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-Dihydroxyethane
• 1,2-Ethandiol
• 1,2-Ethylene glycol
• 146AR
• 2-Hydroxyethanol
• Aethylenglykol
• Aliphatic diol
• Athylenglykol
• Dihydroxyethane
• Dowtherm SR 1
• ETHTLENE DIHYDRATE
• ETHYLENE GLYCOL
• Ethane-1,2-diol
• Ethanediol
• Ethylene alcohol
• Ethylene dihydrate
• Ethylene gycol
• Fridex
• GLYCOL ALCOHOL
• Glycol
• 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

• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• σ_cond : Electrical conductivity (S/m).
• 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.
• P_c : Critical 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 : 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).
• V_c : Critical Volume (m³/kmol).
• v_spec : Specific Volume (m³/kg).
• 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
PAff	815.90	kJ/mol	NIST
Tig	685.93	K	KDB
BasG	773.60	kJ/mol	NIST
μ	2.20	debye	KDB
η	0.0169000	Pa×s	Viscosi...
LFL	3.20	% in Air	KDB
Tflash,cc	388.71	K	KDB
Tflash,oc	384.26	K	KDB
ΔfG°	-304.70	kJ/mol	KDB
Rg	2.4700		KDB
ΔfH°gas	[-394.40; -387.50]	kJ/mol
ΔfH°gas	-389.60	kJ/mol	KDB
ΔfH°gas	Outlier -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°	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. Sol...
logPoct/wat	-1.029		Crippen Calculated Property
McVol	50.780	ml/mol	McGowan Calculated Property
NFPA Fire	1		KDB
NFPA Health	1		KDB
Pc	[7700.00; 13100.00]	kPa
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
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	[469.15; 470.63]	K
Tboil	470.49	K	KDB
Tboil	470.63	K	(Vapour...
Tboil	470.32	K	Separat...
Tboil	470.22	K	Investi...
Tboil	470.38	K	Measure...
Tboil	Outlier 469.15	K	Cosolve...
Tboil	470.47	K	Vapor L...
Tc	[645.00; 790.00]	K
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
Tfus	[259.25; 262.00]	K
Tfus	260.00	K	KDB
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	262.00 ± 1.50	K	NIST
Tfus	261.70 ± 1.00	K	NIST
Ttriple	[256.60; 260.80]	K
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
Vc	0.185	m3/kmol	Joback Calculated Property
Zra	0.25		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[99.75; 121.88]	J/mol×K	[429.52; 589.28]
Cp,gas	99.75	J/mol×K	429.52	Joback Calculated Property
Cp,gas	103.79	J/mol×K	456.15	Joback Calculated Property
Cp,gas	107.68	J/mol×K	482.77	Joback Calculated Property
Cp,gas	111.44	J/mol×K	509.40	Joback Calculated Property
Cp,gas	115.05	J/mol×K	536.02	Joback Calculated Property
Cp,gas	118.53	J/mol×K	562.65	Joback Calculated Property
Cp,gas	121.88	J/mol×K	589.28	Joback Calculated Property
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 Ca...
Cp,liquid	145.60	J/mol×K	293.40	NIST
Cp,liquid	148.57	J/mol×K	294.65	Heat Ca...
Cp,liquid	149.05	J/mol×K	296.15	Heat Ca...
Cp,liquid	149.53	J/mol×K	297.65	Heat Ca...
Cp,liquid	147.30	J/mol×K	298.00	NIST
Cp,liquid	149.30	J/mol×K	298.00	NIST
Cp,liquid	148.87	J/mol×K	298.00	NIST
Cp,liquid	149.80	J/mol×K	298.00	NIST
Cp,liquid	150.33	J/mol×K	298.15	NIST
Cp,liquid	149.69	J/mol×K	298.15	Heat Ca...
Cp,liquid	149.60	J/mol×K	298.15	NIST
Cp,liquid	150.01	J/mol×K	299.15	Heat Ca...
Cp,liquid	150.48	J/mol×K	300.65	Heat Ca...
Cp,liquid	150.60	J/mol×K	301.20	NIST
Cp,liquid	150.96	J/mol×K	302.15	Heat Ca...
Cp,liquid	145.20	J/mol×K	303.00	NIST
Cp,liquid	151.44	J/mol×K	303.65	Heat Ca...
Cp,liquid	151.92	J/mol×K	305.15	Heat Ca...
Cp,liquid	152.40	J/mol×K	306.65	Heat Ca...
Cp,liquid	152.88	J/mol×K	308.15	Heat Ca...
Cp,liquid	153.36	J/mol×K	309.65	Heat Ca...
Cp,liquid	153.83	J/mol×K	311.15	Heat Ca...
Cp,liquid	154.31	J/mol×K	312.65	Heat Ca...
Cp,liquid	154.79	J/mol×K	314.15	Heat Ca...
Cp,liquid	155.27	J/mol×K	315.65	Heat Ca...
