Chemical Properties of 2-Furanmethanol (CAS 98-00-0)

InChI

InChI=1S/C5H6O2/c6-4-5-2-1-3-7-5/h1-3,6H,4H2

InChI Key

XPFVYQJUAUNWIW-UHFFFAOYSA-N

Formula

C5H6O2

SMILES

OCc1ccco1

Molecular Weight¹

98.10

CAS

98-00-0

Other Names

• 2-(Hydroxymethyl)furan
• 2-Furancarbinol
• 2-Furane-methanol (furfurol)
• 2-Furanemethanol
• 2-Furanmethanol (furfuryl alcohol)
• 2-Furanylmethanol
• 2-Furfuryl alcohol
• 2-Furfurylalkohol
• 2-Furylcarbinol
• 2-Hydroxymethylfurane
• 2-furylmethanol
• 2-hydroxymethylfuran
• 5-Hydroxymethylfuran
• ALPHA-FURFURYL ALCOHOL
• Furan-2-methanol
• Furfural alcohol
• Furfuralcohol
• Furfuranol
• Furfurol
• Furyl alcohol
• Furylcarbinol
• Methanol, (2-furyl)-
• NCI-C56224
• NSC 8843
• Qo furfuryl alcohol
• UN 2874
• furanmethanol
• furfuryl alcohol
• furfuryl alcohol (furfurol)
• «alpha»-Furfuryl alcohol
• «alpha»-Furylcarbinol

