Chemical Properties of 1,2-Ethanediamine, N-(2-aminoethyl)- (CAS 111-40-0)

InChI

InChI=1S/C4H13N3/c5-1-3-7-4-2-6/h7H,1-6H2

InChI Key

RPNUMPOLZDHAAY-UHFFFAOYSA-N

Formula

C4H13N3

SMILES

NCCNCCN

Molecular Weight¹

103.17

CAS

111-40-0

Other Names

• (Aminoethyl)ethanediamine
• 1,2-Ethanediamine, N1-(2-aminoethyl)-
• 1,4,7-Triazaheptane
• 1,5-Diamino-3-azapentane
• 2,2'-Diaminodiethylamine
• 2,2'-Iminobis(ethanamine)
• 2,2'-Iminobisethylamine
• 2,2'-Iminodiethylamine
• 2-(2-Aminoethylamino)ethylamine
• 3-Azapentane-1,5-diamine
• Aminoethylethandiamine
• Ancamine DETA
• Barsamide 115
• Bis(2-aminoethyl)amine
• Bis[«beta»-aminoethyl]amine
• ChS-P 1
• D.E.H. 20
• DEH 20
• DETA
• Diethylamine, 2,2'-diamino-
• Diethylene triamine
• Epicure T
• Epon 3223
• Ethylamine, 2,2'-iminobis-
• Ethylenediamine, N-(2-aminoethyl)-
• H 9506
• N,N-Bis(2-aminoethyl)amine
• N-(2-Aminoethyl)-1,2-ethanediamine
• N-(2-Aminoethyl)ethylenediamine
• NSC 446
• Texacure EA-20
• UN 2079
• di(2-aminoethyl)amine
• diethylenetriamine
• «beta»,«beta»'-Diaminodiethylamine

