Chemical Properties of n-Hexane (CAS 110-54-3)

InChI

InChI=1S/C6H14/c1-3-5-6-4-2/h3-6H2,1-2H3

InChI Key

VLKZOEOYAKHREP-UHFFFAOYSA-N

Formula

C6H14

SMILES

CCCCCC

Molecular Weight¹

86.18

CAS

110-54-3

Other Names

• Esani
• Gettysolve-B
• Heksan
• Hexanen
• Hexyl hydride
• NCI-C60571
• NSC 68472
• Skellysolve B
• hexane
• n-C6H14

• ω : Acentric Factor.
• T_ig : Autoignition Temperature (K).
• AP : Aniline Point (K).
• 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).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• ε_r : Dielectric Constant (Relative permittivity).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_c,grossH : Heat of Combustion, Gross form (kJ/mol).
• Δ_c,netH : Heat of Combustion, Net Form (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_subH : Enthalpy of sublimation 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).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• 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(P) : Boiling point at given pressure (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• V_COSTALD : COSTALD Characteristic Volume (m³/kmol).
• ω_SRK : SRK acentric factor.
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

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

Physical Properties

Property	Value	Unit	Source
ω	[0.2957; 0.2990]
ω	0.2975		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2957		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.2970		ChemSep v8.3 pure component data Compiled value
ω	0.2990		KDB
Tig	[496.15; 498.15]	K
Tig	498.15	K	KDB
Tig	496.15	K	NCMS SOLV-DB
AP	341.750	K	KDB
ΔcH°liquid	[-4175.00; -4147.00]	kJ/mol
ΔcH°liquid	-4163.20 ± 0.54	kJ/mol	NIST
ΔcH°liquid	-4163.10 ± 0.71	kJ/mol	NIST
ΔcH°liquid	-4163.00 ± 0.84	kJ/mol	NIST
ΔcH°liquid	-4163.70 ± 1.40	kJ/mol	NIST
ΔcH°liquid	-4147.00	kJ/mol	NIST
ΔcH°liquid	-4175.00	kJ/mol	NIST
μ	[0.00; 0.00]	debye
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
μ	0.00	debye	KDB
η	[0.0003130; 0.0003130]	Pa×s
η	0.0003130	Pa×s	Study of densities, viscosities, and speeds of sound of binary liquid mixtures of butan-1-ol with n-alkanes (C6, C8, and C10) at T = (298.15, 303.15, and 308.15) K
η	0.0003130	Pa×s	Study of molecular interactions in binary liquid mixtures of 1-octanol with n-hexane, n-octane, and n-decane using volumetric, viscometric, and acoustic properties
η	0.0003130	Pa×s	Thermophysical Properties of Binary Mixtures of 2-Methyl-1-propanol with Hexane, Octane, and Decane at 298.15 K
εr	1.88		NCMS SOLV-DB
LFL	1.20	% in Air	KDB
UFL	7.70	% in Air	KDB
Tflash,cc	247.15	K	NCMS SOLV-DB
Tflash,oc	251.48	K	KDB
ΔfG°	[-0.17; -0.07]	kJ/mol
ΔfG°	-0.07	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	-0.17	kJ/mol	KDB
Rg	3.8120		KDB
Δc,grossH	4163.12	kJ/mol	KDB
Δc,netH	3855.012	kJ/mol	KDB
ΔfH°gas	[-167.30; -166.94]	kJ/mol
ΔfH°gas	-166.94 ± 0.48	kJ/mol	Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas	-166.94	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-167.30	kJ/mol	KDB
ΔfH°gas	-167.10	kJ/mol	NIST
ΔfH°gas	-167.20 ± 0.79	kJ/mol	NIST
ΔfH°liquid	[-198.80; -198.70]	kJ/mol
ΔfH°liquid	-198.70 ± 0.67	kJ/mol	NIST
ΔfH°liquid	-198.80 ± 0.79	kJ/mol	NIST
ΔfusH°	11.30	kJ/mol	Joback Calculated Property
ΔvapH°	[30.00; 32.10]	kJ/mol
ΔvapH°	31.55	kJ/mol	NCMS SOLV-DB
ΔvapH°	31.73	kJ/mol	NIST
ΔvapH°	31.40 ± 0.20	kJ/mol	NIST
ΔvapH°	31.50 ± 0.10	kJ/mol	NIST
ΔvapH°	31.50	kJ/mol	NIST
ΔvapH°	32.10	kJ/mol	NIST
ΔvapH°	31.60 ± 0.10	kJ/mol	NIST
ΔvapH°	31.55	kJ/mol	NIST
ΔvapH°	Outlier 30.00	kJ/mol	NIST
ΔvapH°	31.50 ± 0.10	kJ/mol	NIST
ΔvapH°	31.54	kJ/mol	NIST
ΔvapH°	31.00 ± 0.20	kJ/mol	NIST
IE	[9.97; 10.29]	eV
IE	10.13 ± 0.10	eV	NIST
IE	10.29	eV	NIST
IE	9.97	eV	NIST
IE	10.13 ± 0.10	eV	NIST
IE	10.03 ± 0.15	eV	NIST
IE	10.16	eV	NIST
IE	10.22	eV	NIST
IE	10.27	eV	NIST
IE	10.18	eV	NIST
log10WS	[-3.84; -3.84]
log10WS	-3.84		Aq. Solubility Prediction
log10WS	-3.84		Estimated Solubility
logPoct/wat	3.900		NCMS SOLV-DB
McVol	95.400	ml/mol	McGowan Calculated Property
NFPA Fire	[%!d(float64=3); %!d(float64=3)]
NFPA Fire	3		KDB
NFPA Fire	3		NCMS SOLV-DB
NFPA Health	[%!d(float64=1); %!d(float64=1)]
NFPA Health	1		KDB
NFPA Health	1		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	[2940.00; 3058.00]	kPa
Pc	3020.00	kPa	Critical Properties of Binary and Ternary Mixtures of Hexane + Methanol, Hexane + Carbon Dioxide, Methanol + Carbon Dioxide and Hexane + Carbon Dioxide + Methanol
Pc	3025.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Pc	3014.42	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3012.32	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	3025.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3025.00	kPa	KDB
Pc	3030.00 ± 20.00	kPa	NIST
Pc	2990.00 ± 40.00	kPa	NIST
Pc	2980.00 ± 50.00	kPa	NIST
Pc	2990.00 ± 10.00	kPa	NIST
Pc	3014.00 ± 20.00	kPa	NIST
Pc	3012.00	kPa	NIST
Pc	3025.00 ± 5.00	kPa	NIST
Pc	3036.00 ± 30.00	kPa	NIST
Pc	3036.00 ± 100.00	kPa	NIST
Pc	3051.00 ± 50.00	kPa	NIST
Pc	3058.00 ± 50.00	kPa	NIST
Pc	3031.62 ± 8.00	kPa	NIST
Pc	3034.81 ± 3.44	kPa	NIST
Pc	3048.00 ± 3.00	kPa	NIST
Pc	3032.00 ± 3.00	kPa	NIST
Pc	3034.80 ± 3.44	kPa	NIST
Pc	3046.00 ± 6.89	kPa	NIST
Pc	3033.68 ± 20.68	kPa	NIST
Pc	3051.00 ± 3.45	kPa	NIST
Pc	3030.00 ± 50.66	kPa	NIST
Pc	2999.22 ± 151.99	kPa	NIST
Pc	2992.00 ± 55.15	kPa	NIST
Pc	3034.00 ± 5.06	kPa	NIST
Pc	2999.80 ± 33.30	kPa	NIST
Pc	Outlier 2940.00 ± 98.07	kPa	NIST
Ptriple	9.02e-04	kPa	ChemSep v8.3 pure component data Compiled value
ρc	[231.81; 235.26]	kg/m3
ρc	234.40 ± 1.72	kg/m3	NIST
ρc	231.81 ± 10.34	kg/m3	NIST
ρc	232.67 ± 6.03	kg/m3	NIST
ρc	232.67	kg/m3	NIST
ρc	233.62 ± 4.31	kg/m3	NIST
ρc	233.62 ± 2.59	kg/m3	NIST
ρc	235.26 ± 4.31	kg/m3	NIST
ρc	232.67 ± 1.72	kg/m3	NIST
ρc	232.67 ± 1.72	kg/m3	NIST
ρc	234.40 ± 6.03	kg/m3	NIST
S°gas	388.82 ± 0.84	J/mol×K	NIST
S°liquid	[289.50; 297.50]	J/mol×K
S°liquid	296.06	J/mol×K	NIST
S°liquid	289.50	J/mol×K	NIST
S°liquid	295.40	J/mol×K	NIST
S°liquid	297.50	J/mol×K	NIST
Tboil	[340.75; 371.80]	K
Tboil	341.79	K	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Tboil	341.79	K	Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
Tboil	341.80	K	Excess molar volumes of the ternary system {methylcyclohexane (1) + cyclohexane (2) + n-alkanes (3)} at T = 298.15 K
Tboil	341.86	K	Vapour pressures of n-hexane determined by comparative ebulliometry
Tboil	341.85	K	Excess volumes, densities, speeds of sound and viscosities for the binary systems of diisopropyl ether with hydrocarbons at 303.15K
Tboil	341.88	K	Isobaric Vapor-Liquid Equilibrium Data for Two Binary Systems n-Hexane + 1,2-Dimethoxyethane and Methylcyclopentane + 1,2-Dimethoxyethane at 101.3 kPa
Tboil	341.93	K	Densities and Excess Molar Properties of Dimethyl Carbonate with Alkanes (C6 to C10) and VLE of Dimethyl Carbonate with Alkanes (C9 to C10) at 101.3 kPa
Tboil	341.85	K	Vapor-Liquid Equilibrium of Ferrocene in Some Organic Solvents Using Spectroscopic Methods
Tboil	341.76	K	Isobaric Vapor-Liquid Equilibrium Data and Excess Properties of Binary Systems Comprised of Alkyl Methanoates + Hexane
Tboil	341.88	K	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Tboil	341.94	K	Vapor Liquid Equilibrium, Densities, and Interfacial Tensions of the System Hexane + 2,5-Dimethylfuran
Tboil	341.88	K	ChemSep v8.3 pure component data Compiled value
Tboil	341.88	K	KDB
Tboil	341.89	K	NCMS SOLV-DB
Tboil	341.90 ± 0.30	K	NIST
Tboil	341.95 ± 0.10	K	NIST
Tboil	341.85 ± 0.30	K	NIST
Tboil	341.91 ± 0.20	K	NIST
Tboil	341.60 ± 0.30	K	NIST
Tboil	342.25 ± 0.50	K	NIST
Tboil	341.90	K	NIST
Tboil	341.45 ± 0.50	K	NIST
Tboil	341.90	K	NIST
Tboil	341.85 ± 0.50	K	NIST
Tboil	341.90 ± 0.40	K	NIST
Tboil	341.85 ± 0.30	K	NIST
Tboil	341.85 ± 0.30	K	NIST
Tboil	341.89 ± 0.10	K	NIST
Tboil	341.91 ± 0.15	K	NIST
Tboil	341.95 ± 0.20	K	NIST
Tboil	341.75 ± 0.20	K	NIST
Tboil	340.80 ± 0.30	K	NIST
Tboil	341.35 ± 0.40	K	NIST
Tboil	341.85 ± 0.30	K	NIST
Tboil	341.90 ± 0.50	K	NIST
Tboil	341.93 ± 0.30	K	NIST
Tboil	341.90 ± 0.30	K	NIST
Tboil	341.85 ± 0.20	K	NIST
Tboil	340.90 ± 0.20	K	NIST
Tboil	341.86 ± 0.15	K	NIST
Tboil	341.90 ± 0.20	K	NIST
Tboil	341.90 ± 0.30	K	NIST
Tboil	342.00 ± 0.30	K	NIST
Tboil	341.85 ± 0.30	K	NIST
Tboil	341.85 ± 0.30	K	NIST
Tboil	341.85 ± 0.30	K	NIST
Tboil	342.90 ± 0.60	K	NIST
Tboil	341.92 ± 0.10	K	NIST
Tboil	341.80 ± 0.30	K	NIST
Tboil	342.00 ± 0.40	K	NIST
Tboil	341.87 ± 0.38	K	NIST
Tboil	340.85 ± 0.50	K	NIST
Tboil	341.80 ± 0.10	K	NIST
Tboil	341.92 ± 0.10	K	NIST
Tboil	Outlier 371.80 ± 0.20	K	NIST
Tboil	341.97 ± 0.15	K	NIST
Tboil	341.95 ± 0.30	K	NIST
Tboil	342.70 ± 0.30	K	NIST
Tboil	341.83 ± 0.15	K	NIST
Tboil	341.90 ± 0.20	K	NIST
Tboil	342.00 ± 0.30	K	NIST
Tboil	340.75 ± 2.00	K	NIST
Tboil	342.15 ± 1.50	K	NIST
Tboil	341.85 ± 0.30	K	NIST
Tboil	341.80 ± 0.40	K	NIST
Tboil	341.83 ± 0.20	K	NIST
Tboil	341.89 ± 0.01	K	NIST
Tboil	341.85 ± 0.07	K	NIST
Tboil	341.85 ± 0.30	K	NIST
Tboil	341.85 ± 0.50	K	NIST
Tboil	341.89 ± 0.05	K	NIST
Tboil	341.90 ± 0.10	K	NIST
Tboil	341.85 ± 1.00	K	NIST
Tboil	341.85 ± 0.20	K	NIST
Tboil	341.75 ± 0.70	K	NIST
Tboil	341.55 ± 0.80	K	NIST
Tboil	341.55 ± 0.40	K	NIST
Tboil	341.80 ± 0.20	K	NIST
Tboil	341.87 ± 0.20	K	NIST
Tboil	341.87 ± 0.20	K	NIST
Tboil	341.00 ± 2.00	K	NIST
Tboil	341.90 ± 0.20	K	NIST
Tboil	341.88 ± 0.05	K	NIST
Tboil	341.95 ± 0.20	K	NIST
Tboil	341.78 ± 0.15	K	NIST
Tboil	341.91 ± 0.10	K	NIST
Tboil	341.88 ± 0.05	K	NIST
Tboil	341.81 ± 0.07	K	NIST
Tboil	341.85 ± 0.50	K	NIST
Tboil	342.65 ± 0.40	K	NIST
Tboil	342.15 ± 1.00	K	NIST
Tboil	341.85 ± 0.07	K	NIST
Tboil	341.86 ± 0.10	K	NIST
Tboil	342.00 ± 0.30	K	NIST
Tboil	341.95 ± 0.10	K	NIST
Tboil	342.15 ± 0.50	K	NIST
Tboil	341.95 ± 0.15	K	NIST
Tboil	341.65 ± 0.50	K	NIST
Tboil	341.65 ± 0.50	K	NIST
Tboil	341.15 ± 1.00	K	NIST
Tboil	342.15 ± 1.00	K	NIST
Tboil	342.10 ± 0.30	K	NIST
Tboil	342.10 ± 0.50	K	NIST
Tboil	341.00 ± 6.00	K	NIST
Tboil	342.10 ± 0.40	K	NIST
Tboil	341.15 ± 2.00	K	NIST
Tboil	341.90 ± 3.00	K	NIST
Tboil	342.15 ± 2.00	K	NIST
Tboil	342.00 ± 0.20	K	NIST
Tboil	342.00 ± 0.20	K	NIST
Tboil	343.65 ± 1.50	K	NIST
Tboil	341.60 ± 1.00	K	NIST
Tboil	342.00 ± 3.00	K	NIST
Tboil	342.10 ± 0.40	K	NIST
Tc	[500.70; 509.85]	K
Tc	507.80	K	Measurement of critical properties for binary and ternary mixtures containing potential gasoline additive diethyl carbonate (DEC)
Tc	507.90	K	Measurement of critical temperatures and critical pressures for binary mixtures of methyl tert-butyl ether (MTBE) + alcohol and MTBE + alkane
Tc	507.79	K	Experimental determination of critical data of multi-component mixtures containing potential gasoline additives 2-butanol by a flow-type apparatus
Tc	507.40	K	The Critical Temperatures of a Number of (i) (Chloroalkane (C3 C4) + Hydrocarbon (C6 C7)) Binary Mixtures and (ii) (Aromatic Halocarbon (Chlorobenzene, Fluorobenzene, 1,2-Dichlorobenzene, or 1,3-Dichlorobenzene) + Alkane (C8)) Binary Mixtures
Tc	507.80	K	Measurement of Critical Properties for Binary and Ternary Mixtures Containing n-Butanol and n-Alkane
Tc	507.79	K	Determination of the Critical Properties of C6 C10 n-Alkanes and Their Binary Systems Using a Flow Apparatus
Tc	507.60	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Tc	507.40	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	507.43	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	507.60	K	ChemSep v8.3 pure component data Compiled value
Tc	507.60	K	KDB
Tc	507.60 ± 0.20	K	NIST
Tc	Outlier 504.70 ± 2.00	K	NIST
Tc	Outlier 504.50 ± 4.00	K	NIST
Tc	507.20 ± 1.00	K	NIST
Tc	507.50 ± 0.40	K	NIST
Tc	507.30 ± 0.30	K	NIST
Tc	507.40 ± 0.60	K	NIST
Tc	507.30	K	NIST
Tc	507.53 ± 0.10	K	NIST
Tc	507.33 ± 0.40	K	NIST
Tc	507.40	K	NIST
Tc	507.40 ± 0.30	K	NIST
Tc	507.33 ± 0.40	K	NIST
Tc	507.86 ± 0.15	K	NIST
Tc	507.68 ± 0.20	K	NIST
Tc	507.55 ± 0.20	K	NIST
Tc	507.85 ± 0.20	K	NIST
Tc	508.00 ± 0.50	K	NIST
Tc	507.40 ± 0.30	K	NIST
Tc	507.80 ± 0.30	K	NIST
Tc	507.70 ± 0.30	K	NIST
Tc	507.40 ± 0.30	K	NIST
Tc	507.40 ± 0.30	K	NIST
Tc	507.40 ± 0.30	K	NIST
Tc	507.40 ± 0.30	K	NIST
Tc	507.40 ± 0.30	K	NIST
Tc	507.40 ± 0.30	K	NIST
Tc	507.40 ± 0.30	K	NIST
Tc	507.68 ± 0.20	K	NIST
Tc	507.30 ± 0.40	K	NIST
Tc	508.50 ± 0.60	K	NIST
Tc	508.00 ± 0.60	K	NIST
Tc	507.85 ± 0.25	K	NIST
Tc	507.60 ± 0.20	K	NIST
Tc	507.90 ± 0.40	K	NIST
Tc	507.30 ± 0.20	K	NIST
Tc	507.65 ± 0.10	K	NIST
Tc	507.95 ± 1.50	K	NIST
Tc	Outlier 509.85 ± 0.20	K	NIST
Tc	507.90 ± 2.22	K	NIST
Tc	507.90 ± 0.30	K	NIST
Tc	Outlier 500.70 ± 7.00	K	NIST
Tc	508.00 ± 1.00	K	NIST
Tc	507.70 ± 1.00	K	NIST
Tfus	[175.95; 179.15]	K
Tfus	178.80	K	Phase equilibria of didecyldimethylammonium nitrate ionic liquid with water and organic solvents
Tfus	177.39	K	Determination of melting temperatures in hydrocarbon mixtures by differential scanning calorimetry
Tfus	178.07	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	177.83	K	ChemSep v8.3 pure component data Compiled value
Tfus	177.80	K	KDB
Tfus	178.03	K	Aq. Solubility Prediction
Tfus	177.83	K	NCMS SOLV-DB
Tfus	178.15 ± 0.15	K	NIST
Tfus	177.79 ± 0.02	K	NIST
Tfus	177.80 ± 0.04	K	NIST
Tfus	177.78 ± 0.07	K	NIST
Tfus	177.70 ± 0.20	K	NIST
Tfus	177.80 ± 0.07	K	NIST
Tfus	177.80 ± 0.03	K	NIST
Tfus	177.76 ± 0.10	K	NIST
Tfus	177.59 ± 0.20	K	NIST
Tfus	Outlier 176.37 ± 0.30	K	NIST
Tfus	177.59 ± 0.30	K	NIST
Tfus	Outlier 176.45 ± 1.00	K	NIST
Tfus	177.80 ± 0.05	K	NIST
Tfus	177.81 ± 0.03	K	NIST
Tfus	177.76 ± 0.15	K	NIST
Tfus	177.81 ± 0.01	K	NIST
Tfus	177.80 ± 0.06	K	NIST
Tfus	177.83 ± 0.04	K	NIST
Tfus	177.76 ± 0.10	K	NIST
Tfus	Outlier 179.15 ± 1.50	K	NIST
Tfus	177.65 ± 0.30	K	NIST
Tfus	177.65 ± 0.20	K	NIST
Tfus	178.15 ± 2.00	K	NIST
Tfus	177.15 ± 1.00	K	NIST
Tfus	177.15 ± 0.50	K	NIST
Tfus	178.55 ± 0.40	K	NIST
Tfus	177.76 ± 0.08	K	NIST
Tfus	177.76 ± 0.08	K	NIST
Tfus	Outlier 175.95 ± 1.00	K	NIST
Tfus	178.05 ± 0.30	K	NIST
Tfus	177.15 ± 1.00	K	NIST
Tfus	178.85 ± 0.30	K	NIST
Ttriple	[177.82; 178.60]	K
Ttriple	177.85	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	177.83	K	ChemSep v8.3 pure component data Compiled value
Ttriple	177.83	K	KDB
Ttriple	177.83 ± 0.40	K	NIST
Ttriple	177.82 ± 0.05	K	NIST
Ttriple	177.82 ± 0.03	K	NIST
Ttriple	177.84 ± 0.07	K	NIST
Ttriple	177.83 ± 0.03	K	NIST
Ttriple	177.90 ± 0.10	K	NIST
Ttriple	177.90 ± 0.30	K	NIST
Ttriple	178.15 ± 0.30	K	NIST
Ttriple	Outlier 178.60 ± 0.20	K	NIST
UQi	3.86		ChemSep v8.3 pure component data Compiled value
URi	4.50		ChemSep v8.3 pure component data Compiled value
Vc	[0.368; 0.371]	m3/kmol
Vc	0.368	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Vc	0.370	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.368	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.368	m3/kmol	KDB
Vc	0.368	m3/kmol	NIST
Vc	0.371 ± 0.007	m3/kmol	NIST
VCOSTALD	0.37	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.30		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2637640; 0.2640000]
Zc	0.2640000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Zc	0.2640000		ChemSep v8.3 pure component data Compiled value
Zc	0.2637640		KDB
Zra	[0.26; 0.26]
Zra	0.26		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.26		ChemSep v8.3 pure component data Compiled value
Zra	0.26		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[156.27; 206.94]	J/mol×K	[333.85; 468.90]
Cp,gas	156.27 ± 0.31	J/mol×K	333.85	NIST
Cp,gas	168.28 ± 0.34	J/mol×K	365.15	NIST
Cp,gas	181.17 ± 0.36	J/mol×K	398.85	NIST
Cp,gas	194.10 ± 0.39	J/mol×K	433.70	NIST
Cp,gas	206.94 ± 0.41	J/mol×K	468.90	NIST
Cp,liquid	[184.20; 265.20]	J/mol×K	[293.50; 308.35]
Cp,liquid	193.30	J/mol×K	293.50	NIST
Cp,liquid	191.60	J/mol×K	295.10	NIST
Cp,liquid	195.64	J/mol×K	297.32	NIST
Cp,liquid	196.10	J/mol×K	297.32	NIST
Cp,liquid	194.10	J/mol×K	298.00	NIST
Cp,liquid	196.20	J/mol×K	298.00	NIST
Cp,liquid	195.10	J/mol×K	298.00	NIST
Cp,liquid	189.10	J/mol×K	298.10	NIST
Cp,liquid	195.33	J/mol×K	298.15	NIST
Cp,liquid	197.66	J/mol×K	298.15	NIST
Cp,liquid	195.33	J/mol×K	298.15	NIST
Cp,liquid	194.96	J/mol×K	298.15	NIST
Cp,liquid	195.80	J/mol×K	298.15	NIST
Cp,liquid	195.80	J/mol×K	298.15	NIST
Cp,liquid	265.20	J/mol×K	298.15	NIST
Cp,liquid	195.64	J/mol×K	298.15	NIST
Cp,liquid	195.76	J/mol×K	298.15	NIST
Cp,liquid	195.52	J/mol×K	298.15	NIST
Cp,liquid	197.66	J/mol×K	298.15	NIST
Cp,liquid	195.84	J/mol×K	298.15	NIST
Cp,liquid	198.50	J/mol×K	298.15	NIST
Cp,liquid	195.80	J/mol×K	298.15	NIST
Cp,liquid	194.97	J/mol×K	298.15	NIST
Cp,liquid	197.66	J/mol×K	298.15	NIST
Cp,liquid	196.10	J/mol×K	299.80	NIST
Cp,liquid	184.20	J/mol×K	300.00	NIST
Cp,liquid	186.20	J/mol×K	300.70	NIST
Cp,liquid	203.00	J/mol×K	308.35	NIST
η	[0.0000655; 0.0003495]	Pa×s	[283.15; 473.15]
η	0.0003495	Pa×s	283.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0003020	Pa×s	293.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
η	0.0003163	Pa×s	293.15	Viscosities and Densities of Binary Mixtures of Hexane with 1-Chlorohexane between 293.15 K and 333.15 K
η	0.0003100	Pa×s	293.15	Dynamic viscosities of the ternary liquid mixtures (dimethyl carbonate + methanol + ethanol) and (dimethyl carbonate + methanol + hexane) at several temperatures
η	0.0003190	Pa×s	293.15	Densities and Viscosities of Binary Mixtures of Tris(2-ethylhexyl) Phosphate + Cyclohexane or n-Hexane at T ) (293.15, 298.15, and 303.15) K and p ) 0.1 MPa
η	0.0002979	Pa×s	293.15	Viscosity and Density of Binary Mixtures of Ethyl Alcohol with n-Alkanes (C6, C8, and C10)
η	0.0003127	Pa×s	293.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0003036	Pa×s	298.15	Viscosities and Densities of Binary Mixtures of Hexane with 1-Chlorohexane between 293.15 K and 333.15 K
η	0.0003010	Pa×s	298.15	Dynamic viscosities of the ternary liquid mixtures (dimethyl carbonate + methanol + ethanol) and (dimethyl carbonate + methanol + hexane) at several temperatures
η	0.0002886	Pa×s	298.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
η	0.0002990	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of Tributyl Phosphate with Hexane and Dodecane from (298.15 to 328.15) K
η	0.0002865	Pa×s	298.15	Viscosity and Density of Binary Mixtures of Ethyl Alcohol with n-Alkanes (C6, C8, and C10)
η	0.0002940	Pa×s	298.15	NCMS SOLV-DB
η	0.0002944	Pa×s	298.15	Measurements, Correlations, and Predictions of Viscosities for the Ternary Mixture (2-Butanol + Hexane + 1-Chlorobutane) at 298.15 K and 313.15 K
η	0.0003040	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of Tris(2-ethylhexyl) Phosphate + Cyclohexane or n-Hexane at T ) (293.15, 298.15, and 303.15) K and p ) 0.1 MPa
η	0.0002937	Pa×s	298.20	Viscosity of liquid systems involving hydrogenated and fluorinated substances: Liquid mixtures of (hexane + perfluorohexane)
η	0.0002810	Pa×s	303.15	Dynamic viscosities of the ternary liquid mixtures (dimethyl carbonate + methanol + ethanol) and (dimethyl carbonate + methanol + hexane) at several temperatures
η	0.0002900	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of Tris(2-ethylhexyl) Phosphate + Cyclohexane or n-Hexane at T ) (293.15, 298.15, and 303.15) K and p ) 0.1 MPa
η	0.0002850	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of Tributyl Phosphate with Hexane and Dodecane from (298.15 to 328.15) K
η	0.0002914	Pa×s	303.15	Viscosities and Densities of Binary Mixtures of Hexane with 1-Chlorohexane between 293.15 K and 333.15 K
η	0.0002830	Pa×s	303.15	Density, Viscosity, and Speed of Sound of (Methyl Benzoate + Cyclohexane), (Methyl Benzoate + n-Hexane), (Methyl Benzoate + Heptane), and (Methyl Benzoate + Octane) at Temperatures of (303.15, 308.15, and 313.15) K
η	0.0002774	Pa×s	303.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
η	0.0002809	Pa×s	303.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0002798	Pa×s	303.16	Viscosity of liquid systems involving hydrogenated and fluorinated substances: Liquid mixtures of (hexane + perfluorohexane)
η	0.0002669	Pa×s	308.13	Viscosity of liquid systems involving hydrogenated and fluorinated substances: Liquid mixtures of (hexane + perfluorohexane)
η	0.0002730	Pa×s	308.15	Densities and Viscosities of Binary Mixtures of Tributyl Phosphate with Hexane and Dodecane from (298.15 to 328.15) K
η	0.0002797	Pa×s	308.15	Viscosities and Densities of Binary Mixtures of Hexane with 1-Chlorohexane between 293.15 K and 333.15 K
η	0.0002690	Pa×s	308.15	Density, Viscosity, and Speed of Sound of (Methyl Benzoate + Cyclohexane), (Methyl Benzoate + n-Hexane), (Methyl Benzoate + Heptane), and (Methyl Benzoate + Octane) at Temperatures of (303.15, 308.15, and 313.15) K
η	0.0002685	Pa×s	313.15	Viscosities and Densities of Binary Mixtures of Hexane with 1-Chlorohexane between 293.15 K and 333.15 K
η	0.0002600	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of Tributyl Phosphate with Hexane and Dodecane from (298.15 to 328.15) K
η	0.0002546	Pa×s	313.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0002520	Pa×s	313.15	Density, Viscosity, and Speed of Sound of (Methyl Benzoate + Cyclohexane), (Methyl Benzoate + n-Hexane), (Methyl Benzoate + Heptane), and (Methyl Benzoate + Octane) at Temperatures of (303.15, 308.15, and 313.15) K
η	0.0002504	Pa×s	313.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
η	0.0002537	Pa×s	313.15	Measurements, Correlations, and Predictions of Viscosities for the Ternary Mixture (2-Butanol + Hexane + 1-Chlorobutane) at 298.15 K and 313.15 K
η	0.0002560	Pa×s	313.15	Dynamic viscosities of the ternary liquid mixtures (dimethyl carbonate + methanol + ethanol) and (dimethyl carbonate + methanol + hexane) at several temperatures
η	0.0002580	Pa×s	318.15	Viscosities and Densities of Binary Mixtures of Hexane with 1-Chlorohexane between 293.15 K and 333.15 K
η	0.0002490	Pa×s	318.15	Densities and Viscosities of Binary Mixtures of Tributyl Phosphate with Hexane and Dodecane from (298.15 to 328.15) K
η	0.0002339	Pa×s	323.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
η	0.0002482	Pa×s	323.15	Viscosities and Densities of Binary Mixtures of Hexane with 1-Chlorohexane between 293.15 K and 333.15 K
η	0.0002340	Pa×s	323.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0002380	Pa×s	323.15	Densities and Viscosities of Binary Mixtures of Tributyl Phosphate with Hexane and Dodecane from (298.15 to 328.15) K
η	0.0002300	Pa×s	328.15	Densities and Viscosities of Binary Mixtures of Tributyl Phosphate with Hexane and Dodecane from (298.15 to 328.15) K
η	0.0002391	Pa×s	328.15	Viscosities and Densities of Binary Mixtures of Hexane with 1-Chlorohexane between 293.15 K and 333.15 K
η	0.0002114	Pa×s	333.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
η	0.0002308	Pa×s	333.15	Viscosities and Densities of Binary Mixtures of Hexane with 1-Chlorohexane between 293.15 K and 333.15 K
η	0.0001905	Pa×s	348.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0001550	Pa×s	373.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0001268	Pa×s	398.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0001026	Pa×s	423.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0000837	Pa×s	448.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0000655	Pa×s	473.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
ΔfusH	[12.34; 13.08]	kJ/mol	[177.80; 178.60]
ΔfusH	13.08	kJ/mol	177.80	NIST
ΔfusH	13.08	kJ/mol	177.80	NIST
ΔfusH	13.08	kJ/mol	177.84	NIST
ΔfusH	12.34	kJ/mol	177.90	NIST
ΔfusH	13.03	kJ/mol	177.90	NIST
ΔfusH	12.58	kJ/mol	178.60	NIST
ΔsubH	50.80	kJ/mol	178.00	NIST
ΔvapH	[8.90; 35.70]	kJ/mol	[221.50; 498.00]
ΔvapH	32.50	kJ/mol	221.50	NIST
ΔvapH	35.70	kJ/mol	224.00	NIST
ΔvapH	34.90	kJ/mol	268.00	NIST
ΔvapH	31.88	kJ/mol	298.00	Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
ΔvapH	30.90 ± 0.10	kJ/mol	309.00	NIST
ΔvapH	31.60	kJ/mol	310.50	NIST
ΔvapH	30.70 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	30.50 ± 0.20	kJ/mol	313.00	NIST
ΔvapH	32.00	kJ/mol	314.50	NIST
ΔvapH	30.90	kJ/mol	318.00	NIST
ΔvapH	31.50	kJ/mol	320.50	NIST
ΔvapH	29.80 ± 0.10	kJ/mol	328.00	NIST
ΔvapH	29.00 ± 0.20	kJ/mol	333.00	NIST
ΔvapH	29.50 ± 0.10	kJ/mol	333.00	NIST
ΔvapH	28.85	kJ/mol	341.90	KDB
ΔvapH	28.85	kJ/mol	341.90	NIST
ΔvapH	28.20 ± 0.20	kJ/mol	353.00	NIST
ΔvapH	28.20 ± 0.10	kJ/mol	353.00	NIST
ΔvapH	30.10	kJ/mol	359.00	NIST
ΔvapH	26.60	kJ/mol	373.00	NIST
ΔvapH	29.30	kJ/mol	412.50	NIST
ΔvapH	22.50	kJ/mol	423.00	NIST
ΔvapH	15.70	kJ/mol	473.00	NIST
ΔvapH	29.40	kJ/mol	476.50	NIST
ΔvapH	8.90	kJ/mol	498.00	NIST
ν	[0.0000004; 0.0000005]	m2/s	[283.15; 313.15]
ν	0.0000005	m2/s	283.15	Kinematic Viscosities for Ether + Alkane Mixtures: Experimental Results and UNIFAC-VISCO Parameters
ν	0.0000005	m2/s	283.15	Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
ν	0.0000004	m2/s	298.15	Kinematic Viscosities for Ether + Alkane Mixtures: Experimental Results and UNIFAC-VISCO Parameters
ν	0.0000004	m2/s	298.15	Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
ν	0.0000004	m2/s	313.15	Kinematic Viscosities for Ether + Alkane Mixtures: Experimental Results and UNIFAC-VISCO Parameters
ν	0.0000004	m2/s	313.15	Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
Pvap	[12.89; 2876.83]	kPa	[288.15; 504.04]
Pvap	12.89	kPa	288.15	Article Previous Article Next Article Articles ASAP Phase Equilibrium of Binary Mixtures of n-Hexane + Branched Chlorobutanes: Experimental Results and Group Contribution Predictions
Pvap	17.00	kPa	288.24	Isothermal Vapor-Liquid Equilibrium Data for Binary Mixtures of Hexafluoroethane (R116) + n-Pentane or n-Hexane at Two Temperatures, 288 and 296 K
Pvap	15.88	kPa	292.98	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	21.00	kPa	296.23	Isothermal Vapor-Liquid Equilibrium Data for Binary Mixtures of Hexafluoroethane (R116) + n-Pentane or n-Hexane at Two Temperatures, 288 and 296 K
Pvap	18.39	kPa	296.27	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	20.22	kPa	298.15	(Vapour + liquid) equilibrium and excess Gibbs functions of ternary mixtures containing 1-butanol or 2-butanol, n-hexane, and 1-chlorobutane at T = 298.15 K
Pvap	20.22	kPa	298.15	Article Previous Article Next Article Articles ASAP Phase Equilibrium of Binary Mixtures of n-Hexane + Branched Chlorobutanes: Experimental Results and Group Contribution Predictions
Pvap	20.22	kPa	298.15	Thermophysical Study of the n-Hexane or n-Heptane with 1- Chloropropane Systems
Pvap	20.17	kPa	298.15	NCMS SOLV-DB
Pvap	20.69	kPa	298.95	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	23.81	kPa	302.20	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	25.16	kPa	303.15	Measurement and correlation of (vapor + liquid) equilibria for the {2-propoxyethanol (C3E1) + n-hexane} and the {2-propoxyethanol (C3E1) + n-heptane} systems
Pvap	25.01	kPa	303.15	Phase equilibria for mixtures containing nonionic surfactant systems: Modeling and experiments
Pvap	25.04	kPa	303.16	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	26.19	kPa	304.49	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	27.50	kPa	305.43	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	28.77	kPa	306.76	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	29.95	kPa	307.43	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	30.01	kPa	307.66	Measurement and theoretical prediction of the vapor-liquid equilibrium, densities and interfacial tensions of the system hexane + 2-methoxy-2-methylbutane
Pvap	30.00	kPa	307.66	Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
Pvap	30.70	kPa	308.15	Article Previous Article Next Article Articles ASAP Phase Equilibrium of Binary Mixtures of n-Hexane + Branched Chlorobutanes: Experimental Results and Group Contribution Predictions
Pvap	30.68	kPa	308.28	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	32.44	kPa	309.54	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	32.97	kPa	310.14	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	35.07	kPa	311.47	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	35.01	kPa	311.56	Measurement and theoretical prediction of the vapor-liquid equilibrium, densities and interfacial tensions of the system hexane + 2-methoxy-2-methylbutane
Pvap	35.53	kPa	311.96	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	37.04	kPa	313.15	Vapor-Liquid Equilibria in Binary Systems Formed by n-Hexane with Alcohols
Pvap	37.42	kPa	313.15	Measurement and correlation of (vapor + liquid) equilibria for the {2-propoxyethanol (C3E1) + n-hexane} and the {2-propoxyethanol (C3E1) + n-heptane} systems
Pvap	37.54	kPa	313.15	Phase equilibria for mixtures containing nonionic surfactant systems: Modeling and experiments
Pvap	37.27	kPa	313.15	Vapour liquid equilibrium of octane enhancing additives in gasolines 7: Total pressure data and gE for the ternary mixture tert-amyl methyl ether (TAME), methanol and hexane at 313.15K
Pvap	37.19	kPa	313.15	Characterizing second generation biofuels: Excess enthalpies and vapour-liquid equilibria of the binary mixtures containing 1-pentanol or 2-pentanol and n-hexane
Pvap	37.90	kPa	313.20	Isothermal vapor-liquid equilibrium of binary and ternary systems of anisole, hexane, and toluene and ternary system of methyl tert-butyl ether, hexane, and toluene
Pvap	37.51	kPa	313.25	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	37.95	kPa	313.70	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	39.98	kPa	314.84	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	40.01	kPa	315.02	Measurement and theoretical prediction of the vapor-liquid equilibrium, densities and interfacial tensions of the system hexane + 2-methoxy-2-methylbutane
Pvap	40.10	kPa	315.07	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	41.16	kPa	315.74	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	42.30	kPa	316.51	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	42.44	kPa	316.52	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	44.59	kPa	317.91	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	45.02	kPa	317.92	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	45.01	kPa	318.15	Measurement and theoretical prediction of the vapor-liquid equilibrium, densities and interfacial tensions of the system hexane + 2-methoxy-2-methylbutane
Pvap	47.45	kPa	319.49	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	47.35	kPa	319.58	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	50.01	kPa	320.76	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	49.63	kPa	320.83	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	50.01	kPa	321.03	Measurement and theoretical prediction of the vapor-liquid equilibrium, densities and interfacial tensions of the system hexane + 2-methoxy-2-methylbutane
Pvap	50.62	kPa	321.32	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	51.87	kPa	322.02	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	52.52	kPa	322.26	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	54.11	kPa	323.15	Measurement and correlation of (vapor + liquid) equilibria for the {2-propoxyethanol (C3E1) + n-hexane} and the {2-propoxyethanol (C3E1) + n-heptane} systems
Pvap	54.39	kPa	323.15	Phase equilibria for mixtures containing nonionic surfactant systems: Modeling and experiments
Pvap	53.91	kPa	323.15	Vapor-Liquid Equilibria in Binary Systems Formed by n-Hexane with Alcohols
Pvap	55.03	kPa	323.37	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	54.51	kPa	323.45	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	55.01	kPa	323.68	Measurement and theoretical prediction of the vapor-liquid equilibrium, densities and interfacial tensions of the system hexane + 2-methoxy-2-methylbutane
Pvap	56.42	kPa	324.35	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	57.32	kPa	324.59	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	59.15	kPa	325.74	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	60.07	kPa	325.89	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	60.00	kPa	326.11	Isobaric vapor liquid equilibria for the n-hexane + 2-isopropoxyethanol and n-heptane + 2-isopropoxyethanol systems
Pvap	60.01	kPa	326.15	Measurement and theoretical prediction of the vapor-liquid equilibrium, densities and interfacial tensions of the system hexane + 2-methoxy-2-methylbutane
Pvap	62.46	kPa	326.95	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	62.05	kPa	327.09	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	64.02	kPa	327.99	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	64.20	kPa	328.02	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	64.77	kPa	328.09	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	65.01	kPa	328.45	Measurement and theoretical prediction of the vapor-liquid equilibrium, densities and interfacial tensions of the system hexane + 2-methoxy-2-methylbutane
Pvap	66.61	kPa	329.13	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	67.22	kPa	329.19	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	65.63	kPa	329.22	P-x data for binary systems using a novel static total pressure apparatus
Pvap	68.93	kPa	330.14	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	69.64	kPa	330.16	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	70.01	kPa	330.62	Measurement and theoretical prediction of the vapor-liquid equilibrium, densities and interfacial tensions of the system hexane + 2-methoxy-2-methylbutane
Pvap	70.86	kPa	330.93	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	72.45	kPa	331.45	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	73.11	kPa	331.87	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	74.82	kPa	332.28	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	74.53	kPa	332.40	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	75.62	kPa	332.87	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	76.32	kPa	333.15	Vapor-Liquid Equilibria in Binary Systems Formed by n-Hexane with Alcohols
Pvap	77.48	kPa	333.48	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	78.04	kPa	333.77	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	79.84	kPa	334.39	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	80.01	kPa	334.60	Measurement and theoretical prediction of the vapor-liquid equilibrium, densities and interfacial tensions of the system hexane + 2-methoxy-2-methylbutane
Pvap	80.11	kPa	334.61	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	80.00	kPa	334.61	Isobaric vapor liquid equilibria for the n-hexane + 2-isopropoxyethanol and n-heptane + 2-isopropoxyethanol systems
Pvap	82.31	kPa	335.33	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	82.94	kPa	335.65	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	84.88	kPa	336.26	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	84.85	kPa	336.32	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	85.40	kPa	336.53	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	87.26	kPa	337.14	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	87.73	kPa	337.38	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	89.85	kPa	338.02	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	89.92	kPa	338.15	Vapor-Liquid Equilibria in Binary Systems Formed by n-Hexane with Alcohols
Pvap	90.01	kPa	338.21	Measurement and theoretical prediction of the vapor-liquid equilibrium, densities and interfacial tensions of the system hexane + 2-methoxy-2-methylbutane
Pvap	90.28	kPa	338.26	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	92.35	kPa	338.91	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	93.18	kPa	339.25	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	94.85	kPa	339.73	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	95.79	kPa	340.10	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	96.72	kPa	340.39	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	97.02	kPa	340.44	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	98.28	kPa	340.92	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	99.08	kPa	341.17	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	100.00	kPa	341.48	Isobaric vapor liquid equilibria for the n-hexane + 2-isopropoxyethanol and n-heptane + 2-isopropoxyethanol systems
Pvap	100.39	kPa	341.60	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	101.32	kPa	341.76	Isobaric Vapor-Liquid Equilibrium Data and Excess Properties of Binary Systems Comprised of Alkyl Methanoates + Hexane
Pvap	101.30	kPa	341.79	Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
Pvap	101.32	kPa	341.79	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	101.33	kPa	341.85	Vapor-Liquid Equilibrium of Ferrocene in Some Organic Solvents Using Spectroscopic Methods
Pvap	101.31	kPa	341.86	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	101.32	kPa	341.88	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	101.30	kPa	341.88	Isobaric Vapor-Liquid Equilibrium Data for Two Binary Systems n-Hexane + 1,2-Dimethoxyethane and Methylcyclopentane + 1,2-Dimethoxyethane at 101.3 kPa
Pvap	101.80	kPa	342.02	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	101.81	kPa	342.08	Measurement and theoretical prediction of the vapor-liquid equilibrium, densities and interfacial tensions of the system hexane + 2-methoxy-2-methylbutane
