Chemical Properties of Glycerin (CAS 56-81-5)

InChI

InChI=1S/C3H8O3/c4-1-3(6)2-5/h3-6H,1-2H2

InChI Key

PEDCQBHIVMGVHV-UHFFFAOYSA-N

Formula

C3H8O3

SMILES

OCC(O)CO

Molecular Weight¹

92.09

CAS

56-81-5

Other Names

• 1,2,3-Trihydroxypropane
• 1,2,3-propanetriol
• 90 Technical glycerin
• 90 Technical glycerine
• Bulbold
• Clyzerin, wasserfrei
• Cristal
• Dagralax
• Emery 912
• Emery 916
• Glycerin, anhydrous
• Glycerin, synthetic
• Glyceritol
• Glycyl alcohol
• Glyrol
• Glysanin
• Grocolene
• IFP
• Incorporation factor
• MOON
• NSC 9230
• Ophthalgan
• Optim
• Osmoglyn
• Pricerine 9091
• Propanetriol
• Star
• Synthetic glycerin
• Synthetic glycerine
• Trihydroxypropane
• Vitrosupos
• glycerine
• glycerol
• propane-1,2,3-triol

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• 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).
• C_p,solid : Solid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• ε_r : Dielectric Constant (Relative permittivity).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_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).
• 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_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• γ : Surface Tension (N/m).
• S°_{solid,1 bar} : Solid phase molar entropy at standard conditions (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_boil : Boiling point at given pressure (K).
• T_boilr : Boiling point at reduced pressure (K).
• T_c : Critical Temperature (K).
• λ : Gas thermal conductivity (W/m×K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

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

Physical Properties

Property	Value	Unit	Source
ω	1.5441		ChemSep v8.3 pure component data
PAff	[835.80; 874.80]	kJ/mol
PAff	874.80	kJ/mol	NIST
PAff	840.70	kJ/mol	NIST
PAff	835.80	kJ/mol	NIST
PAff	848.60 ± 1.20	kJ/mol	NIST
BasG	[805.50; 820.00]	kJ/mol
BasG	820.00	kJ/mol	NIST
BasG	810.20	kJ/mol	NIST
BasG	805.50	kJ/mol	NIST
BasG	818.90 ± 0.50	kJ/mol	NIST
ΔcH°liquid	[-1665.10; -1654.10]	kJ/mol
ΔcH°liquid	-1654.30 ± 0.40	kJ/mol	NIST
ΔcH°liquid	-1654.10	kJ/mol	NIST
ΔcH°liquid	-1655.30 ± 1.00	kJ/mol	NIST
ΔcH°liquid	-1665.10	kJ/mol	NIST
μ	[3.00; 4.20]	debye
μ	4.20	debye	ChemSep v8.3 pure component data
μ	3.00	debye	KDB
ΔfG°	-447.10	kJ/mol	ChemSep v8.3 pure component data
ΔfH°gas	[-585.30; -576.90]	kJ/mol
ΔfH°gas	-582.80	kJ/mol	ChemSep v8.3 pure component data
ΔfH°gas	-585.30	kJ/mol	KDB
ΔfH°gas	-577.90 ± 1.10	kJ/mol	NIST
ΔfH°gas	-576.90	kJ/mol	NIST
ΔfH°liquid	[-669.60; -668.60]	kJ/mol
ΔfH°liquid	-669.60 ± 0.60	kJ/mol	NIST
ΔfH°liquid	-668.60 ± 0.42	kJ/mol	NIST
ΔfusH°	12.27	kJ/mol	Joback Calculated Property
ΔvapH°	[85.80; 91.70]	kJ/mol
ΔvapH°	91.70 ± 0.90	kJ/mol	NIST
ΔvapH°	91.70	kJ/mol	NIST
ΔvapH°	91.70 ± 0.90	kJ/mol	NIST
ΔvapH°	85.80	kJ/mol	NIST
log10WS	[1.12; 1.12]
log10WS	1.12		Aq. Solubility Prediction
log10WS	1.12		Estimated Solubility
logPoct/wat	-1.668		Crippen Calculated Property
McVol	70.740	ml/mol	McGowan Calculated Property
NFPA Fire	1		KDB
NFPA Health	1		KDB
Pc	[6660.00; 7500.00]	kPa
Pc	6660.00	kPa	ChemSep v8.3 pure component data
Pc	6680.00	kPa	KDB
Pc	7500.00 ± 200.00	kPa	NIST
Ptriple	9.52e-06	kPa	ChemSep v8.3 pure component data
I	[2300.00; 2322.00]
I	2322.00		NIST
I	2314.00		NIST
I	2300.00		NIST
S°solid,1 bar	[37.87; 42.34]	J/mol×K
S°solid,1 bar	37.87	J/mol×K	NIST
S°solid,1 bar	42.34	J/mol×K	NIST
Tboil	[512.25; 563.70]	K
Tboil	563.15	K	ChemSep v8.3 pure component data
Tboil	563.00	K	KDB
Tboil	563.25	K	NIST
Tboil	563.15 ± 3.00	K	NIST
Tboil	563.70 ± 0.70	K	NIST
Tboil	Outlier 512.25 ± 0.40	K	NIST
Tboil	562.00 ± 3.00	K	NIST
Tboil	563.15 ± 0.40	K	NIST
Tboil	563.00 ± 4.00	K	NIST
Tc	[726.00; 850.00]	K
Tc	850.00	K	ChemSep v8.3 pure component data
Tc	726.00	K	KDB
Tc	850.00 ± 4.00	K	NIST
Tfus	[286.00; 292.00]	K
Tfus	291.15	K	ChemSep v8.3 pure component data
Tfus	291.00	K	KDB
Tfus	291.05	K	NIST
Tfus	291.05 ± 0.50	K	NIST
Tfus	291.05 ± 0.50	K	NIST
Tfus	292.00 ± 2.00	K	NIST
Tfus	291.33 ± 0.15	K	NIST
Tfus	291.80 ± 1.00	K	NIST
Tfus	291.20 ± 0.50	K	NIST
Tfus	292.00 ± 3.00	K	NIST
Tfus	Outlier 286.00 ± 3.00	K	NIST
Tfus	Outlier 286.00 ± 4.00	K	NIST
Ttriple	[291.00; 291.80]	K
Ttriple	291.33	K	ChemSep v8.3 pure component data
Ttriple	291.80 ± 0.20	K	NIST
Ttriple	291.00 ± 0.20	K	NIST
UQi	3.06		ChemSep v8.3 pure component data
URi	3.39		ChemSep v8.3 pure component data
Vc	[0.255; 0.264]	m3/kmol
Vc	0.264	m3/kmol	ChemSep v8.3 pure component data
Vc	0.255	m3/kmol	KDB
Zc	[0.2800000; 0.2821910]
Zc	0.2800000		ChemSep v8.3 pure component data
Zc	0.2821910		KDB

