Chemical Properties of Tetrahydrofuran (CAS 109-99-9)

InChI

InChI=1S/C4H8O/c1-2-4-5-3-1/h1-4H2

InChI Key

WYURNTSHIVDZCO-UHFFFAOYSA-N

Formula

C4H8O

SMILES

C1CCOC1

Molecular Weight¹

72.11

CAS

109-99-9

Other Names

• 1,4-epoxybutane
• Butane «alpha»,«delta»-oxide
• Butane «alpha»,«delta»-oxide
• Butane, 1,4-epoxy-
• Cyclotetramethylene oxide
• Diethylene oxide
• Dynasolve 150
• Furan, tetrahydro-
• Furanidine
• Hydrofuran
• NCI-C60560
• NSC 57858
• Oxacyclopentane
• Oxolane
• Rcra waste number U213
• THF
• THF (tetrahydrofuran)
• Tetrahydrofuraan
• Tetrahydrofurane
• Tetrahydrofuranne
• Tetraidrofurano
• Tetramethylene oxide
• UN 2056

• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_gas : Standard gas enthalpy of combustion (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).
• 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_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• ν : Kinematic viscosity (m²/s).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boil : Boiling point at given pressure (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• V_m : Molar Volume (m³/mol).
• 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	822.10	kJ/mol	NIST
BasG	794.70	kJ/mol	NIST
ΔcH°gas	-2533.20 ± 0.67	kJ/mol	NIST
ΔcH°liquid	[-2505.80; -2501.20]	kJ/mol
ΔcH°liquid	-2505.80 ± 2.10	kJ/mol	NIST
ΔcH°liquid	-2501.20 ± 0.84	kJ/mol	NIST
η	0.0004750	Pa×s	A volum...
ΔfG°	-59.06	kJ/mol	Joback Calculated Property
ΔfH°gas	-184.20 ± 0.71	kJ/mol	NIST
ΔfusH°	6.96	kJ/mol	Joback Calculated Property
ΔvapH°	[32.00; 32.90]	kJ/mol
ΔvapH°	32.16	kJ/mol	NIST
ΔvapH°	32.00	kJ/mol	NIST
ΔvapH°	32.90	kJ/mol	NIST
ΔvapH°	32.00	kJ/mol	NIST
IE	[9.38; 9.74]	eV
IE	9.40 ± 0.02	eV	NIST
IE	9.38 ± 0.05	eV	NIST
IE	9.38	eV	NIST
IE	9.41	eV	NIST
IE	9.42 ± 0.01	eV	NIST
IE	9.54	eV	NIST
IE	9.74	eV	NIST
IE	9.71	eV	NIST
IE	9.65	eV	NIST
IE	9.53	eV	NIST
IE	9.57 ± 0.02	eV	NIST
log10WS	0.49		Estimat...
logPoct/wat	0.797		Crippen Calculated Property
McVol	62.230	ml/mol	McGowan Calculated Property
Pc	5190.00 ± 50.66	kPa	NIST
Inp	[608.00; 640.00]
Inp	609.90		NIST
Inp	609.80		NIST
Inp	611.00		NIST
Inp	630.00		NIST
Inp	626.00		NIST
Inp	620.00		NIST
Inp	631.00		NIST
Inp	618.00		NIST
Inp	612.90		NIST
Inp	623.20		NIST
Inp	640.00		NIST
Inp	640.00		NIST
Inp	631.00		NIST
Inp	618.00		NIST
Inp	617.00		NIST
Inp	621.00		NIST
Inp	609.00		NIST
Inp	610.00		NIST
Inp	632.00		NIST
Inp	629.00		NIST
Inp	623.00		NIST
Inp	622.00		NIST
Inp	626.00		NIST
Inp	629.00		NIST
Inp	620.00		NIST
Inp	620.00		NIST
Inp	624.00		NIST
Inp	630.00		NIST
Inp	614.00		NIST
Inp	618.00		NIST
Inp	620.00		NIST
Inp	633.00		NIST
Inp	615.00		NIST
Inp	618.00		NIST
Inp	619.00		NIST
Inp	636.00		NIST
Inp	615.00		NIST
Inp	624.00		NIST
Inp	615.00		NIST
Inp	638.00		NIST
Inp	608.00		NIST
Inp	612.00		NIST
Inp	629.00		NIST
Inp	627.00		NIST
Inp	638.00		NIST
Inp	622.00		NIST
Inp	624.00		NIST
Inp	617.00		NIST
Inp	619.00		NIST
Inp	638.00		NIST
Inp	632.00		NIST
I	[829.00; 915.00]
I	868.00		NIST
I	895.00		NIST
I	888.00		NIST
I	907.00		NIST
I	915.00		NIST
I	900.00		NIST
I	903.00		NIST
I	868.00		NIST
I	861.00		NIST
I	866.00		NIST
I	867.00		NIST
I	854.00		NIST
I	857.00		NIST
I	887.00		NIST
I	829.00		NIST
I	854.00		NIST
I	898.00		NIST
I	872.00		NIST
I	868.00		NIST
I	900.00		NIST
I	829.00		NIST
S°gas	301.70 ± 1.70	J/mol×K	NIST
S°liquid	[203.80; 203.90]	J/mol×K
S°liquid	203.80	J/mol×K	NIST
S°liquid	203.90	J/mol×K	NIST
S°liquid	203.90	J/mol×K	NIST
Tboil	[330.15; 340.20]	K
Tboil	339.12	K	Study o...
Tboil	338.65	K	Measure...
Tboil	339.12	K	Isobari...
Tboil	339.20	K	Experim...
Tboil	338.90	K	NIST
Tboil	339.15 ± 0.10	K	NIST
Tboil	339.05 ± 0.30	K	NIST
Tboil	339.20 ± 0.50	K	NIST
Tboil	340.20	K	NIST
Tboil	339.10	K	NIST
Tboil	338.90 ± 0.15	K	NIST
Tboil	339.35 ± 0.50	K	NIST
Tboil	337.90 ± 0.50	K	NIST
Tboil	339.00 ± 2.00	K	NIST
Tboil	340.00 ± 2.00	K	NIST
Tboil	339.10 ± 0.20	K	NIST
Tboil	339.65 ± 0.30	K	NIST
Tboil	337.65 ± 2.00	K	NIST
Tboil	337.65 ± 2.00	K	NIST
Tboil	Outlier 330.15 ± 2.00	K	NIST
Tboil	340.15 ± 2.00	K	NIST
Tc	[540.10; 541.00]	K
Tc	540.20	K	NIST
Tc	540.10 ± 0.30	K	NIST
Tc	541.00 ± 1.50	K	NIST
Tfus	[164.05; 165.10]	K
Tfus	165.10 ± 0.50	K	NIST
Tfus	164.15 ± 1.00	K	NIST
Tfus	164.63 ± 0.20	K	NIST
Tfus	164.05 ± 0.40	K	NIST
Ttriple	[164.76; 164.76]	K
Ttriple	164.76 ± 0.05	K	NIST
Ttriple	164.76 ± 0.02	K	NIST
Ttriple	164.76 ± 0.02	K	NIST
Vc	0.225 ± 0.003	m3/kmol	NIST
Vm	[8.17e-05; 8.17e-05]	m3/mol
Vm	8.17e-05	m3/mol	Excess ...
Vm	8.17e-05	m3/mol	Excess ...

