Chemical Properties of Monoethanolamine (CAS 141-43-5)

InChI

InChI=1S/C2H7NO/c3-1-2-4/h4H,1-3H2

InChI Key

HZAXFHJVJLSVMW-UHFFFAOYSA-N

Formula

C2H7NO

SMILES

NCCO

Molecular Weight¹

61.08

CAS

141-43-5

Other Names

• 1-Amino-2-hydroxyethane
• 2-Amino-1-Ethanol
• 2-Aminoaethanol
• 2-Aminoetanolo
• 2-Aminoethan-1-ol
• 2-Aminoethanol
• 2-Aminoethyl alcohol
• 2-Ethanolamine
• 2-Hydroxyethanamine
• 2-Hydroxyethylamine
• Aethanolamin
• Aminoethanol
• Colamine
• Etanolamina
• Ethanol, 2-amino-
• Ethanolamine
• Ethylolamine
• Glycinol
• Kolamin
• MEA
• Monoaethanolamin
• NH2CH2CH2OH
• Olamine
• Thiofaco M-50
• UN 2491
• USAF EK-1597
• «beta»-Aminoethanol
• «beta»-Aminoethyl alcohol
• «beta»-Ethanolamine
• «beta»-Hydroxyethylamine

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid 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°_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).
• IE : Ionization energy (eV).
• 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).
• P_triple : Triple Point 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.
• c_sound,fluid : Speed of sound in fluid (m/s).
• 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.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Datasets
4. Correlations
5. Similar Compounds
6. Mixtures
7. Sources

