Chemical Properties of ETHANOL, 2,2'-IMINOBIS- (CAS 111-42-2)

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'-Iminodi-1-ethanol
• 2,2'-Iminodiethanol
• 2,2'-azanediylbis(ethan-1-ol)
• 2,2'-iminobis-ethanol
• 2-[(2-Hydroxyethyl)amino]ethanol
• Bis(2-hydroxyethyl)amine
• Bis(hydroxyethyl)amine
• DEA
• Dabco DEOA-LF
• Di(2-hydroxyethyl)amine
• Diaethanolamin
• Diethanol, 2,2'-imino-
• Diethanolamin
• Diethylamine, 2,2'-dihydroxy-
• Diethylolamine
• Diolamine
• Ethanol, 2,2'-iminodi-
• Iminodiethanol
• N,N'-Iminodiethanol
• N,N-Bis(2-hydroxyethyl)amine
• N,N-Diethanolamine
• NCI-C55174
• NSC 4959
• Niax DEOA-LF
• diethanolamine

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_solid : Standard solid 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).
• C_p,solid : Solid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• ε_r : Dielectric Constant (Relative permittivity).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_solid : Solid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_subH° : Enthalpy of sublimation 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).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• pKa : Log10 of Acid Dissociation Constant.
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I : Polar retention indices.
• c_sound,fluid : Speed of sound in fluid (m/s).
• 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 thermal conductivity (W/m×K).
• λ : 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	0.9915		ChemSep v8.3 pure component data Compiled value
PAff	953.00	kJ/mol	NIST
BasG	920.00	kJ/mol	NIST
ΔcH°solid	-2652.30 ± 2.50	kJ/mol	NIST
μ	0.85	debye	ChemSep v8.3 pure component data Compiled value
η	0.5665700	Pa×s	Densities, Viscosities, and Refractive Indices of Aqueous Alkanolamine Solutions as Potential Carbon Dioxide Removal Reagents
Tflash,cc	410.15	K	NCMS SOLV-DB
ΔfG°	-225.74	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[-397.10; -373.00]	kJ/mol
ΔfH°gas	-373.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
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°	65.23	kJ/mol	NCMS SOLV-DB
log10WS	1.00		Relay (1.0) Calculated Property
logPoct/wat	-1.430		NCMS SOLV-DB
McVol	88.940	ml/mol	McGowan Calculated Property
NFPA Fire	[%!d(float64=1); %!d(float64=1)]
NFPA Fire	1		KDB
NFPA Fire	1		NCMS SOLV-DB
NFPA Health	[%!d(float64=1); %!d(float64=1)]
NFPA Health	1		KDB
NFPA Health	1		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	4720.00	kPa	ChemSep v8.3 pure component data Compiled value
pKa	8.96		NCMS SOLV-DB
Ptriple	1.02e-04	kPa	ChemSep v8.3 pure component data Compiled value
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	Experimental and predicted vapor-liquid equilibrium for binary systems with diethanolamine, m-cresol and p-cresol at 20.0 kPa
Tboil	542.00	K	ChemSep v8.3 pure component data Compiled value
Tboil	541.95	K	NCMS SOLV-DB
Tboil	544.20	K	NIST
Tboil	541.55	K	NIST
Tc	736.60	K	ChemSep v8.3 pure component data Compiled value
Tfus	[300.15; 301.65]	K
Tfus	Outlier 300.15	K	Thermodynamic and Kinetic Studies of CO2 Capture by Glycol and Amine-Based Deep Eutectic Solvents
Tfus	301.15	K	ChemSep v8.3 pure component data Compiled value
Tfus	301.65	K	NCMS SOLV-DB
Tfus	301.15	K	NIST
Tfus	301.10 ± 0.07	K	NIST
Tfus	301.20 ± 0.60	K	NIST
Ttriple	301.15	K	ChemSep v8.3 pure component data Compiled value
UQi	4.96		ChemSep v8.3 pure component data Compiled value
URi	5.23		ChemSep v8.3 pure component data Compiled value
Vc	0.349	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2430000		ChemSep v8.3 pure component data Compiled value
Zra	0.24		ChemSep v8.3 pure component data Compiled value

Cheméo can also estimate Ionization energy 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,solid	137.00	J/mol×K	298.15	NIST
η	[0.0025220; 0.3805000]	Pa×s	[298.15; 423.15]
η	0.3510000	Pa×s	298.15	NCMS SOLV-DB
η	0.3805000	Pa×s	303.15	Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