Pvap	102.22	kPa	342.15	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	102.83	kPa	342.34	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	104.95	kPa	343.01	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	106.98	kPa	343.62	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	110.01	kPa	344.52	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	110.65	kPa	344.69	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	113.16	kPa	345.43	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	115.31	kPa	346.05	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	117.46	kPa	346.66	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	119.99	kPa	347.36	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	122.52	kPa	348.05	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	123.12	kPa	348.15	Measurement, correlation and prediction of isothermal vapor liquid equilibria of different systems containing vegetable oils
Pvap	123.03	kPa	348.15	Measurement, correlation and prediction of isothermal vapor liquid equilibria of different systems containing vegetable oils
Pvap	122.84	kPa	348.15	Measurement, correlation and prediction of isothermal vapor liquid equilibria of different systems containing vegetable oils
Pvap	124.01	kPa	348.44	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	126.23	kPa	349.04	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	128.44	kPa	349.61	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	129.32	kPa	349.82	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	131.23	kPa	350.34	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	133.07	kPa	350.82	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	135.49	kPa	351.42	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	137.54	kPa	351.93	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	139.99	kPa	352.53	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	140.84	kPa	352.74	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	141.31	kPa	352.83	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	142.40	kPa	353.15	Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
Pvap	142.80	kPa	353.22	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	145.75	kPa	353.87	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	146.70	kPa	354.14	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	147.04	kPa	354.23	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	149.34	kPa	354.71	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	152.14	kPa	355.40	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	153.31	kPa	355.66	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	155.14	kPa	356.04	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	157.29	kPa	356.52	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	159.38	kPa	357.01	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	161.05	kPa	357.38	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	162.94	kPa	357.80	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	166.02	kPa	358.47	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	167.98	kPa	358.88	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	169.31	kPa	359.18	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	171.84	kPa	359.69	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	172.89	kPa	359.90	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	175.78	kPa	360.51	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	177.31	kPa	360.80	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	178.41	kPa	361.06	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	178.67	kPa	361.09	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	180.95	kPa	361.54	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	182.61	kPa	361.86	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	185.32	kPa	362.43	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	186.64	kPa	362.68	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	188.20	kPa	362.98	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	188.05	kPa	363.15	Vapor-Liquid Equilibria for Four Binary Systems at 363.15 K: N-Methylformamide + Hexane, + Benzene, + Chlorobenzene, and + Acetonitrile
Pvap	189.72	kPa	363.29	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	191.05	kPa	363.52	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	193.35	kPa	363.95	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	214.05	kPa	367.78	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	247.22	kPa	373.15	Measurement, correlation and prediction of isothermal vapor liquid equilibria of different systems containing vegetable oils
Pvap	245.79	kPa	373.15	Measurement, correlation and prediction of isothermal vapor liquid equilibria of different systems containing vegetable oils
Pvap	245.99	kPa	373.15	Measurement, correlation and prediction of isothermal vapor liquid equilibria of different systems containing vegetable oils
Pvap	254.29	kPa	374.40	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	281.37	kPa	378.42	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	284.18	kPa	378.82	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	324.95	kPa	384.30	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	378.71	kPa	390.79	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	410.00	kPa	393.15	In Situ Determination of Phase Equilibria of Methyl Benzoate + Alkane Mixtures Using an Infrared Absorption Method. Comparison with Polar GC-SAFT Predictions
Pvap	402.46	kPa	393.44	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	417.93	kPa	395.10	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	465.31	kPa	399.91	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	503.73	kPa	403.55	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	509.54	kPa	404.08	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	551.62	kPa	407.80	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	601.70	kPa	411.96	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	633.00	kPa	413.15	In Situ Determination of Phase Equilibria of Methyl Benzoate + Alkane Mixtures Using an Infrared Absorption Method. Comparison with Polar GC-SAFT Predictions
Pvap	664.70	kPa	416.84	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	695.49	kPa	419.10	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	720.50	kPa	420.88	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	796.06	kPa	425.99	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	829.29	kPa	428.13	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	871.03	kPa	430.72	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	918.00	kPa	433.15	In Situ Determination of Phase Equilibria of Methyl Benzoate + Alkane Mixtures Using an Infrared Absorption Method. Comparison with Polar GC-SAFT Predictions
Pvap	911.85	kPa	433.17	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	992.37	kPa	437.76	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	1031.74	kPa	439.90	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	1088.58	kPa	442.89	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	1170.51	kPa	447.01	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	1180.73	kPa	447.50	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	1301.00	kPa	453.15	In Situ Determination of Phase Equilibria of Methyl Benzoate + Alkane Mixtures Using an Infrared Absorption Method. Comparison with Polar GC-SAFT Predictions
Pvap	1310.01	kPa	453.54	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	1399.98	kPa	457.47	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	1504.52	kPa	461.81	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	1584.85	kPa	465.00	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	1725.01	kPa	470.26	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	1801.25	kPa	472.99	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	1961.15	kPa	478.43	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	2057.52	kPa	481.54	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	2106.53	kPa	483.08	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	2109.00	kPa	483.15	Measurement and correlation of vapor-liquid equilibria for the 2-propanol + n-hexane system near the critical
Pvap	2195.23	kPa	485.80	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	2278.56	kPa	488.27	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	2450.36	kPa	493.14	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	2453.00	kPa	493.15	Measurement and correlation of vapor-liquid equilibria for the 2-propanol + n-hexane system near the critical
Pvap	2623.45	kPa	497.75	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	2701.96	kPa	499.76	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	2764.64	kPa	501.32	Vapour pressures of n-hexane determined by comparative ebulliometry
Pvap	2838.00	kPa	503.15	Measurement and correlation of vapor-liquid equilibria for the 2-propanol + n-hexane system near the critical
Pvap	2876.83	kPa	504.04	Vapour pressures of n-hexane determined by comparative ebulliometry
n0	[1.36150; 1.48680]		[293.15; 318.15]
n0	1.37480		293.15	Isobaric Vapor Liquid Equilibrium for Nine Binary Systems of Cracking C5 Fraction at 250 kPa
n0	1.37490		293.15	Vapour liquid equilibrium of carboxylic acid systems: Propionic acid + valeric acid and isobutyric acid + valeric acid
n0	1.37510		293.15	Solubilities of Methyldiphenylphosphine Oxide in Selected Solvents
n0	1.37495		293.15	Mixing properties of binary mixtures presenting azeotropes at several temperatures
n0	1.37486		293.15	Isobaric Vapor-Liquid Equilibria of Hexane + 1-Decene and Octane + 1-Decene Mixtures
n0	1.37480		293.15	Vapor Liquid Equilibrium Data for the Morpholine-4-carbaldehyde + n-Hexane or n-Heptane Binary Systems Using a Static-Synthetic Apparatus
n0	1.37590		293.15	Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
n0	1.48680		293.15	Phase Equilibria of Water + Furfural and Dichloromethane + n-Hexane
n0	1.37250		293.15	Isothermal Vapor-Liquid Equilibrium Measurements for Alcohol + Water/n-Hexane Azeotropic Systems Using Both Dynamic and Automated Static-Synthetic Methods
n0	1.37520		293.15	A novel static analytical apparatus for phase equilibrium measurements
n0	1.37500		293.20	Liquid phase equilibria for mixtures of (an aliphatic hydrocarbon + toluene + gamma-butyrolactone)
n0	1.37440		298.10	Excess Enthalpies and Thermal Conductivity Coefficients for Binary Mixtures of Carbon Tetrachloride and Four Alkanes (C5 to C8) at a Temperature of 298.15 K
n0	1.37514		298.10	Vapor-Liquid Equilibrium for Methoxymethane + Methyl Formate, Methoxymethane + Hexane, and Methyl Formate + Methanol
n0	1.37240		298.15	Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
n0	1.37230		298.15	Multiproperty Correlation of Experimental Data of the Binaries Propyl Ethanoate + Alkanes (Pentane to Decane). New Experimental Information for Vapor Liquid Equilibrium and Mixing Properties
n0	1.37360		298.15	Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
n0	1.37200		298.15	NCMS SOLV-DB
n0	1.37226		298.15	KDB
n0	1.37230		298.15	(Vapor + liquid) equilibria of binary mixtures formed by iso-octane with a variety of compounds at 95.8 kPa
n0	1.37230		298.15	Physical properties of (propyl propanoate + hexane + toluene) at 298.15 K
n0	1.37320		298.15	Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
n0	1.37217		298.15	Mixing properties of binary mixtures presenting azeotropes at several temperatures
n0	1.37234		298.15	Liquid-Liquid Equilibrium for Ternary Mixtures of Hexane + Aromatic Compounds + [EMpy][ESO4] at T = 298.15 K
n0	1.37234		298.15	Extraction of toluene from aliphatic compounds using an ionic liquid as solvent: Influence of the alkane on the (liquid + liquid) equilibrium
n0	1.37241		298.15	Ethanol extraction from its azeotropic mixture with hexane employing different ionic liquids as solvents
n0	1.37510		298.15	Ternary liquid liquid equilibrium data for the (water + butyric acid + n-hexane or n-hexanol) systems at T = (298.2, 308.2, and 318.2) K
n0	1.37223		298.15	Refractive indices and static permittivities of systems containing n-hexane or n-heptane and isomeric chlorobutanes
n0	1.37220		298.15	Volumetric, acoustic, and refractometric properties of (thiophene + hexane/cyclohexane) solutions in the presence of some imidazolium based ionic liquids at T = 298.15 K
n0	1.37240		298.15	Isothermal (vapour + liquid) equilibrium data for binary systems of (n-hexane + CO2 or CHF3)
n0	1.37240		298.15	Physical properties and their corresponding changes of mixing for the ternary mixture acetone + n-hexane +water at 298.15K
n0	1.37374		298.15	Vapor-liquid equilibrium and interfacial tensions of the system ethanol + hexane + tetrahydro-2H-Pyran
n0	1.37374		298.15	Experimental determination and theoretical modeling of the vapor-liquid equilibrium and surface tensions of hexane + tetrahydro-2H-pyran
n0	1.37250		298.15	Measurement and Prediction of Excess Properties of Binary Mixtures Methyl Decanoate + an Even-Numbered n-Alkane (C6-C16) at 298.15 K
n0	1.37280		298.15	Liquid-liquid equilibria for mixtures of (Furfural + an Aromatic hydrocarbon + an alkane) at T=298.15 K
n0	1.37240		298.15	Phase equilibria of binary systems of 3-methylthiophene with four different hydrocarbons
n0	1.37280		298.15	Liquid-Liquid Equilibria for Mixtures of (Furfural + a Chlorinated Aromatic Compound + an Alkane) at T = 298.15 K
n0	1.37280		298.15	Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethanediol, + Hexane, + Tributylamine, or + Triethylamine at (298.15, 303.15, and 308.15) K
n0	1.37226		298.15	Separation of aromatic hydrocarbons from alkanes using ammonium ionic liquid C2NTf2 at T = 298.15K
n0	1.37287		298.15	Phase behaviour of 1-methyl-3-octylimidazolium bis[trifluoromethylsulfonyl]imide with thiophene and aliphatic hydrocarbons: The influence of n-alkane chain length
n0	1.37220		298.15	Solubility of -Carotene in Binary Solvents Formed by Some Hydrocarbons with Dibutyl Ether and 1,2-Dimethoxyethane
n0	1.37470		298.15	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
n0	1.37220		298.15	Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with tert-Butyl Methyl Ether and with tert-Amyl Methyl Ether
n0	1.37230		298.15	Densities, Surface Tensions, and Refractive Indexes of Propyl Propanoate + Hexane + m-Xylene at 298.15 K
n0	1.37290		298.15	Distribution of Butyric Acid between Water and Several Solvents
n0	1.37240		298.15	Vapor-Liquid Equilibrium for Binary System of Thiophene + n-Hexane at (338.15 and 323.15) K and Thiophene + 1-Hexene at (333.15 and 323.15) K
n0	1.37450		298.15	Densities, Viscosities, and Refractive Indices of Mixtures of Hexane with Cyclohexane, Decane, Hexadecane, and Squalane at 298.15K
n0	1.37230		298.15	Vapor-Liquid Equilibrium for Binary System of Diethyl Sulfide + n-Hexane at (338.15 and 323.15) K and Diethyl Sulfide + 1-Hexene at (333.15 and 323.15) K
n0	1.37287		298.15	Extraction Ability of Nitrogen-Containing Compounds Involved in the Desulfurization of Fuels by Using Ionic Liquids
n0	1.37234		298.15	Separation of Benzene from Linear Alkanes (C6-C9) Using 1-Ethyl-3-Methylimidazolium Ethylsulfate at T = 298.15 K
n0	1.37287		298.15	Thiophene separation from aliphatic hydrocarbons using the 1-ethyl-3-methylimidazolium ethylsulfate ionic liquid
n0	1.37237		298.15	Liquid liquid equilibria of lactam containing binary systems
n0	1.37226		298.15	Effect of an Ionic Liquid (IL) Cation on the Ternary System (IL + p-Xylene + Hexane) at T= 298.15 K
n0	1.37217		298.15	A study on the liquid liquid equilibria of 1-alkyl-3-methylimidazolium hexafluorophosphate with ethanol and alkanes
n0	1.37287		298.15	Liquid-Liquid Equilibria for Systems Composed by 1-Methyl-3-octylimidazolium Tetrafluoroborate Ionic Liquid, Thiophene, and n-Hexane or Cyclohexane
n0	1.37230		298.15	Vapor-Liquid Equilibrium and Excess Gibbs Energies of Hexane + N,N-Dimethyl Formamide, 2-Methylpropan-2-ol + 2-Aminophenol, N,N-Dimethyl Formamide, and 2-Propanol + Diisopropyl Amine at 94.4 kPa
n0	1.37090		303.15	Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
n0	1.36980		303.15	Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethanediol, + Hexane, + Tributylamine, or + Triethylamine at (298.15, 303.15, and 308.15) K
n0	1.36936		303.15	Mixing properties of binary mixtures presenting azeotropes at several temperatures
n0	1.37070		303.15	Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
n0	1.36700		308.15	Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethanediol, + Hexane, + Tributylamine, or + Triethylamine at (298.15, 303.15, and 308.15) K
n0	1.36760		308.15	Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
n0	1.36150		318.15	Multiproperty Correlation of Experimental Data of the Binaries Propyl Ethanoate + Alkanes (Pentane to Decane). New Experimental Information for Vapor Liquid Equilibrium and Mixing Properties
ρl	[617.07; 677.18]	kg/m3	[273.15; 338.15]
ρl	677.18	kg/m3	273.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	672.79	kg/m3	278.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	668.37	kg/m3	283.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	663.91	kg/m3	288.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	664.13	kg/m3	288.15	Study of the binary mixtures of {monoglyme + (hexane, cyclohexane, octane, dodecane)} by ECM-average and PFP models
ρl	659.00	kg/m3	293.00	KDB
ρl	659.40	kg/m3	293.15	Solubility and distribution of bicycle derivatives of 1,3-selenazine in pharmaceutically relevant media by saturation shake-flask method
ρl	660.51	kg/m3	293.15	Surface tension and density of mixtures of m-xylene + n-alkane at 293.15 K: Analysis under the extended Langmuir and Shereshefsky models
ρl	659.40	kg/m3	293.15	A thermodynamic study of sublimation, dissolution and distribution processes of anti-inflammatory drug Clonixin
ρl	659.42	kg/m3	293.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	659.00	kg/m3	293.15	Volume expansion prediction of supercritical CO 2 + crude oil
ρl	660.00	kg/m3	293.15	Experimental Solubility Data for Binary Mixtures of Ethane and 2,2,4-Trimethylpentane at Pressures up to 6 MPa Using a New Variable-Volume Sapphire Cell
ρl	659.40	kg/m3	293.15	Densities and Kinematic Viscosities of One Quinary Regular Liquid System and Its Five Quaternary Sub-Systems at Temperatures (293.15 and 298.15) K
ρl	654.89	kg/m3	298.10	Excess enthalpies of binary mixtures of 2-ethoxyethanol with four hydrocarbons at 298.15, 308.15, and 318.15K An experimental and theoretical study
ρl	654.70	kg/m3	298.15	Thermophysical Study of Binary Systems of tert-Amyl Methyl Ether with n-Hexane and m-Xylene
ρl	668.00	kg/m3	298.15	Liquid-Liquid Equilibrium Data for Ternary Systems Containing Alkanes (n-Pentane, n-Hexane, n-Heptane, and n-Octane) + Alcohol (Methanol and Ethanol) + Protic Ionic Liquid (2-HEAF)
ρl	654.90	kg/m3	298.15	Densities and Kinematic Viscosities of One Quinary Regular Liquid System and Its Five Quaternary Sub-Systems at Temperatures (293.15 and 298.15) K
ρl	654.70	kg/m3	298.15	Surface Tension Deviations and Excess Molar Volumes on the Ternary System Propyl Propanoate + Hexane + p-Xylene at 298.15 K
ρl	655.12	kg/m3	298.15	Liquid-liquid equilibrium data for ternary mixtures composed of n-hexane, benzene and acetonitrile at (298.15, 308.15, and 318.15) K
ρl	654.89	kg/m3	298.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	655.07	kg/m3	298.15	Densities and Viscosities of the Ternary Mixtures 2-Methyl-1-propanol (or 2-Methyl-2-propanol) + N-Hexane + 1-Chlorobutane at 298.15 K
ρl	654.80	kg/m3	298.15	A thermodynamic study of sublimation, dissolution and distribution processes of anti-inflammatory drug Clonixin
ρl	655.09	kg/m3	298.15	Hexyl dimethylpyridinium ionic liquids for desulfurization of fuels. Effect of the position of the alkyl side chains
ρl	655.07	kg/m3	298.15	Surface Tensions of the Ternary Mixtures Containing an Isomeric Butanol + n-Hexane + 1-Chlorobutane at 298.15 K
ρl	655.25	kg/m3	298.15	Thermodynamics of Mixtures Containing a Strongly Polar Compound. 8. Liquid-Liquid Equilibria for N,N-Dialkylamide + Selected N-Alkanes
ρl	654.90	kg/m3	298.15	Vapor-Liquid Equilibria and Excess Enthalpies for Binary Systems of Dimethoxymethane with Hydrocarbons
ρl	655.07	kg/m3	298.15	Experimental and predicted viscosities of the ternary mixture (hexane + 1,3-dioxolane + 2-butanol) at 298.15 and 313.15 K
ρl	655.42	kg/m3	298.15	Excess Enthalpies of the Ternary Mixtures: Tetrahydrofuran + (Hexane or Cyclohexane) + Decane at 298.15K
ρl	655.07	kg/m3	298.15	Excess molar volumes and dynamic viscosities for binary mixtures of toluene + n-alkanes (C5 C10) at T = 298.15 K Comparison with Prigogine Flory Patterson theory
ρl	654.80	kg/m3	298.15	Phase diagrams of (hexane + methanol + 2,2,2-trifluoroethanol) at three temperatures: Measurement and correlation
ρl	655.21	kg/m3	298.15	Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
ρl	654.80	kg/m3	298.15	Viscosities of Dimethyl Carbonate or Diethyl Carbonate with Alkanes at Four Temperatures. New UNIFAC-VISCO Parameters
ρl	654.00	kg/m3	298.15	Isothermal Vapor-Liquid Equilibrium Data for the Binary Systems Consisting of 1,1,2,3,3,3-Hexafluoro-1-propene and Either Methylcyclohexane, Cyclohexane, n-Hexane, 2-Methyltetrahydrofuran, or 2,2,3,3,4,4,4-Heptafluoro-1-butanol
ρl	654.82	kg/m3	298.15	Topological and thermodynamic investigations of binary mixtures: Molar excess volumes, molar excess enthalpies and isentropic compressibility changes of mixing
ρl	654.70	kg/m3	298.15	Experimental Study of the Dynamic Viscosity Deviations in the Binary Systems: Hexane + Ethylbenzene, + o-Xylene, + m-Xylene, + p-Xylene at 298.15 K
ρl	654.90	kg/m3	298.15	Excess molar volumes and excess molar enthalpies of binary and ternary mixtures of (ethanol or 1-butanol), triethylamine and n-hexane
ρl	655.20	kg/m3	298.15	Application of 1-alkyl-3-methylpyridinium bis(trifluoromethylsulfonyl)imide ionic liquids for the ethanol removal from its mixtures with alkanes
ρl	655.20	kg/m3	298.15	Cation effect of ammonium imide based ionic liquids in alcohols extraction from alcohol-alkane azeotropic mixtures
ρl	655.19	kg/m3	298.15	Phase behavior of ternary mixtures {aliphatic hydrocarbon + aromatic hydrocarbon + ionic liquid}: Experimental LLE data and their modeling by COSMO-RS
ρl	655.09	kg/m3	298.15	Desulfurization of fuels by liquid-liquid extraction with1-ethyl-3-methylimidazolium ionic liquids
ρl	655.14	kg/m3	298.15	Study of the binary mixtures of {monoglyme + (hexane, cyclohexane, octane, dodecane)} by ECM-average and PFP models
ρl	655.10	kg/m3	298.15	Evaluation of Diethyl Carbonate and Methyl Isobutyl Ketone as Entrainers for the Separation of 1-Hexene and n-Hexane
ρl	655.19	kg/m3	298.15	SAFT-.gamma. force field for the simulation of molecular fluids 6: Binary and ternary mixtures comprising water, carbon dioxide, and n-alkanes
ρl	654.90	kg/m3	298.15	Fully automatized apparatus for determining speed of sound for liquids in the temperature and pressure interval (283.15-343.15) K and (0.1-95) MPa
ρl	655.20	kg/m3	298.15	Capacity of two 1-butyl-1-methylpyrrolidinium-based ionic liquidsfor the extraction of ethanol from its mixtures with heptane and hexane
ρl	655.20	kg/m3	298.15	Ionic liquids as solvents to separate the azeotropic mixture hexane/ethanol
ρl	654.76	kg/m3	298.15	Solubility and distribution of bicycle derivatives of 1,3-selenazine in pharmaceutically relevant media by saturation shake-flask method
ρl	655.00	kg/m3	298.15	VLE measurements and modelling for the binary systems of (CF4 + C6F14) and (CF4 + C8F18)
ρl	659.00	kg/m3	298.15	Liquid Liquid Equilibrium data for the ternary systems of Water, Isopropyl alcohol, and selected entrainers
ρl	654.82	kg/m3	298.15	Excess molar volumes and isentropic compressibilities changes of mixing of tetrahydropyran + benzene + cyclo or n-alkanes ternary mixtures at 308.15 K
ρl	655.04	kg/m3	298.20	Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
ρl	655.29	kg/m3	298.20	Isobaric Vapor Liquid Equilibrium of Binary Systems of Hexane or Octane with 1,2-Dimethylbenzene or 1,3-Dimethylbenzene at 101.3 kPa
ρl	650.21	kg/m3	303.15	Solubility and distribution of bicycle derivatives of 1,3-selenazine in pharmaceutically relevant media by saturation shake-flask method
ρl	652.90	kg/m3	303.15	Unravelling various types of non-covalent interactions of benzyl amine with ethers in n-hexane at 303.15 K by ultrasonic and DFT methods
ρl	650.20	kg/m3	303.15	A thermodynamic study of sublimation, dissolution and distribution processes of anti-inflammatory drug Clonixin
ρl	650.90	kg/m3	303.15	Volumetric Behavior of the Binary Mixtures of Methyl Ethyl Ketone with n-Hexane, Cyclohexane, and Benzene at T ) (303.15, 313.15, and 323.15) K
ρl	650.33	kg/m3	303.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	650.64	kg/m3	303.15	Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
ρl	646.03	kg/m3	308.15	Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
ρl	645.43	kg/m3	308.15	Solubility and distribution of bicycle derivatives of 1,3-selenazine in pharmaceutically relevant media by saturation shake-flask method
ρl	646.10	kg/m3	308.15	Study of the binary mixtures of {monoglyme + (hexane, cyclohexane, octane, dodecane)} by ECM-average and PFP models
ρl	645.40	kg/m3	308.15	A thermodynamic study of sublimation, dissolution and distribution processes of anti-inflammatory drug Clonixin
ρl	645.73	kg/m3	308.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	645.40	kg/m3	308.15	Thermophysical Study of Binary Systems of tert-Amyl Methyl Ether with n-Hexane and m-Xylene
ρl	642.00	kg/m3	313.15	Experimental Phase Equilibrium for the Binary System of n-Pentane +2-Propanol Using a New Equilibrium Cell and the Static Total Pressure Method
ρl	641.08	kg/m3	313.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	641.37	kg/m3	313.15	Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
ρl	641.20	kg/m3	313.15	Experimental measurement of carbon dioxide solubility in 1-methylpyrrolidin-2-one (NMP) + 1-butyl-3-methyl-1H-imidazol-3-ium tetrafluoroborate ([bmim][BF4]) mixtures using a new static-synthetic cell
ρl	640.70	kg/m3	313.15	A thermodynamic study of sublimation, dissolution and distribution processes of anti-inflammatory drug Clonixin
ρl	641.70	kg/m3	313.15	Volumetric Behavior of the Binary Mixtures of Methyl Ethyl Ketone with n-Hexane, Cyclohexane, and Benzene at T ) (303.15, 313.15, and 323.15) K
ρl	640.75	kg/m3	313.15	Solubility and distribution of bicycle derivatives of 1,3-selenazine in pharmaceutically relevant media by saturation shake-flask method
ρl	636.38	kg/m3	318.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	636.67	kg/m3	318.15	Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
ρl	636.20	kg/m3	318.15	Thermophysical Study of Binary Systems of tert-Amyl Methyl Ether with n-Hexane and m-Xylene
ρl	631.64	kg/m3	323.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	631.92	kg/m3	323.15	Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
ρl	630.90	kg/m3	323.15	Volumetric Behavior of the Binary Mixtures of Methyl Ethyl Ketone with n-Hexane, Cyclohexane, and Benzene at T ) (303.15, 313.15, and 323.15) K
ρl	631.20	kg/m3	323.15	Thermophysical Study of Binary Systems of tert-Amyl Methyl Ether with n-Hexane and m-Xylene
ρl	626.40	kg/m3	328.15	Thermophysical Study of Binary Systems of tert-Amyl Methyl Ether with n-Hexane and m-Xylene
ρl	626.84	kg/m3	328.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	621.99	kg/m3	333.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	617.07	kg/m3	338.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ΔfusS	[69.38; 73.54]	J/mol×K	[177.84; 178.60]
ΔfusS	73.54	J/mol×K	177.84	NIST
ΔfusS	69.38	J/mol×K	177.90	NIST
ΔfusS	73.30	J/mol×K	177.90	NIST
ΔfusS	70.44	J/mol×K	178.60	NIST
csound,fluid	[109.70; 1121.40]	m/s	[288.15; 506.15]
csound,fluid	1121.40	m/s	288.15	Excess enthalpy, density, and speed of sound determination for the ternary mixture (methyl tert-butyl ether + 1-butanol + n-hexane)
csound,fluid	1098.00	m/s	293.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	1098.90	m/s	293.15	Acoustic and Thermophysical Properties of Binary Liquid Mixtures of Primary Butanols with Hexane and Cyclohexane at 293.15 K
csound,fluid	1099.00	m/s	293.15	Excess enthalpy, density, and speed of sound determination for the ternary mixture (methyl tert-butyl ether + 1-butanol + n-hexane)
csound,fluid	1098.10	m/s	293.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	1076.00	m/s	298.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	1076.00	m/s	298.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	1076.30	m/s	298.15	Excess enthalpy, density, and speed of sound determination for the ternary mixture (methyl tert-butyl ether + 1-butanol + n-hexane)
csound,fluid	1111.20	m/s	300.09	Speed of sound measurements of di-isopropyl ether (DIPE) from 293.15 K to 673.15 K and up to 10 MPa
csound,fluid	1073.00	m/s	300.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	1053.60	m/s	303.15	Excess enthalpy, density, and speed of sound determination for the ternary mixture (methyl tert-butyl ether + 1-butanol + n-hexane)
csound,fluid	1054.30	m/s	303.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	1054.00	m/s	303.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	1031.10	m/s	308.15	Excess enthalpy, density, and speed of sound determination for the ternary mixture (methyl tert-butyl ether + 1-butanol + n-hexane)
csound,fluid	1031.80	m/s	308.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	1032.00	m/s	308.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	1009.90	m/s	313.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	1010.00	m/s	313.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	993.00	m/s	313.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	988.00	m/s	318.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	987.70	m/s	318.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	966.00	m/s	323.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	965.70	m/s	323.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	926.80	m/s	328.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	943.70	m/s	328.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	944.00	m/s	328.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	921.30	m/s	333.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	921.00	m/s	333.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	900.00	m/s	338.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	899.70	m/s	338.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	878.00	m/s	343.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	877.80	m/s	343.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	882.70	m/s	343.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	856.00	m/s	348.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	855.90	m/s	348.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	898.50	m/s	353.12	Speed of sound measurements of di-isopropyl ether (DIPE) from 293.15 K to 673.15 K and up to 10 MPa
csound,fluid	834.20	m/s	353.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	838.80	m/s	353.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	834.00	m/s	353.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	812.00	m/s	358.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	812.10	m/s	358.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	790.00	m/s	363.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	790.30	m/s	363.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	794.90	m/s	363.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	768.00	m/s	368.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	768.40	m/s	368.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	747.00	m/s	373.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	746.60	m/s	373.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	751.00	m/s	373.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	707.20	m/s	383.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	663.40	m/s	393.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	619.50	m/s	403.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	705.90	m/s	403.17	Speed of sound measurements of di-isopropyl ether (DIPE) from 293.15 K to 673.15 K and up to 10 MPa
csound,fluid	575.60	m/s	413.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	531.60	m/s	423.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	487.50	m/s	433.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	443.10	m/s	443.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	420.70	m/s	448.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	513.00	m/s	453.15	Speed of sound measurements of di-isopropyl ether (DIPE) from 293.15 K to 673.15 K and up to 10 MPa
csound,fluid	398.20	m/s	453.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	375.60	m/s	458.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	352.80	m/s	463.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	329.80	m/s	468.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	306.40	m/s	473.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	282.60	m/s	478.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	258.20	m/s	483.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	233.00	m/s	488.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	206.40	m/s	493.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	177.30	m/s	498.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	323.70	m/s	503.13	Speed of sound measurements of di-isopropyl ether (DIPE) from 293.15 K to 673.15 K and up to 10 MPa
csound,fluid	142.00	m/s	503.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	109.70	m/s	506.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
γ	[0.02; 0.02]	N/m	[283.15; 328.15]
γ	0.02	N/m	283.15	Surface and bulk behaviour of some (n-hexane + chloroalkane) mixtures
γ	0.02	N/m	283.15	Study of the Temperature Dependence of Surface Tensions of Some Alkanol + Hexane Mixtures
γ	0.02	N/m	288.15	Surface and bulk behaviour of some (n-hexane + chloroalkane) mixtures
γ	0.02	N/m	288.15	Study of the Temperature Dependence of Surface Tensions of Some Alkanol + Hexane Mixtures
γ	0.02	N/m	288.15	Interfacial Tensions of Imidazolium-Based Ionic Liquids with N-Alkanes and Cyclohexane
γ	0.02	N/m	293.15	Surface and bulk behaviour of some (n-hexane + chloroalkane) mixtures
γ	0.02	N/m	293.15	Study of the Temperature Dependence of Surface Tensions of Some Alkanol + Hexane Mixtures
γ	0.02	N/m	293.15	Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ	0.02	N/m	293.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.02	N/m	293.20	KDB
γ	0.02	N/m	298.15	NCMS SOLV-DB
γ	0.02	N/m	298.15	Study of the Temperature Dependence of Surface Tensions of Some Alkanol + Hexane Mixtures
γ	0.02	N/m	298.15	Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ	0.02	N/m	298.15	Interfacial Tensions of Imidazolium-Based Ionic Liquids with N-Alkanes and Cyclohexane
γ	0.02	N/m	298.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.02	N/m	298.15	Surface and bulk behaviour of some (n-hexane + chloroalkane) mixtures
γ	0.02	N/m	303.15	Study of the Temperature Dependence of Surface Tensions of Some Alkanol + Hexane Mixtures
γ	0.02	N/m	303.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.02	N/m	303.15	Surface and bulk behaviour of some (n-hexane + chloroalkane) mixtures
γ	0.02	N/m	303.15	Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ	0.02	N/m	308.15	Interfacial Tensions of Imidazolium-Based Ionic Liquids with N-Alkanes and Cyclohexane
γ	0.02	N/m	308.15	Surface and bulk behaviour of some (n-hexane + chloroalkane) mixtures
γ	0.02	N/m	308.15	Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ	0.02	N/m	308.15	Study of the Temperature Dependence of Surface Tensions of Some Alkanol + Hexane Mixtures
γ	0.02	N/m	308.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.02	N/m	313.15	Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ	0.02	N/m	313.15	Surface and bulk behaviour of some (n-hexane + chloroalkane) mixtures
γ	0.02	N/m	313.15	Study of the Temperature Dependence of Surface Tensions of Some Alkanol + Hexane Mixtures
γ	0.02	N/m	313.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.02	N/m	318.15	Interfacial Tensions of Imidazolium-Based Ionic Liquids with N-Alkanes and Cyclohexane
γ	0.02	N/m	328.15	Interfacial Tensions of Imidazolium-Based Ionic Liquids with N-Alkanes and Cyclohexane
λgas	[0.01; 0.01]	W/m×K	[292.90; 322.74]
λgas	0.01	W/m×K	292.90	Thermal conductivity of gaseous and liquid n-hexane
λgas	0.01	W/m×K	296.63	Thermal conductivity of gaseous and liquid n-hexane
λgas	0.01	W/m×K	298.79	Thermal conductivity of gaseous and liquid n-hexane
λgas	0.01	W/m×K	313.06	Thermal conductivity of gaseous and liquid n-hexane
λgas	0.01	W/m×K	322.74	Thermal conductivity of gaseous and liquid n-hexane

