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

• 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).
• 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_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 : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• 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
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	debye	KDB
ΔfG°	-438.52	kJ/mol	Joback Calculated Property
ΔfH°gas	[-585.30; -576.90]	kJ/mol
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. Sol...
log10WS	1.12		Estimat...
logPoct/wat	-1.668		Crippen Calculated Property
McVol	70.740	ml/mol	McGowan Calculated Property
NFPA Fire	1		KDB
NFPA Health	1		KDB
Pc	[6680.00; 7500.00]	kPa
Pc	6680.00	kPa	KDB
Pc	7500.00 ± 200.00	kPa	NIST
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	563.00	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	726.00	K	KDB
Tc	850.00 ± 4.00	K	NIST
Tfus	[286.00; 292.00]	K
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	291.80 ± 0.20	K	NIST
Ttriple	291.00 ± 0.20	K	NIST
Vc	0.255	m3/kmol	KDB
Zc	0.2821910		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[169.59; 196.19]	J/mol×K	[544.14; 702.69]
Cp,gas	169.59	J/mol×K	544.14	Joback Calculated Property
Cp,gas	174.50	J/mol×K	570.56	Joback Calculated Property
Cp,gas	179.21	J/mol×K	596.99	Joback Calculated Property
Cp,gas	183.73	J/mol×K	623.41	Joback Calculated Property
Cp,gas	188.07	J/mol×K	649.84	Joback Calculated Property
Cp,gas	192.22	J/mol×K	676.26	Joback Calculated Property
Cp,gas	196.19	J/mol×K	702.69	Joback Calculated Property
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	221.90	J/mol×K	298.15	NIST
Cp,liquid	218.90	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...
η	1.4700000	Pa×s	292.89	The vis...
η	1.2520000	Pa×s	296.50	Viscosi...
η	0.9338000	Pa×s	298.10	Studies...
η	0.9706000	Pa×s	298.10	The vis...
η	0.9438000	Pa×s	298.15	Densiti...
η	0.6458000	Pa×s	302.59	The vis...
η	0.6734000	Pa×s	302.80	Viscosi...
η	0.6289000	Pa×s	303.15	Densiti...
η	0.4203000	Pa×s	308.10	Studies...
η	0.4319000	Pa×s	308.15	Densiti...
η	0.3053000	Pa×s	312.81	The vis...
η	0.2959000	Pa×s	313.15	Densiti...
η	0.2606000	Pa×s	315.80	Viscosi...
η	0.1956000	Pa×s	318.10	Studies...
η	0.1858000	Pa×s	318.15	Densiti...
η	0.1512000	Pa×s	323.15	Densiti...
η	0.1489000	Pa×s	323.20	Viscosi...
η	0.1474000	Pa×s	323.88	The vis...
η	0.1043000	Pa×s	328.10	Studies...
η	0.1084000	Pa×s	328.15	Densiti...
η	0.0975000	Pa×s	332.70	Viscosi...
η	0.0848000	Pa×s	333.15	Densiti...
η	0.0847100	Pa×s	333.15	The vis...
η	0.0622000	Pa×s	338.15	Densiti...
η	0.0519000	Pa×s	343.20	Viscosi...
η	0.0498300	Pa×s	343.80	The vis...
η	0.0428000	Pa×s	348.20	Viscosi...
η	0.0318000	Pa×s	353.67	The vis...
η	0.0349000	Pa×s	354.20	Viscosi...
η	0.0210500	Pa×s	364.12	The vis...
η	0.0147400	Pa×s	374.38	The vis...
η	0.0110000	Pa×s	383.29	The vis...
η	0.0083200	Pa×s	394.08	The vis...
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	Thermod...
Pvap	4.19e-05	kPa	303.61	Thermod...
Pvap	4.68e-05	kPa	304.56	Thermod...
Pvap	5.56e-05	kPa	306.03	Thermod...
Pvap	7.28e-05	kPa	308.43	Thermod...
Pvap	9.63e-05	kPa	310.89	Thermod...
Pvap	1.25e-04	kPa	313.29	Thermod...
Pvap	1.63e-04	kPa	315.71	Thermod...
Pvap	2.11e-04	kPa	318.12	Thermod...
Pvap	2.70e-04	kPa	320.57	Thermod...
Pvap	3.47e-04	kPa	322.95	Thermod...
Pvap	4.43e-04	kPa	325.42	Thermod...
Pvap	5.64e-04	kPa	327.82	Thermod...
Pvap	7.17e-04	kPa	330.30	Thermod...