• ω : Acentric Factor.
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• 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_fH°_liquid : Liquid phase 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).
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_c : Critical density (kg/m³).
• 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_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).
• T_triple : Triple Point Temperature (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	0.7002		ChemSep v8.3 pure component data Compiled value
ΔcH°liquid	-3366.70 ± 0.50	kJ/mol	NIST
η	0.0056272	Pa×s	Thermodynamic properties of binary liquid mixtures of diethylenetriamine with alcohols at different temperatures
ΔfG°	207.29	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-5.86	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°liquid	[-287.00; -65.20]	kJ/mol
ΔfH°liquid	-65.20 ± 0.50	kJ/mol	NIST
ΔfH°liquid	-287.00	kJ/mol	NIST
ΔfusH°	21.61	kJ/mol	Joback Calculated Property
ΔvapH°	63.40 ± 0.70	kJ/mol	NIST
logPoct/wat	-1.507		Crippen Calculated Property
McVol	97.160	ml/mol	McGowan Calculated Property
Pc	[3050.00; 4220.00]	kPa
Pc	4220.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3050.00 ± 250.00	kPa	NIST
Ptriple	5.25e-05	kPa	ChemSep v8.3 pure component data Compiled value
ρc	286.80 ± 15.47	kg/m3	NIST
Inp	[1025.00; 1030.00]
Inp	1030.00		NIST
Inp	1028.00		NIST
Inp	1025.00		NIST
Inp	1030.00		NIST
Ip	[1727.00; 1763.00]
Ip	1729.00		NIST
Ip	1734.00		NIST
Ip	1729.00		NIST
Ip	Outlier 1763.00		NIST
Ip	1748.00		NIST
Ip	1731.00		NIST
Ip	1727.00		NIST
Ip	1734.00		NIST
Tboil	[477.20; 480.15]	K
Tboil	480.00	K	ChemSep v8.3 pure component data Compiled value
Tboil	477.20	K	NIST
Tboil	480.15 ± 2.00	K	NIST
Tboil	480.05	K	NIST
Tc	[676.00; 677.00]	K
Tc	676.00	K	ChemSep v8.3 pure component data Compiled value
Tc	677.00 ± 6.00	K	NIST
Tfus	[234.00; 234.15]	K
Tfus	234.00	K	ChemSep v8.3 pure component data Compiled value
Tfus	234.15	K	NIST
Ttriple	234.15	K	ChemSep v8.3 pure component data Compiled value
UQi	3.95		ChemSep v8.3 pure component data Compiled value
URi	4.62		ChemSep v8.3 pure component data Compiled value
Vc	0.426	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2570000		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	[254.00; 274.00]	J/mol×K	[303.15; 353.15]
Cp,liquid	269.50	J/mol×K	303.15	Molar heat capacities of diethylenetriamine and 3-(methylamino)propylamine, their aqueous binaries, and aqueous ternaries with piperazine
Cp,liquid	269.90	J/mol×K	308.15	Molar heat capacities of diethylenetriamine and 3-(methylamino)propylamine, their aqueous binaries, and aqueous ternaries with piperazine
Cp,liquid	254.00	J/mol×K	313.00	NIST
Cp,liquid	270.20	J/mol×K	313.15	Molar heat capacities of diethylenetriamine and 3-(methylamino)propylamine, their aqueous binaries, and aqueous ternaries with piperazine
Cp,liquid	270.80	J/mol×K	318.15	Molar heat capacities of diethylenetriamine and 3-(methylamino)propylamine, their aqueous binaries, and aqueous ternaries with piperazine
Cp,liquid	271.20	J/mol×K	323.15	Molar heat capacities of diethylenetriamine and 3-(methylamino)propylamine, their aqueous binaries, and aqueous ternaries with piperazine
Cp,liquid	272.00	J/mol×K	328.15	Molar heat capacities of diethylenetriamine and 3-(methylamino)propylamine, their aqueous binaries, and aqueous ternaries with piperazine
Cp,liquid	272.70	J/mol×K	333.15	Molar heat capacities of diethylenetriamine and 3-(methylamino)propylamine, their aqueous binaries, and aqueous ternaries with piperazine
Cp,liquid	273.20	J/mol×K	338.15	Molar heat capacities of diethylenetriamine and 3-(methylamino)propylamine, their aqueous binaries, and aqueous ternaries with piperazine
Cp,liquid	273.60	J/mol×K	343.15	Molar heat capacities of diethylenetriamine and 3-(methylamino)propylamine, their aqueous binaries, and aqueous ternaries with piperazine
Cp,liquid	273.80	J/mol×K	348.15	Molar heat capacities of diethylenetriamine and 3-(methylamino)propylamine, their aqueous binaries, and aqueous ternaries with piperazine
Cp,liquid	274.00	J/mol×K	353.15	Molar heat capacities of diethylenetriamine and 3-(methylamino)propylamine, their aqueous binaries, and aqueous ternaries with piperazine
ΔvapH	54.80	kJ/mol	406.00	NIST
ρl	[891.90; 951.16]	kg/m3	[293.15; 363.15]
ρl	951.16	kg/m3	293.15	Volumetric and Viscometric Properties of Alcohol Amines + Ethanol Binary Mixtures
ρl	951.00	kg/m3	293.15	Density, viscosity, and excess properties of aqueous solution of diethylenetriamine (DETA)
ρl	945.80	kg/m3	298.15	Thermodynamic properties and CO2 solubility of monoethanolamine + diethylenetriamine/aminoethylethanolamine mixtures: Experimental measurements and thermodynamic modeling
ρl	942.30	kg/m3	303.15	Density, viscosity, and excess properties of aqueous solution of diethylenetriamine (DETA)
ρl	942.19	kg/m3	303.15	Volumetric and Viscometric Properties of Alcohol Amines + Ethanol Binary Mixtures
ρl	942.10	kg/m3	303.15	Mutual diffusion coefficients, density, and viscosity of aqueoussolutions of new polyamine CO2absorbents
ρl	942.10	kg/m3	303.15	Thermodynamic properties and CO2 solubility of monoethanolamine + diethylenetriamine/aminoethylethanolamine mixtures: Experimental measurements and thermodynamic modeling
ρl	937.90	kg/m3	308.15	Mutual diffusion coefficients, density, and viscosity of aqueoussolutions of new polyamine CO2absorbents
ρl	937.80	kg/m3	308.15	Thermodynamic properties and CO2 solubility of monoethanolamine + diethylenetriamine/aminoethylethanolamine mixtures: Experimental measurements and thermodynamic modeling
ρl	933.80	kg/m3	313.15	Density, viscosity, and excess properties of aqueous solution of diethylenetriamine (DETA)
ρl	933.80	kg/m3	313.15	Mutual diffusion coefficients, density, and viscosity of aqueoussolutions of new polyamine CO2absorbents
ρl	933.93	kg/m3	313.15	Volumetric and Viscometric Properties of Alcohol Amines + Ethanol Binary Mixtures
ρl	929.60	kg/m3	318.15	Mutual diffusion coefficients, density, and viscosity of aqueoussolutions of new polyamine CO2absorbents
ρl	925.50	kg/m3	323.15	Mutual diffusion coefficients, density, and viscosity of aqueoussolutions of new polyamine CO2absorbents
ρl	925.50	kg/m3	323.15	Density, viscosity, and excess properties of aqueous solution of diethylenetriamine (DETA)
ρl	925.42	kg/m3	323.15	Volumetric and Viscometric Properties of Alcohol Amines + Ethanol Binary Mixtures
ρl	917.00	kg/m3	333.15	Density, viscosity, and excess properties of aqueous solution of diethylenetriamine (DETA)
ρl	908.90	kg/m3	343.15	Density, viscosity, and excess properties of aqueous solution of diethylenetriamine (DETA)
ρl	900.40	kg/m3	353.15	Density, viscosity, and excess properties of aqueous solution of diethylenetriamine (DETA)
ρl	891.90	kg/m3	363.15	Density, viscosity, and excess properties of aqueous solution of diethylenetriamine (DETA)