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[85.13; 133.68]	J/mol×K	[328.15; 500.15]
Cp,gas	85.13 ± 0.17	J/mol×K	328.15	NIST
Cp,gas	91.36 ± 0.18	J/mol×K	349.15	NIST
Cp,gas	106.12 ± 0.21	J/mol×K	399.15	NIST
Cp,gas	120.39 ± 0.24	J/mol×K	449.15	NIST
Cp,gas	133.68 ± 0.27	J/mol×K	500.15	NIST
Cp,liquid	[105.50; 136.60]	J/mol×K	[180.15; 325.15]
Cp,liquid	105.50	J/mol×K	180.15	Measure...
Cp,liquid	105.60	J/mol×K	185.15	Measure...
Cp,liquid	105.80	J/mol×K	190.15	Measure...
Cp,liquid	106.00	J/mol×K	195.15	Measure...
Cp,liquid	106.30	J/mol×K	200.15	Measure...
Cp,liquid	106.50	J/mol×K	205.15	Measure...
Cp,liquid	106.70	J/mol×K	210.15	Measure...
Cp,liquid	107.20	J/mol×K	215.15	Measure...
Cp,liquid	107.60	J/mol×K	220.15	Measure...
Cp,liquid	107.90	J/mol×K	225.15	Measure...
Cp,liquid	108.50	J/mol×K	230.15	Measure...
Cp,liquid	109.20	J/mol×K	235.15	Measure...
Cp,liquid	109.80	J/mol×K	240.15	Measure...
Cp,liquid	110.60	J/mol×K	245.15	Measure...
Cp,liquid	111.50	J/mol×K	250.15	Measure...
Cp,liquid	112.40	J/mol×K	255.15	Measure...
Cp,liquid	113.40	J/mol×K	260.15	Measure...
Cp,liquid	114.40	J/mol×K	265.15	Measure...
Cp,liquid	115.50	J/mol×K	270.15	Measure...
Cp,liquid	116.60	J/mol×K	275.15	Measure...
Cp,liquid	117.90	J/mol×K	280.15	Measure...
Cp,liquid	119.20	J/mol×K	285.15	Measure...
Cp,liquid	121.10	J/mol×K	288.15	Thermop...
Cp,liquid	120.30	J/mol×K	290.15	Measure...
Cp,liquid	123.80	J/mol×K	293.15	Thermop...
Cp,liquid	121.70	J/mol×K	295.15	Measure...
Cp,liquid	120.50	J/mol×K	298.00	NIST
Cp,liquid	123.56	J/mol×K	298.15	NIST
Cp,liquid	120.00	J/mol×K	298.15	NIST
Cp,liquid	123.90	J/mol×K	298.15	NIST
Cp,liquid	123.90	J/mol×K	298.15	NIST
Cp,liquid	122.92	J/mol×K	298.15	NIST
Cp,liquid	126.40	J/mol×K	298.15	Thermop...
Cp,liquid	124.10	J/mol×K	298.15	NIST
Cp,liquid	124.10	J/mol×K	298.15	NIST
Cp,liquid	123.10	J/mol×K	300.15	Measure...
Cp,liquid	128.50	J/mol×K	303.15	Thermop...
Cp,liquid	124.50	J/mol×K	305.15	Measure...
Cp,liquid	131.40	J/mol×K	308.15	Thermop...
Cp,liquid	126.00	J/mol×K	310.15	Measure...
Cp,liquid	133.20	J/mol×K	313.15	Thermop...
Cp,liquid	127.30	J/mol×K	315.15	Measure...
Cp,liquid	135.20	J/mol×K	318.15	Thermop...
Cp,liquid	128.80	J/mol×K	320.15	Measure...
Cp,liquid	136.60	J/mol×K	323.15	Thermop...
Cp,liquid	130.50	J/mol×K	325.15	Measure...
η	[0.0003762; 0.0005438]	Pa×s	[283.15; 318.15]
η	0.0005438	Pa×s	283.15	Excess ...
η	0.0005080	Pa×s	288.15	Viscosi...
η	0.0004991	Pa×s	288.15	Excess ...
η	0.0004900	Pa×s	293.00	Ultraso...
η	0.0004700	Pa×s	293.00	Ultraso...
η	0.0004620	Pa×s	298.15	Viscosi...
η	0.0004645	Pa×s	298.15	Excess ...
η	0.0004540	Pa×s	298.15	Excess ...
η	0.0004580	Pa×s	298.15	Ultraso...
η	0.0004630	Pa×s	298.15	Densiti...
η	0.0004631	Pa×s	298.15	Studies...
η	0.0004631	Pa×s	298.15	Densiti...
η	0.0004200	Pa×s	303.00	Ultraso...
η	0.0004276	Pa×s	308.15	Studies...
η	0.0004260	Pa×s	308.15	Viscosi...
η	0.0004277	Pa×s	308.15	Densiti...
η	0.0004125	Pa×s	308.15	Ultraso...
η	0.0004172	Pa×s	308.15	Excess ...
η	0.0003900	Pa×s	313.00	Ultraso...
η	0.0003979	Pa×s	313.15	Densiti...
η	0.0003992	Pa×s	313.15	Excess ...
η	0.0003902	Pa×s	318.15	Densiti...
η	0.0003762	Pa×s	318.15	Ultraso...
η	0.0003903	Pa×s	318.15	Studies...
ΔfusH	[8.54; 8.54]	kJ/mol	[164.76; 164.80]
ΔfusH	8.54	kJ/mol	164.76	NIST
ΔfusH	8.54	kJ/mol	164.76	NIST
ΔfusH	8.54	kJ/mol	164.80	NIST
ΔfusH	8.54	kJ/mol	164.80	NIST
ΔvapH	[29.00; 33.10]	kJ/mol	[287.50; 504.00]
ΔvapH	32.50 ± 0.20	kJ/mol	287.50	NIST
ΔvapH	32.80	kJ/mol	290.50	NIST
ΔvapH	33.00	kJ/mol	293.00	NIST
ΔvapH	31.80	kJ/mol	303.00	NIST
ΔvapH	33.10	kJ/mol	306.00	NIST
ΔvapH	32.30	kJ/mol	314.50	NIST
ΔvapH	30.80	kJ/mol	320.50	NIST
ΔvapH	31.90	kJ/mol	334.50	NIST
ΔvapH	29.81	kJ/mol	339.10	NIST
ΔvapH	29.00	kJ/mol	439.00	NIST
ΔvapH	29.60	kJ/mol	504.00	NIST
ν	[0.0000005; 0.0000006]	m2/s	[283.15; 313.15]
ν	0.0000006	m2/s	283.15	Experim...
ν	0.0000005	m2/s	298.15	Experim...
ν	0.0000005	m2/s	313.15	Experim...
Pvap	[6.59; 101.30]	kPa	[273.60; 338.65]
Pvap	6.59	kPa	273.60	Vapor P...
Pvap	7.10	kPa	275.99	Vapor p...
Pvap	7.56	kPa	276.53	Vapor p...
Pvap	7.84	kPa	277.76	Vapor p...
Pvap	8.33	kPa	278.19	Vapor p...
Pvap	8.38	kPa	278.30	Vapor P...
Pvap	8.61	kPa	279.41	Vapor p...
Pvap	9.04	kPa	279.86	Vapor p...
Pvap	8.93	kPa	280.16	Vapor p...
Pvap	9.96	kPa	281.95	Vapor p...
Pvap	10.55	kPa	283.07	Vapor p...
Pvap	10.32	kPa	283.15	Vapor p...
Pvap	10.73	kPa	283.15	Isother...
Pvap	10.90	kPa	283.36	Vapor p...
Pvap	11.68	kPa	284.88	Vapor p...
Pvap	11.81	kPa	285.02	Vapor P...
Pvap	12.44	kPa	286.55	Vapor p...
Pvap	13.02	kPa	286.97	Vapor P...
Pvap	13.67	kPa	288.15	Isother...
Pvap	13.79	kPa	288.50	Vapor p...
Pvap	14.00	kPa	289.00	Vapor p...
Pvap	14.48	kPa	289.66	Vapor p...
Pvap	14.89	kPa	289.75	Vapor P...
Pvap	15.65	kPa	291.04	Vapor p...
Pvap	16.65	kPa	292.31	Vapor p...
Pvap	17.00	kPa	292.65	Vapor P...
Pvap	17.25	kPa	293.15	Isother...
Pvap	17.43	kPa	293.30	Vapor p...
Pvap	19.72	kPa	296.05	Vapor p...
Pvap	20.37	kPa	296.84	Vapor p...
Pvap	20.65	kPa	297.09	Vapor p...
Pvap	21.27	kPa	297.57	Vapor P...
Pvap	21.50	kPa	298.15	Vapor p...
Pvap	21.61	kPa	298.15	Isother...
Pvap	21.60	kPa	298.15	Isother...
Pvap	21.61	kPa	298.15	Isother...
Pvap	22.24	kPa	298.72	Vapor p...
Pvap	23.84	kPa	300.57	Vapor p...
Pvap	25.28	kPa	301.73	Vapor p...
Pvap	26.67	kPa	302.75	Vapor P...
Pvap	26.62	kPa	302.96	Vapor p...
Pvap	26.67	kPa	303.04	Double ...
Pvap	26.68	kPa	303.05	Double ...
Pvap	26.81	kPa	303.15	Isother...