Cp,liquid	155.75	J/mol×K	317.15	Heat Ca...
Cp,liquid	156.23	J/mol×K	318.65	Heat Ca...
Cp,liquid	156.71	J/mol×K	320.15	Heat Ca...
Cp,liquid	157.19	J/mol×K	321.65	Heat Ca...
Cp,liquid	151.57	J/mol×K	323.15	Specifi...
Cp,liquid	157.67	J/mol×K	323.15	Heat Ca...
Cp,liquid	158.15	J/mol×K	324.65	Heat Ca...
Cp,liquid	158.63	J/mol×K	326.15	Heat Ca...
Cp,liquid	159.11	J/mol×K	327.65	Heat Ca...
Cp,liquid	159.60	J/mol×K	329.15	Heat Ca...
Cp,liquid	160.08	J/mol×K	330.65	Heat Ca...
Cp,liquid	160.56	J/mol×K	332.15	Heat Ca...
Cp,liquid	155.23	J/mol×K	333.15	Specifi...
Cp,liquid	161.04	J/mol×K	333.65	Heat Ca...
Cp,liquid	161.52	J/mol×K	335.15	Heat Ca...
Cp,liquid	162.00	J/mol×K	336.65	Heat Ca...
Cp,liquid	162.49	J/mol×K	338.15	Heat Ca...
Cp,liquid	162.97	J/mol×K	339.65	Heat Ca...
Cp,liquid	163.45	J/mol×K	341.15	Heat Ca...
Cp,liquid	163.93	J/mol×K	342.65	Heat Ca...
Cp,liquid	158.58	J/mol×K	343.15	Specifi...
Cp,liquid	164.42	J/mol×K	344.15	Heat Ca...
Cp,liquid	164.90	J/mol×K	345.65	Heat Ca...
Cp,liquid	165.38	J/mol×K	347.15	Heat Ca...
Cp,liquid	165.86	J/mol×K	348.65	Heat Ca...
Cp,liquid	166.35	J/mol×K	350.15	Heat Ca...
Cp,liquid	166.83	J/mol×K	351.65	Heat Ca...
Cp,liquid	161.31	J/mol×K	353.15	Specifi...
Cp,liquid	167.32	J/mol×K	353.15	Heat Ca...
Cp,liquid	164.85	J/mol×K	363.15	Specifi...
η	[0.0006520; 0.0214400]	Pa×s	[293.15; 464.40]
η	0.0214400	Pa×s	293.15	Viscosi...
η	0.0211000	Pa×s	293.15	Experim...
η	0.0191000	Pa×s	295.55	Density...
η	0.0174000	Pa×s	298.15	Densiti...
η	0.0154081	Pa×s	298.15	Densiti...
η	0.0167950	Pa×s	298.15	Density...
η	0.0148200	Pa×s	298.15	Densiti...
η	0.0174100	Pa×s	298.15	Viscosi...
η	0.0163876	Pa×s	298.15	Densiti...
η	0.0138000	Pa×s	303.15	Densiti...
η	0.0143300	Pa×s	303.15	Viscosi...
η	0.0127314	Pa×s	303.15	Densiti...
η	0.0133960	Pa×s	303.15	Density...
η	0.0115000	Pa×s	308.15	Densiti...
η	0.0104780	Pa×s	308.15	Densiti...
η	0.0113330	Pa×s	308.15	Density...
η	0.0111930	Pa×s	308.15	Densiti...
η	0.0111930	Pa×s	308.15	Excess ...
η	0.0107719	Pa×s	308.15	Densiti...
η	0.0106614	Pa×s	308.15	Densiti...
η	0.0099250	Pa×s	312.46	Experim...
η	0.0097400	Pa×s	313.05	Density...
η	0.0094200	Pa×s	313.15	Densiti...
η	0.0094440	Pa×s	313.15	Excess ...
η	0.0094440	Pa×s	313.15	Densiti...
η	0.0100100	Pa×s	313.15	Viscosi...
η	0.0081000	Pa×s	318.15	Densiti...
η	0.0077029	Pa×s	318.15	Densiti...
η	0.0079720	Pa×s	318.15	Excess ...
η	0.0079720	Pa×s	318.15	Densiti...
η	0.0067940	Pa×s	323.15	Excess ...
η	0.0067940	Pa×s	323.15	Densiti...
η	0.0069500	Pa×s	323.15	Densiti...
η	0.0071210	Pa×s	323.15	Viscosi...
η	0.0059600	Pa×s	328.15	Densiti...
η	0.0052400	Pa×s	333.10	Density...
η	0.0052200	Pa×s	333.15	Densiti...
η	0.0050650	Pa×s	333.15	Excess ...
η	0.0050650	Pa×s	333.15	Densiti...
η	0.0053300	Pa×s	333.15	Viscosi...
η	0.0049490	Pa×s	334.87	Experim...