Pvap	9.04e-04	kPa	332.72	Thermod...
Pvap	1.13e-03	kPa	335.14	Thermod...
Pvap	1.50e-03	kPa	338.25	Thermod...
Pvap	1.87e-03	kPa	340.68	Thermod...
Pvap	2.32e-03	kPa	343.08	Thermod...
Pvap	2.88e-03	kPa	345.51	Thermod...
Pvap	3.53e-03	kPa	347.91	Thermod...
Pvap	4.36e-03	kPa	350.34	Thermod...
Pvap	5.83e-03	kPa	351.80	Vapor-L...
Pvap	5.26e-03	kPa	352.57	Thermod...
Pvap	5.27e-03	kPa	352.58	Thermod...
Pvap	5.28e-03	kPa	352.60	Thermod...
Pvap	5.32e-03	kPa	352.73	Thermod...
Pvap	6.39e-03	kPa	354.98	Thermod...
Pvap	6.41e-03	kPa	354.99	Thermod...
Pvap	6.49e-03	kPa	355.18	Thermod...
Pvap	7.77e-03	kPa	357.39	Thermod...
Pvap	7.82e-03	kPa	357.42	Thermod...
Pvap	7.86e-03	kPa	357.57	Thermod...
Pvap	9.38e-03	kPa	359.80	Thermod...
Pvap	9.39e-03	kPa	359.82	Thermod...
Pvap	9.52e-03	kPa	360.01	Thermod...
Pvap	0.01	kPa	362.02	Vapor-L...
Pvap	0.01	kPa	362.42	Thermod...
Pvap	0.01	kPa	362.63	Thermod...
Pvap	0.01	kPa	362.66	Thermod...
Pvap	0.01	kPa	364.82	Thermod...
Pvap	0.01	kPa	365.07	Thermod...
Pvap	0.01	kPa	365.08	Thermod...
Pvap	0.02	kPa	367.45	Thermod...
Pvap	0.02	kPa	367.48	Thermod...
Pvap	0.02	kPa	369.89	Thermod...
Pvap	0.02	kPa	369.91	Thermod...
Pvap	0.03	kPa	372.06	Vapor-L...
Pvap	0.02	kPa	372.27	Thermod...
Pvap	0.02	kPa	372.29	Thermod...
Pvap	0.03	kPa	374.70	Thermod...
Pvap	0.03	kPa	374.73	Thermod...
Pvap	0.03	kPa	377.08	Thermod...
Pvap	0.03	kPa	377.11	Thermod...
Pvap	0.04	kPa	377.77	Thermod...
Pvap	0.04	kPa	380.17	Thermod...
Pvap	0.04	kPa	380.19	Thermod...
Pvap	0.05	kPa	382.08	Vapor-L...
Pvap	0.05	kPa	382.55	Thermod...
Pvap	0.05	kPa	382.59	Thermod...
Pvap	0.05	kPa	382.59	Thermod...
Pvap	0.06	kPa	384.99	Thermod...
Pvap	0.06	kPa	385.01	Thermod...
Pvap	0.07	kPa	387.37	Thermod...
Pvap	0.07	kPa	387.39	Thermod...
Pvap	0.08	kPa	389.80	Thermod...
Pvap	0.08	kPa	389.83	Thermod...
Pvap	0.09	kPa	392.18	Thermod...
Pvap	0.10	kPa	392.18	Vapor-L...
Pvap	0.09	kPa	392.20	Thermod...
Pvap	0.11	kPa	394.61	Thermod...
Pvap	0.11	kPa	394.64	Thermod...
Pvap	0.13	kPa	397.00	Thermod...
Pvap	0.13	kPa	397.02	Thermod...
Pvap	0.15	kPa	399.42	Thermod...
Pvap	0.15	kPa	399.45	Thermod...
Pvap	0.17	kPa	401.81	Thermod...
Pvap	0.17	kPa	401.81	Thermod...
Pvap	0.17	kPa	401.83	Thermod...
Pvap	0.18	kPa	402.16	Vapor-L...
Pvap	0.20	kPa	404.23	Thermod...
Pvap	0.20	kPa	404.26	Thermod...
Pvap	0.22	kPa	406.62	Thermod...
Pvap	0.22	kPa	406.62	Thermod...
Pvap	0.23	kPa	406.64	Thermod...
Pvap	0.27	kPa	409.68	Thermod...
Pvap	0.27	kPa	409.69	Thermod...
Pvap	0.31	kPa	412.08	Thermod...
Pvap	0.31	kPa	412.11	Thermod...
Pvap	0.32	kPa	412.24	Vapor-L...
Pvap	0.35	kPa	414.48	Thermod...
Pvap	0.35	kPa	414.49	Thermod...
Pvap	0.40	kPa	416.89	Thermod...
Pvap	0.40	kPa	416.92	Thermod...
Pvap	0.46	kPa	419.30	Thermod...
Pvap	0.46	kPa	419.30	Thermod...
Pvap	0.52	kPa	421.70	Thermod...
Pvap	0.52	kPa	421.73	Thermod...
Pvap	0.53	kPa	422.28	Vapor-L...
Pvap	0.59	kPa	424.10	Thermod...
Pvap	0.59	kPa	424.11	Thermod...
Pvap	0.67	kPa	426.50	Thermod...
Pvap	0.67	kPa	426.53	Thermod...
Pvap	0.76	kPa	428.91	Thermod...
Pvap	0.76	kPa	428.91	Thermod...
Pvap	0.86	kPa	431.31	Thermod...
Pvap	0.86	kPa	431.34	Thermod...
Pvap	0.98	kPa	432.45	Vapor-L...
Pvap	0.97	kPa	433.72	Thermod...
Pvap	0.97	kPa	433.73	Thermod...
Pvap	1.09	kPa	436.11	Thermod...
Pvap	1.09	kPa	436.13	Thermod...
Pvap	2.75	kPa	452.64	Vapor-L...
Pvap	4.10	kPa	462.86	Vapor-L...
Pvap	3.85	kPa	463.15	Vapor P...
Pvap	6.70	kPa	477.25	Thermop...
Pvap	8.64	kPa	483.15	Vapor P...
Pvap	13.30	kPa	493.35	Thermop...