Pvap	26.87	kPa	303.23	Vapor p...
Pvap	27.79	kPa	304.04	Vapor p...
Pvap	29.09	kPa	305.11	Double ...
Pvap	29.43	kPa	305.35	Vapor p...
Pvap	30.77	kPa	306.54	Vapor p...
Pvap	32.88	kPa	307.83	Vapor P...
Pvap	32.49	kPa	308.07	Vapor p...
Pvap	32.94	kPa	308.15	Isother...
Pvap	34.50	kPa	309.28	Double ...
Pvap	35.55	kPa	310.20	Vapor p...
Pvap	36.65	kPa	310.86	Vapor p...
Pvap	38.54	kPa	311.90	Vapor p...
Pvap	40.15	kPa	313.11	Double ...
Pvap	40.13	kPa	313.12	Vapor p...
Pvap	40.21	kPa	313.15	Isother...
Pvap	40.62	kPa	313.15	Isother...
Pvap	40.09	kPa	313.18	Vapor p...
Pvap	44.65	kPa	315.86	Vapor p...
Pvap	45.51	kPa	316.36	Double ...
Pvap	47.86	kPa	317.71	Vapor p...
Pvap	48.62	kPa	318.10	Double ...
Pvap	48.68	kPa	318.15	Isother...
Pvap	51.31	kPa	319.58	Vapor p...
Pvap	55.34	kPa	321.57	Vapor p...
Pvap	58.54	kPa	323.15	Isother...
Pvap	59.46	kPa	323.59	Vapor p...
Pvap	70.61	kPa	328.15	Isother...
Pvap	70.61	kPa	328.15	Isother...
Pvap	101.30	kPa	338.65	Measure...
n0	[1.39510; 1.40940]		[288.15; 318.15]
n0	1.40940		288.15	Refract...
n0	1.40720		293.15	Bubble-...
n0	1.40700		293.15	Refract...
n0	1.40500		293.15	Solubil...
n0	1.40480		298.15	To the ...
n0	1.40460		298.15	Refract...
n0	1.40490		298.15	Density...
n0	1.40520		298.15	Acousti...
n0	1.40500		298.15	Viscosi...
n0	1.40470		298.15	Solubil...
n0	1.40610		298.15	Vapor L...
n0	1.40720		298.15	Bubble ...
n0	1.40480		303.15	Thermod...
n0	1.40260		303.15	Density...
n0	1.40280		303.15	Densiti...
n0	1.40230		303.15	Refract...
n0	1.39980		308.15	Density...
n0	1.39990		308.15	Refract...
n0	1.39750		313.15	Refract...
n0	1.39510		318.15	Refract...
ρl	[854.56; 903.71]	kg/m3	[278.15; 323.15]
ρl	903.71	kg/m3	278.15	Phenome...
ρl	892.94	kg/m3	288.15	Phenome...
ρl	893.29	kg/m3	288.15	Volumet...
ρl	892.86	kg/m3	288.15	Volumet...
ρl	888.69	kg/m3	293.15	Experim...
ρl	887.87	kg/m3	293.15	Volumet...
ρl	887.01	kg/m3	293.15	Tempera...
ρl	888.77	kg/m3	293.15	Investi...
ρl	888.73	kg/m3	293.15	Volumet...
ρl	887.52	kg/m3	293.15	Volumet...
ρl	887.41	kg/m3	293.15	Volumet...
ρl	882.00	kg/m3	298.00	Densiti...
ρl	882.09	kg/m3	298.15	Excess ...
ρl	882.01	kg/m3	298.15	Standar...
ρl	882.09	kg/m3	298.15	Excess ...
ρl	882.09	kg/m3	298.15	Excess ...
ρl	882.06	kg/m3	298.15	Excess ...
ρl	882.10	kg/m3	298.15	Study o...
ρl	884.99	kg/m3	298.15	Quatern...
ρl	881.98	kg/m3	298.15	Volumet...
ρl	882.04	kg/m3	298.15	Volumet...
ρl	882.09	kg/m3	298.15	Excess ...
ρl	881.95	kg/m3	298.15	Surface...
ρl	882.08	kg/m3	298.15	Excess ...
ρl	882.04	kg/m3	298.15	Phenome...
ρl	881.50	kg/m3	298.15	Densiti...
ρl	882.40	kg/m3	298.15	Volumet...
ρl	882.00	kg/m3	298.15	Vapour ...
ρl	883.24	kg/m3	298.15	Volumet...
ρl	883.30	kg/m3	298.15	Investi...
ρl	882.21	kg/m3	298.15	Experim...
ρl	882.00	kg/m3	298.15	Volumet...
ρl	882.15	kg/m3	298.15	Densiti...
ρl	882.21	kg/m3	298.15	Experim...
ρl	882.00	kg/m3	298.15	Volumet...
ρl	882.05	kg/m3	298.15	Tempera...
ρl	878.00	kg/m3	303.00	Densiti...
ρl	876.47	kg/m3	303.13	Volumet...
ρl	877.81	kg/m3	303.15	Investi...
ρl	878.70	kg/m3	303.15	Densiti...
ρl	876.91	kg/m3	303.15	Volumet...
ρl	876.54	kg/m3	303.15	Volumet...
ρl	876.50	kg/m3	303.15	Unravel...
ρl	877.70	kg/m3	303.15	Experim...
ρl	877.60	kg/m3	303.15	Volumet...
ρl	877.10	kg/m3	303.15	Tempera...
ρl	874.00	kg/m3	308.00	Densiti...
ρl	870.96	kg/m3	308.15	Volumet...
ρl	871.38	kg/m3	308.15	Volumet...
ρl	871.16	kg/m3	308.15	Experim...
ρl	872.02	kg/m3	308.15	Volumet...
ρl	873.00	kg/m3	308.15	Densiti...
ρl	872.28	kg/m3	308.15	Investi...
ρl	872.16	kg/m3	308.15	Experim...
ρl	872.14	kg/m3	308.15	Tempera...
ρl	871.01	kg/m3	308.15	Phenome...
ρl	866.90	kg/m3	313.15	Densiti...
ρl	867.19	kg/m3	313.15	Tempera...
ρl	866.58	kg/m3	313.15	Experim...
ρl	866.71	kg/m3	313.15	Investi...
ρl	865.82	kg/m3	313.15	Volumet...
ρl	866.23	kg/m3	313.15	Volumet...
ρl	860.96	kg/m3	318.15	Experim...
ρl	862.23	kg/m3	318.15	Tempera...
ρl	861.11	kg/m3	318.15	Investi...
ρl	859.84	kg/m3	318.15	Phenome...
ρl	859.96	kg/m3	318.15	Experim...
ρl	860.21	kg/m3	318.15	Volumet...
ρl	855.29	kg/m3	323.15	Experim...
ρl	854.56	kg/m3	323.15	Volumet...
ρl	855.46	kg/m3	323.15	Investi...
ΔfusS	[51.80; 51.83]	J/mol×K	[164.76; 164.76]
ΔfusS	51.80	J/mol×K	164.76	NIST
ΔfusS	51.83	J/mol×K	164.76	NIST
csound,fluid	[1165.00; 1374.98]	m/s	[278.15; 323.15]
csound,fluid	1374.98	m/s	278.15	Ultraso...
csound,fluid	1325.78	m/s	288.15	Ultraso...
csound,fluid	1277.37	m/s	298.15	Ultraso...
csound,fluid	1280.20	m/s	298.15	Compres...
csound,fluid	1254.00	m/s	303.15	Thermod...
csound,fluid	1254.00	m/s	303.15	Thermod...
csound,fluid	1254.00	m/s	303.15	Thermod...
csound,fluid	1256.00	m/s	303.15	Thermod...
csound,fluid	1229.61	m/s	308.15	Ultraso...
csound,fluid	1207.00	m/s	313.15	Thermod...
csound,fluid	1207.00	m/s	313.15	Thermod...
csound,fluid	1212.00	m/s	313.15	Thermod...
csound,fluid	1207.00	m/s	313.15	Thermod...
csound,fluid	1182.37	m/s	318.15	Ultraso...
csound,fluid	1165.00	m/s	323.15	Thermod...
csound,fluid	1165.00	m/s	323.15	Thermod...
csound,fluid	1171.00	m/s	323.15	Thermod...
csound,fluid	1165.00	m/s	323.15	Thermod...
γ	[0.03; 0.03]	N/m	[288.15; 308.15]
γ	0.03	N/m	288.15	Densiti...
γ	0.03	N/m	293.15	Thermod...
γ	0.03	N/m	293.15	Surface...
γ	0.03	N/m	298.15	Thermod...
γ	0.03	N/m	298.15	Densiti...
γ	0.03	N/m	298.15	Surface...
γ	0.03	N/m	303.13	Surface...
γ	0.03	N/m	303.15	Thermod...
γ	0.03	N/m	308.15	Surface...
γ	0.03	N/m	308.15	Thermod...
γ	0.03	N/m	308.15	Densiti...