η	0.0045300	Pa×s	338.15	Densiti...
η	0.0038790	Pa×s	343.15	Densiti...
η	0.0041030	Pa×s	343.15	Viscosi...
η	0.0038790	Pa×s	343.15	Excess ...
η	0.0035170	Pa×s	349.24	Experim...
η	0.0031300	Pa×s	353.05	Density...
η	0.0030580	Pa×s	353.15	Densiti...
η	0.0030580	Pa×s	353.15	Excess ...
η	0.0032420	Pa×s	353.15	Viscosi...
η	0.0023900	Pa×s	365.70	Experim...
η	0.0020600	Pa×s	372.15	Density...
η	0.0018150	Pa×s	380.82	Experim...
η	0.0014400	Pa×s	392.45	Density...
η	0.0014190	Pa×s	395.55	Experim...
η	0.0010700	Pa×s	412.25	Density...
η	0.0009600	Pa×s	421.70	Experim...
η	0.0008670	Pa×s	428.30	Density...
η	0.0006520	Pa×s	464.40	Experim...
σcond	[0.00; 1.68e-04]	S/m	[293.15; 343.15]
σcond	1.50e-05	S/m	293.15	Permitt...
σcond	2.90e-05	S/m	303.15	Permitt...
σcond	0.00	S/m	303.15	Micella...
σcond	4.60e-05	S/m	313.15	Permitt...
σcond	8.00e-05	S/m	323.15	Permitt...
σcond	1.21e-04	S/m	333.15	Permitt...
σcond	1.68e-04	S/m	343.15	Permitt...
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	11.62	kJ/mol	260.80	NIST
ΔfusH	11.60	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	Vaporiz...
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	[0.02; 101.32]	kPa	[303.20; 470.47]
Pvap	0.02	kPa	303.20	Thermod...
Pvap	0.02	kPa	306.20	Thermod...
Pvap	0.03	kPa	307.70	Vapor P...
Pvap	0.03	kPa	308.20	Thermod...
Pvap	0.03	kPa	310.20	Thermod...
Pvap	0.04	kPa	312.60	Vapor P...
Pvap	0.04	kPa	313.20	Thermod...
Pvap	0.05	kPa	316.20	Thermod...
Pvap	0.06	kPa	316.50	Vapor P...
Pvap	0.06	kPa	318.20	Thermod...
Pvap	0.06	kPa	318.80	Vapor P...
Pvap	0.07	kPa	320.20	Thermod...
Pvap	0.08	kPa	322.10	Vapor P...
Pvap	0.08	kPa	323.20	Thermod...
Pvap	0.11	kPa	326.10	Vapor P...
Pvap	0.11	kPa	326.20	Thermod...
Pvap	0.12	kPa	328.10	Thermod...
Pvap	0.12	kPa	328.20	Vapor P...
Pvap	0.15	kPa	331.20	Thermod...
Pvap	0.22	kPa	333.15	Isother...
Pvap	0.18	kPa	333.20	Thermod...
Pvap	0.20	kPa	334.50	Vapor P...
Pvap	0.20	kPa	335.20	Vapor P...
Pvap	0.22	kPa	336.20	Thermod...
Pvap	0.25	kPa	336.45	Determi...
Pvap	0.27	kPa	339.60	Thermod...
Pvap	0.28	kPa	340.20	Vapor P...
Pvap	0.36	kPa	343.60	Thermod...
Pvap	0.48	kPa	345.00	Determi...
Pvap	0.45	kPa	347.90	Vapor P...
Pvap	0.49	kPa	348.60	Thermod...
Pvap	0.77	kPa	353.15	Isother...
Pvap	0.68	kPa	353.60	Thermod...
Pvap	0.90	kPa	355.15	Determi...
Pvap	0.92	kPa	358.60	Thermod...
Pvap	0.90	kPa	359.20	Vapor P...
Pvap	1.24	kPa	363.60	Thermod...
Pvap	1.48	kPa	367.90	Vapor P...
Pvap	1.69	kPa	369.25	Determi...
Pvap	1.95	kPa	373.40	Vapor P...
Pvap	2.13	kPa	374.45	Determi...
Pvap	2.66	kPa	378.95	Determi...
Pvap	3.57	kPa	384.45	Determi...
Pvap	3.47	kPa	384.50	Vapor P...
Pvap	3.92	kPa	386.15	Isobari...
Pvap	4.40	kPa	388.10	Determi...
Pvap	4.51	kPa	389.12	Isobari...
Pvap	4.78	kPa	389.95	Isobari...
Pvap	4.89	kPa	390.75	Isobari...
Pvap	5.33	kPa	391.45	Determi...
Pvap	6.01	kPa	394.56	Determi...
Pvap	6.08	kPa	395.25	Isobari...
Pvap	7.14	kPa	397.25	Determi...
Pvap	7.87	kPa	400.78	Isobari...
Pvap	8.37	kPa	402.15	Isobari...
