Chemical Properties of Ethanol, 2-[(2-aminoethyl)amino]- (CAS 111-41-1)

InChI

InChI=1S/C4H12N2O/c5-1-2-6-3-4-7/h6-7H,1-5H2

InChI Key

LHIJANUOQQMGNT-UHFFFAOYSA-N

Formula

C4H12N2O

SMILES

NCCNCCO

Molecular Weight¹

104.15

CAS

111-41-1

Other Names

• (2-Aminoethyl)ethanolamine
• (2-Hydroxyethyl)ethylenediamine
• («beta»-Hydroxyethyl)ethylenediamine
• 1-Aminoethyl ethanolamine
• 1-[2-(Hydroxyethyl)amino]-2-aminoethane
• 2-(2-Hydroxyethylamino)ethylamine
• 2-(2-aminoethylamino)ethanol
• 2-Amino-2'-hydroxydiethylamine
• 2-[(2-Aminoethyl)amino]ethanol
• Aminoethylethanolamine
• Ethanolethylene diamine
• Monoethanolethylenediamine
• N-(2'-Hydroxyethyl)ethylenediamine
• N-(2-Hydroxyethyl)-1,2-ethanediamine
• N-(2-Hydroxyethyl)ethylenediamine
• N-(2-aminoethyl)ethanolamine
• N-(Aminoethyl)ethanolamine
• N-(Hydroxyethyl)ethylenediamine
• N-(«beta»-Aminoethyl)ethanolamine
• N-(«beta»-Hydroxyethyl)ethylenediamine
• N-Hydroxyethyl-1,2-ethanediamine
• N-aminoethyl ethanolamine
• NSC 461
• ethanolamine, N-(2-aminoethyl)-
• ethylenediamine, N-.beta.-hydroxyethyl-
• «beta»-Aminoethyl-«beta»-hydroxyethylamine

• ω : Acentric Factor.
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced pressure (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.4634; 1.0473]
ω	0.4634		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	1.0473		ChemSep v8.3 pure component data Compiled value
ΔfG°	3.81	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-191.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfusH°	20.50	kJ/mol	Joback Calculated Property
ΔvapH°	72.94	kJ/mol	Relay (1.0) Calculated Property
IE	9.10	eV	Relay (1.0) Calculated Property
logPoct/wat	-1.473		Crippen Calculated Property
McVol	93.050	ml/mol	McGowan Calculated Property
Pc	[4460.00; 4650.00]	kPa
Pc	4650.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 11 Compiled value
Pc	4650.00	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4460.00	kPa	ChemSep v8.3 pure component data Compiled value
Inp	1072.00		NIST
Ip	[1920.00; 1965.00]
Ip	1965.00		NIST
Ip	1920.00		NIST
Ip	1955.00		NIST
Tboil	[512.00; 517.00]	K
Tboil	517.00	K	ChemSep v8.3 pure component data Compiled value
Tboil	512.00 ± 1.00	K	NIST
Tboil	516.95	K	NIST
Tc	[698.00; 739.20]	K
Tc	739.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 11 Compiled value
Tc	739.20	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	698.00	K	ChemSep v8.3 pure component data Compiled value
Tfus	240.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
UQi	4.45		ChemSep v8.3 pure component data Compiled value
URi	4.92		ChemSep v8.3 pure component data Compiled value
Vc	[0.335; 0.387]	m3/kmol
Vc	0.335	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.387	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2520000		ChemSep v8.3 pure component data Compiled value
Zra	0.25		ChemSep v8.3 pure component data Compiled value

