Chemical Properties of 1,2-Ethanediol (CAS 107-21-1)

InChI

InChI=1S/C2H6O2/c3-1-2-4/h3-4H,1-2H2

InChI Key

LYCAIKOWRPUZTN-UHFFFAOYSA-N

Formula

C2H6O2

SMILES

OCCO

Molecular Weight¹

62.07

CAS

107-21-1

Other Names

• 1,2-Ethandiol
• 1,2-Ethylene glycol
• 1,2-dihydroxyethane
• 146AR
• 2-Hydroxyethanol
• Aethylenglykol
• Aliphatic diol
• Athylenglykol
• Dihydroxyethane
• Dowtherm SR 1
• ETHTLENE DIHYDRATE
• Ethanediol
• Ethylene alcohol
• Ethylene dihydrate
• Ethylene gycol
• Fridex
• Glycol
• Glycol alcohol
• Glygen
• HOCH2CH2OH
• Ilexan E
• Lutrol 9
• M.e.g.
• MEG 100
• Macrogol 400 BPC
• Monoethylene glycol
• NSC 93876
• Norkool
• Ramp
• Tescol
• Ucar 17
• Union Carbide XL 54 Type I De-icing Fluid
• Zerex
• ethane-1,2-diol
• ethylene glycol

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• 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).
• σ_cond : Electrical conductivity (S/m).
• ε_r : Dielectric Constant (Relative permittivity).
• LFL : Lower Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• 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_fusH : Enthalpy of fusion at a given temperature (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).
• 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.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• 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 thermal conductivity (W/m×K).
• λ : Liquid thermal conductivity (W/m×K).
• α_diff : Thermal diffusivity (m²/s).
• 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).
• v_spec : Specific Volume (m³/kg).
• 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	0.5068		ChemSep v8.3 pure component data
PAff	815.90	kJ/mol	NIST
Tig	[671.15; 685.93]	K
Tig	685.93	K	KDB
Tig	671.15	K	NCMS SOLV-DB
BasG	773.60	kJ/mol	NIST
ΔcH°liquid	[-1202.60; -1184.60]	kJ/mol
ΔcH°liquid	-1184.60 ± 2.80	kJ/mol	NIST
ΔcH°liquid	-1188.80 ± 0.67	kJ/mol	NIST
ΔcH°liquid	-1190.20	kJ/mol	NIST
ΔcH°liquid	-1189.00 ± 0.80	kJ/mol	NIST
ΔcH°liquid	-1189.60 ± 0.71	kJ/mol	NIST
ΔcH°liquid	Outlier -1202.60 ± 1.20	kJ/mol	NIST
ΔcH°liquid	-1191.40 ± 1.20	kJ/mol	NIST
μ	[2.20; 2.41]	debye
μ	2.41	debye	ChemSep v8.3 pure component data
μ	2.20	debye	KDB
η	0.0169000	Pa×s	Viscosity, thermal and electrical conductivity of silicon dioxide - ethylene glycol transparent nanofluids: An experimental studies
εr	37.70		NCMS SOLV-DB
LFL	3.20	% in Air	KDB
Tflash,cc	[384.15; 388.71]	K
Tflash,cc	388.71	K	KDB
Tflash,cc	384.15	K	NCMS SOLV-DB
Tflash,oc	384.26	K	KDB
ΔfG°	[-304.70; -301.80]	kJ/mol
ΔfG°	-301.80	kJ/mol	ChemSep v8.3 pure component data
ΔfG°	-304.70	kJ/mol	KDB
Rg	2.4700		KDB
ΔfH°gas	[-394.40; -387.50]	kJ/mol
ΔfH°gas	-392.20	kJ/mol	ChemSep v8.3 pure component data
ΔfH°gas	-389.60	kJ/mol	KDB
ΔfH°gas	-394.40 ± 2.80	kJ/mol	NIST
ΔfH°gas	-388.00 ± 2.00	kJ/mol	NIST
ΔfH°gas	-390.30	kJ/mol	NIST
ΔfH°gas	-389.30	kJ/mol	NIST
ΔfH°gas	-387.50	kJ/mol	NIST
ΔfH°liquid	[-460.00; -453.10]	kJ/mol
ΔfH°liquid	-460.00 ± 2.80	kJ/mol	NIST
ΔfH°liquid	-455.60 ± 0.80	kJ/mol	NIST
ΔfH°liquid	-455.85	kJ/mol	NIST
ΔfH°liquid	-454.90 ± 0.30	kJ/mol	NIST
ΔfH°liquid	-453.10 ± 1.20	kJ/mol	NIST
ΔfusH°	9.11	kJ/mol	Joback Calculated Property
ΔvapH°	[63.40; 68.20]	kJ/mol
ΔvapH°	67.78	kJ/mol	NCMS SOLV-DB
ΔvapH°	65.40 ± 0.30	kJ/mol	NIST
ΔvapH°	66.00 ± 0.20	kJ/mol	NIST
ΔvapH°	66.20	kJ/mol	NIST
ΔvapH°	63.40 ± 0.10	kJ/mol	NIST
ΔvapH°	65.60	kJ/mol	NIST
ΔvapH°	65.60 ± 0.30	kJ/mol	NIST
ΔvapH°	65.60 ± 0.30	kJ/mol	NIST
ΔvapH°	63.70 ± 0.10	kJ/mol	NIST
ΔvapH°	66.10 ± 0.30	kJ/mol	NIST
ΔvapH°	68.20 ± 0.80	kJ/mol	NIST
ΔvapH°	67.60	kJ/mol	NIST
ΔvapH°	63.60	kJ/mol	NIST
ΔvapH°	63.80	kJ/mol	NIST
IE	[10.16; 10.55]	eV
IE	10.16	eV	NIST
IE	10.55	eV	NIST
IE	10.55	eV	NIST
IE	10.50	eV	NIST
log10WS	0.08		Aq. Solubility Prediction
logPoct/wat	-1.360		NCMS SOLV-DB
McVol	50.780	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	[7700.00; 13100.00]	kPa
Pc	8200.00	kPa	ChemSep v8.3 pure component data
Pc	7700.00	kPa	KDB
Pc	8200.00 ± 200.00	kPa	NIST
Pc	9000.00 ± 100.00	kPa	NIST
Pc	13100.00 ± 1000.00	kPa	NIST
pKa	14.24		NCMS SOLV-DB
Ptriple	2.19e-04	kPa	ChemSep v8.3 pure component data
Inp	[659.00; 726.00]
Inp	705.00		NIST
Inp	659.00		NIST
Inp	702.00		NIST
Inp	710.00		NIST
Inp	712.00		NIST
Inp	726.00		NIST
Inp	726.00		NIST
Inp	670.00		NIST
Inp	670.00		NIST
Inp	672.00		NIST
I	[1621.00; 1695.00]
I	1695.00		NIST
I	1652.00		NIST
I	1667.00		NIST
I	1670.00		NIST
I	1621.00		NIST
I	1635.00		NIST
I	1635.00		NIST
I	1660.00		NIST
I	1660.00		NIST
I	1660.00		NIST
S°gas	311.84	J/mol×K	NIST
S°liquid	[166.90; 179.50]	J/mol×K
S°liquid	166.90	J/mol×K	NIST
S°liquid	179.50	J/mol×K	NIST
Tboil	[455.00; 472.15]	K
Tboil	470.63	K	(Vapour + liquid) equilibria in the ternary system (acetonitrile + n-propanol + ethylene glycol) and corresponding binary systems at 101.3 kPa
Tboil	470.32	K	Separation of azeotrope (allyl alcohol + water): Isobaric vapour-liquid phase equilibrium measurements and extractive distillation
Tboil	470.22	K	Investigation on Thermodynamics in Separation for Ethylene Glycol + Neopentyl Glycol System by Azeotropic Distillation
Tboil	470.38	K	Measurement and Correlation of Excess Molar Enthalpies for Ethylene Glycol + Alkanol Systems at the Temperatures (298.15, 308.15, and 323.15) K
Tboil	469.15	K	Cosolvent Selection for Benzene-Cyclohexane Separation in Extractive Distillation
Tboil	470.47	K	Vapor Liquid Equilibria for Three Binary Systems of N-Methylethanolamine, N-Methyldiethanolamine, and Ethylene Glycol at P = (40.0, 30.0, and 20.0) kPa
Tboil	470.45	K	ChemSep v8.3 pure component data
Tboil	470.49	K	KDB
Tboil	470.69	K	NCMS SOLV-DB
Tboil	471.20	K	NIST
Tboil	470.45 ± 0.30	K	NIST
Tboil	470.45 ± 0.05	K	NIST
Tboil	470.00 ± 2.00	K	NIST
Tboil	470.75	K	NIST
Tboil	472.15 ± 0.30	K	NIST
Tboil	470.55 ± 0.15	K	NIST
Tboil	470.55 ± 0.50	K	NIST
Tboil	470.55 ± 0.15	K	NIST
Tboil	469.90 ± 1.00	K	NIST
Tboil	Outlier 455.00 ± 1.00	K	NIST
Tboil	470.35 ± 0.50	K	NIST
Tboil	468.65 ± 2.00	K	NIST
Tboil	470.55 ± 0.60	K	NIST
Tboil	470.55 ± 0.30	K	NIST
Tboil	470.70 ± 0.50	K	NIST
Tboil	470.45 ± 0.25	K	NIST
Tboil	470.35 ± 0.50	K	NIST
Tboil	471.00 ± 0.10	K	NIST
Tboil	470.40 ± 0.50	K	NIST
Tboil	470.55 ± 0.40	K	NIST
Tboil	466.15 ± 3.00	K	NIST
Tboil	470.60 ± 0.50	K	NIST
Tboil	470.60 ± 0.50	K	NIST
Tboil	470.60 ± 0.50	K	NIST
Tboil	470.60 ± 0.50	K	NIST
Tboil	470.55 ± 0.50	K	NIST
Tboil	470.70 ± 0.50	K	NIST
Tboil	470.00 ± 2.00	K	NIST
Tboil	470.52 ± 0.50	K	NIST
Tboil	470.65 ± 2.00	K	NIST
Tboil	470.65 ± 3.00	K	NIST
Tc	[645.00; 790.00]	K
Tc	719.00	K	ChemSep v8.3 pure component data
Tc	718.00	K	KDB
Tc	720.00 ± 4.00	K	NIST
Tc	720.00 ± 1.00	K	NIST
Tc	718.00 ± 1.00	K	NIST
Tc	645.00 ± 30.00	K	NIST
Tc	790.00 ± 30.00	K	NIST
Tc	645.00 ± 30.00	K	NIST
Tfus	[259.25; 262.00]	K
Tfus	260.15	K	ChemSep v8.3 pure component data
Tfus	260.00	K	KDB
Tfus	260.55	K	NCMS SOLV-DB
Tfus	260.46 ± 0.05	K	NIST
Tfus	260.45	K	NIST
Tfus	260.15 ± 0.50	K	NIST
Tfus	259.25 ± 0.50	K	NIST
Tfus	260.55 ± 0.25	K	NIST
Tfus	259.95 ± 0.50	K	NIST
Tfus	260.55 ± 0.40	K	NIST
Tfus	Outlier 262.00 ± 1.50	K	NIST
Tfus	261.70 ± 1.00	K	NIST
Ttriple	[256.60; 260.80]	K
Ttriple	259.90	K	Heat Capacity and Phase Behavior of Selected Oligo(ethylene glycol)s
Ttriple	260.15	K	ChemSep v8.3 pure component data
Ttriple	256.60 ± 0.20	K	NIST
Ttriple	260.60 ± 0.20	K	NIST
Ttriple	260.60 ± 0.20	K	NIST
Ttriple	260.80 ± 0.30	K	NIST
Ttriple	256.60 ± 0.20	K	NIST
Ttriple	260.60 ± 0.20	K	NIST
Ttriple	260.80 ± 0.30	K	NIST
UQi	2.25		ChemSep v8.3 pure component data
URi	2.41		ChemSep v8.3 pure component data
Vc	0.191	m3/kmol	ChemSep v8.3 pure component data
Zc	0.2620000		ChemSep v8.3 pure component data
Zra	0.25		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[145.20; 167.32]	J/mol×K	[293.00; 363.15]
Cp,liquid	149.40	J/mol×K	293.00	NIST
Cp,liquid	148.10	J/mol×K	293.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	145.60	J/mol×K	293.40	NIST
Cp,liquid	148.57	J/mol×K	294.65	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	149.05	J/mol×K	296.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	149.53	J/mol×K	297.65	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	148.87	J/mol×K	298.00	NIST
Cp,liquid	149.80	J/mol×K	298.00	NIST
Cp,liquid	149.30	J/mol×K	298.00	NIST
Cp,liquid	147.30	J/mol×K	298.00	NIST
Cp,liquid	149.69	J/mol×K	298.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	150.33	J/mol×K	298.15	NIST
Cp,liquid	149.60	J/mol×K	298.15	NIST
Cp,liquid	150.01	J/mol×K	299.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	150.48	J/mol×K	300.65	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	150.60	J/mol×K	301.20	NIST
Cp,liquid	150.96	J/mol×K	302.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	145.20	J/mol×K	303.00	NIST
Cp,liquid	151.44	J/mol×K	303.65	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	151.92	J/mol×K	305.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	152.40	J/mol×K	306.65	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	152.88	J/mol×K	308.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	153.36	J/mol×K	309.65	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	153.83	J/mol×K	311.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	154.31	J/mol×K	312.65	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	154.79	J/mol×K	314.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	155.27	J/mol×K	315.65	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	155.75	J/mol×K	317.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	156.23	J/mol×K	318.65	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	156.71	J/mol×K	320.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	157.19	J/mol×K	321.65	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	157.67	J/mol×K	323.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	151.57	J/mol×K	323.15	Specific Heat Capacities of Two Functional Ionic Liquids and Two Functional Deep Eutectic Solvents for the Absorption of SO2
Cp,liquid	158.15	J/mol×K	324.65	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	158.63	J/mol×K	326.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	159.11	J/mol×K	327.65	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	159.60	J/mol×K	329.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	160.08	J/mol×K	330.65	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	160.56	J/mol×K	332.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	155.23	J/mol×K	333.15	Specific Heat Capacities of Two Functional Ionic Liquids and Two Functional Deep Eutectic Solvents for the Absorption of SO2
Cp,liquid	161.04	J/mol×K	333.65	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	161.52	J/mol×K	335.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	162.00	J/mol×K	336.65	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	162.49	J/mol×K	338.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	162.97	J/mol×K	339.65	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	163.45	J/mol×K	341.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	163.93	J/mol×K	342.65	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	158.58	J/mol×K	343.15	Specific Heat Capacities of Two Functional Ionic Liquids and Two Functional Deep Eutectic Solvents for the Absorption of SO2
Cp,liquid	164.42	J/mol×K	344.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	164.90	J/mol×K	345.65	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	165.38	J/mol×K	347.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	165.86	J/mol×K	348.65	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	166.35	J/mol×K	350.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	166.83	J/mol×K	351.65	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	167.32	J/mol×K	353.15	Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
Cp,liquid	161.31	J/mol×K	353.15	Specific Heat Capacities of Two Functional Ionic Liquids and Two Functional Deep Eutectic Solvents for the Absorption of SO2
Cp,liquid	164.85	J/mol×K	363.15	Specific Heat Capacities of Two Functional Ionic Liquids and Two Functional Deep Eutectic Solvents for the Absorption of SO2
η	[0.0006520; 0.0214400]	Pa×s	[293.15; 464.40]
η	0.0211000	Pa×s	293.15	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	0.0214400	Pa×s	293.15	Viscosity of binary mixtures of 1-ethyl-3-methylimidazolium tetrafluoroborate ionic liquid with four organic solvents
η	0.0191000	Pa×s	295.55	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0148200	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	0.0154081	Pa×s	298.15	Densities, Viscosities, and Volumetric Properties of Binary Mixtures of 1,2-Propanediol + 1-Heptanol or 1-Hexanol and 1,2-Ethanediol + 2-Butanol or 2-Propanol at T = (298.15, 303.15, and 308.15) K
η	0.0163876	Pa×s	298.15	Densities, Viscosities, and Sound Speeds of Some Acetate Salts in Binary Mixtures of Tetrahydrofuran and Methanol at (303.15, 313.15, and 323.15) K
η	0.0167950	Pa×s	298.15	Density, Viscosity, and Excess Properties for 1,2-Diaminoethane + 1,2-Ethanediol at (298.15, 303.15, and 308.15) K
η	0.0174000	Pa×s	298.15	Densities and Viscosities of Propane-1,2,3-triol + Ethane-1,2-diol at T = (298.15 to 338.15) K
η	0.0137600	Pa×s	298.15	NCMS SOLV-DB
η	0.0174100	Pa×s	298.15	Viscosity of binary mixtures of 1-ethyl-3-methylimidazolium tetrafluoroborate ionic liquid with four organic solvents
η	0.0127314	Pa×s	303.15	Densities, Viscosities, and Volumetric Properties of Binary Mixtures of 1,2-Propanediol + 1-Heptanol or 1-Hexanol and 1,2-Ethanediol + 2-Butanol or 2-Propanol at T = (298.15, 303.15, and 308.15) K
η	0.0143300	Pa×s	303.15	Viscosity of binary mixtures of 1-ethyl-3-methylimidazolium tetrafluoroborate ionic liquid with four organic solvents
η	0.0133960	Pa×s	303.15	Density, Viscosity, and Excess Properties for 1,2-Diaminoethane + 1,2-Ethanediol at (298.15, 303.15, and 308.15) K
η	0.0138000	Pa×s	303.15	Densities and Viscosities of Propane-1,2,3-triol + Ethane-1,2-diol at T = (298.15 to 338.15) K
η	0.0107719	Pa×s	308.15	Densities, Viscosities, and Sound Speeds of Some Acetate Salts in Binary Mixtures of Tetrahydrofuran and Methanol at (303.15, 313.15, and 323.15) K
η	0.0106614	Pa×s	308.15	Densities, Viscosities, and Volumetric Properties of Binary Mixtures of 1,2-Propanediol + 1-Heptanol or 1-Hexanol and 1,2-Ethanediol + 2-Butanol or 2-Propanol at T = (298.15, 303.15, and 308.15) K
η	0.0115000	Pa×s	308.15	Densities and Viscosities of Propane-1,2,3-triol + Ethane-1,2-diol at T = (298.15 to 338.15) K
η	0.0113330	Pa×s	308.15	Density, Viscosity, and Excess Properties for 1,2-Diaminoethane + 1,2-Ethanediol at (298.15, 303.15, and 308.15) K
η	0.0111930	Pa×s	308.15	Excess Molar Volumes and Viscosities of Binary Mixtures of p-Cresol with Ethylene Glycol and Methanol at Different Temperature and Atmospheric Pressure
η	0.0111930	Pa×s	308.15	Densities and Viscosities of Binary Mixtures of m-Cresol with Ethylene Glycol or Methanol over Several Temperatures
η	0.0104780	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	0.0099250	Pa×s	312.46	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	0.0097400	Pa×s	313.05	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0094200	Pa×s	313.15	Densities and Viscosities of Propane-1,2,3-triol + Ethane-1,2-diol at T = (298.15 to 338.15) K
η	0.0094440	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of m-Cresol with Ethylene Glycol or Methanol over Several Temperatures
η	0.0094440	Pa×s	313.15	Excess Molar Volumes and Viscosities of Binary Mixtures of p-Cresol with Ethylene Glycol and Methanol at Different Temperature and Atmospheric Pressure
η	0.0100100	Pa×s	313.15	Viscosity of binary mixtures of 1-ethyl-3-methylimidazolium tetrafluoroborate ionic liquid with four organic solvents
η	0.0079720	Pa×s	318.15	Densities and Viscosities of Binary Mixtures of m-Cresol with Ethylene Glycol or Methanol over Several Temperatures
η	0.0081000	Pa×s	318.15	Densities and Viscosities of Propane-1,2,3-triol + Ethane-1,2-diol at T = (298.15 to 338.15) K
η	0.0077029	Pa×s	318.15	Densities, Viscosities, and Sound Speeds of Some Acetate Salts in Binary Mixtures of Tetrahydrofuran and Methanol at (303.15, 313.15, and 323.15) K
η	0.0079720	Pa×s	318.15	Excess Molar Volumes and Viscosities of Binary Mixtures of p-Cresol with Ethylene Glycol and Methanol at Different Temperature and Atmospheric Pressure
η	0.0067940	Pa×s	323.15	Excess Molar Volumes and Viscosities of Binary Mixtures of p-Cresol with Ethylene Glycol and Methanol at Different Temperature and Atmospheric Pressure
η	0.0067940	Pa×s	323.15	Densities and Viscosities of Binary Mixtures of m-Cresol with Ethylene Glycol or Methanol over Several Temperatures
η	0.0069500	Pa×s	323.15	Densities and Viscosities of Propane-1,2,3-triol + Ethane-1,2-diol at T = (298.15 to 338.15) K
η	0.0071210	Pa×s	323.15	Viscosity of binary mixtures of 1-ethyl-3-methylimidazolium tetrafluoroborate ionic liquid with four organic solvents
η	0.0059600	Pa×s	328.15	Densities and Viscosities of Propane-1,2,3-triol + Ethane-1,2-diol at T = (298.15 to 338.15) K
η	0.0052400	Pa×s	333.10	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0050650	Pa×s	333.15	Excess Molar Volumes and Viscosities of Binary Mixtures of p-Cresol with Ethylene Glycol and Methanol at Different Temperature and Atmospheric Pressure
η	0.0052200	Pa×s	333.15	Densities and Viscosities of Propane-1,2,3-triol + Ethane-1,2-diol at T = (298.15 to 338.15) K
η	0.0050650	Pa×s	333.15	Densities and Viscosities of Binary Mixtures of m-Cresol with Ethylene Glycol or Methanol over Several Temperatures
η	0.0053300	Pa×s	333.15	Viscosity of binary mixtures of 1-ethyl-3-methylimidazolium tetrafluoroborate ionic liquid with four organic solvents
η	0.0049490	Pa×s	334.87	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	0.0045300	Pa×s	338.15	Densities and Viscosities of Propane-1,2,3-triol + Ethane-1,2-diol at T = (298.15 to 338.15) K
η	0.0038790	Pa×s	343.15	Densities and Viscosities of Binary Mixtures of m-Cresol with Ethylene Glycol or Methanol over Several Temperatures
η	0.0038790	Pa×s	343.15	Excess Molar Volumes and Viscosities of Binary Mixtures of p-Cresol with Ethylene Glycol and Methanol at Different Temperature and Atmospheric Pressure
η	0.0041030	Pa×s	343.15	Viscosity of binary mixtures of 1-ethyl-3-methylimidazolium tetrafluoroborate ionic liquid with four organic solvents
η	0.0035170	Pa×s	349.24	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	0.0031300	Pa×s	353.05	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0032420	Pa×s	353.15	Viscosity of binary mixtures of 1-ethyl-3-methylimidazolium tetrafluoroborate ionic liquid with four organic solvents