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil(P)	340.35	K	96.60	Low cost apparatus for rapid boiling point determination of small air sensitive samples under inert atmosphere

Datasets

1. Molar heat capacity at constant pressure, J/K/mol (1)
2. Viscosity, Pa*s (1)
3. Mass density, kg/m3 (8)
4. Speed of sound, m/s (1)
5. Thermal conductivity, W/m/K (1)

Molar heat capacity at constant pressure, J/K/mol

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
323.15	140.00	203.63
328.15	140.00	205.70
333.15	140.00	207.85
323.15	10090.00	200.62
328.15	10090.00	202.43
333.15	10090.00	204.49
338.15	10090.00	206.13
343.15	10090.00	208.11
348.15	10090.00	210.10
353.15	10090.00	211.91
358.15	10090.00	214.15
363.15	10090.00	216.04
368.15	10090.00	218.37
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
273.15	100.00	0.0004
273.15	10000.00	0.0004
273.15	20000.00	0.0005
273.15	30000.00	0.0005
293.15	100.00	0.0003
293.15	10000.00	0.0003
293.15	20000.00	0.0004
293.15	30000.00	0.0004
313.15	100.00	0.0003
313.15	10000.00	0.0003
313.15	20000.00	0.0003
313.15	30000.00	0.0004
333.15	100.00	0.0002
333.15	10000.00	0.0002
333.15	20000.00	0.0003
333.15	30000.00	0.0003
Reference