Physical Properties

Property	Value	Unit	Source
ω	[0.5508; 0.5684]
ω	0.5684		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.5508		ChemSep v8.3 pure component data Compiled value
PAff	930.30	kJ/mol	NIST
Tig	683.15	K	NCMS SOLV-DB
BasG	896.80	kJ/mol	NIST
μ	0.78	debye	ChemSep v8.3 pure component data Compiled value
εr	37.72		NCMS SOLV-DB
Tflash,cc	358.15	K	NCMS SOLV-DB
ΔfG°	-103.30	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-196.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°liquid	-507.50	kJ/mol	NIST
ΔfusH°	10.22	kJ/mol	Joback Calculated Property
ΔvapH°	[49.83; 60.60]	kJ/mol
ΔvapH°	Outlier 49.83	kJ/mol	NCMS SOLV-DB
ΔvapH°	60.60	kJ/mol	NIST
ΔvapH°	59.60 ± 0.30	kJ/mol	NIST
ΔvapH°	59.40	kJ/mol	NIST
ΔvapH°	59.00	kJ/mol	NIST
ΔvapH°	56.10	kJ/mol	NIST
ΔvapH°	54.80	kJ/mol	NIST
ΔvapH°	57.70	kJ/mol	NIST
ΔvapH°	57.40	kJ/mol	NIST
ΔvapH°	57.90	kJ/mol	NIST
IE	[8.90; 9.88]	eV
IE	8.96	eV	NIST
IE	8.90	eV	NIST
IE	8.96	eV	NIST
IE	8.96	eV	NIST
IE	9.88	eV	NIST
IE	9.88	eV	NIST
IE	9.87 ± 0.06	eV	NIST
log10WS	1.30		Relay (1.0) Calculated Property
logPoct/wat	-1.310		NCMS SOLV-DB
McVol	54.890	ml/mol	McGowan Calculated Property
NFPA Fire	2		NCMS SOLV-DB
NFPA Health	2		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	[7573.03; 8030.00]	kPa
Pc	7600.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 11 Compiled value
Pc	7573.03	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	8030.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	8030.00 ± 40.00	kPa	NIST
Ptriple	0.01	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[643.00; 698.00]
Inp	698.00		NIST
Inp	643.00		NIST
Inp	680.00		NIST
Inp	643.00		NIST
Ip	[1402.00; 1470.00]
Ip	1402.00		NIST
Ip	1470.00		NIST
Ip	1450.00		NIST
Ip	1411.00		NIST
Ip	1413.00		NIST
Ip	1427.00		NIST
Ip	1402.00		NIST
Ip	1427.00		NIST
Tboil	[443.20; 444.15]	K
Tboil	444.15	K	ChemSep v8.3 pure component data Compiled value
Tboil	443.95	K	NCMS SOLV-DB
Tboil	Outlier 443.20	K	NIST
Tboil	444.00	K	NIST
Tboil	444.15 ± 1.50	K	NIST
Tboil	443.55	K	NIST
Tboil	444.00 ± 0.50	K	NIST
Tc	[667.12; 675.00]	K
Tc	675.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 11 Compiled value
Tc	667.12	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	671.40	K	ChemSep v8.3 pure component data Compiled value
Tc	671.40 ± 1.50	K	NIST
Tc	670.00 ± 50.00	K	NIST
Tfus	[283.45; 283.70]	K
Tfus	283.45	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	283.65	K	ChemSep v8.3 pure component data Compiled value
Tfus	283.45	K	NCMS SOLV-DB
Tfus	283.45	K	NIST
Tfus	283.46 ± 0.05	K	NIST
Tfus	283.70 ± 0.60	K	NIST
Ttriple	283.65	K	ChemSep v8.3 pure component data Compiled value
UQi	2.98		ChemSep v8.3 pure component data Compiled value
URi	3.04		ChemSep v8.3 pure component data Compiled value
Vc	[0.196; 0.225]	m3/kmol
Vc	0.196	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.225	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2840000		ChemSep v8.3 pure component data Compiled value
Zra	0.27		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[163.70; 182.00]	J/mol×K	[303.15; 353.15]
Cp,liquid	163.70	J/mol×K	303.15	Density, Viscosity, Heat Capacity, Surface Tension, and Solubility of CO2 in Aqueous Solutions of Potassium Serinate
Cp,liquid	168.00	J/mol×K	303.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	169.00	J/mol×K	308.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	169.00	J/mol×K	313.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	167.98	J/mol×K	313.15	Density, Viscosity, Heat Capacity, Surface Tension, and Solubility of CO2 in Aqueous Solutions of Potassium Serinate
Cp,liquid	171.00	J/mol×K	318.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	173.00	J/mol×K	323.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	172.25	J/mol×K	323.15	Density, Viscosity, Heat Capacity, Surface Tension, and Solubility of CO2 in Aqueous Solutions of Potassium Serinate
Cp,liquid	174.00	J/mol×K	328.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	175.00	J/mol×K	333.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	178.00	J/mol×K	338.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	179.00	J/mol×K	343.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	180.00	J/mol×K	348.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	182.00	J/mol×K	353.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
η	[0.0013760; 0.0199000]	Pa×s	[298.15; 393.15]
η	0.0199000	Pa×s	298.15	Density and Viscosity of Monoethanolamine + Water + Carbon Dioxide from (25 to 80) deg C
η	0.0193700	Pa×s	298.15	NCMS SOLV-DB
η	0.0144230	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	0.0095620	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	0.0096100	Pa×s	313.15	Density and Viscosity of Monoethanolamine + Water + Carbon Dioxide from (25 to 80) deg C
η	0.0066650	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	0.0067200	Pa×s	323.15	Density and Viscosity of Monoethanolamine + Water + Carbon Dioxide from (25 to 80) deg C
η	0.0048140	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	0.0035510	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	0.0036900	Pa×s	343.15	Density and Viscosity of Monoethanolamine + Water + Carbon Dioxide from (25 to 80) deg C
η	0.0028500	Pa×s	353.15	Density and Viscosity of Monoethanolamine + Water + Carbon Dioxide from (25 to 80) deg C
η	0.0027640	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	0.0023370	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	0.0019010	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	0.0015880	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	0.0013760	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
εr	31.46		303.15	Dielectric properties and hydrogen bonding interaction behaviour in binary mixtures of glycerol with amides and amines
ΔvapH	[54.70; 61.70]	kJ/mol	[377.00; 411.00]
ΔvapH	61.70	kJ/mol	377.00	NIST
ΔvapH	58.90	kJ/mol	390.50	NIST
ΔvapH	55.90	kJ/mol	396.00	NIST
ΔvapH	54.70	kJ/mol	411.00	NIST
Pvap	[8.48e-03; 97.50]	kPa	[279.00; 442.28]
Pvap	8.48e-03	kPa	279.00	Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap	0.01	kPa	281.10	Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap	0.02	kPa	283.34	Isothermal Vapor-Liquid Equilibria of (Monoethanolamine + Water) and (4-Methylmorpholine + Water) Binary Systems at Several Temperatures
Pvap	0.03	kPa	288.34	Isothermal Vapor-Liquid Equilibria of (Monoethanolamine + Water) and (4-Methylmorpholine + Water) Binary Systems at Several Temperatures
Pvap	0.04	kPa	293.34	Isothermal Vapor-Liquid Equilibria of (Monoethanolamine + Water) and (4-Methylmorpholine + Water) Binary Systems at Several Temperatures
Pvap	0.03	kPa	294.00	Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap	0.04	kPa	297.20	Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap	0.03	kPa	298.15	NCMS SOLV-DB
Pvap	0.06	kPa	298.34	Isothermal Vapor-Liquid Equilibria of (Monoethanolamine + Water) and (4-Methylmorpholine + Water) Binary Systems at Several Temperatures
Pvap	0.05	kPa	300.20	Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap	0.06	kPa	303.20	Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap	0.09	kPa	303.34	Isothermal Vapor-Liquid Equilibria of (Monoethanolamine + Water) and (4-Methylmorpholine + Water) Binary Systems at Several Temperatures
Pvap	0.08	kPa	306.30	Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap	0.13	kPa	308.34	Isothermal Vapor-Liquid Equilibria of (Monoethanolamine + Water) and (4-Methylmorpholine + Water) Binary Systems at Several Temperatures
Pvap	0.11	kPa	309.40	Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap	0.13	kPa	312.40	Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap	0.19	kPa	313.34	Isothermal Vapor-Liquid Equilibria of (Monoethanolamine + Water) and (4-Methylmorpholine + Water) Binary Systems at Several Temperatures
Pvap	0.17	kPa	315.40	Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap	0.27	kPa	318.34	Isothermal Vapor-Liquid Equilibria of (Monoethanolamine + Water) and (4-Methylmorpholine + Water) Binary Systems at Several Temperatures
Pvap	0.20	kPa	318.40	Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap	0.26	kPa	321.40	Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap	0.38	kPa	323.34	Isothermal Vapor-Liquid Equilibria of (Monoethanolamine + Water) and (4-Methylmorpholine + Water) Binary Systems at Several Temperatures
Pvap	0.31	kPa	324.50	Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
Pvap	0.53	kPa	328.34	Isothermal Vapor-Liquid Equilibria of (Monoethanolamine + Water) and (4-Methylmorpholine + Water) Binary Systems at Several Temperatures
Pvap	0.74	kPa	333.34	Isothermal Vapor-Liquid Equilibria of (Monoethanolamine + Water) and (4-Methylmorpholine + Water) Binary Systems at Several Temperatures
Pvap	1.01	kPa	338.34	Isothermal Vapor-Liquid Equilibria of (Monoethanolamine + Water) and (4-Methylmorpholine + Water) Binary Systems at Several Temperatures