η	0.0030580	Pa×s	353.15	Excess Molar Volumes and Viscosities of Binary Mixtures of p-Cresol with Ethylene Glycol and Methanol at Different Temperature and Atmospheric Pressure
η	0.0030580	Pa×s	353.15	Densities and Viscosities of Binary Mixtures of m-Cresol with Ethylene Glycol or Methanol over Several Temperatures
η	0.0023900	Pa×s	365.70	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	0.0020600	Pa×s	372.15	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0018150	Pa×s	380.82	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	0.0014400	Pa×s	392.45	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0014190	Pa×s	395.55	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	0.0010700	Pa×s	412.25	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0009600	Pa×s	421.70	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	0.0008670	Pa×s	428.30	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0006520	Pa×s	464.40	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
σcond	[0.00; 1.68e-04]	S/m	[293.15; 343.15]
σcond	1.50e-05	S/m	293.15	Permittivity and electrical conductivity of copper oxide nanofluid (12 nm) in water at different temperatures
σcond	2.90e-05	S/m	303.15	Permittivity and electrical conductivity of copper oxide nanofluid (12 nm) in water at different temperatures
σcond	0.00	S/m	303.15	Micellar Properties and Related Thermodynamic Parameters of the 14-6-14, 2Br- Gemini Surfactant in Water + Organic Solvent Mixed Media
σcond	4.60e-05	S/m	313.15	Permittivity and electrical conductivity of copper oxide nanofluid (12 nm) in water at different temperatures
σcond	8.00e-05	S/m	323.15	Permittivity and electrical conductivity of copper oxide nanofluid (12 nm) in water at different temperatures
σcond	1.21e-04	S/m	333.15	Permittivity and electrical conductivity of copper oxide nanofluid (12 nm) in water at different temperatures
σcond	1.68e-04	S/m	343.15	Permittivity and electrical conductivity of copper oxide nanofluid (12 nm) in water at different temperatures
εr	39.84		303.15	Dielectric constant and molecular association in binary mixtures of N,N-dimethylethanolamine with alcohols and amides
ΔfusH	[9.96; 11.62]	kJ/mol	[260.60; 260.80]
ΔfusH	9.96	kJ/mol	260.60	NIST
ΔfusH	9.96	kJ/mol	260.60	NIST
ΔfusH	9.96	kJ/mol	260.60	NIST
ΔfusH	11.62	kJ/mol	260.80	NIST
ΔfusH	11.60	kJ/mol	260.80	NIST
ΔfusH	11.62	kJ/mol	260.80	NIST
ΔvapH	[52.51; 68.00]	kJ/mol	[273.00; 470.50]
ΔvapH	61.90 ± 6.30	kJ/mol	273.00	NIST
ΔvapH	63.90	kJ/mol	298.15	Vaporization Enthalpies of the r,o-Alkanediols by Correlation Gas Chromatography
ΔvapH	62.40 ± 4.00	kJ/mol	345.50	NIST
ΔvapH	61.10	kJ/mol	383.00	NIST
ΔvapH	57.40	kJ/mol	385.50	NIST
ΔvapH	62.50	kJ/mol	390.50	NIST
ΔvapH	65.20	kJ/mol	398.00	NIST
ΔvapH	64.00	kJ/mol	398.00	NIST
ΔvapH	68.00 ± 2.00	kJ/mol	409.00	NIST
ΔvapH	61.10	kJ/mol	427.00	NIST
ΔvapH	57.30	kJ/mol	436.50	NIST
ΔvapH	52.51	kJ/mol	470.50	KDB
Pvap	[0.01; 101.32]	kPa	[298.15; 470.47]
Pvap	0.01	kPa	298.15	NCMS SOLV-DB
Pvap	0.02	kPa	303.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.02	kPa	306.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.03	kPa	307.70	Vapor Pressure Measurements of Hydroxyacetaldehyde and Hydroxyacetone in the Temperature Range (273 to 356) K
Pvap	0.03	kPa	308.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.03	kPa	310.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.04	kPa	312.60	Vapor Pressure Measurements of Hydroxyacetaldehyde and Hydroxyacetone in the Temperature Range (273 to 356) K
Pvap	0.04	kPa	313.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.05	kPa	316.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.06	kPa	316.50	Vapor Pressure Measurements of Hydroxyacetaldehyde and Hydroxyacetone in the Temperature Range (273 to 356) K
Pvap	0.06	kPa	318.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.06	kPa	318.80	Vapor Pressure Measurements of Hydroxyacetaldehyde and Hydroxyacetone in the Temperature Range (273 to 356) K
Pvap	0.07	kPa	320.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.08	kPa	322.10	Vapor Pressure Measurements of Hydroxyacetaldehyde and Hydroxyacetone in the Temperature Range (273 to 356) K
Pvap	0.08	kPa	323.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.11	kPa	326.10	Vapor Pressure Measurements of Hydroxyacetaldehyde and Hydroxyacetone in the Temperature Range (273 to 356) K
Pvap	0.11	kPa	326.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.12	kPa	328.10	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.12	kPa	328.20	Vapor Pressure Measurements of Hydroxyacetaldehyde and Hydroxyacetone in the Temperature Range (273 to 356) K
Pvap	0.15	kPa	331.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.22	kPa	333.15	Isothermal Vapor-Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Water + 1,2-Ethanediol and Propene + Acetophenone
Pvap	0.18	kPa	333.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.20	kPa	334.50	Vapor Pressure Measurements of Hydroxyacetaldehyde and Hydroxyacetone in the Temperature Range (273 to 356) K
Pvap	0.20	kPa	335.20	Vapor Pressure Measurements of Hydroxyacetaldehyde and Hydroxyacetone in the Temperature Range (273 to 356) K
Pvap	0.22	kPa	336.20	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.25	kPa	336.45	Determination and Modeling of Isobaric Vapor Liquid Equilibria for the Methylcarbamate + Methyl-N-phenyl Carbamate System at Different Pressures
Pvap	0.27	kPa	339.60	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.28	kPa	340.20	Vapor Pressure Measurements of Hydroxyacetaldehyde and Hydroxyacetone in the Temperature Range (273 to 356) K
Pvap	0.36	kPa	343.60	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.48	kPa	345.00	Determination and Modeling of Isobaric Vapor Liquid Equilibria for the Methylcarbamate + Methyl-N-phenyl Carbamate System at Different Pressures
Pvap	0.45	kPa	347.90	Vapor Pressure Measurements of Hydroxyacetaldehyde and Hydroxyacetone in the Temperature Range (273 to 356) K
Pvap	0.49	kPa	348.60	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.77	kPa	353.15	Isothermal Vapor-Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Water + 1,2-Ethanediol and Propene + Acetophenone
Pvap	0.68	kPa	353.60	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.90	kPa	355.15	Determination and Modeling of Isobaric Vapor Liquid Equilibria for the Methylcarbamate + Methyl-N-phenyl Carbamate System at Different Pressures
Pvap	0.92	kPa	358.60	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	0.90	kPa	359.20	Vapor Pressure Measurements of Hydroxyacetaldehyde and Hydroxyacetone in the Temperature Range (273 to 356) K
Pvap	1.24	kPa	363.60	Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
Pvap	1.48	kPa	367.90	Vapor Pressure Measurements of Hydroxyacetaldehyde and Hydroxyacetone in the Temperature Range (273 to 356) K
Pvap	1.69	kPa	369.25	Determination and Modeling of Isobaric Vapor Liquid Equilibria for the Methylcarbamate + Methyl-N-phenyl Carbamate System at Different Pressures
Pvap	1.95	kPa	373.40	Vapor Pressure Measurements of Hydroxyacetaldehyde and Hydroxyacetone in the Temperature Range (273 to 356) K
Pvap	2.13	kPa	374.45	Determination and Modeling of Isobaric Vapor Liquid Equilibria for the Methylcarbamate + Methyl-N-phenyl Carbamate System at Different Pressures
Pvap	2.66	kPa	378.95	Determination and Modeling of Isobaric Vapor Liquid Equilibria for the Methylcarbamate + Methyl-N-phenyl Carbamate System at Different Pressures
Pvap	3.57	kPa	384.45	Determination and Modeling of Isobaric Vapor Liquid Equilibria for the Methylcarbamate + Methyl-N-phenyl Carbamate System at Different Pressures
Pvap	3.47	kPa	384.50	Vapor Pressure Measurements of Hydroxyacetaldehyde and Hydroxyacetone in the Temperature Range (273 to 356) K
Pvap	3.92	kPa	386.15	Isobaric Vapor Liquid Equilibria for the Binary Mixtures Composed of Ethylene Glycol, 1,2-Propylene Glycol, 1,2-Butanediol, and 1,3-Butanediol at 10.00 kPa
Pvap	4.40	kPa	388.10	Determination and Modeling of Isobaric Vapor Liquid Equilibria for the Methylcarbamate + Methyl-N-phenyl Carbamate System at Different Pressures
Pvap	4.51	kPa	389.12	Isobaric Vapor Liquid Equilibria for the Binary Mixtures Composed of Ethylene Glycol, 1,2-Propylene Glycol, 1,2-Butanediol, and 1,3-Butanediol at 10.00 kPa
Pvap	4.78	kPa	389.95	Isobaric Vapor Liquid Equilibria for the Binary Mixtures Composed of Ethylene Glycol, 1,2-Propylene Glycol, 1,2-Butanediol, and 1,3-Butanediol at 10.00 kPa
Pvap	4.89	kPa	390.75	Isobaric Vapor Liquid Equilibria for the Binary Mixtures Composed of Ethylene Glycol, 1,2-Propylene Glycol, 1,2-Butanediol, and 1,3-Butanediol at 10.00 kPa
Pvap	5.33	kPa	391.45	Determination and Modeling of Isobaric Vapor Liquid Equilibria for the Methylcarbamate + Methyl-N-phenyl Carbamate System at Different Pressures
Pvap	6.01	kPa	394.56	Determination and Modeling of Isobaric Vapor Liquid Equilibria for the Methylcarbamate + Methyl-N-phenyl Carbamate System at Different Pressures
Pvap	6.08	kPa	395.25	Isobaric Vapor Liquid Equilibria for the Binary Mixtures Composed of Ethylene Glycol, 1,2-Propylene Glycol, 1,2-Butanediol, and 1,3-Butanediol at 10.00 kPa
Pvap	7.14	kPa	397.25	Determination and Modeling of Isobaric Vapor Liquid Equilibria for the Methylcarbamate + Methyl-N-phenyl Carbamate System at Different Pressures
Pvap	7.87	kPa	400.78	Isobaric Vapor Liquid Equilibria for the Binary Mixtures Composed of Ethylene Glycol, 1,2-Propylene Glycol, 1,2-Butanediol, and 1,3-Butanediol at 10.00 kPa
Pvap	8.37	kPa	402.15	Isobaric Vapor Liquid Equilibria for the Binary Mixtures Composed of Ethylene Glycol, 1,2-Propylene Glycol, 1,2-Butanediol, and 1,3-Butanediol at 10.00 kPa
Pvap	9.20	kPa	404.05	Determination and Modeling of Isobaric Vapor Liquid Equilibria for the Methylcarbamate + Methyl-N-phenyl Carbamate System at Different Pressures
Pvap	9.85	kPa	405.85	Isobaric Vapor Liquid Equilibria for the Binary Mixtures Composed of Ethylene Glycol, 1,2-Propylene Glycol, 1,2-Butanediol, and 1,3-Butanediol at 10.00 kPa
Pvap	10.00	kPa	406.09	Isobaric Vapor Liquid Equilibria for the Binary Mixtures Composed of Ethylene Glycol, 1,2-Propylene Glycol, 1,2-Butanediol, and 1,3-Butanediol at 10.00 kPa
Pvap	10.02	kPa	406.25	Isobaric Vapor Liquid Equilibria for the Binary Mixtures Composed of Ethylene Glycol, 1,2-Propylene Glycol, 1,2-Butanediol, and 1,3-Butanediol at 10.00 kPa
Pvap	11.34	kPa	408.25	Determination and Modeling of Isobaric Vapor Liquid Equilibria for the Methylcarbamate + Methyl-N-phenyl Carbamate System at Different Pressures
Pvap	11.42	kPa	409.30	Isobaric Vapor Liquid Equilibria for the Binary Mixtures Composed of Ethylene Glycol, 1,2-Propylene Glycol, 1,2-Butanediol, and 1,3-Butanediol at 10.00 kPa
Pvap	12.41	kPa	411.15	Isobaric Vapor Liquid Equilibria for the Binary Mixtures Composed of Ethylene Glycol, 1,2-Propylene Glycol, 1,2-Butanediol, and 1,3-Butanediol at 10.00 kPa
Pvap	12.85	kPa	411.85	Isobaric Vapor Liquid Equilibria for the Binary Mixtures Composed of Ethylene Glycol, 1,2-Propylene Glycol, 1,2-Butanediol, and 1,3-Butanediol at 10.00 kPa
Pvap	13.33	kPa	412.81	Isobaric Vapor-Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems
Pvap	13.85	kPa	413.85	Isobaric Vapor Liquid Equilibria for the Binary Mixtures Composed of Ethylene Glycol, 1,2-Propylene Glycol, 1,2-Butanediol, and 1,3-Butanediol at 10.00 kPa
Pvap	15.37	kPa	416.45	Isobaric Vapor Liquid Equilibria for the Binary Mixtures Composed of Ethylene Glycol, 1,2-Propylene Glycol, 1,2-Butanediol, and 1,3-Butanediol at 10.00 kPa
Pvap	20.00	kPa	420.74	Isobaric Vapor Liquid Equilibrium for the Binary System (Ethane-1,2-diol + Butan-1,2-diol) at (20, 30, and 40) kPa
Pvap	20.00	kPa	422.75	Vapor Liquid Equilibria for Three Binary Systems of N-Methylethanolamine, N-Methyldiethanolamine, and Ethylene Glycol at P = (40.0, 30.0, and 20.0) kPa
Pvap	20.00	kPa	422.78	Isobaric Vapor-Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems
Pvap	20.00	kPa	422.80	Vapor Liquid Equilibria for Three Binary Systems of N-Methylethanolamine, N-Methyldiethanolamine, and Ethylene Glycol at P = (40.0, 30.0, and 20.0) kPa
Pvap	26.66	kPa	430.26	Isobaric Vapor-Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems
Pvap	30.00	kPa	432.29	Isobaric Vapor Liquid Equilibrium for the Binary System (Ethane-1,2-diol + Butan-1,2-diol) at (20, 30, and 40) kPa
Pvap	30.00	kPa	433.66	Vapor Liquid Equilibria for Three Binary Systems of N-Methylethanolamine, N-Methyldiethanolamine, and Ethylene Glycol at P = (40.0, 30.0, and 20.0) kPa
Pvap	30.00	kPa	433.71	Vapor Liquid Equilibria for Three Binary Systems of N-Methylethanolamine, N-Methyldiethanolamine, and Ethylene Glycol at P = (40.0, 30.0, and 20.0) kPa
Pvap	33.33	kPa	436.37	Isobaric Vapor-Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems
Pvap	40.00	kPa	440.15	Isobaric Vapor Liquid Equilibrium for the Binary System (Ethane-1,2-diol + Butan-1,2-diol) at (20, 30, and 40) kPa
Pvap	40.00	kPa	441.50	Isobaric Vapor-Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems
Pvap	40.00	kPa	441.66	Vapor Liquid Equilibria for Three Binary Systems of N-Methylethanolamine, N-Methyldiethanolamine, and Ethylene Glycol at P = (40.0, 30.0, and 20.0) kPa
Pvap	40.00	kPa	441.70	Vapor Liquid Equilibria for Three Binary Systems of N-Methylethanolamine, N-Methyldiethanolamine, and Ethylene Glycol at P = (40.0, 30.0, and 20.0) kPa
Pvap	46.66	kPa	445.96	Isobaric Vapor-Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems
Pvap	53.33	kPa	449.93	Isobaric Vapor-Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems
Pvap	60.00	kPa	453.52	Isobaric Vapor-Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems
Pvap	66.66	kPa	456.78	Isobaric Vapor-Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems
Pvap	73.33	kPa	459.79	Isobaric Vapor-Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems
Pvap	79.99	kPa	462.58	Isobaric Vapor-Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems
Pvap	86.66	kPa	465.18	Isobaric Vapor-Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems
Pvap	93.32	kPa	467.62	Isobaric Vapor-Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems
Pvap	101.32	kPa	469.15	Cosolvent Selection for Benzene-Cyclohexane Separation in Extractive Distillation
Pvap	98.66	kPa	469.48	Isobaric Vapor-Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems
Pvap	100.40	kPa	470.02	Isobaric Vapor-Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems
Pvap	101.30	kPa	470.22	Investigation on Thermodynamics in Separation for Ethylene Glycol + Neopentyl Glycol System by Azeotropic Distillation
Pvap	101.30	kPa	470.47	Vapor Liquid Equilibria for Three Binary Systems of N-Methylethanolamine, N-Methyldiethanolamine, and Ethylene Glycol at P = (40.0, 30.0, and 20.0) kPa
n0	[1.42460; 1.43280]		[293.15; 308.15]
n0	1.43184		293.15	Liquid-Liquid Equilibria of (Limonene + Linalool + Ethylene Glycol or Diethylene Glycol or Triethylene Glycol or 1,2-Propylene Glycol) Ternary Systems
n0	1.43180		293.15	Experimental Vapor-Liquid Equilibrium Data for Binary Mixtures of Methyldiethanolamine in Water and Ethylene Glycol under Vacuum
n0	1.43280		293.15	Isobaric Vapor - Liquid Equilibria for the Ternary System of 2-Methyl-1-butanol, 3-Methyl-1-butanol, and Ethylene Glycol at 101.3 kPa
n0	1.43230		293.15	Densities, Excess Molar Volumes, and Isobaric Thermal Expansibilities for 1,2-Ethanediol + 1-Butanol, or 1-Hexanol, or 1-Octanol in the Temperature Range from (293.15 to 313.15) K
n0	1.43040		298.15	Density and refractive index in mixtures of ionic liquids and organic solvents: Correlations and predictions
n0	1.43070		298.15	Thermodynamic and transport properties of (1,2-ethanediol + 1-nonanol) at temperatures from (298.15 to 313.15) K
n0	1.43159		298.15	Phase Equilibrium Involving Xylose, Water, and Ethylene Glycol or 1,2-Propylene Glycol at Different Temperatures
n0	1.43070		298.15	Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethanediol, + Hexane, + Tributylamine, or + Triethylamine at (298.15, 303.15, and 308.15) K
n0	1.43060		298.15	Liquid liquid equilibria of the systems dipropyl ether + n-propanol +water and dipropyl ether + n-propanol + ethylene glycol at different temperatures
n0	1.43090		298.15	Densities, Excess Molar Volumes, and Isobaric Thermal Expansibilities for 1,2-Ethanediol + 1-Butanol, or 1-Hexanol, or 1-Octanol in the Temperature Range from (293.15 to 313.15) K
n0	1.43100		298.15	NCMS SOLV-DB
n0	1.42690		303.15	Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethanediol, + Hexane, + Tributylamine, or + Triethylamine at (298.15, 303.15, and 308.15) K
n0	1.42460		308.15	Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethanediol, + Hexane, + Tributylamine, or + Triethylamine at (298.15, 303.15, and 308.15) K
ρl	[1056.40; 1127.43]	kg/m3	[273.15; 373.15]
ρl	1127.43	kg/m3	273.15	Solubilities of CO2 in, densities and kinematic viscosities of poly(propylene glycol) diglycidyl ether and poly(ethylene glycol) monooleate
ρl	1127.05	kg/m3	273.15	Density of Working Liquids for Diffusion Vacuum Pumps
ρl	1125.17	kg/m3	276.15	Volumetric Properties of Binary Mixtures of 2,4,6-Trimethylpyridine with 1,2-Ethanediol, Methanol, and Water, and the Association Energies of the O-H***N Bonded Complexes
ρl	1124.48	kg/m3	277.15	Volumetric Properties of Binary Mixtures of 2,4,6-Trimethylpyridine with 1,2-Ethanediol, Methanol, and Water, and the Association Energies of the O-H***N Bonded Complexes
ρl	1123.77	kg/m3	278.15	Densities and Volumetric Properties of Ethylene Glycol + Dimethylsulfoxide Mixtures at Temperatures of (278.15 to 323.15) K and Pressures of (0.1 to 100) MPa
ρl	1123.80	kg/m3	278.15	Liquid phase PVTx properties of binary mixtures of (water + ethylene glycol) in the range from 278.15 to 323.15 K and from 0.1 to 100 MPa. I. Experimental results, partial and excess thermodynamics properties
ρl	1120.35	kg/m3	283.15	Solubilities of CO2 in, densities and kinematic viscosities of poly(propylene glycol) diglycidyl ether and poly(ethylene glycol) monooleate
ρl	1119.29	kg/m3	283.15	Densities and Excess Properties of Primary Amines in Alcoholic Solutions
ρl	1120.39	kg/m3	283.15	Excess volumes and excess heat capacities for alkanediol + water systems in the temperature interval (283.15-313.15) K
ρl	1120.32	kg/m3	283.15	Volumetric Properties of Binary Mixtures of 2,4,6-Trimethylpyridine with 1,2-Ethanediol, Methanol, and Water, and the Association Energies of the O-H***N Bonded Complexes
ρl	1120.50	kg/m3	283.15	Density of Working Liquids for Diffusion Vacuum Pumps
ρl	1120.20	kg/m3	283.15	Thermophysical properties of glycols and glymes
ρl	1120.00	kg/m3	283.15	Density and Viscosity of the Nonaqueous and Aqueous Mixtures of Methyldiethanolamine and Monoethylene Glycol at Temperatures from 283.15 to 353.15 K