• T_ig : Autoignition Temperature (K).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• 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 a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
Tig	764.15	K	NCMS SOLV-DB
ΔcH°liquid	[-2548.70; -2540.00]	kJ/mol
ΔcH°liquid	-2548.70	kJ/mol	NIST
ΔcH°liquid	-2548.00	kJ/mol	NIST
ΔcH°liquid	-2540.00	kJ/mol	NIST
Tflash,cc	338.15	K	NCMS SOLV-DB
ΔfH°gas	[-212.60; -211.80]	kJ/mol
ΔfH°gas	-212.00	kJ/mol	NIST
ΔfH°gas	-212.60	kJ/mol	NIST
ΔfH°gas	-211.80 ± 2.10	kJ/mol	NIST
ΔfH°liquid	[-277.00; -276.20]	kJ/mol
ΔfH°liquid	-276.40	kJ/mol	NIST
ΔfH°liquid	-277.00	kJ/mol	NIST
ΔfH°liquid	-276.20 ± 1.30	kJ/mol	NIST
ΔvapH°	[64.40; 64.43]	kJ/mol
ΔvapH°	64.43	kJ/mol	NCMS SOLV-DB
ΔvapH°	64.40 ± 1.70	kJ/mol	NIST
ΔvapH°	64.40	kJ/mol	NIST
IE	8.81	eV	Relay (1.0) Calculated Property
logPoct/wat	0.280		NCMS SOLV-DB
McVol	73.590	ml/mol	McGowan Calculated Property
NFPA Fire	[%!d(float64=2); %!d(float64=2)]
NFPA Fire	2		KDB
NFPA Fire	2		NCMS SOLV-DB
NFPA Health	[%!d(float64=1); %!d(float64=1)]
NFPA Health	1		KDB
NFPA Health	1		NCMS SOLV-DB
NFPA Safety	[%!d(float64=1); %!d(float64=1)]
NFPA Safety	1		KDB
NFPA Safety	1		NCMS SOLV-DB
Inp	[127.02; 891.00]
Inp	855.00		NIST
Inp	819.00		NIST
Inp	863.00		NIST
Inp	856.00		NIST
Inp	833.00		NIST
Inp	846.00		NIST
Inp	Outlier 127.02		NIST
Inp	840.00		NIST
Inp	830.00		NIST
Inp	827.00		NIST
Inp	844.00		NIST
Inp	856.00		NIST
Inp	857.00		NIST
Inp	857.00		NIST
Inp	858.00		NIST
Inp	855.00		NIST
Inp	850.00		NIST
Inp	856.00		NIST
Inp	851.00		NIST
Inp	852.00		NIST
Inp	819.00		NIST
Inp	851.00		NIST
Inp	826.10		NIST
Inp	880.00		NIST
Inp	813.00		NIST
Inp	863.00		NIST
Inp	876.00		NIST
Inp	880.00		NIST
Inp	830.00		NIST
Inp	819.00		NIST
Inp	856.00		NIST
Inp	830.00		NIST
Inp	865.00		NIST
Inp	857.00		NIST
Inp	832.00		NIST
Inp	833.00		NIST
Inp	835.00		NIST
Inp	827.00		NIST
Inp	835.00		NIST
Inp	835.00		NIST
Inp	846.00		NIST
Inp	875.00		NIST
Inp	875.00		NIST
Inp	864.00		NIST
Inp	845.00		NIST
Inp	891.00		NIST
Inp	864.00		NIST
Inp	864.00		NIST
Inp	884.00		NIST
Inp	868.00		NIST
Inp	853.00		NIST
Inp	823.00		NIST
Inp	866.00		NIST
Inp	844.00		NIST
Inp	855.00		NIST
Inp	861.00		NIST
Inp	867.00		NIST
Inp	845.00		NIST
Inp	857.00		NIST
Inp	850.00		NIST
Inp	853.00		NIST
Inp	884.00		NIST
Inp	852.00		NIST
Inp	864.00		NIST
Inp	864.00		NIST
Inp	854.00		NIST
Inp	857.00		NIST
Inp	854.00		NIST
Inp	832.00		NIST
Inp	865.90		NIST
Inp	827.00		NIST
Inp	829.00		NIST
Inp	866.00		NIST
Inp	853.00		NIST
Inp	830.00		NIST
Inp	839.00		NIST
Inp	842.00		NIST
Inp	835.00		NIST
Inp	827.00		NIST
Inp	827.00		NIST
Inp	849.00		NIST
Inp	827.00		NIST
Inp	823.00		NIST
Inp	865.00		NIST
Inp	863.00		NIST
Inp	825.00		NIST
Inp	826.00		NIST
Inp	829.00		NIST
Inp	826.00		NIST
Inp	827.00		NIST
Inp	826.00		NIST
Inp	874.00		NIST
Inp	860.00		NIST
Inp	864.00		NIST
Inp	862.00		NIST
Inp	866.00		NIST
Inp	848.00		NIST
Inp	848.00		NIST
Inp	864.00		NIST
Inp	850.00		NIST
Inp	858.00		NIST
Inp	882.00		NIST
Inp	857.00		NIST
Inp	860.00		NIST
Inp	860.00		NIST
Inp	853.00		NIST
Inp	856.00		NIST
Inp	853.00		NIST
Inp	860.00		NIST
Inp	853.00		NIST
Inp	858.00		NIST
Inp	834.00		NIST
Inp	827.00		NIST
Inp	824.00		NIST
Inp	852.00		NIST
Inp	853.00		NIST
Inp	867.00		NIST
Inp	850.00		NIST
Inp	825.00		NIST
Inp	823.00		NIST
Inp	863.00		NIST
Inp	875.00		NIST
Inp	881.00		NIST
Inp	812.00		NIST