Cheméo can also estimate Ionization energy for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[207.90; 229.30]	J/mol×K	[289.70; 313.15]
Cp,liquid	225.90	J/mol×K	289.70	NIST
Cp,liquid	219.20	J/mol×K	293.15	NIST
Cp,liquid	221.18	J/mol×K	293.15	NIST
Cp,liquid	218.50	J/mol×K	298.00	NIST
Cp,liquid	213.80	J/mol×K	298.00	NIST
Cp,liquid	207.90	J/mol×K	298.10	NIST
Cp,liquid	218.90	J/mol×K	298.15	NIST
Cp,liquid	221.90	J/mol×K	298.15	NIST
Cp,liquid	223.40	J/mol×K	299.40	NIST
Cp,liquid	221.70	J/mol×K	301.20	NIST
Cp,liquid	229.30	J/mol×K	313.15	NIST
Cp,solid	[49.79; 150.00]	J/mol×K	[85.12; 281.50]
Cp,solid	50.21	J/mol×K	85.12	NIST
Cp,solid	49.79	J/mol×K	86.92	NIST
Cp,solid	150.00	J/mol×K	281.50	NIST
η	[0.0083200; 2.1800000]	Pa×s	[288.10; 394.08]
η	2.1800000	Pa×s	288.10	Studies on viscosity and conductivity of 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures from 288.1 K to 328.1 K
η	1.4700000	Pa×s	292.89	The viscosity of glycerol
η	1.2520000	Pa×s	296.50	Viscosities and Carbon Dioxide Solubilities of Guanidine Carbonate and Malic Acid-Based Eutectic Solvents
η	0.9706000	Pa×s	298.10	The viscosity of glycerol
η	0.9338000	Pa×s	298.10	Studies on viscosity and conductivity of 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures from 288.1 K to 328.1 K
η	0.9438000	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	0.6458000	Pa×s	302.59	The viscosity of glycerol
η	0.6734000	Pa×s	302.80	Viscosities and Carbon Dioxide Solubilities of Guanidine Carbonate and Malic Acid-Based Eutectic Solvents
η	0.6289000	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	0.4203000	Pa×s	308.10	Studies on viscosity and conductivity of 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures from 288.1 K to 328.1 K
η	0.4319000	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	0.3053000	Pa×s	312.81	The viscosity of glycerol
η	0.2959000	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	0.2606000	Pa×s	315.80	Viscosities and Carbon Dioxide Solubilities of Guanidine Carbonate and Malic Acid-Based Eutectic Solvents
η	0.1956000	Pa×s	318.10	Studies on viscosity and conductivity of 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures from 288.1 K to 328.1 K
η	0.1858000	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	0.1512000	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	0.1489000	Pa×s	323.20	Viscosities and Carbon Dioxide Solubilities of Guanidine Carbonate and Malic Acid-Based Eutectic Solvents
η	0.1474000	Pa×s	323.88	The viscosity of glycerol
η	0.1043000	Pa×s	328.10	Studies on viscosity and conductivity of 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures from 288.1 K to 328.1 K
η	0.1084000	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	0.0975000	Pa×s	332.70	Viscosities and Carbon Dioxide Solubilities of Guanidine Carbonate and Malic Acid-Based Eutectic Solvents
η	0.0848000	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	0.0847100	Pa×s	333.15	The viscosity of glycerol
η	0.0622000	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	0.0519000	Pa×s	343.20	Viscosities and Carbon Dioxide Solubilities of Guanidine Carbonate and Malic Acid-Based Eutectic Solvents
η	0.0498300	Pa×s	343.80	The viscosity of glycerol
η	0.0428000	Pa×s	348.20	Viscosities and Carbon Dioxide Solubilities of Guanidine Carbonate and Malic Acid-Based Eutectic Solvents
η	0.0318000	Pa×s	353.67	The viscosity of glycerol
η	0.0349000	Pa×s	354.20	Viscosities and Carbon Dioxide Solubilities of Guanidine Carbonate and Malic Acid-Based Eutectic Solvents
η	0.0210500	Pa×s	364.12	The viscosity of glycerol
η	0.0147400	Pa×s	374.38	The viscosity of glycerol
η	0.0110000	Pa×s	383.29	The viscosity of glycerol
η	0.0083200	Pa×s	394.08	The viscosity of glycerol
εr	[41.17; 41.17]		[303.15; 303.15]
εr	41.17		303.15	Dielectric properties and hydrogen bonding interaction behaviour in binary mixtures of glycerol with amides and amines
εr	41.17		303.15	Dielectric constant and molecular association in binary mixtures of N,N-dimethylethanolamine with alcohols and amides
ΔfusH	[18.28; 18.48]	kJ/mol	[291.00; 293.00]
ΔfusH	18.29	kJ/mol	291.00	NIST
ΔfusH	18.28	kJ/mol	291.00	NIST
ΔfusH	18.48	kJ/mol	291.75	NIST
ΔfusH	18.30	kJ/mol	292.00	NIST
ΔfusH	18.28	kJ/mol	293.00	NIST
ΔfusH	18.28	kJ/mol	293.00	NIST
ΔvapH	[64.80; 86.80]	kJ/mol	[300.50; 516.00]
ΔvapH	71.50	kJ/mol	300.50	NIST
ΔvapH	86.80	kJ/mol	316.00	NIST
ΔvapH	85.80	kJ/mol	318.00	NIST
ΔvapH	67.50	kJ/mol	343.00	NIST
ΔvapH	66.80	kJ/mol	353.00	NIST
ΔvapH	66.20	kJ/mol	363.00	NIST
ΔvapH	65.50	kJ/mol	373.00	NIST
ΔvapH	64.80	kJ/mol	383.00	NIST
ΔvapH	86.00	kJ/mol	504.50	NIST
ΔvapH	78.50	kJ/mol	516.00	NIST
Pvap	[4.15e-05; 95.99]	kPa	[303.59; 560.95]
Pvap	4.15e-05	kPa	303.59	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	4.19e-05	kPa	303.61	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	4.68e-05	kPa	304.56	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	5.56e-05	kPa	306.03	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	7.28e-05	kPa	308.43	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	9.63e-05	kPa	310.89	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	1.25e-04	kPa	313.29	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	1.63e-04	kPa	315.71	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	2.11e-04	kPa	318.12	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	2.70e-04	kPa	320.57	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	3.47e-04	kPa	322.95	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	4.43e-04	kPa	325.42	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	5.64e-04	kPa	327.82	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	7.17e-04	kPa	330.30	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	9.04e-04	kPa	332.72	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	1.13e-03	kPa	335.14	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	1.50e-03	kPa	338.25	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	1.87e-03	kPa	340.68	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	2.32e-03	kPa	343.08	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	2.88e-03	kPa	345.51	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	3.53e-03	kPa	347.91	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	4.36e-03	kPa	350.34	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	5.83e-03	kPa	351.80	Vapor-Liquid Equilibria of Glycerol, 1,3-Propanediol, Glycerol + Water, and Glycerol + 1,3-Propanediol
Pvap	5.26e-03	kPa	352.57	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	5.27e-03	kPa	352.58	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	5.28e-03	kPa	352.60	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	5.32e-03	kPa	352.73	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	6.39e-03	kPa	354.98	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	6.41e-03	kPa	354.99	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	6.49e-03	kPa	355.18	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	7.77e-03	kPa	357.39	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	7.82e-03	kPa	357.42	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	7.86e-03	kPa	357.57	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	9.38e-03	kPa	359.80	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	9.39e-03	kPa	359.82	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	9.52e-03	kPa	360.01	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.01	kPa	362.02	Vapor-Liquid Equilibria of Glycerol, 1,3-Propanediol, Glycerol + Water, and Glycerol + 1,3-Propanediol
Pvap	0.01	kPa	362.42	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.01	kPa	362.63	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.01	kPa	362.66	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.01	kPa	364.82	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.01	kPa	365.07	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.01	kPa	365.08	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.02	kPa	367.45	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.02	kPa	367.48	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.02	kPa	369.89	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.02	kPa	369.91	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.03	kPa	372.06	Vapor-Liquid Equilibria of Glycerol, 1,3-Propanediol, Glycerol + Water, and Glycerol + 1,3-Propanediol
Pvap	0.02	kPa	372.27	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.02	kPa	372.29	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.03	kPa	374.70	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.03	kPa	374.73	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.03	kPa	377.08	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.03	kPa	377.11	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.04	kPa	377.77	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.04	kPa	380.17	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.04	kPa	380.19	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.05	kPa	382.08	Vapor-Liquid Equilibria of Glycerol, 1,3-Propanediol, Glycerol + Water, and Glycerol + 1,3-Propanediol
Pvap	0.05	kPa	382.55	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.05	kPa	382.59	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.05	kPa	382.59	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.06	kPa	384.99	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.06	kPa	385.01	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.07	kPa	387.37	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.07	kPa	387.39	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.08	kPa	389.80	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.08	kPa	389.83	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.09	kPa	392.18	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.10	kPa	392.18	Vapor-Liquid Equilibria of Glycerol, 1,3-Propanediol, Glycerol + Water, and Glycerol + 1,3-Propanediol