ρl	1116.83	kg/m3	288.15	Densities and Volumetric Properties of Ethylene Glycol + Dimethylsulfoxide Mixtures at Temperatures of (278.15 to 323.15) K and Pressures of (0.1 to 100) MPa
ρl	1116.80	kg/m3	288.15	Thermophysical properties of glycols and glymes
ρl	1116.85	kg/m3	288.15	Liquid phase PVTx properties of binary mixtures of (water + ethylene glycol) in the range from 278.15 to 323.15 K and from 0.1 to 100 MPa. I. Experimental results, partial and excess thermodynamics properties
ρl	1117.01	kg/m3	288.15	Volume-related solvation and pair interaction parameters for dilute solutions of urea and tetramethylurea in ethylene glycol between 288.15 K and 328.15 K: A comparative analysis
ρl	1116.86	kg/m3	288.15	Volumetric Properties of Binary Mixtures of 2,4,6-Trimethylpyridine with 1,2-Ethanediol, Methanol, and Water, and the Association Energies of the O-H***N Bonded Complexes
ρl	1118.20	kg/m3	288.15	Thermophysical properties of glycols and glymes
ρl	1116.84	kg/m3	288.15	Effect of structural alteration of ionic liquid on their bulk and molecular level interactions with ethylene glycol
ρl	1114.00	kg/m3	293.00	KDB
ρl	1121.00	kg/m3	293.15	Interfacial Properties, Densities, and Contact Angles of Task Specific Ionic Liquids
ρl	1112.37	kg/m3	293.15	Densities and Excess Properties of Primary Amines in Alcoholic Solutions
ρl	1113.00	kg/m3	293.15	Thermodynamic and transport properties of acetonitrile + alkanediols liquid mixtures at different temperatures, experimental measurements and modeling
ρl	1113.34	kg/m3	293.15	Excess volumes and excess heat capacities for alkanediol + water systems in the temperature interval (283.15-313.15) K
ρl	1113.35	kg/m3	293.15	Effect of structural alteration of ionic liquid on their bulk and molecular level interactions with ethylene glycol
ρl	1113.55	kg/m3	293.15	Densities and Excess Molar Volumes for Binary Mixtures of 1,4-Butanediol + 1,2-Propanediol, + 1,3-Propanediol, and + Ethane-1,2-diol from (293.15 to 328.15) K
ρl	1113.84	kg/m3	293.15	Density of Working Liquids for Diffusion Vacuum Pumps
ρl	1113.37	kg/m3	293.15	Volumetric Properties of Binary Mixtures of 2,4,6-Trimethylpyridine with 1,2-Ethanediol, Methanol, and Water, and the Association Energies of the O-H***N Bonded Complexes
ρl	1113.45	kg/m3	293.15	Density and Refractive Index of Binary Mixtures of Two 1-Alkyl-3-methylimidazolium Ionic Liquids with 1,4-Dioxane and Ethylene Glycol
ρl	1113.30	kg/m3	293.15	Density and refractive index measurements of transition-temperature mixture (deep eutectic analogues) based on potassium carbonate with dual hydrogen bond donors for CO2 capture
ρl	1114.60	kg/m3	293.15	Thermophysical properties of glycols and glymes
ρl	1113.23	kg/m3	293.15	Transport properties of 2:2 symmetrical electrolytes in (water + ethylene glycol) binary mixtures at T = 293.15 K
ρl	1113.72	kg/m3	293.15	Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
ρl	1113.30	kg/m3	293.15	Thermophysical properties of glycols and glymes
ρl	1113.25	kg/m3	293.15	Solubilities of CO2 in, densities and kinematic viscosities of poly(propylene glycol) diglycidyl ether and poly(ethylene glycol) monooleate
ρl	1113.70	kg/m3	293.15	Excess Molar Volumes, Viscosities, and Heat Capacities for the Mixtures of Ethylene Glycol + Water from 273.15 K to 353.15 K
ρl	1120.70	kg/m3	295.00	New device for fast measuring surface tension, density and viscosity of liquids
ρl	1109.87	kg/m3	298.14	Volumetric Properties of Binary Mixtures of 2,4,6-Trimethylpyridine with 1,2-Ethanediol, Methanol, and Water, and the Association Energies of the O-H***N Bonded Complexes
ρl	1109.70	kg/m3	298.15	Thermodynamic study on some alkanediol solutions: measurement and molecular modeling
ρl	1109.82	kg/m3	298.15	Isobaric Vapor Liquid Equilibrium for Two Binary Systems{Propane-1,2-diol + Ethane-1,2-diol and Propane-1,2-diol + Butane-1,2-diol} at p = (10.0, 20.0, and 40.0) kPa
ρl	1109.86	kg/m3	298.15	Densities and Excess Molar Volumes for Binary Mixtures of 1,4-Butanediol + 1,2-Propanediol, + 1,3-Propanediol, and + Ethane-1,2-diol from (293.15 to 328.15) K
ρl	1109.70	kg/m3	298.15	Investigation on some thermophysical properties of poly(ethylene glycol) binary mixtures at different temperatures
ρl	1109.80	kg/m3	298.15	Thermodynamic Study of Binary Mixtures Containing Glycols or Polyethylene Glycols + Benzyl Alcohol at 308.15 K
ρl	1110.08	kg/m3	298.15	Volume-related solvation and pair interaction parameters for dilute solutions of urea and tetramethylurea in ethylene glycol between 288.15 K and 328.15 K: A comparative analysis
ρl	1110.20	kg/m3	298.15	Solubility for dilute sulfur dioxide in binary mixtures of N,N-dimethylformamide + Ethylene Glycol at T = 308.15 Kand p = 122.66 kPa
ρl	1109.89	kg/m3	298.15	Viscosity and density data for the ternary system water(1) ethanol(2) ethylene glycol(3) between 298.15 K and 328.15 K
ρl	1111.10	kg/m3	298.15	Thermophysical properties of glycols and glymes
ρl	1109.90	kg/m3	298.15	Density and Viscosity of the Nonaqueous and Aqueous Mixtures of Methyldiethanolamine and Monoethylene Glycol at Temperatures from 283.15 to 353.15 K
ρl	1109.85	kg/m3	298.15	Effect of structural alteration of ionic liquid on their bulk and molecular level interactions with ethylene glycol
ρl	1110.00	kg/m3	298.15	Activity coefficients at infinite dilution of hydrocarbons in glycols: Experimental data and thermodynamic modeling with the GCA-EoS
ρl	1109.71	kg/m3	298.15	Surface Properties of Binary Mixtures of Ethylene Glycol with a Series of Aliphatic Alcohols (1-Pentanol, 1-Hexanol, and 1-Heptanol)
ρl	1109.00	kg/m3	298.15	Thermodynamic and transport properties of acetonitrile + alkanediols liquid mixtures at different temperatures, experimental measurements and modeling
ρl	1109.80	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	1109.79	kg/m3	298.15	Excess volumes and excess heat capacities for alkanediol + water systems in the temperature interval (283.15-313.15) K
ρl	1109.80	kg/m3	298.15	Density and refractive index measurements of transition-temperature mixture (deep eutectic analogues) based on potassium carbonate with dual hydrogen bond donors for CO2 capture
ρl	1109.88	kg/m3	298.15	Liquid phase PVTx properties of binary mixtures of (water + ethylene glycol) in the range from 278.15 to 323.15 K and from 0.1 to 100 MPa. I. Experimental results, partial and excess thermodynamics properties
ρl	1109.90	kg/m3	298.15	Phase equilibria for the ternary systems ethanol, water + ethylene glycol or + glycerol at 101.3 kPa
ρl	1110.20	kg/m3	298.15	Solubility Properties and Spectral Characterization of Dilute SO2 in Binary Mixtures of Urea + Ethylene Glycol
ρl	1107.92	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	1109.83	kg/m3	298.15	Densities and Volumetric Properties of Ethylene Glycol + Dimethylsulfoxide Mixtures at Temperatures of (278.15 to 323.15) K and Pressures of (0.1 to 100) MPa
ρl	1109.96	kg/m3	298.15	Density and Refractive Index of Binary Mixtures of Two 1-Alkyl-3-methylimidazolium Ionic Liquids with 1,4-Dioxane and Ethylene Glycol
ρl	1109.80	kg/m3	298.15	Thermophysical properties of glycols and glymes
ρl	1109.60	kg/m3	298.15	Solubility of Carbonyl Sulfide in Aqueous Solutions of Ethylene Glycol at Temperatures from (308.15 K to 323.15) K
ρl	1109.90	kg/m3	298.15	Binary liquid liquid equilibrium in the systems containing monofunctional benzene derivates and 1,2-ethanediol
ρl	1109.90	kg/m3	298.15	Revision of the volumetric method for measurements of liquid liquid equilibria in binary systems
ρl	1110.22	kg/m3	298.15	Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
ρl	1109.90	kg/m3	298.15	Liquid-Liquid Equilibrium in Ternary Systems Containing Ethylene Glycol, Monofunctional Benzene Derivative, and Ethyl Acetate
ρl	1106.26	kg/m3	303.15	Solubilities of CO2 in, densities and kinematic viscosities of poly(propylene glycol) diglycidyl ether and poly(ethylene glycol) monooleate
ρl	1107.60	kg/m3	303.15	Thermophysical properties of glycols and glymes
ρl	1106.36	kg/m3	303.15	Volumetric Properties of Binary Mixtures of 2,4,6-Trimethylpyridine with 1,2-Ethanediol, Methanol, and Water, and the Association Energies of the O-H***N Bonded Complexes
ρl	1106.54	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	1106.71	kg/m3	303.15	Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
ρl	1105.39	kg/m3	303.15	Densities and Excess Properties of Primary Amines in Alcoholic Solutions
ρl	1106.30	kg/m3	303.15	Thermophysical properties of glycols and glymes
ρl	1106.45	kg/m3	303.15	Density and Refractive Index of Binary Mixtures of Two 1-Alkyl-3-methylimidazolium Ionic Liquids with 1,4-Dioxane and Ethylene Glycol
ρl	1106.23	kg/m3	303.15	Excess volumes and excess heat capacities for alkanediol + water systems in the temperature interval (283.15-313.15) K
ρl	1106.30	kg/m3	303.15	Density and refractive index measurements of transition-temperature mixture (deep eutectic analogues) based on potassium carbonate with dual hydrogen bond donors for CO2 capture
ρl	1106.33	kg/m3	303.15	Effect of structural alteration of ionic liquid on their bulk and molecular level interactions with ethylene glycol
ρl	1106.00	kg/m3	303.15	Thermodynamic and transport properties of acetonitrile + alkanediols liquid mixtures at different temperatures, experimental measurements and modeling
ρl	1106.60	kg/m3	303.15	Solubility Properties and Spectral Characterization of Dilute SO2 in Binary Mixtures of Urea + Ethylene Glycol
ρl	1107.07	kg/m3	303.15	Density of Working Liquids for Diffusion Vacuum Pumps
ρl	1106.60	kg/m3	303.15	Solubility for dilute sulfur dioxide in binary mixtures of N,N-dimethylformamide + Ethylene Glycol at T = 308.15 Kand p = 122.66 kPa
ρl	1106.30	kg/m3	303.15	Measurements and correlations of solubility of N2O in and density, viscosity of partially CO2 loaded water-lean amino acid salts
ρl	1106.82	kg/m3	303.15	Densities and Excess Molar Volumes for Binary Mixtures of 1,4-Butanediol + 1,2-Propanediol, + 1,3-Propanediol, and + Ethane-1,2-diol from (293.15 to 328.15) K
ρl	1106.00	kg/m3	303.15	Investigation on some thermophysical properties of poly(ethylene glycol) binary mixtures at different temperatures
ρl	1106.00	kg/m3	303.15	Thermodynamic study on some alkanediol solutions: measurement and molecular modeling
ρl	1106.38	kg/m3	303.15	Viscosity and density data for the ternary system water(1) ethanol(2) ethylene glycol(3) between 298.15 K and 328.15 K
ρl	1103.20	kg/m3	303.15	Excess Molar Volumes, Viscosities, and Heat Capacities for the Mixtures of Ethylene Glycol + Water from 273.15 K to 353.15 K
ρl	1103.08	kg/m3	308.15	Volume-related solvation and pair interaction parameters for dilute solutions of urea and tetramethylurea in ethylene glycol between 288.15 K and 328.15 K: A comparative analysis
ρl	1102.86	kg/m3	308.15	Viscosity and density data for the ternary system water(1) ethanol(2) ethylene glycol(3) between 298.15 K and 328.15 K
ρl	1103.00	kg/m3	308.15	Solubility Properties and Spectral Characterization of Dilute SO2 in Binary Mixtures of Urea + Ethylene Glycol
ρl	1102.93	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	1102.93	kg/m3	308.15	Excess Molar Enthalpies of Binary Mixtures Containing Glycols or Polyglycols + Dimethyl Sulfoxide at 308.15 K
ρl	1102.70	kg/m3	308.15	Thermodynamic study on some alkanediol solutions: measurement and molecular modeling
ρl	1102.90	kg/m3	308.15	Molecular interactions of a,x-alkanediols in pyrrolidin-2-one: Thermophysical and spectroscopic measurements
ρl	1102.90	kg/m3	308.15	Structural and interactional studies of homologous series of a,x-alkanediols in N,N-dimethylformamide
ρl	1103.30	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	1102.93	kg/m3	308.15	Thermodynamic Study of Binary Mixtures Containing Glycols or Polyethylene Glycols + Benzyl Alcohol at 308.15 K
ρl	1102.70	kg/m3	308.15	Investigation on some thermophysical properties of poly(ethylene glycol) binary mixtures at different temperatures
ρl	1104.10	kg/m3	308.15	Thermophysical properties of glycols and glymes
ρl	1103.20	kg/m3	308.15	Densities and Excess Molar Volumes for Binary Mixtures of 1,4-Butanediol + 1,2-Propanediol, + 1,3-Propanediol, and + Ethane-1,2-diol from (293.15 to 328.15) K
ρl	1102.80	kg/m3	308.15	Effect of structural alteration of ionic liquid on their bulk and molecular level interactions with ethylene glycol
ρl	1103.00	kg/m3	308.15	Solubility for dilute sulfur dioxide in binary mixtures of N,N-dimethylformamide + Ethylene Glycol at T = 308.15 Kand p = 122.66 kPa
ρl	1102.93	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	1102.80	kg/m3	308.15	Density and refractive index measurements of transition-temperature mixture (deep eutectic analogues) based on potassium carbonate with dual hydrogen bond donors for CO2 capture
ρl	1102.84	kg/m3	308.15	Liquid phase PVTx properties of binary mixtures of (water + ethylene glycol) in the range from 278.15 to 323.15 K and from 0.1 to 100 MPa. I. Experimental results, partial and excess thermodynamics properties
ρl	1102.70	kg/m3	308.15	Thermophysical properties of glycols and glymes
ρl	1102.81	kg/m3	308.15	Densities and Volumetric Properties of Ethylene Glycol + Dimethylsulfoxide Mixtures at Temperatures of (278.15 to 323.15) K and Pressures of (0.1 to 100) MPa
ρl	1103.19	kg/m3	308.15	Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
ρl	1102.84	kg/m3	308.15	Volumetric Properties of Binary Mixtures of 2,4,6-Trimethylpyridine with 1,2-Ethanediol, Methanol, and Water, and the Association Energies of the O-H***N Bonded Complexes
ρl	1102.70	kg/m3	308.15	Measurements and correlations of solubility of N2O in and density, viscosity of partially CO2 loaded water-lean amino acid salts
ρl	1099.30	kg/m3	313.15	Solubility for dilute sulfur dioxide in binary mixtures of N,N-dimethylformamide + Ethylene Glycol at T = 308.15 Kand p = 122.66 kPa
ρl	1099.30	kg/m3	313.15	Solubility Properties and Spectral Characterization of Dilute SO2 in Binary Mixtures of Urea + Ethylene Glycol
ρl	1099.30	kg/m3	313.15	Volumetric Properties of Binary Mixtures of 2,4,6-Trimethylpyridine with 1,2-Ethanediol, Methanol, and Water, and the Association Energies of the O-H***N Bonded Complexes
ρl	1098.34	kg/m3	313.15	Densities and Excess Properties of Primary Amines in Alcoholic Solutions
ρl	1099.07	kg/m3	313.15	Excess volumes and excess heat capacities for alkanediol + water systems in the temperature interval (283.15-313.15) K
ρl	1098.90	kg/m3	313.15	Solubilities of CO2 in, and Densities and Viscosities of, the Piperazine + 1-Ethyl-3-methyl-imidazolium Acetate + H2O System
ρl	1099.20	kg/m3	313.15	Solubilities of CO2 in, densities and kinematic viscosities of poly(propylene glycol) diglycidyl ether and poly(ethylene glycol) monooleate
ρl	1099.38	kg/m3	313.15	Density and Refractive Index of Binary Mixtures of Two 1-Alkyl-3-methylimidazolium Ionic Liquids with 1,4-Dioxane and Ethylene Glycol
ρl	1099.20	kg/m3	313.15	Thermophysical properties of glycols and glymes
ρl	1093.60	kg/m3	313.15	Excess Molar Volumes, Viscosities, and Heat Capacities for the Mixtures of Ethylene Glycol + Water from 273.15 K to 353.15 K
ρl	1099.80	kg/m3	313.15	Densities and Excess Molar Volumes for Binary Mixtures of 1,4-Butanediol + 1,2-Propanediol, + 1,3-Propanediol, and + Ethane-1,2-diol from (293.15 to 328.15) K
ρl	1099.26	kg/m3	313.15	Effect of structural alteration of ionic liquid on their bulk and molecular level interactions with ethylene glycol
ρl	1099.20	kg/m3	313.15	Measurements and correlations of solubility of N2O in and density, viscosity of partially CO2 loaded water-lean amino acid salts
ρl	1099.31	kg/m3	313.15	Viscosity and density data for the ternary system water(1) ethanol(2) ethylene glycol(3) between 298.15 K and 328.15 K
ρl	1099.20	kg/m3	313.15	Density and refractive index measurements of transition-temperature mixture (deep eutectic analogues) based on potassium carbonate with dual hydrogen bond donors for CO2 capture
ρl	1099.10	kg/m3	313.15	Density and Viscosity of the Nonaqueous and Aqueous Mixtures of Methyldiethanolamine and Monoethylene Glycol at Temperatures from 283.15 to 353.15 K
ρl	1100.19	kg/m3	313.15	Density of Working Liquids for Diffusion Vacuum Pumps
ρl	1100.50	kg/m3	313.15	Thermophysical properties of glycols and glymes
ρl	1095.69	kg/m3	318.15	Effect of structural alteration of ionic liquid on their bulk and molecular level interactions with ethylene glycol
ρl	1095.80	kg/m3	318.15	Solubility for dilute sulfur dioxide in binary mixtures of N,N-dimethylformamide + Ethylene Glycol at T = 308.15 Kand p = 122.66 kPa
ρl	1095.80	kg/m3	318.15	Solubility Properties and Spectral Characterization of Dilute SO2 in Binary Mixtures of Urea + Ethylene Glycol
ρl	1095.75	kg/m3	318.15	Viscosity and density data for the ternary system water(1) ethanol(2) ethylene glycol(3) between 298.15 K and 328.15 K
ρl	1097.00	kg/m3	318.15	Thermophysical properties of glycols and glymes
ρl	1095.60	kg/m3	318.15	Measurements and correlations of solubility of N2O in and density, viscosity of partially CO2 loaded water-lean amino acid salts
ρl	1095.70	kg/m3	318.15	Density and refractive index measurements of transition-temperature mixture (deep eutectic analogues) based on potassium carbonate with dual hydrogen bond donors for CO2 capture
ρl	1096.23	kg/m3	318.15	Densities and Excess Molar Volumes for Binary Mixtures of 1,4-Butanediol + 1,2-Propanediol, + 1,3-Propanediol, and + Ethane-1,2-diol from (293.15 to 328.15) K
ρl	1096.00	kg/m3	318.15	Volume-related solvation and pair interaction parameters for dilute solutions of urea and tetramethylurea in ethylene glycol between 288.15 K and 328.15 K: A comparative analysis
ρl	1091.70	kg/m3	323.15	Solubilities of CO2 in, and Densities and Viscosities of, the Piperazine + 1-Ethyl-3-methyl-imidazolium Acetate + H2O System
ρl	1092.59	kg/m3	323.15	Densities and Excess Molar Volumes for Binary Mixtures of 1,4-Butanediol + 1,2-Propanediol, + 1,3-Propanediol, and + Ethane-1,2-diol from (293.15 to 328.15) K
ρl	1093.20	kg/m3	323.15	Density of Working Liquids for Diffusion Vacuum Pumps
ρl	1092.10	kg/m3	323.15	Measurements and correlations of solubility of N2O in and density, viscosity of partially CO2 loaded water-lean amino acid salts
ρl	1092.10	kg/m3	323.15	Thermophysical properties of glycols and glymes
ρl	1084.70	kg/m3	323.15	Excess Molar Volumes, Viscosities, and Heat Capacities for the Mixtures of Ethylene Glycol + Water from 273.15 K to 353.15 K
ρl	1092.10	kg/m3	323.15	Density and refractive index measurements of transition-temperature mixture (deep eutectic analogues) based on potassium carbonate with dual hydrogen bond donors for CO2 capture