Pvap	9.20	kPa	404.05	Determi...
Pvap	9.85	kPa	405.85	Isobari...
Pvap	10.00	kPa	406.09	Isobari...
Pvap	10.02	kPa	406.25	Isobari...
Pvap	11.34	kPa	408.25	Determi...
Pvap	11.42	kPa	409.30	Isobari...
Pvap	12.41	kPa	411.15	Isobari...
Pvap	12.85	kPa	411.85	Isobari...
Pvap	13.33	kPa	412.81	Isobari...
Pvap	13.85	kPa	413.85	Isobari...
Pvap	15.37	kPa	416.45	Isobari...
Pvap	20.00	kPa	420.74	Isobari...
Pvap	20.00	kPa	422.75	Vapor L...
Pvap	20.00	kPa	422.78	Isobari...
Pvap	20.00	kPa	422.80	Vapor L...
Pvap	26.66	kPa	430.26	Isobari...
Pvap	30.00	kPa	432.29	Isobari...
Pvap	30.00	kPa	433.66	Vapor L...
Pvap	30.00	kPa	433.71	Vapor L...
Pvap	33.33	kPa	436.37	Isobari...
Pvap	40.00	kPa	440.15	Isobari...
Pvap	40.00	kPa	441.50	Isobari...
Pvap	40.00	kPa	441.66	Vapor L...
Pvap	40.00	kPa	441.70	Vapor L...
Pvap	46.66	kPa	445.96	Isobari...
Pvap	53.33	kPa	449.93	Isobari...
Pvap	60.00	kPa	453.52	Isobari...
Pvap	66.66	kPa	456.78	Isobari...
Pvap	73.33	kPa	459.79	Isobari...
Pvap	79.99	kPa	462.58	Isobari...
Pvap	86.66	kPa	465.18	Isobari...
Pvap	93.32	kPa	467.62	Isobari...
Pvap	101.32	kPa	469.15	Cosolve...
Pvap	98.66	kPa	469.48	Isobari...
Pvap	100.40	kPa	470.02	Isobari...
Pvap	101.30	kPa	470.22	Investi...
Pvap	101.30	kPa	470.47	Vapor L...
n0	[1.42460; 1.43280]		[293.15; 308.15]
n0	1.43280		293.15	Isobari...
n0	1.43180		293.15	Experim...
n0	1.43230		293.15	Densiti...
n0	1.43184		293.15	Liquid-...
n0	1.43060		298.15	Liquid ...
n0	1.43040		298.15	Density...
n0	1.43070		298.15	Density...
n0	1.43070		298.15	Thermod...
n0	1.43159		298.15	Phase E...
n0	1.43090		298.15	Densiti...
n0	1.42690		303.15	Density...
n0	1.42460		308.15	Density...
ρl	[1056.40; 1127.43]	kg/m3	[273.15; 373.15]
ρl	1127.05	kg/m3	273.15	Density...
ρl	1127.43	kg/m3	273.15	Solubil...
ρl	1125.17	kg/m3	276.15	Volumet...
ρl	1124.48	kg/m3	277.15	Volumet...
ρl	1123.80	kg/m3	278.15	Liquid ...
ρl	1123.77	kg/m3	278.15	Densiti...
ρl	1120.00	kg/m3	283.15	Density...
ρl	1120.50	kg/m3	283.15	Density...
ρl	1120.35	kg/m3	283.15	Solubil...
ρl	1119.29	kg/m3	283.15	Densiti...
ρl	1120.20	kg/m3	283.15	Thermop...
ρl	1120.32	kg/m3	283.15	Volumet...
ρl	1120.39	kg/m3	283.15	Excess ...
ρl	1116.83	kg/m3	288.15	Densiti...
ρl	1118.20	kg/m3	288.15	Thermop...
ρl	1116.85	kg/m3	288.15	Liquid ...
ρl	1116.84	kg/m3	288.15	Effect ...
ρl	1117.01	kg/m3	288.15	Volume-...
ρl	1116.86	kg/m3	288.15	Volumet...
ρl	1116.80	kg/m3	288.15	Thermop...
ρl	1114.00	kg/m3	293.00	KDB
ρl	1113.00	kg/m3	293.15	Thermod...
ρl	1113.30	kg/m3	293.15	Thermop...
ρl	1113.34	kg/m3	293.15	Excess ...
ρl	1113.84	kg/m3	293.15	Density...
ρl	1113.35	kg/m3	293.15	Effect ...
ρl	1113.70	kg/m3	293.15	Excess ...
ρl	1114.60	kg/m3	293.15	Thermop...
ρl	1112.37	kg/m3	293.15	Densiti...
ρl	1113.45	kg/m3	293.15	Density...
ρl	1113.25	kg/m3	293.15	Solubil...
ρl	1113.55	kg/m3	293.15	Densiti...
ρl	1113.23	kg/m3	293.15	Transpo...