Pvap	0.09	kPa	392.20	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.11	kPa	394.61	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.11	kPa	394.64	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.13	kPa	397.00	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.13	kPa	397.02	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.15	kPa	399.42	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.15	kPa	399.45	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.17	kPa	401.81	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.17	kPa	401.81	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.17	kPa	401.83	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.18	kPa	402.16	Vapor-Liquid Equilibria of Glycerol, 1,3-Propanediol, Glycerol + Water, and Glycerol + 1,3-Propanediol
Pvap	0.20	kPa	404.23	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.20	kPa	404.26	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.22	kPa	406.62	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.22	kPa	406.62	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.23	kPa	406.64	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.27	kPa	409.68	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.27	kPa	409.69	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.31	kPa	412.08	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.31	kPa	412.11	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.32	kPa	412.24	Vapor-Liquid Equilibria of Glycerol, 1,3-Propanediol, Glycerol + Water, and Glycerol + 1,3-Propanediol
Pvap	0.35	kPa	414.48	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.35	kPa	414.49	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.40	kPa	416.89	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.40	kPa	416.92	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.46	kPa	419.30	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.46	kPa	419.30	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.52	kPa	421.70	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.52	kPa	421.73	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.53	kPa	422.28	Vapor-Liquid Equilibria of Glycerol, 1,3-Propanediol, Glycerol + Water, and Glycerol + 1,3-Propanediol
Pvap	0.59	kPa	424.10	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.59	kPa	424.11	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.67	kPa	426.50	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.67	kPa	426.53	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.76	kPa	428.91	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.76	kPa	428.91	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.86	kPa	431.31	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.86	kPa	431.34	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.98	kPa	432.45	Vapor-Liquid Equilibria of Glycerol, 1,3-Propanediol, Glycerol + Water, and Glycerol + 1,3-Propanediol
Pvap	0.97	kPa	433.72	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	0.97	kPa	433.73	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	1.09	kPa	436.11	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	1.09	kPa	436.13	Thermodynamic properties of glycerol: experimental and theoretical study
Pvap	2.75	kPa	452.64	Vapor-Liquid Equilibria of Glycerol, 1,3-Propanediol, Glycerol + Water, and Glycerol + 1,3-Propanediol
Pvap	4.10	kPa	462.86	Vapor-Liquid Equilibria of Glycerol, 1,3-Propanediol, Glycerol + Water, and Glycerol + 1,3-Propanediol
Pvap	3.85	kPa	463.15	Vapor Pressures and Evaporation Studies of Sugars and Sugar Alcohols
Pvap	6.70	kPa	477.25	Thermophysical properties of biodiesel and related systems. Part I. Vapour liquid equilibrium at low pressures of binary and ternary systems involving methanol, ethanol, glycerol, water and NaCl
Pvap	8.64	kPa	483.15	Vapor Pressures and Evaporation Studies of Sugars and Sugar Alcohols
Pvap	13.30	kPa	493.35	Thermophysical properties of biodiesel and related systems. Part I. Vapour liquid equilibrium at low pressures of binary and ternary systems involving methanol, ethanol, glycerol, water and NaCl
Pvap	17.90	kPa	503.15	Vapor Pressures and Evaporation Studies of Sugars and Sugar Alcohols
Pvap	20.00	kPa	505.55	Thermophysical properties of biodiesel and related systems. Part I. Vapour liquid equilibrium at low pressures of binary and ternary systems involving methanol, ethanol, glycerol, water and NaCl
Pvap	26.70	kPa	513.95	Thermophysical properties of biodiesel and related systems. Part I. Vapour liquid equilibrium at low pressures of binary and ternary systems involving methanol, ethanol, glycerol, water and NaCl
Pvap	33.30	kPa	520.65	Thermophysical properties of biodiesel and related systems. Part I. Vapour liquid equilibrium at low pressures of binary and ternary systems involving methanol, ethanol, glycerol, water and NaCl
Pvap	34.50	kPa	523.15	Vapor Pressures and Evaporation Studies of Sugars and Sugar Alcohols
Pvap	62.60	kPa	543.15	Vapor Pressures and Evaporation Studies of Sugars and Sugar Alcohols
Pvap	66.66	kPa	547.25	Isobaric Phase Equilibrium of tert-Butyl Alcohol + Glycerol at Local and Subatmospheric Pressures, Volumetric Properties, and Molar Refractivity from 303.15 to 333.15 K of tert-Butyl Alcohol + Glycerol, tert-Butyl Alcohol + Water, and Water + Glycerol Binary Systems
Pvap	79.99	kPa	553.96	Isobaric Phase Equilibrium of tert-Butyl Alcohol + Glycerol at Local and Subatmospheric Pressures, Volumetric Properties, and Molar Refractivity from 303.15 to 333.15 K of tert-Butyl Alcohol + Glycerol, tert-Butyl Alcohol + Water, and Water + Glycerol Binary Systems
Pvap	95.99	kPa	560.95	Isobaric Phase Equilibrium of tert-Butyl Alcohol + Glycerol at Local and Subatmospheric Pressures, Volumetric Properties, and Molar Refractivity from 303.15 to 333.15 K of tert-Butyl Alcohol + Glycerol, tert-Butyl Alcohol + Water, and Water + Glycerol Binary Systems
n0	[1.46674; 1.47552]		[288.15; 323.15]
n0	1.47552		288.15	Experimental determination and modeling of excess molar volumes, viscosities and refractive indices of the binary systems (pyridine + 1-propanol, + 1,2-propanediol, + 1,3-propanediol, and + glycerol). New UNIFAC-VISCO parameters determination
n0	1.47400		293.15	Experimental (vapour + liquid) equilibrium data of (methanol + water), (water + glycerol) and (methanol + glycerol) systems at atmospheric and sub-atmospheric pressures
n0	1.47427		293.15	Experimental determination and modeling of excess molar volumes, viscosities and refractive indices of the binary systems (pyridine + 1-propanol, + 1,2-propanediol, + 1,3-propanediol, and + glycerol). New UNIFAC-VISCO parameters determination
n0	1.47260		298.15	Liquid liquid equilibria of the systems isobutyl acetate + isobutyl alcohol +water and isobutyl acetate + isobutyl alcohol + glycerol at different temperatures
n0	1.47100		298.15	(Vapor + liquid) equilibrium for the binary systems {water + glycerol} and {ethanol + glycerol, ethyl stearate, and ethyl palmitate} at low pressures
n0	1.47301		298.15	Experimental determination and modeling of excess molar volumes, viscosities and refractive indices of the binary systems (pyridine + 1-propanol, + 1,2-propanediol, + 1,3-propanediol, and + glycerol). New UNIFAC-VISCO parameters determination
n0	1.47175		303.15	Experimental determination and modeling of excess molar volumes, viscosities and refractive indices of the binary systems (pyridine + 1-propanol, + 1,2-propanediol, + 1,3-propanediol, and + glycerol). New UNIFAC-VISCO parameters determination
n0	1.47048		308.15	Experimental determination and modeling of excess molar volumes, viscosities and refractive indices of the binary systems (pyridine + 1-propanol, + 1,2-propanediol, + 1,3-propanediol, and + glycerol). New UNIFAC-VISCO parameters determination
n0	1.46920		313.15	Experimental determination and modeling of excess molar volumes, viscosities and refractive indices of the binary systems (pyridine + 1-propanol, + 1,2-propanediol, + 1,3-propanediol, and + glycerol). New UNIFAC-VISCO parameters determination
n0	1.46791		318.15	Experimental determination and modeling of excess molar volumes, viscosities and refractive indices of the binary systems (pyridine + 1-propanol, + 1,2-propanediol, + 1,3-propanediol, and + glycerol). New UNIFAC-VISCO parameters determination
n0	1.46674		323.15	Experimental determination and modeling of excess molar volumes, viscosities and refractive indices of the binary systems (pyridine + 1-propanol, + 1,2-propanediol, + 1,3-propanediol, and + glycerol). New UNIFAC-VISCO parameters determination
ρl	[1214.80; 1270.87]	kg/m3	[278.15; 363.15]
ρl	1270.87	kg/m3	278.15	Volume properties of liquid mixture of water + glycerol over the temperature range from 278.15 to 348.15 K at atmospheric pressure
ρl	1270.87	kg/m3	278.15	Volumetric properties of binary liquid-phase mixture of (water + glycerol) at temperatures of (278.15 to 323.15) K and pressures of (0.1 to 100) MPa
ρl	1267.00	kg/m3	283.15	Effect of temperature on density, sound velocity, and their derived properties for the binary systems glycerol with water or alcohols
ρl	1264.40	kg/m3	288.15	Volume properties of liquid mixture of water + glycerol over the temperature range from 278.15 to 348.15 K at atmospheric pressure
ρl	1264.40	kg/m3	288.15	Volumetric properties of binary liquid-phase mixture of (water + glycerol) at temperatures of (278.15 to 323.15) K and pressures of (0.1 to 100) MPa
ρl	1262.70	kg/m3	288.15	Density studies of 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures between 288.15 K and 328.15 K
ρl	1261.00	kg/m3	293.00	KDB
ρl	1262.00	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	1260.98	kg/m3	293.15	(Vapor-liquid) equilibria and excess Gibbs free energy functions of (ethanol + glycerol), or (water + glycerol) binary mixtures at several temperatures