Inp	830.00		NIST
Inp	832.00		NIST
Inp	856.00		NIST
Inp	Outlier 127.02		NIST
Ip	[1613.00; 1698.00]
Ip	1658.00		NIST
Ip	1632.00		NIST
Ip	1668.00		NIST
Ip	1667.00		NIST
Ip	1668.00		NIST
Ip	Outlier 1617.00		NIST
Ip	1666.00		NIST
Ip	1623.00		NIST
Ip	Outlier 1614.00		NIST
Ip	Outlier 1617.00		NIST
Ip	1640.00		NIST
Ip	1669.00		NIST
Ip	1665.00		NIST
Ip	1660.00		NIST
Ip	1667.00		NIST
Ip	1658.00		NIST
Ip	1631.00		NIST
Ip	1669.00		NIST
Ip	1649.00		NIST
Ip	1656.00		NIST
Ip	1662.00		NIST
Ip	Outlier 1613.00		NIST
Ip	1643.00		NIST
Ip	1665.00		NIST
Ip	1635.00		NIST
Ip	1652.00		NIST
Ip	1665.00		NIST
Ip	1693.00		NIST
Ip	1650.00		NIST
Ip	1655.00		NIST
Ip	1656.00		NIST
Ip	1666.00		NIST
Ip	1666.00		NIST
Ip	1656.00		NIST
Ip	1659.00		NIST
Ip	1664.00		NIST
Ip	1664.00		NIST
Ip	1662.00		NIST
Ip	1667.00		NIST
Ip	1659.00		NIST
Ip	1651.00		NIST
Ip	1665.00		NIST
Ip	1678.00		NIST
Ip	1661.00		NIST
Ip	1690.00		NIST
Ip	1690.00		NIST
Ip	1665.00		NIST
Ip	1620.00		NIST
Ip	Outlier 1698.00		NIST
Ip	1692.00		NIST
Ip	1655.00		NIST
Ip	1651.00		NIST
Ip	1652.00		NIST
Ip	1685.00		NIST
Ip	1687.00		NIST
Ip	1671.00		NIST
Ip	1694.00		NIST
Ip	1626.00		NIST
Ip	1667.00		NIST
Ip	1670.00		NIST
Ip	1647.00		NIST
Ip	1678.00		NIST
Ip	1664.00		NIST
Ip	1671.00		NIST
Ip	1689.00		NIST
Ip	1670.00		NIST
Ip	1694.00		NIST
Ip	1646.00		NIST
Ip	1647.00		NIST
Ip	Outlier 1619.00		NIST
Ip	1666.00		NIST
Ip	1659.00		NIST
Ip	1657.00		NIST
Ip	1659.00		NIST
Ip	1675.00		NIST
Ip	1669.00		NIST
Ip	1660.00		NIST
Ip	1661.00		NIST
Ip	1673.00		NIST
Ip	1673.00		NIST
Ip	1664.00		NIST
Ip	1665.00		NIST
Ip	1687.00		NIST
Ip	1685.00		NIST
Ip	1640.00		NIST
Ip	1648.00		NIST
Ip	Outlier 1616.00		NIST
Ip	1686.00		NIST
Ip	1686.00		NIST
Ip	1686.00		NIST
Ip	1650.00		NIST
Ip	1656.00		NIST
Ip	1659.00		NIST
Ip	1656.00		NIST
Ip	1686.00		NIST
Ip	1666.00		NIST
Ip	1660.00		NIST
Ip	1623.00		NIST
Ip	1647.00		NIST
Ip	1663.00		NIST
Ip	1663.00		NIST
Ip	1659.00		NIST
Ip	1638.00		NIST
Ip	1660.00		NIST
Ip	1626.00		NIST
Ip	1622.00		NIST
Ip	1653.00		NIST
Ip	1650.00		NIST
Ip	1661.00		NIST
Ip	1650.00		NIST
Ip	1625.00		NIST
Ip	1630.00		NIST
Ip	1658.00		NIST
Ip	1661.00		NIST
Ip	1680.00		NIST
Ip	1678.00		NIST
Ip	1661.00		NIST
Ip	1632.00		NIST
Ip	1661.00		NIST
Ip	1647.00		NIST
Ip	1662.00		NIST
Ip	1647.00		NIST
Ip	1668.00		NIST
Ip	1686.00		NIST
Ip	1660.00		NIST
Ip	1663.00		NIST
Ip	1669.00		NIST
Ip	1667.00		NIST
Ip	1657.00		NIST
Ip	1656.00		NIST
Ip	1662.00		NIST
Ip	1656.00		NIST
Ip	1668.00		NIST
Ip	1620.00		NIST
Ip	1662.00		NIST
Ip	1670.00		NIST
Ip	1640.00		NIST
Ip	Outlier 1617.00		NIST
Ip	1685.00		NIST
Ip	1671.00		NIST
Ip	1647.00		NIST
Ip	1657.00		NIST
Ip	1661.00		NIST
Ip	1687.00		NIST
Ip	Outlier 1616.00		NIST
Ip	1686.00		NIST
Ip	1663.00		NIST
Ip	1660.00		NIST
Ip	1650.00		NIST
Ip	1678.00		NIST
Ip	1620.00		NIST
Ip	1651.00		NIST
S°liquid	[215.50; 215.90]	J/mol×K
S°liquid	215.90	J/mol×K	NIST
S°liquid	215.50	J/mol×K	NIST
Tboil	[347.65; 444.15]	K
Tboil	444.15	K	NCMS SOLV-DB
Tboil	443.20	K	NIST
Tboil	444.15 ± 2.00	K	NIST
Tboil	444.00 ± 2.00	K	NIST
Tboil	442.50 ± 0.50	K	NIST
Tboil	442.50 ± 0.30	K	NIST
Tboil	Outlier 347.65 ± 1.50	K	NIST
Tfus	[244.15; 250.35]	K
Tfus	250.35	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	244.15	K	NCMS SOLV-DB
Ttriple	[253.50; 258.60]	K
Ttriple	258.60 ± 0.20	K	NIST
Ttriple	253.50 ± 0.30	K	NIST
Ttriple	258.60 ± 0.20	K	NIST
Ttriple	253.50 ± 0.30	K	NIST

