Chemical Properties of Octane (CAS 111-65-9)

InChI

InChI=1S/C8H18/c1-3-5-7-8-6-4-2/h3-8H2,1-2H3

InChI Key

TVMXDCGIABBOFY-UHFFFAOYSA-N

Formula

C8H18

SMILES

CCCCCCCC

Molecular Weight¹

114.23

CAS

111-65-9

Other Names

• Oktan
• Oktanen
• Ottani
• UN 1262
• n-C8H18
• n-octane

• 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).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• 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).
• 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.
• 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	[0.3940; 0.3980]
ω	0.3940		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.3942		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.3970		ChemSep v8.3 pure component data Compiled value
ω	0.3980		KDB
Tig	493.15	K	KDB
AP	343.750	K	KDB
ΔcH°liquid	[-5471.80; -5270.40]	kJ/mol
ΔcH°liquid	-5470.30 ± 1.60	kJ/mol	NIST
ΔcH°liquid	-5470.71 ± 0.67	kJ/mol	NIST
ΔcH°liquid	-5466.60	kJ/mol	NIST
ΔcH°liquid	-5471.80 ± 5.40	kJ/mol	NIST
ΔcH°liquid	-5441.30	kJ/mol	NIST
ΔcH°liquid	Outlier -5270.40	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	[0.0005180; 0.0005180]	Pa×s
η	0.0005180	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	0.0005180	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	0.0005180	Pa×s	Thermophysical Properties of Binary Mixtures of 2-Methyl-1-propanol with Hexane, Octane, and Decane at 298.15 K
LFL	1.00	% in Air	KDB
UFL	6.50	% in Air	KDB
Tflash,oc	286.48	K	KDB
ΔfG°	[16.00; 16.40]	kJ/mol
ΔfG°	16.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	16.40	kJ/mol	KDB
Rg	4.6800		KDB
Δc,grossH	5470.71	kJ/mol	KDB
Δc,netH	5074.565	kJ/mol	KDB
ΔfH°gas	[-208.75; -208.22]	kJ/mol
ΔfH°gas	-208.22 ± 0.79	kJ/mol	Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas	-208.75	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-208.60	kJ/mol	KDB
ΔfH°gas	-208.70	kJ/mol	NIST
ΔfH°gas	-208.40 ± 0.67	kJ/mol	NIST
ΔfH°liquid	[-250.30; -250.00]	kJ/mol
ΔfH°liquid	-250.30 ± 1.80	kJ/mol	NIST
ΔfH°liquid	-250.00 ± 0.84	kJ/mol	NIST
ΔfusH°	16.48	kJ/mol	Joback Calculated Property
ΔvapH°	[34.00; 41.60]	kJ/mol
ΔvapH°	41.53	kJ/mol	NIST
ΔvapH°	41.60	kJ/mol	NIST
ΔvapH°	41.50 ± 0.10	kJ/mol	NIST
ΔvapH°	41.50 ± 0.10	kJ/mol	NIST
ΔvapH°	41.50	kJ/mol	NIST
ΔvapH°	41.60 ± 0.08	kJ/mol	NIST
ΔvapH°	41.60 ± 0.08	kJ/mol	NIST
ΔvapH°	41.50 ± 0.10	kJ/mol	NIST
ΔvapH°	41.48	kJ/mol	NIST
ΔvapH°	Outlier 34.00	kJ/mol	NIST
IE	[9.71; 10.25]	eV
IE	9.80 ± 0.15	eV	NIST
IE	10.01	eV	NIST