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	293.15	659.4
100.00	298.15	654.9
100.00	303.15	650.2
100.00	308.15	645.7
100.00	313.15	640.9
5000.00	293.15	664.8
5000.00	298.15	660.4
5000.00	303.15	655.8
5000.00	308.15	651.5
5000.00	313.15	647.0
10000.00	293.15	669.7
10000.00	298.15	665.5
10000.00	303.15	661.2
10000.00	308.15	657.0
10000.00	313.15	652.8
20000.00	293.15	678.7
20000.00	298.15	674.8
20000.00	303.15	670.8
20000.00	308.15	666.9
20000.00	313.15	663.1
30000.00	293.15	686.9
30000.00	298.15	683.2
30000.00	303.15	679.3
30000.00	308.15	675.8
30000.00	313.15	672.1
40000.00	293.15	694.3
40000.00	298.15	690.7
40000.00	303.15	687.0
40000.00	308.15	683.6
40000.00	313.15	680.2
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.22	1999.00	661.4
293.22	3994.00	663.53
293.22	5999.00	665.43
293.22	8007.00	667.57
293.23	10003.00	669.41
293.23	13000.00	672.26
293.23	16006.00	675.2
293.23	19000.00	677.83
293.22	22004.00	680.38
293.23	25002.00	682.87
293.22	28004.00	685.01
293.23	30001.00	686.72
313.10	2005.00	643.6
313.10	3997.00	645.97
313.10	5999.00	648.24
313.10	8000.00	650.44
313.10	9999.00	652.57
313.10	12997.00	655.73
313.10	15999.00	659.0
313.10	18003.00	661.04
313.10	21999.00	664.77
313.10	24998.00	667.58
313.10	28001.00	670.32
313.10	30004.00	672.03
333.00	2004.00	624.85
333.00	4002.00	627.59
333.00	6003.00	630.29
333.00	8005.00	632.82
333.00	10008.00	635.78
333.00	12998.00	639.36
333.00	16002.00	642.74
333.00	19000.00	646.04
333.00	21993.00	649.32
333.00	25001.00	652.41
333.00	28000.00	655.31
333.00	30005.00	657.29
353.15	2003.00	605.15
353.14	4001.00	608.43
353.15	5997.00	611.57
353.14	8003.00	614.97
353.15	10009.00	618.0
353.15	13000.00	622.08
353.14	15997.00	625.92
353.15	19000.00	629.87
353.14	21998.00	633.46
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
278.15	100.00	673.3
278.15	1000.00	673.9
278.15	5000.00	677.6
278.15	10000.00	681.8
278.15	20000.00	689.6
278.15	30000.00	696.8
278.15	40000.00	703.2
278.15	50000.00	709.2
278.15	60000.00	715.0
298.15	100.00	656.1
298.15	1000.00	655.9
298.15	5000.00	660.1
298.15	10000.00	665.1
298.15	20000.00	673.9
298.15	30000.00	681.9
298.15	40000.00	689.0
298.15	50000.00	695.5
298.15	60000.00	701.7
323.15	100.00	631.7
323.15	1000.00	633.1
323.15	5000.00	638.2
323.15	10000.00	644.2
323.15	20000.00	654.7
323.15	30000.00	663.9
323.15	40000.00	671.9
323.15	50000.00	679.3
323.15	60000.00	686.1
348.15	1000.00	608.5
348.15	5000.00	614.9
348.15	10000.00	622.1
348.15	20000.00	634.6
348.15	30000.00	645.2
348.15	40000.00	654.4
348.15	50000.00	662.6
348.15	60000.00	670.2
373.15	1000.00	582.6
373.15	5000.00	591.0
373.15	10000.00	600.0
373.15	20000.00	614.8
373.15	30000.00	627.0
373.15	40000.00	637.4
373.15	50000.00	646.6
373.15	60000.00	654.9
423.15	1000.00	521.2
423.15	5000.00	536.9
423.15	10000.00	551.5
423.15	20000.00	573.2
423.15	30000.00	589.7
423.15	40000.00	603.2
423.15	50000.00	614.6
423.15	60000.00	624.8
463.15	5000.00	484.2
463.15	10000.00	508.5
463.15	20000.00	538.9
463.15	30000.00	559.8
463.15	40000.00	575.9
463.15	50000.00	589.3
463.15	60000.00	600.7
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.12	1019.00	642.2
313.12	2044.00	643.5
313.12	3023.00	644.6
313.12	4018.00	645.8
313.12	5016.00	647.0
313.12	6012.00	648.1
313.12	7016.00	649.2
313.12	8016.00	650.3
313.12	9020.00	651.4
313.12	10018.00	652.5
313.12	11020.00	653.5
313.12	12004.00	654.6
313.12	13007.00	655.6
313.12	14015.00	656.6
313.12	15006.00	657.6
313.12	16023.00	658.6
313.12	17015.00	659.6
313.12	18011.00	660.5
313.12	19009.00	661.4
313.12	20016.00	662.4
313.12	20995.00	663.3
313.12	22018.00	664.2
313.12	23018.00	665.1
313.12	24013.00	666.0
313.12	25002.00	666.8
323.05	1030.00	633.0
323.05	2010.00	634.3
323.05	3021.00	635.6
323.05	4018.00	636.9
323.05	5014.00	638.1
323.05	6007.00	639.4
323.05	7010.00	640.6
323.05	8012.00	641.8
323.05	9020.00	643.0
323.05	10008.00	644.1
323.05	11021.00	645.2
323.05	12011.00	646.4
323.05	13007.00	647.4
323.05	14007.00	648.5
323.05	15035.00	649.6
323.05	16011.00	650.6
323.05	17021.00	651.6
323.05	18020.00	652.7
323.05	19013.00	653.7
323.05	20001.00	654.6
323.05	21028.00	655.6
323.05	22004.00	656.6
323.05	23010.00	657.5
323.05	24021.00	658.5
323.05	25018.00	659.4
332.85	1020.00	623.5
332.85	2021.00	625.0
332.85	3022.00	626.5
332.85	4020.00	627.8
332.85	5011.00	629.2
332.85	6016.00	630.6
332.85	7012.00	631.9
332.85	8025.00	633.3
332.85	9012.00	634.5
332.85	10010.00	635.7
332.85	11012.00	636.9
332.85	12019.00	638.1
332.85	13007.00	639.2
332.85	14021.00	640.4
332.85	15014.00	641.6
332.85	16025.00	642.8
332.85	17011.00	643.8
332.85	18035.00	644.9
332.85	19014.00	646.0
332.85	20011.00	647.1
332.85	21015.00	648.1
332.85	22000.00	649.1
332.85	23012.00	650.1
332.85	24022.00	651.2
332.85	25030.00	652.2
342.73	1010.00	613.9
342.73	2010.00	615.5
342.73	3011.00	617.1
342.73	4010.00	618.6
342.73	5005.00	620.0
342.73	6031.00	621.6
342.73	7020.00	623.0
342.73	8009.00	624.4
342.73	9015.00	625.7
342.73	10012.00	627.0
342.73	11006.00	628.4
342.73	12014.00	629.7
342.73	13011.00	630.9
342.73	14014.00	632.2
342.73	15008.00	633.4
342.73	16006.00	634.6
342.73	17021.00	635.7
342.73	18016.00	636.9
342.73	19025.00	638.0
342.73	20037.00	639.2
342.73	21025.00	640.3
342.73	22016.00	641.3
342.73	23010.00	642.5
342.73	24023.00	643.5
342.73	25006.00	644.5
352.56	1017.00	604.0
352.56	2028.00	605.8
352.56	3030.00	607.6
352.56	4024.00	609.2
352.56	5022.00	610.9
352.56	6024.00	612.5
352.56	7027.00	614.0
352.56	8021.00	615.5
352.56	9022.00	617.0
352.56	10020.00	618.4
352.56	11023.00	619.9
352.56	12003.00	621.2
352.56	13021.00	622.6
352.56	14012.00	623.9
352.56	15007.00	625.2
352.56	16016.00	626.5
352.56	17012.00	627.7
352.56	18015.00	629.0
352.56	19003.00	630.2
352.56	20040.00	631.4
352.56	21005.00	632.5
352.56	22035.00	633.8
352.56	23002.00	634.8
352.56	24039.00	636.0
352.56	25000.00	637.1
362.40	1029.00	593.8
362.40	2020.00	595.8
362.40	3028.00	597.6
362.40	4029.00	599.5
362.40	5040.00	601.3
362.40	6026.00	602.9
362.40	7026.00	604.7
362.40	8004.00	606.3
362.40	9007.00	607.9
362.40	10009.00	609.4
362.40	11009.00	610.9
362.40	12010.00	612.5
362.40	13000.00	614.0
362.40	14028.00	615.5
362.40	15017.00	616.8
362.40	16014.00	618.1
362.40	17004.00	619.5
362.40	18002.00	620.9
362.40	18988.00	622.1
362.40	20027.00	623.4
362.40	21002.00	624.7
362.40	22018.00	625.9
362.40	23013.00	627.1
362.40	24001.00	628.4
362.40	25000.00	629.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	668.07
283.15	2500.00	670.36
283.15	5000.00	672.69
283.15	10000.00	677.06
283.15	15000.00	681.19
283.15	20000.00	685.08
283.15	25000.00	688.82
283.15	30000.00	692.35
283.15	35000.00	695.65
293.15	100.00	659.18
293.15	2500.00	661.67
293.15	5000.00	664.17
293.15	10000.00	668.87
293.15	15000.00	673.27
293.15	20000.00	677.4
293.15	25000.00	681.33
293.15	30000.00	685.07
293.15	35000.00	688.63
298.15	100.00	654.61
298.15	2500.00	657.21
298.15	5000.00	659.81
298.15	10000.00	664.66
298.15	15000.00	669.24
298.15	20000.00	673.51
298.15	25000.00	677.56
298.15	30000.00	681.4
298.15	35000.00	685.02
303.15	100.00	649.97
303.15	2500.00	652.7
303.15	5000.00	655.36
303.15	10000.00	660.53
303.15	15000.00	665.23
303.15	20000.00	669.63
303.15	25000.00	673.81
303.15	30000.00	677.77
303.15	35000.00	681.45
313.15	100.00	640.82
313.15	2500.00	643.76
313.15	5000.00	646.69
313.15	10000.00	652.13
313.15	15000.00	657.16
313.15	20000.00	661.86
313.15	25000.00	666.28
313.15	30000.00	670.44
313.15	35000.00	674.41
323.15	100.00	631.41
323.15	2500.00	634.61
323.15	5000.00	637.8
323.15	10000.00	643.69
323.15	15000.00	649.12
323.15	20000.00	654.14
323.15	25000.00	658.84
323.15	30000.00	663.23
323.15	35000.00	667.4
333.15	100.00	621.8
333.15	2500.00	625.32
333.15	5000.00	628.77
333.15	10000.00	635.13
333.15	15000.00	640.94
333.15	20000.00	646.27
333.15	25000.00	651.23
333.15	30000.00	655.89
333.15	35000.00	660.3
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
278.15	100.00	670.8
278.15	5000.00	675.9
278.15	10000.00	680.5
278.15	15000.00	683.5
278.15	20000.00	688.7
283.15	100.00	667.5
283.15	5000.00	671.8
283.15	10000.00	676.2
283.15	15000.00	680.7
283.15	20000.00	684.4
288.15	100.00	664.0
288.15	5000.00	668.5
288.15	10000.00	672.9
288.15	15000.00	677.6
288.15	20000.00	681.3
293.15	100.00	658.8
293.15	5000.00	663.7
293.15	10000.00	668.8
293.15	15000.00	672.8
293.15	20000.00	677.4
298.15	100.00	654.2
298.15	5000.00	659.5
298.15	10000.00	664.7
298.15	15000.00	669.2
298.15	20000.00	673.2
303.15	100.00	649.8
303.15	5000.00	655.5
303.15	10000.00	660.2
303.15	15000.00	664.9
303.15	20000.00	669.3
308.15	100.00	645.1
308.15	5000.00	651.1
308.15	10000.00	656.3
308.15	15000.00	661.2
308.15	20000.00	666.0
313.15	100.00	641.3
313.15	5000.00	647.3
313.15	10000.00	652.8
313.15	15000.00	657.4
313.15	20000.00	662.5
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	283.15	668.8
100.00	288.15	664.2
100.00	293.15	659.7
100.00	298.15	655.2
100.00	303.15	650.7
100.00	308.15	646.0
100.00	313.15	641.4
100.00	318.15	636.7
100.00	323.15	631.8
5000.00	283.15	673.2
5000.00	288.15	669.0
5000.00	293.15	664.7
5000.00	298.15	660.3
5000.00	303.15	655.9
5000.00	308.15	651.6
5000.00	313.15	647.2
5000.00	318.15	642.7
5000.00	323.15	638.1
10000.00	283.15	677.6
10000.00	288.15	673.5
10000.00	293.15	669.3
10000.00	298.15	665.2
10000.00	303.15	661.0
10000.00	308.15	656.8
10000.00	313.15	652.6
10000.00	318.15	648.3
10000.00	323.15	644.0
20000.00	283.15	685.7
20000.00	288.15	681.9
20000.00	293.15	678.0
20000.00	298.15	674.1
20000.00	303.15	670.2
20000.00	308.15	666.3
20000.00	313.15	662.4
20000.00	318.15	658.4
20000.00	323.15	654.4
30000.00	283.15	693.1
30000.00	288.15	689.4
30000.00	293.15	685.7
30000.00	298.15	682.1
30000.00	303.15	678.4
30000.00	308.15	674.7
30000.00	313.15	671.0
30000.00	318.15	667.3
30000.00	323.15	663.5
40000.00	283.15	699.8
40000.00	288.15	696.3
40000.00	293.15	692.9
40000.00	298.15	689.3
40000.00	303.15	685.9
40000.00	308.15	682.4
40000.00	313.15	678.9
40000.00	318.15	675.3
40000.00	323.15	671.7
50000.00	283.15	706.1
50000.00	288.15	702.8
50000.00	293.15	699.4
50000.00	298.15	696.1
50000.00	303.15	692.7
50000.00	308.15	689.3
50000.00	313.15	686.0
50000.00	318.15	682.5
50000.00	323.15	679.2
60000.00	283.15	711.5
60000.00	288.15	708.8
60000.00	293.15	705.6
60000.00	298.15	702.4
60000.00	303.15	699.1
60000.00	308.15	695.8
60000.00	313.15	692.7
60000.00	318.15	689.3
60000.00	323.15	686.0
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	20.22	654.96
Reference

Speed of sound, m/s

Fixed		Measured
Temperature, K - Fluid (supercritical or subcritical phases)	Pressure, kPa - Fluid (supercritical or subcritical phases)	Speed of sound, m/s - Fluid (supercritical or subcritical phases)
509.17	3500.00	162.1
511.69	3500.00	138.7
514.46	3500.00	112.5
517.72	3500.00	95.8
519.87	3500.00	100.4
523.79	3500.00	112.7
527.85	3500.00	120.4
533.83	3500.00	134.2
538.84	3500.00	140.1
543.69	3500.00	145.3
548.31	3500.00	149.2
553.10	3500.00	155.1
558.44	3500.00	161.5
562.56	3500.00	164.9
568.21	3500.00	168.8
574.58	3500.00	174.8
578.77	3500.00	177.5
584.09	3500.00	183.0
588.59	3500.00	186.5
594.05	3500.00	188.6
598.83	3500.00	192.2
603.41	3500.00	195.9
608.96	3500.00	198.5
614.50	3500.00	203.1
618.79	3500.00	204.3
624.52	3500.00	206.1
629.29	3500.00	209.3
573.18	5500.00	150.0
578.22	5500.00	154.0
582.79	5500.00	157.3
588.07	5500.00	160.4
592.61	5500.00	164.2
597.98	5500.00	169.1
602.85	5500.00	172.0
608.05	5500.00	178.0
612.50	5500.00	180.2
618.05	5500.00	184.3
622.80	5500.00	186.5
628.11	5500.00	190.4
633.07	5500.00	193.6
636.04	5500.00	195.0
509.44	6500.00	331.1
511.27	6500.00	324.2
514.43	6500.00	314.1
517.58	6500.00	303.6
520.46	6500.00	289.0
523.63	6500.00	278.2
528.58	6500.00	263.2
533.48	6500.00	248.1
538.58	6500.00	231.5
543.14	6500.00	219.9
548.14	6500.00	207.4
553.55	6500.00	194.1
559.79	6500.00	180.9
633.86	3500.00	210.4
637.99	3500.00	211.6
509.40	4500.00	243.8
511.26	4500.00	232.7
514.50	4500.00	216.4
517.47	4500.00	201.9
520.36	4500.00	183.7
523.40	4500.00	168.4
527.66	4500.00	155.0
533.30	4500.00	131.7
538.14	4500.00	125.0
543.00	4500.00	125.6
547.96	4500.00	130.2
553.60	4500.00	134.9
558.48	4500.00	139.2
562.44	4500.00	142.8
567.95	4500.00	150.6
573.36	4500.00	155.7
578.08	4500.00	161.3
582.93	4500.00	164.7
587.91	4500.00	170.5
593.04	4500.00	174.8
597.84	4500.00	178.5
602.73	4500.00	181.2
608.03	4500.00	183.5
612.70	4500.00	187.0
617.91	4500.00	193.6
623.06	4500.00	195.6
628.15	4500.00	198.3
563.76	6500.00	171.7
568.59	6500.00	169.0
573.51	6500.00	165.9
578.65	6500.00	167.9
583.09	6500.00	165.5
588.45	6500.00	166.4
592.78	6500.00	168.5
598.14	6500.00	168.6
603.05	6500.00	173.4
608.12	6500.00	175.1
612.69	6500.00	179.7
618.21	6500.00	182.0
622.49	6500.00	184.8
628.16	6500.00	189.0
632.99	6500.00	192.3
635.50	6500.00	194.3
509.67	7500.00	361.3
511.34	7500.00	355.3
514.25	7500.00	347.2
517.46	7500.00	336.8
520.19	7500.00	328.5
523.93	7500.00	316.5
528.42	7500.00	304.2
533.43	7500.00	285.3
538.81	7500.00	270.8
543.52	7500.00	259.9
548.56	7500.00	248.3
553.44	7500.00	235.1
560.33	7500.00	222.2
632.52	4500.00	202.1
636.79	4500.00	204.9
509.57	5500.00	291.1
511.22	5500.00	286.1
514.60	5500.00	272.0
517.82	5500.00	260.2
520.54	5500.00	245.2
523.89	5500.00	229.4
528.22	5500.00	210.9
533.62	5500.00	194.1
538.33	5500.00	174.8
543.21	5500.00	165.4
547.89	5500.00	158.2
554.09	5500.00	150.9
558.90	5500.00	144.8
563.13	5500.00	143.4
568.40	5500.00	146.5
563.92	7500.00	215.1
568.54	7500.00	205.6
573.12	7500.00	201.1
579.07	7500.00	191.7
583.30	7500.00	190.5
589.01	7500.00	188.8
593.24	7500.00	187.8
598.52	7500.00	186.2
603.44	7500.00	186.0
608.49	7500.00	185.6
613.43	7500.00	187.8
618.56	7500.00	190.1
622.59	7500.00	191.0
628.12	7500.00	194.6
633.06	7500.00	196.8
635.27	7500.00	198.0
Reference