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil	339.15	K	96.60	Low cos...

Datasets

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

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
333.20	10200.00	0.0004
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.15	101.33	0.0003
Reference

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
85.90	298.15	882.02
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.27e-04; 5170.61]	kPa	[164.65; 540.15]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			7.83577e+01
Coefficient B			-6.33998e+03
Coefficient C			-9.60880e+00
Coefficient D			8.18348e-06
Temperature range, min.			164.65
Temperature range, max.			540.15
Pvap	1.27e-04	kPa	164.65	Calculated Property
Pvap	0.04	kPa	206.37	Calculated Property
Pvap	1.38	kPa	248.09	Calculated Property
Pvap	14.80	kPa	289.82	Calculated Property
Pvap	78.83	kPa	331.54	Calculated Property
Pvap	272.18	kPa	373.26	Calculated Property
Pvap	709.91	kPa	414.98	Calculated Property
Pvap	1537.51	kPa	456.71	Calculated Property
Pvap	2939.69	kPa	498.43	Calculated Property
Pvap	5170.61	kPa	540.15	Calculated Property

Similar Compounds

Find more compounds similar to Tetrahydrofuran.

Mixtures

• Butane, 1-chloro- + Tetrahydrofuran
• Butane, 2-chloro- + Tetrahydrofuran
• Propane, 1-chloro-2-methyl- + Tetrahydrofuran
• Propane, 2-chloro-2-methyl- + Tetrahydrofuran
• Carbon dioxide + Tetrahydrofuran
• Propylene Carbonate + Tetrahydrofuran
• Decane + Tetrahydrofuran
• 2-Pyrrolidinone, 1-methyl- + Tetrahydrofuran
• 1-Propanol + Tetrahydrofuran
• Isopropyl Alcohol + Tetrahydrofuran
• Pentane, 1-chloro- + Tetrahydrofuran
• Hexane, 1-chloro- + Tetrahydrofuran
• Benzene + Tetrahydrofuran
• Toluene + Tetrahydrofuran
• o-Xylene + Tetrahydrofuran
• Benzene, 1,3-dimethyl- + Tetrahydrofuran
• p-Xylene + Tetrahydrofuran
• Tetrahydrofuran + Mesitylene
• n-Propyl chloride + Tetrahydrofuran
• Trichloromethane + Tetrahydrofuran