IE	9.80 ± 0.10	eV	NIST
IE	9.71 ± 0.15	eV	NIST
IE	9.79	eV	NIST
IE	10.25	eV	NIST
log10WS	[-5.24; -5.24]
log10WS	-5.24		Aq. Solubility Prediction
log10WS	-5.24		Estimated Solubility
logPoct/wat	3.367		Crippen Calculated Property
McVol	123.580	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
Pc	[2470.00; 2497.12]	kPa
Pc	2490.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Pc	2494.62	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	2486.25	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	2490.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	2490.00	kPa	KDB
Pc	2490.00 ± 30.00	kPa	NIST
Pc	2495.00 ± 20.00	kPa	NIST
Pc	2487.00	kPa	NIST
Pc	2480.00 ± 5.00	kPa	NIST
Pc	2490.00 ± 30.00	kPa	NIST
Pc	2486.93 ± 17.23	kPa	NIST
Pc	2486.20 ± 40.53	kPa	NIST
Pc	2488.00 ± 40.53	kPa	NIST
Pc	2492.59 ± 50.66	kPa	NIST
Pc	2497.10 ± 20.00	kPa	NIST
Pc	2497.12 ± 19.99	kPa	NIST
Pc	Outlier 2470.00 ± 98.07	kPa	NIST
Ptriple	2.11e-03	kPa	ChemSep v8.3 pure component data Compiled value
ρc	[231.88; 233.03]	kg/m3
ρc	231.88 ± 3.43	kg/m3	NIST
ρc	233.03 ± 10.05	kg/m3	NIST
ρc	231.88 ± 5.71	kg/m3	NIST
ρc	231.88	kg/m3	NIST
ρc	231.88 ± 2.51	kg/m3	NIST
ρc	232.68 ± 5.71	kg/m3	NIST
ρc	232.68 ± 2.28	kg/m3	NIST
S°gas	467.06 ± 0.92	J/mol×K	NIST
S°liquid	[359.80; 361.20]	J/mol×K
S°liquid	361.20	J/mol×K	NIST
S°liquid	359.80	J/mol×K	NIST
S°liquid	359.80	J/mol×K	NIST
Tboil	[393.15; 401.65]	K
Tboil	398.57	K	Isobaric vapor-liquid equilibrium for binary systemof 2-ethylthiophene + n-octane at 101.33 kPa
Tboil	398.83	K	Solutions of alkyl methanoates and alkanes: Simultaneous modeling of phase equilibria and mixing properties. Estimation of behavior by UNIFAC with recalculation of parameters
Tboil	398.79	K	Isothermal and isobaric (vapour + liquid) equilibria of (alpha-pinene + n-butanol + n-octane)
Tboil	398.60	K	Excess molar volumes of the ternary system {methylcyclohexane (1) + cyclohexane (2) + n-alkanes (3)} at T = 298.15 K
Tboil	399.15	K	Excess volumes, densities, speeds of sound and viscosities for the binary systems of diisopropyl ether with hydrocarbons at 303.15K
Tboil	398.65	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	398.83	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	398.49	K	Measurement and Modeling of Vapor Liquid Equilibria for the Octane + Sulfuric Acid + Water + Ethanol System
Tboil	398.74	K	Measurement and Modeling of Vapor Liquid Equilibria for the Octane + Sulfuric Acid + Water + Ethanol System
