Chemical Properties of Triethylene glycol (CAS 112-27-6)

InChI

InChI=1S/C6H14O4/c7-1-3-9-5-6-10-4-2-8/h7-8H,1-6H2

InChI Key

ZIBGPFATKBEMQZ-UHFFFAOYSA-N

Formula

C6H14O4

SMILES

OCCOCCOCCO

Molecular Weight¹

150.17

CAS

112-27-6

Other Names

• 1,2-bis(2-hydroxyethoxy)ethane
• 1,2-di(.beta.-hydroxyethoxy)ethane
• 2,2'-(1,2-Ethanediylbis(oxy))bisethanol
• 2,2'-(ethane-1,2-diylbis(oxy))bis(ethan-1-ol)
• 2,2'-(ethylenedioxy)diethanol
• 2,2'-Ethylenedioxybis(ethanol)
• 2,2'-Ethylenedioxyethanol
• 2,2'-ethylenedioxydiethanol
• 2-(2-(2-hydroxyethoxy)ethoxy)ethanol
• 3,6-dioxa-1,8-octanediol
• 3,6-dioxaoctane-1,8-diol
• Di-«beta»-hydroxyethoxyethane
• Ethanol, 2,2'-(ethylenedioxy)di-
• Ethanol, 2,2'-[1,2-ethanediylbis(oxy)]bis-
• Ethylene glycol dihydroxydiethyl ether
• Ethylene glycol-bis-(2-hydroxyethyl ether)
• NSC 60758
• TEG
• Triethylenglykol
• Trigen
• Trigenos
• Trigol
• ethylene glycol bis(2-hydroxyethyl) ether
• glycol bis(hydroxyethyl) ether
• triglycol

• ω : Acentric Factor.
• T_ig : Autoignition Temperature (K).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• 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).
• μ_JT : Joule-Thomson coefficient (K/kPa).
• 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_np : Non-polar retention indices.
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (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.

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	0.7560		ChemSep v8.3 pure component data
Tig	644.15	K	NCMS SOLV-DB
ΔcH°liquid	-3557.60 ± 3.60	kJ/mol	NIST
μ	2.99	debye	ChemSep v8.3 pure component data
εr	23.69		NCMS SOLV-DB
Tflash,cc	439.15	K	NCMS SOLV-DB
ΔfG°	-486.00	kJ/mol	ChemSep v8.3 pure component data
ΔfH°gas	-725.10	kJ/mol	ChemSep v8.3 pure component data
ΔfH°liquid	-804.20 ± 3.60	kJ/mol	NIST
ΔfusH°	21.85	kJ/mol	Joback Calculated Property
ΔvapH°	[60.50; 71.55]	kJ/mol
ΔvapH°	71.55	kJ/mol	NCMS SOLV-DB
ΔvapH°	60.50	kJ/mol	NIST
IE	9.85	eV	Relay (1.0) Calculated Property
log10WS	0.57		Relay (1.0) Calculated Property
logPoct/wat	-1.750		NCMS SOLV-DB
McVol	118.880	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	[3300.00; 3320.00]	kPa
Pc	3320.00	kPa	ChemSep v8.3 pure component data
Pc	3300.00 ± 60.00	kPa	NIST
pKa	14.50		NCMS SOLV-DB
Ptriple	3.27e-07	kPa	ChemSep v8.3 pure component data
Inp	[206.80; 1177.00]
Inp	1143.00		NIST
Inp	1177.00		NIST
Inp	206.80		NIST
Inp	206.80		NIST
Tboil	[439.00; 571.60]	K
Tboil	561.50	K	ChemSep v8.3 pure component data
Tboil	560.55	K	NCMS SOLV-DB
Tboil	558.20	K	NIST
Tboil	551.50	K	NIST
Tboil	549.00 ± 2.00	K	NIST
Tboil	Outlier 439.00 ± 5.00	K	NIST
Tboil	571.60 ± 1.00	K	NIST
Tboil	561.15	K	NIST
Tboil	549.00 ± 3.00	K	NIST
Tc	[713.00; 797.00]	K
Tc	788.00	K	Critical temperatures and pressures of ethylene glycols
Tc	769.50	K	ChemSep v8.3 pure component data
Tc	797.00 ± 10.00	K	NIST
Tc	713.00 ± 20.00	K	NIST
Tc	713.00 ± 20.00	K	NIST
Tfus	[263.75; 268.85]	K
Tfus	265.95	K	ChemSep v8.3 pure component data
Tfus	265.95	K	NCMS SOLV-DB
Tfus	268.85	K	NIST
Tfus	263.75 ± 0.50	K	NIST
Ttriple	[262.70; 265.95]	K
Ttriple	262.70	K	Heat Capacity and Phase Behavior of Selected Oligo(ethylene glycol)s
Ttriple	265.95	K	ChemSep v8.3 pure component data
UQi	6.12		ChemSep v8.3 pure component data
URi	6.53		ChemSep v8.3 pure component data
Vc	0.443	m3/kmol	ChemSep v8.3 pure component data
Zc	0.2300000		ChemSep v8.3 pure component data
Zra	0.24		ChemSep v8.3 pure component data

