cp,liquid 239.04 J/mol×K 417.22 Calculated Property
Cp,liquid 248.95 J/mol×K 441.11 Calculated Property
Cp,liquid 258.87 J/mol×K 465.00 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0344763; 0.0000855] Pa×s [268.65; 530.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is η in Pa×s, T in K
Coefficient A-8.81130e+00
Coefficient B2.94700e+03
Coefficient C-9.93160e-01
Coefficient D4.06030e-07
Coefficient E2.00000e+00
Temperature range, min.268.65
Temperature range, max.530.00
η 0.0344763 Pa×s 268.65 Calculated Property
η 0.0107504 Pa×s 297.69 Calculated Property
η 0.0040960 Pa×s 326.73 Calculated Property
η 0.0018172 Pa×s 355.77 Calculated Property
η 0.0009075 Pa×s 384.81 Calculated Property
η 0.0004980 Pa×s 413.84 Calculated Property
η 0.0002948 Pa×s 442.88 Calculated Property
η 0.0001858 Pa×s 471.92 Calculated Property
η 0.0001233 Pa×s 500.96 Calculated Property
η 0.0000855 Pa×s 530.00 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [58.74; 18.60] kJ/mol [268.65; 610.98] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc
Y is ΔvapH in kJ/mol, T in K
Coefficient A8.37150e+01
Coefficient B1.13040e+00
Coefficient C-1.77360e+00
Coefficient D1.73330e+00
Coefficient E-6.69610e-01
Critical temperature, Tc (K)6.30000e+02
Temperature range, min.268.65
Temperature range, max.610.98
ΔvapH 58.74 kJ/mol 268.65 Calculated Property
ΔvapH 56.08 kJ/mol 306.69 Calculated Property
ΔvapH 53.33 kJ/mol 344.72 Calculated Property
ΔvapH 50.40 kJ/mol 382.76 Calculated Property
ΔvapH 47.21 kJ/mol 420.80 Calculated Property
ΔvapH 43.67 kJ/mol 458.83 Calculated Property
ΔvapH 39.62 kJ/mol 496.87 Calculated Property
ΔvapH 34.80 kJ/mol 534.91 Calculated Property
ΔvapH 28.59 kJ/mol 572.94 Calculated Property
ΔvapH 18.60 kJ/mol 610.98 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.63] kPa [329.98; 455.24] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.56909e+01
Coefficient B-3.98645e+03
Coefficient C-7.11700e+01
Temperature range, min.329.98
Temperature range, max.455.24
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
Pvap [0.01; 5111.25] kPa [268.65; 630.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is Pvap in kPa, T in K
Coefficient A9.42190e+01
Coefficient B-9.89646e+03
Coefficient C-1.11223e+01
Coefficient D4.33388e-06
Coefficient E2.00000e+00
Temperature range, min.268.65
Temperature range, max.630.00
Pvap 0.01 kPa 268.65 Calculated Property
Pvap 0.31 kPa 308.80 Calculated Property
Pvap 3.55 kPa 348.95 Calculated Property
Pvap 22.41 kPa 389.10 Calculated Property
Pvap 93.55 kPa 429.25 Calculated Property
Pvap 290.72 kPa 469.40 Calculated Property
Pvap 728.59 kPa 509.55 Calculated Property
Pvap 1556.86 kPa 549.70 Calculated Property
Pvap 2951.59 kPa 589.85 Calculated Property
Pvap 5111.25 kPa 630.00 Calculated Property
Property Value Unit Temperature (K) Source
ρl [958.09; 529.89] kg/m3 [268.65; 610.98] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A / B^(1 + (1 − T/C)^D)
Y is ρl in kg/m3, T in K
Coefficient A7.38229e+01
Coefficient B2.55663e-01
Coefficient C6.30000e+02
Coefficient D2.31239e-01
Temperature range, min.268.65
Temperature range, max.610.98
ρl 958.09 kg/m3 268.65 Calculated Property
ρl 929.35 kg/m3 306.69 Calculated Property