η	0.1835000	Pa×s	313.15	Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
η	0.1006000	Pa×s	323.15	Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
η	0.0613600	Pa×s	333.15	Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
η	0.0337900	Pa×s	343.15	Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
η	0.0231350	Pa×s	353.15	Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
η	0.0148080	Pa×s	363.15	Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
η	0.0104110	Pa×s	373.15	Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
η	0.0080110	Pa×s	383.15	Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
η	0.0059850	Pa×s	393.15	Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
η	0.0045840	Pa×s	403.15	Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
η	0.0036090	Pa×s	413.15	Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
η	0.0025220	Pa×s	423.15	Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
εr	[22.13; 24.69]		[303.15; 328.15]
εr	24.69		303.15	Dielectric Constants of Aqueous Diisopropanolamine, Diethanolamine, N-Methyldiethanolamine, Triethanolamine, and 2-Amino-2-methyl-1-propanol Solutions
εr	24.30		308.15	Dielectric Constants of Aqueous Diisopropanolamine, Diethanolamine, N-Methyldiethanolamine, Triethanolamine, and 2-Amino-2-methyl-1-propanol Solutions
εr	23.86		313.15	Dielectric Constants of Aqueous Diisopropanolamine, Diethanolamine, N-Methyldiethanolamine, Triethanolamine, and 2-Amino-2-methyl-1-propanol Solutions
εr	23.28		318.15	Dielectric Constants of Aqueous Diisopropanolamine, Diethanolamine, N-Methyldiethanolamine, Triethanolamine, and 2-Amino-2-methyl-1-propanol Solutions
εr	22.63		323.15	Dielectric Constants of Aqueous Diisopropanolamine, Diethanolamine, N-Methyldiethanolamine, Triethanolamine, and 2-Amino-2-methyl-1-propanol Solutions
εr	22.13		328.15	Dielectric Constants of Aqueous Diisopropanolamine, Diethanolamine, N-Methyldiethanolamine, Triethanolamine, and 2-Amino-2-methyl-1-propanol Solutions
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	[1.33e-03; 4.94]	kPa	[293.15; 452.40]
Pvap	1.33e-03	kPa	293.15	NCMS SOLV-DB
Pvap	1.44	kPa	427.50	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	1.94	kPa	433.00	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	2.94	kPa	441.40	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	3.94	kPa	447.40	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	4.94	kPa	452.40	Vapor Pressures of Several Commercially Used Alkanolamines
n0	1.47700		298.15	NCMS SOLV-DB
ρl	[1050.24; 1107.05]	kg/m3	[278.14; 363.15]
ρl	1107.05	kg/m3	278.14	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
ρl	1103.88	kg/m3	283.14	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
ρl	1097.51	kg/m3	293.15	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
ρl	1097.40	kg/m3	293.15	Volumetric and viscometric behaviour of the binary systems of N-methyldiethanolamine and diethanolamine with 1-butyl-3-methylimidazolium acetate at various temperatures
ρl	1096.10	kg/m3	293.15	Density and Viscosity for Binary Mixtures of Diethylene Glycol Monobutyl Ether with Monoethanolamine, Diethanolamine, and Triethanolamine from (293.15 to 333.15) K
ρl	1097.61	kg/m3	293.15	Volumetric properties of binary mixtures of dimethyl sulfoxide with amines from (293.15 to 363.15) K
ρl	1094.02	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	1091.06	kg/m3	303.14	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
ρl	1090.50	kg/m3	303.15	Volumetric and viscometric behaviour of the binary systems of N-methyldiethanolamine and diethanolamine with 1-butyl-3-methylimidazolium acetate at various temperatures
ρl	1089.80	kg/m3	303.15	Density and Viscosity for Binary Mixtures of Diethylene Glycol Monobutyl Ether with Monoethanolamine, Diethanolamine, and Triethanolamine from (293.15 to 333.15) K