Thermal conductivity, W/m/K

Fixed		Measured
Temperature, K - Fluid (supercritical or subcritical phases)	Pressure, kPa - Fluid (supercritical or subcritical phases)	Thermal conductivity, W/m/K - Fluid (supercritical or subcritical phases)
508.17	2949.00	0.0646
508.17	2953.00	0.0651
508.17	2956.00	0.0651
508.17	2963.00	0.0660
508.17	2966.00	0.0663
508.17	2970.00	0.0668
508.17	2974.00	0.0673
508.17	2979.00	0.0683
508.17	2982.00	0.0687
508.17	2990.00	0.0704
508.17	2991.00	0.0707
508.17	2995.00	0.0713
508.17	2998.00	0.0722
508.17	3002.00	0.0732
508.17	3007.00	0.0744
508.17	3009.00	0.0749
508.17	3013.00	0.0758
508.17	3015.00	0.0765
508.17	3017.00	0.0770
508.17	3021.00	0.0782
508.17	3022.00	0.0785
508.17	3024.00	0.0792
508.17	3026.00	0.0799
508.17	3029.00	0.0807
508.17	3031.00	0.0819
508.17	3033.00	0.0829
508.17	3034.00	0.0834
508.17	3036.00	0.0847
508.17	3037.00	0.0847
508.17	3038.00	0.0860
508.17	3039.00	0.0857
508.17	3040.00	0.0873
508.17	3041.00	0.0865
508.17	3041.00	0.0882
508.17	3042.00	0.0910
508.17	3043.00	0.0920
508.17	3045.00	0.0940
508.17	3046.00	0.0950
508.17	3047.00	0.0961
508.17	3048.00	0.0983
508.17	3049.00	0.0994
508.17	3050.00	0.1017
508.17	3051.00	0.1048
508.17	3052.00	0.1081
508.17	3053.00	0.1119
508.17	3054.00	0.1168
508.17	3055.00	0.1226
508.17	3056.00	0.1319
508.17	3057.00	0.1487
508.17	3058.00	0.1625
508.17	3059.00	0.1438
508.17	3060.00	0.1319
508.17	3061.00	0.1231
508.17	3062.00	0.1168
508.17	3063.00	0.1123
508.17	3064.00	0.1088
508.17	3065.00	0.1060
508.17	3066.00	0.1039
508.17	3067.00	0.1024
508.17	3068.00	0.1006
508.17	3069.00	0.0994
508.17	3070.00	0.0983
508.17	3071.00	0.0974
508.17	3073.00	0.0961
508.17	3074.00	0.0951
508.17	3075.00	0.0946
508.17	3076.00	0.0940
508.17	3077.00	0.0932
508.17	3078.00	0.0929
508.17	3079.00	0.0924
508.17	3080.00	0.0917
508.17	3081.00	0.0913
508.17	3082.00	0.0908
508.17	3083.00	0.0903
508.17	3084.00	0.0898
508.17	3085.00	0.0896
508.17	3086.00	0.0889
508.17	3087.00	0.0885
508.17	3088.00	0.0880
508.17	3089.00	0.0876
508.17	3090.00	0.0876
508.17	3091.00	0.0871
508.17	3092.00	0.0867
508.17	3094.00	0.0858
508.17	3095.00	0.0854
508.17	3100.00	0.0833
508.17	3105.00	0.0827
508.17	3108.00	0.0822
508.17	3115.00	0.0812
508.17	3120.00	0.0803
508.17	3125.00	0.0803
508.17	3130.00	0.0803
508.17	3132.00	0.0803
508.92	900.00	0.0377
508.92	1100.00	0.0386
508.92	1234.00	0.0389
508.92	1401.00	0.0393
508.92	1510.00	0.0396
508.92	1603.00	0.0400
508.92	1710.00	0.0403
508.92	1806.00	0.0407
508.92	1908.00	0.0412
508.92	2006.00	0.0417
508.92	2111.00	0.0425
508.92	2210.00	0.0430
508.92	2300.00	0.0435
508.92	2409.00	0.0446
508.92	2509.00	0.0458
508.92	2600.00	0.0470
508.92	2650.00	0.0478
508.92	2726.00	0.0491
508.92	2744.00	0.0494
508.92	2752.00	0.0496
508.92	2763.00	0.0499
508.92	2847.00	0.0526
508.92	2898.00	0.0543
508.92	2902.00	0.0546
508.92	2927.00	0.0557
508.92	2955.00	0.0575
508.92	2968.00	0.0589
508.92	2975.00	0.0595
508.92	2985.00	0.0603
508.92	2988.00	0.0609
508.92	2992.00	0.0612
508.92	2999.00	0.0620
508.92	3004.00	0.0625
508.92	3011.00	0.0634
508.92	3015.00	0.0643
508.92	3019.00	0.0648
508.92	3025.00	0.0657
508.92	3028.00	0.0662
508.92	3033.00	0.0675
508.92	3035.00	0.0680
508.92	3039.00	0.0686
508.92	3042.00	0.0694
508.92	3044.00	0.0699
508.92	3048.00	0.0711
508.92	3050.00	0.0715
508.92	3052.00	0.0722
508.92	3055.00	0.0734
508.92	3056.00	0.0737
508.92	3059.00	0.0747
508.92	3060.00	0.0753
508.92	3063.00	0.0763
508.92	3065.00	0.0775
508.92	3067.00	0.0787
508.92	3068.00	0.0790
508.92	3069.00	0.0801
508.92	3070.00	0.0805
508.92	3071.00	0.0808
508.92	3073.00	0.0825
508.92	3074.00	0.0835
508.92	3075.00	0.0841
508.92	3076.00	0.0853
508.92	3077.00	0.0859
508.92	3078.00	0.0870
508.92	3079.00	0.0880
508.92	3080.00	0.0893
508.92	3081.00	0.0907
508.92	3082.00	0.0923
508.92	3083.00	0.0938
508.92	3084.00	0.0957
508.92	3085.00	0.0977
508.92	3086.00	0.1001
508.92	3087.00	0.1030
508.92	3088.00	0.1061
508.92	3089.00	0.1087
508.92	3090.00	0.1096
508.92	3091.00	0.1100
508.92	3092.00	0.1093
508.92	3093.00	0.1071
508.92	3094.00	0.1049
508.92	3095.00	0.1028
508.92	3096.00	0.1010
508.92	3097.00	0.0987
508.92	3098.00	0.0967
508.92	3099.00	0.0947
508.92	3100.00	0.0936
508.92	3101.00	0.0922
508.92	3102.00	0.0913
508.92	3103.00	0.0905
508.92	3104.00	0.0892
508.92	3105.00	0.0884
508.92	3106.00	0.0875
508.92	3107.00	0.0871
508.92	3108.00	0.0867
508.92	3109.00	0.0860
508.92	3110.00	0.0854
508.92	3111.00	0.0850
508.92	3112.00	0.0846
508.92	3113.00	0.0840
508.92	3114.00	0.0832
508.92	3115.00	0.0832
508.92	3120.00	0.0812
508.92	3125.00	0.0798
508.92	3130.00	0.0787
508.92	3135.00	0.0776
508.92	3140.00	0.0766
508.92	3145.00	0.0760
508.92	3150.00	0.0756
508.92	3155.00	0.0746
508.92	3159.00	0.0746
508.92	3160.00	0.0743
508.92	3165.00	0.0740
508.92	3170.00	0.0736
508.92	3175.00	0.0731
508.92	3180.00	0.0731
508.92	3185.00	0.0728
508.92	3190.00	0.0725
508.92	3195.00	0.0722
508.92	3200.00	0.0723
508.92	3205.00	0.0719
508.92	3215.00	0.0716
508.92	3220.00	0.0713
508.92	3225.00	0.0713
508.92	3230.00	0.0711
508.92	3235.00	0.0710
508.92	3240.00	0.0709
508.92	3245.00	0.0708
508.92	3250.00	0.0710
508.92	3255.00	0.0710
508.92	3260.00	0.0710
508.92	3265.00	0.0707
508.92	3270.00	0.0707
508.92	3275.00	0.0707
508.92	3280.00	0.0707
508.92	3285.00	0.0707
508.92	3290.00	0.0704
508.92	3295.00	0.0704
508.92	3300.00	0.0704
508.92	3310.00	0.0704
508.92	3320.00	0.0707
508.92	3330.00	0.0707
508.92	3340.00	0.0707
508.92	3350.00	0.0707
508.92	3355.00	0.0704
508.92	3360.00	0.0704
508.92	3365.00	0.0704
508.92	3370.00	0.0704
508.92	3375.00	0.0704
508.92	3380.00	0.0704
508.92	3385.00	0.0704
508.92	3390.00	0.0701
508.92	3395.00	0.0701
508.92	3500.00	0.0701
508.92	3535.00	0.0701
508.92	3540.00	0.0701
508.92	3545.00	0.0698
508.92	3550.00	0.0704
508.92	3555.00	0.0704
508.92	3560.00	0.0704
508.92	3565.00	0.0704
508.92	3570.00	0.0704
508.92	3605.00	0.0698
508.92	3670.00	0.0698
508.92	3690.00	0.0698
508.92	3700.00	0.0707
508.92	3900.00	0.0707
508.92	4000.00	0.0707
508.92	4300.00	0.0713
508.92	4400.00	0.0716
508.92	4500.00	0.0719
508.92	4600.00	0.0722
508.92	4700.00	0.0722
508.92	4800.00	0.0725
508.92	4900.00	0.0725
508.92	5000.00	0.0728
508.92	5100.00	0.0728
508.92	5200.00	0.0734
508.92	5300.00	0.0734
508.92	5400.00	0.0734
508.92	5500.00	0.0737
508.92	5600.00	0.0744
508.92	5800.00	0.0744
508.92	6000.00	0.0744
508.92	6100.00	0.0744
508.92	6200.00	0.0747
508.92	6400.00	0.0750
508.92	6500.00	0.0753
508.92	7000.00	0.0763
508.92	7500.00	0.0770
508.92	8000.00	0.0777
508.92	8500.00	0.0777
508.92	9000.00	0.0783
508.92	9500.00	0.0791
508.92	10000.00	0.0795
509.85	2686.00	0.0464
509.85	2700.00	0.0467
509.85	2710.00	0.0466
509.85	2720.00	0.0471
509.85	2730.00	0.0472
509.85	2740.00	0.0473
509.85	2750.00	0.0476
509.85	2760.00	0.0479
509.85	2770.00	0.0481
509.85	2780.00	0.0483
509.85	2790.00	0.0484
509.85	2800.00	0.0485
509.85	2805.00	0.0487
509.85	2810.00	0.0488
509.85	2815.00	0.0491
509.85	2820.00	0.0493
509.85	2825.00	0.0494
509.85	2830.00	0.0495
509.85	2835.00	0.0497
509.85	2840.00	0.0496
509.85	2845.00	0.0497
509.85	2850.00	0.0499
509.85	2855.00	0.0500
509.85	2860.00	0.0502
509.85	2865.00	0.0503
509.85	2870.00	0.0505
509.85	2875.00	0.0506
509.85	2880.00	0.0508
509.85	2885.00	0.0512
509.85	2890.00	0.0512
509.85	2895.00	0.0514
509.85	2900.00	0.0515
509.85	2905.00	0.0517
509.85	2910.00	0.0519
509.85	2915.00	0.0522
509.85	2920.00	0.0524
509.85	2925.00	0.0526
509.85	2930.00	0.0529
509.85	2935.00	0.0531
509.85	2940.00	0.0533
509.85	2945.00	0.0534
509.85	2950.00	0.0538
509.85	2955.00	0.0539
509.85	2960.00	0.0543
509.85	2965.00	0.0547
509.85	2970.00	0.0550
509.85	2975.00	0.0556
509.85	2980.00	0.0556
509.85	2985.00	0.0559
509.85	2990.00	0.0559
509.85	2995.00	0.0565
509.85	3000.00	0.0569
509.85	3005.00	0.0575
509.85	3010.00	0.0579
509.85	3015.00	0.0583
509.85	3020.00	0.0587
509.85	3025.00	0.0597
509.85	3030.00	0.0597
509.85	3035.00	0.0597
509.85	3040.00	0.0609
509.85	3045.00	0.0613
509.85	3050.00	0.0618
509.85	3055.00	0.0626
509.85	3060.00	0.0630
509.85	3065.00	0.0643
509.85	3070.00	0.0651
509.85	3080.00	0.0670
509.85	3085.00	0.0681
509.85	3090.00	0.0696
509.85	3095.00	0.0714
509.85	3100.00	0.0733
509.85	3105.00	0.0757
509.85	3110.00	0.0775
509.85	3115.00	0.0810
509.85	3120.00	0.0857
509.85	3125.00	0.0893
509.85	3130.00	0.0910
509.85	3135.00	0.0920
509.85	3140.00	0.0883
509.85	3145.00	0.0851
509.85	3150.00	0.0829
509.85	3155.00	0.0815
509.85	3160.00	0.0798
509.85	3170.00	0.0775
509.85	3180.00	0.0765
509.85	3190.00	0.0751
509.85	3200.00	0.0744
509.85	3210.00	0.0737
509.85	3220.00	0.0732
509.85	3230.00	0.0726
509.85	3240.00	0.0725
509.85	3250.00	0.0721
509.85	3260.00	0.0718
509.85	3270.00	0.0718
509.85	3280.00	0.0714
509.85	3290.00	0.0713
509.85	3300.00	0.0709
509.85	3310.00	0.0710
509.85	3320.00	0.0705
509.85	3330.00	0.0703
509.85	3340.00	0.0699
509.85	3390.00	0.0699
509.85	3400.00	0.0699
509.85	3450.00	0.0695
509.85	3500.00	0.0696
509.85	3600.00	0.0698
509.85	3800.00	0.0703
509.85	4000.00	0.0706
509.85	4200.00	0.0711
509.85	4400.00	0.0713
509.85	4600.00	0.0718
509.85	4800.00	0.0722
509.85	5000.00	0.0725
509.85	5200.00	0.0728
509.85	5400.00	0.0732
509.85	5600.00	0.0736
509.85	5800.00	0.0739
509.85	6000.00	0.0742
509.85	6200.00	0.0745
509.85	6400.00	0.0748
509.85	6600.00	0.0751
509.85	6800.00	0.0754
509.85	7000.00	0.0757
509.85	7200.00	0.0760
509.85	7400.00	0.0762
509.85	7600.00	0.0765
509.85	7800.00	0.0767
509.85	8000.00	0.0768
509.85	8200.00	0.0770
509.85	8500.00	0.0774
509.85	9000.00	0.0780
509.85	9500.00	0.0786
509.85	10000.00	0.0791
510.36	245.00	0.0379
510.36	1000.00	0.0385
510.36	2245.00	0.0418
510.36	2715.00	0.0466
510.36	3110.00	0.0680
510.36	3112.00	0.0682
510.36	3114.00	0.0688
510.36	3116.00	0.0694
510.36	3118.00	0.0703
510.36	3120.00	0.0709
510.36	3122.00	0.0715
510.36	3124.00	0.0724
510.36	3126.00	0.0734
510.36	3128.00	0.0740
510.36	3130.00	0.0747
510.36	3132.00	0.0754
510.36	3133.00	0.0761
510.36	3134.00	0.0762
510.36	3137.00	0.0784
510.36	3138.00	0.0791
510.36	3139.00	0.0799
510.36	3140.00	0.0806
510.36	3141.00	0.0812
510.36	3142.00	0.0820
510.36	3143.00	0.0827
510.36	3144.00	0.0833
510.36	3145.00	0.0839
510.36	3146.00	0.0846
510.36	3147.00	0.0850
510.36	3148.00	0.0855
510.36	3150.00	0.0863
510.36	3151.00	0.0866
510.36	3152.00	0.0867
510.36	3153.00	0.0869
510.36	3154.00	0.0871
510.36	3155.00	0.0870
510.36	3156.00	0.0869
510.36	3157.00	0.0868
510.36	3158.00	0.0866
510.36	3159.00	0.0863
510.36	3160.00	0.0860
510.36	3161.00	0.0858
510.36	3162.00	0.0855
510.36	3163.00	0.0852
510.36	3164.00	0.0848
510.36	3166.00	0.0839
510.36	3168.00	0.0832
510.36	3170.00	0.0825
510.36	3172.00	0.0817
510.36	3174.00	0.0809
510.36	3176.00	0.0802
510.36	3178.00	0.0794
510.36	3180.00	0.0788
510.36	3182.00	0.0783
510.36	3184.00	0.0777
510.36	3186.00	0.0772
510.36	3188.00	0.0765
510.36	3190.00	0.0760
510.36	3192.00	0.0756
510.36	3194.00	0.0752
510.36	3196.00	0.0749
510.36	3198.00	0.0745
510.36	3200.00	0.0742
510.36	3202.00	0.0738
510.36	3204.00	0.0736
510.36	3206.00	0.0734
510.36	3208.00	0.0731
510.36	3210.00	0.0729
510.36	3212.00	0.0727
510.36	3214.00	0.0724
510.36	3216.00	0.0724
510.36	3218.00	0.0721
510.36	3220.00	0.0721
510.36	3222.00	0.0719
510.36	3225.00	0.0717
510.36	3228.00	0.0716
510.36	3230.00	0.0716
510.36	3232.00	0.0714
510.36	3234.00	0.0713
510.36	3236.00	0.0712
510.36	3238.00	0.0712
510.36	3242.00	0.0711
510.36	3245.00	0.0711
510.36	3248.00	0.0711
510.36	3250.00	0.0707
510.36	3252.00	0.0707
510.36	3254.00	0.0707
510.36	3256.00	0.0704
510.36	3258.00	0.0704
510.36	3260.00	0.0704
510.36	3265.00	0.0704
510.36	3270.00	0.0701
510.36	3280.00	0.0698
510.36	3290.00	0.0696
510.36	3300.00	0.0694
510.36	3310.00	0.0694
510.36	3320.00	0.0691
510.36	3340.00	0.0688
510.36	3350.00	0.0685
510.36	3360.00	0.0685
510.36	3370.00	0.0685
510.36	3380.00	0.0685
510.36	3392.00	0.0683
510.36	3450.00	0.0682
510.36	3500.00	0.0685
510.36	3520.00	0.0686
510.36	3540.00	0.0686
510.36	3560.00	0.0686
510.36	3580.00	0.0686
510.36	3600.00	0.0685
510.36	3620.00	0.0685
510.36	3640.00	0.0685
510.36	3650.00	0.0686
510.36	3670.00	0.0686
510.36	3680.00	0.0686
510.36	3700.00	0.0686
510.36	3720.00	0.0687
510.36	3740.00	0.0688
510.36	3750.00	0.0689
510.36	3800.00	0.0691
510.36	3810.00	0.0692
510.36	3820.00	0.0692
510.36	3830.00	0.0692
510.36	3840.00	0.0692
510.36	3860.00	0.0693
510.36	3970.00	0.0697
510.36	3980.00	0.0696
510.36	4010.00	0.0698
511.55	900.00	0.0385
511.55	1000.00	0.0382
511.55	1100.00	0.0383
511.55	1200.00	0.0386
511.55	1300.00	0.0388
511.55	1400.00	0.0389
511.55	1500.00	0.0391
511.55	1600.00	0.0393
511.55	1700.00	0.0397
511.55	1800.00	0.0401
511.55	1900.00	0.0405
511.55	2000.00	0.0409
511.55	2100.00	0.0413
511.55	2200.00	0.0419
511.55	2300.00	0.0425
511.55	2400.00	0.0434
511.55	2462.00	0.0439
511.55	2466.00	0.0439
511.55	2500.00	0.0443
511.55	2600.00	0.0453
511.55	2700.00	0.0466
511.55	2800.00	0.0485
511.55	2900.00	0.0508
511.55	2973.00	0.0529
511.55	2988.00	0.0536
511.55	3050.00	0.0556
511.55	3065.00	0.0563
511.55	3084.00	0.0578
511.55	3096.00	0.0591
511.55	3103.00	0.0597
511.55	3110.00	0.0606
511.55	3116.00	0.0613
511.55	3130.00	0.0634
511.55	3140.00	0.0651
511.55	3145.00	0.0659
511.55	3150.00	0.0668
511.55	3155.00	0.0679
511.55	3160.00	0.0688
511.55	3165.00	0.0699
511.55	3168.00	0.0706
511.55	3170.00	0.0710
511.55	3173.00	0.0718
511.55	3175.00	0.0723
511.55	3180.00	0.0734
511.55	3183.00	0.0740
511.55	3185.00	0.0745
511.55	3187.00	0.0750
511.55	3190.00	0.0757
511.55	3192.00	0.0762
511.55	3193.00	0.0763
511.55	3195.00	0.0767
511.55	3200.00	0.0776
511.55	3205.00	0.0782
511.55	3212.00	0.0787
511.55	3220.00	0.0787
511.55	3225.00	0.0785
511.55	3230.00	0.0777
511.55	3235.00	0.0770
511.55	3240.00	0.0764
511.55	3245.00	0.0757
511.55	3250.00	0.0751
511.55	3255.00	0.0739
511.55	3260.00	0.0727
511.55	3265.00	0.0715
511.55	3270.00	0.0715
511.55	3275.00	0.0721
511.55	3280.00	0.0721
511.55	3285.00	0.0721
511.55	3290.00	0.0727
511.55	3295.00	0.0727
511.55	3300.00	0.0715
511.55	3305.00	0.0715
511.55	3310.00	0.0715
511.55	3315.00	0.0709
511.55	3325.00	0.0709
511.55	3330.00	0.0709
511.55	3335.00	0.0714
511.55	3340.00	0.0714
511.55	3345.00	0.0714
511.55	3350.00	0.0714
511.55	3360.00	0.0709
511.55	3365.00	0.0709
511.55	3370.00	0.0703
511.55	3375.00	0.0703
511.55	3385.00	0.0703
511.55	3395.00	0.0703
511.55	3400.00	0.0703
511.55	3410.00	0.0709
511.55	3450.00	0.0708
511.55	3455.00	0.0708
511.55	3455.00	0.0708
511.55	3460.00	0.0706
511.55	3460.00	0.0706
511.55	3470.00	0.0706
511.55	3480.00	0.0705
511.55	3490.00	0.0705
511.55	3500.00	0.0703
511.55	3550.00	0.0701
511.55	3600.00	0.0700
511.55	3650.00	0.0699
511.55	3700.00	0.0699
511.55	3750.00	0.0697
511.55	3800.00	0.0696
511.55	3850.00	0.0698
511.55	3900.00	0.0699
511.55	3950.00	0.0699
511.55	4000.00	0.0699
511.55	4100.00	0.0701
511.55	4150.00	0.0701
511.55	4300.00	0.0702
511.55	4400.00	0.0705
511.55	4500.00	0.0705
511.55	4600.00	0.0708
511.55	4700.00	0.0711
511.55	4800.00	0.0711
511.55	5000.00	0.0716
511.55	5100.00	0.0716
511.55	5300.00	0.0722
511.55	5500.00	0.0724
511.55	5800.00	0.0728
511.55	6000.00	0.0731
511.55	6200.00	0.0734
511.55	6400.00	0.0737
511.55	6600.00	0.0741
511.55	6800.00	0.0744
511.55	6900.00	0.0746
511.55	7100.00	0.0748
511.55	7200.00	0.0750
511.55	7300.00	0.0751
511.55	7500.00	0.0762
511.55	7800.00	0.0766
511.55	8000.00	0.0769
511.55	8200.00	0.0771
511.55	8300.00	0.0772
511.55	8400.00	0.0773
511.55	8500.00	0.0775
511.55	8600.00	0.0776
511.55	8700.00	0.0777
511.55	9000.00	0.0780
511.55	9100.00	0.0781
511.55	9200.00	0.0782
511.55	9300.00	0.0783
511.55	9400.00	0.0784
511.55	9700.00	0.0787
511.55	10000.00	0.0790
511.79	1600.00	0.0396
511.79	1800.00	0.0401
511.79	1900.00	0.0405
511.79	2000.00	0.0410
511.79	2090.00	0.0413
511.79	2100.00	0.0415
511.79	2110.00	0.0415
511.79	2200.00	0.0420
511.79	2300.00	0.0427
511.79	2400.00	0.0435
511.79	2500.00	0.0443
511.79	2600.00	0.0454
511.79	2700.00	0.0466
511.79	2800.00	0.0482
511.79	2817.00	0.0486
511.79	2911.00	0.0508
511.79	2958.00	0.0520
511.79	2987.00	0.0528
511.79	3000.00	0.0534
511.79	3049.00	0.0556
511.79	3076.00	0.0573
511.79	3093.00	0.0587
511.79	3101.00	0.0593
511.79	3113.00	0.0604
511.79	3121.00	0.0613
511.79	3133.00	0.0627
511.79	3143.00	0.0641
511.79	3151.00	0.0654
511.79	3156.00	0.0661
511.79	3163.00	0.0674
511.79	3167.00	0.0681
511.79	3169.00	0.0685
511.79	3172.00	0.0691
511.79	3175.00	0.0696
511.79	3177.00	0.0701
511.79	3179.00	0.0705
511.79	3181.00	0.0709
511.79	3183.00	0.0713
511.79	3185.00	0.0717
511.79	3186.00	0.0719
511.79	3188.00	0.0723
511.79	3189.00	0.0726
511.79	3190.00	0.0727
511.79	3191.00	0.0730
511.79	3192.00	0.0732
511.79	3193.00	0.0734
511.79	3194.00	0.0737
511.79	3195.00	0.0738
511.79	3196.00	0.0740
511.79	3197.00	0.0742
511.79	3198.00	0.0745
511.79	3199.00	0.0746
511.79	3200.00	0.0748
511.79	3202.00	0.0753
511.79	3204.00	0.0756
511.79	3205.00	0.0758
511.79	3206.00	0.0760
511.79	3209.00	0.0764
511.79	3212.00	0.0768
511.79	3214.00	0.0770
511.79	3216.00	0.0772
511.79	3219.00	0.0775
511.79	3221.00	0.0775
511.79	3223.00	0.0776
511.79	3226.00	0.0776
511.79	3231.00	0.0777
511.79	3234.00	0.0777
511.79	3236.00	0.0775
511.79	3237.00	0.0775
511.79	3240.00	0.0773
511.79	3243.00	0.0770
511.79	3246.00	0.0766
511.79	3247.00	0.0763
511.79	3247.00	0.0763
511.79	3251.00	0.0750
511.79	3253.00	0.0750
511.79	3256.00	0.0746
511.79	3257.00	0.0743
511.79	3264.00	0.0740
511.79	3265.00	0.0737
511.79	3269.00	0.0734
511.79	3270.00	0.0734
511.79	3276.00	0.0734
511.79	3278.00	0.0734
511.79	3280.00	0.0734
511.79	3285.00	0.0734
511.79	3291.00	0.0724
511.79	3293.00	0.0724
511.79	3295.00	0.0724
511.79	3300.00	0.0721
511.79	3301.00	0.0718
511.79	3306.00	0.0718
511.79	3310.00	0.0715
511.79	3313.00	0.0712
511.79	3315.00	0.0712
511.79	3319.00	0.0712
511.79	3321.00	0.0712
511.79	3325.00	0.0712
511.79	3327.00	0.0712
511.79	3330.00	0.0712
511.79	3332.00	0.0712
511.79	3335.00	0.0712
511.79	3340.00	0.0712
511.79	3346.00	0.0712
511.79	3350.00	0.0712
511.79	3353.00	0.0712
511.79	3355.00	0.0712
511.79	3360.00	0.0712
511.79	3365.00	0.0706
511.79	3367.00	0.0706
511.79	3368.00	0.0706
511.79	3370.00	0.0706
511.79	3375.00	0.0706
511.79	3380.00	0.0706
511.79	3385.00	0.0706
511.79	3390.00	0.0706
511.79	3395.00	0.0706
511.79	3400.00	0.0706
511.79	3410.00	0.0706
511.79	3420.00	0.0707
511.79	3440.00	0.0707
511.79	3460.00	0.0707
511.79	3500.00	0.0704
511.79	3600.00	0.0699
511.79	3657.00	0.0698
511.79	3700.00	0.0697
511.79	3750.00	0.0697
511.79	3800.00	0.0697
511.79	3850.00	0.0697
511.79	3900.00	0.0697
511.79	3950.00	0.0698
511.79	3980.00	0.0698
511.79	4000.00	0.0699
511.79	4030.00	0.0699
511.79	4100.00	0.0701
511.79	4180.00	0.0704
511.79	4190.00	0.0703
511.79	4200.00	0.0703
511.79	4400.00	0.0710
511.79	4600.00	0.0716
511.79	4800.00	0.0718
511.79	5400.00	0.0730
511.79	6000.00	0.0740
511.79	7000.00	0.0757
511.79	8000.00	0.0770
511.79	9000.00	0.0781
511.79	10000.00	0.0792
513.09	2634.00	0.0455
513.09	2645.00	0.0456
513.09	2653.00	0.0457
513.09	2654.00	0.0457
513.09	2655.00	0.0457
513.09	2661.00	0.0459
513.09	2722.00	0.0455
513.09	2740.00	0.0468
513.09	2760.00	0.0471
513.09	2763.00	0.0470
513.09	2839.00	0.0483
513.09	2849.00	0.0486
513.09	2879.00	0.0492
513.09	2894.00	0.0493
513.09	2909.00	0.0496
513.09	2931.00	0.0501
513.09	2953.00	0.0505
513.09	2983.00	0.0515
513.09	3010.00	0.0524
513.09	3034.00	0.0532
513.09	3054.00	0.0539
513.09	3098.00	0.0560
513.09	3114.00	0.0568
513.09	3152.00	0.0594
513.09	3163.00	0.0604
513.09	3169.00	0.0609
513.09	3176.00	0.0615
513.09	3180.00	0.0622
513.09	3184.00	0.0626
513.09	3186.00	0.0629
513.09	3193.00	0.0631
513.09	3195.00	0.0631
513.09	3200.00	0.0633
513.09	3205.00	0.0643
513.09	3207.00	0.0650
513.09	3212.00	0.0660
513.09	3216.00	0.0665
513.09	3231.00	0.0690
513.09	3232.00	0.0692
513.09	3234.00	0.0694
513.09	3235.00	0.0695
513.09	3236.00	0.0697
513.09	3237.00	0.0699
513.09	3238.00	0.0700
513.09	3240.00	0.0702
513.09	3242.00	0.0705
513.09	3243.00	0.0707
513.09	3244.00	0.0708
513.09	3246.00	0.0711
513.09	3247.00	0.0712