Pvap	1.36	kPa	343.34	Isothermal Vapor-Liquid Equilibria of (Monoethanolamine + Water) and (4-Methylmorpholine + Water) Binary Systems at Several Temperatures
Pvap	1.83	kPa	348.34	Isothermal Vapor-Liquid Equilibria of (Monoethanolamine + Water) and (4-Methylmorpholine + Water) Binary Systems at Several Temperatures
Pvap	2.43	kPa	353.34	Isothermal Vapor-Liquid Equilibria of (Monoethanolamine + Water) and (4-Methylmorpholine + Water) Binary Systems at Several Temperatures
Pvap	2.98	kPa	357.46	Ebulliometric Determination of Vapor
Pvap	3.19	kPa	358.34	Isothermal Vapor-Liquid Equilibria of (Monoethanolamine + Water) and (4-Methylmorpholine + Water) Binary Systems at Several Temperatures
Pvap	3.02	kPa	358.60	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	3.98	kPa	362.99	Ebulliometric Determination of Vapor
Pvap	4.11	kPa	363.09	Isothermal Vapor-Liquid Equilibria of (Monoethanolamine + Water) and (4-Methylmorpholine + Water) Binary Systems at Several Temperatures
Pvap	5.48	kPa	369.33	Ebulliometric Determination of Vapor
Pvap	6.40	kPa	373.00	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	6.64	kPa	373.15	Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap	6.17	kPa	373.15	Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap	6.16	kPa	373.15	Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap	6.98	kPa	374.29	Ebulliometric Determination of Vapor
Pvap	8.47	kPa	378.41	Ebulliometric Determination of Vapor
Pvap	10.97	kPa	384.07	Ebulliometric Determination of Vapor
Pvap	11.70	kPa	385.70	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	14.96	kPa	391.14	Ebulliometric Determination of Vapor
Pvap	19.97	kPa	398.01	Ebulliometric Determination of Vapor
Pvap	24.97	kPa	403.43	Ebulliometric Determination of Vapor
Pvap	24.90	kPa	403.60	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	29.97	kPa	408.19	Ebulliometric Determination of Vapor
Pvap	39.98	kPa	415.78	Ebulliometric Determination of Vapor
Pvap	39.95	kPa	415.81	Ebulliometric Determination of Vapor
Pvap	51.10	kPa	422.70	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	51.97	kPa	423.15	Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap	52.71	kPa	423.15	Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap	50.62	kPa	423.15	Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap	54.95	kPa	424.61	Ebulliometric Determination of Vapor
Pvap	64.95	kPa	429.44	Ebulliometric Determination of Vapor
Pvap	69.95	kPa	431.61	Ebulliometric Determination of Vapor
Pvap	71.80	kPa	432.60	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	79.95	kPa	435.61	Ebulliometric Determination of Vapor
Pvap	97.50	kPa	441.90	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	95.30	kPa	442.28	Activity Coefficients and Excess Gibbs Energies for Binary Mixtures of N-Methyl-2-pyrrolidone with Some Substituted Ethanols
n0	[1.43472; 1.45601]		[293.15; 353.15]
n0	1.45250		293.15	Density, Speed of Sound, Viscosity, Refractive Index, and Excess Volume of N-Methyl-2-pyrrolidone + Ethanol (or Water or Ethanolamine) from T = (293.15 to 323.15) K
n0	1.45420		293.15	Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
n0	1.45601		293.15	Densities, Refractive Indices and Excess Properties of Binary Mixtures of 1-Butyl-3-Methylimidazolium Tetraflouroborate with Water and Monoethanolamine
n0	1.45250		298.15	Vapor-Liquid Equilibrium and Excess Gibbs Energies of Hexane + N,N-Dimethyl Formamide, 2-Methylpropan-2-ol + 2-Aminophenol, N,N-Dimethyl Formamide, and 2-Propanol + Diisopropyl Amine at 94.4 kPa
n0	1.45200		298.15	NCMS SOLV-DB
n0	1.45432		298.15	Densities, Refractive Indices and Excess Properties of Binary Mixtures of 1-Butyl-3-Methylimidazolium Tetraflouroborate with Water and Monoethanolamine
n0	1.44880		303.15	Density, Speed of Sound, Viscosity, Refractive Index, and Excess Volume of N-Methyl-2-pyrrolidone + Ethanol (or Water or Ethanolamine) from T = (293.15 to 323.15) K
n0	1.45273		303.15	Densities, Refractive Indices and Excess Properties of Binary Mixtures of 1-Butyl-3-Methylimidazolium Tetraflouroborate with Water and Monoethanolamine
n0	1.44490		313.15	Density, Speed of Sound, Viscosity, Refractive Index, and Excess Volume of N-Methyl-2-pyrrolidone + Ethanol (or Water or Ethanolamine) from T = (293.15 to 323.15) K
n0	1.44913		313.15	Densities, Refractive Indices and Excess Properties of Binary Mixtures of 1-Butyl-3-Methylimidazolium Tetraflouroborate with Water and Monoethanolamine
n0	1.44561		323.15	Densities, Refractive Indices and Excess Properties of Binary Mixtures of 1-Butyl-3-Methylimidazolium Tetraflouroborate with Water and Monoethanolamine
n0	1.44170		323.15	Density, Speed of Sound, Viscosity, Refractive Index, and Excess Volume of N-Methyl-2-pyrrolidone + Ethanol (or Water or Ethanolamine) from T = (293.15 to 323.15) K
n0	1.44213		333.15	Densities, Refractive Indices and Excess Properties of Binary Mixtures of 1-Butyl-3-Methylimidazolium Tetraflouroborate with Water and Monoethanolamine
n0	1.43862		343.15	Densities, Refractive Indices and Excess Properties of Binary Mixtures of 1-Butyl-3-Methylimidazolium Tetraflouroborate with Water and Monoethanolamine
n0	1.43472		353.15	Densities, Refractive Indices and Excess Properties of Binary Mixtures of 1-Butyl-3-Methylimidazolium Tetraflouroborate with Water and Monoethanolamine
ρl	[959.54; 1025.55]	kg/m3	[281.15; 363.15]
ρl	1025.55	kg/m3	281.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	1023.99	kg/m3	283.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	1024.11	kg/m3	283.15	Densities and Excess Properties of Primary Amines in Alcoholic Solutions
ρl	1022.42	kg/m3	285.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	1020.84	kg/m3	287.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	1019.87	kg/m3	288.15	Excess Enthalpy and Excess Volume for Pyridine + Methyldiethanolamine and Pyridine + Ethanolamine Mixtures
ρl	1019.26	kg/m3	289.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	1017.68	kg/m3	291.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	1016.10	kg/m3	293.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	1016.70	kg/m3	293.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	1016.10	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	1016.90	kg/m3	293.15	Volumetric and viscometric properties of binary and ternary mixtures of monoethanolamine, 2-(diethylamino) ethanol and water from (293.15 to 333.15) K
ρl	1017.90	kg/m3	293.15	Experiment and model for the viscosity of carbonated MDEA - MEA aqueous solutions
ρl	1016.47	kg/m3	293.15	Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρl	1016.23	kg/m3	293.15	Densities and Excess Properties of Primary Amines in Alcoholic Solutions
ρl	1016.30	kg/m3	293.15	Volumetric and viscometric properties of ternary solution of (N-methyldiethanolamine + monoethanolamine + ethanol)
ρl	1016.00	kg/m3	293.15	Volumetric, acoustic and transport properties of mixtures containing dimethyl sulfoxide and some amines or alkanolamines: Measurement and correlation
ρl	1015.50	kg/m3	293.15	Volumetric and viscometric properties of binary and ternary mixtures of 1-butyl-3-methylimidazolium tetrafluoroborate, monoethanolamine and water
ρl	1012.10	kg/m3	293.15	Viscosity of aqueous solutions of 2-methoxyethanol, 2-ethoxyethanol, and ethanolamine
ρl	1015.96	kg/m3	293.15	Solubility of CO2 in aqueous mixtures of monoethanolamine and dicyanamide-based ionic liquids
ρl	1016.34	kg/m3	293.16	Volumetric properties of binary mixtures of dimethyl sulfoxide with amines from (293.15 to 363.15) K
ρl	1014.52	kg/m3	295.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	1012.94	kg/m3	297.15	Volumetric Properties of Water + Monoethanolamine + Methanol Mixtures at Atmospheric Pressure from 283.15 to 353.15 K
ρl	1012.94	kg/m3	297.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	1012.38	kg/m3	298.15	Physicochemical Properties of Aqueous Solutions of Sodium l-Prolinate as an Absorbent for CO2 Removal
ρl	1012.00	kg/m3	298.15	Volumetric, acoustic and transport properties of mixtures containing dimethyl sulfoxide and some amines or alkanolamines: Measurement and correlation
ρl	1011.79	kg/m3	298.15	Hydrogen bond interactions in the blends of 1,4-dioxane with some 1, 2- disubstituted ethanes at T = (298.15, 308.15 and 318.15) K
ρl	1012.53	kg/m3	298.15	Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρl	1011.98	kg/m3	298.15	Density, Speed of Sound, and Viscosity of N-Methyl-2-pyrrolidone + Ethanolamine + Water from T = (293.15 to 323.15) K
ρl	1011.98	kg/m3	298.15	Density, Speed of Sound, and Viscosity of Monoethanolamine + Water + N-Ethyl-2-pyrrolidone from T = (293.15 to 323.15) K
ρl	1012.12	kg/m3	298.15	Excess Enthalpy and Excess Volume for Pyridine + Methyldiethanolamine and Pyridine + Ethanolamine Mixtures