ρl	1113.37	kg/m3	293.15	Volumet...
ρl	1113.72	kg/m3	293.15	Thermod...
ρl	1113.30	kg/m3	293.15	Density...
ρl	1121.00	kg/m3	293.15	Interfa...
ρl	1120.70	kg/m3	295.00	New dev...
ρl	1109.87	kg/m3	298.14	Volumet...
ρl	1109.00	kg/m3	298.15	Thermod...
ρl	1109.80	kg/m3	298.15	Excess ...
ρl	1109.86	kg/m3	298.15	Densiti...
ρl	1109.70	kg/m3	298.15	Investi...
ρl	1109.80	kg/m3	298.15	Thermod...
ρl	1109.70	kg/m3	298.15	Thermod...
ρl	1110.20	kg/m3	298.15	Solubil...
ρl	1109.80	kg/m3	298.15	Density...
ρl	1109.88	kg/m3	298.15	Liquid ...
ρl	1109.80	kg/m3	298.15	Thermop...
ρl	1109.90	kg/m3	298.15	Binary ...
ρl	1110.00	kg/m3	298.15	Activit...
ρl	1109.90	kg/m3	298.15	Revisio...
ρl	1109.71	kg/m3	298.15	Surface...
ρl	1109.83	kg/m3	298.15	Densiti...
ρl	1109.89	kg/m3	298.15	Viscosi...
ρl	1107.92	kg/m3	298.15	Isobari...
ρl	1109.79	kg/m3	298.15	Excess ...
ρl	1109.60	kg/m3	298.15	Solubil...
ρl	1109.90	kg/m3	298.15	Phase e...
ρl	1111.10	kg/m3	298.15	Thermop...
ρl	1110.20	kg/m3	298.15	Solubil...
ρl	1109.82	kg/m3	298.15	Isobari...
ρl	1109.90	kg/m3	298.15	Density...
ρl	1109.96	kg/m3	298.15	Density...
ρl	1109.90	kg/m3	298.15	Liquid-...
ρl	1109.85	kg/m3	298.15	Effect ...
ρl	1110.22	kg/m3	298.15	Thermod...
ρl	1110.08	kg/m3	298.15	Volume-...
ρl	1106.71	kg/m3	303.15	Thermod...
ρl	1106.30	kg/m3	303.15	Measure...
ρl	1107.60	kg/m3	303.15	Thermop...
ρl	1105.39	kg/m3	303.15	Densiti...
ρl	1106.33	kg/m3	303.15	Effect ...
ρl	1106.45	kg/m3	303.15	Density...
ρl	1106.60	kg/m3	303.15	Solubil...
ρl	1107.07	kg/m3	303.15	Density...
ρl	1106.30	kg/m3	303.15	Density...
ρl	1106.00	kg/m3	303.15	Thermod...
ρl	1106.38	kg/m3	303.15	Viscosi...
ρl	1106.00	kg/m3	303.15	Investi...
ρl	1106.30	kg/m3	303.15	Thermop...
ρl	1106.00	kg/m3	303.15	Thermod...
ρl	1103.20	kg/m3	303.15	Excess ...
ρl	1106.26	kg/m3	303.15	Solubil...
ρl	1106.82	kg/m3	303.15	Densiti...
ρl	1106.23	kg/m3	303.15	Excess ...
ρl	1106.36	kg/m3	303.15	Volumet...
ρl	1106.60	kg/m3	303.15	Solubil...
ρl	1102.84	kg/m3	308.15	Volumet...
ρl	1103.08	kg/m3	308.15	Volume-...
ρl	1102.93	kg/m3	308.15	Excess ...
ρl	1104.10	kg/m3	308.15	Thermop...
ρl	1102.93	kg/m3	308.15	Excess ...
ρl	1103.30	kg/m3	308.15	Liquid-...
ρl	1102.70	kg/m3	308.15	Thermod...
ρl	1102.90	kg/m3	308.15	Structu...
ρl	1102.80	kg/m3	308.15	Effect ...
ρl	1102.81	kg/m3	308.15	Densiti...
ρl	1102.93	kg/m3	308.15	Thermod...
ρl	1102.70	kg/m3	308.15	Measure...
ρl	1103.19	kg/m3	308.15	Thermod...
ρl	1102.90	kg/m3	308.15	Molecul...
ρl	1103.00	kg/m3	308.15	Solubil...
ρl	1102.80	kg/m3	308.15	Density...
ρl	1103.00	kg/m3	308.15	Solubil...
ρl	1102.84	kg/m3	308.15	Liquid ...
ρl	1102.70	kg/m3	308.15	Thermop...
ρl	1102.70	kg/m3	308.15	Investi...
ρl	1103.20	kg/m3	308.15	Densiti...
ρl	1102.93	kg/m3	308.15	Excess ...
ρl	1102.86	kg/m3	308.15	Viscosi...
ρl	1100.19	kg/m3	313.15	Density...