ρl	1260.99	kg/m3	293.15	Volume properties of liquid mixture of water + glycerol over the temperature range from 278.15 to 348.15 K at atmospheric pressure
ρl	1260.50	kg/m3	293.15	Density studies of 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures between 288.15 K and 328.15 K
ρl	1261.00	kg/m3	293.15	Effect of temperature on density, sound velocity, and their derived properties for the binary systems glycerol with water or alcohols
ρl	1260.73	kg/m3	293.15	Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
ρl	1267.40	kg/m3	295.00	New device for fast measuring surface tension, density and viscosity of liquids
ρl	1257.20	kg/m3	298.15	Density studies of 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures between 288.15 K and 328.15 K
ρl	1262.00	kg/m3	298.15	Solubility of glucose in tetrabutylammonium bromide based deep eutectic solvents: Experimental and molecular dynamic simulations
ρl	1259.00	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	1258.52	kg/m3	298.15	Phase equilibria for the ternary systems ethanol, water + ethylene glycol or + glycerol at 101.3 kPa
ρl	1258.90	kg/m3	298.15	Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
ρl	1257.91	kg/m3	298.15	Volume properties of liquid mixture of water + glycerol over the temperature range from 278.15 to 348.15 K at atmospheric pressure
ρl	1258.52	kg/m3	298.15	Measurements and correlation at different temperatures of liquid-liquid equilibria of 2-butanol or 2-methyl-2-butanol + 1,2,3-propanetriol + water ternary systems
ρl	1257.91	kg/m3	298.15	Volumetric properties of binary liquid-phase mixture of (water + glycerol) at temperatures of (278.15 to 323.15) K and pressures of (0.1 to 100) MPa
ρl	1257.65	kg/m3	298.15	Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
ρl	1257.70	kg/m3	298.20	Deterpenation of Citrus Essential Oils Using Glycerol-Based Deep Eutectic Solvents
ρl	1254.80	kg/m3	303.15	Density studies of 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures between 288.15 K and 328.15 K
ρl	1255.80	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	1255.60	kg/m3	303.15	Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
ρl	1255.00	kg/m3	303.15	Effect of temperature on density, sound velocity, and their derived properties for the binary systems glycerol with water or alcohols
ρl	1254.48	kg/m3	303.15	Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
ρl	1257.13	kg/m3	303.15	Measurement of phase equilibria data for the extraction of toluene from alkane using different solvents
ρl	1251.66	kg/m3	308.15	Volume properties of liquid mixture of water + glycerol over the temperature range from 278.15 to 348.15 K at atmospheric pressure
ρl	1251.38	kg/m3	308.15	Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
ρl	1251.50	kg/m3	308.15	Density studies of 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures between 288.15 K and 328.15 K
ρl	1252.70	kg/m3	308.15	Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
ρl	1252.70	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	1251.66	kg/m3	308.15	Volumetric properties of binary liquid-phase mixture of (water + glycerol) at temperatures of (278.15 to 323.15) K and pressures of (0.1 to 100) MPa
ρl	1249.00	kg/m3	313.15	Experimental densities and viscosities of binary mixture of 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide or glycerol with sulfolane and their molecular interaction by COSMO-RS
ρl	1248.90	kg/m3	313.15	Density studies of 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures between 288.15 K and 328.15 K
ρl	1248.00	kg/m3	313.15	Effect of temperature on density, sound velocity, and their derived properties for the binary systems glycerol with water or alcohols
ρl	1249.50	kg/m3	313.15	Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
ρl	1249.60	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	1246.00	kg/m3	318.15	Density studies of 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures between 288.15 K and 328.15 K
ρl	1246.20	kg/m3	318.15	Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
ρl	1246.40	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	1243.20	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	1242.90	kg/m3	323.15	Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
ρl	1242.40	kg/m3	323.15	Experimental densities and viscosities of binary mixture of 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide or glycerol with sulfolane and their molecular interaction by COSMO-RS
ρl	1242.11	kg/m3	323.15	Volume properties of liquid mixture of water + glycerol over the temperature range from 278.15 to 348.15 K at atmospheric pressure
ρl	1242.11	kg/m3	323.15	Volumetric properties of binary liquid-phase mixture of (water + glycerol) at temperatures of (278.15 to 323.15) K and pressures of (0.1 to 100) MPa
ρl	1242.40	kg/m3	323.15	Density studies of 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures between 288.15 K and 328.15 K
ρl	1239.60	kg/m3	328.15	Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
ρl	1240.00	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	1240.50	kg/m3	328.15	Density studies of 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures between 288.15 K and 328.15 K
ρl	1235.70	kg/m3	333.15	Experimental densities and viscosities of binary mixture of 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide or glycerol with sulfolane and their molecular interaction by COSMO-RS
ρl	1236.70	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	1235.71	kg/m3	333.15	Volume properties of liquid mixture of water + glycerol over the temperature range from 278.15 to 348.15 K at atmospheric pressure
ρl	1236.00	kg/m3	333.15	Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
ρl	1233.40	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	1230.10	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	1228.90	kg/m3	343.15	Experimental densities and viscosities of binary mixture of 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide or glycerol with sulfolane and their molecular interaction by COSMO-RS
ρl	1225.79	kg/m3	348.15	Volume properties of liquid mixture of water + glycerol over the temperature range from 278.15 to 348.15 K at atmospheric pressure
ρl	1221.90	kg/m3	353.15	Experimental densities and viscosities of binary mixture of 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide or glycerol with sulfolane and their molecular interaction by COSMO-RS
ρl	1214.80	kg/m3	363.15	Experimental densities and viscosities of binary mixture of 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide or glycerol with sulfolane and their molecular interaction by COSMO-RS
ΔfusS	[62.70; 62.80]	J/mol×K	[291.00; 292.00]
ΔfusS	62.80	J/mol×K	291.00	NIST
ΔfusS	62.70	J/mol×K	292.00	NIST
γ	[0.06; 0.07]	N/m	[288.10; 333.20]
γ	0.07	N/m	288.10	Studies on surface tension of 1,8-diazabicyclo [5.4.0] undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures from 288.1 K to 323.1 K
γ	0.06	N/m	293.10	Studies on surface tension of 1,8-diazabicyclo [5.4.0] undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures from 288.1 K to 323.1 K
γ	0.06	N/m	293.20	Surface tension and interfacial compositions of binary glycerol/alcohol mixtures
γ	0.06	N/m	298.10	Studies on surface tension of 1,8-diazabicyclo [5.4.0] undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures from 288.1 K to 323.1 K
γ	0.06	N/m	298.20	Surface tension and interfacial compositions of binary glycerol/alcohol mixtures
γ	0.06	N/m	303.10	Studies on surface tension of 1,8-diazabicyclo [5.4.0] undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures from 288.1 K to 323.1 K
γ	0.06	N/m	303.20	Surface tension and interfacial compositions of binary glycerol/alcohol mixtures
γ	0.06	N/m	308.10	Studies on surface tension of 1,8-diazabicyclo [5.4.0] undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures from 288.1 K to 323.1 K
γ	0.06	N/m	313.10	Studies on surface tension of 1,8-diazabicyclo [5.4.0] undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures from 288.1 K to 323.1 K
γ	0.06	N/m	313.20	Surface tension and interfacial compositions of binary glycerol/alcohol mixtures
γ	0.06	N/m	318.10	Studies on surface tension of 1,8-diazabicyclo [5.4.0] undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures from 288.1 K to 323.1 K
γ	0.06	N/m	323.10	Studies on surface tension of 1,8-diazabicyclo [5.4.0] undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures from 288.1 K to 323.1 K
γ	0.06	N/m	323.20	Surface tension and interfacial compositions of binary glycerol/alcohol mixtures
γ	0.06	N/m	333.20	Surface tension and interfacial compositions of binary glycerol/alcohol mixtures
λ	[0.28; 0.28]	W/m×K	[283.15; 333.15]
λ	0.28	W/m×K	283.15	Measurements of the density, refractive index, electrical conductivity, thermal conductivity and dynamic viscosity for tributylmethylphosphonium and methylsulfate based ionic liquids
λ	0.28	W/m×K	293.15	Measurements of the density, refractive index, electrical conductivity, thermal conductivity and dynamic viscosity for tributylmethylphosphonium and methylsulfate based ionic liquids
λ	0.28	W/m×K	303.15	Measurements of the density, refractive index, electrical conductivity, thermal conductivity and dynamic viscosity for tributylmethylphosphonium and methylsulfate based ionic liquids
λ	0.28	W/m×K	313.15	Measurements of the density, refractive index, electrical conductivity, thermal conductivity and dynamic viscosity for tributylmethylphosphonium and methylsulfate based ionic liquids
λ	0.28	W/m×K	323.15	Measurements of the density, refractive index, electrical conductivity, thermal conductivity and dynamic viscosity for tributylmethylphosphonium and methylsulfate based ionic liquids
λ	0.28	W/m×K	333.15	Measurements of the density, refractive index, electrical conductivity, thermal conductivity and dynamic viscosity for tributylmethylphosphonium and methylsulfate based ionic liquids