Cheméo can also estimate Log10 of Water solubility in mol/l for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[279.00; 296.00]	J/mol×K	[303.15; 353.15]
Cp,liquid	279.00	J/mol×K	303.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	284.00	J/mol×K	308.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	285.00	J/mol×K	313.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	286.00	J/mol×K	318.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	287.00	J/mol×K	323.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	289.00	J/mol×K	328.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	290.00	J/mol×K	333.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	292.00	J/mol×K	338.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	293.00	J/mol×K	343.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	295.00	J/mol×K	348.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	296.00	J/mol×K	353.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
η	[0.0127400; 0.1536200]	Pa×s	[293.15; 333.15]
η	0.1536200	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	0.0992700	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	0.0713100	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	0.0529400	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	0.0376700	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	0.0282300	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	0.0215500	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	0.0164300	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	0.0127400	Pa×s	333.15	Experimental Data and Modeling for Viscosity and Refractive Index of Aqueous Mixtures with 2-(Methylamino)ethanol (MAE) and Aminoethylethanolamine (AEEA)
ΔvapH	62.80	kJ/mol	450.00	NIST
Pvap	[6.47e-03; 0.24]	kPa	[323.20; 374.20]
Pvap	6.47e-03	kPa	323.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	6.52e-03	kPa	323.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	6.81e-03	kPa	324.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	7.11e-03	kPa	324.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	8.20e-03	kPa	326.10	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	8.09e-03	kPa	326.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.01	kPa	329.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.01	kPa	329.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.01	kPa	332.10	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.01	kPa	332.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.02	kPa	335.10	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.02	kPa	335.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.02	kPa	335.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.02	kPa	336.90	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.02	kPa	338.10	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.02	kPa	338.10	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.03	kPa	341.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.03	kPa	341.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.03	kPa	344.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.03	kPa	344.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.04	kPa	345.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.04	kPa	347.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.05	kPa	350.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.06	kPa	353.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.08	kPa	356.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.10	kPa	359.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.09	kPa	359.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.11	kPa	362.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.14	kPa	365.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.17	kPa	368.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.20	kPa	371.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.23	kPa	373.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
Pvap	0.24	kPa	374.20	Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
n0	[1.47128; 1.48454]		[298.15; 333.15]
n0	1.48454		298.15	Volumetric Properties, Viscosities, and Refractive Indices for Aqueous 2-((2-Aminoethyl)amino)ethanol Solutions from (298.15 to 343.15) K
n0	1.48269		303.15	Volumetric Properties, Viscosities, and Refractive Indices for Aqueous 2-((2-Aminoethyl)amino)ethanol Solutions from (298.15 to 343.15) K
n0	1.47884		313.15	Volumetric Properties, Viscosities, and Refractive Indices for Aqueous 2-((2-Aminoethyl)amino)ethanol Solutions from (298.15 to 343.15) K
n0	1.47516		323.15	Volumetric Properties, Viscosities, and Refractive Indices for Aqueous 2-((2-Aminoethyl)amino)ethanol Solutions from (298.15 to 343.15) K
n0	1.47128		333.15	Volumetric Properties, Viscosities, and Refractive Indices for Aqueous 2-((2-Aminoethyl)amino)ethanol Solutions from (298.15 to 343.15) K
ρl	[1006.54; 1029.14]	kg/m3	[293.15; 323.15]
ρl	1029.14	kg/m3	293.15	Volumetric and Viscometric Properties of Alcohol Amines + Ethanol Binary Mixtures
ρl	1025.80	kg/m3	298.15	Thermodynamic properties and CO2 solubility of monoethanolamine + diethylenetriamine/aminoethylethanolamine mixtures: Experimental measurements and thermodynamic modeling
ρl	1021.30	kg/m3	303.15	Thermodynamic properties and CO2 solubility of monoethanolamine + diethylenetriamine/aminoethylethanolamine mixtures: Experimental measurements and thermodynamic modeling
ρl	1021.45	kg/m3	303.15	Volumetric and Viscometric Properties of Alcohol Amines + Ethanol Binary Mixtures
ρl	1016.30	kg/m3	308.15	Thermodynamic properties and CO2 solubility of monoethanolamine + diethylenetriamine/aminoethylethanolamine mixtures: Experimental measurements and thermodynamic modeling
ρl	1014.18	kg/m3	313.15	Volumetric and Viscometric Properties of Alcohol Amines + Ethanol Binary Mixtures
ρl	1006.54	kg/m3	323.15	Volumetric and Viscometric Properties of Alcohol Amines + Ethanol Binary Mixtures