ρl	1099.31	kg/m3	313.15	Viscosi...
ρl	1098.34	kg/m3	313.15	Densiti...
ρl	1099.07	kg/m3	313.15	Excess ...
ρl	1099.26	kg/m3	313.15	Effect ...
ρl	1099.80	kg/m3	313.15	Densiti...
ρl	1099.30	kg/m3	313.15	Volumet...
ρl	1093.60	kg/m3	313.15	Excess ...
ρl	1099.30	kg/m3	313.15	Solubil...
ρl	1099.20	kg/m3	313.15	Thermop...
ρl	1099.20	kg/m3	313.15	Measure...
ρl	1098.90	kg/m3	313.15	Solubil...
ρl	1100.50	kg/m3	313.15	Thermop...
ρl	1099.38	kg/m3	313.15	Density...
ρl	1099.30	kg/m3	313.15	Solubil...
ρl	1099.20	kg/m3	313.15	Density...
ρl	1099.10	kg/m3	313.15	Density...
ρl	1099.20	kg/m3	313.15	Solubil...
ρl	1095.80	kg/m3	318.15	Solubil...
ρl	1096.23	kg/m3	318.15	Densiti...
ρl	1095.75	kg/m3	318.15	Viscosi...
ρl	1095.60	kg/m3	318.15	Measure...
ρl	1095.70	kg/m3	318.15	Density...
ρl	1097.00	kg/m3	318.15	Thermop...
ρl	1095.80	kg/m3	318.15	Solubil...
ρl	1096.00	kg/m3	318.15	Volume-...
ρl	1095.69	kg/m3	318.15	Effect ...
ρl	1091.21	kg/m3	323.15	Densiti...
ρl	1091.70	kg/m3	323.15	Solubil...
ρl	1091.60	kg/m3	323.15	Density...
ρl	1092.10	kg/m3	323.15	Thermop...
ρl	1092.12	kg/m3	323.15	Densiti...
ρl	1092.16	kg/m3	323.15	Viscosi...
ρl	1084.70	kg/m3	323.15	Excess ...
ρl	1092.14	kg/m3	323.15	Liquid ...
ρl	1093.40	kg/m3	323.15	Thermop...
ρl	1092.10	kg/m3	323.15	Measure...
ρl	1092.10	kg/m3	323.15	Density...
ρl	1092.59	kg/m3	323.15	Densiti...
ρl	1092.07	kg/m3	323.15	Solubil...
ρl	1093.20	kg/m3	323.15	Density...
ρl	1092.24	kg/m3	323.15	Density...
ρl	1089.80	kg/m3	328.15	Thermop...
ρl	1088.66	kg/m3	328.15	Densiti...
ρl	1088.40	kg/m3	328.15	Measure...
ρl	1088.56	kg/m3	328.15	Viscosi...
ρl	1088.50	kg/m3	328.15	Density...
ρl	1088.83	kg/m3	328.15	Volume-...
ρl	1084.20	kg/m3	333.15	Solubil...
ρl	1086.20	kg/m3	333.15	Thermop...
ρl	1076.40	kg/m3	333.15	Excess ...
ρl	1084.80	kg/m3	333.15	Measure...
ρl	1086.11	kg/m3	333.15	Density...
ρl	1085.00	kg/m3	333.15	Density...
ρl	1083.99	kg/m3	333.15	Densiti...
ρl	1084.80	kg/m3	333.15	Thermop...
ρl	1084.90	kg/m3	333.15	Density...
ρl	1085.00	kg/m3	333.15	Density...
ρl	1084.84	kg/m3	333.15	Solubil...
ρl	1081.20	kg/m3	338.15	Density...
ρl	1082.60	kg/m3	338.15	Thermop...
ρl	1081.20	kg/m3	338.15	Measure...
ρl	1067.50	kg/m3	343.15	Excess ...
ρl	1077.50	kg/m3	343.15	Density...
ρl	1077.60	kg/m3	343.15	Density...
ρl	1076.65	kg/m3	343.15	Densiti...
ρl	1078.90	kg/m3	343.15	Thermop...
ρl	1077.65	kg/m3	343.15	Density...
ρl	1077.50	kg/m3	343.15	Measure...
ρl	1077.50	kg/m3	343.15	Thermop...
ρl	1078.10	kg/m3	343.15	Solubil...
ρl	1078.91	kg/m3	343.15	Density...
ρl	1075.20	kg/m3	348.15	Thermop...
ρl	1073.70	kg/m3	348.15	Measure...
ρl	1070.10	kg/m3	353.15	Density...
ρl	1071.50	kg/m3	353.15	Thermop...
ρl	1071.60	kg/m3	353.15	Density...
ρl	1070.17	kg/m3	353.15	Density...
ρl	1070.00	kg/m3	353.15	Measure...
ρl	1060.00	kg/m3	353.15	Excess ...