ρl	1012.40	kg/m3	298.15	Thermodynamic properties and CO2 solubility of monoethanolamine + diethylenetriamine/aminoethylethanolamine mixtures: Experimental measurements and thermodynamic modeling
ρl	1012.40	kg/m3	298.15	Thermodynamic properties and CO2 solubility of monoethanolamine + diethylenetriamine/aminoethylethanolamine mixtures: Experimental measurements and thermodynamic modeling
ρl	1012.80	kg/m3	298.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	1011.35	kg/m3	299.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	1009.76	kg/m3	301.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	1008.40	kg/m3	303.14	Volumetric properties of binary mixtures of dimethyl sulfoxide with amines from (293.15 to 363.15) K
ρl	1007.60	kg/m3	303.15	Volumetric and viscometric properties of binary and ternary mixtures of 1-butyl-3-methylimidazolium tetrafluoroborate, monoethanolamine and water
ρl	1008.47	kg/m3	303.15	Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρl	1008.40	kg/m3	303.15	Thermodynamic properties and CO2 solubility of monoethanolamine + diethylenetriamine/aminoethylethanolamine mixtures: Experimental measurements and thermodynamic modeling
ρl	1008.00	kg/m3	303.15	Volumetric, acoustic and transport properties of mixtures containing dimethyl sulfoxide and some amines or alkanolamines: Measurement and correlation
ρl	1009.50	kg/m3	303.15	Volumetric and viscometric properties of binary and ternary mixtures of monoethanolamine, 2-(diethylamino) ethanol and water from (293.15 to 333.15) K
ρl	1008.17	kg/m3	303.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	1008.02	kg/m3	303.15	Volumetric and viscometric properties of ternary solution of (N-methyldiethanolamine + monoethanolamine + ethanol)
ρl	1008.80	kg/m3	303.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	1008.05	kg/m3	303.15	Solubility of CO2 in aqueous mixtures of monoethanolamine and dicyanamide-based ionic liquids
ρl	1007.70	kg/m3	303.15	CO2 absorption into aqueous potassium salts of lysine and proline: Density, viscosity and solubility of CO2
ρl	1007.90	kg/m3	303.15	Densities, Viscosities and Excess Properties of Binary Mixtures of 1,1,3,3-Tetramethylguanidinium Lactate + Water at T = (303.15 to 328.15) K
ρl	1009.35	kg/m3	303.15	Physicochemical Properties of Aqueous Solutions of Sodium l-Prolinate as an Absorbent for CO2 Removal
ρl	1008.80	kg/m3	303.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	1008.32	kg/m3	303.15	Densities and Excess Properties of Primary Amines in Alcoholic Solutions
ρl	1008.40	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	1008.40	kg/m3	303.15	Thermodynamic properties and CO2 solubility of monoethanolamine + diethylenetriamine/aminoethylethanolamine mixtures: Experimental measurements and thermodynamic modeling
ρl	1010.67	kg/m3	303.15	Densities and Excess Molar Volumes of Binary Mixtures of Bis(2-hydroxyethyl)ammonium Acetate + Water and Monoethanolamine + Bis(2-hydroxyethyl)ammonium Acetate at Temperatures from (303.15 to 353.15) K
ρl	1008.72	kg/m3	303.15	Volumetric, acoustic and spectroscopic properties of 3-chloroaniline with substituted ethanols at various temperatures
ρl	1006.58	kg/m3	305.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	1004.99	kg/m3	307.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	1004.68	kg/m3	308.15	Hydrogen bond interactions in the blends of 1,4-dioxane with some 1, 2- disubstituted ethanes at T = (298.15, 308.15 and 318.15) K
ρl	1004.90	kg/m3	308.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	1004.50	kg/m3	308.15	Thermodynamic properties and CO2 solubility of monoethanolamine + diethylenetriamine/aminoethylethanolamine mixtures: Experimental measurements and thermodynamic modeling
ρl	1004.49	kg/m3	308.15	Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρl	1004.65	kg/m3	308.15	Volumetric, acoustic and spectroscopic properties of 3-chloroaniline with substituted ethanols at various temperatures
ρl	1006.80	kg/m3	308.15	Liquid-liquid phase equilibrium for ternary mixtures of formamide (or ethylene glycol, or monoethanolamine) + indole + 2-methylnaphthalene at 308.15 K
ρl	1004.50	kg/m3	308.15	Thermodynamic properties and CO2 solubility of monoethanolamine + diethylenetriamine/aminoethylethanolamine mixtures: Experimental measurements and thermodynamic modeling
ρl	1004.20	kg/m3	308.15	Densities, Viscosities and Excess Properties of Binary Mixtures of 1,1,3,3-Tetramethylguanidinium Lactate + Water at T = (303.15 to 328.15) K
ρl	1003.40	kg/m3	309.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	1001.80	kg/m3	311.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	1000.41	kg/m3	313.14	Volumetric properties of binary mixtures of dimethyl sulfoxide with amines from (293.15 to 363.15) K
ρl	1001.10	kg/m3	313.15	Volumetric and viscometric properties of binary and ternary mixtures of monoethanolamine, 2-(diethylamino) ethanol and water from (293.15 to 333.15) K
ρl	1000.74	kg/m3	313.15	Volumetric, acoustic and spectroscopic properties of 3-chloroaniline with substituted ethanols at various temperatures
ρl	1000.37	kg/m3	313.15	Densities and Excess Properties of Primary Amines in Alcoholic Solutions
ρl	999.98	kg/m3	313.15	Volumetric and viscometric properties of ternary solution of (N-methyldiethanolamine + monoethanolamine + ethanol)
ρl	1000.90	kg/m3	313.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	1000.50	kg/m3	313.15	Densities, Viscosities and Excess Properties of Binary Mixtures of 1,1,3,3-Tetramethylguanidinium Lactate + Water at T = (303.15 to 328.15) K
ρl	1000.10	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	1002.77	kg/m3	313.15	Densities and Excess Molar Volumes of Binary Mixtures of Bis(2-hydroxyethyl)ammonium Acetate + Water and Monoethanolamine + Bis(2-hydroxyethyl)ammonium Acetate at Temperatures from (303.15 to 353.15) K
ρl	1000.50	kg/m3	313.15	Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρl	1000.00	kg/m3	313.15	Volumetric, acoustic and transport properties of mixtures containing dimethyl sulfoxide and some amines or alkanolamines: Measurement and correlation
ρl	999.80	kg/m3	313.15	CO2 absorption into aqueous potassium salts of lysine and proline: Density, viscosity and solubility of CO2
ρl	1002.16	kg/m3	313.15	Physicochemical Properties of Aqueous Solutions of Sodium l-Prolinate as an Absorbent for CO2 Removal
ρl	1000.09	kg/m3	313.15	Solubility of CO2 in aqueous mixtures of monoethanolamine and dicyanamide-based ionic liquids
ρl	1000.90	kg/m3	313.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	999.70	kg/m3	313.15	Volumetric and viscometric properties of binary and ternary mixtures of 1-butyl-3-methylimidazolium tetrafluoroborate, monoethanolamine and water
ρl	1000.21	kg/m3	313.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	998.60	kg/m3	315.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	997.00	kg/m3	317.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	996.90	kg/m3	318.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	996.20	kg/m3	318.15	Densities, Viscosities and Excess Properties of Binary Mixtures of 1,1,3,3-Tetramethylguanidinium Lactate + Water at T = (303.15 to 328.15) K
ρl	996.39	kg/m3	318.15	Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρl	996.04	kg/m3	318.15	Volumetric, acoustic and spectroscopic properties of 3-chloroaniline with substituted ethanols at various temperatures
ρl	998.15	kg/m3	318.15	Hydrogen bond interactions in the blends of 1,4-dioxane with some 1, 2- disubstituted ethanes at T = (298.15, 308.15 and 318.15) K
ρl	995.40	kg/m3	319.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	993.79	kg/m3	321.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	992.38	kg/m3	323.15	Volumetric properties of binary mixtures of dimethyl sulfoxide with amines from (293.15 to 363.15) K
ρl	991.90	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	991.70	kg/m3	323.15	CO2 absorption into aqueous potassium salts of lysine and proline: Density, viscosity and solubility of CO2
ρl	992.19	kg/m3	323.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	992.36	kg/m3	323.15	Densities and Excess Properties of Primary Amines in Alcoholic Solutions
ρl	992.00	kg/m3	323.15	Volumetric, acoustic and transport properties of mixtures containing dimethyl sulfoxide and some amines or alkanolamines: Measurement and correlation
ρl	992.90	kg/m3	323.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	994.80	kg/m3	323.15	Densities and Excess Molar Volumes of Binary Mixtures of Bis(2-hydroxyethyl)ammonium Acetate + Water and Monoethanolamine + Bis(2-hydroxyethyl)ammonium Acetate at Temperatures from (303.15 to 353.15) K
ρl	991.97	kg/m3	323.15	Volumetric and viscometric properties of ternary solution of (N-methyldiethanolamine + monoethanolamine + ethanol)