513.09	3248.00	0.0713
513.09	3249.00	0.0715
513.09	3251.00	0.0717
513.09	3252.00	0.0718
513.09	3253.00	0.0720
513.09	3254.00	0.0721
513.09	3255.00	0.0723
513.09	3256.00	0.0724
513.09	3257.00	0.0726
513.09	3258.00	0.0727
513.09	3260.00	0.0728
513.09	3261.00	0.0730
513.09	3261.00	0.0730
513.09	3262.00	0.0731
513.09	3263.00	0.0732
513.09	3265.00	0.0734
513.09	3266.00	0.0735
513.09	3267.00	0.0735
513.09	3274.00	0.0741
513.09	3277.00	0.0743
513.09	3279.00	0.0743
513.09	3280.00	0.0744
513.09	3282.00	0.0745
513.09	3284.00	0.0745
513.09	3287.00	0.0745
513.09	3288.00	0.0746
513.09	3290.00	0.0746
513.09	3292.00	0.0746
513.09	3292.00	0.0746
513.09	3295.00	0.0747
513.09	3298.00	0.0746
513.09	3303.00	0.0746
513.09	3306.00	0.0744
513.09	3310.00	0.0733
513.09	3312.00	0.0733
513.09	3313.00	0.0723
513.09	3318.00	0.0723
513.09	3319.00	0.0723
513.09	3322.00	0.0723
513.09	3326.00	0.0723
513.09	3330.00	0.0723
513.09	3331.00	0.0723
513.09	3332.00	0.0723
513.09	3334.00	0.0723
513.09	3336.00	0.0723
513.09	3340.00	0.0723
513.09	3343.00	0.0720
513.09	3345.00	0.0709
513.09	3346.00	0.0709
513.09	3347.00	0.0709
513.09	3350.00	0.0709
513.09	3360.00	0.0709
513.09	3370.00	0.0709
513.09	3380.00	0.0709
513.09	3390.00	0.0709
513.09	3400.00	0.0694
513.09	3420.00	0.0694
513.09	3430.00	0.0694
513.09	3450.00	0.0682
513.09	3450.00	0.0684
513.09	3500.00	0.0682
513.09	3600.00	0.0682
513.09	3700.00	0.0682
513.09	3800.00	0.0682
513.09	3900.00	0.0682
513.09	4000.00	0.0706
513.09	4100.00	0.0708
513.09	4100.00	0.0706
513.09	4200.00	0.0709
513.09	4300.00	0.0709
513.09	4600.00	0.0712
513.09	4700.00	0.0712
513.09	4800.00	0.0714
513.09	4900.00	0.0717
513.09	5000.00	0.0719
513.09	5100.00	0.0721
513.09	5200.00	0.0722
513.09	5300.00	0.0725
513.09	5400.00	0.0727
513.09	5500.00	0.0729
513.09	5600.00	0.0730
513.09	5700.00	0.0732
513.09	5800.00	0.0734
513.09	5900.00	0.0736
513.09	6000.00	0.0737
513.09	6100.00	0.0739
513.09	6200.00	0.0741
513.09	6300.00	0.0742
513.09	6400.00	0.0744
513.09	6500.00	0.0745
513.09	6600.00	0.0747
513.09	6700.00	0.0749
513.09	6800.00	0.0750
513.09	6900.00	0.0751
513.09	7000.00	0.0753
513.09	7100.00	0.0754
513.09	7150.00	0.0755
513.09	7200.00	0.0756
513.09	7211.00	0.0756
513.09	7292.00	0.0757
513.09	7496.00	0.0760
513.09	7501.00	0.0760
513.09	7517.00	0.0760
513.09	7533.00	0.0760
513.09	7800.00	0.0764
513.09	8100.00	0.0768
513.09	8200.00	0.0769
513.09	8500.00	0.0772
513.09	8790.00	0.0776
513.09	8830.00	0.0776
513.09	8882.00	0.0777
513.09	9275.00	0.0782
513.09	9297.00	0.0782
513.09	9300.00	0.0782
513.09	9344.00	0.0782
513.09	9367.00	0.0782
513.09	9700.00	0.0786
513.09	9900.00	0.0788
513.09	10000.00	0.0789
515.56	676.00	0.0383
515.56	700.00	0.0384
515.56	900.00	0.0385
515.56	1220.00	0.0390
515.56	1221.00	0.0390
515.56	1672.00	0.0401
515.56	1786.00	0.0404
515.56	1822.00	0.0406
515.56	2209.00	0.0423
515.56	2287.00	0.0428
515.56	2404.00	0.0434
515.56	2503.00	0.0439
515.56	2607.00	0.0447
515.56	2688.00	0.0455
515.56	2751.00	0.0461
515.56	2811.00	0.0470
515.56	2856.00	0.0471
515.56	2919.00	0.0471
515.56	2953.00	0.0478
515.56	2989.00	0.0493
515.56	3019.00	0.0500
515.56	3062.00	0.0508
515.56	3072.00	0.0508
515.56	3083.00	0.0516
515.56	3103.00	0.0525
515.56	3114.00	0.0525
515.56	3122.00	0.0525
515.56	3140.00	0.0525
515.56	3153.00	0.0533
515.56	3164.00	0.0533
515.56	3174.00	0.0542
515.56	3180.00	0.0542
515.56	3193.00	0.0561
515.56	3201.00	0.0561
515.56	3209.00	0.0561
515.56	3220.00	0.0561
515.56	3230.00	0.0581
515.56	3235.00	0.0581
515.56	3243.00	0.0581
515.56	3249.00	0.0581
515.56	3257.00	0.0602
515.56	3265.00	0.0602
515.56	3270.00	0.0602
515.56	3275.00	0.0602
515.56	3283.00	0.0621
515.56	3293.00	0.0621
515.56	3301.00	0.0637
515.56	3309.00	0.0647
515.56	3316.00	0.0650
515.56	3322.00	0.0654
515.56	3329.00	0.0658
515.56	3334.00	0.0660
515.56	3339.00	0.0663
515.56	3342.00	0.0666
515.56	3347.00	0.0669
515.56	3350.00	0.0670
515.56	3352.00	0.0671
515.56	3357.00	0.0674
515.56	3360.00	0.0675
515.56	3362.00	0.0676
515.56	3368.00	0.0679
515.56	3373.00	0.0682
515.56	3386.00	0.0687
515.56	3394.00	0.0691
515.56	3426.00	0.0700
515.56	3453.00	0.0691
515.56	3462.00	0.0691
515.56	3482.00	0.0691
515.56	3490.00	0.0691
515.56	3499.00	0.0691
515.56	3520.00	0.0691
515.56	3541.00	0.0691
515.56	3550.00	0.0691
515.56	3566.00	0.0691
515.56	3579.00	0.0677
515.56	3614.00	0.0677
515.56	3638.00	0.0677
515.56	3682.00	0.0677
515.56	3700.00	0.0677
515.56	3750.00	0.0694
515.56	3800.00	0.0694
515.56	3841.00	0.0694
515.56	3900.00	0.0695
515.56	3928.00	0.0695
515.56	3941.00	0.0696
515.56	3995.00	0.0697
515.56	4000.00	0.0697
515.56	4025.00	0.0697
515.56	4104.00	0.0698
515.56	4200.00	0.0700
515.56	4307.00	0.0702
515.56	4388.00	0.0703
515.56	4400.00	0.0704
515.56	4488.00	0.0706
515.56	4537.00	0.0707
515.56	4593.00	0.0708
515.56	4620.00	0.0709
515.56	4700.00	0.0710
515.56	4790.00	0.0711
515.56	4800.00	0.0712
515.56	4830.00	0.0712
515.56	4900.00	0.0713
515.56	5000.00	0.0715
515.56	5100.00	0.0717
515.56	5130.00	0.0717
515.56	5200.00	0.0718
515.56	5300.00	0.0720
515.56	5400.00	0.0722
515.56	5580.00	0.0724
515.56	5600.00	0.0725
515.56	5690.00	0.0727
515.56	5740.00	0.0727
515.56	5800.00	0.0728
515.56	5900.00	0.0730
515.56	6050.00	0.0733
515.56	6060.00	0.0733
515.56	6080.00	0.0733
515.56	6300.00	0.0737
515.56	6380.00	0.0738
515.56	6460.00	0.0739
515.56	6610.00	0.0742
515.56	6920.00	0.0746
515.56	6950.00	0.0747
515.56	7020.00	0.0748
515.56	7100.00	0.0749
515.56	7470.00	0.0754
515.56	7560.00	0.0755
515.56	7570.00	0.0756
515.56	7600.00	0.0756
515.56	7840.00	0.0759
515.56	7870.00	0.0760
515.56	7940.00	0.0760
515.56	8050.00	0.0762
515.56	8100.00	0.0762
515.56	8140.00	0.0762
515.56	8230.00	0.0764
515.56	8370.00	0.0766
515.56	8470.00	0.0766
515.56	8540.00	0.0767
515.56	8730.00	0.0770
515.56	8870.00	0.0771
515.56	9080.00	0.0774
515.56	9100.00	0.0774
525.42	1000.00	0.0403
525.42	1500.00	0.0416
525.42	1975.00	0.0421
525.42	1984.00	0.0421
525.42	2100.00	0.0421
525.42	2200.00	0.0421
525.42	2300.00	0.0421
525.42	2404.00	0.0421
525.42	2423.00	0.0421
525.42	2425.00	0.0421
525.42	2500.00	0.0437
525.42	2740.00	0.0444
525.42	2850.00	0.0444
525.42	3000.00	0.0470
525.42	3050.00	0.0476
525.42	3100.00	0.0486
525.42	3150.00	0.0486
525.42	3200.00	0.0496
525.42	3250.00	0.0503
525.42	3300.00	0.0507
525.42	3350.00	0.0518
525.42	3400.00	0.0531
525.42	3450.00	0.0538
525.42	3500.00	0.0553
525.42	3550.00	0.0566
525.42	3600.00	0.0578
525.42	3650.00	0.0590
525.42	3700.00	0.0603
525.42	3750.00	0.0616
525.42	3800.00	0.0628
525.42	3850.00	0.0638
525.42	3900.00	0.0648
525.42	4000.00	0.0663
525.42	4100.00	0.0669
525.42	4200.00	0.0669
525.42	4300.00	0.0669
525.42	4400.00	0.0668
525.42	4500.00	0.0668
525.42	4600.00	0.0668
525.42	4700.00	0.0668
525.42	4800.00	0.0668
525.42	4900.00	0.0685
525.42	5000.00	0.0685
525.42	5100.00	0.0685
525.42	5200.00	0.0685
525.42	5300.00	0.0714
525.42	5400.00	0.0717
525.42	5500.00	0.0717
525.42	5600.00	0.0717
525.42	5700.00	0.0720
525.42	5800.00	0.0720
525.42	5900.00	0.0722
525.42	6000.00	0.0723
525.42	6100.00	0.0725
525.42	6200.00	0.0725
525.42	6300.00	0.0727
525.42	6400.00	0.0728
525.42	6500.00	0.0728
525.42	6600.00	0.0730
525.42	6700.00	0.0731
525.42	6800.00	0.0733
525.42	6900.00	0.0735
525.42	7000.00	0.0736
525.42	7100.00	0.0738
525.42	7200.00	0.0739
525.42	7317.00	0.0741
525.42	7328.00	0.0741
525.42	7405.00	0.0741
525.42	7500.00	0.0743
525.42	7600.00	0.0745
525.42	7700.00	0.0746
525.42	7800.00	0.0748
525.42	7900.00	0.0748
525.42	8000.00	0.0750
525.42	8100.00	0.0751
525.42	8200.00	0.0753
525.42	8300.00	0.0755
525.42	8400.00	0.0755
525.42	8500.00	0.0755
525.42	8600.00	0.0756
525.42	8700.00	0.0758
525.42	8800.00	0.0760
525.42	8900.00	0.0761
525.42	9000.00	0.0763
525.42	9100.00	0.0763
525.42	9200.00	0.0765
525.42	9300.00	0.0767
525.42	9400.00	0.0767
525.42	9500.00	0.0768
525.42	9600.00	0.0770
525.42	9700.00	0.0771
525.42	9800.00	0.0773
525.42	9900.00	0.0774
525.42	10150.00	0.0777
525.42	10200.00	0.0778
525.42	10300.00	0.0779
525.42	10400.00	0.0780
525.42	10500.00	0.0781
525.42	10600.00	0.0783
525.42	10800.00	0.0785
525.42	11500.00	0.0794
525.42	11600.00	0.0796
525.42	11800.00	0.0798
525.42	12000.00	0.0799
525.42	12300.00	0.0803
525.42	12500.00	0.0805
553.00	1000.00	0.0435
553.00	1120.00	0.0439
553.00	1400.00	0.0441
553.00	1500.00	0.0443
553.00	1600.00	0.0444
553.00	1700.00	0.0445
553.00	1800.00	0.0448
553.00	1900.00	0.0449
553.00	2000.00	0.0452
553.00	2100.00	0.0454
553.00	2200.00	0.0456
553.00	2300.00	0.0458
553.00	2400.00	0.0461
553.00	2500.00	0.0464
553.00	2600.00	0.0466
553.00	2700.00	0.0469
553.00	2800.00	0.0472
553.00	2900.00	0.0474
553.00	3000.00	0.0474
553.00	3100.00	0.0481
553.00	3200.00	0.0486
553.00	3300.00	0.0490
553.00	3400.00	0.0494
553.00	3500.00	0.0500
553.00	3600.00	0.0505
553.00	3700.00	0.0513
553.00	3800.00	0.0519
553.00	3900.00	0.0525
553.00	4000.00	0.0532
553.00	4100.00	0.0539
553.00	4200.00	0.0547
553.00	4268.00	0.0552
553.00	4390.00	0.0562
553.00	4700.00	0.0589
553.00	4800.00	0.0599
553.00	4900.00	0.0607
553.00	5000.00	0.0617
553.00	5300.00	0.0642
553.00	5500.00	0.0656
553.00	5800.00	0.0675
553.00	6000.00	0.0684
553.00	6300.00	0.0697
553.00	6500.00	0.0702
553.00	6800.00	0.0711
553.00	7000.00	0.0717
553.00	7200.00	0.0720
553.00	7500.00	0.0727
553.00	7800.00	0.0733
553.00	8000.00	0.0736
553.00	8300.00	0.0743
553.00	8500.00	0.0743
553.00	8800.00	0.0755
553.00	9000.00	0.0755
553.00	9250.00	0.0756
553.00	9500.00	0.0758
553.00	9800.00	0.0762
553.00	10000.00	0.0764
553.00	10300.00	0.0765
553.00	10500.00	0.0769
553.00	10800.00	0.0772
553.00	11000.00	0.0773
553.00	11500.00	0.0778
553.00	12000.00	0.0783
553.00	12300.00	0.0787
553.00	12870.00	0.0791
553.00	13500.00	0.0798
553.00	14000.00	0.0802
553.00	14500.00	0.0807
553.00	15000.00	0.0812
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[110.16; 386.90]	J/mol×K	[200.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			9.46490e+01
Coefficient B			-6.98410e+02
Coefficient C			6.25624e+00
Coefficient D			-1.19920e-04
Coefficient E			2.97190e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	110.16	J/mol×K	200.00	Calculated Property
Cp,gas	160.73	J/mol×K	344.44	Calculated Property
Cp,gas	213.30	J/mol×K	488.89	Calculated Property
Cp,gas	256.95	J/mol×K	633.33	Calculated Property
Cp,gas	291.61	J/mol×K	777.78	Calculated Property
Cp,gas	319.09	J/mol×K	922.22	Calculated Property
Cp,gas	341.15	J/mol×K	1066.67	Calculated Property
Cp,gas	359.17	J/mol×K	1211.11	Calculated Property
Cp,gas	374.17	J/mol×K	1355.56	Calculated Property
Cp,gas	386.90	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[169.11; 275.32]	J/mol×K	[177.83; 460.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			1.55690e+02
Coefficient B			5.91370e+00
Coefficient C			4.04545e-01
Coefficient D			1.38090e-02
Coefficient E			-9.38140e-06
Temperature range, min.			177.83
Temperature range, max.			460.00
Cp,liquid	169.11	J/mol×K	177.83	Calculated Property
Cp,liquid	174.06	J/mol×K	209.18	Calculated Property
Cp,liquid	180.42	J/mol×K	240.53	Calculated Property
Cp,liquid	188.39	J/mol×K	271.89	Calculated Property
Cp,liquid	198.16	J/mol×K	303.24	Calculated Property
Cp,liquid	209.87	J/mol×K	334.59	Calculated Property
Cp,liquid	223.57	J/mol×K	365.94	Calculated Property
Cp,liquid	239.19	J/mol×K	397.30	Calculated Property
Cp,liquid	256.56	J/mol×K	428.65	Calculated Property
Cp,liquid	275.32	J/mol×K	460.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0023873; 0.0000405]	Pa×s	[174.65; 507.60]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-6.25820e+01
Coefficient B			2.30870e+03
Coefficient C			8.50850e+00
Coefficient D			-1.97410e-05
Coefficient E			2.00000e+00
Temperature range, min.			174.65
Temperature range, max.			507.60
η	0.0023873	Pa×s	174.65	Calculated Property
η	0.0009159	Pa×s	211.64	Calculated Property
η	0.0005084	Pa×s	248.64	Calculated Property
η	0.0003365	Pa×s	285.63	Calculated Property
η	0.0002408	Pa×s	322.63	Calculated Property
η	0.0001765	Pa×s	359.62	Calculated Property
η	0.0001284	Pa×s	396.62	Calculated Property
η	0.0000910	Pa×s	433.61	Calculated Property
η	0.0000621	Pa×s	470.61	Calculated Property
η	0.0000405	Pa×s	507.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[39.55; 10.97]	kJ/mol	[177.83; 493.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			4.08624e+01
Coefficient B			-1.01485e+00
Coefficient C			4.97802e+00
Coefficient D			-6.26617e+00
Coefficient E			2.68553e+00
Critical temperature, Tc (K)			5.07600e+02
Temperature range, min.			177.83
Temperature range, max.			493.15
ΔvapH	39.55	kJ/mol	177.83	Calculated Property
ΔvapH	37.28	kJ/mol	212.87	Calculated Property
ΔvapH	34.92	kJ/mol	247.90	Calculated Property
ΔvapH	32.57	kJ/mol	282.94	Calculated Property
ΔvapH	30.27	kJ/mol	317.97	Calculated Property
ΔvapH	27.94	kJ/mol	353.01	Calculated Property
ΔvapH	25.41	kJ/mol	388.04	Calculated Property
ΔvapH	22.37	kJ/mol	423.08	Calculated Property
ΔvapH	18.17	kJ/mol	458.11	Calculated Property
ΔvapH	10.97	kJ/mol	493.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[248.86; 365.27]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40796e+01
Coefficient B			-2.80205e+03
Coefficient C			-4.56990e+01
Temperature range, min.			248.86
Temperature range, max.			365.27
Pvap	1.33	kPa	248.86	Calculated Property
Pvap	3.04	kPa	261.79	Calculated Property
Pvap	6.33	kPa	274.73	Calculated Property
Pvap	12.17	kPa	287.66	Calculated Property
Pvap	21.91	kPa	300.60	Calculated Property
Pvap	37.25	kPa	313.53	Calculated Property
Pvap	60.32	kPa	326.47	Calculated Property
Pvap	93.61	kPa	339.40	Calculated Property
Pvap	139.99	kPa	352.34	Calculated Property
Pvap	202.64	kPa	365.27	Calculated Property
Pvap	[6.98e-04; 2892.68]	kPa	[174.15; 507.60]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			6.46585e+01
Coefficient B			-5.84897e+03
Coefficient C			-7.46028e+00
Coefficient D			5.08230e-06
Coefficient E			2.00000e+00
Temperature range, min.			174.15
Temperature range, max.			507.60
Pvap	6.98e-04	kPa	174.15	Calculated Property
Pvap	0.06	kPa	211.20	Calculated Property
Pvap	1.31	kPa	248.25	Calculated Property
Pvap	10.96	kPa	285.30	Calculated Property
Pvap	52.14	kPa	322.35	Calculated Property
Pvap	170.92	kPa	359.40	Calculated Property
Pvap	433.74	kPa	396.45	Calculated Property
Pvap	918.86	kPa	433.50	Calculated Property
Pvap	1709.41	kPa	470.55	Calculated Property
Pvap	2892.68	kPa	507.60	Calculated Property
Pvap	[8.39e-04; 3068.94]	kPa	[177.84; 507.43]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			1.05960e+02
Coefficient B			-7.28457e+03
Coefficient C			-1.39993e+01
Coefficient D			1.41032e-05
Coefficient E			0.00000e+00
Temperature range, min.			177.84
Temperature range, max.			507.43
Pvap	8.39e-04	kPa	177.84	Calculated Property
Pvap	0.08	kPa	214.46	Calculated Property
Pvap	1.62	kPa	251.08	Calculated Property
Pvap	12.74	kPa	287.70	Calculated Property
Pvap	56.97	kPa	324.32	Calculated Property
Pvap	177.26	kPa	360.95	Calculated Property
Pvap	435.10	kPa	397.57	Calculated Property
Pvap	913.27	kPa	434.19	Calculated Property
Pvap	1729.95	kPa	470.81	Calculated Property
Pvap	3068.94	kPa	507.43	Calculated Property
Pvap	[1.06e-03; 3.23]	kPa	[177.70; 264.93]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.25630e+01
Coefficient B			-2.40399e+03
Coefficient C			-5.38930e+01
Reference			Carruth and Kobayashi, 1973
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			177.70
Temperature range, max.			264.93
Pvap	1.06e-03	kPa	177.70	Calculated Property
Pvap	4.32e-03	kPa	187.39	Calculated Property
Pvap	0.01	kPa	197.08	Calculated Property
Pvap	0.04	kPa	206.78	Calculated Property
Pvap	0.11	kPa	216.47	Calculated Property
Pvap	0.25	kPa	226.16	Calculated Property
Pvap	0.52	kPa	235.85	Calculated Property
Pvap	1.02	kPa	245.55	Calculated Property
Pvap	1.87	kPa	255.24	Calculated Property
Pvap	3.23	kPa	264.93	Calculated Property
Pvap	[11.69; 103.89]	kPa	[286.18; 342.69]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38216e+01
Coefficient B			-2.69755e+03
Coefficient C			-4.87840e+01
Reference			Williamham, Taylor, et al., 1945
Temperature range, min.			286.18
Temperature range, max.			342.69
Pvap	11.69	kPa	286.18	Calculated Property
Pvap	15.66	kPa	292.46	Calculated Property
Pvap	20.69	kPa	298.74	Calculated Property
Pvap	26.95	kPa	305.02	Calculated Property
Pvap	34.66	kPa	311.30	Calculated Property
Pvap	44.07	kPa	317.57	Calculated Property
Pvap	55.41	kPa	323.85	Calculated Property
Pvap	68.97	kPa	330.13	Calculated Property
Pvap	85.03	kPa	336.41	Calculated Property
Pvap	103.89	kPa	342.69	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[752.13; 256.71]	kg/m3	[177.83; 507.35]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			4.79661e+01
Coefficient B			2.35060e-01
Coefficient C			5.07600e+02
Coefficient D			2.41830e-01
Temperature range, min.			177.83
Temperature range, max.			507.35
ρl	752.13	kg/m3	177.83	Calculated Property
ρl	725.10	kg/m3	214.44	Calculated Property
ρl	696.49	kg/m3	251.06	Calculated Property
ρl	665.93	kg/m3	287.67	Calculated Property
ρl	632.85	kg/m3	324.28	Calculated Property
ρl	596.37	kg/m3	360.90	Calculated Property
ρl	554.97	kg/m3	397.51	Calculated Property
ρl	505.59	kg/m3	434.12	Calculated Property
ρl	439.80	kg/m3	470.74	Calculated Property
ρl	256.71	kg/m3	507.35	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.01]	N/m	[177.75; 341.85]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			4.83559e-02
Coefficient B			-1.02200e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			177.75
Temperature range, max.			341.85
γ	0.03	N/m	177.75	Calculated Property
γ	0.03	N/m	195.98	Calculated Property
γ	0.03	N/m	214.22	Calculated Property
γ	0.02	N/m	232.45	Calculated Property
γ	0.02	N/m	250.68	Calculated Property
γ	0.02	N/m	268.92	Calculated Property
γ	0.02	N/m	287.15	Calculated Property
γ	0.02	N/m	305.38	Calculated Property
γ	0.02	N/m	323.62	Calculated Property
γ	0.01	N/m	341.85	Calculated Property
γ	[0.03; 3.68e-04]	N/m	[177.83; 493.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-1.03850e-01
Coefficient B			-1.41310e+01
Coefficient C			-1.66760e+00
Coefficient D			-1.56180e-03
Coefficient E			8.43690e-07
Temperature range, min.			177.83
Temperature range, max.			493.15
γ	0.03	N/m	177.83	Calculated Property
γ	0.03	N/m	212.87	Calculated Property
γ	0.02	N/m	247.90	Calculated Property
γ	0.02	N/m	282.94	Calculated Property
γ	0.02	N/m	317.97	Calculated Property
γ	0.01	N/m	353.01	Calculated Property
γ	0.01	N/m	388.04	Calculated Property
γ	0.01	N/m	423.08	Calculated Property
γ	0.00	N/m	458.11	Calculated Property
γ	3.68e-04	N/m	493.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.12]	W/m×K	[177.83; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			-5.69520e+02
Coefficient B			7.94300e-01
Coefficient C			-1.13790e+09
Coefficient D			-8.20550e+09
Temperature range, min.			177.83
Temperature range, max.			1000.00
λgas	0.01	W/m×K	177.83	Calculated Property
λgas	0.01	W/m×K	269.18	Calculated Property
λgas	0.02	W/m×K	360.53	Calculated Property
λgas	0.03	W/m×K	451.89	Calculated Property
λgas	0.04	W/m×K	543.24	Calculated Property
λgas	0.05	W/m×K	634.59	Calculated Property
λgas	0.07	W/m×K	725.94	Calculated Property
λgas	0.08	W/m×K	817.30	Calculated Property
λgas	0.10	W/m×K	908.65	Calculated Property
λgas	0.12	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.16; 0.09]	W/m×K	[177.83; 370.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			-1.26820e-01
Coefficient B			-1.50150e+00
Coefficient C			-1.04670e+00
Coefficient D			-8.87090e-04
Coefficient E			-9.36790e-07
Temperature range, min.			177.83
Temperature range, max.			370.00
λliquid	0.16	W/m×K	177.83	Calculated Property
λliquid	0.15	W/m×K	199.18	Calculated Property
λliquid	0.15	W/m×K	220.53	Calculated Property
λliquid	0.14	W/m×K	241.89	Calculated Property
λliquid	0.13	W/m×K	263.24	Calculated Property
λliquid	0.12	W/m×K	284.59	Calculated Property
λliquid	0.12	W/m×K	305.94	Calculated Property
λliquid	0.11	W/m×K	327.30	Calculated Property
λliquid	0.10	W/m×K	348.65	Calculated Property
λliquid	0.09	W/m×K	370.00	Calculated Property