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[327.60; 359.30]	J/mol×K	[298.00; 353.15]
Cp,liquid	333.70	J/mol×K	298.00	NIST
Cp,liquid	327.60	J/mol×K	298.00	NIST
Cp,liquid	336.30	J/mol×K	303.15	Heat capacities of the mixed-solvents desiccants (glycols +water + salts)
Cp,liquid	339.50	J/mol×K	313.15	Heat capacities of the mixed-solvents desiccants (glycols +water + salts)
Cp,liquid	343.10	J/mol×K	323.15	Heat capacities of the mixed-solvents desiccants (glycols +water + salts)
Cp,liquid	347.90	J/mol×K	333.15	Heat capacities of the mixed-solvents desiccants (glycols +water + salts)
Cp,liquid	353.70	J/mol×K	343.15	Heat capacities of the mixed-solvents desiccants (glycols +water + salts)
Cp,liquid	359.30	J/mol×K	353.15	Heat capacities of the mixed-solvents desiccants (glycols +water + salts)
η	[0.0009970; 0.0490000]	Pa×s	[293.20; 462.25]
η	0.0483200	Pa×s	293.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0300120	Pa×s	298.15	Thermophysical Properties For Diethylene Glycol + Nitrobenzene and Triethylene Glycol + (Chloro-, Bromo-, Nitro-) Benzene Systems at Different Temperatures
η	0.0490000	Pa×s	298.15	NCMS SOLV-DB
η	0.0343980	Pa×s	298.15	Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for Alkyl (Methyl, Ethyl, Butyl, and Isoamyl) Acetates + Glycols at Different Temperatures
η	0.0368200	Pa×s	298.15	Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 473 K and at atmospheric pressure
η	0.0371600	Pa×s	298.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0351000	Pa×s	299.65	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0292700	Pa×s	303.15	Vapour pressures, densities, and viscosities of the aqueous solutions containing (triethylene glycol or propylene glycol) and (LiCl or LiBr)
η	0.0292700	Pa×s	303.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0169720	Pa×s	308.15	Thermophysical Properties For Diethylene Glycol + Nitrobenzene and Triethylene Glycol + (Chloro-, Bromo-, Nitro-) Benzene Systems at Different Temperatures
η	0.0213060	Pa×s	308.15	Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for Alkyl (Methyl, Ethyl, Butyl, and Isoamyl) Acetates + Glycols at Different Temperatures
η	0.0237400	Pa×s	308.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0190300	Pa×s	312.96	Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 473 K and at atmospheric pressure
η	0.0195000	Pa×s	313.05	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0189600	Pa×s	313.15	Vapour pressures, densities, and viscosities of the aqueous solutions containing (triethylene glycol or propylene glycol) and (LiCl or LiBr)
η	0.0192600	Pa×s	313.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0164100	Pa×s	318.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0129600	Pa×s	323.15	Vapour pressures, densities, and viscosities of the aqueous solutions containing (triethylene glycol or propylene glycol) and (LiCl or LiBr)
η	0.0135100	Pa×s	323.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0113500	Pa×s	328.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0096600	Pa×s	333.10	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0092880	Pa×s	333.15	Vapour pressures, densities, and viscosities of the aqueous solutions containing (triethylene glycol or propylene glycol) and (LiCl or LiBr)
η	0.0096020	Pa×s	333.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0090020	Pa×s	334.96	Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 473 K and at atmospheric pressure
η	0.0082780	Pa×s	338.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0069060	Pa×s	343.15	Vapour pressures, densities, and viscosities of the aqueous solutions containing (triethylene glycol or propylene glycol) and (LiCl or LiBr)
η	0.0073510	Pa×s	343.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0059450	Pa×s	349.25	Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 473 K and at atmospheric pressure
η	0.0055500	Pa×s	353.05	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0041310	Pa×s	364.44	Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 473 K and at atmospheric pressure
η	0.0034100	Pa×s	373.50	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0023600	Pa×s	393.30	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0017100	Pa×s	413.25	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0016790	Pa×s	413.73	Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 473 K and at atmospheric pressure
η	0.0013900	Pa×s	428.10	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0009970	Pa×s	462.25	Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 473 K and at atmospheric pressure
εr	[22.43; 23.69]		[293.15; 303.15]
εr	23.69		293.15	Excess molar volumes and deviations of the relative permittivity of the binary mixtures of 2-propoxyethanol with diethylene, triethylene, and tetraethylene glycols at various temperatures
εr	23.07		298.15	Excess molar volumes and deviations of the relative permittivity of the binary mixtures of 2-propoxyethanol with diethylene, triethylene, and tetraethylene glycols at various temperatures
εr	22.43		303.15	Excess molar volumes and deviations of the relative permittivity of the binary mixtures of 2-propoxyethanol with diethylene, triethylene, and tetraethylene glycols at various temperatures
ΔvapH	[60.80; 79.20]	kJ/mol	[273.00; 502.00]
ΔvapH	79.20 ± 7.90	kJ/mol	273.00	NIST
ΔvapH	67.70	kJ/mol	295.50	NIST
ΔvapH	77.00	kJ/mol	300.50	NIST
ΔvapH	71.50	kJ/mol	469.50	NIST
ΔvapH	72.20 ± 0.30	kJ/mol	502.00	NIST
ΔvapH	68.50 ± 0.30	kJ/mol	502.00	NIST
ΔvapH	64.60 ± 0.30	kJ/mol	502.00	NIST
ΔvapH	60.80 ± 0.50	kJ/mol	502.00	NIST
Pvap	1.76e-04	kPa	298.15	NCMS SOLV-DB
n0	[1.45314; 1.45560]		[293.15; 298.15]
n0	1.45560		293.15	Infinite Dilution Activity Coefficients of Hydrocarbons in Triethylene Glycol and Tetraethylene Glycol
n0	1.45314		293.15	Liquid-Liquid Equilibria of (Limonene + Linalool + Ethylene Glycol or Diethylene Glycol or Triethylene Glycol or 1,2-Propylene Glycol) Ternary Systems
n0	1.45400		298.15	NCMS SOLV-DB
ρl	[1061.90; 1135.14]	kg/m3	[278.15; 373.15]
ρl	1135.14	kg/m3	278.15	Acoustic and volumetric studies on (triethylene glycol + water) mixtures in a wide temperature range
ρl	1131.30	kg/m3	283.15	Thermophysical properties of glycols and glymes
ρl	1131.29	kg/m3	283.15	Acoustic and volumetric studies on (triethylene glycol + water) mixtures in a wide temperature range
ρl	1127.37	kg/m3	288.15	Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
ρl	1127.43	kg/m3	288.15	Acoustic and volumetric studies on (triethylene glycol + water) mixtures in a wide temperature range
ρl	1128.60	kg/m3	288.15	Thermophysical properties of glycols and glymes
ρl	1127.40	kg/m3	288.15	Thermophysical properties of glycols and glymes
ρl	1124.60	kg/m3	293.15	Thermophysical properties of glycols and glymes
ρl	1124.50	kg/m3	293.15	Measurement and Correlation of Densities and Viscosities of Thiourea in Triglycol + Water at Temperatures from (302.85 to 341.45) K
ρl	1124.60	kg/m3	293.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1124.70	kg/m3	293.15	Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
ρl	1123.48	kg/m3	293.15	Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
ρl	1124.60	kg/m3	293.15	Experimental and prediction of volumetric properties of aqueous solution of (allyltriphenylPhosphonium bromide - Triethylene glycol) deep eutectic solvents
ρl	1123.50	kg/m3	293.15	Thermophysical properties of glycols and glymes
ρl	1123.12	kg/m3	293.15	Experimental isobaric vapor-liquid equilibrium at sub-atmospheric and local atmospheric pressures, volumetric properties and molar refractivity from 293.15 to 313.15 K of water + triethylene glycol.
ρl	1123.56	kg/m3	293.15	Acoustic and volumetric studies on (triethylene glycol + water) mixtures in a wide temperature range
ρl	1123.20	kg/m3	293.35	Measurement and Correlation of Densities and Viscosities of Thiourea in Triglycol + Water at Temperatures from (302.85 to 341.45) K
ρl	1116.05	kg/m3	298.00	Removal of aromatic hydrocarbons from hydrocarbon mixture using glycols at 303.15 K and 333.15 K and atmospheric pressure: Experimental and calculated data by NRTL and UNIQUAC models
ρl	1119.69	kg/m3	298.15	Acoustic and volumetric studies on (triethylene glycol + water) mixtures in a wide temperature range
ρl	1120.80	kg/m3	298.15	Experimental and prediction of volumetric properties of aqueous solution of (allyltriphenylPhosphonium bromide - Triethylene glycol) deep eutectic solvents
ρl	1119.01	kg/m3	298.15	Experimental isobaric vapor-liquid equilibrium at sub-atmospheric and local atmospheric pressures, volumetric properties and molar refractivity from 293.15 to 313.15 K of water + triethylene glycol.
ρl	1119.59	kg/m3	298.15	Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
ρl	1120.70	kg/m3	298.15	Isobaric Vapor-Liquid Equilibrium for Four Binary Systems of Ethane-1,2-diol, Butane-1,4-diol, 2-(2- Hydroxyethoxy)ethan-1-ol and 2-[2-(2- Hydroxyethoxy)ethoxy]ethanol at 10.0 kPa, 20.0 kPa and 40.0 kPa