ρl	1092.24	kg/m3	323.15	Density and Refractive Index of Binary Mixtures of Two 1-Alkyl-3-methylimidazolium Ionic Liquids with 1,4-Dioxane and Ethylene Glycol
ρl	1091.60	kg/m3	323.15	Density and Viscosity of the Nonaqueous and Aqueous Mixtures of Methyldiethanolamine and Monoethylene Glycol at Temperatures from 283.15 to 353.15 K
ρl	1092.12	kg/m3	323.15	Densities and Volumetric Properties of Ethylene Glycol + Dimethylsulfoxide Mixtures at Temperatures of (278.15 to 323.15) K and Pressures of (0.1 to 100) MPa
ρl	1092.07	kg/m3	323.15	Solubilities of CO2 in, densities and kinematic viscosities of poly(propylene glycol) diglycidyl ether and poly(ethylene glycol) monooleate
ρl	1092.14	kg/m3	323.15	Liquid phase PVTx properties of binary mixtures of (water + ethylene glycol) in the range from 278.15 to 323.15 K and from 0.1 to 100 MPa. I. Experimental results, partial and excess thermodynamics properties
ρl	1093.40	kg/m3	323.15	Thermophysical properties of glycols and glymes
ρl	1092.16	kg/m3	323.15	Viscosity and density data for the ternary system water(1) ethanol(2) ethylene glycol(3) between 298.15 K and 328.15 K
ρl	1091.21	kg/m3	323.15	Densities and Excess Properties of Primary Amines in Alcoholic Solutions
ρl	1088.66	kg/m3	328.15	Densities and Excess Molar Volumes for Binary Mixtures of 1,4-Butanediol + 1,2-Propanediol, + 1,3-Propanediol, and + Ethane-1,2-diol from (293.15 to 328.15) K
ρl	1089.80	kg/m3	328.15	Thermophysical properties of glycols and glymes
ρl	1088.40	kg/m3	328.15	Measurements and correlations of solubility of N2O in and density, viscosity of partially CO2 loaded water-lean amino acid salts
ρl	1088.50	kg/m3	328.15	Density and refractive index measurements of transition-temperature mixture (deep eutectic analogues) based on potassium carbonate with dual hydrogen bond donors for CO2 capture
ρl	1088.56	kg/m3	328.15	Viscosity and density data for the ternary system water(1) ethanol(2) ethylene glycol(3) between 298.15 K and 328.15 K
ρl	1088.83	kg/m3	328.15	Volume-related solvation and pair interaction parameters for dilute solutions of urea and tetramethylurea in ethylene glycol between 288.15 K and 328.15 K: A comparative analysis
ρl	1084.80	kg/m3	333.15	Measurements and correlations of solubility of N2O in and density, viscosity of partially CO2 loaded water-lean amino acid salts
ρl	1084.90	kg/m3	333.15	Density and refractive index measurements of transition-temperature mixture (deep eutectic analogues) based on potassium carbonate with dual hydrogen bond donors for CO2 capture
ρl	1084.80	kg/m3	333.15	Thermophysical properties of glycols and glymes
ρl	1086.20	kg/m3	333.15	Thermophysical properties of glycols and glymes
ρl	1086.11	kg/m3	333.15	Density of Working Liquids for Diffusion Vacuum Pumps
ρl	1083.99	kg/m3	333.15	Densities and Excess Properties of Primary Amines in Alcoholic Solutions
ρl	1085.00	kg/m3	333.15	Density and Viscosity of the Nonaqueous and Aqueous Mixtures of Methyldiethanolamine and Monoethylene Glycol at Temperatures from 283.15 to 353.15 K
ρl	1076.40	kg/m3	333.15	Excess Molar Volumes, Viscosities, and Heat Capacities for the Mixtures of Ethylene Glycol + Water from 273.15 K to 353.15 K
ρl	1085.00	kg/m3	333.15	Density and Refractive Index of Binary Mixtures of Two 1-Alkyl-3-methylimidazolium Ionic Liquids with 1,4-Dioxane and Ethylene Glycol
ρl	1084.20	kg/m3	333.15	Solubilities of CO2 in, and Densities and Viscosities of, the Piperazine + 1-Ethyl-3-methyl-imidazolium Acetate + H2O System
ρl	1084.84	kg/m3	333.15	Solubilities of CO2 in, densities and kinematic viscosities of poly(propylene glycol) diglycidyl ether and poly(ethylene glycol) monooleate
ρl	1082.60	kg/m3	338.15	Thermophysical properties of glycols and glymes
ρl	1081.20	kg/m3	338.15	Measurements and correlations of solubility of N2O in and density, viscosity of partially CO2 loaded water-lean amino acid salts
ρl	1081.20	kg/m3	338.15	Density and refractive index measurements of transition-temperature mixture (deep eutectic analogues) based on potassium carbonate with dual hydrogen bond donors for CO2 capture
ρl	1078.90	kg/m3	343.15	Thermophysical properties of glycols and glymes
ρl	1067.50	kg/m3	343.15	Excess Molar Volumes, Viscosities, and Heat Capacities for the Mixtures of Ethylene Glycol + Water from 273.15 K to 353.15 K
ρl	1077.65	kg/m3	343.15	Density and Refractive Index of Binary Mixtures of Two 1-Alkyl-3-methylimidazolium Ionic Liquids with 1,4-Dioxane and Ethylene Glycol
ρl	1077.50	kg/m3	343.15	Measurements and correlations of solubility of N2O in and density, viscosity of partially CO2 loaded water-lean amino acid salts
ρl	1078.10	kg/m3	343.15	Solubilities of CO2 in, and Densities and Viscosities of, the Piperazine + 1-Ethyl-3-methyl-imidazolium Acetate + H2O System
ρl	1077.60	kg/m3	343.15	Density and Viscosity of the Nonaqueous and Aqueous Mixtures of Methyldiethanolamine and Monoethylene Glycol at Temperatures from 283.15 to 353.15 K
ρl	1076.65	kg/m3	343.15	Densities and Excess Properties of Primary Amines in Alcoholic Solutions
ρl	1077.50	kg/m3	343.15	Thermophysical properties of glycols and glymes
ρl	1077.50	kg/m3	343.15	Density and refractive index measurements of transition-temperature mixture (deep eutectic analogues) based on potassium carbonate with dual hydrogen bond donors for CO2 capture
ρl	1078.91	kg/m3	343.15	Density of Working Liquids for Diffusion Vacuum Pumps
ρl	1073.70	kg/m3	348.15	Measurements and correlations of solubility of N2O in and density, viscosity of partially CO2 loaded water-lean amino acid salts
ρl	1075.20	kg/m3	348.15	Thermophysical properties of glycols and glymes
ρl	1070.17	kg/m3	353.15	Density and Refractive Index of Binary Mixtures of Two 1-Alkyl-3-methylimidazolium Ionic Liquids with 1,4-Dioxane and Ethylene Glycol
ρl	1071.60	kg/m3	353.15	Density of Working Liquids for Diffusion Vacuum Pumps
ρl	1070.10	kg/m3	353.15	Density and Viscosity of the Nonaqueous and Aqueous Mixtures of Methyldiethanolamine and Monoethylene Glycol at Temperatures from 283.15 to 353.15 K
ρl	1070.00	kg/m3	353.15	Measurements and correlations of solubility of N2O in and density, viscosity of partially CO2 loaded water-lean amino acid salts
ρl	1060.00	kg/m3	353.15	Excess Molar Volumes, Viscosities, and Heat Capacities for the Mixtures of Ethylene Glycol + Water from 273.15 K to 353.15 K
ρl	1071.50	kg/m3	353.15	Thermophysical properties of glycols and glymes
ρl	1067.80	kg/m3	358.15	Thermophysical properties of glycols and glymes
ρl	1064.18	kg/m3	363.15	Density of Working Liquids for Diffusion Vacuum Pumps
ρl	1064.00	kg/m3	363.15	Thermophysical properties of glycols and glymes
ρl	1060.20	kg/m3	368.15	Thermophysical properties of glycols and glymes
ρl	1056.40	kg/m3	373.15	Thermophysical properties of glycols and glymes
ΔfusS	[38.21; 44.57]	J/mol×K	[260.60; 260.80]
ΔfusS	38.21	J/mol×K	260.60	NIST
ΔfusS	38.21	J/mol×K	260.60	NIST
ΔfusS	44.57	J/mol×K	260.80	NIST
ΔfusS	44.57	J/mol×K	260.80	NIST
csound,fluid	[1654.38; 1656.10]	m/s	[298.15; 298.15]
csound,fluid	1656.10	m/s	298.15	Volumetric and compressibility properties of liquid water as a solute in glycolic, propylene carbonate, and tetramethylurea solutions at T = 298.15 K
csound,fluid	1654.38	m/s	298.15	Densities, Speeds of Sound, and Isentropic Compressibilities for Binary Mixtures of 1,2-Ethanediol with 2-Ethyl-1-hexanol, 1-Heptanol, or Ethanol at the Temperature 298.15 K and Densities for Mixtures of 1,2-Ethanediol with 1-Nonanol at the Temperatures (293.15 and 298.15) K
γ	[0.05; 0.05]	N/m	[283.15; 323.15]
γ	0.05	N/m	283.15	Surface tension of non-ideal binary and ternary liquid mixtures at various temperatures and p = 81.5 kPa
γ	0.05	N/m	293.15	Surface Tension of Binary Mixtures of Ethanol + Ethylene glycol from 20 to 50 oC
γ	0.05	N/m	293.15	Surface Properties of Pure Liquids and Binary Liquid Mixtures of Ethylene Glycol + Methylcyclohexanols
γ	0.05	N/m	293.15	Surface Tensions of Dilute Solutions of Cycloheptanol in Ethylene Glycol
γ	0.05	N/m	293.15	Equilibrium Surface Tensions of Benzyl Alcohol + Ethylene Glycol Mixtures
γ	0.05	N/m	293.20	KDB
γ	0.05	N/m	298.15	NCMS SOLV-DB
γ	0.05	N/m	298.15	Surface Tension of Binary Mixtures of Ethanol + Ethylene glycol from 20 to 50 oC
γ	0.05	N/m	298.15	Surface tension of non-ideal binary and ternary liquid mixtures at various temperatures and p = 81.5 kPa
γ	0.05	N/m	298.15	Surface Tensions of Dilute Solutions of Cycloheptanol in Ethylene Glycol
γ	0.05	N/m	298.15	Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes
γ	0.05	N/m	298.15	Equilibrium Surface Tensions of Benzyl Alcohol + Ethylene Glycol Mixtures
γ	0.05	N/m	298.15	Surface Properties of Pure Liquids and Binary Liquid Mixtures of Ethylene Glycol + Methylcyclohexanols
γ	0.05	N/m	303.15	Surface Tensions of Dilute Solutions of Cycloheptanol in Ethylene Glycol
γ	0.05	N/m	303.15	Equilibrium Surface Tensions of Benzyl Alcohol + Ethylene Glycol Mixtures
γ	0.05	N/m	303.15	Surface Tension of Binary Mixtures of Ethanol + Ethylene glycol from 20 to 50 oC
γ	0.05	N/m	303.15	Surface Properties of Pure Liquids and Binary Liquid Mixtures of Ethylene Glycol + Methylcyclohexanols
γ	0.05	N/m	308.15	Gas-Liquid Equilibrium Data for a Mixture Gas of Sulfur Dioxide + Nitrogen with Ethylene Glycol Aqueous Solutions at 298.15 K and 123.15 kPa
γ	0.05	N/m	308.15	Surface Tension of Binary Mixtures of Ethanol + Ethylene glycol from 20 to 50 oC
γ	0.05	N/m	308.15	Surface tension of non-ideal binary and ternary liquid mixtures at various temperatures and p = 81.5 kPa
γ	0.05	N/m	308.15	Surface Properties of Pure Liquids and Binary Liquid Mixtures of Ethylene Glycol + Methylcyclohexanols
γ	0.05	N/m	308.15	Equilibrium Surface Tensions of Benzyl Alcohol + Ethylene Glycol Mixtures
γ	0.05	N/m	308.15	Surface Tensions of Dilute Solutions of Cycloheptanol in Ethylene Glycol
γ	0.05	N/m	313.15	Gas-Liquid Equilibrium Data for a Mixture Gas of Sulfur Dioxide + Nitrogen with Ethylene Glycol Aqueous Solutions at 298.15 K and 123.15 kPa
γ	0.05	N/m	313.15	Surface Tensions of Dilute Solutions of Cycloheptanol in Ethylene Glycol
γ	0.05	N/m	313.15	Surface Properties of Pure Liquids and Binary Liquid Mixtures of Ethylene Glycol + Methylcyclohexanols
γ	0.05	N/m	313.15	Surface Tension of Binary Mixtures of Ethanol + Ethylene glycol from 20 to 50 oC
γ	0.05	N/m	313.15	Equilibrium Surface Tensions of Benzyl Alcohol + Ethylene Glycol Mixtures
γ	0.05	N/m	318.15	Surface Tensions of Dilute Solutions of Cycloheptanol in Ethylene Glycol
γ	0.05	N/m	318.15	Surface Properties of Pure Liquids and Binary Liquid Mixtures of Ethylene Glycol + Methylcyclohexanols
γ	0.05	N/m	318.15	Surface Tension of Binary Mixtures of Ethanol + Ethylene glycol from 20 to 50 oC
γ	0.05	N/m	318.15	Gas-Liquid Equilibrium Data for a Mixture Gas of Sulfur Dioxide + Nitrogen with Ethylene Glycol Aqueous Solutions at 298.15 K and 123.15 kPa
γ	0.05	N/m	318.15	Equilibrium Surface Tensions of Benzyl Alcohol + Ethylene Glycol Mixtures
γ	0.05	N/m	323.15	Surface Tension of Binary Mixtures of Ethanol + Ethylene glycol from 20 to 50 oC
γ	0.05	N/m	323.15	Surface Tensions of Dilute Solutions of Cycloheptanol in Ethylene Glycol
γ	0.05	N/m	323.15	Surface Properties of Pure Liquids and Binary Liquid Mixtures of Ethylene Glycol + Methylcyclohexanols
γ	0.05	N/m	323.15	Gas-Liquid Equilibrium Data for a Mixture Gas of Sulfur Dioxide + Nitrogen with Ethylene Glycol Aqueous Solutions at 298.15 K and 123.15 kPa
γ	0.05	N/m	323.15	Equilibrium Surface Tensions of Benzyl Alcohol + Ethylene Glycol Mixtures
λ	[0.24; 0.27]	W/m×K	[283.15; 343.15]
λ	0.24	W/m×K	283.15	Thermal conductivity of dry anatase and rutile nano-powders and ethylene and propylene glycol-based TiO2 nanofluids
λ	0.24	W/m×K	283.15	Thermophysical profile of ethylene glycol-based ZnO nanofluids
λ	0.25	W/m×K	293.15	Measurement of the thermal conductivity of SiO2 nanofluids with an optimized transient hot wire method
λ	0.25	W/m×K	298.15	An experimental study on thermal conductivity enhancement of DI water-EG based ZnO(CuO)/graphene wrapped carbon nanotubes nanofluids
λ	0.24	W/m×K	298.15	Experimental studies on viscosity, thermal and electrical conductivity of aluminum nitride ethylene glycol (AlN-EG) nanofluids
λ	0.25	W/m×K	298.20	Application of the Multi-Current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols
λ	0.25	W/m×K	303.15	Thermophysical profile of ethylene glycol-based ZnO nanofluids
λ	0.25	W/m×K	303.15	Thermal conductivity enhancement of ethylene glycol and water with graphene nanoplatelets
λ	0.25	W/m×K	303.15	An experimental study on thermal conductivity enhancement of DI water-EG based ZnO(CuO)/graphene wrapped carbon nanotubes nanofluids
λ	0.25	W/m×K	303.15	Thermal conductivity of dry anatase and rutile nano-powders and ethylene and propylene glycol-based TiO2 nanofluids
λ	0.25	W/m×K	308.10	Application of the Multi-Current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols
λ	0.26	W/m×K	308.15	An experimental study on thermal conductivity enhancement of DI water-EG based ZnO(CuO)/graphene wrapped carbon nanotubes nanofluids
λ	0.26	W/m×K	313.15	Thermal conductivity enhancement of ethylene glycol and water with graphene nanoplatelets
λ	0.26	W/m×K	313.15	An experimental study on thermal conductivity enhancement of DI water-EG based ZnO(CuO)/graphene wrapped carbon nanotubes nanofluids
λ	0.26	W/m×K	318.15	An experimental study on thermal conductivity enhancement of DI water-EG based ZnO(CuO)/graphene wrapped carbon nanotubes nanofluids
λ	0.25	W/m×K	318.30	Application of the Multi-Current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols
λ	0.25	W/m×K	323.15	Thermophysical profile of ethylene glycol-based ZnO nanofluids
λ	0.26	W/m×K	323.15	Thermal conductivity enhancement of ethylene glycol and water with graphene nanoplatelets
λ	0.26	W/m×K	323.15	Thermal conductivity of dry anatase and rutile nano-powders and ethylene and propylene glycol-based TiO2 nanofluids
λ	0.26	W/m×K	323.15	An experimental study on thermal conductivity enhancement of DI water-EG based ZnO(CuO)/graphene wrapped carbon nanotubes nanofluids
λ	0.26	W/m×K	328.30	Application of the Multi-Current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols
λ	0.26	W/m×K	338.30	Application of the Multi-Current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols
λ	0.27	W/m×K	343.15	Thermal conductivity of dry anatase and rutile nano-powders and ethylene and propylene glycol-based TiO2 nanofluids
λ	0.26	W/m×K	343.15	Thermophysical profile of ethylene glycol-based ZnO nanofluids
αdiff	[9.42e-08; 9.84e-08]	m2/s	[298.15; 338.15]
αdiff	9.84e-08	m2/s	298.15	Temperature controlled photoacoustic device for thermal diffusivity measurements of liquids and nanofluids
αdiff	9.73e-08	m2/s	308.15	Temperature controlled photoacoustic device for thermal diffusivity measurements of liquids and nanofluids
αdiff	9.68e-08	m2/s	318.15	Temperature controlled photoacoustic device for thermal diffusivity measurements of liquids and nanofluids
αdiff	9.49e-08	m2/s	328.15	Temperature controlled photoacoustic device for thermal diffusivity measurements of liquids and nanofluids
αdiff	9.42e-08	m2/s	338.15	Temperature controlled photoacoustic device for thermal diffusivity measurements of liquids and nanofluids
vspec	[8.87e-04; 9.10e-04]	m3/kg	[273.15; 313.15]
vspec	8.87e-04	m3/kg	273.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.88e-04	m3/kg	274.14	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.88e-04	m3/kg	275.14	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.89e-04	m3/kg	276.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.89e-04	m3/kg	277.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.90e-04	m3/kg	278.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.90e-04	m3/kg	279.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.91e-04	m3/kg	280.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.91e-04	m3/kg	281.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.92e-04	m3/kg	282.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.93e-04	m3/kg	283.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.93e-04	m3/kg	284.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.94e-04	m3/kg	285.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.94e-04	m3/kg	286.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.95e-04	m3/kg	287.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.95e-04	m3/kg	288.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.95e-04	m3/kg	288.16	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.95e-04	m3/kg	288.21	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.95e-04	m3/kg	288.22	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.96e-04	m3/kg	289.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.96e-04	m3/kg	290.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.97e-04	m3/kg	291.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.98e-04	m3/kg	292.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.98e-04	m3/kg	293.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.99e-04	m3/kg	294.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	8.99e-04	m3/kg	295.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	9.00e-04	m3/kg	296.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	9.00e-04	m3/kg	297.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	9.01e-04	m3/kg	298.16	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	9.02e-04	m3/kg	299.16	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	9.02e-04	m3/kg	300.16	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	9.03e-04	m3/kg	301.16	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	9.03e-04	m3/kg	302.16	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	9.04e-04	m3/kg	303.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	9.04e-04	m3/kg	304.16	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	9.05e-04	m3/kg	305.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	9.06e-04	m3/kg	306.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	9.06e-04	m3/kg	307.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	9.07e-04	m3/kg	308.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	9.07e-04	m3/kg	309.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	9.08e-04	m3/kg	310.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	9.08e-04	m3/kg	311.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	9.09e-04	m3/kg	312.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
vspec	9.10e-04	m3/kg	313.15	Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture

Datasets

1. Viscosity, Pa*s (2)
2. Refractive index (Na D-line) (1)
3. Mass density, kg/m3 (4)
4. Speed of sound, m/s (1)
5. Thermal conductivity, W/m/K (1)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
293.15	98.00	0.0211
293.15	49030.00	0.0267
293.15	98060.00	0.0334
293.15	147100.00	0.0412
293.15	196130.00	0.0503
293.15	245160.00	0.0604
312.46	98.00	0.0099
312.46	98060.00	0.0148
312.49	49030.00	0.0122
312.49	147100.00	0.0176
312.65	245160.00	0.0247
334.87	98.00	0.0049
335.00	49030.00	0.0060
335.30	98060.00	0.0070
335.35	245160.00	0.0112
335.43	147100.00	0.0082
335.45	196130.00	0.0096
349.24	98.00	0.0035
349.50	49030.00	0.0042
349.65	98060.00	0.0049
349.67	147100.00	0.0057
349.80	196130.00	0.0065
349.91	245160.00	0.0075
365.70	98.00	0.0024
366.10	49030.00	0.0028
366.15	98060.00	0.0033
366.37	147100.00	0.0038
366.48	196130.00	0.0043
366.80	245160.00	0.0049
380.15	98060.00	0.0026
380.82	98.00	0.0019
381.00	49030.00	0.0022
381.20	196130.00	0.0033
381.27	147100.00	0.0029
381.30	245160.00	0.0038
395.55	98.00	0.0014
395.60	49030.00	0.0017
395.61	98060.00	0.0019
395.65	147100.00	0.0022
395.73	196130.00	0.0025
395.80	245160.00	0.0028
421.70	98.00	0.0010
421.71	49030.00	0.0012
421.80	98060.00	0.0013
421.90	147100.00	0.0015
422.00	196130.00	0.0017
422.00	245160.00	0.0019
464.40	98.00	0.0007
464.47	98060.00	0.0010
464.53	196130.00	0.0012
464.53	245160.00	0.0014
464.54	147100.00	0.0011
464.60	49030.00	0.0009
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
101.30	308.15	0.0106
Reference

Refractive index (Na D-line)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Refractive index (Na D-line) - Liquid
298.15	100.00	1.4304
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.11	100.00	1120.2
283.11	1000.00	1120.5
283.11	2000.00	1120.9
283.11	5000.00	1122.1
283.11	7000.00	1123.0
283.11	10000.00	1124.3
283.11	12000.00	1125.1
283.11	16000.00	1126.7
283.11	20000.00	1128.2
283.11	25000.00	1130.1
283.11	30000.00	1132.0
283.11	35000.00	1133.9
283.11	40000.00	1135.7
283.11	45000.00	1137.5
283.11	50000.00	1139.3
283.11	55000.00	1141.0
283.11	60000.00	1142.9
283.11	65000.00	1144.5
283.11	70000.00	1146.1
283.11	75000.00	1147.8
283.11	80000.00	1149.4
283.11	85000.00	1151.1
283.11	90000.00	1152.6
283.11	95000.00	1154.2
293.13	100.00	1113.0
293.13	1000.00	1113.4
293.13	2000.00	1113.9
293.13	5000.00	1115.1
293.13	7000.00	1116.0
293.13	10000.00	1117.2
293.13	12000.00	1118.0
293.13	16000.00	1119.8
293.13	20000.00	1121.3
293.13	25000.00	1123.3
293.13	30000.00	1125.3
293.13	35000.00	1127.1
293.13	40000.00	1129.0
293.13	45000.00	1130.7
293.13	50000.00	1132.7
293.13	55000.00	1134.5
293.13	60000.00	1136.3
293.13	65000.00	1138.0
293.13	70000.00	1139.7
293.13	75000.00	1141.3
293.13	80000.00	1143.1
293.13	85000.00	1144.6
293.13	90000.00	1146.3
293.13	95000.00	1147.8
303.13	100.00	1106.0
303.13	1000.00	1106.4
303.13	2000.00	1106.8
303.13	5000.00	1108.2
303.13	7000.00	1109.2
303.13	10000.00	1110.4
303.13	12000.00	1111.2
303.13	16000.00	1112.9
303.13	20000.00	1114.6
303.13	25000.00	1116.6
303.13	30000.00	1118.6
303.13	35000.00	1120.7
303.13	40000.00	1122.6
303.13	45000.00	1124.5
303.13	50000.00	1126.2
303.13	55000.00	1128.0
303.13	60000.00	1129.8
303.13	65000.00	1131.7
303.13	70000.00	1133.4
303.13	75000.00	1135.2
303.13	80000.00	1136.9
303.13	85000.00	1138.4
303.13	90000.00	1140.1
303.13	95000.00	1141.7
313.16	100.00	1099.1
313.16	1000.00	1099.4
313.16	2000.00	1099.8
313.16	5000.00	1101.2
313.16	7000.00	1102.1
313.16	10000.00	1103.5
313.16	12000.00	1104.2
313.16	16000.00	1106.1
313.16	20000.00	1107.8
313.16	25000.00	1109.8
313.16	30000.00	1111.8
313.16	35000.00	1113.8
313.16	40000.00	1115.9
313.16	45000.00	1117.9
313.16	50000.00	1119.8
313.16	55000.00	1121.5
313.16	60000.00	1123.4
313.16	65000.00	1125.2
313.16	70000.00	1127.0
313.16	75000.00	1128.8
313.16	80000.00	1130.6
313.16	85000.00	1132.3
313.16	90000.00	1133.9
313.16	95000.00	1135.5
323.15	100.00	1092.0
323.15	1000.00	1092.3
323.15	2000.00	1092.9
323.15	5000.00	1094.2
323.15	7000.00	1095.2
323.15	10000.00	1096.5
323.15	12000.00	1097.4
323.15	16000.00	1099.3
323.15	20000.00	1100.9
323.15	25000.00	1103.1
323.15	30000.00	1105.2
323.15	35000.00	1107.3
323.15	40000.00	1109.3
323.15	45000.00	1111.3
323.15	50000.00	1113.3
323.15	55000.00	1115.1
323.15	60000.00	1117.1
323.15	65000.00	1119.1
323.15	70000.00	1120.9
323.15	75000.00	1122.7
323.15	80000.00	1124.4
323.15	85000.00	1126.2
323.15	90000.00	1127.8
323.15	95000.00	1129.5
333.18	100.00	1084.7
333.18	1000.00	1085.1
333.18	2000.00	1085.6
333.18	5000.00	1087.1
333.18	7000.00	1088.0
333.18	10000.00	1089.5
333.18	12000.00	1090.4
333.18	16000.00	1092.2
333.18	20000.00	1094.0
333.18	25000.00	1096.3
333.18	30000.00	1098.4
333.18	35000.00	1100.4
333.18	40000.00	1102.6
333.18	45000.00	1104.5
333.18	50000.00	1106.4
333.18	55000.00	1108.5
333.18	60000.00	1110.6
333.18	65000.00	1112.5
333.18	70000.00	1114.3
333.18	75000.00	1116.2
333.18	80000.00	1118.0
333.18	85000.00	1119.7
333.18	90000.00	1121.5
333.18	95000.00	1123.1
343.16	100.00	1077.3
343.16	1000.00	1077.8
343.16	2000.00	1078.3
343.16	5000.00	1080.0
343.16	7000.00	1080.9
343.16	10000.00	1082.3
343.16	12000.00	1083.1
343.16	16000.00	1085.1
343.16	20000.00	1086.9
343.16	25000.00	1089.3
343.16	30000.00	1091.5
343.16	35000.00	1093.7
343.16	40000.00	1095.8
343.16	45000.00	1097.8
343.16	50000.00	1100.0
343.16	55000.00	1102.0
343.16	60000.00	1104.0
343.16	65000.00	1106.1
343.16	70000.00	1108.0
343.16	75000.00	1109.8
343.16	80000.00	1111.7
343.16	85000.00	1113.5
343.16	90000.00	1115.3
343.16	95000.00	1117.0
353.18	100.00	1069.9
353.18	1000.00	1070.5
353.18	2000.00	1071.0
353.18	5000.00	1072.5
353.18	7000.00	1073.5
353.18	10000.00	1075.0
353.18	12000.00	1076.0
353.18	16000.00	1078.0
353.18	20000.00	1079.9
353.18	25000.00	1082.2
353.18	30000.00	1084.5
353.18	35000.00	1086.8
353.18	40000.00	1089.0
353.18	45000.00	1091.0
353.18	50000.00	1093.2
353.18	55000.00	1095.4
353.18	60000.00	1097.4
353.18	65000.00	1099.4
353.18	70000.00	1101.3
353.18	75000.00	1103.2
353.18	80000.00	1105.2
353.18	85000.00	1106.9
353.18	90000.00	1108.8
353.18	95000.00	1110.6
363.18	100.00	1062.4
363.18	1000.00	1062.8
363.18	2000.00	1063.4
363.18	5000.00	1065.0
363.18	7000.00	1066.0
363.18	10000.00	1067.6
363.18	12000.00	1068.6
363.18	16000.00	1070.6
363.18	20000.00	1072.5
363.18	25000.00	1075.0
363.18	30000.00	1077.4
363.18	35000.00	1079.6
363.18	40000.00	1082.0
363.18	45000.00	1084.2
363.18	50000.00	1086.2
363.18	55000.00	1088.4
363.18	60000.00	1090.5
363.18	65000.00	1092.6
363.18	70000.00	1094.5
363.18	75000.00	1096.6
363.18	80000.00	1098.5
363.18	85000.00	1100.4
363.18	90000.00	1102.3
363.18	95000.00	1104.1
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	298.15	1112.1
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
278.15	100.00	1122.4
278.15	1000.00	1122.6
278.15	5000.00	1124.1
278.15	10000.00	1126.0
278.15	15000.00	1127.8
278.15	20000.00	1129.6
278.15	25000.00	1131.4
278.15	30000.00	1133.1
278.15	35000.00	1134.8
278.15	40000.00	1136.6
278.15	45000.00	1138.2
278.15	50000.00	1139.9
278.15	55000.00	1141.6
278.15	60000.00	1143.3
288.15	100.00	1115.8
288.15	1000.00	1116.0
288.15	5000.00	1117.6
288.15	10000.00	1119.5
288.15	15000.00	1121.5
288.15	20000.00	1123.3
288.15	25000.00	1125.2
288.15	30000.00	1127.0
288.15	35000.00	1128.8
288.15	40000.00	1130.6
288.15	45000.00	1132.3
288.15	50000.00	1134.1
288.15	55000.00	1135.7
288.15	60000.00	1137.4
298.15	100.00	1109.0
298.15	1000.00	1109.2
298.15	5000.00	1110.9
298.15	10000.00	1112.9
298.15	15000.00	1114.9
298.15	20000.00	1116.8
298.15	25000.00	1118.7
298.15	30000.00	1120.6
298.15	35000.00	1122.4
298.15	40000.00	1124.3
298.15	45000.00	1126.1
298.15	50000.00	1127.8
298.15	55000.00	1129.6
298.15	60000.00	1131.3
308.15	100.00	1102.2
308.15	1000.00	1102.4
308.15	5000.00	1104.1
308.15	10000.00	1106.1
308.15	15000.00	1108.2
308.15	20000.00	1110.1
308.15	25000.00	1112.1
308.15	30000.00	1114.0
308.15	35000.00	1115.9
308.15	40000.00	1117.7
308.15	45000.00	1119.6
308.15	50000.00	1121.4
308.15	55000.00	1123.2
308.15	60000.00	1125.0
318.15	100.00	1095.2
318.15	1000.00	1095.4
318.15	5000.00	1097.1
318.15	10000.00	1099.2
318.15	15000.00	1101.3
318.15	20000.00	1103.3
318.15	25000.00	1105.3
318.15	30000.00	1107.3
318.15	35000.00	1109.3
318.15	40000.00	1111.2
318.15	45000.00	1113.1
318.15	50000.00	1115.0
318.15	55000.00	1116.8
318.15	60000.00	1118.6
328.15	100.00	1088.2
328.15	1000.00	1088.3
328.15	5000.00	1090.2
328.15	10000.00	1092.3
328.15	15000.00	1094.4
328.15	20000.00	1096.5
328.15	25000.00	1098.6
328.15	30000.00	1100.6
328.15	35000.00	1102.6
328.15	40000.00	1104.6
328.15	45000.00	1106.5
328.15	50000.00	1108.4
328.15	55000.00	1110.3
328.15	60000.00	1112.1
338.15	100.00	1080.9
338.15	1000.00	1081.2
338.15	5000.00	1083.1
338.15	10000.00	1085.4
338.15	15000.00	1087.6
338.15	20000.00	1089.8
338.15	25000.00	1091.9
338.15	30000.00	1094.0
338.15	35000.00	1096.0
338.15	40000.00	1097.9
338.15	45000.00	1099.9
338.15	50000.00	1101.9
338.15	55000.00	1103.9
338.15	60000.00	1105.8
348.15	100.00	1073.6
348.15	1000.00	1073.9
348.15	5000.00	1075.8
348.15	10000.00	1078.1
348.15	15000.00	1080.4
348.15	20000.00	1082.7
348.15	25000.00	1084.9
348.15	30000.00	1087.0
348.15	35000.00	1089.2
348.15	40000.00	1091.3
348.15	45000.00	1093.4
348.15	50000.00	1095.3
348.15	55000.00	1097.3
348.15	60000.00	1099.4
358.15	100.00	1066.1
358.15	1000.00	1066.2
358.15	5000.00	1068.2
358.15	10000.00	1070.7
358.15	15000.00	1073.1
358.15	20000.00	1075.4
358.15	25000.00	1077.8
358.15	30000.00	1079.9
358.15	35000.00	1082.1
358.15	40000.00	1084.3
358.15	45000.00	1086.5
358.15	50000.00	1088.6
358.15	55000.00	1090.7
358.15	60000.00	1092.7
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	101.13	1105.0
Reference