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[141.60; 378.64]	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			7.37370e+01
Coefficient B			-4.51700e+02
Coefficient C			5.79724e+00
Coefficient D			3.01970e-04
Coefficient E			-1.01810e-07
Comment			ChemSep eq 16, IdealGasHeatCapacityCp
Temperature range, min.			273.00
Temperature range, max.			1500.00
Cp,gas	141.60	J/mol×K	273.00	Calculated Property
Cp,gas	195.28	J/mol×K	409.33	Calculated Property
Cp,gas	238.40	J/mol×K	545.67	Calculated Property
Cp,gas	272.78	J/mol×K	682.00	Calculated Property
Cp,gas	300.57	J/mol×K	818.33	Calculated Property
Cp,gas	323.27	J/mol×K	954.67	Calculated Property
Cp,gas	341.87	J/mol×K	1091.00	Calculated Property
Cp,gas	357.03	J/mol×K	1227.33	Calculated Property
Cp,gas	369.18	J/mol×K	1363.67	Calculated Property
Cp,gas	378.64	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[204.40; 274.05]	J/mol×K	[338.00; 498.00]	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			4.22910e+01
Coefficient B			-1.30860e+02
Coefficient C			4.78824e+00
Coefficient D			2.42430e-03
Coefficient E			-1.15760e-06
Comment			ChemSep eq 16, LiquidHeatCapacityCp
Temperature range, min.			338.00
Temperature range, max.			498.00
Cp,liquid	204.40	J/mol×K	338.00	Calculated Property
Cp,liquid	212.40	J/mol×K	355.78	Calculated Property
Cp,liquid	220.33	J/mol×K	373.56	Calculated Property
Cp,liquid	228.20	J/mol×K	391.33	Calculated Property
Cp,liquid	236.02	J/mol×K	409.11	Calculated Property
Cp,liquid	243.76	J/mol×K	426.89	Calculated Property
Cp,liquid	251.45	J/mol×K	444.67	Calculated Property
Cp,liquid	259.06	J/mol×K	462.44	Calculated Property
Cp,liquid	266.59	J/mol×K	480.22	Calculated Property
Cp,liquid	274.05	J/mol×K	498.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0322145; 0.0001404]	Pa×s	[234.15; 576.00]	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			-1.01170e+01
Coefficient B			2.07570e+03
Coefficient C			-4.07110e-01
Coefficient D			6.93220e-07
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, LiquidViscosity
Temperature range, min.			234.15
Temperature range, max.			576.00
η	0.0322145	Pa×s	234.15	Calculated Property
η	0.0089105	Pa×s	272.13	Calculated Property
η	0.0033708	Pa×s	310.12	Calculated Property
η	0.0015763	Pa×s	348.10	Calculated Property
η	0.0008569	Pa×s	386.08	Calculated Property
η	0.0005206	Pa×s	424.07	Calculated Property
η	0.0003441	Pa×s	462.05	Calculated Property
η	0.0002430	Pa×s	500.03	Calculated Property
η	0.0001808	Pa×s	538.02	Calculated Property
η	0.0001404	Pa×s	576.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[59.36; 0.00]	kJ/mol	[234.15; 676.00]	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			6.20087e+01
Coefficient B			-5.21717e-01
Coefficient C			2.92251e+00
Coefficient D			-3.78597e+00
Coefficient E			1.59195e+00
Critical temperature, Tc (K)			6.76000e+02
Comment			ChemSep eq 106, HeatOfVaporization
Temperature range, min.			234.15
Temperature range, max.			676.00
ΔvapH	59.36	kJ/mol	234.15	Calculated Property
ΔvapH	57.00	kJ/mol	283.24	Calculated Property
ΔvapH	54.56	kJ/mol	332.34	Calculated Property
ΔvapH	52.17	kJ/mol	381.43	Calculated Property
ΔvapH	49.86	kJ/mol	430.53	Calculated Property
ΔvapH	47.56	kJ/mol	479.62	Calculated Property
ΔvapH	45.04	kJ/mol	528.72	Calculated Property
ΔvapH	41.80	kJ/mol	577.81	Calculated Property
ΔvapH	36.49	kJ/mol	626.91	Calculated Property
ΔvapH	0.00	kJ/mol	676.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[9.39e-06; 4123.40]	kPa	[234.15; 676.00]	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			9.32776e+01
Coefficient B			-1.06084e+04
Coefficient C			-1.09620e+01
Coefficient D			4.74905e-06
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			234.15
Temperature range, max.			676.00
Pvap	9.39e-06	kPa	234.15	Calculated Property
Pvap	3.38e-03	kPa	283.24	Calculated Property
Pvap	0.17	kPa	332.34	Calculated Property
Pvap	2.72	kPa	381.43	Calculated Property
Pvap	20.76	kPa	430.53	Calculated Property
Pvap	97.85	kPa	479.62	Calculated Property