Find more mixtures with Tetrahydrofuran.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Surface Tension of Mixtures of Tetrahydrofuran or Tetrahydropyran with Isomeric Chlorobutanes
• Volumetric Properties of the Ionic Liquid, 1-Butyl-3-methylimidazolium Tetrafluoroborate, in Organic Solvents at T = 298.15 K
• A Digital Variable-Angle Rolling-Ball Viscometer for Measurement of Viscosity, Density, and Bubble-Point Pressure of CO2 and Organic Liquid Mixtures
• Viscosity Behavior of Some Oxygen Containing Compounds
• Bubble temperature measurements on the binary mixtures formed by decane with a variety of compounds at 95.8 kPa
• (Solid + liquid) phase equilibria of binary mixtures containing N-methyl-2-pyrrolidinone and ethers at atmospheric pressure
• Measurement and correlation of vapor liquid equilibria of binary systems containing the ionic liquids [EMIM][(CF3SO2)2N], [BMIM][(CF3SO2)2N], [MMIM][(CH3)2PO4] and oxygenated organic compounds respectively water
• Ultrasonic velocity, viscosity and excess properties of binary mixture of tetrahydrofuran with 1-propanol and 2-propanol
• Excess molar volume and viscosity study for the ternary system tetrahydrofuran (1) + 1-chlorobutane (2) + 2-butanol (3) at 283.15, 298.15 and 313.15 K
• Measurement of heat capacities of ionic liquids by differential scanning calorimetry
• Isothermal vapour-liquid equilibrium for cyclic ethers with 1-chloropentane
• Liquid liquid equilibria and partitioning in organic aqueous systems
• Vapour liquid equilibrium of cyclic ethers with 1-chlorohexane: Experimental results and UNIFAC predictions
• Ultrasonic and viscometric study of molecular interactions in binary mixtures of aniline with 1-propanol, 2-propanol, 2-methyl-1-propanol, and 2-methyl-2-propanol at different temperatures
• Temperature dependence of limiting activity coefficients and Henry s law constants of cyclic and open-chain ethers in water
• Study of isobaric vapour liquid equilibrium of some cyclic ethers with 1-chloropropane: Experimental results and SAFT-VR modelling
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
• Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
• Phase equilibrium and thermophysical properties of mixtures containing a cyclic ether and 1-chloropropane
• High-pressure vapor-liquid equilibria for carbon dioxide + tetrahydrofuran mixtures
• Excess Gibbs energies and volumes of the ternary system chloroform + tetrahydrofuran + cyclohexane at 298.15 K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Densities and ultrasonic studies for binary mixtures of tetrahydrofuran with chlorobenzenes, chlorotoluenes and nitrotoluenes at 298.15 K
• Solubility of citric, malonic, and malic acids in different solvents from 303.2 to 333.2 K
• Determination of the solubility, dissolution enthalpy and entropy of pyrene in different solvents
• Conductivity is a contrivance to explore ion-pair and triple-ion structure of ethanoates in tetrahydrofuran, dimethyl sulfoxide and their binaries
• Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
• Determination of the solubility, dissolution enthalpy and entropy of suberic acid in different solvents
• Effect of solvent on the volumetric behavior ofN,N' -salicylidenephenyl diamine (Salophen) Schiff base at differenttemperatures (288.15 - 318.15) K
• Measurement and correlation solubility and mixing properties of dimethyl succinylsuccinate in pure and mixture organic solvents from (278.15 to 333.15) K
• Excess Gibbs energies and volumes of the ternary system ethanol + dimethylformamide + tetrahydrofuran at 298.15K
• Solubility of 1, 3, 2-dioxaphosphorinane-5,5-dimethyl -2- (2,4,6-tribromophenoxy)-2-oxide in selected solvents
• Determination and correlation of solubilities of 1,2-bis(2-oxo-5,5-dimethyl-1,3,2-dioxyphosphacyclohexyl-2-imino) ethane in selected solvents
• Vapor-Liquid Equilibrium for Tetrahydrofuran + Methanol + Tetrafluoroborate-based ionic liquids at 101.3 kPa
• Experiments on the continuous separation of gas mixtures via dissolution and hydrate formation in the presence of THF
• Thermodynamic models for determination of the solubility of 2, 5-bis(2-furylmethylidene) cyclopentan-1-one in different solvents at temperatures ranging from 308.15 to 403.15 K.
• Vapor-liquid equilibria for tetrahydrofuran + ethanol system containing three different ionic liquids at 101.3 kPa
• Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
• Thermostabilities and solubilities of flame retardant bisphenol S-bis (5,5-dimethyl-1,3-dioxaphosphorinanyl-2-oxy phosphate ester) as a function of temperature
• (Liquid + liquid) equilibria in the (water + tetrahydrofuran + methylcyclohexane) ternary system at temperatures between (278 and 343) K and atmospheric pressure: Experimental data and correlation
• Solid-liquid equilibrium of diphenyl anilinophosphonate in the different organic solvents
• Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
• Measurement and correlation of isobaric vapor-liquid equilibria of methanol + tetrahydrofuran + 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide at 101.3 kPa
• Partitioning of diuron in a novel aqueous two-phase system based on polyols and tetrahydrofuran
• Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 K
• Novel phase diagrams of aqueous two-phase systems based on tetrahydrofuran + carbohydrates + water: equilibrium data and partitioning experiments
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• Guaiacol and its mixtures: new data and predictive models Part 2: Gibbs energy of solvation
• Quaternary isothermal vapor-liquid equilibrium of the model biofuel 2-butanone + n-heptane + tetrahydrofuran + cyclohexane using Raman spectroscopic characterization
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
• New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
• Unravelling various types of non-covalent interactions of benzyl amine with ethers in n-hexane at 303.15 K by ultrasonic and DFT methods
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
• Dissolution behavior and thermodynamic properties of lapatinib ditosylate in pure and mixed organic solvents from T = (283.15-323.15) K
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• Salt effect on liquid-liquid equilibria of tetrahydrofuran/water/5-hydroxymethylfurfural systems
• Standard partial molar volumes of some electrolytes in ethylene carbonate based mixtures
• Excess molar enthalpies of the ternary mixtures: {tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether + n-dodecane} at the temperature 298.15 K
• Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
• Tailor-made ionic liquids
• Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
• Phase equilibria for ternary liquid systems of (water + tetrahydrofuran + nonprotic aromatic solvent) at T = 298.2 K
• Excess molar enthalpies of the ternary mixtures: (tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether + n-octane) at the temperature 298.15 K
• Volumetric and compressibility behaviour of ionic liquid, 1-n-butyl-3-methylimidazolium hexafluorophosphate and tetrabutylammonium hexafluorophosphate in organic solvents at T = 298.15 K
• Excess molar enthalpies of the ternary mixtures (1-hexene + tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether) at the temperature 298.15K.
• Isothermal compressibility and internal pressure studies of some non-electrolytes in aqueous solutions at low temperatures
• Apparent molar volumes and apparent molar heat capacities of aqueous tetrahydrofuran, dimethyl sulfoxide, 1,4-dioxane, and 1,2-dimethoxyethane at temperatures from 278.15 K to 393.15 K and at the pressure 0.35 MPa
• Volumetric properties of binary mixtures of ethers and acetonitrile: Experimental results and application of the Prigogine Flory Patterson theory