ρl	1090.79	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	1091.17	kg/m3	303.15	Volumetric properties of binary mixtures of dimethyl sulfoxide with amines from (293.15 to 363.15) K
ρl	1087.51	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	1084.49	kg/m3	313.14	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
ρl	1084.60	kg/m3	313.15	Volumetric properties of binary mixtures of dimethyl sulfoxide with amines from (293.15 to 363.15) K
ρl	1083.90	kg/m3	313.15	Volumetric and viscometric behaviour of the binary systems of N-methyldiethanolamine and diethanolamine with 1-butyl-3-methylimidazolium acetate at various temperatures
ρl	1084.20	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	1084.70	kg/m3	313.15	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
ρl	1083.70	kg/m3	313.15	Density and Viscosity for Binary Mixtures of Diethylene Glycol Monobutyl Ether with Monoethanolamine, Diethanolamine, and Triethanolamine from (293.15 to 333.15) K
ρl	1080.86	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	1077.78	kg/m3	323.14	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
ρl	1077.88	kg/m3	323.15	Volumetric properties of binary mixtures of dimethyl sulfoxide with amines from (293.15 to 363.15) K
ρl	1077.49	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	1077.40	kg/m3	323.15	Density and Viscosity for Binary Mixtures of Diethylene Glycol Monobutyl Ether with Monoethanolamine, Diethanolamine, and Triethanolamine from (293.15 to 333.15) K
ρl	1077.40	kg/m3	323.15	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
ρl	1077.10	kg/m3	323.15	Volumetric and viscometric behaviour of the binary systems of N-methyldiethanolamine and diethanolamine with 1-butyl-3-methylimidazolium acetate at various temperatures
ρl	1071.00	kg/m3	333.14	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
ρl	1071.11	kg/m3	333.14	Volumetric properties of binary mixtures of dimethyl sulfoxide with amines from (293.15 to 363.15) K
ρl	1070.30	kg/m3	333.15	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
ρl	1070.70	kg/m3	333.15	Density and Viscosity for Binary Mixtures of Diethylene Glycol Monobutyl Ether with Monoethanolamine, Diethanolamine, and Triethanolamine from (293.15 to 333.15) K
ρl	1070.30	kg/m3	333.15	Volumetric and viscometric behaviour of the binary systems of N-methyldiethanolamine and diethanolamine with 1-butyl-3-methylimidazolium acetate at various temperatures
ρl	1064.25	kg/m3	343.14	Volumetric properties of binary mixtures of dimethyl sulfoxide with amines from (293.15 to 363.15) K
ρl	1064.14	kg/m3	343.14	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
ρl	1063.50	kg/m3	343.15	Volumetric and viscometric behaviour of the binary systems of N-methyldiethanolamine and diethanolamine with 1-butyl-3-methylimidazolium acetate at various temperatures
ρl	1060.68	kg/m3	348.14	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
ρl	1057.31	kg/m3	353.14	Volumetric properties of binary mixtures of dimethyl sulfoxide with amines from (293.15 to 363.15) K
ρl	1056.83	kg/m3	353.15	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
ρl	1050.24	kg/m3	363.15	Volumetric properties of binary mixtures of dimethyl sulfoxide with amines from (293.15 to 363.15) K
csound,fluid	[1660.36; 1739.20]	m/s	[293.15; 323.15]
csound,fluid	1739.20	m/s	293.15	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
csound,fluid	1736.54	m/s	293.15	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
csound,fluid	1723.96	m/s	298.15	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
csound,fluid	1711.30	m/s	303.15	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
csound,fluid	1711.55	m/s	303.15	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
csound,fluid	1698.70	m/s	308.15	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
csound,fluid	1685.90	m/s	313.15	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
csound,fluid	1686.13	m/s	313.15	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