Tboil	398.82	K	ChemSep v8.3 pure component data Compiled value
Tboil	398.82	K	KDB
Tboil	398.80 ± 0.20	K	NIST
Tboil	398.80 ± 0.20	K	NIST
Tboil	398.90	K	NIST
Tboil	398.73 ± 0.10	K	NIST
Tboil	398.80	K	NIST
Tboil	398.76 ± 0.20	K	NIST
Tboil	398.96 ± 0.20	K	NIST
Tboil	398.96 ± 0.50	K	NIST
Tboil	398.93 ± 0.08	K	NIST
Tboil	398.70 ± 0.50	K	NIST
Tboil	398.75 ± 0.15	K	NIST
Tboil	398.55 ± 0.20	K	NIST
Tboil	398.12 ± 0.20	K	NIST
Tboil	398.77 ± 0.10	K	NIST
Tboil	398.95 ± 0.40	K	NIST
Tboil	398.76 ± 0.20	K	NIST
Tboil	398.75 ± 0.50	K	NIST
Tboil	398.55 ± 0.30	K	NIST
Tboil	398.77 ± 0.15	K	NIST
Tboil	398.27 ± 0.30	K	NIST
Tboil	399.00 ± 0.60	K	NIST
Tboil	398.40 ± 1.00	K	NIST
Tboil	398.85 ± 0.25	K	NIST
Tboil	398.82 ± 0.30	K	NIST
Tboil	399.15 ± 1.50	K	NIST
Tboil	397.80 ± 0.30	K	NIST
Tboil	Outlier 396.40 ± 2.00	K	NIST
Tboil	398.85 ± 0.40	K	NIST
Tboil	399.09 ± 0.30	K	NIST
Tboil	398.75 ± 0.10	K	NIST
Tboil	398.81 ± 0.44	K	NIST
Tboil	398.55 ± 0.30	K	NIST
Tboil	398.71 ± 0.20	K	NIST
Tboil	398.80 ± 0.40	K	NIST
Tboil	398.95 ± 0.50	K	NIST
Tboil	Outlier 393.15 ± 3.00	K	NIST
Tboil	398.81 ± 0.10	K	NIST
Tboil	398.90 ± 0.20	K	NIST
Tboil	398.25 ± 0.30	K	NIST
Tboil	398.62 ± 0.30	K	NIST
Tboil	397.85 ± 0.30	K	NIST
Tboil	397.20 ± 2.00	K	NIST
Tboil	398.75 ± 0.30	K	NIST
Tboil	398.80 ± 0.40	K	NIST
Tboil	398.85 ± 0.50	K	NIST
Tboil	397.35 ± 0.50	K	NIST
Tboil	398.75 ± 0.30	K	NIST
Tboil	398.90 ± 0.30	K	NIST
Tboil	398.75 ± 0.40	K	NIST
Tboil	398.81 ± 0.01	K	NIST
Tboil	397.65 ± 0.50	K	NIST
Tboil	397.40 ± 1.00	K	NIST
Tboil	398.15 ± 2.00	K	NIST
Tboil	398.70 ± 0.20	K	NIST
Tboil	398.95 ± 0.50	K	NIST
Tboil	398.90 ± 0.20	K	NIST
Tboil	398.75 ± 0.30	K	NIST
Tboil	398.81 ± 0.10	K	NIST
Tboil	398.80 ± 0.30	K	NIST
Tboil	397.15 ± 1.00	K	NIST
Tboil	398.75 ± 0.20	K	NIST
Tboil	Outlier 401.65 ± 0.50	K	NIST
Tboil	398.75 ± 0.30	K	NIST
Tboil	398.90 ± 0.20	K	NIST
Tboil	398.81 ± 0.20	K	NIST
Tboil	398.95 ± 0.20	K	NIST
Tboil	398.80 ± 0.05	K	NIST
Tboil	398.55 ± 0.50	K	NIST
Tboil	398.15 ± 0.60	K	NIST
Tboil	Outlier 396.00 ± 2.00	K	NIST
Tboil	398.55 ± 0.50	K	NIST
Tboil	398.75 ± 0.50	K	NIST
Tboil	398.74 ± 0.10	K	NIST
Tboil	398.35 ± 0.30	K	NIST
Tboil	398.55 ± 0.50	K	NIST
Tboil	398.74 ± 0.15	K	NIST
Tboil	397.75 ± 0.50	K	NIST
Tboil	398.95 ± 0.20	K	NIST
Tboil	398.15 ± 1.00	K	NIST
Tboil	397.65 ± 0.30	K	NIST
Tboil	399.00 ± 0.70	K	NIST
Tboil	399.00 ± 1.00	K	NIST
Tboil	398.15 ± 1.00	K	NIST
Tboil	398.95 ± 0.30	K	NIST
Tboil	398.15 ± 2.00	K	NIST
Tboil	398.95 ± 0.30	K	NIST
Tboil	398.64 ± 0.10	K	NIST