• Measurement and correlation of solubility of trans-resveratrol in 11 solvents at T = (278.2, 288.2, 298.2, 308.2, and 318.2) K
• Isothermal (vapour + liquid) equilibrium of (cyclic ethers + chlorohexane) mixtures: Experimental results and SAFT modelling
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
• Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
• Volumetric properties of the (tetrahydrofuran + water) and (tetra-n-butyl ammonium bromide + water) systems: Experimental measurements and correlations
• Partial molar volumes of organic solutes in water. XXII. Cyclic ethers at temperatures (298 to 573) K and pressures up to 30 MPa
• Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
• Excess molar volume, viscosity, and refractive index study for the ternary mixture {2-methyl-2-butanol (1) + tetrahydrofuran (2) + propylamine (3)} at different temperatures. Application of the ERAS-model and Peng Robinson Stryjek Vera equation of state
• Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
• Phenomenon of "negative partial molar expansibility" of water in tetrahydrofuran: How plausible is it? Discussion on the paper "Volumetric properties on the (tetrahydrofuran + water) and (tetra-n-butylammonium bromide + water) systems: Experimental measurements and correlations" by Veronica Belandria, Ammir H. Mohammadi and Dominique Richon [J. Chem. Thermodyn. 41 (2009) 1382 1386]
• Excess molar enthalpies of ternary mixtures (1-hexene + tetrahydrofuran + 2,2-dimethylbutane or 2,3-dimethylbutane) at the temperature 298.15 K
• Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
• A volumetric and viscosity study for the binary mixtures of 1-hexyl-3-methylimidazolium tetrafluoroborate with some molecular solvents
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
• Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
• Vapor pressures and activity coefficients of binary mixtures of 1-ethyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide with acetonitrile and tetrahydrofuran
• Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Solubilities of some organic solutes in 1-ethyl-3-methylimidazolium acetate. Chromatographic measurements and predictions from COSMO-RS
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
• The potential of head-space gas chromatography for VLE measurements
• Volumetric properties of binary mixtures of N-ethylformamide with tetrahydrofuran, 2-butanone and ethylacetate from (293.15 to 313.15) K
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
• Measurement and correlation of the solubility of 2,3,4,5-tetrabromothiophene in different solvents
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
• Henry s constants and activity coefficients of some organic solutes in 1-butyl,3-methylimidazolium hydrogen sulfate and in 1-methyl,3-trimethylsilylmethylimidazolium chloride
• Clarification of the volumetric properties of the (tetrahydrofuran + water) systems [J. Chem. Thermodyn. 41 (2009) 1382 1386]: Author s statement
• Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
• On the solubility of nicotinic acid and isonicotinic acid in water and organic solvents
• Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
• Thermodynamic surface properties of [BMIm][NTf2] or [EMIm][NTf2] binary mixtures with tetrahydrofuran, acetonitrile or dimethylsulfoxide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
• Solubility and solution thermodynamics of 2,3,4,5-tetrabromothiophene in (ethanol + tetrahydrofuran) binary solvent mixtures
• Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
• The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
• Densities, speeds of sound and viscosities of binary mixtures of tetrahydrofuran with 1-hexanol, 1-octanol and 1-decanol at T = (298.15 to 313.15) K
• Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
• Experimental and theoretical excess molar properties of imidazolium based ionic liquids with molecular organic solvents I. 1-Hexyl-3- methylimidazlouim tetraflouroborate and 1-octyl-3-methylimidazlouim tetraflouroborate with cyclic ethers
• To the issue of temperature-dependent behavior of standard molar volumes of components in the binary system (water + tetrahydrofuran) at ambient pressure
• Measurement, correlation and dissolution thermodynamics of biological active chalcone in organic solvents at different temperatures
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium methyl sulfate
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• (Liquid + liquid), (solid + liquid), and (solid + liquid + liquid) equilibria of systems containing cyclic ether (tetrahydrofuran or 1,3-dioxolane), water, and a biological buffer MOPS
• Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
• Investigation on thermophysical and excess properties of binary mixtures of imidazolium based ionic liquids at temperatures (293.15 to 323.15) K: III [Cnmim][PF6] (n = 4, 6, 8) + THF
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Solubility of daidzin in different organic solvents and (ethyl alcohol + water) mixed solvents
• Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
• Measurement and correlation of the solubility of genistin in eleven organic solvents from T = (283.2 to 323.2) K
• Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• Measurement and correlation of the solubility of rivaroxaban (form I) in binary mixtures of ethyl acetate with tetrahydrofuran, N,N-dimethylformamide, and N,N-dimethylacetamide from T = (278.15 to 318.15) K
• Thermodynamic models for determination of the solubility of omeprazole in pure and mixture organic solvents from T = (278.15 to 333.15) K
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Thermodynamic models for determination of the solubility of 4-(4-aminophenyl)-3-morpholinone in different pure solvents and (1,4-dioxane + ethyl acetate) binary mixtures with temperatures from (278.15 to 333.15) K
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
• Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-hexyl-2,3-dimethylimidazolium bis(trifluoromethylsulfonyl)imide
• Densities, ultrasonic speeds and refractive indices of phenetole with N-methyl-2-pyrrolidone, N,N-dimethylformamide and tetrahydrofuran binary mixtures at different temperatures
• Determination and correlation thermodynamic models for solid liquid equilibrium of the Nifedipine in pure and mixture organic solvents
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Solubility of oxcarbazepine in eight solvents within the temperature range T = (288.15 308.15) K
• Measurement and correlation of solubility of succinic anhydride in pure solvents and binary solvent mixtures
• Temperature and concentration dependence of volumetric properties of (tetrahydrofuran + methyl acrylate, or + ethyl acrylate, or + n-butyl acrylate, or + tert-butyl acrylate) binary mixtures
• Thermodynamic models for determination of solid liquid equilibrium of the 6-benzyladenine in pure and binary organic solvents
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Thermodynamic models for determination of the solid-liquid equilibrium of istradefylline in ethyl acetate plus (isopropanol, tetrahydrofuran, acetone) binary solvent mixtures
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
• Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
• Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
• Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
• Determination and correlation of solubility and solution thermodynamics of musk xylene in different pure solvents
• Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
• Densities, speeds of sound, isentropic compressibilities, refractive indexes, and viscosities of tetrahydrofuran with haloalkane or alkyl ethanoate at T = 303.15 K
• Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
• Experimental and predicted viscosities of binary mixtures of cyclic ethers with 1-chloropentane or 1-chlorohexane at 283.15, 298.15, and 313.15K
• Studies of viscosities of dilute solutions of alkylamines in non-electrolyte solvents: IV. Alkylamines in 1,4-dioxane and oxolane at 303.15K
• Thermodynamic and acoustic properties of binary mixtures of oxolane with aniline and substituted anilines at 303.15, 313.15 and 323.15 K
• Thermodynamic and acoustic properties of binary mixtures of ethers. III. Diisopropyl ether or oxolane with o- or m-toluidines at 303.15, 313.15 and 323.15 K
• Thermodynamic and acoustic properties of binary mixtures of ethers. IV. Diisopropyl ether or oxolane with N,N-dimethylaniline or N,Ndiethylaniline at 303.15, 313.15 and 323.15 K
• Thermodynamic and acoustic properties of binary mixtures of ethers. V. Diisopropyl ether or oxolane with 2- or 3-chloroanilines at 303.15, 313.15 and 323.15 K
• Solubilities of succinimide in different pure solvents and binary methanol+ethyl acetate solvent mixtures
• Thermodynamic properties of betulinic acid in THF + water mixed solvents at different temperatures
• Low cost apparatus for rapid boiling point determination of small air sensitive samples under inert atmosphere
• Solubilities of Phosphoramidic Acid, N-(phenylmethyl)-, Diphenyl Ester in Selected Solvents
• Thermodynamic Models for Determination of the Solubility of Boc-(R)-3-Amino-4-(2, 4, 5-trifluorophenyl)butanoic acid in Different Pure Solvents and (Tetrahydrofuran + n-Butanol) Binary Mixtures with Temperatures from 280.15 to 330.15 K
• Solubility Determination and Modeling of Sodium Mononitrobenzenesulphonate in Different Solvents at Temperatures Ranging from (283.15 to 323.15) K
• Solubility Measurement and Correlation of (+)-Biotin Intermediate Lactone in Different Organic Solvents from (287.15 to 323.75) K
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Solubility of 3,7,9,11-Tetraoxo-2,4,6,8,10-pentaaza[3.3.3] Propellane (TOPAP) in Different Pure Solvents at Temperatures between 273.15 and 318.15 K
• Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
• Solubility and Thermodynamic Behavior of Veramoss in Different Pure Solvents and {Ethanol + Water} Mixtures from T = 283.15 to 333.15 K
• Solubility Measurement and the Correlation of 1-Naphthaleneacetic Acid in Pure and Methanol + Water Binary Solvents from T = (278.25 to 323.55) K
• Solubilities of 4',5,7-Triacetoxyflavanone in Fourteen Organic Solvents at Different Temperatures
• Phase Behavior of Binary Mixtures Containing Succinic Acid or Its Esters
• Solid Liquid Phase Equilibrium of N,N'-Piperazinebis(neopentylglycol)phosphoramidate in Selected Solvents from T = (293.15 to 333.15) K
• Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
• Solid-Liquid Phase Equilibrium and Thermodynamic Properties of Olaparib in Selected Organic Solvents and (Tetrahydrofuran + MTBE, Acetonitrile + Isopropyl Alcohol) Binary Solvent Mixtures
• Isobaric Vapor-Liquid Equilibrium for Binary System of Tetrahydrofuran + 1,4-Butanediol and gamma-Butyrolactone at 50.0 and 70.0 kPa
• Synthesis and Solubility of 5,5-Dimethyl-2-(phenyl(phenylamino)methyl)-1,3,2-dioxaphosphinane 2-oxide in Selected Solvents between 278.15 K and 347.15 K
• Determination and Thermodynamic Analysis of the Solubility of Limonin in Eight Organic Solvents and Ethyl Acetate + 2-Propanol Binary Solvents from 283.2 to 323.2 K
• Solubility Measurement and Thermodynamic Modeling of N-(4-Methylphenyl-Z-3-chloro-2-(phenylthio)propenamide in 12 Pure Solvents at Temperatures Ranging from 278.15 to 318.15 K
• Determination of Activity Coefficients at Infinite Dilution of Organic Solutes in the Ionic Liquid 1-(2-Hydroxyethyl)-3-methylimidazolium Nonafluoro-1-butanesulfonate Using Gas-Liquid Chromatography
• Experimental Determination and Thermodynamic Models for Solid-Liquid Equilibrium of 4-(4-Aminophenoxy)-N-methylpyridine-2-carboxamide in Pure and Binary Solvent Mixtures for T = (278.15-328.15) K
• Measurement and Correlation of the Solubility of 5-Fluorouracil in Pure and Binary Solvents
• Thermodynamic Study of Solubility for Imatinib Mesylate in Nine Monosolvents and Two Binary Solvent Mixtures from 278.15 to 318.15 K
• Solubility Measurements at 296 and 310 K and Physicochemical Characterization of Abiraterone and Abiraterone Acetate
• Measurement and Correlation of the Solubility of Mifepristone in Eight Pure and Water + Methanol Mixed Solvents at Temperatures from 273.15 to 318.15 K
• Solid-Liquid Equilibrium of Azacyclotridecan-2-one in 15 Pure Solvents from T = 273.15 to 323.15 K: Experimental Determination and Thermodynamic Modeling
• Measurement and Correlation of the Solubility of 2-Cyanoacetamide in 14 Pure Solvents and the Mixing Properties of Solutions
• Solubility Measurement, Correlation, and Molecular Interactions of 3-Methyl-6-nitroindazole in Different Neat Solvents and Mixed Solvents from T = 278.15 to 328.15 K
• Solubility Study of (2E)-1-(3-Pyridyl)-3-(dimethylamino)-2-propen-1-one in Different Pure Solvents and Binary Solvent Mixtures from 278.15 to 328.15 K
• Solubility Measurement and Correlation of 2-Oxindole in 12 Pure Organic Solvents
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• Solubility Measurement and Phase Equilibrium Modeling of 2-Aminobenzamide in 15 Pure Solvents
• Determination and Correlation of Solubilities of 1,3,5-Trifluoro-2,4,6-triiodobenzene in Different Solvents from 289.25 to 332.15 K
• Solubility, Solubility Modeling, and Antisolvent Precipitation of 1,3-Bis(9-carbazolyl)benzene in Organic Solvents
• Measurement and Correlation of Solubility of Marbofloxacin in 12 Pure Solvents from 283.15 to 328.15 K
• Solubility Measurement and Modeling of 3-Hydroxy-2-nitropyridine in Ten Pure Solvents and Two Binary Mixed Solvents for T = (278.15-318.15) K
• Measurement and Correlation of the Solubility of Dienogest in Twelve Pure and Water + Methanol Binary Solvents at Temperatures from 273.15 to 318.15 K
• Thermodynamic Properties of Mixtures Containing Precursors of Vitamin B5
• Excess Enthalpies of the Ternary Mixtures: Tetrahydrofuran + (Hexane or Cyclohexane) + Decane at 298.15K
• Vapor-Liquid Equilibria of the Binary Carbon Dioxide-Tetrahydrofuran Mixture System
• Measurement of Activity Coefficients of Solutes at Infinite Dilution in (Dimethyl Sulfoxide + Acetamide, or Formamide, or Urea) Using Gas Liquid Chromatography at the Temperature 298.15 K
• Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
• Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Tri-n-butylamine + Triethylamine, + Tetrahydrofuran, + Tetradecane, + Tetrachloroethylene, + Pyridine, or + Trichloroethylene at (298.15, 303.15, and 308.15) K
• Thermodynamic Properties of Water + Tetrahydrofuran and Water + 1,4-Dioxane Mixtures at (303.15, 313.15, and 323.15) K
• Excess Enthalpy, Excess Volume, Viscosity Deviation, and Speed of Sound Deviation for the Mixture Tetrahydrofuran + 2,2,2-Trifluoroethanol at (283.15, 298.15, and 313.15) K
• Double Azeotropy in Binary Mixtures 1,1,1,2,3,4,4,5,5,5-Decafluoropentane High-Boiling Diastereomer + Tetrahydrofuran
• Solubilities of Bis (2,2,6,6-Tetramethyl-4-Piperidinyl) Maleate in Hexane, Heptane, Octane, m-Xylene and Tetrahydrofuran from (253.15 to 310.15) K
• Influence of Ionic Liquids on the Phase Behavior of Aqueous Azeotropic Systems
• Excess Molar volumes and Surface Tensions of Trimethylbenzene with Tetrahydrofuran Tetrachloromethane and Dimethylsulfoxide at 298.15 K
• Liquid-Liquid Equilibria for the Ternary Systems of (Water + Tetrahydrofuran + Polar Solvent) at 298.15 K
• High-Pressure Vapor-Liquid Equilbria of Some Carbon Dioxide + Organic Binary Systems
• Solubilities of Proxetine Hydrochloride Hemihydrate between 286 K and 363 K