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	[376.80; 512.20]	K	[1.30; 100.00]
Tboilr	376.80	K	1.30	NIST
Tboilr	512.20	K	100.00	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[135.09; 361.40]	J/mol×K	[273.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			7.55330e+01
Coefficient B			-4.95370e+02
Coefficient C			5.86224e+00
Coefficient D			1.57140e-04
Coefficient E			-4.98520e-08
Temperature range, min.			273.00
Temperature range, max.			1500.00
Cp,gas	135.09	J/mol×K	273.00	Calculated Property
Cp,gas	186.37	J/mol×K	409.33	Calculated Property
Cp,gas	227.75	J/mol×K	545.67	Calculated Property
Cp,gas	260.44	J/mol×K	682.00	Calculated Property
Cp,gas	286.59	J/mol×K	818.33	Calculated Property
Cp,gas	307.81	J/mol×K	954.67	Calculated Property
Cp,gas	325.24	J/mol×K	1091.00	Calculated Property
Cp,gas	339.65	J/mol×K	1227.33	Calculated Property
Cp,gas	351.58	J/mol×K	1363.67	Calculated Property
Cp,gas	361.40	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[259.68; 354.04]	J/mol×K	[349.00; 519.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			6.56040e+01
Coefficient B			-1.21740e+02
Coefficient C			4.89424e+00
Coefficient D			2.34850e-03
Coefficient E			-7.94780e-07
Temperature range, min.			349.00
Temperature range, max.			519.00
Cp,liquid	259.68	J/mol×K	349.00	Calculated Property
Cp,liquid	269.94	J/mol×K	367.89	Calculated Property
Cp,liquid	280.24	J/mol×K	386.78	Calculated Property
Cp,liquid	290.60	J/mol×K	405.67	Calculated Property
Cp,liquid	301.01	J/mol×K	424.56	Calculated Property
Cp,liquid	311.49	J/mol×K	443.44	Calculated Property
Cp,liquid	322.03	J/mol×K	462.33	Calculated Property
Cp,liquid	332.63	J/mol×K	481.22	Calculated Property
Cp,liquid	343.31	J/mol×K	500.11	Calculated Property
Cp,liquid	354.04	J/mol×K	519.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.5236152; 0.0000236]	Pa×s	[273.15; 598.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-2.76629e+01
Coefficient B			5.32650e+03
Coefficient C			1.36238e+00
Coefficient D			-1.70645e-06
Coefficient E			2.00000e+00
Temperature range, min.			273.15
Temperature range, max.			598.00
η	0.5236152	Pa×s	273.15	Calculated Property
η	0.0614323	Pa×s	309.24	Calculated Property
η	0.0113334	Pa×s	345.34	Calculated Property
η	0.0028831	Pa×s	381.43	Calculated Property
η	0.0009283	Pa×s	417.53	Calculated Property
η	0.0003570	Pa×s	453.62	Calculated Property
η	0.0001573	Pa×s	489.72	Calculated Property
η	0.0000772	Pa×s	525.81	Calculated Property
η	0.0000412	Pa×s	561.91	Calculated Property
η	0.0000236	Pa×s	598.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[93.07; 28.62]	kJ/mol	[273.15; 675.64]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			1.20050e+02
Coefficient B			3.46500e-01
Coefficient C			9.71000e-01
Coefficient D			-1.71320e+00
Coefficient E			8.10910e-01
Critical temperature, Tc (K)			6.98000e+02
Temperature range, min.			273.15
Temperature range, max.			675.64
ΔvapH	93.07	kJ/mol	273.15	Calculated Property
ΔvapH	88.06	kJ/mol	317.87	Calculated Property
ΔvapH	83.08	kJ/mol	362.59	Calculated Property
ΔvapH	78.09	kJ/mol	407.31	Calculated Property
ΔvapH	72.99	kJ/mol	452.03	Calculated Property
ΔvapH	67.57	kJ/mol	496.76	Calculated Property
ΔvapH	61.51	kJ/mol	541.48	Calculated Property
ΔvapH	54.22	kJ/mol	586.20	Calculated Property
ΔvapH	44.54	kJ/mol	630.92	Calculated Property
ΔvapH	28.62	kJ/mol	675.64	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[3.20e-06; 4480.14]	kPa	[273.15; 698.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			2.07522e+02