ρl	1120.70	kg/m3	298.15	Thermophysical properties of glycols and glymes
ρl	1119.70	kg/m3	298.15	Thermophysical properties of glycols and glymes
ρl	1119.78	kg/m3	298.15	Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Glycols or Poly(Ethylene Glycols) and 2-Phenylethyl Alcohol at 308.15 K and Atmospheric Pressure
ρl	1119.78	kg/m3	298.15	Thermodynamic Study of Binary Mixtures Containing Glycols or Polyethylene Glycols + Benzyl Alcohol at 308.15 K
ρl	1120.80	kg/m3	298.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1116.60	kg/m3	302.85	Measurement and Correlation of Densities and Viscosities of Thiourea in Triglycol + Water at Temperatures from (302.85 to 341.45) K
ρl	1115.70	kg/m3	303.15	Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
ρl	1116.80	kg/m3	303.15	Thermophysical properties of glycols and glymes
ρl	1116.90	kg/m3	303.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1114.79	kg/m3	303.15	Experimental isobaric vapor-liquid equilibrium at sub-atmospheric and local atmospheric pressures, volumetric properties and molar refractivity from 293.15 to 313.15 K of water + triethylene glycol.
ρl	1115.83	kg/m3	303.15	Thermodynamic and physicochemical properties of binary mixtures of sulfolane with ethylene glycol, diethylene glycol, triethylene glycol, and tetraethylene glycol systems at 303.15K
ρl	1117.00	kg/m3	303.15	Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
ρl	1115.80	kg/m3	303.15	Thermophysical properties of glycols and glymes
ρl	1115.81	kg/m3	303.15	Acoustic and volumetric studies on (triethylene glycol + water) mixtures in a wide temperature range
ρl	1116.50	kg/m3	303.15	Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
ρl	1111.90	kg/m3	307.75	Measurement and Correlation of Densities and Viscosities of Thiourea in Triglycol + Water at Temperatures from (302.85 to 341.45) K
ρl	1111.90	kg/m3	308.15	Thermophysical properties of glycols and glymes
ρl	1111.81	kg/m3	308.15	Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
ρl	1112.09	kg/m3	308.15	Excess molar enthalpies of binary mixtures containing ethylene glycols or poly(ethylene glycols) + ethyl alcohol at 308.15K and atmospheric pressure
ρl	1111.92	kg/m3	308.15	Acoustic and volumetric studies on (triethylene glycol + water) mixtures in a wide temperature range
ρl	1113.00	kg/m3	308.15	Experimental and prediction of volumetric properties of aqueous solution of (allyltriphenylPhosphonium bromide - Triethylene glycol) deep eutectic solvents
ρl	1112.90	kg/m3	308.15	Thermophysical properties of glycols and glymes
ρl	1112.61	kg/m3	308.15	Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Glycols or Poly(Ethylene Glycols) and 2-Phenylethyl Alcohol at 308.15 K and Atmospheric Pressure
ρl	1113.00	kg/m3	308.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1110.81	kg/m3	308.15	Experimental isobaric vapor-liquid equilibrium at sub-atmospheric and local atmospheric pressures, volumetric properties and molar refractivity from 293.15 to 313.15 K of water + triethylene glycol.
ρl	1112.10	kg/m3	308.15	Excess Molar Enthalpies of Binary Mixtures Containing Glycols or Polyglycols + Dimethyl Sulfoxide at 308.15 K
ρl	1112.61	kg/m3	308.15	Thermodynamic Study of Binary Mixtures Containing Glycols or Polyethylene Glycols + Benzyl Alcohol at 308.15 K
ρl	1112.59	kg/m3	308.50	Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Ethers and Benzyl Alcohol at 308.15 K and Atmospheric Pressure
ρl	1108.40	kg/m3	312.65	Measurement and Correlation of Densities and Viscosities of Thiourea in Triglycol + Water at Temperatures from (302.85 to 341.45) K
ρl	1108.00	kg/m3	313.15	Thermophysical properties of glycols and glymes
ρl	1106.70	kg/m3	313.15	Experimental isobaric vapor-liquid equilibrium at sub-atmospheric and local atmospheric pressures, volumetric properties and molar refractivity from 293.15 to 313.15 K of water + triethylene glycol.
ρl	1109.00	kg/m3	313.15	Thermophysical properties of glycols and glymes
ρl	1109.10	kg/m3	313.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1108.03	kg/m3	313.15	Acoustic and volumetric studies on (triethylene glycol + water) mixtures in a wide temperature range
ρl	1109.20	kg/m3	313.15	Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
ρl	1108.90	kg/m3	313.15	Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
ρl	1104.70	kg/m3	317.45	Measurement and Correlation of Densities and Viscosities of Thiourea in Triglycol + Water at Temperatures from (302.85 to 341.45) K
ρl	1105.20	kg/m3	318.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1105.10	kg/m3	318.15	Thermophysical properties of glycols and glymes
ρl	1104.13	kg/m3	318.15	Acoustic and volumetric studies on (triethylene glycol + water) mixtures in a wide temperature range
ρl	1105.20	kg/m3	318.15	Experimental and prediction of volumetric properties of aqueous solution of (allyltriphenylPhosphonium bromide - Triethylene glycol) deep eutectic solvents
ρl	1101.00	kg/m3	322.25	Measurement and Correlation of Densities and Viscosities of Thiourea in Triglycol + Water at Temperatures from (302.85 to 341.45) K
ρl	1101.10	kg/m3	323.15	Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
ρl	1101.50	kg/m3	323.15	Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
ρl	1100.22	kg/m3	323.15	Acoustic and volumetric studies on (triethylene glycol + water) mixtures in a wide temperature range
ρl	1100.20	kg/m3	323.15	Thermophysical properties of glycols and glymes
ρl	1101.20	kg/m3	323.15	Thermophysical properties of glycols and glymes
ρl	1101.30	kg/m3	323.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1097.90	kg/m3	327.05	Measurement and Correlation of Densities and Viscosities of Thiourea in Triglycol + Water at Temperatures from (302.85 to 341.45) K
ρl	1097.40	kg/m3	328.15	Experimental and prediction of volumetric properties of aqueous solution of (allyltriphenylPhosphonium bromide - Triethylene glycol) deep eutectic solvents
ρl	1096.30	kg/m3	328.15	Acoustic and volumetric studies on (triethylene glycol + water) mixtures in a wide temperature range
ρl	1097.40	kg/m3	328.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1097.30	kg/m3	328.15	Thermophysical properties of glycols and glymes
ρl	1093.50	kg/m3	332.15	Measurement and Correlation of Densities and Viscosities of Thiourea in Triglycol + Water at Temperatures from (302.85 to 341.45) K
ρl	1093.70	kg/m3	333.15	Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
ρl	1092.40	kg/m3	333.15	Thermophysical properties of glycols and glymes
ρl	1092.38	kg/m3	333.15	Acoustic and volumetric studies on (triethylene glycol + water) mixtures in a wide temperature range
ρl	1093.50	kg/m3	333.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1093.40	kg/m3	333.15	Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
ρl	1093.40	kg/m3	333.15	Thermophysical properties of glycols and glymes
ρl	1089.60	kg/m3	338.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1089.50	kg/m3	338.15	Thermophysical properties of glycols and glymes
ρl	1086.10	kg/m3	341.45	Measurement and Correlation of Densities and Viscosities of Thiourea in Triglycol + Water at Temperatures from (302.85 to 341.45) K
ρl	1084.50	kg/m3	343.15	Thermophysical properties of glycols and glymes
ρl	1085.50	kg/m3	343.15	Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
ρl	1085.90	kg/m3	343.15	Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
ρl	1085.60	kg/m3	343.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1085.60	kg/m3	343.15	Experimental and prediction of volumetric properties of aqueous solution of (allyltriphenylPhosphonium bromide - Triethylene glycol) deep eutectic solvents
ρl	1085.60	kg/m3	343.15	Thermophysical properties of glycols and glymes
ρl	1081.70	kg/m3	348.15	Thermophysical properties of glycols and glymes
ρl	1077.80	kg/m3	353.15	Thermophysical properties of glycols and glymes
ρl	1073.80	kg/m3	358.15	Thermophysical properties of glycols and glymes
ρl	1069.80	kg/m3	363.15	Thermophysical properties of glycols and glymes
ρl	1065.90	kg/m3	368.15	Thermophysical properties of glycols and glymes
ρl	1061.90	kg/m3	373.15	Thermophysical properties of glycols and glymes
γ	0.05	N/m	298.15	NCMS SOLV-DB
λ	[0.19; 0.19]	W/m×K	[298.10; 338.40]
λ	0.19	W/m×K	298.10	Application of the Multi-Current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols
λ	0.19	W/m×K	308.20	Application of the Multi-Current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols
λ	0.19	W/m×K	318.40	Application of the Multi-Current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols
λ	0.19	W/m×K	328.40	Application of the Multi-Current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols
λ	0.19	W/m×K	338.40	Application of the Multi-Current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols

Datasets

1. Viscosity, Pa*s (2)
2. Joule-Thomson coefficient, K/kPa (1)
3. Mass density, kg/m3 (2)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.15	98.00	0.0368
298.15	49030.00	0.0552
298.15	98060.00	0.0803
298.15	147100.00	0.1144
298.15	196130.00	0.1606
298.15	245160.00	0.2218
312.96	98.00	0.0190
313.05	49030.00	0.0274
313.10	98060.00	0.0383
313.18	147100.00	0.0525
313.25	196130.00	0.0707
313.26	245160.00	0.0940
334.96	98.00	0.0090
335.11	49030.00	0.0124
335.14	98060.00	0.0167
335.20	147100.00	0.0220
335.25	196130.00	0.0285
335.26	245160.00	0.0364
349.25	98.00	0.0059
349.94	196130.00	0.0175
349.98	49030.00	0.0081
349.98	98060.00	0.0107
349.99	245160.00	0.0218
350.03	147100.00	0.0138
364.44	98.00	0.0041
364.44	49030.00	0.0055
364.72	98060.00	0.0071
365.03	147100.00	0.0090
365.07	196130.00	0.0112
365.20	245160.00	0.0138
413.73	98.00	0.0017
414.00	49030.00	0.0022
414.15	98060.00	0.0028
414.27	147100.00	0.0033
414.30	196130.00	0.0040
414.43	245160.00	0.0045
462.25	98.00	0.0010
462.26	49030.00	0.0013
462.32	98060.00	0.0016
462.41	147100.00	0.0019
462.45	196130.00	0.0023
462.58	245160.00	0.0027
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
101.30	308.15	0.0238
Reference