Cheméo can also estimate Critical Temperature, Critical Pressure, Critical Volume, Standard Gibbs free energy of formation, Acentric Factor, Log10 of Water solubility in mol/l for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[193.30; 204.01]	J/mol×K	[298.15; 303.00]
Cp,liquid	204.01	J/mol×K	298.15	NIST
Cp,liquid	193.30	J/mol×K	303.00	NIST
η	0.0046200	Pa×s	298.15	NCMS SOLV-DB
ΔfusH	[13.10; 14.81]	kJ/mol	[253.50; 258.60]
ΔfusH	14.81	kJ/mol	253.50	NIST
ΔfusH	13.10	kJ/mol	258.60	NIST
ΔfusH	13.13	kJ/mol	258.60	NIST
ΔfusH	13.13	kJ/mol	258.60	NIST
ΔvapH	53.60	kJ/mol	373.50	NIST
Pvap	[9.00e-03; 36.53]	kPa	[273.11; 412.11]
Pvap	9.00e-03	kPa	273.11	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	0.02	kPa	283.08	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	0.05	kPa	293.16	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	0.08	kPa	298.15	NCMS SOLV-DB
Pvap	0.12	kPa	303.09	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	0.24	kPa	313.15	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	0.47	kPa	323.15	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	0.47	kPa	323.16	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	0.81	kPa	331.87	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	0.89	kPa	333.15	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	0.88	kPa	333.17	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	1.48	kPa	341.85	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	1.60	kPa	343.15	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	1.61	kPa	343.19	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	2.58	kPa	351.81	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	2.75	kPa	353.15	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	2.79	kPa	353.20	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	2.60	kPa	353.30	Isothermal vapor liquid equilibrium for binary mixtures containing furfural and its derivatives
Pvap	4.37	kPa	362.09	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	4.59	kPa	363.15	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	4.65	kPa	363.20	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	7.07	kPa	372.04	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	7.00	kPa	373.00	Isothermal vapor liquid equilibrium for binary mixtures containing furfural and its derivatives
Pvap	7.40	kPa	373.15	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	11.09	kPa	382.09	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	11.59	kPa	383.15	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	17.10	kPa	392.15	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	17.68	kPa	393.15	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	25.11	kPa	402.18	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	30.10	kPa	407.90	Isothermal vapor liquid equilibrium for binary mixtures containing furfural and its derivatives
Pvap	36.53	kPa	412.11	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
n0	1.48700		298.15	NCMS SOLV-DB
ρl	[1113.63; 1141.46]	kg/m3	[283.15; 313.15]
ρl	1141.46	kg/m3	283.15	Volumetric and acoustic properties of binary systems (furfural or furfuryl alcohol + toluene) and (furfuryl alcohol + ethanol) at different temperatures
ρl	1132.26	kg/m3	293.15	Volumetric and acoustic properties of binary systems (furfural or furfuryl alcohol + toluene) and (furfuryl alcohol + ethanol) at different temperatures
ρl	1130.27	kg/m3	298.15	Self-aggregation of liquids from biomass in aqueous solution
ρl	1122.99	kg/m3	303.15	Volumetric and acoustic properties of binary systems (furfural or furfuryl alcohol + toluene) and (furfuryl alcohol + ethanol) at different temperatures
ρl	1113.63	kg/m3	313.15	Volumetric and acoustic properties of binary systems (furfural or furfuryl alcohol + toluene) and (furfuryl alcohol + ethanol) at different temperatures
ΔfusS	[50.77; 58.40]	J/mol×K	[253.50; 258.60]
ΔfusS	58.40	J/mol×K	253.50	NIST
ΔfusS	50.77	J/mol×K	258.60	NIST
ΔfusS	50.77	J/mol×K	258.60	NIST
γ	0.04	N/m	298.15	NCMS SOLV-DB