Coefficient B			-1.87690e+04
Coefficient C			-2.71500e+01
Coefficient D			1.14100e-05
Coefficient E			2.00000e+00
Temperature range, min.			273.15
Temperature range, max.			698.00
Pvap	3.20e-06	kPa	273.15	Calculated Property
Pvap	1.45e-03	kPa	320.36	Calculated Property
Pvap	0.09	kPa	367.56	Calculated Property
Pvap	1.79	kPa	414.77	Calculated Property
Pvap	15.65	kPa	461.97	Calculated Property
Pvap	81.34	kPa	509.18	Calculated Property
Pvap	296.74	kPa	556.38	Calculated Property
Pvap	849.72	kPa	603.59	Calculated Property
Pvap	2062.48	kPa	650.79	Calculated Property
Pvap	4480.14	kPa	698.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1047.15; 530.75]	kg/m3	[273.15; 675.64]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			8.00171e+01
Coefficient B			2.52380e-01
Coefficient C			6.98000e+02
Coefficient D			2.85650e-01
Temperature range, min.			273.15
Temperature range, max.			675.64
ρl	1047.15	kg/m3	273.15	Calculated Property
ρl	1008.75	kg/m3	317.87	Calculated Property
ρl	968.57	kg/m3	362.59	Calculated Property
ρl	926.20	kg/m3	407.31	Calculated Property
ρl	881.07	kg/m3	452.03	Calculated Property
ρl	832.30	kg/m3	496.76	Calculated Property
ρl	778.48	kg/m3	541.48	Calculated Property
ρl	716.96	kg/m3	586.20	Calculated Property
ρl	641.77	kg/m3	630.92	Calculated Property
ρl	530.75	kg/m3	675.64	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.05; 0.00]	N/m	[273.15; 675.64]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-4.64190e-02
Coefficient B			1.23520e+01
Coefficient C			-2.07920e+00
Coefficient D			-1.08200e-03
Coefficient E			-5.49500e-07
Temperature range, min.			273.15
Temperature range, max.			675.64
γ	0.05	N/m	273.15	Calculated Property
γ	0.04	N/m	317.87	Calculated Property
γ	0.03	N/m	362.59	Calculated Property
γ	0.03	N/m	407.31	Calculated Property
γ	0.02	N/m	452.03	Calculated Property
γ	0.02	N/m	496.76	Calculated Property
γ	0.01	N/m	541.48	Calculated Property
γ	0.01	N/m	586.20	Calculated Property
γ	0.01	N/m	630.92	Calculated Property
γ	0.00	N/m	675.64	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.08]	W/m×K	[274.00; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			1.92610e-04
Coefficient B			9.37310e-01
Coefficient C			6.15430e+02
Coefficient D			2.39180e+04
Temperature range, min.			274.00
Temperature range, max.			1000.00
λgas	0.01	W/m×K	274.00	Calculated Property
λgas	0.02	W/m×K	354.67	Calculated Property
λgas	0.02	W/m×K	435.33	Calculated Property
λgas	0.03	W/m×K	516.00	Calculated Property
λgas	0.04	W/m×K	596.67	Calculated Property
λgas	0.04	W/m×K	677.33	Calculated Property
λgas	0.05	W/m×K	758.00	Calculated Property
λgas	0.06	W/m×K	838.67	Calculated Property
λgas	0.07	W/m×K	919.33	Calculated Property
λgas	0.08	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.20; 0.13]	W/m×K	[273.00; 517.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			-1.25700e-01
Coefficient B			-1.06070e+01
Coefficient C			-8.89280e-01
Coefficient D			-6.01020e-04
Coefficient E			-5.94780e-07
Temperature range, min.			273.00
Temperature range, max.			517.00
λliquid	0.20	W/m×K	273.00	Calculated Property
λliquid	0.19	W/m×K	300.11	Calculated Property
λliquid	0.18	W/m×K	327.22	Calculated Property
λliquid	0.17	W/m×K	354.33	Calculated Property
λliquid	0.17	W/m×K	381.44	Calculated Property
λliquid	0.16	W/m×K	408.56	Calculated Property
λliquid	0.15	W/m×K	435.67	Calculated Property
λliquid	0.14	W/m×K	462.78	Calculated Property
λliquid	0.13	W/m×K	489.89	Calculated Property
λliquid	0.13	W/m×K	517.00	Calculated Property