Joule-Thomson coefficient, K/kPa

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Joule-Thomson coefficient, K/kPa - Liquid
293.10	7000.00	-0.0004
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.08	100.00	1131.7
283.08	1000.00	1132.4
283.08	2000.00	1132.8
283.08	5000.00	1134.1
283.08	7000.00	1134.9
283.08	10000.00	1136.2
283.08	12000.00	1137.1
283.08	16000.00	1138.8
283.08	20000.00	1140.5
283.08	25000.00	1142.5
283.08	30000.00	1144.5
283.08	35000.00	1146.5
283.08	40000.00	1148.4
283.08	45000.00	1150.2
283.08	50000.00	1152.1
283.08	55000.00	1154.0
283.08	60000.00	1155.8
283.08	65000.00	1157.6
283.08	70000.00	1159.4
283.08	75000.00	1161.0
283.08	80000.00	1162.8
283.08	85000.00	1164.5
283.08	90000.00	1166.1
283.08	95000.00	1167.7
293.14	100.00	1124.1
293.14	1000.00	1124.5
293.14	2000.00	1124.9
293.14	5000.00	1126.3
293.14	7000.00	1127.3
293.14	10000.00	1128.6
293.14	12000.00	1129.4
293.14	16000.00	1131.3
293.14	20000.00	1132.9
293.14	25000.00	1135.0
293.14	30000.00	1137.1
293.14	35000.00	1139.2
293.14	40000.00	1141.1
293.14	45000.00	1143.0
293.14	50000.00	1145.0
293.14	55000.00	1146.9
293.14	60000.00	1148.7
293.14	65000.00	1150.5
293.14	70000.00	1152.4
293.14	75000.00	1154.2
293.14	80000.00	1155.9
293.14	85000.00	1157.6
293.14	90000.00	1159.2
293.14	95000.00	1160.9
303.12	100.00	1116.2
303.12	1000.00	1116.6
303.12	2000.00	1117.1
303.12	5000.00	1118.5
303.12	7000.00	1119.5
303.12	10000.00	1120.9
303.12	12000.00	1121.8
303.12	16000.00	1123.6
303.12	20000.00	1125.4
303.12	25000.00	1127.6
303.12	30000.00	1129.7
303.12	35000.00	1131.8
303.12	40000.00	1133.9
303.12	45000.00	1135.9
303.12	50000.00	1137.9
303.12	55000.00	1139.9
303.12	60000.00	1141.8
303.12	65000.00	1143.7
303.12	70000.00	1145.5
303.12	75000.00	1147.3
303.12	80000.00	1149.1
303.12	85000.00	1150.8
303.12	90000.00	1152.6
303.12	95000.00	1154.2
313.18	100.00	1108.3
313.18	1000.00	1108.7
313.18	2000.00	1109.2
313.18	5000.00	1110.7
313.18	7000.00	1111.7
313.18	10000.00	1113.1
313.18	12000.00	1114.1
313.18	16000.00	1115.9
313.18	20000.00	1117.8
313.18	25000.00	1120.0
313.18	30000.00	1122.3
313.18	35000.00	1124.4
313.18	40000.00	1126.6
313.18	45000.00	1128.7
313.18	50000.00	1130.6
313.18	55000.00	1132.6
313.18	60000.00	1134.6
313.18	65000.00	1136.6
313.18	70000.00	1138.5
313.18	75000.00	1140.3
313.18	80000.00	1142.1
313.18	85000.00	1143.9
313.18	90000.00	1145.6
313.18	95000.00	1147.4
323.14	100.00	1100.5
323.14	1000.00	1101.0
323.14	2000.00	1101.5
323.14	5000.00	1103.0
323.14	7000.00	1104.1
323.14	10000.00	1105.5
323.14	12000.00	1106.5
323.14	16000.00	1108.4
323.14	20000.00	1110.3
323.14	25000.00	1112.6
323.14	30000.00	1114.9
323.14	35000.00	1117.1
323.14	40000.00	1119.4
323.14	45000.00	1121.5
323.14	50000.00	1123.7
323.14	55000.00	1125.7
323.14	60000.00	1127.7
323.14	65000.00	1129.7
323.14	70000.00	1131.7
323.14	75000.00	1133.5
323.14	80000.00	1135.4
323.14	85000.00	1137.3
323.14	90000.00	1139.0
323.14	95000.00	1140.8
333.10	100.00	1092.7
333.10	1000.00	1093.2
333.10	2000.00	1093.8
333.10	5000.00	1095.4
333.10	7000.00	1096.4
333.10	10000.00	1098.0
333.10	12000.00	1098.9
333.10	16000.00	1100.9
333.10	20000.00	1102.9
333.10	25000.00	1105.3
333.10	30000.00	1107.7
333.10	35000.00	1110.1
333.10	40000.00	1112.3
333.10	45000.00	1114.5
333.10	50000.00	1116.6
333.10	55000.00	1118.9
333.10	60000.00	1120.8
333.10	65000.00	1122.9
333.10	70000.00	1124.9
333.10	75000.00	1126.9
333.10	80000.00	1128.8
333.10	85000.00	1130.7
333.10	90000.00	1132.5
333.10	95000.00	1134.4
343.14	100.00	1084.7
343.14	1000.00	1085.3
343.14	2000.00	1086.0
343.14	5000.00	1087.6
343.14	7000.00	1088.6
343.14	10000.00	1090.2
343.14	12000.00	1091.3
343.14	16000.00	1093.4
343.14	20000.00	1095.4
343.14	25000.00	1097.9
343.14	30000.00	1100.4
343.14	35000.00	1102.8
343.14	40000.00	1105.1
343.14	45000.00	1107.4
343.14	50000.00	1109.6
343.14	55000.00	1111.9
343.14	60000.00	1114.0
343.14	65000.00	1116.1
343.14	70000.00	1118.1
343.14	75000.00	1120.1
343.14	80000.00	1122.1
343.14	85000.00	1124.1
343.14	90000.00	1126.0
343.14	95000.00	1128.0
353.10	100.00	1077.0
353.10	1000.00	1076.9
353.10	2000.00	1078.0
353.10	5000.00	1079.8
353.10	7000.00	1080.9
353.10	10000.00	1082.6
353.10	12000.00	1083.6
353.10	16000.00	1085.7
353.10	20000.00	1088.0
353.10	25000.00	1090.5
353.10	30000.00	1093.2
353.10	35000.00	1095.5
353.10	40000.00	1098.0
353.10	45000.00	1100.3
353.10	50000.00	1102.6
353.10	55000.00	1104.9
353.10	60000.00	1107.3
353.10	65000.00	1109.1
353.10	70000.00	1111.5
353.10	75000.00	1113.3
353.10	80000.00	1115.6
353.10	85000.00	1117.4
353.10	90000.00	1119.5
353.10	95000.00	1121.3
363.16	100.00	1068.9
363.16	1000.00	1069.4
363.16	2000.00	1070.1
363.16	5000.00	1071.8
363.16	7000.00	1073.0
363.16	10000.00	1074.6
363.16	12000.00	1075.8
363.16	16000.00	1078.2
363.16	20000.00	1080.3
363.16	25000.00	1082.9
363.16	30000.00	1085.6
363.16	35000.00	1088.1
363.16	40000.00	1090.6
363.16	45000.00	1093.0
363.16	50000.00	1095.4
363.16	55000.00	1097.8
363.16	60000.00	1100.1
363.16	65000.00	1102.3
363.16	70000.00	1104.5
363.16	75000.00	1106.6
363.16	80000.00	1108.7
363.16	85000.00	1110.7
363.16	90000.00	1112.8
363.16	95000.00	1114.8
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	1130.8
283.15	100.00	1130.8
283.15	660.00	1131.0
283.15	1150.00	1131.2
283.15	1570.00	1131.4
283.15	2090.00	1131.6
283.15	3090.00	1132.0
283.15	5060.00	1132.9
283.15	6940.00	1133.6
283.15	10020.00	1134.9
283.15	14850.00	1136.9
283.15	19830.00	1138.9
283.15	24700.00	1140.8
283.15	29600.00	1142.7
283.15	34510.00	1144.6
283.15	39360.00	1146.4
283.15	44290.00	1148.2
283.15	49180.00	1150.0
283.15	54110.00	1151.7
283.15	58970.00	1153.4
283.15	63860.00	1155.1
283.15	68790.00	1156.8
293.15	100.00	1122.9
293.15	100.00	1122.9
293.15	640.00	1123.1
293.15	1090.00	1123.4
293.15	1600.00	1123.6
293.15	2140.00	1123.8
293.15	3080.00	1124.2
293.15	5030.00	1125.1
293.15	7010.00	1125.9
293.15	9950.00	1127.2
293.15	14850.00	1129.3
293.15	19770.00	1131.3
293.15	24660.00	1133.3
293.15	29510.00	1135.2
293.15	34610.00	1137.2
293.15	39370.00	1139.1
293.15	44320.00	1141.0
293.15	49130.00	1142.8
293.15	54050.00	1144.6
293.15	59060.00	1146.4
293.15	63780.00	1148.0
303.15	100.00	1115.2
303.15	100.00	1115.1
303.15	630.00	1115.4
303.15	1130.00	1115.6
303.15	1620.00	1115.9
303.15	2140.00	1116.1
303.15	3070.00	1116.5
303.15	5080.00	1117.4
303.15	6960.00	1118.3
303.15	9960.00	1119.6