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil	[459.28; 560.68]	K	[3.47; 94.93]
Tboil	459.28	K	3.47	Improving a variation of the DSC technique for measuring the boiling points of pure compounds at low pressures
Tboil	560.68	K	94.93	Experimental vapour - liquid equilibrium data of the quaternary system Methanol (1) + Isopropyl Alcohol (2) + Water (3) + Glycerol (4) along with Isopropyl Alcohol (2) + Glycerol (4) and Isopropyl Alcohol (2) + Water (3) binary data at atmospheric and sub-atmospheric pressures.
Tboilr	455.20	K	2.70	NIST

Datasets

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

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.15	100.00	1.2
Reference

Refractive index (Na D-line)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Refractive index (Na D-line) - Liquid
298.15	100.00	1.4722
Reference

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
91.20	303.15	1255.0
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	1258.4
298.15	5000.00	1260.7
298.15	10000.00	1262.3
298.15	15000.00	1263.7
298.15	20000.00	1265.2
298.15	25000.00	1266.6
303.15	100.00	1255.7
303.15	5000.00	1257.8
303.15	10000.00	1259.3
303.15	15000.00	1260.8
303.15	20000.00	1262.3
303.15	25000.00	1263.7
308.15	100.00	1252.9
308.15	5000.00	1254.9
308.15	10000.00	1256.3
308.15	15000.00	1257.9
308.15	20000.00	1259.4
308.15	25000.00	1260.8
313.15	100.00	1250.1
313.15	5000.00	1251.8
313.15	10000.00	1253.4
313.15	15000.00	1254.9
313.15	20000.00	1256.4
313.15	25000.00	1257.9
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	101.13	1238.0
Reference