ρl	1067.80	kg/m3	358.15	Thermop...
ρl	1064.18	kg/m3	363.15	Density...
ρl	1064.00	kg/m3	363.15	Thermop...
ρl	1060.20	kg/m3	368.15	Thermop...
ρl	1056.40	kg/m3	373.15	Thermop...
ΔfusS	[38.21; 44.57]	J/mol×K	[260.60; 260.80]
ΔfusS	38.21	J/mol×K	260.60	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	Volumet...
csound,fluid	1654.38	m/s	298.15	Densiti...
γ	[0.05; 0.05]	N/m	[283.15; 323.15]
γ	0.05	N/m	283.15	Surface...
γ	0.05	N/m	293.15	Equilib...
γ	0.05	N/m	293.15	Surface...
γ	0.05	N/m	293.15	Surface...
γ	0.05	N/m	293.15	Surface...
γ	0.05	N/m	293.20	KDB
γ	0.05	N/m	298.15	Surface...
γ	0.05	N/m	298.15	Surface...
γ	0.05	N/m	298.15	Concent...
γ	0.05	N/m	298.15	Surface...
γ	0.05	N/m	298.15	Surface...
γ	0.05	N/m	298.15	Equilib...
γ	0.05	N/m	303.15	Surface...
γ	0.05	N/m	303.15	Equilib...
γ	0.05	N/m	303.15	Surface...
γ	0.05	N/m	303.15	Surface...
γ	0.05	N/m	308.15	Equilib...
γ	0.05	N/m	308.15	Surface...
γ	0.05	N/m	308.15	Gas-Liq...
γ	0.05	N/m	308.15	Surface...
γ	0.05	N/m	308.15	Surface...
γ	0.05	N/m	308.15	Surface...
γ	0.05	N/m	313.15	Surface...
γ	0.05	N/m	313.15	Surface...
γ	0.05	N/m	313.15	Surface...
γ	0.05	N/m	313.15	Gas-Liq...
γ	0.05	N/m	313.15	Equilib...
γ	0.05	N/m	318.15	Equilib...
γ	0.05	N/m	318.15	Surface...
γ	0.05	N/m	318.15	Surface...
γ	0.05	N/m	318.15	Gas-Liq...
γ	0.05	N/m	318.15	Surface...
γ	0.05	N/m	323.15	Surface...
γ	0.05	N/m	323.15	Surface...
γ	0.05	N/m	323.15	Equilib...
γ	0.05	N/m	323.15	Surface...
γ	0.05	N/m	323.15	Gas-Liq...
λ	[0.24; 0.27]	W/m×K	[283.15; 343.15]
λ	0.24	W/m×K	283.15	Thermal...
λ	0.24	W/m×K	283.15	Thermop...
λ	0.25	W/m×K	293.15	Measure...
λ	0.25	W/m×K	298.15	An expe...
λ	0.24	W/m×K	298.15	Experim...
λ	0.25	W/m×K	298.20	Applica...
λ	0.25	W/m×K	303.15	An expe...
λ	0.25	W/m×K	303.15	Thermop...
λ	0.25	W/m×K	303.15	Thermal...
λ	0.25	W/m×K	303.15	Thermal...
λ	0.25	W/m×K	308.10	Applica...
λ	0.26	W/m×K	308.15	An expe...
λ	0.26	W/m×K	313.15	An expe...
λ	0.26	W/m×K	313.15	Thermal...
λ	0.26	W/m×K	318.15	An expe...
λ	0.25	W/m×K	318.30	Applica...
λ	0.26	W/m×K	323.15	An expe...
λ	0.26	W/m×K	323.15	Thermal...
λ	0.26	W/m×K	323.15	Thermal...
λ	0.25	W/m×K	323.15	Thermop...
λ	0.26	W/m×K	328.30	Applica...
λ	0.26	W/m×K	338.30	Applica...
λ	0.26	W/m×K	343.15	Thermop...
λ	0.27	W/m×K	343.15	Thermal...
αdiff	[9.42e-08; 9.84e-08]	m2/s	[298.15; 338.15]
αdiff	9.84e-08	m2/s	298.15	Tempera...
αdiff	9.73e-08	m2/s	308.15	Tempera...
αdiff	9.68e-08	m2/s	318.15	Tempera...
αdiff	9.49e-08	m2/s	328.15	Tempera...