ρl	992.41	kg/m3	323.15	Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρl	992.07	kg/m3	323.15	Solubility of CO2 in aqueous mixtures of monoethanolamine and dicyanamide-based ionic liquids
ρl	992.70	kg/m3	323.15	Densities, Viscosities and Excess Properties of Binary Mixtures of 1,1,3,3-Tetramethylguanidinium Lactate + Water at T = (303.15 to 328.15) K
ρl	992.70	kg/m3	323.15	Volumetric and viscometric properties of binary and ternary mixtures of monoethanolamine, 2-(diethylamino) ethanol and water from (293.15 to 333.15) K
ρl	991.70	kg/m3	323.15	Volumetric and viscometric properties of binary and ternary mixtures of 1-butyl-3-methylimidazolium tetrafluoroborate, monoethanolamine and water
ρl	994.40	kg/m3	323.15	Physicochemical Properties of Aqueous Solutions of Sodium l-Prolinate as an Absorbent for CO2 Removal
ρl	990.58	kg/m3	325.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	988.96	kg/m3	327.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	988.80	kg/m3	328.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	988.70	kg/m3	328.15	Densities, Viscosities and Excess Properties of Binary Mixtures of 1,1,3,3-Tetramethylguanidinium Lactate + Water at T = (303.15 to 328.15) K
ρl	987.34	kg/m3	329.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	985.72	kg/m3	331.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	984.30	kg/m3	333.14	Volumetric properties of binary mixtures of dimethyl sulfoxide with amines from (293.15 to 363.15) K
ρl	983.60	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	984.30	kg/m3	333.15	Densities and Excess Properties of Primary Amines in Alcoholic Solutions
ρl	986.24	kg/m3	333.15	Physicochemical Properties of Aqueous Solutions of Sodium l-Prolinate as an Absorbent for CO2 Removal
ρl	984.30	kg/m3	333.15	Volumetric and viscometric properties of binary and ternary mixtures of monoethanolamine, 2-(diethylamino) ethanol and water from (293.15 to 333.15) K
ρl	984.80	kg/m3	333.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	984.10	kg/m3	333.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	983.98	kg/m3	333.15	Solubility of CO2 in aqueous mixtures of monoethanolamine and dicyanamide-based ionic liquids
ρl	983.70	kg/m3	333.15	CO2 absorption into aqueous potassium salts of lysine and proline: Density, viscosity and solubility of CO2
ρl	983.60	kg/m3	333.15	Volumetric and viscometric properties of binary and ternary mixtures of 1-butyl-3-methylimidazolium tetrafluoroborate, monoethanolamine and water
ρl	986.75	kg/m3	333.15	Densities and Excess Molar Volumes of Binary Mixtures of Bis(2-hydroxyethyl)ammonium Acetate + Water and Monoethanolamine + Bis(2-hydroxyethyl)ammonium Acetate at Temperatures from (303.15 to 353.15) K
ρl	982.48	kg/m3	335.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	980.85	kg/m3	337.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	980.70	kg/m3	338.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	979.21	kg/m3	339.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	977.58	kg/m3	341.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	976.14	kg/m3	343.14	Volumetric properties of binary mixtures of dimethyl sulfoxide with amines from (293.15 to 363.15) K
ρl	975.50	kg/m3	343.15	CO2 absorption into aqueous potassium salts of lysine and proline: Density, viscosity and solubility of CO2
ρl	976.15	kg/m3	343.15	Densities and Excess Properties of Primary Amines in Alcoholic Solutions
ρl	976.60	kg/m3	343.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	975.94	kg/m3	343.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	978.62	kg/m3	343.15	Densities and Excess Molar Volumes of Binary Mixtures of Bis(2-hydroxyethyl)ammonium Acetate + Water and Monoethanolamine + Bis(2-hydroxyethyl)ammonium Acetate at Temperatures from (303.15 to 353.15) K
ρl	974.30	kg/m3	345.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	972.65	kg/m3	347.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	972.50	kg/m3	348.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	970.99	kg/m3	349.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	969.34	kg/m3	351.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	967.89	kg/m3	353.14	Volumetric properties of binary mixtures of dimethyl sulfoxide with amines from (293.15 to 363.15) K
ρl	968.33	kg/m3	353.15	Excess Enthalpy and Excess Volume for Pyridine + Methyldiethanolamine and Pyridine + Ethanolamine Mixtures
ρl	967.68	kg/m3	353.15	Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
ρl	970.40	kg/m3	353.15	Densities and Excess Molar Volumes of Binary Mixtures of Bis(2-hydroxyethyl)ammonium Acetate + Water and Monoethanolamine + Bis(2-hydroxyethyl)ammonium Acetate at Temperatures from (303.15 to 353.15) K
ρl	968.40	kg/m3	353.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	959.54	kg/m3	363.15	Volumetric properties of binary mixtures of dimethyl sulfoxide with amines from (293.15 to 363.15) K
csound,fluid	[1637.20; 1735.46]	m/s	[293.15; 323.15]
csound,fluid	1734.40	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	1735.46	m/s	293.15	Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of (Monoethanolamine + 2-Amino-2-methyl-1-propanol), (Monoethanolamine + Triethanolamine), and (Monoethanolamine + N-Methyldiethanolamine) at Temperatures from (293.15 to 323.15) K
csound,fluid	1719.23	m/s	298.15	Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of (Monoethanolamine + 2-Amino-2-methyl-1-propanol), (Monoethanolamine + Triethanolamine), and (Monoethanolamine + N-Methyldiethanolamine) at Temperatures from (293.15 to 323.15) K
csound,fluid	1702.10	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	1703.09	m/s	303.15	Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of (Monoethanolamine + 2-Amino-2-methyl-1-propanol), (Monoethanolamine + Triethanolamine), and (Monoethanolamine + N-Methyldiethanolamine) at Temperatures from (293.15 to 323.15) K
csound,fluid	1686.79	m/s	308.15	Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of (Monoethanolamine + 2-Amino-2-methyl-1-propanol), (Monoethanolamine + Triethanolamine), and (Monoethanolamine + N-Methyldiethanolamine) at Temperatures from (293.15 to 323.15) K
csound,fluid	1670.10	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	1670.54	m/s	313.15	Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of (Monoethanolamine + 2-Amino-2-methyl-1-propanol), (Monoethanolamine + Triethanolamine), and (Monoethanolamine + N-Methyldiethanolamine) at Temperatures from (293.15 to 323.15) K
csound,fluid	1654.19	m/s	318.15	Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of (Monoethanolamine + 2-Amino-2-methyl-1-propanol), (Monoethanolamine + Triethanolamine), and (Monoethanolamine + N-Methyldiethanolamine) at Temperatures from (293.15 to 323.15) K
csound,fluid	1637.20	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	1637.86	m/s	323.15	Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of (Monoethanolamine + 2-Amino-2-methyl-1-propanol), (Monoethanolamine + Triethanolamine), and (Monoethanolamine + N-Methyldiethanolamine) at Temperatures from (293.15 to 323.15) K
γ	[0.04; 0.05]	N/m	[293.15; 333.15]
γ	0.05	N/m	293.15	Density and Surface Tension Measurements of Partially Carbonated Aqueous Monoethanolamine Solutions
γ	0.05	N/m	293.15	Densities and Surface Tensions of CO2 Loaded Aqueous Monoethanolamine Solutions with r = (0.2 to 0.7) at T = (303.15 to 333.15) K
γ	0.05	N/m	298.15	NCMS SOLV-DB
γ	0.05	N/m	303.15	Densities and Surface Tensions of CO2 Loaded Aqueous Monoethanolamine Solutions with r = (0.2 to 0.7) at T = (303.15 to 333.15) K
γ	0.05	N/m	303.15	Density of Water (1) + Monoethanolamine (2) + CO2 (3) from (298.15 to 413.15) K and Surface Tension of Water (1) + Monoethanolamine (2) from (303.15 to 333.15) K
γ	0.05	N/m	303.15	Density and Surface Tension Measurements of Partially Carbonated Aqueous Monoethanolamine Solutions
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 and Surface Tension Measurements of Partially Carbonated Aqueous Monoethanolamine Solutions
γ	0.05	N/m	313.15	Density of Water (1) + Monoethanolamine (2) + CO2 (3) from (298.15 to 413.15) K and Surface Tension of Water (1) + Monoethanolamine (2) from (303.15 to 333.15) K
γ	0.05	N/m	313.15	Densities and Surface Tensions of CO2 Loaded Aqueous Monoethanolamine Solutions with r = (0.2 to 0.7) at T = (303.15 to 333.15) K
γ	0.05	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 of Water (1) + Monoethanolamine (2) + CO2 (3) from (298.15 to 413.15) K and Surface Tension of Water (1) + Monoethanolamine (2) from (303.15 to 333.15) K
γ	0.04	N/m	323.20	Investigation of surface tension and viscosity for aqueous solutions of MEA-MeOH and DEA-MeOH
γ	0.04	N/m	333.15	Density of Water (1) + Monoethanolamine (2) + CO2 (3) from (298.15 to 413.15) K and Surface Tension of Water (1) + Monoethanolamine (2) from (303.15 to 333.15) K