Similar Compounds

Find more compounds similar to n-Hexane.

Mixtures

• n-Hexane + Acetonitrile
• n-Hexane + Trichloromethane + Acetone
• n-Hexane + Acetone + Cyclohexane
• n-Hexane + Acetone + Cyclohexane + Methyl Alcohol
• n-Hexane + Acetone + Ethyl ether
• Benzene + n-Hexane + Ethanol + Acetone
• n-Hexane + Trichloromethane + Ethanol + Acetone
• n-Hexane + Ethanol + Acetone
• n-Hexane + Acetone + Ethyl Acetate
• n-Hexane + Acetone
• n-Hexane + 2-Propanol + Acetone
• n-Hexane + Acetone + Methyl Alcohol
• n-Hexane + Acetone + Water
• Benzene + n-Hexane + Ethanol
• n-Hexane + Trichloromethane + Ethanol
• n-Hexane + Ethanol
• n-Hexane + 1-Hexene + Ethanol
• n-Hexane + Ethanol + Water
• n-Hexane + Ethyl ether
• n-Hexane + Ethyl ether + Methyl Alcohol

Find more mixtures with n-Hexane.

Sources

• KDB Vapor Pressure Data
• Active Thermochemical Tables 1.112, gas-phase enthalpies of formation ChEDL chemicals 1.5.2, from Active Thermochemical Tables (ATcT), version 1.112, Argonne National Laboratory; Ruscic, B. et al. Active Thermochemical Tables: Thermochemistry for the 21st Century. J. Phys.: Conf. Ser. 2005, 16, 561.
• 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).
• Hankinson and Thomson (1979), COSTALD parameters ChEDL chemicals 1.5.2, from Hankinson, R. W.; Thomson, G. H. A New Correlation for Saturated Densities of Liquids and Their Mixtures. AIChE J. 1979, 25, 653-663.
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 ChEDL chemicals 1.5.2, from Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 2. Normal Alkanes. J. Chem. Eng. Data 1995, 40, 531-546.
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• Passut and Danner (1973), critical constants and acentric factors ChEDL chemicals 1.5.2, from Passut, C. A.; Danner, R. P. Acentric Factor. A Valuable Correlating Parameter for the Properties of Hydrocarbons. Ind. Eng. Chem. Process Des. Dev. 1973, 12, 365-368.
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Densities, Viscosities, and Refractive Indices of Mixtures of Hexane with Cyclohexane, Decane, Hexadecane, and Squalane at 298.15K
• Measurements of the Liquid Viscosities of Mixtures of n-Butane, n-Hexane, and n-Octane with Squalane to 30MPa
• Liquid-Liquid Coexistence Curve of n-Perfluorohexane - n-Hexane System
• Kinematic Viscosities for Ether + Alkane Mixtures: Experimental Results and UNIFAC-VISCO Parameters
• Experimental Study of the Dynamic Viscosity Deviations in the Binary Systems: Hexane + Ethylbenzene, + o-Xylene, + m-Xylene, + p-Xylene at 298.15 K
• Acoustic and Thermophysical Properties of Binary Liquid Mixtures of Primary Butanols with Hexane and Cyclohexane at 293.15 K
• Densities and Kinematic Viscosities of One Quinary Regular Liquid System and Its Five Quaternary Sub-Systems at Temperatures (293.15 and 298.15) K
• High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
• Activity coefficient at infinite dilution, azeotropic data, excess enthalpies and solid liquid-equilibria for binary systems of alkanes and aromatics with esters
• Vapour pressures and excess functions of (3,5; 2,6)dimethylpyridine + n-hexane, n-heptane and n-octane measurement and prediction
• Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, trihexyl(tetradecyl)-phosphonium tris(pentafluoroethyl) trifluorophosphate, by gas liquid chromatography
• Excess molar volumes and excess molar enthalpies of binary and ternary mixtures of (ethanol or 1-butanol), triethylamine and n-hexane
• Vapour liquid equilibrium of carboxylic acid systems: Propionic acid + valeric acid and isobutyric acid + valeric acid
• Vapor liquid equilibrium of methane and methane + nitrogen and an equimolar hexane + decane mixture under isothermal conditions
• Experimental liquid liquid equilibria of 1-methylimidazole with hydrocarbons and ethers
• Solubility of chlorobutane, ethyl methacrylate and trifluoroethyl acrylate in supercritical carbon dioxide
• Vapour liquid equilibrium of octane enhancing additives in gasolines 7: Total pressure data and gE for the ternary mixture tert-amyl methyl ether (TAME), methanol and hexane at 313.15K
• Excess molar enthalpies for mixtures of carbon dioxide + a modifier (5 mol% methanol or 1-octanol) and hexane at 308.15K and 12.40MPa
• Liquid liquid equilibrium of (perfluoroalkane + alkane) binary mixtures
• Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, tributylmethylphosphonium methylsulphate by gas liquid chromatography
• Excess enthalpies of binary mixtures of 2-ethoxyethanol with four hydrocarbons at 298.15, 308.15, and 318.15K An experimental and theoretical study
• Phase behaviour of I-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium based ionic liquids with alcohols, water, ketones and hydrocarbons: The effect of cation and anion on solubility
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• Liquid liquid equilibria and partitioning in organic aqueous systems
• Determination and correlation of liquid liquid equilibria for four binary N,N-dimethylformamide + hydrocarbon systems
• Isobaric vapor liquid and vapor liquid liquid equilibrium data for the water ethanol hexane system
• Solution thermodynamics near the liquid liquid critical point I. First-order excess derivatives
• Measurement of vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide and prediction of these properties and A using modified UNIFAC (Dortmund)
• Separation of aromatic hydrocarbons from alkanes using ammonium ionic liquid C2NTf2 at T = 298.15K
• Phase behaviour of 1-methyl-3-octylimidazolium bis[trifluoromethylsulfonyl]imide with thiophene and aliphatic hydrocarbons: The influence of n-alkane chain length
• Ternary liquid liquid equilibria for mixtures of an ionic liquid + n-hexane + an organic compound involved in the kinetic resolution of rac-1-phenyl ethanol (rac-1-phenyl ethanol, vinyl propionate, rac-1-phenylethyl propionate or propionic acid) at 298.2K and atmospheric pressure
• Liquid liquid equilibria of lactam containing binary systems
• A study on the liquid liquid equilibria of 1-alkyl-3-methylimidazolium hexafluorophosphate with ethanol and alkanes
• Thiophene separation from aliphatic hydrocarbons using the 1-ethyl-3-methylimidazolium ethylsulfate ionic liquid
• Solubility of hydrocarbons in water: Experimental measurements and modeling using a group contribution with association equation of state (GCA-EoS)
• Isobaric vapor liquid equilibria for the n-hexane + 2-isopropoxyethanol and n-heptane + 2-isopropoxyethanol systems
• Isobaric thermal expansivity of the binary system 1-hexanol + n-hexane as a function of temperature and pressure
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid N-butyl-4-methylpyridinium tosylate using GLC at T = (328.15, 333.15, 338.15, and 343.15)K
• Measurement and prediction of activity coefficients at infinite dilution ( ), vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1,1-dialkyl-pyrrolidinium bis(trifluoromethylsulfonyl)imide using mod. UNIFAC (Dortmund)
• Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
• (Solid + liquid) and (liquid + liquid) phase equilibria measurements and correlation of the binary systems {tri-iso-butyl(methyl)phosphonium tosylate + alcohol, or +hydrocarbon}
• Solubility of pyrene in simple and mixed solvent systems
• Liquid liquid equilibria for {hexane + benzene + 1-ethyl-3-methylimidazolium ethylsulfate} at (298.2, 313.2 and 328.2)K
• Activity coefficients at infinite dilution of alkanes and alkenes in 1-alkyl-3-methylimidazolium tetrafluoroborate
• Solubilities of cholesterol and desmosterol in binary solvent mixtures of n-hexane + ethanol
• 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
• Measurement and correlation of solid-liquid equilibria of Irganox 1010 with n-hexane
• Liquid phase equilibria for mixtures of (an aliphatic hydrocarbon + toluene + gamma-butyrolactone)
• Phase equilibria of binary systems of 3-methylthiophene with four different hydrocarbons
• Alkylsulfate-based ionic liquids to separate azeotropic mixtures
• Ionic liquids on desulfurization of fuel oils
• (Solid + liquid) and (liquid + liquid) phase equilibria study and correlation of the binary systems {N-butyl-3-methylpyridinium tosylate + water, or + an alcohol, or + a hydrocarbon}
• Measurements of different thermodynamic properties of systems containing ionic liquids and correlation of these properties using modified UNIFAC (Dortmund)
• Infinite dilution activity coefficient and vapour liquid equilibrium measurements for dimethylsulphide and tetrahydrothiophene with hydrocarbons
• Alkylsulfate-based ionic liquids to separate azeotropic mixtures
• Application of [EMpy][ESO4] ionic liquid as solvent for the liquid extraction of xylenes from hexane
• Liquid-liquid equilibrium data for binary perfluoroalkane (C6 and C8) + n-alkane systems
• Measurements of binary diffusion coefficients for metal complexes in organic solvents by the Taylor dispersion method
• Experimental data on binary and ternary mixtures of perfluoro-1,3-dimethylcyclohexane with normal alkanes at 373.15 K
• Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
• Influence of anion structure on the liquid-liquid equilibria of 1-(3-hydroxypropyl)pyridinium cation based ionic liquid-hydrocarbon binary systems
• Influence of temperature on the (liquid + liquid) equilibria of {methanol + benzene + hexane} ternary system
• Study of [EMim][ESO4] ionic liquid as solvent in the liquid-liquid extraction of xylenes from their mixtures with hexane
• Physical properties of 3-methyl-N-butylpyridinium tricyanomethanide and ternary LLE data with an aromatic and an aliphatic hydrocarbon at T = (303.2 and 328.2) K and p = 0.1 MPa
• Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
• Experimental determination and calculation of the critical curves for the binary systems of CO2 containing ketone, alkane, ester and alcohol, respectively
• Measurement and theoretical prediction of the vapor-liquid equilibrium, densities and interfacial tensions of the system hexane + 2-methoxy-2-methylbutane
• P-x data for binary systems using a novel static total pressure apparatus
• Hexyl dimethylpyridinium ionic liquids for desulfurization of fuels. Effect of the position of the alkyl side chains
• Vapor-liquid equilibrium for the ternary carbon dioxide + ethanol + n-hexane and quaternary carbon dioxide + ethanol + n-hexane + thiophene systems
• LLE, VLE and VLLE data for the water n-butanol n-hexane system at atmospheric pressure
• Experimental determination and theoretical modeling of the vapor-liquid equilibrium and surface tensions of hexane + tetrahydro-2H-pyran
• Liquid-liquid equilibria of mixtures with ethyl lactate and various hydrocarbons
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid ethyl(2-hydroxyethyl)dimethyl-ammonium diethylphosphate using gas liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
• Vapour-liquid equilibrium (VLE) for the systems furan + n-hexane and furan + toluene. Measurements, data treatment and modeling using molecular models
• Ionic liquids as solvents to separate the azeotropic mixture hexane/ethanol
• A novel static analytical apparatus for phase equilibrium measurements
• Ternary (liquid liquid) equilibria of nitrate based ionic liquid + alkane + benzene at 298.15 K: Experiments and correlation
• Measurement and correlation of vapor-liquid equilibria for alkane + alkanol andalkane + alkanediol systems with group contribution COSMOSPACE model
• Capacity of two 1-butyl-1-methylpyrrolidinium-based ionic liquidsfor the extraction of ethanol from its mixtures with heptane and hexane
• Enthalpies and Gibbs free energies of solvation in ethylene glycol at298 K: Influence of the solvophobic effect
• Desulfurization of fuels by liquid-liquid extraction with1-ethyl-3-methylimidazolium ionic liquids
• Viscosity of liquid systems involving hydrogenated and fluorinated substances: Liquid mixtures of (hexane + perfluorohexane)
• Measurements of activity coefficients at infinite dilution in vegetable oils and capric acid using the dilutor technique
• Vapor-liquid equilibrium and interfacial tensions of the system ethanol + hexane + tetrahydro-2H-Pyran
• Extraction of toluene from alkane using [Bmim][NO3] or [Omim][NO3] ionic liquid at 298.15 K and atmospheric pressure
• Prediction and measurement of phase equilibria for the extraction of BTX from naphtha reformate using BMIMPF6 ionic liquid
• Liquid-liquid equilibrium data for ternary mixtures composed of n-hexane, benzene and acetonitrile at (298.15, 308.15, and 318.15) K
• Solid-liquid equilibrium and thermodynamic of 2,5-thiophenedicarboxylic acid in different organic solvents
• Study of critical and maximum temperatures of coexistence of liquid and gas phase in hydrocarbons binary mixtures of aromatic hydrocarbons with alkanes and cycloalkanes
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• Measurement, correlation and prediction of isothermal vapor liquid equilibria of different systems containing vegetable oils
• Determination and correlation of solubility and solution thermodynamics of coumarin in different pure solvents
• The ionic liquid 1-ethyl-3-methylimidazolium tris(pentafluoroethyl) trifluorophosphate as alternative extractant for BTEX separation
• Experimental study on liquid - liquid equilibria of ionic liquids + alkane + ethyl benzene or p-xylene at 298.15 K
• Novel liquid-liquid equilibrium data for six ternary systems containing IL, hydrocarbon and thiophene at 25 C
• Liquid-liquid equilibria in the ternary and multicomponent systems involving hydrocarbons, thiophene or pyridine and ionic liquid (1-benzyl-3-metylimidazolium bis(trifluorometylsulfonyl)imide)
• 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
• Liquid-liquid equilibrium data for (n-hexane + ethyl acetate + acetonitrile) ternary system at (298.15, 308.15, and 318.15) K
• Characterizing second generation biofuels: Excess enthalpies and vapour-liquid equilibria of the binary mixtures containing 1-pentanol or 2-pentanol and n-hexane
• Separation of hex-1-ene/hexane and cyclohexene/cyclohexane compounds with [EMIM]-based ionic liquids
• Preferential solvation and mixing behaviour of the essential oil 1,8-cineole with short-chain hydrocarbons
• Equilibrium data and GC-PC SAFT predictions for furanic extraction
• Equilibrium study and diversified models of drug Norfloxacin in eight pure organic and binary solvents at T = (278.15 to 328.15) K
• Volume expansion prediction of supercritical CO 2 + crude oil
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Liquid-liquid equilibrium data for extractive desulfurization using 1-butyl-3-methyl imidazolium thiocyanate, n-alkane and thiophene
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• Ternary liquid-liquid equilibrium of an azeotropic mixture (hexane + methanol) with different imidazolium-based ionic liquids at T = 298.15 K and 101.325 kPa
• Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
• Ternary LLE measurements for the separation of hex-1-ene/hexane and cyclohexene/cyclohexane compounds with [DCA]-based ionic liquids
• Measurement of critical properties for binary and ternary mixtures containing potential gasoline additive diethyl carbonate (DEC)
• Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
• Thermal conductivity of gaseous and liquid n-hexane
• Vapor-liquid equilibrium in the binary and ternary systems containing ethyl propionate, ethanol and alkane at 101.3 kPa
• 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
• Experimental measurement of carbon dioxide solubility in 1-methylpyrrolidin-2-one (NMP) + 1-butyl-3-methyl-1H-imidazol-3-ium tetrafluoroborate ([bmim][BF4]) mixtures using a new static-synthetic cell
• Experimental measurement and thermodynamic modeling of phase equilibria of {CO2 + tetralin + n-alkanes (with n = 6, 16)} and its binary systems
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Measurements of the thermal conductivity of n-hexane in the supercritical region
• Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
• Effective extraction of benzene and thiophene by novel deep eutectic solvents from hexane / aromatic mixture at different temperatures
• VLE measurements and modelling for the binary systems of (CF4 + C6F14) and (CF4 + C8F18)
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• Measurement of the speed of sound in supercritical n-hexane at temperatures from (509.17-637.99) K and pressures from (3.5-7.5) MPa
• High-pressure experimental vapour-liquid-liquid equilibrium measurements and modelling for natural gas processing: Equipment validation, and the system CH4 + nC6H14 + H2O
• The determination of activity coefficients at infinite dilution using g.l.c. for hydrocarbons in furfural at T = 278:15 K and T = 298:15 K
• Activity coefficients at infinite dilution for hydrocarbons in furfuryl alcohol at T=(278.15 and 298.15) K, determined by g.l.c.
• Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid 1-butyl-3-methyl-imidazolium 2-(2-methoxyethoxy) ethyl sulfate using g.l.c. at T = (298.15, 303.15, and 308.15) K
• Excess molar volumes of the ternary system {methylcyclohexane (1) + cyclohexane (2) + n-alkanes (3)} at T = 298.15 K
• Liquid phase behaviour of 1-hexyloxymethyl-3-methyl-imidazolium-based ionic liquids with hydrocarbons: The influence of anion
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid hexyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)-imide using g.l.c. at T = (298.15, 313.15, and 333.15) K
• Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
• (Vapor + liquid) equilibria of binary mixtures formed by iso-octane with a variety of compounds at 95.8 kPa
• 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)
• Vapour pressures of n-hexane determined by comparative ebulliometry
• Experimental measurements and prediction of liquid densities for n-alkane mixtures
• Measurement of activity coefficients at infinite dilution using polar and non-polar solutes in the ionic liquid 1-methyl-3-octyl-imidazolium diethyleneglycolmonomethylethersulfate at T = (288.15, 298.15, and 313.15) K
• Dynamic viscosities of the ternary liquid mixtures (dimethyl carbonate + methanol + ethanol) and (dimethyl carbonate + methanol + hexane) at several temperatures
• Excess molar volumes and dynamic viscosities for binary mixtures of toluene + n-alkanes (C5 C10) at T = 298.15 K Comparison with Prigogine Flory Patterson theory
• Excess molar volumes and excess molar enthalpies of binary and ternary mixtures of 1-butanol, a tertiary amine (tri-n-butylamine or tri-n-octylamine) and n-hexane: Experimental results and ERAS-model calculations
• Physical properties of (propyl propanoate + hexane + toluene) at 298.15 K
• Phase equilibria of didecyldimethylammonium nitrate ionic liquid with water and organic solvents
• Determination of solvation and specific interaction enthalpies of adamantane derivatives in aprotic solvents
• (Liquid + liquid) equilibria of ternary and quaternary systems containing n-hexane, toluene, m-xylene, propanol, sulfolane, and water at T = 303.15 K
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• Excess enthalpy, density, and speed of sound determination for the ternary mixture (methyl tert-butyl ether + 1-butanol + n-hexane)
• Mixing properties of binary mixtures presenting azeotropes at several temperatures
• Thermodynamic study of (perfluoroalkane + alkane) mixtures: Excess and solvation enthalpies
• Study of densities, viscosities, and speeds of sound of binary liquid mixtures of butan-1-ol with n-alkanes (C6, C8, and C10) at T = (298.15, 303.15, and 308.15) K
• Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
• Excess properties and vapour pressure of (3-diethylaminopropylamine + n-alkanes)
• Development of a Henry s constant correlation and solubility measurements of n-pentane, i-pentane, cyclopentane, n-hexane, and toluene in water
• Study of molecular interactions in binary liquid mixtures of 1-octanol with n-hexane, n-octane, and n-decane using volumetric, viscometric, and acoustic properties
• Phase equilibria for mixtures containing nonionic surfactant systems: Modeling and experiments
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid trihexyltetradecylphosphonium-bis-(2,4,4-trimethylpentyl)- phosphinate using g.l.c. at T = (303.15, 308.15, 313.15, and 318.15) K
• Evaluation of (vapor + liquid) equilibria for the binary systems (1-octanol + cyclohexane) and (1-octanol + n-hexane), at low alcohol compositions
• Measurement and correlation of (vapor + liquid) equilibria for the {2-propoxyethanol (C3E1) + n-hexane} and the {2-propoxyethanol (C3E1) + n-heptane} systems
• Surface and bulk behaviour of some (n-hexane + chloroalkane) mixtures
• Phase diagrams of (hexane + methanol + 2,2,2-trifluoroethanol) at three temperatures: Measurement and correlation
• Thermodynamics of biofuels: Excess enthalpies for binary mixtures involving ethyl 1,1-dimethylethyl ether and hydrocarbons at different temperatures using a new flow calorimeter
• 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
• Experimental densities, refractive indices, and speeds of sound of 12 binary mixtures containing alkanes and aromatic compounds at T = 313.15 K
• (Vapour + liquid) equilibrium and excess Gibbs functions of ternary mixtures containing 1-butanol or 2-butanol, n-hexane, and 1-chlorobutane at T = 298.15 K
• (Liquid + liquid) equilibria for ternary mixtures of (alkane + benzene + [EMpy] [ESO4]) at several temperatures and atmospheric pressure
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium trifluoromethanesulfonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• (Liquid + liquid) equilibria in the binary systems (aliphatic, or aromatic hydrocarbons + 1-ethyl-3-methylimidazolium ethylsulfate, or 1-butyl-3-methylimidazolium methylsulfate ionic liquids)
• Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
• (Liquid + liquid) equilibria of (sulfolane + benzene + n-hexane), (N-formylmorpholine + benzene + n-hexane), and (sulfolane + N-formylmorpholine + benzene + n-hexane) at temperatures ranging from (298.15 to 318.15) K: Experimental results and correlation
• LLE data for the ionic liquid 3-methyl-N-butyl pyridinium dicyanamide with several aromatic and aliphatic hydrocarbons
• (Liquid + liquid) equilibria of (heptane, or hexane, or cyclohexane + toluene + 1,3- dimethyl-2-imidazolidinone) ternary systems at T = 298.15 K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-octyl-3-methylimidazolium hexafluorophosphate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate [EMIM][TCB] using gas liquid chromatography
• (Vapour + liquid) equilibria of ternary systems with ionic liquids using headspace gas chromatography
• Separation of benzene from alkanes by solvent extraction with 1-ethylpyridinium ethylsulfate ionic liquid
• 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.
• Volumetric and acoustic behaviour of systems containing n-hexane, or n-heptane and isomeric chlorobutanes
• Activity coefficients at infinite dilution of organic solutes in N-alkylpyridinium bis(trifluoromethylsulfonyl)imide ([CnPY][NTf2], n = 2, 4, 5) using gas liquid chromatography
• Densities, excess molar volume, isothermal compressibility, and isobaric expansivity of (dimethyl carbonate + n-hexane) systems at temperatures (293.15 to 313.15) K and pressures from 0.1 MPa up to 40 MPa
• Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
• Extraction of toluene from aliphatic compounds using an ionic liquid as solvent: Influence of the alkane on the (liquid + liquid) equilibrium
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyl(tetradecyl)phosphonium tetrafluoroborate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 373.15) K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium hexafluoroantimonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid, methyl(trioctyl)ammonium thiosalicylate, [N1888][TS] by gas liquid chromatography at T = (303.15, 313.15, and 323.15) K
• 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
• Physical properties of 3-methyl-N-butylpyridinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium tetracyanoborate and ternary LLE data of [3-mebupy]B(CN)4 with an aromatic and an aliphatic hydrocarbon at T = 303.2 K and 328.2 K and p = 0.1 MPa
• Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium 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 of organic solutes in the ionic liquid trihexyltetradecylphosphonium hexafluorophosphate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 363.15) K
• Determination of infinite dilution activity coefficients using HS-SPME/GC/FID for hydrocarbons in furfural at temperatures of (298.15, 308.15, and 318.15) K
• 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
• Experimental study on vapor-liquid equilibria of ternary systems of hydrocarbons/ionic liquid using headspace gas chromatography
• 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
• Liquid-liquid extraction of aromatics from their mixtures with alkanes using 1-methyl 3-octylimidazolium thiocyanate ionic liquid
• 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
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
• Ethanol extraction from its azeotropic mixture with hexane employing different ionic liquids as 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
• Desulfurization of fuel-oils with [C2mim][NTf2]: A comparative study
• Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• Solubilities of evodiamine in twelve organic solvents from T = (283.2 to 323.2) K
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
• Application of 1-alkyl-3-methylpyridinium bis(trifluoromethylsulfonyl)imide ionic liquids for the ethanol removal from its mixtures with alkanes
• 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
• Ternary liquid liquid equilibrium data for the (water + butyric acid + n-hexane or n-hexanol) systems at T = (298.2, 308.2, and 318.2) K
• Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
• Activity coefficients at infinite dilution of organic solutes in N-formylmorpholine and N-methylpyrrolidone from gas-liquid chromatography
• Measurement of critical temperatures and critical pressures for binary mixtures of methyl tert-butyl ether (MTBE) + alcohol and MTBE + alkane
• Phase equilibria study of the (N-octylisoquinolinium thiocyanate ionic liquid + aliphatic and aromatic hydrocarbon, or thiophene) binary systems
• Thermodynamics of solvation and solvophobic effect in formamide
• 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
• Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography at T = (313.15, 333.15, 353.15 and 373.15) K
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Cation effect of ammonium imide based ionic liquids in alcohols extraction from alcohol-alkane azeotropic mixtures
• 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
• Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium 2-(2-methoxyethoxy) ethylsulfate at T = (308.15, 313.15, 323.15 and 333.15) K using gas + liquid chromatography
• 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
• Phase behavior of ternary mixtures {aliphatic hydrocarbon + aromatic hydrocarbon + ionic liquid}: Experimental LLE data and their modeling by COSMO-RS
• Contribution to study of the thermodynamics properties of mixtures containing 2-methoxy-2-methylpropane, alkanol, alkane
• Use of water in aiding olefin/paraffin (liquid + liquid) extraction via complexation with a silver bis(trifluoromethylsulfonyl)imide salt
• Application of 1-pentyl-3-methylimidazolium bis(trifluoromethylsulfonyl) imide for desulfurization, denitrification and dearomatization of FCC gasoline
• 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
• Thermodynamics of solvation in propylene glycol and methyl cellosolve
• (Solid + liquid) phase equilibria of tetraphenyl piperazine-1,4-diyldiphosphonate in pure solvents
• Phosphoric-based ionic liquids as solvents to separate the azeotropic mixture of ethanol and hexane
• Solvation parameter model and thermodynamic parameters in a dicationic ionic liquid based on pyrrolidinium
• Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
• 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
• Refractive indices and static permittivities of systems containing n-hexane or n-heptane and isomeric chlorobutanes
• Volumetric, acoustic, and refractometric properties of (thiophene + hexane/cyclohexane) solutions in the presence of some imidazolium based ionic liquids at T = 298.15 K
• (Liquid + liquid) extraction of methanol from alkanes using dialkylphosphate-based ionic liquids as solvents
• Study of the binary mixtures of {monoglyme + (hexane, cyclohexane, octane, dodecane)} by ECM-average and PFP models
• 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
• Activity coefficients at infinite dilution of alkanes, alkenes, alkyl benzenes in dimethylphosphate based ionic liquids using gas liquid chromatography
• Screening of environmental friendly ionic liquid as a solvent for the different types of separations problem: Insight from activity coefficients at infinite dilution measurement using (gas + liquid) chromatography technique
• Experimental determination and correlation of the solubility of 4-hydroxy-2,5-dimethyl-3(2H)-furanone (DMHF) in six different solvents
• Isothermal (vapour + liquid) equilibrium data for binary systems of (n-hexane + CO2 or CHF3)
• SAFT-.gamma. force field for the simulation of molecular fluids 6: Binary and ternary mixtures comprising water, carbon dioxide, and n-alkanes
• Impact of structural modification of 1,2,4-thiadiazole derivatives on thermodynamics of solubility and solvation processes in 1-octanol and n-hexane
• Selective recovery of aliphatics from aromatics in the presence of the {[4empy][Tf2N] + [emim][DCA]} ionic liquid mixture
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Solubility of methane in n-hexane and a petroleum benzine at ambient temperatures
• Experimental determination of critical data of multi-component mixtures containing potential gasoline additives 2-butanol by a flow-type apparatus
• 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
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Liquid-liquid equilibria for ternary mixtures of 1-alkyl-3-methyl imidazolium bis{(trifluoromethyl)sulfonyl}imides, n-hexane and organic compounds at 303.15 K and 0.1 MPa
• Speed of sound measurements of di-isopropyl ether (DIPE) from 293.15 K to 673.15 K and up to 10 MPa
• 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
• Fully automatized apparatus for determining speed of sound for liquids in the temperature and pressure interval (283.15-343.15) K and (0.1-95) MPa
• Activity coefficients at infinite dilution of hydrocarbons in glycols: Experimental data and thermodynamic modeling with the GCA-EoS
• Determination and correlation of Avermectin B1a solubility in different binary solvent mixtures at temperatures from (283.15 to 313.15) K
• Bis(trifluoromethylsulfonyl)imide, or dicyanamide-based ionic liquids in the liquid liquid extraction of hex-1-ene from hexane and cyclohexene from cyclohexane
• Surface tension and density of mixtures of m-xylene + n-alkane at 293.15 K: Analysis under the extended Langmuir and Shereshefsky models
• Experimental determination of the critical loci for R-23 + (npropane or n-hexane) and R-116 + n-propane binary mixtures
• Determination of melting temperatures in hydrocarbon mixtures by differential scanning calorimetry
• Physico-chemical characterization antituberculosis thioacetazone: Vapor pressure, solubility and lipophilicity
• Liquid-liquid separation of hex-1-ene from hexane and cyclohexene from cyclohexane with ionic liquids
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Heat capacity and Joule-Thomson coefficient of selected n-alkanes at 0.1 and 10 MPa in broad temperature ranges
• Physical properties of systems of interest to the edible oil industry: Viscosities and densities of model systems formed by (triacylglycerol + fatty acid + solvent)
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• Solubility and distribution of bicycle derivatives of 1,3-selenazine in pharmaceutically relevant media by saturation shake-flask method
• Measurement and correlation of ternary phase equilibrium of (hexane + ethyl acetate) with four ILs
• Liquid-liquid separation of hexane/hex-1-ene and cyclohexane/cyclohexene by dicyanamide-based ionic liquids
• 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
• A thermodynamic study of sublimation, dissolution and distribution processes of anti-inflammatory drug Clonixin
• Solubility and vapor pressure data of bioactive 6-(acetylamino)-N-(5-ethyl-1,3,4-thiadiazol-2-yl) hexanamide
• 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
• Thermodynamic study of aceclofenac solubility, distribution and sublimation
• Liquid-liquid extraction of methanol from its mixtures with hexane using three imidazolium-based ionic liquids