Thermal conductivity, W/m/K

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Thermal conductivity, W/m/K - Liquid
77.00	295.00	0.2890
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[106.61; 249.54]	J/mol×K	[273.00; 1200.15]	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			3.13663e+01
Coefficient B			-3.11254e+02
Coefficient C			5.40735e+00
Coefficient D			1.95602e-04
Coefficient E			1.75208e-09
Comment			ChemSep eq 16, IdealGasHeatCapacityCp
Temperature range, min.			273.00
Temperature range, max.			1200.15
Cp,gas	106.61	J/mol×K	273.00	Calculated Property
Cp,gas	136.31	J/mol×K	376.02	Calculated Property
Cp,gas	159.32	J/mol×K	479.03	Calculated Property
Cp,gas	177.87	J/mol×K	582.05	Calculated Property
Cp,gas	193.41	J/mol×K	685.07	Calculated Property
Cp,gas	206.87	J/mol×K	788.08	Calculated Property
Cp,gas	218.86	J/mol×K	891.10	Calculated Property
Cp,gas	229.80	J/mol×K	994.12	Calculated Property
Cp,gas	239.96	J/mol×K	1097.13	Calculated Property
Cp,gas	249.54	J/mol×K	1200.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[168.37; 347.99]	J/mol×K	[187.40; 561.00]	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			1.15636e-01
Coefficient B			-3.33362e+01
Coefficient C			4.89230e+00
Coefficient D			2.38285e-03
Coefficient E			-1.00980e-06
Comment			ChemSep eq 16, LiquidHeatCapacityCp
Temperature range, min.			187.40
Temperature range, max.			561.00
Cp,liquid	168.37	J/mol×K	187.40	Calculated Property
Cp,liquid	188.64	J/mol×K	228.91	Calculated Property
Cp,liquid	208.54	J/mol×K	270.42	Calculated Property
Cp,liquid	228.37	J/mol×K	311.93	Calculated Property
Cp,liquid	248.27	J/mol×K	353.44	Calculated Property
Cp,liquid	268.25	J/mol×K	394.96	Calculated Property
Cp,liquid	288.30	J/mol×K	436.47	Calculated Property
Cp,liquid	308.33	J/mol×K	477.98	Calculated Property
Cp,liquid	328.27	J/mol×K	519.49	Calculated Property
Cp,liquid	347.99	J/mol×K	561.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[27.1949230; 0.0000782]	Pa×s	[260.00; 500.00]	ChemSep v8.3 pure component data
Equation			ln(Y) = A + B/(T + C) Y is η in Pa×s, T in K
Coefficient A			-2.70000e+01
Coefficient B			1.00000e+04
Coefficient C			7.00000e+01
Comment			ChemSep eq 10, LiquidViscosity
Temperature range, min.			260.00
Temperature range, max.			500.00
η	27.1949230	Pa×s	260.00	Calculated Property
η	2.8218231	Pa×s	286.67	Calculated Property
η	0.4013010	Pa×s	313.33	Calculated Property
η	0.0735525	Pa×s	340.00	Calculated Property
η	0.0165853	Pa×s	366.67	Calculated Property
η	0.0044393	Pa×s	393.33	Calculated Property
η	0.0013715	Pa×s	420.00	Calculated Property
η	0.0004784	Pa×s	446.67	Calculated Property
η	0.0001850	Pa×s	473.33	Calculated Property
η	0.0000782	Pa×s	500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[89.24; 0.00]	kJ/mol	[291.33; 850.00]	ChemSep v8.3 pure component data
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			1.12325e+02
Coefficient B			1.03267e+00
Coefficient C			-2.40171e+00
Coefficient D			3.40853e+00
Coefficient E			-1.53507e+00
Critical temperature, Tc (K)			8.50000e+02
Comment			ChemSep eq 106, HeatOfVaporization
Temperature range, min.			291.33
Temperature range, max.			850.00
ΔvapH	89.24	kJ/mol	291.33	Calculated Property
ΔvapH	85.26	kJ/mol	353.40	Calculated Property
ΔvapH	80.64	kJ/mol	415.48	Calculated Property
ΔvapH	75.15	kJ/mol	477.55	Calculated Property
ΔvapH	68.64	kJ/mol	539.63	Calculated Property
ΔvapH	61.01	kJ/mol	601.70	Calculated Property
ΔvapH	52.20	kJ/mol	663.78	Calculated Property
ΔvapH	42.00	kJ/mol	725.85	Calculated Property
ΔvapH	29.38	kJ/mol	787.93	Calculated Property
ΔvapH	0.00	kJ/mol	850.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[451.47; 591.41]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39571e+01
Coefficient B			-3.29185e+03
Coefficient C			-2.10657e+02
Temperature range, min.			451.47
Temperature range, max.			591.41
Pvap	1.33	kPa	451.47	Calculated Property
Pvap	3.05	kPa	467.02	Calculated Property
Pvap	6.36	kPa	482.57	Calculated Property
Pvap	12.25	kPa	498.12	Calculated Property
Pvap	22.05	kPa	513.67	Calculated Property
Pvap	37.47	kPa	529.21	Calculated Property
Pvap	60.61	kPa	544.76	Calculated Property
Pvap	93.93	kPa	560.31	Calculated Property
Pvap	140.24	kPa	575.86	Calculated Property
Pvap	202.65	kPa	591.41	Calculated Property
Pvap	[1.11e-05; 5741.68]	kPa	[291.33; 850.00]	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			9.26669e+01
Coefficient B			-1.36739e+04
Coefficient C			-1.00700e+01
Coefficient D			1.22772e-11
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			291.33
Temperature range, max.			850.00
Pvap	1.11e-05	kPa	291.33	Calculated Property
Pvap	6.03e-03	kPa	353.40	Calculated Property
Pvap	0.38	kPa	415.48	Calculated Property
Pvap	6.79	kPa	477.55	Calculated Property
Pvap	53.43	kPa	539.63	Calculated Property
Pvap	243.72	kPa	601.70	Calculated Property
Pvap	759.39	kPa	663.78	Calculated Property
Pvap	1797.20	kPa	725.85	Calculated Property
Pvap	3469.55	kPa	787.93	Calculated Property
Pvap	5741.68	kPa	850.00	Calculated Property
Pvap	[7.84e-06; 3545.31]	kPa	[290.15; 723.00]	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			1.65510e+02
Coefficient B			-1.67263e+04
Coefficient C			-2.12587e+01
Coefficient D			1.10048e-05
Coefficient E			0.00000e+00
Temperature range, min.			290.15
Temperature range, max.			723.00
Pvap	7.84e-06	kPa	290.15	Calculated Property
Pvap	1.52e-03	kPa	338.24	Calculated Property
Pvap	0.06	kPa	386.34	Calculated Property
Pvap	0.96	kPa	434.43	Calculated Property
Pvap	7.77	kPa	482.53	Calculated Property
Pvap	40.79	kPa	530.62	Calculated Property
Pvap	159.30	kPa	578.72	Calculated Property
Pvap	507.43	kPa	626.81	Calculated Property
Pvap	1405.71	kPa	674.91	Calculated Property
Pvap	3545.31	kPa	723.00	Calculated Property
Pvap	[2.63; 50.00]	kPa	[456.40; 533.60]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.36713e+01
Coefficient B			-3.25017e+03
Coefficient C			-2.00566e+02
Reference			Richardson, 1886, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			456.40
Temperature range, max.			533.60
Pvap	2.63	kPa	456.40	Calculated Property
Pvap	3.97	kPa	464.98	Calculated Property
Pvap	5.84	kPa	473.56	Calculated Property
Pvap	8.40	kPa	482.13	Calculated Property
Pvap	11.82	kPa	490.71	Calculated Property
Pvap	16.30	kPa	499.29	Calculated Property
Pvap	22.08	kPa	507.87	Calculated Property
Pvap	29.43	kPa	516.44	Calculated Property
Pvap	38.63	kPa	525.02	Calculated Property
Pvap	50.00	kPa	533.60	Calculated Property
Pvap	[2.63; 50.00]	kPa	[456.40; 533.60]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.36713e+01
Coefficient B			-3.25017e+03
Coefficient C			-2.00566e+02
Reference			Richardson, 1886
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			456.40
Temperature range, max.			533.60
Pvap	2.63	kPa	456.40	Calculated Property
Pvap	3.97	kPa	464.98	Calculated Property
Pvap	5.84	kPa	473.56	Calculated Property
Pvap	8.40	kPa	482.13	Calculated Property
Pvap	11.82	kPa	490.71	Calculated Property
Pvap	16.30	kPa	499.29	Calculated Property
Pvap	22.08	kPa	507.87	Calculated Property
Pvap	29.43	kPa	516.44	Calculated Property
Pvap	38.63	kPa	525.02	Calculated Property
Pvap	50.00	kPa	533.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1253.06; 349.23]	kg/m3	[291.33; 850.00]	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			8.59847e+01
Coefficient B			2.46209e-01
Coefficient C			8.50000e+02
Coefficient D			2.20672e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			291.33
Temperature range, max.			850.00
ρl	1253.06	kg/m3	291.33	Calculated Property
ρl	1212.65	kg/m3	353.40	Calculated Property
ρl	1169.61	kg/m3	415.48	Calculated Property
ρl	1123.27	kg/m3	477.55	Calculated Property
ρl	1072.69	kg/m3	539.63	Calculated Property
ρl	1016.39	kg/m3	601.70	Calculated Property
ρl	951.75	kg/m3	663.78	Calculated Property
ρl	873.49	kg/m3	725.85	Calculated Property
ρl	766.98	kg/m3	787.93	Calculated Property
ρl	349.23	kg/m3	850.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.06; 0.05]	N/m	[291.33; 453.15]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			2.57537e-03
Coefficient B			-9.14476e+01
Coefficient C			-2.24949e+00
Coefficient D			2.63632e-04
Coefficient E			-3.69750e-06
Comment			ChemSep eq 16, SurfaceTension
Temperature range, min.			291.33
Temperature range, max.			453.15
γ	0.06	N/m	291.33	Calculated Property
γ	0.06	N/m	309.31	Calculated Property
γ	0.06	N/m	327.29	Calculated Property
γ	0.06	N/m	345.27	Calculated Property
γ	0.06	N/m	363.25	Calculated Property
γ	0.06	N/m	381.23	Calculated Property
γ	0.05	N/m	399.21	Calculated Property
γ	0.05	N/m	417.19	Calculated Property
γ	0.05	N/m	435.17	Calculated Property
γ	0.05	N/m	453.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.00; 0.07]	W/m×K	[274.00; 1000.00]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λ in W/m×K, T in K
Coefficient A			-8.80104e-03
Coefficient B			-4.45798e+02
Coefficient C			-2.85734e+00
Coefficient D			6.77005e-04
Coefficient E			8.72276e-08
Comment			ChemSep eq 16, VaporThermalConductivity
Temperature range, min.			274.00
Temperature range, max.			1000.00
λ	0.00	W/m×K	274.00	Calculated Property
λ	0.01	W/m×K	354.67	Calculated Property
λ	0.02	W/m×K	435.33	Calculated Property
λ	0.03	W/m×K	516.00	Calculated Property
λ	0.03	W/m×K	596.67	Calculated Property
λ	0.04	W/m×K	677.33	Calculated Property
λ	0.05	W/m×K	758.00	Calculated Property
λ	0.05	W/m×K	838.67	Calculated Property
λ	0.06	W/m×K	919.33	Calculated Property
λ	0.07	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.29; 0.32]	W/m×K	[293.15; 550.00]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λ in W/m×K, T in K
Coefficient A			8.21317e-03
Coefficient B			-1.34710e+01
Coefficient C			-1.28502e+00
Coefficient D			1.97192e-04
Coefficient E			1.22666e-07
Comment			ChemSep eq 16, LiquidThermalConductivity
Temperature range, min.			293.15
Temperature range, max.			550.00
λ	0.29	W/m×K	293.15	Calculated Property
λ	0.29	W/m×K	321.69	Calculated Property
λ	0.30	W/m×K	350.23	Calculated Property
λ	0.30	W/m×K	378.77	Calculated Property
λ	0.30	W/m×K	407.31	Calculated Property
λ	0.31	W/m×K	435.84	Calculated Property
λ	0.31	W/m×K	464.38	Calculated Property
λ	0.31	W/m×K	492.92	Calculated Property
λ	0.32	W/m×K	521.46	Calculated Property
λ	0.32	W/m×K	550.00	Calculated Property

Similar Compounds

Find more compounds similar to Glycerin.