Datasets

1. Viscosity, Pa*s (1)
2. Mass density, kg/m3 (1)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.15	100.00	0.0187
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	1012.0
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[80.32; 205.90]	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			5.06680e+01
Coefficient B			-5.16860e+02
Coefficient C			5.25924e+00
Coefficient D			8.64100e-05
Coefficient E			2.86560e-10
Temperature range, min.			273.00
Temperature range, max.			1500.00
Cp,gas	80.32	J/mol×K	273.00	Calculated Property
Cp,gas	107.04	J/mol×K	409.33	Calculated Property
Cp,gas	128.87	J/mol×K	545.67	Calculated Property
Cp,gas	146.29	J/mol×K	682.00	Calculated Property
Cp,gas	160.46	J/mol×K	818.33	Calculated Property
Cp,gas	172.25	J/mol×K	954.67	Calculated Property
Cp,gas	182.31	J/mol×K	1091.00	Calculated Property
Cp,gas	191.08	J/mol×K	1227.33	Calculated Property
Cp,gas	198.87	J/mol×K	1363.67	Calculated Property
Cp,gas	205.90	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[164.66; 204.50]	J/mol×K	[293.15; 443.15]	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			7.86534e+01
Coefficient B			3.11416e-01
Coefficient C			-6.07137e-05
Coefficient D			-2.71322e-09
Coefficient E			0.00000e+00
Temperature range, min.			293.15
Temperature range, max.			443.15
Cp,liquid	164.66	J/mol×K	293.15	Calculated Property
Cp,liquid	169.23	J/mol×K	309.82	Calculated Property
Cp,liquid	173.76	J/mol×K	326.48	Calculated Property
Cp,liquid	178.26	J/mol×K	343.15	Calculated Property
Cp,liquid	182.72	J/mol×K	359.82	Calculated Property
Cp,liquid	187.15	J/mol×K	376.48	Calculated Property
Cp,liquid	191.54	J/mol×K	393.15	Calculated Property
Cp,liquid	195.89	J/mol×K	409.82	Calculated Property
Cp,liquid	200.21	J/mol×K	426.48	Calculated Property
Cp,liquid	204.50	J/mol×K	443.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0398170; 0.0001782]	Pa×s	[283.65; 542.56]	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			-3.70300e+02
Coefficient B			1.77800e+04
Coefficient C			5.46240e+01
Coefficient D			-5.10650e-05
Coefficient E			2.00000e+00
Temperature range, min.			283.65
Temperature range, max.			542.56
η	0.0398170	Pa×s	283.65	Calculated Property
η	0.0101091	Pa×s	312.42	Calculated Property
η	0.0039207	Pa×s	341.19	Calculated Property
η	0.0019960	Pa×s	369.95	Calculated Property
η	0.0012031	Pa×s	398.72	Calculated Property
η	0.0007991	Pa×s	427.49	Calculated Property
η	0.0005558	Pa×s	456.26	Calculated Property
η	0.0003900	Pa×s	485.02	Calculated Property
η	0.0002688	Pa×s	513.79	Calculated Property
η	0.0001782	Pa×s	542.56	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[63.57; 28.89]	kJ/mol	[283.65; 595.14]	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			1.01203e+02
Coefficient B			1.97696e+00
Coefficient C			-4.39989e+00
Coefficient D			4.90605e+00
Coefficient E			-1.94589e+00
Critical temperature, Tc (K)			6.71400e+02
Temperature range, min.			283.65
Temperature range, max.			595.14
ΔvapH	63.57	kJ/mol	283.65	Calculated Property
ΔvapH	61.06	kJ/mol	318.26	Calculated Property
ΔvapH	58.41	kJ/mol	352.87	Calculated Property
ΔvapH	55.51	kJ/mol	387.48	Calculated Property
ΔvapH	52.30	kJ/mol	422.09	Calculated Property
ΔvapH	48.69	kJ/mol	456.70	Calculated Property
ΔvapH	44.65	kJ/mol	491.31	Calculated Property
ΔvapH	40.09	kJ/mol	525.92	Calculated Property
ΔvapH	34.92	kJ/mol	560.53	Calculated Property
ΔvapH	28.89	kJ/mol	595.14	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[0.02; 8127.13]	kPa	[283.65; 671.40]	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			1.61850e+01
Coefficient B			-4.31962e+03
Coefficient C			-6.99502e+01
Comment			Range stopped at Tc; ChemSep gives it to 678.2 K.
Temperature range, min.			283.65
Temperature range, max.			671.40
Pvap	0.02	kPa	283.65	Calculated Property
Pvap	0.53	kPa	326.73	Calculated Property
Pvap	5.93	kPa	369.82	Calculated Property
Pvap	36.22	kPa	412.90	Calculated Property
Pvap	147.70	kPa	455.98	Calculated Property
Pvap	454.26	kPa	499.07	Calculated Property
Pvap	1138.09	kPa	542.15	Calculated Property
Pvap	2445.42	kPa	585.23	Calculated Property
Pvap	4669.47	kPa	628.32	Calculated Property
Pvap	8127.13	kPa	671.40	Calculated Property
Pvap	[0.01; 6609.81]	kPa	[283.65; 638.00]	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			1.62291e+02
Coefficient B			-1.33605e+04
Coefficient C			-2.13543e+01
Coefficient D			1.31668e-05
Coefficient E			0.00000e+00
Temperature range, min.			283.65
Temperature range, max.			638.00
Pvap	0.01	kPa	283.65	Calculated Property
Pvap	0.34	kPa	323.02	Calculated Property
Pvap	3.74	kPa	362.39	Calculated Property
Pvap	22.75	kPa	401.77	Calculated Property
Pvap	93.06	kPa	441.14	Calculated Property
Pvap	289.19	kPa	480.51	Calculated Property
Pvap	742.24	kPa	519.88	Calculated Property
Pvap	1668.11	kPa	559.26	Calculated Property
Pvap	3422.56	kPa	598.63	Calculated Property
Pvap	6609.81	kPa	638.00	Calculated Property
Pvap	[0.91; 99.37]	kPa	[338.60; 444.10]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.44891e+01
Coefficient B			-3.24405e+03
Coefficient C			-1.16093e+02
Reference			Matthews, Sumner, et al., 1950, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			338.60
Temperature range, max.			444.10
Pvap	0.91	kPa	338.60	Calculated Property
Pvap	1.89	kPa	350.32	Calculated Property
Pvap	3.67	kPa	362.04	Calculated Property
Pvap	6.68	kPa	373.77	Calculated Property
Pvap	11.56	kPa	385.49	Calculated Property
Pvap	19.09	kPa	397.21	Calculated Property
Pvap	30.30	kPa	408.93	Calculated Property
Pvap	46.41	kPa	420.66	Calculated Property
Pvap	68.88	kPa	432.38	Calculated Property
Pvap	99.37	kPa	444.10	Calculated Property
Pvap	[0.91; 99.37]	kPa	[338.60; 444.10]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.44891e+01
Coefficient B			-3.24405e+03
Coefficient C			-1.16093e+02
Reference			Matthews, Sumner, et al., 1950
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			338.60
Temperature range, max.			444.10
Pvap	0.91	kPa	338.60	Calculated Property
Pvap	1.89	kPa	350.32	Calculated Property
Pvap	3.67	kPa	362.04	Calculated Property
Pvap	6.68	kPa	373.77	Calculated Property
Pvap	11.56	kPa	385.49	Calculated Property
Pvap	19.09	kPa	397.21	Calculated Property
Pvap	30.30	kPa	408.93	Calculated Property
Pvap	46.41	kPa	420.66	Calculated Property
Pvap	68.88	kPa	432.38	Calculated Property
Pvap	99.37	kPa	444.10	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1022.66; 459.23]	kg/m3	[283.15; 671.40]	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			3.95818e+01
Coefficient B			1.81830e-01
Coefficient C			6.78210e+02
Coefficient D			1.79470e-01
Comment			Range stopped at Tc; ChemSep gives it to 678.2 K.
Temperature range, min.			283.15
Temperature range, max.			671.40
ρl	1022.66	kg/m3	283.15	Calculated Property
ρl	990.68	kg/m3	326.29	Calculated Property
ρl	956.46	kg/m3	369.43	Calculated Property
ρl	919.47	kg/m3	412.57	Calculated Property
ρl	878.93	kg/m3	455.71	Calculated Property
ρl	833.60	kg/m3	498.84	Calculated Property
ρl	781.38	kg/m3	541.98	Calculated Property
ρl	718.13	kg/m3	585.12	Calculated Property
ρl	633.00	kg/m3	628.26	Calculated Property
ρl	459.23	kg/m3	671.40	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.05; 0.03]	N/m	[283.45; 444.15]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			8.16209e-02
Coefficient B			-1.11700e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			283.45
Temperature range, max.			444.15
γ	0.05	N/m	283.45	Calculated Property
γ	0.05	N/m	301.31	Calculated Property
γ	0.05	N/m	319.16	Calculated Property
γ	0.04	N/m	337.02	Calculated Property
γ	0.04	N/m	354.87	Calculated Property
γ	0.04	N/m	372.73	Calculated Property
γ	0.04	N/m	390.58	Calculated Property
γ	0.04	N/m	408.44	Calculated Property
γ	0.03	N/m	426.29	Calculated Property
γ	0.03	N/m	444.15	Calculated Property
γ	[0.05; 0.01]	N/m	[270.00; 600.00]	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			-6.71390e-02
Coefficient B			-7.90000e+00
Coefficient C			-1.90607e+00
Coefficient D			-4.71900e-04
Coefficient E			-9.53300e-07
Temperature range, min.			270.00
Temperature range, max.			600.00
γ	0.05	N/m	270.00	Calculated Property
γ	0.05	N/m	306.67	Calculated Property
γ	0.04	N/m	343.33	Calculated Property
γ	0.04	N/m	380.00	Calculated Property
γ	0.03	N/m	416.67	Calculated Property
γ	0.03	N/m	453.33	Calculated Property
γ	0.03	N/m	490.00	Calculated Property
γ	0.02	N/m	526.67	Calculated Property
γ	0.02	N/m	563.33	Calculated Property
γ	0.01	N/m	600.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.08]	W/m×K	[283.65; 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			-9.53990e+03
Coefficient B			3.98520e-01
Coefficient C			-1.74330e+09
Coefficient D			-6.37150e+10
Temperature range, min.			283.65
Temperature range, max.			1000.00
λgas	0.01	W/m×K	283.65	Calculated Property
λgas	0.02	W/m×K	363.24	Calculated Property
λgas	0.03	W/m×K	442.84	Calculated Property
λgas	0.03	W/m×K	522.43	Calculated Property
λgas	0.04	W/m×K	602.03	Calculated Property
λgas	0.05	W/m×K	681.62	Calculated Property
λgas	0.06	W/m×K	761.22	Calculated Property
λgas	0.06	W/m×K	840.81	Calculated Property
λgas	0.07	W/m×K	920.41	Calculated Property
λgas	0.08	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.24; 0.12]	W/m×K	[283.65; 583.15]	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			-3.72180e-01
Coefficient B			7.88000e+01
Coefficient C			-1.59160e+00
Coefficient D			4.38950e-03
Coefficient E			-5.32910e-06
Temperature range, min.			283.65
Temperature range, max.			583.15
λliquid	0.24	W/m×K	283.65	Calculated Property
λliquid	0.24	W/m×K	316.93	Calculated Property
λliquid	0.24	W/m×K	350.21	Calculated Property
λliquid	0.24	W/m×K	383.48	Calculated Property
λliquid	0.24	W/m×K	416.76	Calculated Property
λliquid	0.22	W/m×K	450.04	Calculated Property
λliquid	0.20	W/m×K	483.32	Calculated Property
λliquid	0.18	W/m×K	516.59	Calculated Property
λliquid	0.15	W/m×K	549.87	Calculated Property
λliquid	0.12	W/m×K	583.15	Calculated Property