csound,fluid	1673.76	m/s	318.15	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
csound,fluid	1661.10	m/s	323.15	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
csound,fluid	1660.36	m/s	323.15	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
γ	[0.04; 0.05]	N/m	[293.15; 323.20]
γ	0.05	N/m	293.15	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
γ	0.05	N/m	298.15	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
γ	0.05	N/m	298.15	NCMS SOLV-DB
γ	0.05	N/m	303.15	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
γ	0.05	N/m	303.20	Investigation of surface tension and viscosity for aqueous solutions of MEA-MeOH and DEA-MeOH
γ	0.05	N/m	313.15	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
γ	0.04	N/m	313.20	Investigation of surface tension and viscosity for aqueous solutions of MEA-MeOH and DEA-MeOH
γ	0.05	N/m	323.15	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
γ	0.04	N/m	323.20	Investigation of surface tension and viscosity for aqueous solutions of MEA-MeOH and DEA-MeOH

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
Cp,gas	[133.02; 347.35]	J/mol×K	[273.00; 1500.10]	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			9.22160e+01
Coefficient B			-6.24100e+02
Coefficient C			6.03024e+00
Coefficient D			-1.47790e-04
Coefficient E			6.63370e-08
Comment			ChemSep eq 16, IdealGasHeatCapacityCp
Temperature range, min.			273.00
Temperature range, max.			1500.10
Cp,gas	133.02	J/mol×K	273.00	Calculated Property
Cp,gas	178.38	J/mol×K	409.34	Calculated Property
Cp,gas	216.88	J/mol×K	545.69	Calculated Property
Cp,gas	247.50	J/mol×K	682.03	Calculated Property
Cp,gas	271.89	J/mol×K	818.38	Calculated Property
Cp,gas	291.74	J/mol×K	954.72	Calculated Property
Cp,gas	308.36	J/mol×K	1091.07	Calculated Property
Cp,gas	322.73	J/mol×K	1227.41	Calculated Property
Cp,gas	335.55	J/mol×K	1363.76	Calculated Property
Cp,gas	347.35	J/mol×K	1500.10	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[194.95; 505.85]	J/mol×K	[200.00; 715.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K
Coefficient A			8.82347e+01
Coefficient B			4.83257e-01
Coefficient C			2.94569e-04
Coefficient D			-2.14761e-07
Coefficient E			0.00000e+00
Comment			ChemSep eq 4, LiquidHeatCapacityCp
Temperature range, min.			200.00
Temperature range, max.			715.00
Cp,liquid	194.95	J/mol×K	200.00	Calculated Property
Cp,liquid	228.37	J/mol×K	257.22	Calculated Property
Cp,liquid	262.64	J/mol×K	314.44	Calculated Property
Cp,liquid	297.51	J/mol×K	371.67	Calculated Property
Cp,liquid	332.74	J/mol×K	428.89	Calculated Property
Cp,liquid	368.09	J/mol×K	486.11	Calculated Property
Cp,liquid	403.32	J/mol×K	543.33	Calculated Property
Cp,liquid	438.18	J/mol×K	600.56	Calculated Property
Cp,liquid	472.44	J/mol×K	657.78	Calculated Property
Cp,liquid	505.85	J/mol×K	715.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.7943674; 0.0000834]	Pa×s	[293.15; 589.28]	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			-2.87020e-01
Coefficient B			6.08050e+03
Coefficient C			-3.87080e+00
Coefficient D			1.51700e-05
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, LiquidViscosity
Temperature range, min.			293.15
Temperature range, max.			589.28
η	0.7943674	Pa×s	293.15	Calculated Property
η	0.0883851	Pa×s	326.05	Calculated Property
η	0.0155189	Pa×s	358.96	Calculated Property
η	0.0038767	Pa×s	391.86	Calculated Property
η	0.0012821	Pa×s	424.76	Calculated Property
η	0.0005331	Pa×s	457.67	Calculated Property
η	0.0002683	Pa×s	490.57	Calculated Property
η	0.0001589	Pa×s	523.47	Calculated Property
η	0.0001082	Pa×s	556.38	Calculated Property
η	0.0000834	Pa×s	589.28	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[87.10; 36.10]	kJ/mol	[301.15; 713.68]	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			7.90134e+01
Coefficient B			-1.86515e+00
Coefficient C			6.82097e+00
Coefficient D			-7.96305e+00
Coefficient E			3.25155e+00
Critical temperature, Tc (K)			7.36600e+02