Mixtures

• Urea + Glycerin + Water
• Glucose + Glycerin + Water
• Choline chloride + Glycerin
• Glycerin + Ethanol, 2-diethylamino-, hydrochloride
• Glycerin + METHYLTRIPHENYLPHOSPHONIUM BROMIDE
• Choline chloride + Glycerin + Water
• Ethanol + Glycerin + Water
• Carbon dioxide + Glycerin
• Glycerin + Methyl Alcohol
• Ethanol + Glycerin
• Glycerin + Water
• Glycerin + Methyl Alcohol + Water
• sodium chloride + Glycerin + Water
• sodium chloride + Glycerin
• Dodecanoic acid, methyl ester + Glycerin + Methyl Alcohol
• Glycerin + Methyl tetradecanoate + Methyl Alcohol
• Glycerin + Hexadecanoic acid, methyl ester + Methyl Alcohol
• Carbon dioxide + Ethanol + Glycerin
• 1-Propanol + Carbon dioxide + Glycerin
• Carbon dioxide + 1-Butanol + Glycerin

Find more mixtures with Glycerin.

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.
• Crippen Method
• Conductometric Study of Some Metal Halides in Glycerol + Water Mixtures
• Liquid liquid equilibria of the systems isobutyl acetate + isobutyl alcohol +water and isobutyl acetate + isobutyl alcohol + glycerol at different temperatures
• Dielectric properties and hydrogen bonding interaction behaviour in binary mixtures of glycerol with amides and amines
• 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
• Phase equilibria of glycerol containing systems and their description with the Cubic-Plus-Association (CPA) Equation of State
• Measurement and calculation of vapor liquid equilibria for methanol + glycerol and ethanol + glycerol systems at 493 573K
• 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
• Liquid-liquid equilibria for mixtures containing water, methanol, fatty acid methyl esters, and glycerol
• VLE of CO2 + glycerol + (ethanol or 1-propanol or 1-butanol)
• Densities of a deep eutectic solvent based on choline chloride and glycerol and its aqueous mixtures at elevated pressures
• Phase equilibria for the ternary systems ethanol, water + ethylene glycol or + glycerol at 101.3 kPa
• LLE for the systems ethyl palmitate (palmiticacid)(1) + ethanol(2) + glycerol (water)(3)
• 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
• Solubility of CO2 in glycerol at high pressures
• Densities and dynamic viscosities of (choline chloride + glycerol) deep eutectic solvent and its aqueous mixtures in the temperature range (283.15-363.15) K
• Measurements and modeling of CO2 solubility in 1,8-diazabicyclo-[5.4.0]-undec-7-ene - glycerol solutions
• Measurements and correlation at different temperatures of liquid-liquid equilibria of 2-butanol or 2-methyl-2-butanol + 1,2,3-propanetriol + water ternary systems
• Acoustic investigation of choline chloride based ionic liquids analogues
• Thermodynamic properties of glycerol: experimental and theoretical study
• Measurement of phase equilibria data for the extraction of toluene from alkane using different solvents
• Phase equilibria of triolein to biodiesel reactor systems
• Experimental vapour - liquid equilibrium data of the quaternary system Methanol (1) + Isopropyl Alcohol (2) + Water (3) + Glycerol (4) along with Isopropyl Alcohol (2) + Glycerol (4) and Isopropyl Alcohol (2) + Water (3) binary data at atmospheric and sub-atmospheric pressures.
• Liquid-liquid equilibrium for the ternary system of isopropyl acetate + 2-propanol + glycerol at different temperatures under atmospheric pressure
• A model to calculate concentration-dependent surface tension of binary systems
• Measurement and correlation of ternary vapor-liquid equilibria for methanol + glycerol + fatty acid methyl ester (methyl laurate, methyl myristate, methyl palmitate) systems at elevated temperatures and pressures
• Partitioning of diuron in a novel aqueous two-phase system based on polyols and tetrahydrofuran
• 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
• Thermodynamics of phase transfer for polar molecules from alkanes to deep eutectic solvents
• Liquid pharmaceuticals formulation by eutectic formation
• Solubility of glucose in tetrabutylammonium bromide based deep eutectic solvents: Experimental and molecular dynamic simulations
• Oil desulfurization using deep eutectic solvents as sustainable and economical extractants via liquid-liquid extraction: Experimental and PC-SAFT predictions
• Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
• Viscometric study of myo-inositol in aqueous deep eutectic solvent solutions
• Extraction of benzothiazole and thiophene from their mixtures with n-heptane using tetrahexylammonium bromide-based deep eutectic solvents as extractive denitrogenation and desulfurization agents
• The experimental study on the influence of crown ethers and glycols on the mutual solubility of lithium bromide in water
• Sodium salts solubility in ternary glycerol+water+alcohol mixtures present in purification process of crude glycerol from the biodiesel industry
• 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
• Apparent molar volumes and apparent molar heat capacities of aqueous adonitol, dulcitol, glycerol, meso-erythritol, myo-inositol, D-sorbitol, and xylitol at temperatures from (278.15 to 368.15) K and at the pressure 0.35 MPa
• Experimental (vapour + liquid) equilibrium data of (methanol + water), (water + glycerol) and (methanol + glycerol) systems at atmospheric and sub-atmospheric pressures
• (Vapor + liquid) equilibrium for the binary systems {water + glycerol} and {ethanol + glycerol, ethyl stearate, and ethyl palmitate} at low pressures
• (Liquid + liquid) equilibrium for the system {ethyl stearate(1) + ethanol(2) + glycerol(3)}
• Experimental determination and modeling of excess molar volumes, viscosities and refractive indices of the binary systems (pyridine + 1-propanol, + 1,2-propanediol, + 1,3-propanediol, and + glycerol). New UNIFAC-VISCO parameters determination
• Solubility of carbon dioxide in a eutectic mixture of choline chloride and glycerol at moderate pressures
• Thermophysical properties of biodiesel and related systems. Part I. Vapour liquid equilibrium at low pressures of binary and ternary systems involving methanol, ethanol, glycerol, water and NaCl
• Densities, refractive indices, and viscosities of N,N-diethylethanol ammonium chloride - glycerol or - ethylene glycol deep eutectic solvents and their aqueous solutions
• Vapor-liquid equilibrium of the (water + ethanol + glycerol) system: Experimental and modelling data at normal pressure
• (Vapor-liquid) equilibria and excess Gibbs free energy functions of (ethanol + glycerol), or (water + glycerol) binary mixtures at several temperatures
• Volumetric properties of binary liquid-phase mixture of (water + glycerol) at temperatures of (278.15 to 323.15) K and pressures of (0.1 to 100) MPa
• Liquid extraction of polyhydric alcohols from water using [A336][SCN] as a solvent
• NaCl and KCl effect on (vapour + liquid) equilibrium of binary, ternary and quaternary systems involving water, ethanol and glycerol at low pressures
• Improving a variation of the DSC technique for measuring the boiling points of pure compounds at low pressures
• Liquid glycerol: Experimental densities at pressures of up to 25 MPa, and some derived thermodynamic properties
• Measurement and modelling of urea solubility in aqueous propane-1,2,3-triol and prop-2-enoic acid solutions
• 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
• Effect of temperature on density, sound velocity, and their derived properties for the binary systems glycerol with water or alcohols
• The viscosity of glycerol
• Density and refractive index measurements of transition-temperature mixture (deep eutectic analogues) based on potassium carbonate with dual hydrogen bond donors for CO2 capture
• Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
• Density studies of 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures between 288.15 K and 328.15 K
• Experimental and modeling vapor-liquid equilibrium for the binary systems {ethanol(1) + glycerol(2)} and {tert-butanol(1) + glycerol(2)} at high pressures