Speed of sound, m/s

Operational condition: Frequency, MHz = 8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
273.15	99.00	1713.847
273.15	5204.00	1727.491
273.15	10344.00	1740.939
273.15	15152.00	1753.194
273.15	20194.00	1765.939
273.15	25132.00	1778.134
273.15	30171.00	1789.896
293.15	99.00	1665.836
293.15	5051.00	1679.764
293.15	10070.00	1693.534
293.15	15176.00	1707.192
293.15	20158.00	1720.201
293.15	25108.00	1732.878
293.15	30024.00	1745.294
313.15	100.00	1618.547
313.15	5031.00	1633.093
313.15	10028.00	1647.339
313.15	15117.00	1661.696
313.15	20088.00	1675.281
313.15	25102.00	1688.742
313.15	29983.00	1701.571
333.15	99.00	1570.742
333.15	5054.00	1586.116
333.15	10048.00	1601.104
333.15	15067.00	1615.849
333.15	20106.00	1630.289
333.15	25103.00	1644.305
333.15	29958.00	1657.658
353.15	100.00	1521.783
353.15	5079.00	1538.084
353.15	10048.00	1553.832
353.15	15054.00	1569.282
353.15	20071.00	1584.393
353.15	25078.00	1599.138
353.15	29995.00	1613.263
Reference

Thermal conductivity, W/m/K

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Thermal conductivity, W/m/K - Liquid
77.00	295.00	0.2540
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[71.26; 180.97]	J/mol×K	[260.15; 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			5.29480e+01
Coefficient B			-6.04610e+02
Coefficient C			5.20724e+00
Coefficient D			1.06070e-04
Coefficient E			-4.93520e-08
Comment			ChemSep eq 16, IdealGasHeatCapacityCp
Temperature range, min.			260.15
Temperature range, max.			1500.00
Cp,gas	71.26	J/mol×K	260.15	Calculated Property
Cp,gas	94.30	J/mol×K	397.91	Calculated Property
Cp,gas	114.58	J/mol×K	535.67	Calculated Property
Cp,gas	131.09	J/mol×K	673.43	Calculated Property
Cp,gas	144.37	J/mol×K	811.19	Calculated Property
Cp,gas	155.09	J/mol×K	948.96	Calculated Property
Cp,gas	163.76	J/mol×K	1086.72	Calculated Property
Cp,gas	170.79	J/mol×K	1224.48	Calculated Property
Cp,gas	176.46	J/mol×K	1362.24	Calculated Property
Cp,gas	180.97	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[138.70; 205.75]	J/mol×K	[260.15; 493.15]	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			8.69900e+01
Coefficient B			-7.23260e+01
Coefficient C			2.83884e+00
Coefficient D			6.54560e-03
Coefficient E			-4.70000e-06
Comment			ChemSep eq 16, LiquidHeatCapacityCp
Temperature range, min.			260.15
Temperature range, max.			493.15
Cp,liquid	138.70	J/mol×K	260.15	Calculated Property
Cp,liquid	145.77	J/mol×K	286.04	Calculated Property
Cp,liquid	153.11	J/mol×K	311.93	Calculated Property
Cp,liquid	160.66	J/mol×K	337.82	Calculated Property
Cp,liquid	168.35	J/mol×K	363.71	Calculated Property
Cp,liquid	176.11	J/mol×K	389.59	Calculated Property
Cp,liquid	183.83	J/mol×K	415.48	Calculated Property
Cp,liquid	191.41	J/mol×K	441.37	Calculated Property
Cp,liquid	198.75	J/mol×K	467.26	Calculated Property
Cp,liquid	205.75	J/mol×K	493.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.1324806; 0.0001166]	Pa×s	[260.15; 576.00]	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			-3.09380e+02
Coefficient B			1.49280e+04
Coefficient C			4.54900e+01
Coefficient D			-4.44050e-05
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, LiquidViscosity
Temperature range, min.			260.15
Temperature range, max.			576.00
η	0.1324806	Pa×s	260.15	Calculated Property
η	0.0192341	Pa×s	295.24	Calculated Property
η	0.0055817	Pa×s	330.34	Calculated Property
η	0.0024309	Pa×s	365.43	Calculated Property
η	0.0013321	Pa×s	400.53	Calculated Property
η	0.0008203	Pa×s	435.62	Calculated Property
η	0.0005269	Pa×s	470.72	Calculated Property
η	0.0003356	Pa×s	505.81	Calculated Property
η	0.0002047	Pa×s	540.91	Calculated Property
η	0.0001166	Pa×s	576.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[67.65; 19.05]	kJ/mol	[260.15; 695.80]	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			7.41400e+01
Coefficient B			1.68070e-01
Coefficient C			-1.96940e-01
Coefficient D			1.04170e+00
Coefficient E			-6.14880e-01
Critical temperature, Tc (K)			7.19000e+02
Comment			ChemSep eq 106, HeatOfVaporization
Temperature range, min.			260.15
Temperature range, max.			695.80
ΔvapH	67.65	kJ/mol	260.15	Calculated Property
ΔvapH	65.29	kJ/mol	308.56	Calculated Property
ΔvapH	62.38	kJ/mol	356.96	Calculated Property
ΔvapH	58.87	kJ/mol	405.37	Calculated Property
ΔvapH	54.74	kJ/mol	453.77	Calculated Property
ΔvapH	49.97	kJ/mol	502.18	Calculated Property
ΔvapH	44.48	kJ/mol	550.58	Calculated Property
ΔvapH	38.13	kJ/mol	598.99	Calculated Property
ΔvapH	30.40	kJ/mol	647.39	Calculated Property
ΔvapH	19.05	kJ/mol	695.80	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 5004.89]	kPa	[370.66; 623.15]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			2.03109e+01
Coefficient B			-7.24361e+03
Coefficient C			-8.90400e+00
Temperature range, min.			370.66
Temperature range, max.			623.15
Pvap	1.33	kPa	370.66	Calculated Property
Pvap	5.63	kPa	398.71	Calculated Property
Pvap	19.61	kPa	426.77	Calculated Property
Pvap	58.36	kPa	454.82	Calculated Property
Pvap	152.65	kPa	482.88	Calculated Property
Pvap	358.59	kPa	510.93	Calculated Property
Pvap	769.55	kPa	538.99	Calculated Property
Pvap	1529.45	kPa	567.04	Calculated Property
Pvap	2846.34	kPa	595.10	Calculated Property
Pvap	5004.89	kPa	623.15	Calculated Property
Pvap	[2.57e-04; 7296.63]	kPa	[260.15; 720.00]	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			6.12102e+01
Coefficient B			-9.61727e+03
Coefficient C			-5.83171e+00
Coefficient D			-1.13705e-06
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			260.15
Temperature range, max.			720.00
Pvap	2.57e-04	kPa	260.15	Calculated Property
Pvap	0.04	kPa	311.24	Calculated Property
Pvap	1.17	kPa	362.34	Calculated Property
Pvap	13.75	kPa	413.43	Calculated Property
Pvap	85.53	kPa	464.53	Calculated Property
Pvap	342.04	kPa	515.62	Calculated Property
Pvap	994.92	kPa	566.72	Calculated Property
Pvap	2284.50	kPa	617.81	Calculated Property
Pvap	4380.07	kPa	668.91	Calculated Property
Pvap	7296.63	kPa	720.00	Calculated Property
Pvap	[1.98e-04; 7495.90]	kPa	[260.15; 645.00]	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			1.91425e+02
Coefficient B			-1.47686e+04
Coefficient C			-2.59977e+01
Coefficient D			2.06233e-05
Coefficient E			0.00000e+00
Temperature range, min.			260.15
Temperature range, max.			645.00
Pvap	1.98e-04	kPa	260.15	Calculated Property
Pvap	0.02	kPa	302.91	Calculated Property
Pvap	0.45	kPa	345.67	Calculated Property
Pvap	4.55	kPa	388.43	Calculated Property
Pvap	26.91	kPa	431.19	Calculated Property
Pvap	112.46	kPa	473.96	Calculated Property
Pvap	375.86	kPa	516.72	Calculated Property
Pvap	1091.97	kPa	559.48	Calculated Property
Pvap	2921.27	kPa	602.24	Calculated Property
Pvap	7495.90	kPa	645.00	Calculated Property
Pvap	[0.08; 108.33]	kPa	[323.00; 473.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.60493e+01
Coefficient B			-4.40934e+03
Coefficient C			-8.49960e+01
Reference			Jones and Tamplin, 1952, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			323.00
Temperature range, max.			473.00
Pvap	0.08	kPa	323.00	Calculated Property
Pvap	0.28	kPa	339.67	Calculated Property
Pvap	0.82	kPa	356.33	Calculated Property
Pvap	2.09	kPa	373.00	Calculated Property
Pvap	4.84	kPa	389.67	Calculated Property
Pvap	10.25	kPa	406.33	Calculated Property
Pvap	20.17	kPa	423.00	Calculated Property
Pvap	37.23	kPa	439.67	Calculated Property
Pvap	65.05	kPa	456.33	Calculated Property
Pvap	108.33	kPa	473.00	Calculated Property
Pvap	[0.08; 108.33]	kPa	[323.00; 473.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.60493e+01
Coefficient B			-4.40934e+03
Coefficient C			-8.49960e+01
Reference			Jones and Tamplin, 1952
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			323.00
Temperature range, max.			473.00
Pvap	0.08	kPa	323.00	Calculated Property
Pvap	0.28	kPa	339.67	Calculated Property
Pvap	0.82	kPa	356.33	Calculated Property
Pvap	2.09	kPa	373.00	Calculated Property
Pvap	4.84	kPa	389.67	Calculated Property
Pvap	10.25	kPa	406.33	Calculated Property
Pvap	20.17	kPa	423.00	Calculated Property
Pvap	37.23	kPa	439.67	Calculated Property
Pvap	65.05	kPa	456.33	Calculated Property
Pvap	108.33	kPa	473.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1136.38; 626.94]	kg/m3	[260.15; 695.80]	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			8.13461e+01
Coefficient B			2.50840e-01
Coefficient C			7.20000e+02
Coefficient D			2.18380e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			260.15
Temperature range, max.			695.80
ρl	1136.38	kg/m3	260.15	Calculated Property
ρl	1102.70	kg/m3	308.56	Calculated Property
ρl	1066.90	kg/m3	356.96	Calculated Property
ρl	1028.52	kg/m3	405.37	Calculated Property
ρl	986.86	kg/m3	453.77	Calculated Property
ρl	940.88	kg/m3	502.18	Calculated Property
ρl	888.85	kg/m3	550.58	Calculated Property
ρl	827.57	kg/m3	598.99	Calculated Property
ρl	749.65	kg/m3	647.39	Calculated Property
ρl	626.94	kg/m3	695.80	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.05; 0.03]	N/m	[260.15; 470.45]	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			-6.43280e-03
Coefficient B			9.47960e+01
Coefficient C			-3.42320e+00
Coefficient D			1.82400e-03
Coefficient E			-3.97320e-06
Comment			ChemSep eq 16, SurfaceTension
Temperature range, min.			260.15
Temperature range, max.			470.45
γ	0.05	N/m	260.15	Calculated Property
γ	0.05	N/m	283.52	Calculated Property
γ	0.05	N/m	306.88	Calculated Property
γ	0.05	N/m	330.25	Calculated Property
γ	0.04	N/m	353.62	Calculated Property
γ	0.04	N/m	376.98	Calculated Property
γ	0.04	N/m	400.35	Calculated Property
γ	0.04	N/m	423.72	Calculated Property
γ	0.03	N/m	447.08	Calculated Property
γ	0.03	N/m	470.45	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.01; 0.10]	W/m×K	[260.15; 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			-8.96290e+06
Coefficient B			-3.12570e-01
Coefficient C			2.53130e+09
Coefficient D			-1.29550e+13
Comment			ChemSep eq 102, VaporThermalConductivity
Temperature range, min.			260.15
Temperature range, max.			1000.00
λ	0.01	W/m×K	260.15	Calculated Property
λ	0.01	W/m×K	342.36	Calculated Property
λ	0.02	W/m×K	424.56	Calculated Property
λ	0.03	W/m×K	506.77	Calculated Property
λ	0.04	W/m×K	588.97	Calculated Property
λ	0.05	W/m×K	671.18	Calculated Property
λ	0.06	W/m×K	753.38	Calculated Property
λ	0.07	W/m×K	835.59	Calculated Property
λ	0.08	W/m×K	917.79	Calculated Property
λ	0.10	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.25; 0.25]	W/m×K	[260.15; 470.45]	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			1.68400e-01
Coefficient B			-3.13750e+02
Coefficient C			-1.07200e+00
Coefficient D			-5.80540e-05
Coefficient E			-3.24430e-06
Comment			ChemSep eq 16, LiquidThermalConductivity
Temperature range, min.			260.15
Temperature range, max.			470.45
λ	0.25	W/m×K	260.15	Calculated Property
λ	0.25	W/m×K	283.52	Calculated Property
λ	0.26	W/m×K	306.88	Calculated Property
λ	0.26	W/m×K	330.25	Calculated Property
λ	0.26	W/m×K	353.62	Calculated Property
λ	0.26	W/m×K	376.98	Calculated Property
λ	0.26	W/m×K	400.35	Calculated Property
λ	0.26	W/m×K	423.72	Calculated Property
λ	0.25	W/m×K	447.08	Calculated Property
λ	0.25	W/m×K	470.45	Calculated Property

Similar Compounds

Find more compounds similar to 1,2-Ethanediol.

Mixtures

• Acetonitrile + 1,2-Ethanediol
• Acetonitrile + 1,2-Ethanediol + Water
• 1,2-Ethanediol + Acetone
• 1,2-Ethanediol + Acetone + Methyl Alcohol
• 1,2-Ethanediol + Acetone + Water
• 1,2-Ethanediol + 1-Butanol
• 2-Propanol + 1,2-Ethanediol
• 1,2-Ethanediol + Acetic acid
• 1,2-Ethanediol + Acetic acid, butyl ester
• 1,2-Ethanediol + Ethanol
• 1,2-Ethanediol + Ethanol + Ethyl Acetate
• 1,2-Ethanediol + Ethanol + Water
• 1,2-Ethanediol + Ethyl Acetate
• 1,2-Ethanediol + Methyl Alcohol
• 1,2-Ethanediol + Tetrahydrofuran + Methyl Alcohol
• 1,2-Ethanediol + 2-Pyrrolidinone, 1-methyl-
• 1,2-Ethanediol + Naphthalene
• 1,2-Ethanediol + Tetrahydrofuran
• 1,2-Ethanediol + Water
• Methane + 1,2-Ethanediol

Find more mixtures with 1,2-Ethanediol.