Pvap	17.90	kPa	503.15	Vapor P...
Pvap	20.00	kPa	505.55	Thermop...
Pvap	26.70	kPa	513.95	Thermop...
Pvap	33.30	kPa	520.65	Thermop...
Pvap	34.50	kPa	523.15	Vapor P...
Pvap	62.60	kPa	543.15	Vapor P...
Pvap	66.66	kPa	547.25	Isobari...
Pvap	79.99	kPa	553.96	Isobari...
Pvap	95.99	kPa	560.95	Isobari...
n0	[1.46674; 1.47552]		[288.15; 323.15]
n0	1.47552		288.15	Experim...
n0	1.47400		293.15	Experim...
n0	1.47427		293.15	Experim...
n0	1.47260		298.15	Liquid ...
n0	1.47100		298.15	(Vapor ...
n0	1.47301		298.15	Experim...
n0	1.47175		303.15	Experim...
n0	1.47048		308.15	Experim...
n0	1.46920		313.15	Experim...
n0	1.46791		318.15	Experim...
n0	1.46674		323.15	Experim...
ρl	[1214.80; 1270.87]	kg/m3	[278.15; 363.15]
ρl	1270.87	kg/m3	278.15	Volume ...
ρl	1267.00	kg/m3	283.15	Effect ...
ρl	1264.40	kg/m3	288.15	Volume ...
ρl	1262.70	kg/m3	288.15	Density...
ρl	1261.00	kg/m3	293.00	KDB
ρl	1262.00	kg/m3	293.15	Density...
ρl	1260.98	kg/m3	293.15	(Vapor-...
ρl	1260.99	kg/m3	293.15	Volume ...
ρl	1261.00	kg/m3	293.15	Effect ...
ρl	1260.50	kg/m3	293.15	Density...
ρl	1260.73	kg/m3	293.15	Thermod...
ρl	1267.40	kg/m3	295.00	New dev...
ρl	1259.00	kg/m3	298.15	Density...
ρl	1258.52	kg/m3	298.15	Measure...
ρl	1257.91	kg/m3	298.15	Volume ...
ρl	1257.20	kg/m3	298.15	Density...
ρl	1262.00	kg/m3	298.15	Solubil...
ρl	1258.90	kg/m3	298.15	Densiti...
ρl	1257.65	kg/m3	298.15	Thermod...
ρl	1258.52	kg/m3	298.15	Phase e...
ρl	1257.70	kg/m3	298.20	Deterpe...
ρl	1254.80	kg/m3	303.15	Density...
ρl	1255.00	kg/m3	303.15	Effect ...
ρl	1255.80	kg/m3	303.15	Density...
ρl	1254.48	kg/m3	303.15	Thermod...
ρl	1257.13	kg/m3	303.15	Measure...
ρl	1255.60	kg/m3	303.15	Densiti...
ρl	1251.50	kg/m3	308.15	Density...
ρl	1251.38	kg/m3	308.15	Thermod...
ρl	1252.70	kg/m3	308.15	Density...
ρl	1252.70	kg/m3	308.15	Densiti...
ρl	1251.66	kg/m3	308.15	Volume ...
ρl	1248.00	kg/m3	313.15	Effect ...
ρl	1249.50	kg/m3	313.15	Densiti...
ρl	1248.90	kg/m3	313.15	Density...
ρl	1249.60	kg/m3	313.15	Density...
ρl	1249.00	kg/m3	313.15	Experim...
ρl	1246.00	kg/m3	318.15	Density...
ρl	1246.20	kg/m3	318.15	Densiti...
ρl	1246.40	kg/m3	318.15	Density...
ρl	1242.90	kg/m3	323.15	Densiti...
ρl	1242.40	kg/m3	323.15	Density...
ρl	1242.11	kg/m3	323.15	Volume ...
ρl	1242.40	kg/m3	323.15	Experim...
ρl	1243.20	kg/m3	323.15	Density...
ρl	1240.50	kg/m3	328.15	Density...
ρl	1240.00	kg/m3	328.15	Density...
ρl	1239.60	kg/m3	328.15	Densiti...
ρl	1236.70	kg/m3	333.15	Density...
ρl	1235.70	kg/m3	333.15	Experim...
ρl	1236.00	kg/m3	333.15	Densiti...
ρl	1235.71	kg/m3	333.15	Volume ...
ρl	1233.40	kg/m3	338.15	Density...
ρl	1230.10	kg/m3	343.15	Density...
ρl	1228.90	kg/m3	343.15	Experim...
ρl	1225.79	kg/m3	348.15	Volume ...
ρl	1221.90	kg/m3	353.15	Experim...
ρl	1214.80	kg/m3	363.15	Experim...
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...
γ	0.06	N/m	293.10	Studies...
γ	0.06	N/m	293.20	Surface...
γ	0.06	N/m	298.10	Studies...
γ	0.06	N/m	298.20	Surface...
γ	0.06	N/m	303.10	Studies...
γ	0.06	N/m	303.20	Surface...
γ	0.06	N/m	308.10	Studies...
γ	0.06	N/m	313.10	Studies...
γ	0.06	N/m	313.20	Surface...
γ	0.06	N/m	318.10	Studies...
γ	0.06	N/m	323.10	Studies...
γ	0.06	N/m	323.20	Surface...
γ	0.06	N/m	333.20	Surface...
λ	[0.28; 0.28]	W/m×K	[283.15; 333.15]
λ	0.28	W/m×K	283.15	Measure...
λ	0.28	W/m×K	293.15	Measure...
λ	0.28	W/m×K	303.15	Measure...
λ	0.28	W/m×K	313.15	Measure...
λ	0.28	W/m×K	323.15	Measure...
λ	0.28	W/m×K	333.15	Measure...