• Studies on surface tension of 1,8-diazabicyclo [5.4.0] undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures from 288.1 K to 323.1 K
• 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
• Acoustical and volumetric investigation of polyethylene glycol 400 and polyethylene glycol 4000 in aqueous solutions of glycerol at different temperatures
• The NADES glyceline as a potential Green Solvent: A comprehensive study of its thermophysical properties and effect of water inclusion
• Solubility modelling and thermodynamic properties of allopurinol in aqueous solutions of four deep eutectic solvents
• Solubility and thermodynamic properties of NH3 in choline chloride-based deep eutectic solvents
• Surface tension and interfacial compositions of binary glycerol/alcohol mixtures
• Studies on viscosity and conductivity of 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures from 288.1 K to 328.1 K
• Solubility of CO2 in methanol, ethanol, 1,2-propanediol and glycerol from 283.15 K to 373.15 K and up to 6.0 MPa
• Enthalpies of solution of l-threonine in aqueous alcohol solutions
• Enthalpies of dilution of formamide in aqueous alcohol solutions at 298.15K
• 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
• 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
• Molar heat capacities and electrical conductivities of two ammonium-based deepeutectic solvents and their aqueous solutions
• Volume properties of liquid mixture of water + glycerol over the temperature range from 278.15 to 348.15 K at atmospheric pressure
• 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
• Experimental densities and viscosities of binary mixture of 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide or glycerol with sulfolane and their molecular interaction by COSMO-RS
• Measurements of the density, refractive index, electrical conductivity, thermal conductivity and dynamic viscosity for tributylmethylphosphonium and methylsulfate based ionic liquids
• Thermal transport properties of heptane-isooctane mixtures
• Vapor Liquid Equilibrium of Water + Ethanol + Glycerol: Experimental Measurement and Modeling for Ethanol Dehydration by Extractive Distillation
• Glycerol-Based Deep Eutectic Solvents as Extractants for the Separation of MEK and Ethanol via Liquid Liquid Extraction
• Molar Heat Capacity of Selected Type III Deep Eutectic Solvents
• Experimental Measurement and Modeling of Vapor-Liquid Equilibrium for the Ternary System Water + 1-Propanol + Glycerol
• Isobaric Phase Equilibrium of tert-Butyl Alcohol + Glycerol at Local and Subatmospheric Pressures, Volumetric Properties, and Molar Refractivity from 303.15 to 333.15 K of tert-Butyl Alcohol + Glycerol, tert-Butyl Alcohol + Water, and Water + Glycerol Binary Systems
• Liquid Liquid Equilibrium for the Ternary System of Methyl Laurate/Methyl Myristate + Ethanol + Glycerol at 318.15 and 333.15 K
• Excess Molar Enthalpies of Deep Eutectic Solvents (DESs) Composed of Quaternary Ammonium Salts and Glycerol or Ethylene Glycol
• Viscosities and Carbon Dioxide Solubilities of Guanidine Carbonate and Malic Acid-Based Eutectic Solvents
• Solubilities of Diethyl Phthalate, Dicyclopentadiene, and Styrene in Ionic Liquid 1-Ethyl-3-methylimidazolium Acetate
• Density Measurements of CO2-Expanded Liquids
• Solubility of Etoricoxib in Aqueous Solutions of Glycerin, Methanol, Polyethylene Glycols 200, 400, 600, and Propylene Glycol at 298.2 K
• Binary Diffusion Coefficients of Glycerol-Water Mixtures for Temperatures from 323 to 448 K by Dynamic Light Scattering
• Effect of the Type of Ammonium Salt on the Extractive Desulfurization of Fuels Using Deep Eutectic Solvents
• Deterpenation of Citrus Essential Oils Using Glycerol-Based Deep Eutectic Solvents
• 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
• Effect of Cosolvents DMSO and Glycerol on the Self-Assembly Behavior of SDBS and CPC: An Experimental and Theoretical Approach
• Thermophysical Properties of Ternary Systems Potassium Formate + Propylene Glycol/Glycerol + Water
• Solubilities and Thermodynamic Properties of NH3 in Glycerin and its Derivatives
• Thermophysical and Molar Volume Aberration of Amphiphilic Eutectic Mix of Bivalent Diols and Ammonium-Ionic Liquid
• Fixed-Path Length Laser-Induced Sound Pinging: A Streamlined Method for Sound Speed Determination in Arbitrary Liquids
• Measurement and Correlation of Mutual Solubilities for High Viscosity Binary Systems: Aniline + Methylcyclohexane, Phenol + Heptane, Phenol + Octane, and Glycerol + 1-Pentanol
• Ternary Diffusion Coefficients of Glycerol + Acetone + Water by Taylor Dispersion Measurements at 298.15 K
• Solubility of Valdecoxib in the Presence of Glycerol, Propylene Glycol, and Poly(ethylene glycol) 400 at (298.15, 303.15, and 308.15) K
• Solubility of Rofecoxib in the Presence of Aqueous Solutions of Glycerol, Propylene Glycol, Ethanol, Span 20, Tween 80, and Sodium Lauryl Sulfate at (298.15, 303.15, and 308.15) K
• 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
• Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
• Phosphonium-Based Ionic Liquids Analogues and Their Physical Properties
• Experimental and Predicted (Vapor + Liquid) Equilibrium Data of Ternary Mixtures of Methanol, Water, and Propan-1,2,3-triol at 96 kPa
• Measurement and Correlation of Solubilities of Potassium Chloride and Potassium Sulfate in Aqueous Glycerol Solutions
• Solubilities, Densities, and Refractive Indices for the Ternary Systems Glycerin + MCl + H2O (M = Na, K, Rb, Cs) at (298.15 and 308.15) K
• Vapor-Liquid Equilibria of Glycerol, 1,3-Propanediol, Glycerol + Water, and Glycerol + 1,3-Propanediol
• Liquid-Liquid Equilibria for the System Dimethyl Carbonate + Methanol + Glycerol in the Temperature Range of (303.15 to 333.15) K
• Partial Molar Volumes and Partial Molar Isentropic Compressions of Three Polyhydric Alcohols Derived from Propane at Infinite Dilution in Water at Temperatures T = (278 to 318) K and Atmospheric Pressure
• 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
• Article Ternary Liquid Liquid Equilibrium of Biodiesel Compounds for Systems Consisting of a Methyl Ester + Glycerin + Water
• Solubility of Sodium Salts in Ammonium-Based Deep Eutectic Solvents
• Experimental Vapor Liquid Equilibria for the Systems {2-Ethyl-1-hexanol + Glycerol + CO2} and {2-Methyl-2-propanol + Glycerol + CO2}
• Tetrabutylammonium Chloride Based Ionic Liquid Analogues and Their Physical Properties
• Liquid-liquid equilibria for the system acetone + solketal + glycerol at 303.2, 313.2 and 323.2 K
• Liquid Liquid Equilibrium in Mixtures Containing Propane-1,2,3-triol and Mixtures Containing Vegetable Oils at Atmospheric Pressure
• Experimental Measurement and Modeling of Ternary Vapor Liquid Equilibrium for Water + 2-Propanol + Glycerol
• Liquid Liquid Equilibria of Three Ternary Systems: {Glycerol + Benzene + Methanol}, {Glycerol + Benzene + Ethanol}, and {Glycerol + Benzene + 1-Propanol}
• Isothermal Vapor Liquid Equilibrium of Ethanol + Glycerol and 2-Propanol + Glycerol at Different Temperatures
• Solubilities of 2-Methyl-1,4-naphthoquinone in Water + (Methanol, Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, and Glycerin, Respectively) from (293.15 to 337.92) K
• Solubilities of Menadione Sodium Bisulfite in Water + (Methanol, Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, and Glycerin, Respectively) from (297.67 to 337.76) K
• Vapor Pressures and Evaporation Studies of Sugars and Sugar Alcohols
• Physical Properties (Density, Excess Molar Volume, Viscosity, Surface Tension, and Refractive Index) of Ethanol + Glycerol
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
• Densities and Viscosities of Propane-1,2,3-triol + Ethane-1,2-diol at T = (298.15 to 338.15) K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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