Sources

• KDB Vapor Pressure Data
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Application of the Multi-Current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols
• Vapor Liquid Equilibrium for Binary Mixtures of 1,4-Diazabicyclo[2.2.2]octane with Ethylenediamine, Ethanolamine, and Ethylene Glycol
• Volumetric Properties of Binary Mixtures of 2,4,6-Trimethylpyridine with 1,2-Ethanediol, Methanol, and Water, and the Association Energies of the O-H***N Bonded Complexes
• Revision of the volumetric method for measurements of liquid liquid equilibria in binary systems
• Solubility of 9-fluorenone, thianthrene and xanthene in organic solvents
• Vapor liquid equilibrium in the system ethane + ethylene glycol
• Binary liquid liquid equilibrium in the systems containing monofunctional benzene derivates and 1,2-ethanediol
• Binary vapor liquid equilibrium of methyl glycolate and ethylene glycol
• High-pressure vapor liquid equilibria of systems containing ethylene glycol, water and methane Experimental measurements and modeling
• Measurement of the thermodynamic properties for the reactive system ethylene glycol acetic acid
• Liquid liquid equilibria of the systems dipropyl ether + n-propanol +water and dipropyl ether + n-propanol + ethylene glycol 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
• New device for fast measuring surface tension, density and viscosity of liquids
• Osmotic coefficient data and an excess Gibbs energy function for single-phase complex system of glucose + alcohol +water
• Study on ion solvent interactions of alkali metal salts in pure methanol and its binary mixtures with ethane-1,2-diol by a conductometric technique
• Mutual diffusion coefficients of aqueous solutions of some glycols
• Dielectric constant and molecular association in binary mixtures of N,N-dimethylethanolamine with alcohols and amides
• Static permittivity and molecular interactions in binary mixtures of ethanolamine with alcohols and amides
• Solubility of decanedioic acid in binary solvent mixtures
• Measurement and correlation of solubility of benzamide in supercritical carbon dioxide with and without cosolvent
• Liquid phase behavior of hexafluorophosphate ionic liquids with polyhydric alcohols
• Solubility of o-tolidine in pure and modified supercritical carbon dioxide
• 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
• Distribution of MEG and methanol in well-defined hydrocarbon and water systems: Experimental measurement and modeling using the CPA EoS
• Phase equilibria for the ternary systems ethanol, water + ethylene glycol or + glycerol at 101.3 kPa
• Liquid phase PVTx properties of binary mixtures of (water + ethylene glycol) in the range from 278.15 to 323.15 K and from 0.1 to 100 MPa. I. Experimental results, partial and excess thermodynamics properties
• Measurement and correlation of vapor-liquid equilibria for alkane + alkanol andalkane + alkanediol systems with group contribution COSMOSPACE model
• Enthalpies and Gibbs free energies of solvation in ethylene glycol at298 K: Influence of the solvophobic effect
• Excess volumes and excess heat capacities for alkanediol + water systems in the temperature interval (283.15-313.15) K
• Prediction of refractive index and density of deep eutectic solvents using atomic contributions
• Electrical conductivity of ammonium and phosphonium based deepeutectic solvents: Measurements and artificial intelligence-basedprediction
• Effect of structural alteration of ionic liquid on their bulk and molecular level interactions with ethylene glycol
• Mutual diffusion coefficients, density, and viscosity of aqueoussolutions of new polyamine CO2absorbents
• Solid-liquid equilibrium of dicyandiamide in different solvents
• A simple method for estimating mutual diffusion coefficients of ionic liquids-water based on an optofluidic chip
• Acoustic investigation of choline chloride based ionic liquids analogues
• Phase behavior of imidazolium and phosphonium tetrafluoroborates with dihydroxy alcohols
• tert-Butyl chloride as a probe of the solvophobic effects
• Liquid-liquid equilibrium data for binary systems containing o-dichlorobenzene and nitrobenzene
• Solubility of dilute sulfur dioxide in binary mixtures of ethylene glycol and tetraethylene glycol dimethyl ether
• Density, transport properties and electrochemical potential windows for the 2-hydroxy-N,N,N-trimethylethanaminium chlorides based ionic liquids at several temperatures
• Liquid-liquid phase equilibrium for ternary mixtures of formamide (or ethylene glycol, or monoethanolamine) + indole + 2-methylnaphthalene at 308.15 K
• Absorption, desorption and spectroscopic investigation of sulfur dioxide in the binary system ethylene glycol + dimethyl sulfoxide
• Liquid-liquid equilibria for the extraction of phenols from alkane using ethylene glycol
• New measurements and modeling of high pressure thermodynamic properties of glycols
• Formation of type III deep eutectic solvents and effect of water on their intermolecular interactions
• Acoustic, volumetric, transport, optical and rheological properties of benzyltripropylammonium based Deep Eutectic Solvents
• Thermodynamic analysis of the solubility of polymorphic cytarabine in a variety of pure solvents
• Thermodynamics of phase transfer for polar molecules from alkanes to deep eutectic solvents
• Solubility of glucose in tetrabutylammonium bromide based deep eutectic solvents: Experimental and molecular dynamic simulations
• Solubility and dissolution characteristics of capecitabine in pure lower alcohols and water with methanol mixture solvents at atmospheric pressure and different temperatures
• Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
• Extractive distillation of methylal/methanol mixture using ethylene glycol as entrainer
• An investigation on the solid-liquid phase equilibrium of the quaternary system KH2PO4-H3PO4-CH2OHCH2OH-H2O
• Oil desulfurization using deep eutectic solvents as sustainable and economical extractants via liquid-liquid extraction: Experimental and PC-SAFT predictions
• Extraction of benzothiazole and thiophene from their mixtures with n-heptane using tetrahexylammonium bromide-based deep eutectic solvents as extractive denitrogenation and desulfurization agents
• Effective extraction of benzene and thiophene by novel deep eutectic solvents from hexane / aromatic mixture at different temperatures
• Solubilities of carbon dioxide, oxygen, and nitrogen ethylene glycol solution under low pressures
• The experimental study on the influence of crown ethers and glycols on the mutual solubility of lithium bromide in water
• Thermodynamic equilibrium of hexamethylenediammonium glutarate in mono-solvents and binary solvent systems
• Thermophysical characterization of the deep eutectic solvent choline chloride:ethylene glycol and one of its mixtures with water
• Thermodynamic characterization of deep eutectic solvents at high pressures
• Partial molar volumes of organic solutes in water. XIV. Polyhydric alcohols derived from ethane and propane at temperatures T = 298 K to T = 573 K and at pressures up to 30 MPa
• Transport properties of 2:2 symmetrical electrolytes in (water + ethylene glycol) binary mixtures at T = 293.15 K
• Densities and volumetric properties of (formamide + ethanol, or 1-propanol, or 1,2-ethanediol, or 1,2-propanediol) mixtures at temperatures between 293.15 K and 318.15 K
• Structural and interactional studies of homologous series of a,x-alkanediols in N,N-dimethylformamide
• Volumetric and compressibility properties of liquid water as a solute in glycolic, propylene carbonate, and tetramethylurea solutions at T = 298.15 K
• Molecular interactions of a,x-alkanediols in pyrrolidin-2-one: Thermophysical and spectroscopic measurements
• Density and refractive index in mixtures of ionic liquids and organic solvents: Correlations and predictions
• (Liquid + liquid) equilibria for ternary mixtures of (ethylene glycol + toluene + n-octane)
• Thermodynamic and transport properties of (1,2-ethanediol + 1-nonanol) at temperatures from (298.15 to 313.15) K
• Non-ideal behaviour of imidazolium based room temperature ionic liquids in ethylene glycol at T = (298.15 to 318.15) K
• Solubility of methane and carbon dioxide in ethylene glycol at pressures up to 14 MPa and temperatures ranging from (303 to 423) K
• Solubilities, densities and refractive indices for the ternary systems ethylene glycol + MCl + H2O (M = Na, K, Rb, Cs) at (15 and 35) C
• Surface tension of non-ideal binary and ternary liquid mixtures at various temperatures and p = 81.5 kPa
• (Liquid + liquid) equilibria for mixtures of (ethylene glycol + benzene + cyclohexane) at temperatures (298.15, 308.15, and 318.15) K
• 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
• Thermodynamic and spectroscopic studies on binary mixtures of imidazolium ionic liquids in ethylene glycol
• Solubility of sodium 4-nitrotoluene-2-sulfonate in (propanol + water) and (ethylene glycol + water) systems
• Liquid liquid equilibrium data for mono ethylene glycol extraction from water with the new ionic liquid tetraoctyl ammonium 2-methyl-1-naphtoate as solvent
• PqT measurements and derived properties of liquid 1,2-alkanediols
• Viscosity and density data for the ternary system water(1) ethanol(2) ethylene glycol(3) between 298.15 K and 328.15 K
• Investigation on some thermophysical properties of poly(ethylene glycol) binary mixtures at different temperatures
• Liquid liquid equilibria for ternary systems of (ethylene glycol + toluene + heptane) at temperatures (303.15, 308.15, and 313.15) K and atmospheric pressure: Experimental results and correlation with UNIQUAC and NRTL models
• Solubility for dilute sulfur dioxide in binary mixtures of N,N-dimethylformamide + Ethylene Glycol at T = 308.15 Kand p = 122.66 kPa
• Solubilities of some gases in four immidazolium-based ionic liquids
• Densities, refractive indices, and viscosities of N,N-diethylethanol ammonium chloride - glycerol or - ethylene glycol deep eutectic solvents and their aqueous solutions
• Thermophysical profile of ethylene glycol-based ZnO nanofluids
• (Vapour + liquid) equilibria in the ternary system (acetonitrile + n-propanol + ethylene glycol) and corresponding binary systems at 101.3 kPa
• Aggregation properties and thermodynamics of micellization of gemini surfactants with diethyl ether spacer in water and water organic solvent mixed media
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Thermal conductivity of dry anatase and rutile nano-powders and ethylene and propylene glycol-based TiO2 nanofluids
• Liquid extraction of polyhydric alcohols from water using [A336][SCN] as a solvent
• Solubility of rosuvastatin calcium in different neat solvents at different temperatures
• Solubility and thermodynamic function of a bioactive compound bergenin in various pharmaceutically acceptable neat solvents at different temperatures
• Speed of sound in saturated aliphatic alcohols (propan-2-ol, butan-2-ol, and 2-methylpropan-1-ol) and alkanediols (ethane-1,2-diol, propane-1,2- and -1,3-diol) at temperature between 253.15 K and 353.15 K and pressures up to 30 MPa
• Viscosity of binary mixtures of 1-ethyl-3-methylimidazolium tetrafluoroborate ionic liquid with four organic solvents
• Measurement and prediction of dabigatran etexilate mesylate Form II solubility in mono-solvents and mixed solvents
• Experimental determination of the LLE data of systems consisting of {hexane + benzene + deep eutectic solvent} and prediction using the Conductor-like Screening Model for Real Solvents
• Molar enthalpy of mixing and refractive indices of choline chloride-based deep eutectic solvents with water
• Activity coefficients at infinite dilution of hydrocarbons in glycols: Experimental data and thermodynamic modeling with the GCA-EoS
• Measurement and thermodynamic modeling of ternary (liquid + liquid) equilibrium for extraction of ethanol from diethoxymethane solution with different solvents
• Phase equilibria in the system Na+, K+//SO4(2-)-(CH2OH)2-H2O and Na+, K+//Cl , SO4(2-)-(CH2OH)2-H2O at 328.15 K
• Thermodynamic and transport properties of acetonitrile + alkanediols liquid mixtures at different temperatures, experimental measurements and modeling
• Liquid-liquid equilibria for toluene/heptane + phenol/cresols + ethylene glycol system
• Density and refractive index measurements of transition-temperature mixture (deep eutectic analogues) based on potassium carbonate with dual hydrogen bond donors for CO2 capture
• Separation of azeotrope (allyl alcohol + water): Isobaric vapour-liquid phase equilibrium measurements and extractive distillation
• Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
• 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
• Removal of 2- and 3-methylthiophene from their mixtures with n-heptane using tetrahexylammonium bromide-based deep eutectic solvents as extractive desulfurization agents
• Measurements and correlations of solubility of N2O in and density, viscosity of partially CO2 loaded water-lean amino acid salts
• Acoustic and thermodynamic study of D-Panthenol in aqueous solutions of glycol at different temperatures
• Solvent screening and liquid-liquid measurement for extraction of phenols from aromatic hydrocarbon mixtures
• Solubilities of CO2 in, densities and kinematic viscosities of poly(propylene glycol) diglycidyl ether and poly(ethylene glycol) monooleate
• Enthalpies and heat capacities of solution of urea and tetramethylurea in water, ethylene glycol and formamide
• Permittivity and electrical conductivity of copper oxide nanofluid (12 nm) in water at different temperatures
• Equilibrium solubility determination, modelling and preferential solvation of bioactive iminodibenzyl in aqueous co-solvent mixtures at various temperatures
• Equilibrium solubility of dinitolmide in several neat solvents and binary aqueous co-solvent mixtures: Experimental determination and thermodynamic analysis
• Solubility modelling and thermodynamic properties of allopurinol in aqueous solutions of four deep eutectic solvents
• Equilibrium solubility investigation and thermodynamic aspects of biologically active gimeracil (form P) dissolved in aqueous co-solvent mixtures of isopropanol, N,N-dimethylformamide, ethylene glycol and dimethylsulfoxide
• Solubility and thermodynamic properties of NH3 in choline chloride-based deep eutectic solvents
• Volume-related solvation and pair interaction parameters for dilute solutions of urea and tetramethylurea in ethylene glycol between 288.15 K and 328.15 K: A comparative analysis
• Thermodynamic solubility modelling, solvent effect and preferential solvation of p-nitrobenzamide in aqueous co-solvent mixtures of dimethyl sulfoxide, ethanol, isopropanol and ethylene glycol
• Excess molar enthalpies of binary mixtures containing ethylene glycols or poly(ethylene glycols) + ethyl alcohol at 308.15K and atmospheric pressure
• Experimental and predicted excess molar enthalpies of some working pairs for absorption cycles
• Dielectric constants and hydrogen bonded structures in amide-alcohol mixed solvents
• Enthalpic Interaction Coefficients of N,N-Dimethylformamide in Aqueous Ethylene Glycol and Glycerol Solutions at 298.15K
• Densities of Ammonium and Phosphonium based Deep Eutectic Solvents: Prediction using Artificial Intelligent and Group Contribution Techniques
• Solubilities of benzene sulfonamide in supercritical CO2 in the absence and presence of cosolvent
• Molar heat capacities of choline chloride-based deep eutectic solvents and their binary mixtures with water
• Vapor pressure of aqueous choline chloride-based deep eutectic solvents (ethaline, glyceline, maline and reline) at 30 to 70 deg C
• Enthalpies and heat capacities of interaction of tetraalkylammonium bromides with hexamethyl phosphoric triamide in water, methanol and ethylene glycol: the comparative analysis of aqueous and non-aqueous systems
• High-pressure volumetric properties of choline chloride-ethylene glycol based deep eutectic solvent and its mixtures with water
• Solubility of carbon dioxide in a choline chloride-ethylene glycol based deep eutectic solvent
• Thermodynamic study on some alkanediol solutions: measurement and molecular modeling
• Molar heat capacities and electrical conductivities of two ammonium-based deepeutectic solvents and their aqueous solutions
• Application of the Eotvos and Guggenheim empirical rules for predicting the density and surface tension of ionic liquids analogues
• Ionic Liquids Analogues Based on Potassium Carbonate
• Thermodynamics of the amino acid -ethylene glycol pair interaction
• Densities of aqueous mixtures of (choline chloride + ethylene glycol) and (choline chloride + malonic acid) deep eutectic solvents in temperature range 283.15-363.15 K
• Temperature controlled photoacoustic device for thermal diffusivity measurements of liquids and nanofluids
• Standard molar Gibbs free energy and enthalpy of solvation of lowpolar solutes in formamide derivatives at 298 K
• Thermodynamics of hydrogen bonding and van der Waals interactions of organic solutes in solutions of imidazolium based ionic liquids: "structure-property" relationships
• Experimental studies on viscosity, thermal and electrical conductivity of aluminum nitride ethylene glycol (AlN-EG) nanofluids
• Thermal conductivity enhancement of ethylene glycol and water with graphene nanoplatelets
• Enthalpies of solution and enthalpies of solvation of organic solutes in ethylene glycol at 298.15 K: Prediction and analysis of intermolecular interaction contributions
• Viscosity, thermal and electrical conductivity of silicon dioxide - ethylene glycol transparent nanofluids: An experimental studies
• Analysis of solute-pyridine intermolecular interactions based on experimental enthalpies of solution and enthalpies of solvation of solutes dissolved in pyridine
• Measurement of the thermal conductivity of SiO2 nanofluids with an optimized transient hot wire method
• An experimental study on thermal conductivity enhancement of DI water-EG based ZnO(CuO)/graphene wrapped carbon nanotubes nanofluids
• Thermal transport properties of heptane-isooctane mixtures
• Solubility Measurement and Modeling for the NaCl-NH4Cl-Monoethylene Glycol-H2O System from (278 to 353) K
• Solubility and Thermodynamic Analysis of Tenoxicam in Different Pure Solvents at Different Temperatures
• 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 of Hydrogen Sulfide in Ethanediol, 1,2-Propanediol, 1-Propanol, and 2-Propanol: Experimental Measurement and Modeling
• Solubility of 1,3,5-Benzenetricarboxylic Acid in Different Solvents
• Molar Heat Capacity of Selected Type III Deep Eutectic Solvents