303.15	14840.00	1121.7
303.15	19750.00	1123.8
303.15	24670.00	1125.9
303.15	29570.00	1127.9
303.15	34500.00	1129.9
303.15	39360.00	1131.9
303.15	44300.00	1133.8
303.15	49190.00	1135.7
303.15	54090.00	1137.6
303.15	58850.00	1139.3
303.15	63890.00	1141.2
303.15	68750.00	1142.9
313.15	100.00	1107.4
313.15	100.00	1107.4
313.15	670.00	1107.6
313.15	1130.00	1107.9
313.15	1600.00	1108.1
313.15	2080.00	1108.3
313.15	3100.00	1108.8
313.15	5030.00	1109.7
313.15	7010.00	1110.6
313.15	10010.00	1112.0
313.15	14880.00	1114.2
313.15	19750.00	1116.4
313.15	24680.00	1118.6
313.15	29560.00	1120.6
313.15	34510.00	1122.7
313.15	39330.00	1124.7
313.15	44290.00	1126.7
313.15	49180.00	1128.6
313.15	54160.00	1130.6
313.15	59000.00	1132.4
313.15	63910.00	1134.3
313.15	68840.00	1136.0
323.15	100.00	1099.6
323.15	100.00	1099.5
323.15	590.00	1099.8
323.15	1140.00	1100.0
323.15	1600.00	1100.3
323.15	2080.00	1100.5
323.15	3020.00	1101.0
323.15	5050.00	1101.9
323.15	7000.00	1102.9
323.15	9970.00	1104.3
323.15	14870.00	1106.7
323.15	19780.00	1108.9
323.15	24700.00	1111.2
323.15	29650.00	1113.3
323.15	34470.00	1115.4
323.15	39340.00	1117.5
323.15	44250.00	1119.6
323.15	49170.00	1121.6
323.15	54080.00	1123.5
323.15	58970.00	1125.5
323.15	63800.00	1127.3
323.15	68780.00	1129.2
333.15	100.00	1091.7
333.15	100.00	1091.7
333.15	660.00	1092.0
333.15	1110.00	1092.2
333.15	1600.00	1092.5
333.15	2100.00	1092.7
333.15	3070.00	1093.2
333.15	5060.00	1094.2
333.15	6980.00	1095.2
333.15	9970.00	1096.6
333.15	14840.00	1099.0
333.15	19660.00	1101.3
333.15	24670.00	1103.7
333.15	29610.00	1106.0
333.15	34530.00	1108.2
333.15	39400.00	1110.3
333.15	44280.00	1112.5
333.15	49110.00	1114.5
333.15	54040.00	1116.5
333.15	59060.00	1118.6
333.15	63830.00	1120.5
333.15	68770.00	1122.4
343.15	100.00	1083.9
343.15	100.00	1083.9
343.15	640.00	1084.2
343.15	1120.00	1084.4
343.15	1600.00	1084.7
343.15	2110.00	1084.9
343.15	3040.00	1085.5
343.15	5040.00	1086.6
343.15	6960.00	1087.5
343.15	9920.00	1089.0
343.15	14810.00	1091.6
343.15	19680.00	1093.9
343.15	24620.00	1096.4
343.15	29580.00	1098.7
343.15	34460.00	1101.0
343.15	39370.00	1103.3
343.15	44240.00	1105.4
343.15	49160.00	1107.6
343.15	54020.00	1109.7
343.15	58940.00	1111.7
343.15	63890.00	1113.8
343.15	68680.00	1115.7
353.15	100.00	1076.0
353.15	100.00	1076.0
353.15	650.00	1076.3
353.15	1100.00	1076.5
353.15	1550.00	1076.7
353.15	2100.00	1077.1
353.15	3050.00	1077.6
353.15	5040.00	1078.6
353.15	7010.00	1079.8
353.15	9960.00	1081.3
353.15	14810.00	1084.0
353.15	19780.00	1086.5
353.15	24610.00	1089.0
353.15	29560.00	1091.9
353.15	34450.00	1093.8
353.15	39370.00	1096.1
353.15	44270.00	1098.4
353.15	49200.00	1100.6
353.15	54090.00	1102.8
353.15	59010.00	1104.9
353.15	63820.00	1107.0
353.15	68800.00	1109.0
363.15	100.00	1068.1
363.15	100.00	1068.0
363.15	660.00	1068.4
363.15	1120.00	1068.7
363.15	1560.00	1068.9
363.15	2130.00	1069.2
363.15	3050.00	1069.8
363.15	5090.00	1070.9
363.15	6990.00	1072.0
363.15	9980.00	1073.7
363.15	14880.00	1076.4
363.15	19680.00	1079.0
363.15	24720.00	1081.7
363.15	29630.00	1084.2
363.15	34490.00	1086.6
363.15	39430.00	1089.0
363.15	44200.00	1091.4
363.15	49240.00	1093.7
363.15	54100.00	1095.9
363.15	59010.00	1098.1
363.15	63880.00	1100.2
363.15	68830.00	1102.3
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[174.71; 454.06]	J/mol×K	[265.95; 1500.00]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			8.84420e+01
Coefficient B			-4.17200e+02
Coefficient C			5.93724e+00
Coefficient D			3.71630e-04
Coefficient E			-1.39990e-07
Comment			ChemSep eq 16, IdealGasHeatCapacityCp
Temperature range, min.			265.95
Temperature range, max.			1500.00
Cp,gas	174.71	J/mol×K	265.95	Calculated Property
Cp,gas	241.26	J/mol×K	403.07	Calculated Property
Cp,gas	293.81	J/mol×K	540.18	Calculated Property
Cp,gas	335.29	J/mol×K	677.30	Calculated Property
Cp,gas	368.44	J/mol×K	814.42	Calculated Property
Cp,gas	395.08	J/mol×K	951.53	Calculated Property
Cp,gas	416.33	J/mol×K	1088.65	Calculated Property
Cp,gas	432.94	J/mol×K	1225.77	Calculated Property
Cp,gas	445.39	J/mol×K	1362.88	Calculated Property
Cp,gas	454.06	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[316.53; 564.32]	J/mol×K	[265.79; 666.48]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			2.34210e+02
Coefficient B			-8.97410e+01
Coefficient C			3.42024e+00
Coefficient D			5.80890e-03
Coefficient E			-3.05650e-06
Comment			ChemSep eq 16, LiquidHeatCapacityCp
Temperature range, min.			265.79
Temperature range, max.			666.48
Cp,liquid	316.53	J/mol×K	265.79	Calculated Property
Cp,liquid	337.68	J/mol×K	310.31	Calculated Property
Cp,liquid	361.15	J/mol×K	354.83	Calculated Property
Cp,liquid	386.82	J/mol×K	399.35	Calculated Property
Cp,liquid	414.45	J/mol×K	443.87	Calculated Property
Cp,liquid	443.66	J/mol×K	488.40	Calculated Property
Cp,liquid	473.93	J/mol×K	532.92	Calculated Property
Cp,liquid	504.63	J/mol×K	577.44	Calculated Property
Cp,liquid	535.03	J/mol×K	621.96	Calculated Property
Cp,liquid	564.32	J/mol×K	666.48	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.2818884; 0.0003114]	Pa×s	[265.95; 769.50]	ChemSep v8.3 pure component data
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-3.54991e+02
Coefficient B			1.64717e+04
Coefficient C			5.45539e+01
Coefficient D			-4.81353e-02
Coefficient E			1.00000e+00
Comment			ChemSep eq 101, LiquidViscosity
Temperature range, min.			265.95
Temperature range, max.			769.50
η	0.2818884	Pa×s	265.95	Calculated Property
η	0.0134555	Pa×s	321.90	Calculated Property
η	0.0029207	Pa×s	377.85	Calculated Property
η	0.0013355	Pa×s	433.80	Calculated Property
η	0.0008836	Pa×s	489.75	Calculated Property
η	0.0006950	Pa×s	545.70	Calculated Property
η	0.0005832	Pa×s	601.65	Calculated Property
η	0.0004913	Pa×s	657.60	Calculated Property
η	0.0004012	Pa×s	713.55	Calculated Property
η	0.0003114	Pa×s	769.50	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[91.85; 0.00]	kJ/mol	[265.95; 769.50]	ChemSep v8.3 pure component data
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			1.39290e+02
Coefficient B			1.42282e+00
Coefficient C			-1.62580e+00
Coefficient D			1.20767e+00
Coefficient E			-5.63316e-01
Critical temperature, Tc (K)			7.69500e+02
Comment			ChemSep eq 106, HeatOfVaporization
Temperature range, min.			265.95
Temperature range, max.			769.50
ΔvapH	91.85	kJ/mol	265.95	Calculated Property