Similar Compounds

Find more compounds similar to Monoethanolamine.

Mixtures

• Monoethanolamine + Water
• Monoethanolamine + Carbon dioxide + Water
• Monoethanolamine + Dimethyl Sulfoxide
• Monoethanolamine + Glycerin
• Monoethanolamine + Methyl Alcohol
• Monoethanolamine + Methyl Alcohol + Water
• Monoethanolamine + Choline chloride
• Monoethanolamine + Tetra-N-butylammonium bromide
• Monoethanolamine + METHYLTRIPHENYLPHOSPHONIUM BROMIDE
• Monoethanolamine + Ethanol
• Monoethanolamine + Methyldiethanolamine
• Monoethanolamine + Ethanol + Methyldiethanolamine
• Monoethanolamine + m-Chloroaniline
• Monoethanolamine + Methyldiethanolamine + Water
• Monoethanolamine + 1,4-Dioxane
• Toluene + Monoethanolamine + Water
• Nitrous oxide + Monoethanolamine + Ethanol, 2-methoxy-
• Monoethanolamine + Ethanol, 2-methoxy-
• Monoethanolamine + Ethanol, 2-ethoxy-
• Nitrous oxide + Monoethanolamine + Ethanol, 2-ethoxy-

Find more mixtures with Monoethanolamine.