Pvap	331.65	kPa	528.72	Calculated Property
Pvap	892.03	kPa	577.81	Calculated Property
Pvap	2034.94	kPa	626.91	Calculated Property
Pvap	4123.40	kPa	676.00	Calculated Property
Pvap	[5.21e-05; 3989.70]	kPa	[234.15; 676.00]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			8.10727e+01
Coefficient B			-9.24563e+03
Coefficient C			-9.48992e+00
Coefficient D			5.98254e-06
Coefficient E			0.00000e+00
Temperature range, min.			234.15
Temperature range, max.			676.00
Pvap	5.21e-05	kPa	234.15	Calculated Property
Pvap	9.35e-03	kPa	283.24	Calculated Property
Pvap	0.31	kPa	332.34	Calculated Property
Pvap	3.66	kPa	381.43	Calculated Property
Pvap	23.34	kPa	430.53	Calculated Property
Pvap	98.57	kPa	479.62	Calculated Property
Pvap	314.84	kPa	528.72	Calculated Property
Pvap	828.98	kPa	577.81	Calculated Property
Pvap	1906.90	kPa	626.91	Calculated Property
Pvap	3989.70	kPa	676.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1005.33; 301.56]	kg/m3	[234.15; 676.00]	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			7.74592e+01
Coefficient B			2.56860e-01
Coefficient C			6.76000e+02
Coefficient D			2.85000e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			234.15
Temperature range, max.			676.00
ρl	1005.33	kg/m3	234.15	Calculated Property
ρl	966.15	kg/m3	283.24	Calculated Property
ρl	925.04	kg/m3	332.34	Calculated Property
ρl	881.53	kg/m3	381.43	Calculated Property
ρl	834.93	kg/m3	430.53	Calculated Property
ρl	784.15	kg/m3	479.62	Calculated Property
ρl	727.33	kg/m3	528.72	Calculated Property
ρl	660.70	kg/m3	577.81	Calculated Property
ρl	574.04	kg/m3	626.91	Calculated Property
ρl	301.56	kg/m3	676.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.05; 2.66e-05]	N/m	[234.15; 672.02]	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			-2.17030e-02
Coefficient B			4.75190e+01
Coefficient C			-2.65920e+00
Coefficient D			-8.08470e-05
Coefficient E			-2.62670e-06
Comment			ChemSep eq 16, SurfaceTension, ChemSep Tmax 676 K
Temperature range, min.			234.15
Temperature range, max.			672.02
γ	0.05	N/m	234.15	Calculated Property
γ	0.04	N/m	282.80	Calculated Property
γ	0.04	N/m	331.46	Calculated Property
γ	0.03	N/m	380.11	Calculated Property
γ	0.02	N/m	428.76	Calculated Property
γ	0.02	N/m	477.41	Calculated Property
γ	0.01	N/m	526.07	Calculated Property
γ	0.01	N/m	574.72	Calculated Property
γ	0.00	N/m	623.37	Calculated Property
γ	2.66e-05	N/m	672.02	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.08]	W/m×K	[234.15; 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			1.77370e-04
Coefficient B			9.49140e-01
Coefficient C			5.91080e+02
Coefficient D			2.70110e+04
Comment			ChemSep eq 102, VaporThermalConductivity
Temperature range, min.			234.15
Temperature range, max.			1000.00
λgas	0.01	W/m×K	234.15	Calculated Property
λgas	0.01	W/m×K	319.24	Calculated Property
λgas	0.02	W/m×K	404.34	Calculated Property
λgas	0.03	W/m×K	489.43	Calculated Property
λgas	0.03	W/m×K	574.53	Calculated Property
λgas	0.04	W/m×K	659.62	Calculated Property
λgas	0.05	W/m×K	744.72	Calculated Property
λgas	0.06	W/m×K	829.81	Calculated Property
λgas	0.07	W/m×K	914.91	Calculated Property
λgas	0.08	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.10]	W/m×K	[234.15; 480.25]	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			-7.86670e-02
Coefficient B			1.41140e+00
Coefficient C			-1.31670e+00
Coefficient D			-4.16560e-04
Coefficient E			-8.78440e-07
Comment			ChemSep eq 16, LiquidThermalConductivity
Temperature range, min.			234.15
Temperature range, max.			480.25
λliquid	0.15	W/m×K	234.15	Calculated Property
λliquid	0.15	W/m×K	261.49	Calculated Property
λliquid	0.14	W/m×K	288.84	Calculated Property
λliquid	0.14	W/m×K	316.18	Calculated Property
λliquid	0.13	W/m×K	343.53	Calculated Property
λliquid	0.13	W/m×K	370.87	Calculated Property
λliquid	0.12	W/m×K	398.22	Calculated Property
λliquid	0.11	W/m×K	425.56	Calculated Property
λliquid	0.11	W/m×K	452.91	Calculated Property
λliquid	0.10	W/m×K	480.25	Calculated Property