ΔvapH	84.94	kJ/mol	321.90	Calculated Property
ΔvapH	78.51	kJ/mol	377.85	Calculated Property
ΔvapH	72.38	kJ/mol	433.80	Calculated Property
ΔvapH	66.41	kJ/mol	489.75	Calculated Property
ΔvapH	60.42	kJ/mol	545.70	Calculated Property
ΔvapH	54.13	kJ/mol	601.65	Calculated Property
ΔvapH	46.96	kJ/mol	657.60	Calculated Property
ΔvapH	37.12	kJ/mol	713.55	Calculated Property
ΔvapH	0.00	kJ/mol	769.50	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[427.16; 586.55]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.94699e+01
Coefficient B			-8.61684e+03
Coefficient C			2.20480e+01
Temperature range, min.			427.16
Temperature range, max.			586.55
Pvap	1.33	kPa	427.16	Calculated Property
Pvap	2.76	kPa	444.87	Calculated Property
Pvap	5.42	kPa	462.58	Calculated Property
Pvap	10.14	kPa	480.29	Calculated Property
Pvap	18.18	kPa	498.00	Calculated Property
Pvap	31.38	kPa	515.71	Calculated Property
Pvap	52.31	kPa	533.42	Calculated Property
Pvap	84.47	kPa	551.13	Calculated Property
Pvap	132.56	kPa	568.84	Calculated Property
Pvap	202.63	kPa	586.55	Calculated Property
Pvap	[7.39e-06; 657.95]	kPa	[265.95; 769.50]	ChemSep v8.3 pure component data
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			-1.55005e+02
Coefficient B			-1.44689e+03
Coefficient C			2.69582e+01
Coefficient D			-2.66538e-05
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			265.95
Temperature range, max.			769.50
Pvap	7.39e-06	kPa	265.95	Calculated Property
Pvap	1.36e-03	kPa	321.90	Calculated Property
Pvap	0.07	kPa	377.85	Calculated Property
Pvap	1.42	kPa	433.80	Calculated Property
Pvap	13.79	kPa	489.75	Calculated Property
Pvap	73.59	kPa	545.70	Calculated Property
Pvap	236.37	kPa	601.65	Calculated Property
Pvap	487.49	kPa	657.60	Calculated Property
Pvap	677.43	kPa	713.55	Calculated Property
Pvap	657.95	kPa	769.50	Calculated Property
Pvap	[5.30e-06; 3249.79]	kPa	[265.79; 700.00]	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			2.93684e+01
Coefficient B			-8.89710e+03
Coefficient C			-1.46752e+00
Coefficient D			2.12637e-06
Coefficient E			0.00000e+00
Temperature range, min.			265.79
Temperature range, max.			700.00
Pvap	5.30e-06	kPa	265.79	Calculated Property
Pvap	7.53e-04	kPa	314.04	Calculated Property
Pvap	0.03	kPa	362.28	Calculated Property
Pvap	0.46	kPa	410.53	Calculated Property
Pvap	4.17	kPa	458.77	Calculated Property
Pvap	25.19	kPa	507.02	Calculated Property
Pvap	112.94	kPa	555.26	Calculated Property
Pvap	405.21	kPa	603.51	Calculated Property
Pvap	1226.12	kPa	651.75	Calculated Property
Pvap	3249.79	kPa	700.00	Calculated Property
Pvap	[0.13; 100.71]	kPa	[387.00; 551.40]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			2.01633e+01
Coefficient B			-8.55461e+03
Coefficient C			-1.29900e+00
Reference			Stull, 1947
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			387.00
Temperature range, max.			551.40
Pvap	0.13	kPa	387.00	Calculated Property
Pvap	0.36	kPa	405.27	Calculated Property
Pvap	0.91	kPa	423.53	Calculated Property
Pvap	2.10	kPa	441.80	Calculated Property
Pvap	4.56	kPa	460.07	Calculated Property
Pvap	9.30	kPa	478.33	Calculated Property
Pvap	18.02	kPa	496.60	Calculated Property
Pvap	33.32	kPa	514.87	Calculated Property
Pvap	59.04	kPa	533.13	Calculated Property
Pvap	100.71	kPa	551.40	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1141.37; 344.69]	kg/m3	[265.95; 769.50]	ChemSep v8.3 pure component data
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			9.11505e+01
Coefficient B			2.64440e-01
Coefficient C			7.69500e+02
Coefficient D			2.48050e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			265.95
Temperature range, max.			769.50
ρl	1141.37	kg/m3	265.95	Calculated Property
ρl	1102.69	kg/m3	321.90	Calculated Property
ρl	1061.70	kg/m3	377.85	Calculated Property
ρl	1017.82	kg/m3	433.80	Calculated Property
ρl	970.24	kg/m3	489.75	Calculated Property
ρl	917.65	kg/m3	545.70	Calculated Property
ρl	857.81	kg/m3	601.65	Calculated Property
ρl	786.15	kg/m3	657.60	Calculated Property
ρl	690.15	kg/m3	713.55	Calculated Property
ρl	344.69	kg/m3	769.50	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.05; 0.02]	N/m	[293.15; 548.15]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-5.38810e-02
Coefficient B			-2.47050e+01
Coefficient C			-1.94390e+00
Coefficient D			-8.47170e-04
Coefficient E			-3.91890e-07
Comment			ChemSep eq 16, SurfaceTension
Temperature range, min.			293.15
Temperature range, max.			548.15
γ	0.05	N/m	293.15	Calculated Property
γ	0.04	N/m	321.48	Calculated Property
γ	0.04	N/m	349.82	Calculated Property
γ	0.04	N/m	378.15	Calculated Property
γ	0.04	N/m	406.48	Calculated Property
γ	0.03	N/m	434.82	Calculated Property
γ	0.03	N/m	463.15	Calculated Property
γ	0.03	N/m	491.48	Calculated Property
γ	0.03	N/m	519.82	Calculated Property
γ	0.02	N/m	548.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.00; 0.07]	W/m×K	[199.82; 1000.00]	ChemSep v8.3 pure component data
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K
Coefficient A			4.80350e-06
Coefficient B			1.40250e+00
Coefficient C			1.64430e+02
Coefficient D			1.51140e+04
Comment			ChemSep eq 102, VaporThermalConductivity
Temperature range, min.			199.82
Temperature range, max.			1000.00
λ	0.00	W/m×K	199.82	Calculated Property
λ	0.01	W/m×K	288.73	Calculated Property
λ	0.01	W/m×K	377.64	Calculated Property
λ	0.02	W/m×K	466.55	Calculated Property
λ	0.03	W/m×K	555.46	Calculated Property
λ	0.03	W/m×K	644.36	Calculated Property
λ	0.04	W/m×K	733.27	Calculated Property
λ	0.05	W/m×K	822.18	Calculated Property
λ	0.06	W/m×K	911.09	Calculated Property
λ	0.07	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.19; 0.12]	W/m×K	[265.95; 666.48]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λ in W/m×K, T in K
Coefficient A			-8.98060e-02
Coefficient B			4.30770e-01
Coefficient C			-1.68020e+00
Coefficient D			2.40030e-03
Coefficient E			-3.36120e-06
Comment			ChemSep eq 16, LiquidThermalConductivity
Temperature range, min.			265.95
Temperature range, max.			666.48
λ	0.19	W/m×K	265.95	Calculated Property
λ	0.19	W/m×K	310.45	Calculated Property
λ	0.20	W/m×K	354.96	Calculated Property
λ	0.19	W/m×K	399.46	Calculated Property
λ	0.19	W/m×K	443.96	Calculated Property
λ	0.18	W/m×K	488.47	Calculated Property
λ	0.17	W/m×K	532.97	Calculated Property
λ	0.15	W/m×K	577.47	Calculated Property
λ	0.14	W/m×K	621.98	Calculated Property
λ	0.12	W/m×K	666.48	Calculated Property