• Investigation on Thermodynamics in Separation for Ethylene Glycol + Neopentyl Glycol System by Azeotropic Distillation
• Experimental Measurement and Modeling of Vapor Liquid Equilibrium for the Ternary Systems Water + Ethanol + Ethylene Glycol, Water + 2-Propanol + Ethylene Glycol, and Water + 1-Propanol + Ethylene Glycol
• Solubility of 3,7,9,11-Tetraoxo-2,4,6,8,10-pentaaza[3.3.3] Propellane (TOPAP) in Different Pure Solvents at Temperatures between 273.15 and 318.15 K
• Experimental Study on the Solubility of Carbon Dioxide in Systems Containing Ethane-1,2-diol + Water + Salt (Sodium Chloride or Calcium Carbonate)
• Isobaric Vapor Liquid Equilibria for Binary Mixtures of .gamma.-Valerolactone + Methanol, Ethanol, and 2-Propanol
• Excess Molar Enthalpies of Deep Eutectic Solvents (DESs) Composed of Quaternary Ammonium Salts and Glycerol or Ethylene Glycol
• Solubility of 4-Methylsulfonylacetophenone in Nine Pure Solvents and (Ethyl Acetate + n-Hexane) Binary Solvent Mixtures from 278.15 K to 328.15 K
• Viscosities and Carbon Dioxide Solubilities of Guanidine Carbonate and Malic Acid-Based Eutectic Solvents
• Thermodynamic Properties and Solubility of Sodium and Potassium Chloride in Ethane-1,2-diol/Water Mixed Solvent Systems to High Temperatures
• Liquid Liquid Equilibria of Binary, Ternary, and Quaternary Systems Involving Monoethylene Glycol, Water, Toluene, p-Xylene, Hexane, and Octane
• Specific Heat Capacities of Two Functional Ionic Liquids and Two Functional Deep Eutectic Solvents for the Absorption of SO2
• Experimental Measurement and Modeling of Vapor Liquid Equilibrium for the Ternary System Water + Acetonitrile + Ethylene Glycol
• Thermophysical Properties and Solubility of Different Sugar-Derived Molecules in Deep Eutectic Solvents
• Solubility and Thermodynamic Behavior of Syringic Acid in Eight Pure and Water + Methanol Mixed Solvents
• Investigation on Temperature-Dependent Volumetric and Acoustical Properties of Homologous Series of Glycols in Aqueous Sorbitol Solutions
• Phase Behavior of CO2 in Monoethylene Glycol between 263.15-343.15 K and 0.2-40.3 MPa: An Experimental and Modeling Approach
• Liquid-Liquid Equilibrium for Ternary System n-Butanol + n-Hexane + Ethylene Glycol at 298.15-323.15 K
• Effect of the Type of Ammonium Salt on the Extractive Desulfurization of Fuels Using Deep Eutectic Solvents
• Measurement and Correlation of the Dissolution Equilibria of o-Iodoaniline and p-Iodoaniline in Pure Solvents
• Measurement and Modeling of Isobaric Vapor-Liquid Equilibrium of Water + Glycols
• Solubility of p-Aminobenzoic Acid Potassium in Organic Solvents and Binary (Water + Isopropyl Alcohol) Mixture at Temperatures from (283.15 to 318.15) K
• Thermodynamic and Kinetic Studies of CO2 Capture by Glycol and Amine-Based Deep Eutectic Solvents
• Density of Working Liquids for Diffusion Vacuum Pumps
• Experimental Vapor-Liquid Equilibrium Data for Binary Mixtures of Methyldiethanolamine in Water and Ethylene Glycol under Vacuum
• Thermodynamic Interactions Study of Some Ethylene Glycols in Aqueous Aniline Solutions at Different Temperatures: An Acoustical and Volumetric Approach
• Ternary Vapor-Liquid Equilibrium Measurements and Modeling of Ethylene Glycol (1) + Water (2) + Methane (3) Systems at 6 and 12.5 MPa
• Solubility of Acetylene in Alcohols and Ketones
• 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
• Solubilities of Organic Semiconductors and Nonsteroidal Anti-inflammatory Drugs in Pure and Mixed Organic Solvents: Measurement and Modeling with Hansen Solubility Parameter
• The Dependence of Temperature and Composition on the Equilibrium Solubility and Thermodynamic Studies of Bioactive N-(9-Fluorenylmethoxycarbonyloxy)succinimide in Various Water-Cosolvent Mixtures
• Solid-Liquid Equilibrium of Rebaudioside A in Pure and Binary Mixed Solvents at T = (288.15 to 328.15) K
• Solubility Modeling and Solvent Effect of 2-Amino-6-chloropurine in Twelve Neat Solvents
• Measurement and Correlation of the Solubility of Palmatine Chloride in Four Different Binary Solvent Systems at (283.15-328.15) K
• Phase Equilibrium Involving Xylose, Water, and Ethylene Glycol or 1,2-Propylene Glycol at Different Temperatures
• Liquid-Liquid Equilibrium Measurements and Correlation for Ternary Systems (Butyl Acetate + 1-Butanol + Ethylene Glycol/1,3-Propanediol/Ethanolamine) at 298.15 K
• Salt Effect on the Liquid-Liquid Equilibrium for the Water-Ethylene Glycol-Ethylene Glycol Diacetate System
• Solubility and Solution Thermodynamics of 3-Nitrophthalonitrile in 12 Neat Solvents at Temperatures from 278.15 to 323.15 K
• Experimental Determination and Modeling of Liquid-Liquid Equilibrium for Ternary Mixtures of Ethylene Glycol + 1,2-Butanediol + 3-Heptanone or Anisole
• Solubility Determination and Modeling of p-Nitrobenzamide Dissolved in Twelve Neat Solvents from 283.15 to 328.15 K
• Liquid-Liquid Equilibrium of the Ternary System sec-Butyl Acetate + sec-Butyl Alcohol + Ethylene Glycol at 298.2, 308.2, and 318.2 K
• Thermophysical and Molar Volume Aberration of Amphiphilic Eutectic Mix of Bivalent Diols and Ammonium-Ionic Liquid
• Heat Capacity and Phase Behavior of Selected Oligo(ethylene glycol)s
• Propylthiouracil Solubility in Aqueous Solutions of Ethylene Glycol, N,N-Dimethylformamide, N-Methyl-2-pyrrolidone, and Dimethylsulfoxide: Measurement and Thermodynamic Modeling
• Solubility of d-Tryptophan and l-Tyrosine in Several Organic Solvents: Determination and Solvent Effect
• Measurement and Correlation of Solubilities of 5,5'-Dinitramino-3,3'-bi[1,2,4-triazolate] Carbohydrazide Salt (CBNT) in Various Pure Solvents and a Binary Mixture (Dimethyl Sulfoxide + Water) from 298.15 to 343.15 K
• Solubility and Solvent Effect of Acetamiprid in Thirteen Pure Solvents and Aqueous Solutions of Ethanol
• Liquid-Liquid Equilibria for Benzene/Thiophene + Cyclohexane/Hexadecane + Deep Eutectic Solvents: Data and Correlation
• Solubility of d-Aspartic Acid in Several Neat Solvents: Determination, Modeling, and Solvent Effect Analysis
• Liquid-Liquid Equilibrium Measurements for the Extraction of Pyridine and Benzothiazole from n-Alkanes Using Deep Eutectic Solvents
• Fixed-Path Length Laser-Induced Sound Pinging: A Streamlined Method for Sound Speed Determination in Arbitrary Liquids
• Equilibrium Solubility Determination and Modeling of Fenbendazole in Cosolvent Mixtures at (283.15-328.15) K
• Solubility and Solvent Effect of 1-(2-Bromo-phenyl)-pyrrole-2,5-dione in 14 Pure Solvents from 278.15 to 323.15 K
• Solubility of Acetoguanamine in Twelve Neat Solvents from 283.15 to 323.15 K
• Density and Viscosity of the Nonaqueous and Aqueous Mixtures of Methyldiethanolamine and Monoethylene Glycol at Temperatures from 283.15 to 353.15 K
• Determination and Modeling of d-Histidine Solubility in Several Pure Solvents from 293.15 to 333.15 K
• Solubility and Data Correlation of b-Arbutin in Different Monosolvents from 283.15 to 323.15 K
• Solubility and Solution Thermodynamics of 2,6-Dichloro-4-nitroaniline in 12 Pure Solvents at Temperatures from 278.15 to 323.15 K
• Thermodynamic Solubility and Mixing Properties of Phenformin in 14 Pure Solvents at Temperatures Ranging from 278.15 to 323.15 K
• Infinite Dilution Activity Coefficients in Ethylene Glycol and Ethylene Carbonate
• Excess Molar Volumes, Viscosities, and Heat Capacities for the Mixtures of Ethylene Glycol + Water from 273.15 K to 353.15 K
• Densities, Viscosities, and Excess Properties for Binary Mixtures of Some Glycols and Polyglycols in N-Methylacetamide at 308.15 K
• Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
• Surface Tension of Binary Mixtures of Ethanol + Ethylene glycol from 20 to 50 oC
• Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethanediol, + Hexane, + Tributylamine, or + Triethylamine at (298.15, 303.15, and 308.15) K
• Measurement and Correlation of Excess Molar Enthalpies for Ethylene Glycol + Alkanol Systems at the Temperatures (298.15, 308.15, and 323.15) K
• Isobaric Vapor - Liquid Equilibria for the Ternary System of 2-Methyl-1-butanol, 3-Methyl-1-butanol, and Ethylene Glycol at 101.3 kPa
• 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
• Solubility of Tripolycyanamide and Cyanuric Acid in Ethanediol, N,N-Dimethylformamide, and N,N-Dimethylacetamide from (301.07 to 363.35) K
• Thermodynamic Study of Binary Mixtures Containing Glycols or Polyethylene Glycols + Benzyl Alcohol at 308.15 K
• Isothermal Vapor-Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Water + 1,2-Ethanediol and Propene + Acetophenone
• Liquid-Liquid Equilibria for Monoethylene Glycol + Water + Alkane Systems in the Range (273 to 313) K and Atmospheric Pressure
• Equilibrium Surface Tensions of Benzyl Alcohol + Ethylene Glycol Mixtures
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
• Isobaric Vapor-Liquid Equilibria of Binary Mixtures Containing the Carbonate Group -OCOO-
• Surface Properties of Pure Liquids and Binary Liquid Mixtures of Ethylene Glycol + Methylcyclohexanols
• 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
• Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes
• Surface Tensions of Dilute Solutions of Cycloheptanol in Ethylene Glycol
• Static Relative Permittivities of Water + Ethane-1,2-diol and Water + Propane-1,2,3-triol under Pressures up to 300 MPa at 298.15 K
• Excess Molar Volumes and Viscosities of Binary Mixtures of p-Cresol with Ethylene Glycol and Methanol at Different Temperature and Atmospheric Pressure
• Densities and Viscosities of Binary Mixtures of m-Cresol with Ethylene Glycol or Methanol over Several Temperatures
• Liquid-Liquid Equilibria for Binary and Ternary Systems Containing Glycols, Aromatic Hydrocarbons, and Water: Experimental Measurements and Modeling with the CPA EoS
• Densities, Viscosities, and Sound Speeds of Some Acetate Salts in Binary Mixtures of Tetrahydrofuran and Methanol at (303.15, 313.15, and 323.15) K
• Vaporization Enthalpies of the r,o-Alkanediols by Correlation Gas Chromatography
• Cosolvent Selection for Benzene-Cyclohexane Separation in Extractive Distillation
• Densities and Volumetric Properties of Ethylene Glycol + Dimethylsulfoxide Mixtures at Temperatures of (278.15 to 323.15) K and Pressures of (0.1 to 100) MPa
• Phosphonium-Based Ionic Liquids Analogues and Their Physical Properties
• Density, Viscosity, and Excess Properties for 1,2-Diaminoethane + 1,2-Ethanediol at (298.15, 303.15, and 308.15) K
• Solubility of 3,5-Dinitrobenzoic Acid in Supercritical Carbon Dioxide with Cosolvent at Temperatures from (308 to 328) K and Pressures from (10.0 to 21.0) MPa
• Solubility of Carbonyl Sulfide in Aqueous Solutions of Ethylene Glycol at Temperatures from (308.15 K to 323.15) K
• Viscosities of Acetate or Chloride-Based Ionic Liquids and Some of Their Mixtures with Water or Other Common Solvents
• Liquid-Liquid Equilibrium in Ternary Systems Containing Ethylene Glycol, Monofunctional Benzene Derivative, and Ethyl Acetate
• Densities and Viscosities for Binary Mixtures of 1-Butyl-3-Methylimidazolium Tetrafluoroborate Ionic Liquid with Molecular Solvents
• Solubility of CO2 in Alcohols, Glycols, Ethers, and Ketones at High Pressures from (288.15 to 318.15) K
• Measurement and Correlation of Solubilities of (Z)-2-(2-Aminothiazol-4-yl)-2-methoxyiminoacetic Acid in Different Pure Solvents and Binary Mixtures of Water + (Ethanol, Methanol, or Glycol)
• Activity Coefficients of RbF or CsF in the Ethene Glycol + Water System by Potentiometric Measurements at 298.15 K
• Isobaric Vapor-Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems
• Solubility of Ethylene Glycol in Supercritical Carbon Dioxide at Pressures up to 19.0 MPa
• Solubility, Density, Refractive Index, and Viscosity for the Polyhydric Alcohol + CsBr + H2O Ternary Systems at Different Temperatures
• Solid Liquid Equilibria of 1-Ethyl-3-methylimidazolium Hexafluorophosphate + Polyols
• Densities and Excess Properties of Primary Amines in Alcoholic Solutions
• Solubility of Sodium Salts in Ammonium-Based Deep Eutectic Solvents
• Isobaric Vapor Liquid Equilibria for the Binary Mixtures Composed of Ethylene Glycol, 1,2-Propylene Glycol, 1,2-Butanediol, and 1,3-Butanediol at 10.00 kPa
• Partial Molar Volumes and Partial Molar Isentropic Compressions of Selected Alkane-?,?-diols at Infinite Dilution in Water at Temperatures T = (278 to 318) K and Atmospheric Pressure
• Vapor Liquid Equilibria for Three Binary Systems of N-Methylethanolamine, N-Methyldiethanolamine, and Ethylene Glycol at P = (40.0, 30.0, and 20.0) kPa
• Physicochemical Studies on the Micellization of Cationic, Anionic, and Nonionic Surfactants in Water Polar Organic Solvent Mixtures
• Solubilities of CO2 in, and Densities and Viscosities of, the Piperazine + 1-Ethyl-3-methyl-imidazolium Acetate + H2O System
• Determination and Modeling of Isobaric Vapor Liquid Equilibria for the Methylcarbamate + Methyl-N-phenyl Carbamate System at Different Pressures
• Density and Refractive Index of Binary Mixtures of Two 1-Alkyl-3-methylimidazolium Ionic Liquids with 1,4-Dioxane and Ethylene Glycol
• Solubility of Carbon Dioxide in Ethane-1,2-diol Water Mixtures
• Equilibrium Solubilities of 2-Cyanoguanidine in Water + (Ethane-1,2-diol or N,N-Dimethylformamide) Mixtures at Different Temperatures: An Experimental and Correlational Study
• Comparative Study of the Solubilities of SO2 in Five Low Volatile Organic Solvents (Sulfolane, Ethylene Glycol, Propylene Carbonate, N-Methylimidazole, and N-Methylpyrrolidone)
• Isobaric Vapor Liquid Equilibrium for the Binary System (Ethane-1,2-diol + Butan-1,2-diol) at (20, 30, and 40) kPa
• 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 Metoclopramide Hydrochloride in Six Green Solvents at (298.15 to 338.15) K
• Tetrabutylammonium Chloride Based Ionic Liquid Analogues and Their Physical Properties
• Solubility of (2Z)-N-Cyclohexyl-2-(3-hydroxybenzylidine) Hydrazine Carbothioamide in Different Pure Solvents at (298.15 to 338.15) K
• Solubility of N-(4-Chlorophenyl)-2-(pyridin-4-ylcarbonyl)hydrazinecarbothioamide (Isoniazid Analogue) in Five Pure Solvents at (298.15 to 338.15) K
• Liquid Liquid Equilibria at Three Temperatures (between 280.15 K and 333.15 K) of Binary, Ternary, and Quaternary Systems Involving Monoethylene Glycol, Water, Cyclohexane, para-Xylene, trans- and cis-Dimethylcyclohexane, and trans- and cis-Decahydronaphthalene
• Solubility and Solvation Thermodynamics of a Series of Homologous a-Amino Acids in Nonaqueous Binary Mixtures of Ethylene Glycol and Dimethyl Sulfoxide
• Correlation of Solubility of Bioactive Compound Reserpine in Eight Green Solvents at (298.15 to 338.15) K
• Solubility Properties and Spectral Characterization of Dilute SO2 in Binary Mixtures of Urea + Ethylene Glycol
• Measurement, Correlation, and Thermodynamics of Solubility of Isatin in Nine Different Green Solvents at (298.15 to 338.15) K
• Solubility Determination and Thermodynamic Models for 2-Methylnaphthalene in Different Solvents from T = (278.15 to 303.15) K
• Isobaric Vapor Liquid Equilibrium for Two Binary Systems{Propane-1,2-diol + Ethane-1,2-diol and Propane-1,2-diol + Butane-1,2-diol} at p = (10.0, 20.0, and 40.0) kPa
• Experimental Study of Solubility of Natural Gas Components in Aqueous Solutions of Ethylene Glycol at Low-Temperature and High-Pressure Conditions
• Densities and Excess Molar Volumes for Binary Mixtures of 1,4-Butanediol + 1,2-Propanediol, + 1,3-Propanediol, and + Ethane-1,2-diol from (293.15 to 328.15) K
• Liquid-Liquid Equilibria of (Limonene + Linalool + Ethylene Glycol or Diethylene Glycol or Triethylene Glycol or 1,2-Propylene Glycol) Ternary Systems
• Densities, Excess Molar Volumes, and Isobaric Thermal Expansibilities for 1,2-Ethanediol + 1-Butanol, or 1-Hexanol, or 1-Octanol in the Temperature Range from (293.15 to 313.15) K
• Surface Properties of Binary Mixtures of Ethylene Glycol with a Series of Aliphatic Alcohols (1-Pentanol, 1-Hexanol, and 1-Heptanol)
• Gas-Liquid Equilibrium Data for the Mixture Gas of Sulfur Dioxide/Nitrogen with Ethylene Glycol at Temperatures from (298.15 to 313.15) K under Low Pressures
• Gas-Liquid Equilibrium Data for a Mixture Gas of Sulfur Dioxide + Nitrogen with Ethylene Glycol Aqueous Solutions at 298.15 K and 123.15 kPa
• Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
• Solubility of p-Toluenesulfonamide in Pure and Modified Supercritical Carbon Dioxide
• Solubility of l-Lysine Hydrochloride in Dimethyl Sulfoxide, Methanol, Ethanol, Water, and Glycol between (283 and 323) K
• Electrical Conductances of Tetrabutylammonium Bromide, Sodium Tetraphenylborate, and Sodium Bromide in Ethylene Glycol (1) + Water (2) Mixtures at (298.15, 303.15, 308.15, and 318.15) K
• Apparent Molar Volumes and Electrical Conductance of Ionic Liquids [Cnmim]Br (n = 8, 10, 12) in Ethylene Glycol, N,N-Dimethylformamide, and Dimethylsulfoxide at 298.15 K
• Liquid-Liquid Equilibria for Monoethylene Glycol + Hexane and 2,2,4-Trimethylpentane, Water + Hexane and 2,2,4-Trimethylpentane, Monoethylene Glycol + Water + Hexane, and Monoethylene Glycol + Water + 2,2,4-Trimethylpentane in the Temperature Range between T = 283.15 K and T = 323.15 K
• Vapor Pressure Measurements of Hydroxyacetaldehyde and Hydroxyacetone in the Temperature Range (273 to 356) K
• Interfacial Properties, Densities, and Contact Angles of Task Specific Ionic Liquids
• Enthalpies of Solution of 1-Butyl-3-methylimidazolium Tetrafluoroborate in 15 Solvents at 298.15 K
• Compositions, Densities, and Refractive Indices for the Ternary Systems Ethylene Glycol + NaCl + H2O, Ethylene Glycol + KCl + H2O, Ethylene Glycol + RbCl + H2O, and Ethylene Glycol + CsCl + H2O at 298.15 K
• Activity Coefficients of Potassium Chloride in Ethylene Glycol-Water Mixtures Using Electromotive Force Measurements at (278.15, 288.15, 298.15, and 308.15) K
• Micellar Properties and Related Thermodynamic Parameters of the 14-6-14, 2Br- Gemini Surfactant in Water + Organic Solvent Mixed Media
• Densities and Viscosities of Propane-1,2,3-triol + Ethane-1,2-diol at T = (298.15 to 338.15) K
• Densities, Viscosities, and Volumetric Properties of Binary Mixtures of 1,2-Propanediol + 1-Heptanol or 1-Hexanol and 1,2-Ethanediol + 2-Butanol or 2-Propanol at T = (298.15, 303.15, and 308.15) K
• Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
• Densities, Speeds of Sound, and Isentropic Compressibilities for Binary Mixtures of 1,2-Ethanediol with 2-Ethyl-1-hexanol, 1-Heptanol, or Ethanol at the Temperature 298.15 K and Densities for Mixtures of 1,2-Ethanediol with 1-Nonanol at the Temperatures (293.15 and 298.15) K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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