ρl 898.87 kg/m3 344.72 Calculated Property
ρl 866.26 kg/m3 382.76 Calculated Property
ρl 830.94 kg/m3 420.80 Calculated Property
ρl 792.05 kg/m3 458.83 Calculated Property
ρl 748.19 kg/m3 496.87 Calculated Property
ρl 696.72 kg/m3 534.91 Calculated Property
ρl 631.60 kg/m3 572.94 Calculated Property
ρl 529.89 kg/m3 610.98 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.04; 9.74e-04] N/m [268.65; 610.98] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is γ in N/m, T in K
Coefficient A-1.13590e-02
Coefficient B1.94040e+02
Coefficient C-4.21680e+00
Coefficient D3.94470e-03
Coefficient E-7.78570e-06
Temperature range, min.268.65
Temperature range, max.610.98
γ 0.04 N/m 268.65 Calculated Property
γ 0.03 N/m 306.69 Calculated Property
γ 0.03 N/m 344.72 Calculated Property
γ 0.02 N/m 382.76 Calculated Property
γ 0.02 N/m 420.80 Calculated Property
γ 0.02 N/m 458.83 Calculated Property
γ 0.01 N/m 496.87 Calculated Property
γ 0.01 N/m 534.91 Calculated Property
γ 0.00 N/m 572.94 Calculated Property
γ 9.74e-04 N/m 610.98 Calculated Property
Property Value Unit Temperature (K) Source
λgas [0.01; 0.09] W/m×K [268.65; 1000.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·T^B / (1 + C/T + D/T²)
Y is λgas in W/m×K, T in K
Coefficient A2.14630e-04
Coefficient B9.48570e-01
Coefficient C6.22070e+02
Coefficient D1.53720e+04
Temperature range, min.268.65
Temperature range, max.1000.00
λgas 0.01 W/m×K 268.65 Calculated Property
λgas 0.02 W/m×K 349.91 Calculated Property
λgas 0.03 W/m×K 431.17 Calculated Property
λgas 0.04 W/m×K 512.43 Calculated Property
λgas 0.04 W/m×K 593.69 Calculated Property
λgas 0.05 W/m×K 674.96 Calculated Property
λgas 0.06 W/m×K 756.22 Calculated Property
λgas 0.07 W/m×K 837.48 Calculated Property
λgas 0.08 W/m×K 918.74 Calculated Property
λgas 0.09 W/m×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
λliquid [0.19; 0.14] W/m×K [268.65; 431.15] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is λliquid in W/m×K, T in K
Coefficient A-1.13780e-02
Coefficient B-9.68490e+01
Coefficient C-4.76050e-01
Coefficient D-2.94280e-03
Coefficient E4.71290e-07
Temperature range, min.268.65
Temperature range, max.431.15
λliquid 0.19 W/m×K 268.65 Calculated Property
λliquid 0.19 W/m×K 286.71 Calculated Property
λliquid 0.18 W/m×K 304.76 Calculated Property
λliquid 0.18 W/m×K 322.82 Calculated Property
λliquid 0.17 W/m×K 340.87 Calculated Property
λliquid 0.16 W/m×K 358.93 Calculated Property
λliquid 0.16 W/m×K 376.98 Calculated Property
λliquid 0.15 W/m×K 395.04 Calculated Property
λliquid 0.15 W/m×K 413.09 Calculated Property
λliquid 0.14 W/m×K 431.15 Calculated Property

Similar Compounds

ETHANOL, 2,2'-IMINOBIS-. Ethanol, 2-(ethylamino)-. 2-((2-[(2-Hydroxyethyl)amino]ethyl)amino)ethanol. Ethanol, 2-[(2-aminoethyl)amino]-. Ethanol, 2-[(1-methylethyl)amino]-. N,N-Dimethylaminoethanol. Acetamide, N-(2-hydroxyethyl)-. 2-(Propylamino)ethanol. 2-(tert-Butylamino)ethanol. Ethanamine, N-methyl-. 2-(isobutylamino)ethanol. Urea, (2-hydroxyethyl)-. Methyldiethanolamine. Monoethanolamine. Morpholine.

Find more compounds similar to Ethanol, 2-(methylamino)-.

Mixtures

Sources

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