Similar Compounds

Find more compounds similar to Triethylene glycol.

Mixtures

• Choline chloride + Triethylene glycol + Water
• Choline chloride + Triethylene glycol
• Triethylene glycol + Lithium chloride + Water
• lithium bromide + Triethylene glycol + Water
• Thiophene + Triethylene glycol + Heptane
• Benzo[b]thiophene + Triethylene glycol + Heptane
• Triethylene glycol + Heptane
• Magnesium chloride + Triethylene glycol + Water
• Triethylene glycol + Potassium carbonate + Water
• potassium fluoride + Triethylene glycol + Water
• Benzene + Triethylene glycol
• Toluene + Triethylene glycol
• Triethylene glycol + Benzene, ethyl-
• Triethylene glycol + o-Xylene
• Benzene, 1,3-dimethyl- + Triethylene glycol
• p-Xylene + Triethylene glycol
• Ethanol, 2-propoxy- + Triethylene glycol
• 1,2-Ethanediol + Triethylene glycol
• Triethylene glycol + Ethanol, 2,2'-oxybis-
• 1,2-Ethanediol + Triethylene glycol + Ethanol, 2,2'-oxybis-

Find more mixtures with Triethylene glycol.

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
• Application of the Multi-Current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols
• Thermophysical Properties For Diethylene Glycol + Nitrobenzene and Triethylene Glycol + (Chloro-, Bromo-, Nitro-) Benzene Systems at Different Temperatures
• Thermodynamic and physicochemical properties of binary mixtures of sulfolane with ethylene glycol, diethylene glycol, triethylene glycol, and tetraethylene glycol systems at 303.15K
• Measurement of the triethylene glycol solubility in supercritical methane at pressures up to 9MPa
• Mutual diffusion coefficients of aqueous solutions of some glycols
• Liquid-liquid equilibrium in the ternary systems triethylene glycol + salts + water at different temperatures; experiment and correlation
• Temperature change from isenthalpic expansion of aqueous triethylene glycol mixtures for natural gas dehydration
• Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 465 K and at high pressures up to 245 MPa
• Experimental study and phase equilibrium modeling of systems containing acid gas and glycol
• Prediction of refractive index and density of deep eutectic solvents using atomic contributions
• tert-Butyl chloride as a probe of the solvophobic effects
• Removal of aromatic hydrocarbons from hydrocarbon mixture using glycols at 303.15 K and 333.15 K and atmospheric pressure: Experimental and calculated data by NRTL and UNIQUAC models
• Experimental isobaric vapor-liquid equilibrium at sub-atmospheric and local atmospheric pressures, volumetric properties and molar refractivity from 293.15 to 313.15 K of water + triethylene glycol.
• Liquid-liquid phase diagrams of poly(ethylene glycol) and aromatic hydrocarbons
• Carbon dioxide solubility in triethylene glycol and aqueous solutions
• New measurements and modeling of high pressure thermodynamic properties of glycols
• Critical temperatures and pressures of ethylene glycols
• Viscosity of liquid diethylene, triethylene and tetraethylene glycols at moderately high pressures using a vibrating wire instrument
• Separation of thiophene, or benzothiophene from model fuel using glycols. Liquid-liquid phase equilibria and oxidative desulfurization study
• Effective extraction of benzene and thiophene by novel deep eutectic solvents from hexane / aromatic mixture at different temperatures
• The experimental study on the influence of crown ethers and glycols on the mutual solubility of lithium bromide in water
• Relative permittivity of the binary mixtures of 2-methoxyethanol with diethylene glycol, triethylene glycol, tetraethylene glycol, and polyethylene glycol 200 at various temperatures
• Excess molar volumes and deviations of the relative permittivity of the binary mixtures of 2-propoxyethanol with diethylene, triethylene, and tetraethylene glycols at various temperatures
• Vapour pressures, densities, and viscosities of the aqueous solutions containing (triethylene glycol or propylene glycol) and (LiCl or LiBr)
• Densities and vapor pressures of mixed-solvent desiccant systems containing {glycol (diethylene, or triethylene, or tetraethylene glycol) + salt (magnesium chloride) + water}
• Experimental and predicted refractive index properties in ternary mixtures of associated liquids
• Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 473 K and at atmospheric pressure
• Molar heat capacities of some aqueous 2-amino-2-hydroxymethyl-1,3-propanediol + glycol systems
• Thermophysical property characterization of ternary system containing {glycol (DEG/TEG/T4EG) + 2-amino-2-hydroxymethyl-1,3-propanediol + water}
• Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
• Isobaric specific heat capacity of typical lithium chloride liquid desiccants using scanning calorimetry
• Solubilities and thermodynamic properties of CO2 in choline-chloride based deep eutectic solvents
• Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
• Acoustic and volumetric studies on (triethylene glycol + water) mixtures in a wide temperature range
• Partial molar volumes of organic solutes in water. XXVIII. Three aliphatic poly(ethylene glycols) at temperatures T = 298 K 573 K and pressures up to 30 MPa
• Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
• Thermal stability analysis, experimental conductivity and pH of phosphonium-based deep eutectic solvents and their prediction by a new empirical equation
• Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
• Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
• Volumetric and ultrasonic studies on interactions of ethylene glycol, diethylene glycol and triethylene glycol in aqueous solutions of glycerol at temperatures T = (293.15 K - 308.15) K
• Acoustic and thermodynamic study of D-Panthenol in aqueous solutions of glycol at different temperatures
• Excess molar enthalpies of binary mixtures containing ethylene glycols or poly(ethylene glycols) + ethyl alcohol at 308.15K and atmospheric pressure
• Heat capacities of the mixed-solvents desiccants (glycols +water + salts)
• Experimental and predicted excess molar enthalpies of some working pairs for absorption cycles
• Heat Capacity of Several Mixed-Solvent Desiccants Containing Glycol + Water + MgCl2
• Molar heat capacity of several aqueous solutions of n-[tris(hydroxymethyl)methyl-3-amino]- propanesulfonic acid (TAPS) + glycol
• Density of aqueous choline chloride-based ionic liquids analogues
• Experimental and prediction of volumetric properties of aqueous solution of (allyltriphenylPhosphonium bromide - Triethylene glycol) deep eutectic solvents
• Partial Molar Volumes and Partial Molar Isentropic Compressions of Four Poly(Ethylene Glycols) at Infinite Dilution in Water at Temperatures T = (278 to 343) K and Atmospheric Pressure
• Thermophysical properties of glycols and glymes
• Solubility and Spectral Studies for SO2 in Binary System of Tri-ethylene Glycol + Dimethyl Sulfoxide at T = (298.15, 303.15, and 308.15) K and p = 123.15 kPa
• Molar Heat Capacity of Selected Type III Deep Eutectic Solvents
• Investigation on Temperature-Dependent Volumetric and Acoustical Properties of Homologous Series of Glycols in Aqueous Sorbitol Solutions
• Measurement and Modeling of Isobaric Vapor-Liquid Equilibrium of Water + Glycols
• Thermodynamic Interactions Study of Some Ethylene Glycols in Aqueous Aniline Solutions at Different Temperatures: An Acoustical and Volumetric Approach
• Effect of Ethylene, Diethylene, and Triethylene Glycols and Glycerol on the Physicochemical Properties and Phase Behavior of Benzyltrimethyl and Benzyltributylammonium Chloride Based Deep Eutectic Solvents at 283.15-343.15 K
• Vapor-Liquid Phase Equilibrium for Separation of Isopropanol from Its Aqueous Solution by Choline Chloride-Based Deep Eutectic Solvent Selected by COSMO-SAC Model
• Heat Capacity and Phase Behavior of Selected Oligo(ethylene glycol)s
• Liquid-Liquid Equilibria for Benzene/Thiophene + Cyclohexane/Hexadecane + Deep Eutectic Solvents: Data and Correlation
• Densities, Viscosities, and Excess Properties for Binary Mixtures of Some Glycols and Polyglycols in N-Methylacetamide at 308.15 K
• Infinite Dilution Activity Coefficients of Hydrocarbons in Triethylene Glycol and Tetraethylene Glycol
• Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
• Excess Molar Enthalpies of Binary Mixtures Containing Glycols or Polyglycols + Dimethyl Sulfoxide at 308.15 K
• Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for Alkyl (Methyl, Ethyl, Butyl, and Isoamyl) Acetates + Glycols at Different Temperatures
• Thermodynamic Study of Binary Mixtures Containing Glycols or Polyethylene Glycols + Benzyl Alcohol at 308.15 K
• Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Glycols or Poly(Ethylene Glycols) and 2-Phenylethyl Alcohol at 308.15 K and Atmospheric Pressure
• Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Ethers and Benzyl Alcohol at 308.15 K and Atmospheric Pressure
• Liquid-Liquid Equilibria for Binary and Ternary Systems Containing Glycols, Aromatic Hydrocarbons, and Water: Experimental Measurements and Modeling with the CPA EoS
• Heat Capacities of Four Promising Alternatives to Lithium Bromide Aqueous Solution in Absorption Refrigerators
• Isobaric Vapor-Liquid Equilibrium for Four Binary Systems of Ethane-1,2-diol, Butane-1,4-diol, 2-(2- Hydroxyethoxy)ethan-1-ol and 2-[2-(2- Hydroxyethoxy)ethoxy]ethanol at 10.0 kPa, 20.0 kPa and 40.0 kPa
• Solubility of CO2 in Nonaqueous Absorption System of 2-(2-Aminoethylamine)ethanol + Benzyl Alcohol
• Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
• Tetrabutylammonium Chloride Based Ionic Liquid Analogues and Their Physical Properties
• Liquid-Liquid Equilibria of (Limonene + Linalool + Ethylene Glycol or Diethylene Glycol or Triethylene Glycol or 1,2-Propylene Glycol) Ternary Systems
• Vapor-Liquid Equilibria of Water + Triethylene Glycol (TEG) and Water + TEG + Toluene at 85 kPa
• Measurement and Correlation for Solubility of Thiourea in Triglycol + Water at Temperatures from (292.05 to 357.75) K
• Measurement and Correlation of Densities and Viscosities of Thiourea in Triglycol + Water at Temperatures from (302.85 to 341.45) K
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.
Outlier This icon means that the value is more than 2 standard deviations away from the property mean.
These property values are available through the Cheméo API. A free account gives you an access key.