αdiff	9.42e-08	m2/s	338.15	Tempera...
vspec	[8.87e-04; 9.10e-04]	m3/kg	[273.15; 313.15]
vspec	8.87e-04	m3/kg	273.15	Volumet...
vspec	8.88e-04	m3/kg	274.14	Volumet...
vspec	8.88e-04	m3/kg	275.14	Volumet...
vspec	8.89e-04	m3/kg	276.15	Volumet...
vspec	8.89e-04	m3/kg	277.15	Volumet...
vspec	8.90e-04	m3/kg	278.15	Volumet...
vspec	8.90e-04	m3/kg	279.15	Volumet...
vspec	8.91e-04	m3/kg	280.15	Volumet...
vspec	8.91e-04	m3/kg	281.15	Volumet...
vspec	8.92e-04	m3/kg	282.15	Volumet...
vspec	8.93e-04	m3/kg	283.15	Volumet...
vspec	8.93e-04	m3/kg	284.15	Volumet...
vspec	8.94e-04	m3/kg	285.15	Volumet...
vspec	8.94e-04	m3/kg	286.15	Volumet...
vspec	8.95e-04	m3/kg	287.15	Volumet...
vspec	8.95e-04	m3/kg	288.15	Volumet...
vspec	8.95e-04	m3/kg	288.16	Volumet...
vspec	8.95e-04	m3/kg	288.21	Volumet...
vspec	8.95e-04	m3/kg	288.22	Volumet...
vspec	8.96e-04	m3/kg	289.15	Volumet...
vspec	8.96e-04	m3/kg	290.15	Volumet...
vspec	8.97e-04	m3/kg	291.15	Volumet...
vspec	8.98e-04	m3/kg	292.15	Volumet...
vspec	8.98e-04	m3/kg	293.15	Volumet...
vspec	8.99e-04	m3/kg	294.15	Volumet...
vspec	8.99e-04	m3/kg	295.15	Volumet...
vspec	9.00e-04	m3/kg	296.15	Volumet...
vspec	9.00e-04	m3/kg	297.15	Volumet...
vspec	9.01e-04	m3/kg	298.16	Volumet...
vspec	9.02e-04	m3/kg	299.16	Volumet...
vspec	9.02e-04	m3/kg	300.16	Volumet...
vspec	9.03e-04	m3/kg	301.16	Volumet...
vspec	9.03e-04	m3/kg	302.16	Volumet...
vspec	9.04e-04	m3/kg	303.15	Volumet...
vspec	9.04e-04	m3/kg	304.16	Volumet...
vspec	9.05e-04	m3/kg	305.15	Volumet...
vspec	9.06e-04	m3/kg	306.15	Volumet...
vspec	9.06e-04	m3/kg	307.15	Volumet...
vspec	9.07e-04	m3/kg	308.15	Volumet...
vspec	9.07e-04	m3/kg	309.15	Volumet...
vspec	9.08e-04	m3/kg	310.15	Volumet...
vspec	9.08e-04	m3/kg	311.15	Volumet...
vspec	9.09e-04	m3/kg	312.15	Volumet...
vspec	9.10e-04	m3/kg	313.15	Volumet...

Datasets

1. Viscosity, Pa*s (2)
2. Mass density, kg/m3 (4)
3. Speed of sound, m/s (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

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

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 5004.89]	kPa	[370.66; 623.15]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
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	[1.98e-04; 7495.90]	kPa	[260.15; 645.00]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			1.91425e+02
Coefficient B			-1.47686e+04
Coefficient C			-2.59977e+01
Coefficient D			2.06233e-05
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

Similar Compounds

Find more compounds similar to 1,2-Ethanediol.

Mixtures

• 1,2-Ethanediol + Pyridine, 2,4,6-trimethyl-
• 1,2-Ethanediol + Ethyl Acetate
• 1,2-Ethanediol + Acetic acid, phenyl ester
• Toluene + 1,2-Ethanediol
• 1,2-Ethanediol + Anisole
• 1,2-Ethanediol + Benzene, chloro-
• 1,2-Ethanediol + Acetophenone
• 1,2-Ethanediol + Acetic acid, hydroxy-, methyl ester
• 1,2-Ethanediol, diacetate + 1,2-Ethanediol
• 1,2-Ethanediol + 1,2-Ethanediol, monoacetate
• 1,2-Ethanediol + Acetic acid
• 1-Propanol + 1,2-Ethanediol + Di-n-propyl ether
• 1,2-Ethanediol + Ethanol, 2,2'-oxybis-
• 1,2-Ethanediol + Triethylene glycol
• 1,2-Ethanediol + Triethylene glycol + Ethanol, 2,2'-oxybis-
• 1,2-Ethanediol + Ethanol + Water
• 1,2-Ethanediol + Water
• 1,2-Ethanediol + Dicyandiamide
• Naphthalene, 2-methyl- + 1,2-Ethanediol + Indole
• 1,2-Ethanediol + Tetra-N-butylammonium bromide

Find more mixtures with 1,2-Ethanediol.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• 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
• 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
• Mutual diffusion coefficients of aqueous solutions of some glycols
• 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
• 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
• 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
• 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
• 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
• 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
• 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
• 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
• Viscosity, thermal and electrical conductivity of silicon dioxide - ethylene glycol transparent nanofluids: An experimental studies
• 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
• 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
• 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
• 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
• 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
• 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
• 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
• 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
• The Yaws Handbook of Vapor Pressure

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