Similar Compounds

Find more compounds similar to Ethanol, 2-[(2-aminoethyl)amino]-.

Mixtures

• Ethanol, 2-[(2-aminoethyl)amino]- + Hydrogen sulfide + Water
• Ethanol, 2-[(2-aminoethyl)amino]- + Water
• Monoethanolamine + Ethanol, 2-[(2-aminoethyl)amino]-
• Ethanol, 2-[(2-aminoethyl)amino]- + Methyldiethanolamine + Water
• Ethanol + Ethanol, 2-[(2-aminoethyl)amino]-
• Carbon dioxide + Ethanol, 2-[(2-aminoethyl)amino]- + Water
• Carbon dioxide + Benzyl alcohol + Ethanol, 2-[(2-aminoethyl)amino]-
• Carbon dioxide + Ethanol, 2-[(2-aminoethyl)amino]- + Ethanol, 2,2'-oxybis-
• Carbon dioxide + Ethanol, 2-[(2-aminoethyl)amino]- + Triethylene glycol
• Ethanol, 2-[(2-aminoethyl)amino]- + Ethanol, 2-(methylamino)- + Water
• Ethanol, 2-[(2-aminoethyl)amino]- + Benzylamine + Water

Sources

• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 11 ChEDL chemicals 1.5.2, from Ambrose, D.; Tsonopoulos, C.; Nikitin, E. D. Vapor-Liquid Critical Properties of Elements and Compounds. 11. Organic Compounds Containing B + O; Halogens + N, + O, + O + S, + S, + Si; N + O; and O + S, + Si. J. Chem. Eng. Data 2009, 54, 669-689.
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• Cheméo Relay (1.0)
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Crippen Method
• Thermodynamic properties and CO2 solubility of monoethanolamine + diethylenetriamine/aminoethylethanolamine mixtures: Experimental measurements and thermodynamic modeling
• Experimental and e-NRTL model predicted VLE of CO2 in aqueous solutions of 2-((2-aminoethyl)-amino)-ethanol and speciation study
• Molar excess enthalpy (HEm) for various {alkanolamine (1) + water (2)} systems at T = (298.15, 313.15, and 323.15) K
• Equilibrium solubility of carbon dioxide in aqueous 2-((2-aminoethyl)amino)ethanol and N-methyldiethanolamine solution and modeling by electrolyte mPR-CPA EoS
• Measuring solubility of carbon dioxide in aqueous blends of N-methyldiethanolamine and 2-((2-aminoethyl)amino)ethanol at low CO2 loadings and modelling by electrolyte SAFT-HR EoS
• Excess molar enthalpies for binary mixtures of different amines with water
• Measuring and correlating solubility of hydrogen sulfide in aqueous solution of 2-((2 aminoethyl)amino)ethanol
• Volumetric and Viscometric Properties of Alcohol Amines + Ethanol Binary Mixtures
• Experimental Data and Modeling for Viscosity and Refractive Index of Aqueous Mixtures with 2-(Methylamino)ethanol (MAE) and Aminoethylethanolamine (AEEA)
• Heat of Absorption of CO2 and Heat Capacity Measurements in Aqueous Solutions of Benzylamine, N-(2-Aminoethyl)-ethanolamine, and Their Blends Using a Reaction Calorimeter
• Heat of Absorption of Carbon Dioxide (CO2) in Monoethanolamine (MEA) and 2-(Aminoethyl)ethanolamine (AEEA) Solutions
• Volumetric Properties, Viscosities, and Refractive Indices for Aqueous 2-((2-Aminoethyl)amino)ethanol Solutions from (298.15 to 343.15) K
• Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
• Vapor Pressures and Enthalpies of Vaporization of a Series of Low-Volatile Alkanolamines
• Solubility of CO2 in Nonaqueous Absorption System of 2-(2-Aminoethylamine)ethanol + Benzyl Alcohol
• Joback Method
• McGowan Method
• NIST Webbook

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