Comment			ChemSep eq 106, HeatOfVaporization
Temperature range, min.			301.15
Temperature range, max.			713.68
ΔvapH	87.10	kJ/mol	301.15	Calculated Property
ΔvapH	83.10	kJ/mol	346.99	Calculated Property
ΔvapH	78.96	kJ/mol	392.82	Calculated Property
ΔvapH	74.87	kJ/mol	438.66	Calculated Property
ΔvapH	70.86	kJ/mol	484.50	Calculated Property
ΔvapH	66.83	kJ/mol	530.33	Calculated Property
ΔvapH	62.46	kJ/mol	576.17	Calculated Property
ΔvapH	57.12	kJ/mol	622.01	Calculated Property
ΔvapH	49.56	kJ/mol	667.84	Calculated Property
ΔvapH	36.10	kJ/mol	713.68	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[425.18; 567.97]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
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
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	[6.53e-05; 4183.59]	kPa	[301.15; 736.60]	ChemSep v8.3 pure component data Compiled value
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.68272e+01
Coefficient B			-5.44170e+03
Coefficient C			-9.55190e+01
Comment			ChemSep eq 10, VaporPressure
Temperature range, min.			301.15
Temperature range, max.			736.60
Pvap	6.53e-05	kPa	301.15	Calculated Property
Pvap	0.01	kPa	349.53	Calculated Property
Pvap	0.31	kPa	397.92	Calculated Property
Pvap	3.72	kPa	446.30	Calculated Property
Pvap	24.40	kPa	494.68	Calculated Property
Pvap	106.52	kPa	543.07	Calculated Property
Pvap	348.82	kPa	591.45	Calculated Property
Pvap	925.09	kPa	639.83	Calculated Property
Pvap	2092.27	kPa	688.22	Calculated Property
Pvap	4183.59	kPa	736.60	Calculated Property
Pvap	[7.74e-05; 102.80]	kPa	[301.15; 542.15]	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			2.16769e+02
Coefficient B			-1.89915e+04
Coefficient C			-2.88239e+01
Coefficient D			1.48221e-05
Coefficient E			0.00000e+00
Temperature range, min.			301.15
Temperature range, max.			542.15
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
Pvap	[7.75; 281.85]	kPa	[464.00; 582.40]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.67273e+01
Coefficient B			-5.36171e+03
Coefficient C			-9.87510e+01
Reference			McDonald, Shrader, et al., 1959, 2
Temperature range, min.			464.00
Temperature range, max.			582.40
Pvap	7.75	kPa	464.00	Calculated Property
Pvap	12.91	kPa	477.16	Calculated Property
Pvap	20.78	kPa	490.31	Calculated Property
Pvap	32.43	kPa	503.47	Calculated Property
Pvap	49.22	kPa	516.62	Calculated Property
Pvap	72.82	kPa	529.78	Calculated Property
Pvap	105.25	kPa	542.93	Calculated Property
Pvap	148.95	kPa	556.09	Calculated Property
Pvap	206.73	kPa	569.24	Calculated Property
Pvap	281.85	kPa	582.40	Calculated Property
Pvap	[8.71; 46.04]	kPa	[466.93; 514.47]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.65658e+01
Coefficient B			-5.23596e+03
Coefficient C			-1.03362e+02
Reference			McDonald, Shrader, et al., 1959, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			466.93
Temperature range, max.			514.47
Pvap	8.71	kPa	466.93	Calculated Property
Pvap	10.70	kPa	472.21	Calculated Property
Pvap	13.08	kPa	477.49	Calculated Property
Pvap	15.89	kPa	482.78	Calculated Property
Pvap	19.21	kPa	488.06	Calculated Property
Pvap	23.09	kPa	493.34	Calculated Property
Pvap	27.63	kPa	498.62	Calculated Property
Pvap	32.91	kPa	503.91	Calculated Property
Pvap	39.01	kPa	509.19	Calculated Property
Pvap	46.04	kPa	514.47	Calculated Property
Pvap	[7.75; 281.85]	kPa	[464.00; 582.40]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.67273e+01
Coefficient B			-5.36171e+03
Coefficient C			-9.87510e+01
Reference			McDonald, Shrader, et al., 1959
Temperature range, min.			464.00
Temperature range, max.			582.40
Pvap	7.75	kPa	464.00	Calculated Property
Pvap	12.91	kPa	477.16	Calculated Property
Pvap	20.78	kPa	490.31	Calculated Property
Pvap	32.43	kPa	503.47	Calculated Property
Pvap	49.22	kPa	516.62	Calculated Property
Pvap	72.82	kPa	529.78	Calculated Property
Pvap	105.25	kPa	542.93	Calculated Property
Pvap	148.95	kPa	556.09	Calculated Property