Similar Compounds

Find more compounds similar to 1,2-Ethanediamine, N-(2-aminoethyl)-.

Mixtures

• 1,2-Ethanediamine, N-(2-aminoethyl)- + Water
• 1,2-Ethanediamine, N-(2-aminoethyl)- + 1-Propanol, 2-methyl-
• 2-Propanol + 1,2-Ethanediamine, N-(2-aminoethyl)-
• 1,2-Ethanediamine, N-(2-aminoethyl)- + 1-Butanol
• Monoethanolamine + 1,2-Ethanediamine, N-(2-aminoethyl)-
• 1,2-Ethanediamine, N-(2-aminoethyl)- + Carbon dioxide + Water
• Piperazine + 1,2-Ethanediamine, N-(2-aminoethyl)- + Water
• 1,2-Ethanediamine, N-(2-aminoethyl)- + Ethanol
• Nitrous oxide + 1,2-Ethanediamine, N-(2-aminoethyl)-
• Nitrous oxide + 1,2-Ethanediamine, N-(2-aminoethyl)- + Water

Sources

• KDB Vapor Pressure Data
• 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
• Mutual diffusion coefficients, density, and viscosity of aqueoussolutions of new polyamine CO2absorbents
• Thermodynamic properties and CO2 solubility of monoethanolamine + diethylenetriamine/aminoethylethanolamine mixtures: Experimental measurements and thermodynamic modeling
• Density, viscosity, and excess properties of aqueous solution of diethylenetriamine (DETA)
• Equilibrium solubility of carbon dioxide in aqueous solutions of (diethylenetriamine + piperazine)
• Excess molar enthalpies for binary mixtures of different amines with water
• Thermodynamic properties of binary liquid mixtures of diethylenetriamine with alcohols at different temperatures
• Molar heat capacities of diethylenetriamine and 3-(methylamino)propylamine, their aqueous binaries, and aqueous ternaries with piperazine
• Volumetric and Viscometric Properties of Alcohol Amines + Ethanol Binary Mixtures
• Solubility of N2O in Aqueous Solution of Diethylenetriamine
• Joback Method
• KDB
• McGowan Method
• NIST Webbook

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