• Study of the Surface Tension of Chlorocyclohexane or Bromocyclohexane with Some Cyclic Ethers
• Solubility of Organic Systems Containing 1,4-Dioxan-2-one
• Densities and Viscosities of the Binary Mixtures of Tetrahydrofuran with Isomeric Chlorobutanes at 298.15 K and 313.15 K
• Compressibility Studies of Binary Solutions Involving Water as a Solute in Nonaqueous Solvents at T ) 298.15 K
• Densities, Viscosities, and Sound Speeds of Some Acetate Salts in Binary Mixtures of Tetrahydrofuran and Methanol at (303.15, 313.15, and 323.15) K
• Studies on Thermodynamic and Transport Properties of Binary Mixtures of Acetonitrile with Some Cyclic Ethers at Different Temperatures by Volumetric, Viscometric, and Interferometric Techniques
• Solubility of 4-(3,4-Dichlorophenyl)-1-tetralone in Some Organic Solvents
• Solubility of 3-Nitrophthalic Acid in Different Solvents between 278 K and 353 K
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
• Solubility of Sulpiride in Pure Organic Solvents between (278 and 333) K
• Volumetric Properties of Binary Mixtures Containing Ionic Liquids and Some Aprotic Solvents
• Solubility of Decabromodiphenyl Ether in Different Solvents at (283.0 to 323.0) K
• Solubilities of Phosphorus-Containing Compounds in Selected Solvents
• Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
• Excess Gibbs Energies of the Ternary System 2-Methoxyethanol + Tetrahydrofuran + Cyclohexane and Other Relevant Binaries at 298.15 K
• Solubilities of N-[(4-Bromo-3,5-difluorine)-phenyl]maleimide in Pyridine, Acetone, Tetrahydrofuran, Ethanol, Trichloromethane, and Acetonitrile at Temperature between (285.00 and 350.15) K
• Solubility of Florfenicol in Different Solvents at Temperatures from (278 to 318) K
• Solubilities of (a,Z)-2-Amino-a-(methoxyimino)-4-thiazoleethanethioic Acid S-2-Benzothiazolyl Ester in Different Pure Solvents and Binary Mixtures of Tetrahydrofuran + Dichloromethane or 1,2-Dichloroethane
• Excess Molar Enthalpies of Dipropyl Ether + Dibutyl Ether + (1-Hexene or Tetrahydrofuran) at 298.15 K
• Solubilities of Phenylphosphinic Acid, Methylphenylphosphinic Acid, Hexachlorocyclotriphosphazene, and Hexaphenoxycyclotriphosphazene in Selected Solvents
• Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
• Surface Tensions and the Gibbs Excess Surface Concentration of Binary Mixtures of the Ionic Liquid 1-Ethyl-3-methylimidazolium Bis[(trifluoromethyl)sulfonyl]imide with Tetrahydrofuran and Acetonitrile
• Solubilities of Tris(o-phenylenedioxy)cyclotriphosphazene in Selected Solvents
• Solubilities of Betulinic Acid in Thirteen Organic Solvents at Different Temperatures
• Ultrasonic and Volumetric Properties of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate Ionic Liquid with 2-Propanol or Tetrahydrofuran at Several Temperatures
• Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
• Antisolvent Precipitation of Vitamin B6: A Thermodynamic Study
• Crystal Structures, Reaction Rates, and Selected Physical Properties of Halo-Boronsubphthalocyanines (Halo = Fluoride, Chloride, and Bromide)
• Biomass-Derived Platform Chemicals: Thermodynamic Studies on the Extraction of 5-Hydroxymethylfurfural from Ionic Liquids
• Liquid Liquid Equilibria for the Ternary Systems of Perfluorohexane or Perfluamine + Hydrofluoroether + Tetrahydrofuran at 298.15 K or 273.15 K
• Thermodynamic and Spectroscopic Study of the Ternary System Dimethyladipate + Tetrahydrofuran +1-Butanol at T = (288.15 to 323.15) K
• Solubilities of Phosphonic Acid, P,P'-(1,4-Piperazinediyl)bis-,P,P,P',P'-tetraphenyl Ester in Selected Solvents
• Vapor Liquid Equilibrium for Ternary and Binary Mixtures of Tetrahydrofuran, Cyclohexane, and 1,2-Propanediol at 101.3 kPa
• Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
• Acoustic and Volumetric Properties of Binary Mixtures of Ionic Liquid 1-Butyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide with Acetonitrile and Tetrahydrofuran
• Thermodynamics of Fluconazole Solubility in Various Solvents at Different Temperatures
• Solid Liquid Phase Equilibria of N,N'-[1,3-Phenylenebis(methylene)]bis(phosphoramidic acid) P,P,P',P'-Tetraphenyl Ester in 10 Pure Solvents
• Determination and Correlation of Solubilities of Lithium Bis(oxalate)borate in Six Different Solvents from (293.15 to 363.15) K
• 4-Amino-3,6-dichloropyridazine Solubility Measurement and Correlation in Seven Pure Organic Solvents from (278.15 to 333.15) K
• Solubility and Thermodynamic Functions of Isatin in Pure Solvents
• Solid Liquid Phase Equilibrium of Phosphoramidic acid, N,N'-1,2-Ethanediylbis-P,P,P',P'-tetraphenyl Ester in Selected Solvents
• Solubility of Phenacetinum in Methanol, Ethanol, 1-Propanol, 1-Butanol, 1-Pentanol, Tetrahydrofuran, Ethyl Acetate, and Benzene between 282.65 K and 333.70 K
• Liquid-Liquid Equilibrium for the Quaternary System Water + Tetrahydrofuran + Toluene + 1-Butanol Mixture at 25 deg C and Atmospheric Pressure
• Solubility of Irbesartan (Form A) in Different Solvents between 278 K and 323 K
• Solubilities of the Gaseous and Liquid Solutes and Their Thermodynamics of Solubilization in the Novel Room-Temperature Ionic Liquids at Infinite Dilution by Gas Chromatography
• Viscosity, Density, Speed of Sound, and Refractive Index of Binary Mixtures of Organic Solvent + Ionic Liquid, 1-Butyl-3-methylimidazolium Hexafluorophosphate at 298.15 K
• Solubility of 2-(4-Ethylbenzoyl)benzoic Acid in Eleven Organic Solvents between 279.55 K and 343.15 K
• Ion-Pair and Triple-Ion Formation by Some Tetraalkylammonium Iodides in Binary Mixtures of 1,4-Dioxane + Tetrahydrofuran
• Solubility of Trimethoprim (TMP) in Different Organic Solvents from (278 to 333) K
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas Liquid Chromatography
• Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
• Phase Equilibria of (1-Ethyl-3-methylimidazolium Ethylsulfate + Hydrocarbon, + Ketone, and + Ether) Binary Systems
• Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary and Ternary Mixtures of Tetrahydofuran, 2-Propanol, and 2,2,4-Trimethylpentane
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas Liquid Chromatography
• solubility of L-(+)-ascorbic acid in water, ethanol, methanol, propan-2-ol, acetone, acetonitrile, ethyl acetate, and tetrahydrofuran from (293 to 323) K
• Experimental Isobaric Vapor-Liquid Equilibrium Data for Binary Mixtures of Cyclic Ethers with (1-Methylethyl)benzene
• Solubility of Carbamazepine (Form III) in Different Solvents from (275 to 343) K
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Solubility of Methane in Tetrahydrofuran + Ethanol at High Pressures
• Solubility of Naphthalene in Isobutyl Acetate, n-Butyric Acid, Ethyl Acetate, N-Methyl Pyrrolidone, N,N-Dimethylformamide, and Tetrahydrofuran
• Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water)
• Solubility of Chloroquine Diphosphate and 4,7-Dichloroquinoline in Water, Ethanol, Tetrahydrofuran, Acetonitrile, and Acetone from (298.2 to 333.2) K
• Solubilities of Terephthalic Acid, Phthalic Acid, and Isophthalic Acid in Tetrahydrofuran, Cyclohexanone, 1,2-Diethoxyethane, and Acetophenone
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Excess Enthalpies of Dibromomethane with Acetone, 1,4-Dioxane, Pyridine, Diethyl Ether, Ethyl Methyl Ketone, and Tetrahydrofuran at 303.15 K
• Measurement and Correlation of Solubility of Pimelic Acid in Ether, Tetrahydrofuran, Ethanol, and Methanol
• Solubility of 5-Amino Salicylic Acid in Different Solvents at Various Temperatures
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
• Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
• Joback Method
• KDB
• Estimated Solubility Method
• McGowan Method
• NIST Webbook

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