Pvap	206.73	kPa	569.24	Calculated Property
Pvap	281.85	kPa	582.40	Calculated Property
Pvap	[8.71; 46.04]	kPa	[466.93; 514.47]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.65658e+01
Coefficient B			-5.23596e+03
Coefficient C			-1.03362e+02
Reference			McDonald, Shrader, et al., 1959
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			466.93
Temperature range, max.			514.47
Pvap	8.71	kPa	466.93	Calculated Property
Pvap	10.70	kPa	472.21	Calculated Property
Pvap	13.08	kPa	477.49	Calculated Property
Pvap	15.89	kPa	482.78	Calculated Property
Pvap	19.21	kPa	488.06	Calculated Property
Pvap	23.09	kPa	493.34	Calculated Property
Pvap	27.63	kPa	498.62	Calculated Property
Pvap	32.91	kPa	503.91	Calculated Property
Pvap	39.01	kPa	509.19	Calculated Property
Pvap	46.04	kPa	514.47	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1103.56; 322.19]	kg/m3	[283.15; 736.60]	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			5.52067e+01
Coefficient B			2.09240e-01
Coefficient C			7.36610e+02
Coefficient D			1.83630e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			283.15
Temperature range, max.			736.60
ρl	1103.56	kg/m3	283.15	Calculated Property
ρl	1070.29	kg/m3	333.53	Calculated Property
ρl	1034.60	kg/m3	383.92	Calculated Property
ρl	995.88	kg/m3	434.30	Calculated Property
ρl	953.27	kg/m3	484.68	Calculated Property
ρl	905.36	kg/m3	535.07	Calculated Property
ρl	849.70	kg/m3	585.45	Calculated Property
ρl	781.32	kg/m3	635.83	Calculated Property
ρl	686.25	kg/m3	686.22	Calculated Property
ρl	322.19	kg/m3	736.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.05; 5.02e-06]	N/m	[301.15; 736.60]	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			-1.46398e-01
Coefficient B			4.58626e+01
Coefficient C			-1.69670e+00
Coefficient D			-2.91273e-04
Coefficient E			-1.33437e-07
Comment			ChemSep eq 16, SurfaceTension
Temperature range, min.			301.15
Temperature range, max.			736.60
γ	0.05	N/m	301.15	Calculated Property
γ	0.04	N/m	349.53	Calculated Property
γ	0.03	N/m	397.92	Calculated Property
γ	0.03	N/m	446.30	Calculated Property
γ	0.02	N/m	494.68	Calculated Property
γ	0.02	N/m	543.07	Calculated Property
γ	0.01	N/m	591.45	Calculated Property
γ	0.01	N/m	639.83	Calculated Property
γ	0.00	N/m	688.22	Calculated Property
γ	5.02e-06	N/m	736.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.01; 0.07]	W/m×K	[301.15; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K
Coefficient A			-1.02210e+04
Coefficient B			4.25960e-01
Coefficient C			-2.51720e+09
Coefficient D			-7.99320e+10
Comment			ChemSep eq 102, VaporThermalConductivity
Temperature range, min.			301.15
Temperature range, max.			1000.00
λ	0.01	W/m×K	301.15	Calculated Property
λ	0.02	W/m×K	378.80	Calculated Property
λ	0.02	W/m×K	456.45	Calculated Property
λ	0.03	W/m×K	534.10	Calculated Property
λ	0.04	W/m×K	611.75	Calculated Property
λ	0.04	W/m×K	689.40	Calculated Property
λ	0.05	W/m×K	767.05	Calculated Property
λ	0.06	W/m×K	844.70	Calculated Property
λ	0.07	W/m×K	922.35	Calculated Property
λ	0.07	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.21; 0.10]	W/m×K	[301.15; 673.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λ in W/m×K, T in K
Coefficient A			-9.13280e-01
Coefficient B			1.68240e+01
Coefficient C			-1.59970e-01
Coefficient D			1.15160e-03
Coefficient E			-1.37560e-06
Comment			ChemSep eq 16, LiquidThermalConductivity
Temperature range, min.			301.15
Temperature range, max.			673.15
λ	0.21	W/m×K	301.15	Calculated Property
λ	0.22	W/m×K	342.48	Calculated Property
λ	0.22	W/m×K	383.82	Calculated Property
λ	0.21	W/m×K	425.15	Calculated Property
λ	0.21	W/m×K	466.48	Calculated Property
λ	0.20	W/m×K	507.82	Calculated Property
λ	0.18	W/m×K	549.15	Calculated Property
λ	0.16	W/m×K	590.48	Calculated Property
λ	0.13	W/m×K	631.82	Calculated Property
λ	0.10	W/m×K	673.15	Calculated Property

Similar Compounds

Find more compounds similar to ETHANOL, 2,2'-IMINOBIS-.