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	Improvi...
Tboil	560.68	K	94.93	Experim...
Tboilr	455.20	K	2.70	NIST

Datasets

1. Viscosity, Pa*s (1)
2. Mass density, kg/m3 (3)

Viscosity, Pa*s

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

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[451.47; 591.41]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
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	[7.84e-06; 3545.31]	kPa	[290.15; 723.00]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			1.65510e+02
Coefficient B			-1.67263e+04
Coefficient C			-2.12587e+01
Coefficient D			1.10048e-05
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

Similar Compounds

Find more compounds similar to Glycerin.

Mixtures

• Isobutyl acetate + Glycerin + 1-Propanol, 2-methyl-
• Ethanol + Glycerin + Water
• Carbon dioxide + Glycerin
• Carbon dioxide + Pyrimido[1,2-a]azepine, 2,3,4,6,7,8,9,10-octahydro- + Glycerin
• Amylene hydrate + Glycerin + Water
• Toluene + Decane + Glycerin
• Isopropyl Alcohol + Glycerin
• Glycerin + Tetracycline hydrochloride
• Tetra-N-butylammonium bromide + Glycerin
• Glucose + Tetra-N-butylammonium bromide + Glycerin
• Choline chloride + Glycerin + Water
• Glycerin + Water
• Glycerin + Methyl Alcohol
• Ethanol + Glycerin
• Pyridine + Glycerin
• Glycerin + Methyl Alcohol + Water
• sodium chloride + Glycerin + Water
• sodium chloride + Glycerin
• Glycerin + Ethanol, 2-diethylamino-, hydrochloride
• Glycerin + Water + Ethanol, 2-diethylamino-, hydrochloride

Find more mixtures with Glycerin.

Sources

• KDB Vapor Pressure Data
• 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
• 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
• 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
• 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
• 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
• 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
• 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
• 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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