Sources

• KDB Vapor Pressure Data
• 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.
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• 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
• Enthalpy of solution of carbon dioxide in (water + monoethanolamine, or diethanolamine, or N-methyldiethanolamine) and (water + monoethanolamine + N-methyldiethanolamine) at T = 298.15 K
• Vapor Liquid Equilibrium for Binary Mixtures of 1,4-Diazabicyclo[2.2.2]octane with Ethylenediamine, Ethanolamine, and Ethylene Glycol
• Studies on Hydrogen-Bond Interactions in Ternary Mixtures of Polar Solvents by Dielectric Constant Measurements
• Experimental Solubility and Thermodynamic Modeling of Carbon Dioxide in Aqueous Alkanolamine Solutions in the High Gas Loading Region
• Dielectric properties and hydrogen bonding interaction behaviour in binary mixtures of glycerol with amides and amines
• Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
• High pressure solubility of carbon dioxide (CO2) in aqueous piperazine solutions
• Static permittivity and molecular interactions in binary mixtures of ethanolamine with alcohols and amides
• Experiment and model for the viscosity of carbonated MDEA - MEA aqueous solutions
• Experiment and model for the surface tension of carbonated MEA-MDEA aqueous solutions
• Solubility of CO2 in aqueous mixtures of monoethanolamine and dicyanamide-based ionic liquids
• Comparative study: Absorption enthalpy of carbon dioxide into aqueous diisopropanolamine and monoethanolamine solutions and densities of the carbonated amine solutions
• Equilibrium solubility of carbon dioxide in aqueous solutions of 3-amino-1-propanol, 4-amino-1-butanol and 5-amino-1-pentanol at low partial pressures
• CO2 solubility measurement and thermodynamic modeling for 1-methylpiperazine/water/CO2
• Liquid-liquid phase equilibrium for ternary mixtures of formamide (or ethylene glycol, or monoethanolamine) + indole + 2-methylnaphthalene at 308.15 K
• CO2 absorption into aqueous potassium salts of lysine and proline: Density, viscosity and solubility of CO2
• Vapor-liquid equilibrium measurement and ENRTL Modeling of CO2 absorption in aqueous hexamethylenediamine
• Hydrogen bond interactions in the blends of 1,4-dioxane with some 1, 2- disubstituted ethanes at T = (298.15, 308.15 and 318.15) K
• Monoethanolamine-based deep eutectic solvents, their synthesis and characterization
• Thermodynamic properties and CO2 solubility of monoethanolamine + diethylenetriamine/aminoethylethanolamine mixtures: Experimental measurements and thermodynamic modeling
• Effective extraction of benzene and thiophene by novel deep eutectic solvents from hexane / aromatic mixture at different temperatures
• Viscosity of aqueous solutions of 2-methoxyethanol, 2-ethoxyethanol, and ethanolamine
• Solubility data for toluene in various aqueous alkanolamine solutions
• Volumetric properties of binary mixtures of dimethyl sulfoxide with amines from (293.15 to 363.15) K
• Equilibrium solubility of carbon dioxide in aqueous solutions of (diethylenetriamine + piperazine)
• 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
• Carbon dioxide solubility in aqueous potassium salt solutions of L-proline and DL-.alpha.-aminobutyric acid at high pressures
• Volumetric, acoustic and spectroscopic properties of 3-chloroaniline with substituted ethanols at various temperatures
• Solubility and viscosity for CO2 capture process using MEA promoted DEAE aqueous solution
• Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
• Sync-measurement experimental study of (fluoroethane + dimethylether tetraethylene glycol), (fluoroethane + dimethylether triethylene glycol) and (fluoroethane + dimethylether diethylene glycol) systems
• Viscosity and density measurements of aqueous amines at high pressures: MDEA-water and MEA-water mixtures for CO2 capture
• Volumetric and viscometric properties of binary and ternary mixtures of 1-butyl-3-methylimidazolium tetrafluoroborate, monoethanolamine and water
• Experiments and model for the surface tension of DEAE-PZ and DEAE-MEA aqueous solutions
• Experimental solubility of diosgenin and estriol in various solvents between T = (293.2-328.2) K
• Surface thermodynamics of DMA2P, DMA2P-MEA and DMA2P-PZ aqueous solutions
• CO2 solubility in aqueous potassium lysinate solutions at absorber conditions
• Absorption performance of (CO2 + N2) gas mixtures in amino acid ionic liquids promoted N-methyldiethanolamine aqueous solutions
• Measurement of CO2 absorption enthalpy and heat capacity of aqueous hexamethylenediamine and its aqueous mixture with N-methyldiethanolamine
• CO2 absorption using aqueous potassium lysinate solutions: Vapor - liquid equilibrium data and modelling
• Investigation of surface tension and viscosity for aqueous solutions of MEA-MeOH and DEA-MeOH
• Volumetric, acoustic and transport properties of mixtures containing dimethyl sulfoxide and some amines or alkanolamines: Measurement and correlation
• Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
• Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
• Volumetric and viscometric properties of ternary solution of (N-methyldiethanolamine + monoethanolamine + ethanol)
• Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
• Vapour-liquid equilibrium study of tertiary amines, single and in blend with 3-(methylamino)propylamine, for post-combustion CO2 capture
• Volumetric and viscometric properties of binary and ternary mixtures of monoethanolamine, 2-(diethylamino) ethanol and water from (293.15 to 333.15) K
• Experimental investigation on CO2 absorption capacity and viscosity for high concentrated 1-dimethylamino-2-propanol-monoethanolamine aqueous blends
• Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
• Low-temperature thermal properties of the aqueous solutions of simple aminoalcohols: Finding of peculiarities in 1-amino-2-propanol solutions
• Carbon dioxide loading capacity in aqueous solution of Potassium salt of Proline blended with Piperazine as new absorbents
• CO2 Solubility in Hybrid Solvents Containing 1-Butyl-3- methylimidazolium tetrafluoroborate and Mixtures of Alkanolamines
• Density and Viscosity of Partially Carbonated Aqueous Tertiary Alkanolamine Solutions at Temperatures between (298.15 and 353.15) K
• Density, Speed of Sound, Viscosity, and Surface Tension of Dimethylethylenediamine + Water and (Ethanolamine + Dimethylethanolamine) + Water from T = (293.15 to 323.15) K
• Effect of the Presence of MEA on the CO2 Capture Ability of Superbase Ionic Liquids
• Specific Heat Capacities of Two Functional Ionic Liquids and Two Functional Deep Eutectic Solvents for the Absorption of SO2
• Characteristics of Potassium Prolinate + Water + Ethanol Solution as a Phase Changing Absorbent for CO2 Capture
• Density, Viscosity, Refractive Index, and Electrical Conductivity of Degraded Monoethanolamine Solutions at Standard Temperatures
• Density, Viscosity, and N2O Solubility of Aqueous Solutions of MEA, BmimBF4, and Their Mixtures from 293.15 to 333.15 K
• Investigation of Thermodynamic Properties on CO2 Absorbents Blended with Ammonia, Amino Acids, and Corrosion Inhibitors at 313.15, 333.15, and 353.15 K
• Viscosity, Density, and Volatility of Binary Mixtures of Imidazole, 2-Methylimidazole, 2,4,5-Trimethylimidazole, and 1,2,4,5-Tetramethylimidazole with Water
• Liquid-Liquid Equilibrium Measurements and Correlation for Ternary Systems (Butyl Acetate + 1-Butanol + Ethylene Glycol/1,3-Propanediol/Ethanolamine) at 298.15 K
• Liquid-Liquid Equilibria for Benzene/Thiophene + Cyclohexane/Hexadecane + Deep Eutectic Solvents: Data and Correlation
• Vapor-Liquid Equilibrium of Carbon Dioxide in Aqueous Mixtures of Monoethanolamine and Methyldiethanolamine
• Model of Vapor-Liquid Equilibria for Aqueous Acid Gas-Alkanolamine Systems. 2. Representation of H2S and CO2 Solubility in Aqueous MDEA and CO2 Solubility in Aqueous Mixtures of MDEA with MEA or DEA
• Heat of Absorption of Carbon Dioxide (CO2) in Monoethanolamine (MEA) and 2-(Aminoethyl)ethanolamine (AEEA) Solutions
• Solubility of Carbon Dioxide in Aqueous Mixtures of Alkanolamines
• 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
• Volumetric Properties of Water + Monoethanolamine + Methanol Mixtures at Atmospheric Pressure from 283.15 to 353.15 K
• Vapor Pressures and Vaporization Enthalpies of a Series of Ethanolamines
• 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
• Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
• Density, Viscosity, and Performances of Carbon Dioxide Capture in 16 Absorbents of Amine + Ionic Liquid + H2O, Ionic Liquid + H2O, and Amine + H2O Systems
• Densities and Excess Molar Volumes of Binary Mixtures of Bis(2-hydroxyethyl)ammonium Acetate + Water and Monoethanolamine + Bis(2-hydroxyethyl)ammonium Acetate at Temperatures from (303.15 to 353.15) K
• Density, Speed of Sound, Viscosity, Refractive Index, and Excess Volume of N-Methyl-2-pyrrolidone + Ethanol (or Water or Ethanolamine) from T = (293.15 to 323.15) K
• Freezing Point Depressions of Aqueous MEA, MDEA, and MEA-MDEA Measured with a New Apparatus
• Density, Viscosity, Heat Capacity, Surface Tension, and Solubility of CO2 in Aqueous Solutions of Potassium Serinate
• CO2 Absorption Rate into Concentrated Aqueous Monoethanolamine and Piperazine
• Vapor Pressures of Several Commercially Used Alkanolamines
• Enthalpy of Solution of Carbon Dioxide in Aqueous Solutions of Monoethanolamine at Temperatures of 322.5 K and 372.9 K and Pressures up to 5 MPa
• Densities, Refractive Indices and Excess Properties of Binary Mixtures of 1-Butyl-3-Methylimidazolium Tetraflouroborate with Water and Monoethanolamine
• Density of Water (1) + Monoethanolamine (2) + CO2 (3) from (298.15 to 413.15) K and Surface Tension of Water (1) + Monoethanolamine (2) from (303.15 to 333.15) K
• Activity Coefficients and Excess Gibbs Energies for Binary Mixtures of N-Methyl-2-pyrrolidone with Some Substituted Ethanols
• Density, Speed of Sound, and Viscosity of N-Methyl-2-pyrrolidone + Ethanolamine + Water from T = (293.15 to 323.15) K
• Densities, Viscosities and Excess Properties of Binary Mixtures of 1,1,3,3-Tetramethylguanidinium Lactate + Water at T = (303.15 to 328.15) K
• Density and Surface Tension Measurements of Partially Carbonated Aqueous Monoethanolamine Solutions
• Solubility of Carbon Dioxide in Aqueous Solutions of Monoethanolamine in the Low and High Gas Loading Regions
• Oxygen Solubility Measurements in a MEA/H2O/CO2 Mixture
• 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
• Densities and Surface Tensions of CO2 Loaded Aqueous Monoethanolamine Solutions with r = (0.2 to 0.7) at T = (303.15 to 333.15) K
• Densities and Excess Properties of Primary Amines in Alcoholic Solutions
• Solubility of N2O in Density and Viscosity of Aqueous Solutions of 1,4-Butanediamine, 2-(Diethylamino)-ethanol, and Their Mixtures from (298.15 to 333.15) K
• Density and Viscosity for Binary Mixtures of Diethylene Glycol Monobutyl Ether with Monoethanolamine, Diethanolamine, and Triethanolamine from (293.15 to 333.15) K
• Excess Enthalpy and Excess Volume for Pyridine + Methyldiethanolamine and Pyridine + Ethanolamine Mixtures
• Density, Speed of Sound, and Viscosity of Monoethanolamine + Water + N-Ethyl-2-pyrrolidone from T = (293.15 to 323.15) K
• Physicochemical Properties of Aqueous Solutions of Sodium l-Prolinate as an Absorbent for CO2 Removal
• Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
• Equilibrium Total Pressure and CO2 Solubility in Binary and Ternary Aqueous Solutions of 2-(Diethylamino)ethanol (DEEA) and 3-(Methylamino)propylamine (MAPA)
• Physical Properties of Partially CO2 Loaded Aqueous Monoethanolamine (MEA)
• Bubble Point Determination for CO2 + Ethanol + Alkanolamines (Monoethanolamine, Diethanolamine, or Triethanolamine) at High Pressures
• Gas Sweetening Data: Equilibrium Solubility of Hydrogen Sulfide and Carbon Dioxide in Aqueous Monoethanolamine and Aqueous Diethanolamine Solutions
• Vapor-Liquid Equilibrium and Excess Gibbs Energies of Hexane + N,N-Dimethyl Formamide, 2-Methylpropan-2-ol + 2-Aminophenol, N,N-Dimethyl Formamide, and 2-Propanol + Diisopropyl Amine at 94.4 kPa
• Ebulliometric Determination of Vapor
• Isothermal Vapor-Liquid Equilibria of (Monoethanolamine + Water) and (4-Methylmorpholine + Water) Binary Systems at Several Temperatures
• Density and Viscosity of Monoethanolamine + Water + Carbon Dioxide from (25 to 80) deg C
• Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of (Monoethanolamine + 2-Amino-2-methyl-1-propanol), (Monoethanolamine + Triethanolamine), and (Monoethanolamine + N-Methyldiethanolamine) at Temperatures from (293.15 to 323.15) K
• 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
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB

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