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[339.70; 467.51]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.68800e+01
Coefficient B			-4.88331e+03
Coefficient C			-4.53900e+01
Temperature range, min.			339.70
Temperature range, max.			467.51
Pvap	1.33	kPa	339.70	Calculated Property
Pvap	2.86	kPa	353.90	Calculated Property
Pvap	5.74	kPa	368.10	Calculated Property
Pvap	10.87	kPa	382.30	Calculated Property
Pvap	19.53	kPa	396.50	Calculated Property
Pvap	33.53	kPa	410.71	Calculated Property
Pvap	55.30	kPa	424.91	Calculated Property
Pvap	87.96	kPa	439.11	Calculated Property
Pvap	135.46	kPa	453.31	Calculated Property
Pvap	202.64	kPa	467.51	Calculated Property

Similar Compounds

Find more compounds similar to 2-Furanmethanol.

Mixtures

• Furan, 2-methyl- + 2-Furanmethanol
• 2-Furanmethanol + 2-Propanol
• 2-Furanmethanol + Furan, 2,5-dimethyl-
• Toluene + 2-Furanmethanol
• 2-Furanmethanol + Ethanol
• 2-Furanmethanol + Pentane
• n-Hexane + 2-Furanmethanol
• 2-Furanmethanol + Heptane
• 2-Furanmethanol + Cyclopentane
• 2-Furanmethanol + Cyclohexane
• 2-Furanmethanol + Cycloheptane
• 2-Furanmethanol + 1-Hexene
• 2-Furanmethanol + 1-Heptene
• 2-Furanmethanol + 1-Hexyne
• 1-Heptyne + 2-Furanmethanol
• Benzene + 2-Furanmethanol
• 2-Furanmethanol + Water
• 2-Furanmethanol + Carbon dioxide

Sources

• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• Cheméo Relay (1.0)
• Cheméo Relay (1.0, beta) Beta: served but experimental, data-limited and below our cross-validation release bar; the Joback value is recommended where available.
• Crippen Method
• Isothermal vapor liquid equilibrium for binary mixtures containing furfural and its derivatives
• Activity coefficients at infinite dilution for hydrocarbons in furfuryl alcohol at T=(278.15 and 298.15) K, determined by g.l.c.
• Self-aggregation of liquids from biomass in aqueous solution
• Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
• Volumetric and acoustic properties of binary systems (furfural or furfuryl alcohol + toluene) and (furfuryl alcohol + ethanol) at different temperatures
• Solubilities of Carbon Dioxide in Five Bio-based Solvents
• KDB
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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