• Volumetric and viscometric studies of molecular interaction of the ternary system toluene (1) + cyclohexane (2) + n-hexane (3) at 298.15K
• Excess volumes, densities, speeds of sound and viscosities for the binary systems of diisopropyl ether with hydrocarbons at 303.15K
• Physical properties and their corresponding changes of mixing for the ternary mixture acetone + n-hexane +water at 298.15K
• Thermophysical properties and thermodynamic phase behavior of ionic liquids
• Topological and thermodynamic investigations of binary mixtures: Molar excess volumes, molar excess enthalpies and isentropic compressibility changes of mixing
• Excess molar volumes and isentropic compressibilities changes of mixing of tetrahydropyran + benzene + cyclo or n-alkanes ternary mixtures at 308.15 K
• Thermodynamic properties of binary mixtures containing Tetrahydropyran: Excess molar volumes, Excess molar enthalpies and isentropic compressibilities changes of mixing
• Thermophysical Study of the n-Hexane or n-Heptane with 1- Chloropropane Systems
• THERMODYNAMIC PROPERTIES OF DONOR ACCEPTOR COMPLEXES OF TERTIARY AMINE WITH ARYL KETONES IN HEXANE MEDIUM
• Calorimetric study of solvation of low polar solutes in propylene glycol and methyl cellosolve at 298 K
• Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
• Effect of halogen substitution on the enthalpies of solvation and hydrogen bonding of organic solutes in chlorobenzene and 1,2-dichlorobenzene derived using multi-parameter correlations
• Standard molar Gibbs free energy and enthalpy of solvation of lowpolar solutes in formamide derivatives at 298 K
• Thermodynamic of dissolution and hydrogen bond of the pyrrole, N-methylpyrrole with proton acceptors
• The solubility of ethionamide and structural analogues in buffer solutions, octanol and hexane at several temperatures
• Low cost apparatus for rapid boiling point determination of small air sensitive samples under inert atmosphere
• Physico-chemical study of bioactive N-(5-ethyl-1,3,4-thiadiazole-2-yl)-4-nitrobenzamide: Sublimation, solubility and distribution
• Thermochemistry of hydrogen bonding of proton acceptors in the media of linear and cyclic amides. Cooperativity effects in multi-particle complexes of amides
• Isothermal vapor-liquid equilibrium of binary and ternary systems of anisole, hexane, and toluene and ternary system of methyl tert-butyl ether, hexane, and toluene
• Experimental solubility of clotrimazole and some thermodynamic aspects of dissolution in different solvents
• Dissociation Constants and Solubilities of Dalbergin and Nordalbergin in Different Solvents
• Capillary Viscometer and Vibrating Tube Densimeter for Simultaneous Measurements up to 70 MPa and 423 K
• Phase Equilibria in Systems of Morpholine, Acetonitrile, and n-Alkanes
• Solubility of Hexane in Aqueous Solutions of Methyldiethanolamine
• Solubility Measurement and Correlation for 2- Naphthaldehyde in Pure Organic Solvents and Methanol + Ethanol Mixtures
• Liquid Liquid Equilibrium data for the ternary systems of Water, Isopropyl alcohol, and selected entrainers
• Mass Diffusion Coefficient and Soret Coefficient of o-Dichlorobenzene Solutions of PCBM and [60]Fullerene by the Soret Forced Rayleigh Scattering Method
• Densities of the binary systems n-hexane + n-decane and nhexane + n-hexadecane up to 60 MPa and 463 K
• Solubility of Ethene in n-Hexane and n-Heptane as Common Slurry-Phase Polymerization Solvents: Experimental Measurement and Modeling
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Liquid Liquid Equilibria of Binary and Ternary Systems Methanol/Water + n-Hexane, + n-Octane, + n-Dodecane, and + n-Hexadecane in the Temperature Range between T = 283.15 K and T = 333.15 K
• Vapor Liquid Equilibria for (n-Hexane, n-Octane, Cyclohexane, or 2,3-Dimethylpentane) + Toluene + {[4empy][Tf2N] (0.3) + [emim][DCA] (0.7)} Mixed Ionic Liquids
• Isobaric Vapor Liquid Equilibrium for Nine Binary Systems of Cracking C5 Fraction at 250 kPa
• Phase Behavior and Densities of Propylene + Hexane Binary Mixtures to 585 K and 70 MPa
• Solubility of 2-Ethylanthraquinone in Binary Mixtures of Oligooxymethylene Dimethyl Ethers with Different Number of CH2O Groups of n = 2, 3, and 4 from 293.15 to 343.15 K
• Sulfasalazine: Dissolution and Distribution in Pharmaceutically Relevant Mediums
• Solubility of 4-Methylsulfonylacetophenone in Nine Pure Solvents and (Ethyl Acetate + n-Hexane) Binary Solvent Mixtures from 278.15 K to 328.15 K
• Diffusion Coefficients of Carbon Dioxide in Eight Hydrocarbon Liquids at Temperatures between (298.15 and 423.15) K at Pressures up to 69 MPa
• Measurement and Correlation of Solubility of Amorphous Cefmetazole Sodium in Pure Solvents and Binary Solvent Mixtures
• Evaluation of Diethyl Carbonate and Methyl Isobutyl Ketone as Entrainers for the Separation of 1-Hexene and n-Hexane
• Measurement and Modeling of Solubility of para-tert-Butylbenzoic Acid in Pure and Mixed Organic Solvents at Different Temperatures
• Liquid Liquid Equilibria of Binary, Ternary, and Quaternary Systems Involving Monoethylene Glycol, Water, Toluene, p-Xylene, Hexane, and Octane
• Ternary Liquid Liquid Equilibrium for Mixtures of Water + (+-)alpha-Phenylethylamine + n-Hexane at T = 298.2, 318.2, and 333.2 K
• Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
• The Critical Temperatures of a Number of (i) (Chloroalkane (C3 C4) + Hydrocarbon (C6 C7)) Binary Mixtures and (ii) (Aromatic Halocarbon (Chlorobenzene, Fluorobenzene, 1,2-Dichlorobenzene, or 1,3-Dichlorobenzene) + Alkane (C8)) Binary Mixtures
• Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
• Experimental and Modeling Studies on the Solubility of 2-Chloro-N-(4-methylphenyl)propanamide (S1) in Binary Ethyl Acetate + Hexane, Toluene + Hexane, Acetone + Hexane, and Butanone + Hexane Solvent Mixtures Using Polythermal Method
• Measurement and Correlation of High Pressure Phase Equilibria for CO2 + Alkanes and CO2 + Crude Oil Systems
• Liquid-Liquid Equilibrium for Ternary System n-Butanol + n-Hexane + Ethylene Glycol at 298.15-323.15 K
• Experimental Solubility Data for Binary Mixtures of Ethane and 2,2,4-Trimethylpentane at Pressures up to 6 MPa Using a New Variable-Volume Sapphire Cell
• Thermodynamic Aspects of Solubility and Solvation of Bioactive Bicyclic Derivatives in Organic Solvents
• Separation of Azeotropes Hexane + Ethanol/1-Propanol by Ionic Liquid Extraction: Liquid-Liquid Phase Equilibrium Measurements and Thermodynamic Modeling
• Determination and Correlation of Solubility and Thermodynamic Properties of trans-Cinnamyl Alcohol in Pure and Binary Solvents from 253.15 K to 293.15 K
• Measurement and Correlation of Solubility of Resorcinol Bis(cyclic 2,2-dimethyl-1,3-propanediol phosphate) in Selected Solvents from T = 293.15 to 333.15 K
• Measurement and Correlation of the Solubilities of Sulfur S8 in 10 Solvents
• Isobaric Vapor-Liquid Equilibrium Data for Two Binary Systems n-Hexane + 1,2-Dimethoxyethane and Methylcyclopentane + 1,2-Dimethoxyethane at 101.3 kPa
• Effect of the Type of Ammonium Salt on the Extractive Desulfurization of Fuels Using Deep Eutectic Solvents
• Isothermal Vapor-Liquid Equilibrium Data for Binary Mixtures of Hexafluoroethane (R116) + n-Pentane or n-Hexane at Two Temperatures, 288 and 296 K
• Measurement and Correlation of the Dissolution Equilibria of o-Iodoaniline and p-Iodoaniline in Pure Solvents
• Determination, Correlation, and Application of Sodium l-Ascorbate Solubility in Nine Pure Solvents and Two Binary Solvents at Temperatures from 278.15 to 323.15 K
• Experimental Phase Equilibrium for the Binary System of n-Pentane +2-Propanol Using a New Equilibrium Cell and the Static Total Pressure Method
• Solubility Measurement and Thermodynamic Modeling of Benzoic Acid in Monosolvents and Binary Mixtures
• 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
• Solubility Measurement and Correlation for epsilon-2,4,6,8,10,12-Hexanitro-2,4,6,8,10,12-hexaazaisowurtzitane in Different Alkanes/Aromatic Hydrocarbon + Ethyl Acetate Binary Solvents at Temperatures of between 283.15 and 323.15 K
• Liquid-Liquid Extraction of Alcohols from Their Azeotropic Mixtures with Hexane Using Ionic Liquid
• Solubilities of Organic Semiconductors and Nonsteroidal Anti-inflammatory Drugs in Pure and Mixed Organic Solvents: Measurement and Modeling with Hansen Solubility Parameter
• Measurement of Critical Properties for Binary and Ternary Mixtures Containing n-Butanol and n-Alkane
• Thermophysical Study of Binary Systems of tert-Amyl Methyl Ether with n-Hexane and m-Xylene
• Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
• Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
• Solubility Determination and Correlation of Warfarin Sodium 2-Propanol Solvate in Pure, Binary, and Ternary Solvent Mixtures
• Binary Solid-Liquid Solubility Determination and Model Correlation of Quizalofop-p-ethyl in Different Pure Solvents
• Isothermal Vapor-Liquid Equilibrium Measurements for Alcohol + Water/n-Hexane Azeotropic Systems Using Both Dynamic and Automated Static-Synthetic Methods
• Measuring Activity Coefficient at Infinite Dilution of Hydrocarbons in Ionic Liquids and Evaluation of Other Thermodynamic Properties using Gas Chromatography
• Thermodynamic Models for Determination of Solid-Liquid Equilibrium of the Buprofezin in Pure and Binary Organic Solvents
• Measurement and Prediction of Excess Properties of Binary Mixtures Methyl Decanoate + an Even-Numbered n-Alkane (C6-C16) at 298.15 K
• Reactive Extraction of Gallic Acid Using Tributyl Phosphate in Different Classes of Diluents
• Liquid-Liquid Equilibrium for Ternary Systems of N-Methylformamide + Pyrrole/Indole + Alkanes at 298.15 K: Phase Equilibrium Measurement and Correlation
• Influence of a-Olefin Concentration and Length on the High-Pressure Phase Behavior of (a-Olefin + n-Hexane + LLDPE) Systems
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• Liquid-Liquid Equilibrium Data for Ternary Systems Containing Alkanes (n-Pentane, n-Hexane, n-Heptane, and n-Octane) + Alcohol (Methanol and Ethanol) + Protic Ionic Liquid (2-HEAF)
• 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 of n-Hexane and Setchenov's Constants in Aqueous Solutions of KCl, NaCl, NaBr, and NaNO3
• Liquid-Liquid Equilibrium Measurements for the Extraction of Pyridine and Benzothiazole from n-Alkanes Using Deep Eutectic Solvents
• Solubility, Solubility Modeling, and Antisolvent Precipitation of 1,3-Bis(9-carbazolyl)benzene in Organic Solvents
• Isothermal Vapor-Liquid Equilibrium Data for the Binary Systems Consisting of 1,1,2,3,3,3-Hexafluoro-1-propene and Either Methylcyclohexane, Cyclohexane, n-Hexane, 2-Methyltetrahydrofuran, or 2,2,3,3,4,4,4-Heptafluoro-1-butanol
• Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
• 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
• Solubility measurement and thermodynamic model correlation of sancycline in twelve pure solvents
• Liquid-liquid equilibria for mixtures of (Furfural + an Aromatic hydrocarbon + an alkane) at T=298.15 K
• Phase Equilibria of Water + Furfural and Dichloromethane + n-Hexane
• Thermodynamic Properties of Mixtures Containing Precursors of Vitamin B5
• Liquid-Liquid Equilibria for Mixtures of (Furfural + a Chlorinated Aromatic Compound + an Alkane) at T = 298.15 K
• Measurements, Correlations, and Predictions of Viscosities for the Ternary Mixture (2-Butanol + Hexane + 1-Chlorobutane) at 298.15 K and 313.15 K
• Vapor-Liquid Equilibria for Four Binary Systems at 363.15 K: N-Methylformamide + Hexane, + Benzene, + Chlorobenzene, and + Acetonitrile
• Viscosities of Dimethyl Carbonate or Diethyl Carbonate with Alkanes at Four Temperatures. New UNIFAC-VISCO Parameters
• Solubility of 1-Alkyl-3-methylimidazolium Hexafluorophosphate in Hydrocarbons
• Excess Enthalpies of the Ternary Mixtures: Tetrahydrofuran + (Hexane or Cyclohexane) + Decane at 298.15K
• Measurement and correlation of vapor-liquid equilibria for the 2-propanol + n-hexane system near the critical
• Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
• Determination of Isobaric Thermal Expansivity of Organic Compounds from 0.1 to 30 MPa at 30 C with an Isothermal Pressure Scanning Microcalorimeter
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Hexyl-3-methylimidazolium Hexafluorophosphate from Gas-Liquid Chromatography
• Solubilities of n-Alkanes (C6 to C8) in Water from 30 0C to 180 0C.
• Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethanediol, + Hexane, + Tributylamine, or + Triethylamine at (298.15, 303.15, and 308.15) K
• Solubility of -Carotene in Binary Solvents Formed by Some Hydrocarbons with Dibutyl Ether and 1,2-Dimethoxyethane
• Densities and Excess Molar Properties of Dimethyl Carbonate with Alkanes (C6 to C10) and VLE of Dimethyl Carbonate with Alkanes (C9 to C10) at 101.3 kPa
• Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid 1-Hexyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography at the Temperatures 298.15 K and 323.15 K
• Partition Coefficients of Organic Solutes between Supercritical Carbon Dioxide and Water: Experimental Measurements and Empirical Correlations
• Measurement and Correlation of Phase Equilibria for Water + Decane + 2-Propanol, Water + Hexane + 2-Propanol, and Water + Decane + 2-Butanol Ternary Systems at 573 and 593 K and 15.0 and 20.0 MPa
• Viscosities and Densities of Binary Mixtures of Hexane with 1-Chlorohexane between 293.15 K and 333.15 K
• Solubility of Benzophenone in Binary Alkane + Carbon Tetrachloride Solvent Mixtures
• Critical Properties of Binary and Ternary Mixtures of Hexane + Methanol, Hexane + Carbon Dioxide, Methanol + Carbon Dioxide and Hexane + Carbon Dioxide + Methanol
• Determination and Study on the Solubility of Methane in Heptane + Cyclohexane and Heptane + Ethanol at High Pressures
• 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
• Measurement and Prediction of Excess Molar Enthalpies and Excess Molar Volumes of the Ternary System 1,3-dichlorobenzene + Benzene + Hexane at 298.15 K.
• Liquid-Liquid Equilibria for Monoethylene Glycol + Water + Alkane Systems in the Range (273 to 313) K and Atmospheric Pressure
• Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with tert-Butyl Methyl Ether and with tert-Amyl Methyl Ether
• Experimental and predicted viscosities of the ternary mixture (hexane + 1,3-dioxolane + 2-butanol) at 298.15 and 313.15 K
• Measurement and Prediction of Solubility of Four Arylamine Molecules in Benzene, Hexane, and Methanol
• Phase Separation in Binary Mixtures Containing Linear Perfluoroalkanes
• Vapor-Liquid Equilibria and Excess Enthalpies for Binary Systems of Dimethoxymethane with Hydrocarbons
• Measurement of Diffusion Coefficients in Thermodynamically Nonideal Systems
• Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
• Determination of Activity Coefficients at Infinite Dilution of Polar and Nonpolar Solutes in the Ionic Liquid 1-Ethyl-3-methyl- imidazolium Bis(trifluoromethylsulfonyl) Imidate Using Gas-Liquid Chromatography at the Temperature 303.15 K or 318.15 K
• High-Pressure Densities of the Binary Mixture Methyl Nonafluorobutyl Ether + Hexane
• Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid 1-Butyl-3-methylimidazolium Octyl Sulfate Using Gas-Liquid Chromatography at a Temperature of 298.15 K, 313.15 K, or 328.15 K
• Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
• Vapor-Liquid Equilibrium Data for the Ethylene + Hexane System
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 5. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-butyl-imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 6. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-octyl-imidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
• Experimental (P, V, T, x) Data for the Mixture Ethyl Nonafluorobutyl Ether + n-Hexane
• Densities, Surface Tensions, and Refractive Indexes of Propyl Propanoate + Hexane + m-Xylene at 298.15 K
• Thermodynamics of Mixtures Containing a Strongly Polar Compound. 8. Liquid-Liquid Equilibria for N,N-Dialkylamide + Selected N-Alkanes
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
• Determination and Study of the Solubility of Methane in Mixtures of Methanol plus Various Hydrocarbons at High Pressures
• Solubilities at High Dilution of Toluene, Ethylbenzene, 1,2,4-Trimethylbenzene, and Hexane in Di-2-ethylhexyl, Diisoheptyl, and Diisononyl Phthalates
• Liquid-Liquid Coexistence Curves for Binary Systems: Methanol + Cyclohexane and + Several Isomers of Hexane
• Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Vapor-Liquid Equilibrium of Ferrocene in Some Organic Solvents Using Spectroscopic Methods
• Distribution of Butyric Acid between Water and Several Solvents
• Thermodynamic Properties of Mixtures Containing Ionic Liquids: Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Propyl Boronic Acid-3-Alkylimidazolium Bromide and 1-Propenyl-3-alkylimidazolium Bromide Using Inverse Gas Chromatography
• Measurement and Correlation of Solubilities of Luteolin in Organic Solvents at Different Temperatures
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Ternary Liquid-Liquid Equilibria for Mixtures of an Aromatic + an Aliphatic Hydrocarbon + 4-Methyl-N-butylpyridinium Tetrafluoroborate
• Phase Equilibrium Properties of Binary and Ternary Mixtures Containing 1,1-Dimethylethyl Methyl Ether, 1-Propanol, and Hexane at T ) 313.15 K
• Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Binary Mixtures at 298.15 K
• Infinite Dilution Activity Coefficients for Trihexyltetradecyl Phosphonium Ionic Liquids: Measurements and COSMO-RS Prediction
• Measurement and Correlation of CO2 Solubility in the Systems of CO2 + Toluene, CO2 + Benzene, and CO2 + n-Hexane at Near-Critical and Supercritical Conditions
• Vapor-Liquid Equilibrium for Binary System of Thiophene + n-Hexane at (338.15 and 323.15) K and Thiophene + 1-Hexene at (333.15 and 323.15) K
• High-Pressure Vapor-Liquid Equilibria in the Nitrogen + n-Hexane System
• Isobaric Vapor-Liquid Equilibrium Data and Excess Properties of Binary Systems Comprised of Alkyl Methanoates + Hexane
• Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
• Solubility of Anthracene in Binary Diisopropyl Ether + Alkane Solvent Mixtures at 298.15 K
• Thermophysical Properties of Binary Mixtures of 2-Methyl-1-propanol with Hexane, Octane, and Decane at 298.15 K
• Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Vapor-Liquid Equilibrium for Binary System of Diethyl Sulfide + n-Hexane at (338.15 and 323.15) K and Diethyl Sulfide + 1-Hexene at (333.15 and 323.15) K
• Densities and Viscosities of Binary Mixtures of Tributyl Phosphate with Hexane and Dodecane from (298.15 to 328.15) K
• Solubility of 5-(Dithiolan-3-yl)pentanoic Acid in the Mixed Solvents of Cyclohexane + Ethyl Acetate, Heptane + Ethyl Acetate, and Hexane + Ethyl Acetate
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
• Extraction Ability of Nitrogen-Containing Compounds Involved in the Desulfurization of Fuels by Using Ionic Liquids
• Solubility of Artemisinin in Different Single and Binary Solvent Mixtures Between (284.15 and 323.15) K and NRTL Interaction Parameters
• Separation of Benzene from Linear Alkanes (C6-C9) Using 1-Ethyl-3-Methylimidazolium Ethylsulfate at T = 298.15 K
• Surface Tensions of the Ternary Mixtures Containing an Isomeric Butanol + n-Hexane + 1-Chlorobutane at 298.15 K
• Interfacial Tension of n-Alkane and Ionic Liquid Systems
• 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
• Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
• Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
• Measurement and Correlation for the Solubilities of Dihydrocapsaicin in n-Heptane, n-Hexane, n-Pentane, Ethyl Acetate, Acetone, Ethanol, and Water
• Influence of Anion Structure on the Liquid-Liquid Equilibria of 1-Ethyl-3-methyl-imidazolium Cation Based Ionic Liquid-Hydrocarbon Binary Systems
• Solubility of Dexibuprofen in Different Solvents from (263.15 to 293.15) K
• Solubility of Imperatorin in Ethyl Acetate, Ethanol, Methanol, n-Hexane, and Petroleum Ether from (278.2 to 318.2) K
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Butyl-3-methylimidazolium Nitrate Using Gas-Liquid Chromatography
• Vapor-Liquid Equilibria Measurements of the Methane + Pentane and Methane + Hexane Systems at Temperatures from (173 to 330) K and Pressures to 14 MPa
• Vapor-Liquid Equilibrium for Methoxymethane + Methyl Formate, Methoxymethane + Hexane, and Methyl Formate + Methanol
• Solubilities of 1-Hexyl-3-methylimidazole Nitrate and 1-Octyl-3-methylimidazole Nitrate in Selected Solvents
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Experimental Determination of Quaternary and Ternary Isobaric Vapor Liquid Liquid Equilibrium and Vapor Liquid Equilibrium for the Systems Water Ethanol Hexane Toluene and Water Hexane Toluene at 101.3 kPa
• Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Ethyl-3-methylimidazolium Diethylphosphate Using Gas Liquid Chromatography
• Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
• Interfacial Tensions of Imidazolium-Based Ionic Liquids with N-Alkanes and Cyclohexane
• Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
• Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
• Volumetric Properties for the Binary Systems Hexane + Octane and Hexane + Decane at High Temperatures and Pressures
• Computer Aided Solvent scanning for the Separation of 2-methoxynaphthene and 2-acetyl-6-methoxynaphthalene
• Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Dibutylphosphate Using Gas Liquid Chromatography
• Thermodynamics of Solubility Processes of Novel Drug-like Spiro-Derivatives in Model Biological Solutions
• Isobaric Vapor Liquid Equilibrium of Binary Systems of Hexane or Octane with 1,2-Dimethylbenzene or 1,3-Dimethylbenzene at 101.3 kPa
• Solubilities of Bis(2,4,6-trimethylbenzoyl)phenylphosphine Oxide in Different Organic Solvents at Several Temperatures
• Solubility of Benzoic Acid in Mixtures of CO2 + Hexane
• Biomass-Derived Platform Chemicals: Thermodynamic Studies on the Extraction of 5-Hydroxymethylfurfural from Ionic Liquids
• Isobaric Vapor Liquid Equilibria of Tertiary Amine and n-Alkane/Alkanol Binary Mixtures: Experimental Measurements and Modeling with GC-PPC-SAFT
• Vapor Liquid Equilibrium, Densities, and Interfacial Tensions of the System Hexane + 2,5-Dimethylfuran
• Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
• Liquid Liquid Equilibria for Dipropylene Glycol Hydrocarbon Binary Systems: Experimental Data and Regression
• Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
• Solubility of p-Nitroaniline in Supercritical Carbon Dioxide with and without Mixed Cosolvents
• Multiproperty Correlation of Experimental Data of the Binaries Propyl Ethanoate + Alkanes (Pentane to Decane). New Experimental Information for Vapor Liquid Equilibrium and Mixing Properties
• A Promising Ionic Liquid [BMIM][FeCl4] for the Extractive Separation of Aromatic and Aliphatic Hydrocarbons
• Solubilities of Rutaecarpine in Twelve Organic Solvents from (283.2 to 323.2) K
• Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
• Solubility of Benzyl Disulfide in Five Organic Solvents between (283.45 and 333.15) K
• Vapor Liquid Equilibrium Data for the Morpholine-4-carbaldehyde + n-Hexane or n-Heptane Binary Systems Using a Static-Synthetic Apparatus
• Solubility and Transfer Processes of Some Hydrazones in Biologically Relevant Solvents
• Solubility and Dissolution Thermodynamic Data of Mefenamic Acid Crystals in Different Classes of Organic Solvents
• Solubility of Dichloronitrobenzene in Eight Organic Solvents from T = (278.15 to 303.15) K: Measurement and Thermodynamic Modeling
• Interfacial Tension of the n-Hexane Water System under the Influence of Magnetite Nanoparticles and Sodium Dodecyl Sulfate Assembly at Different Temperatures
• Dissociation Constants and Solubilities of Daidzein and Genistein in Different Solvents
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Liquid Liquid Equilibria for the Ternary Systems of FC3283 + HFE7300 + Hexane, FC3283 + HFE7500 + Octane, and FC72 + HFE7100 + (Acetonitrile or Ethyl Acetate) at 273.15 K, 298.15 K, and 313.15 K
• Article Previous Article Next Article Articles ASAP Phase Equilibrium of Binary Mixtures of n-Hexane + Branched Chlorobutanes: Experimental Results and Group Contribution Predictions
• New Vapor Liquid Liquid Equilibrium Solubility Data for iso-Butane, n-Butane, n-Pentane, and n-Hexane in Alkanolamine Aqueous Solutions
• Liquid Liquid Extraction of Toluene from n-Alkanes using {[4empy][Tf2N] + [emim][DCA]} Ionic Liquid Mixtures
• Solubility and Solution Thermodynamics of Novel Bicyclic Derivatives of 1,3-Selenazine in Biological Relevant Solvents
• Comparison Study on Temperature Dependence of the Interfacial Tension of n-Alkane Water and n-Alcohol Water Two Binary Systems
• Enhancing liquid-phase olefin-paraffin separations using novel silver-based ionic liquids
• Liquid Liquid Equilibrium in Mixtures Containing Propane-1,2,3-triol and Mixtures Containing Vegetable Oils at Atmospheric Pressure
• Measurement and Correlation of Solubility of Tetraphenyl Piperazine-1,4-diyldiphosphonate in Mixed Solvents
• Determination of the Critical Properties of C6 C10 n-Alkanes and Their Binary Systems Using a Flow Apparatus
• Impact of Sulfonamide Structure on Solubility and Transfer Processes in Biologically Relevant Solvents
• Solubilities of Naringin and Naringenin in Different Solvents and Dissociation Constants of Naringenin
• Selective Separation of Aromatics from Paraffins and Cycloalkanes Using Morpholinium-Based Ionic Liquid
• Solubility Determination and Thermodynamic Models for 2-Methylnaphthalene in Different Solvents from T = (278.15 to 303.15) K
• Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
• Measurement of the Critical Properties of the Ternary Systems Hexane + Heptane + Octane and Octane + Nonane + Decane Using a Flow Apparatus
• Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
• Solubility of Atractylenolide III in Hexane, Ethyl Acetate, Diethyl Ether, and Ethanol from (283.2 to 323.2) K
• Measurement and Correlation of Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Alkane and Cycloalkane Solvents
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Liquid-Liquid Equilibria for Systems Composed by 1-Methyl-3-octylimidazolium Tetrafluoroborate Ionic Liquid, Thiophene, and n-Hexane or Cyclohexane
• Vapor-Liquid Equilibrium and Excess Gibbs Energies of Hexane + N,N-Dimethyl Formamide, 2-Methylpropan-2-ol + 2-Aminophenol, N,N-Dimethyl Formamide, and 2-Propanol + Diisopropyl Amine at 94.4 kPa
• Liquid - Liquid Equilibria for the Binary Systems of Sulfolane with Alkanes
• Measurements and Calculation of Vapor-Liquid Equilibria for the Binary Mixtures of Fluorobenzene and Alkanes at a Pressure of 101.4 kPa
• Study of the Temperature Dependence of Surface Tensions of Some Alkanol + Hexane Mixtures
• Henry s Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethylether, Chloroethane, 1,1-Difluoroethane, and Hexane in Tetrahydropyran
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• Isobaric Vapor-Liquid Equilibrium for the Binary Systems 1-Pentanol + Cyclohexane and 1-Pentanol + n-Hexane at Low Alcohol Compositions
• 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
• Effect of an Ionic Liquid (IL) Cation on the Ternary System (IL + p-Xylene + Hexane) at T= 298.15 K
• Experimental Densities of Hexane + Benzothiophene Mixtures from (313 to 363) K and up to 20 MPa
• Liquid Liquid Equilibria of Mixtures Containing Methyl Acetate + Methanol + Hexane or Heptane
• Isobaric Vapor-Liquid Equilibria of Hexane + 1-Decene and Octane + 1-Decene Mixtures
• Diffusion Coefficients of Organic Compounds at Infinite Dilution in Mixtures Involving Associating Compounds. Experimental Determination and Modeling by Group Contribution Methods
• Phase Equilibria of (1-Ethyl-3-methylimidazolium Ethylsulfate + Hydrocarbon, + Ketone, and + Ether) Binary Systems
• Solubilities of Stearic Acid in Organic Solvents and in Azeotropic Solvent Mixtures
• Excess Enthalpies and Thermal Conductivity Coefficients for Binary Mixtures of Carbon Tetrachloride and Four Alkanes (C5 to C8) at a Temperature of 298.15 K
• Densities and Excess Volumes of the 1-Chlorobutane + n-Hexane System at Temperatures from (283.15 to 333.15) K and Pressures from (0.1 to 35) MPa
• Setup and Validation of a PGT Measuring Device. Volumetric Behavior of the Mixture 1,8-Cineole + Ethanol
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Hexyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• Densities and Viscosities of the Ternary Mixtures 2-Methyl-1-propanol (or 2-Methyl-2-propanol) + N-Hexane + 1-Chlorobutane at 298.15 K
• Phase Equilibria of the Azeotropic Mixture Hexane + Ethyl Acetate with Ionic Liquids at 298.15 K
• Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
• Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid, Trihexyltetradecylphosphonium Bis(trifluoromethylsulfonyl) Imide, Using Gas-Liquid Chromatography at T ) (303.15, 308.15, 313.15, and 318.15) K
• Determination and Correlation of Excess Molar Enthalpies of Eight Binary Systems Containing Acetophenone at Different Temperatures
• 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
• Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
• Solubilities of Palmitic Acid in Pure Solvents and Its Mixtures
• Densities and Viscosities of Binary Mixtures of Tris(2-ethylhexyl) Phosphate + Cyclohexane or n-Hexane at T ) (293.15, 298.15, and 303.15) K and p ) 0.1 MPa
• Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water)
• Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
• Thermophysical Characterization of Liquids Using Precise Density and Isobaric Heat Capacity Measurements As a Function of Pressure
• Solubilities of Lauric Acid in n-Hexane, Acetone, Propanol, 2-Propanol, 1-Bromopropane, and Trichloroethylene from (279.0 to 315.3) K
• Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
• In Situ Determination of Phase Equilibria of Methyl Benzoate + Alkane Mixtures Using an Infrared Absorption Method. Comparison with Polar GC-SAFT Predictions
• Separation of Hexane/Ethanol Mixtures. LLE of Ternary Systems (Ionic Liquid or Hyperbranched Polymer + Ethanol + Hexane) at T ) 298.15 K
• Solubility of Deflazacort in Binary Solvent Mixtures
• Volumetric Behavior of the Binary Mixtures of Methyl Ethyl Ketone with n-Hexane, Cyclohexane, and Benzene at T ) (303.15, 313.15, and 323.15) K
• Viscosity and Density of Binary Mixtures of Ethyl Alcohol with n-Alkanes (C6, C8, and C10)
• Liquid-Liquid-Supercritical Fluid Equilibria for Systems Containing Carbon Dioxide, Propane, and Triglycerides
• Solubility of Valsartan in Ethyl Acetate + Hexane Binary Mixtures from (278.15 to 313.15) K
• Solubilities of Methyldiphenylphosphine Oxide in Selected Solvents
• Liquid-Liquid Equilibria for Monoethylene Glycol + Hexane and 2,2,4-Trimethylpentane, Water + Hexane and 2,2,4-Trimethylpentane, Monoethylene Glycol + Water + Hexane, and Monoethylene Glycol + Water + 2,2,4-Trimethylpentane in the Temperature Range between T = 283.15 K and T = 323.15 K
• Measurement and Correlation of Bubble Point Pressure in (CO2 + C6H6), (CO2 + CH3C6H5), (CO2 + C6H14), and (CO2 + C7H16) at Temperatures from (293.15 to 313.15) K
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Ternary Liquid-Liquid Equilibria Measurement for Hexane and Benzene with the Ionic Liquid 1-Butyl-3-methylimidazolium Methylsulfate at T = (298.2, 313.2, and 328.2) K
• Isothermal Vapor-Liquid Equilibrium of Ternary Mixtures Containing 2-Methyl-1-propanol or 2-Methyl-2-propanol, n-Hexane, and 1-Chlorobutane at 298.15 K
• Solubilities of Cinnamic Acid Esters in Organic Solvents
• Phase Equilibria of (1-Hexyl-3-methylimidazolium Thiocyanate + Water, Alcohol, or Hydrocarbon) Binary Systems
• Vapor-Liquid Equilibria in Binary Systems Formed by n-Hexane with Alcohols
• Liquid-Liquid Equilibrium for Ternary Mixtures of Hexane + Aromatic Compounds + [EMpy][ESO4] at T = 298.15 K
• Phase Equilibria for Liquid Mixtures of (an Alkane + Toluene + Dimethyl Phthalate)
• Surface Tension Deviations and Excess Molar Volumes on the Ternary System Propyl Propanoate + Hexane + p-Xylene at 298.15 K
• Density, Viscosity, and Speed of Sound of (Methyl Benzoate + Cyclohexane), (Methyl Benzoate + n-Hexane), (Methyl Benzoate + Heptane), and (Methyl Benzoate + Octane) at Temperatures of (303.15, 308.15, and 313.15) K
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
• Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tris(pentafluoroethyl)trifluorophosphate [EMIM][FAP] Using Gas-Liquid Chromatography
• ss-Sitosterol Solubility in Selected Organic Solvents
• Miscibility of Trihexyl(tetradecyl)phosphonium Chloride with Alkanes
• Solubility of Triadimefon in Organic Solvents at Temperatures between (288.15 and 333.15) K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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