Mixtures

• ETHANOL, 2,2'-IMINOBIS- + Water
• ETHANOL, 2,2'-IMINOBIS- + Dimethyl Sulfoxide
• ETHANOL, 2,2'-IMINOBIS- + Methyldiethanolamine
• ETHANOL, 2,2'-IMINOBIS- + Methyldiethanolamine + Water
• ETHANOL, 2,2'-IMINOBIS- + Methyl Alcohol + Water
• Toluene + ETHANOL, 2,2'-IMINOBIS- + Water
• n-Hexane + ETHANOL, 2,2'-IMINOBIS-
• n-Hexane + Choline chloride + ETHANOL, 2,2'-IMINOBIS-
• Benzene + ETHANOL, 2,2'-IMINOBIS-
• Benzene + Choline chloride + ETHANOL, 2,2'-IMINOBIS-
• ETHANOL, 2,2'-IMINOBIS- + Thiophene
• Choline chloride + ETHANOL, 2,2'-IMINOBIS- + Thiophene
• ETHANOL, 2,2'-IMINOBIS- + Methyl Alcohol
• ETHANOL, 2,2'-IMINOBIS- + Ethanol
• ETHANOL, 2,2'-IMINOBIS- + Ethanol + Water
• PHENOL, 4-METHYL- + ETHANOL, 2,2'-IMINOBIS-
• Phenol, 3-methyl- + ETHANOL, 2,2'-IMINOBIS-
• Carbon dioxide + ETHANOL, 2,2'-IMINOBIS- + Water
• ETHANOL, 2,2'-IMINOBIS- + 2-Pyrrolidinone, 1-methyl-
• ETHANOL, 2,2'-IMINOBIS- + Thiophene, tetrahydro-, 1,1-dioxide

Find more mixtures with ETHANOL, 2,2'-IMINOBIS-.

Sources

• KDB Vapor Pressure Data
• 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
• Excess properties of (alkyldiethanolamine + H2O) mixtures at temperatures from (298.15 to 338.15) K
• Enthalpy of solution of carbon dioxide in (water + monoethanolamine, or diethanolamine, or N-methyldiethanolamine) and (water + monoethanolamine + N-methyldiethanolamine) at T = 298.15 K
• Experimental Solubility and Thermodynamic Modeling of Carbon Dioxide in Aqueous Alkanolamine Solutions in the High Gas Loading Region
• CO2 Absorption/Desorption in Mixtures of Methyldiethanolamine with Monoethanolamine or Diethanolamine
• Experimental determination of carbon dioxide solubility data in aqueous alkanolamine solutions
• Experimental determination of hydrogen sulfide solubility data in aqueous alkanolamine solutions
• 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
• Effect of piperazine on solubility of carbon dioxide using aqueous diethanolamnie
• Equilibrium CO2 solubility and thermophysical properties of aqueous blends of 1-(2-aminoethyl) piperazine and N-methyldiethanolamine
• 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
• Solubility of Carbon Dioxide in Aqueous Mixtures of Alkanolamines
• 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
• Measurement and Modeling of Enthalpy of Solution of Carbon Dioxide in Aqueous Solutions of Diethanolamine at Temperatures of (322.5 and 372.9) K and Pressures up to 3 MPa
• 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
• Dielectric Constants of Aqueous Diisopropanolamine, Diethanolamine, N-Methyldiethanolamine, Triethanolamine, and 2-Amino-2-methyl-1-propanol Solutions
• Gas Sweetening Data: Equilibrium Solubility of Hydrogen Sulfide and Carbon Dioxide in Aqueous Monoethanolamine and Aqueous Diethanolamine Solutions
• 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
• Excess Molar Enthalpies of (Water + Alkanolamine) Systems and Some Thermodynamic Calculations
• Heat Capacity of Aqueous Monoethanolamine, Diethanolamine, N-Methyldiethanolamine, and N-Methyldiethanolamine-Based Blends with Carbon Dioxide
• Density and Viscosity of Some Partially Carbonated Aqueous Alkanolamine Solutions and Their Blends
• Analysis of Equilibrium Data of CO2 in Aqueous Solutions of Diethanolamine (DEA), Methyldiethanolamine (MDEA) and Their Mixtures Using the Modified Kent Eisenberg Model
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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