Tboil	398.45 ± 0.50	K	NIST
Tboil	Outlier 396.70 ± 1.50	K	NIST
Tc	[568.50; 569.60]	K
Tc	568.90	K	Measurement of critical properties for binary and ternary mixtures containing potential gasoline additive diethyl carbonate (DEC)
Tc	568.92	K	Experimental determination of critical data of multi-component mixtures containing potential gasoline additives 2-butanol by a flow-type apparatus
Tc	568.80	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	568.90	K	Measurement of Critical Properties for Binary and Ternary Mixtures Containing n-Butanol and n-Alkane
Tc	568.92	K	Determination of the Critical Properties of C6 C10 n-Alkanes and Their Binary Systems Using a Flow Apparatus
Tc	568.70	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Tc	568.80	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	568.83	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	568.70	K	ChemSep v8.3 pure component data Compiled value
Tc	568.70	K	KDB
Tc	568.70 ± 0.30	K	NIST
Tc	568.50 ± 1.00	K	NIST
Tc	568.60 ± 0.30	K	NIST
Tc	568.65 ± 0.20	K	NIST
Tc	568.80 ± 0.60	K	NIST
Tc	568.70	K	NIST
Tc	568.92 ± 0.10	K	NIST
Tc	568.60 ± 0.20	K	NIST
Tc	568.80	K	NIST
Tc	568.80 ± 0.70	K	NIST
Tc	568.80 ± 0.20	K	NIST
Tc	568.80 ± 0.40	K	NIST
Tc	569.00 ± 0.30	K	NIST
Tc	569.00 ± 0.40	K	NIST
Tc	568.80 ± 0.20	K	NIST
Tc	568.75 ± 0.30	K	NIST
Tc	568.74 ± 0.40	K	NIST
Tc	568.77 ± 0.40	K	NIST
Tc	568.56 ± 0.20	K	NIST
Tc	569.15 ± 0.60	K	NIST
Tc	Outlier 569.40 ± 1.00	K	NIST
Tc	Outlier 569.35 ± 0.50	K	NIST
Tc	Outlier 569.60 ± 1.00	K	NIST
Tfus	[215.85; 227.31]	K
Tfus	216.30	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	216.38	K	ChemSep v8.3 pure component data Compiled value
Tfus	216.30	K	KDB
Tfus	216.26	K	Aq. Solubility Prediction
Tfus	216.32 ± 0.10	K	NIST
Tfus	216.36 ± 0.20	K	NIST
Tfus	216.35 ± 0.15	K	NIST
Tfus	216.34 ± 0.02	K	NIST
Tfus	216.35 ± 0.15	K	NIST
Tfus	216.35 ± 0.10	K	NIST
Tfus	216.34 ± 0.15	K	NIST
Tfus	216.35 ± 0.10	K	NIST
Tfus	216.35 ± 0.15	K	NIST
Tfus	216.35 ± 0.10	K	NIST
Tfus	216.36 ± 0.19	K	NIST
Tfus	216.28 ± 0.03	K	NIST
Tfus	216.34 ± 0.15	K	NIST
Tfus	216.34 ± 0.10	K	NIST
Tfus	216.30 ± 0.20	K	NIST
Tfus	216.35 ± 0.20	K	NIST
Tfus	216.26 ± 0.08	K	NIST
Tfus	216.15 ± 0.30	K	NIST
Tfus	216.59 ± 0.20	K	NIST
Tfus	215.85 ± 0.30	K	NIST
Tfus	216.59 ± 0.20	K	NIST
Tfus	216.34 ± 0.01	K	NIST
Tfus	216.34 ± 0.02	K	NIST
Tfus	216.34 ± 0.02	K	NIST
Tfus	216.35 ± 0.01	K	NIST
Tfus	215.90 ± 0.40	K	NIST
Tfus	Outlier 227.31 ± 0.20	K	NIST
Tfus	216.00 ± 2.00	K	NIST
Tfus	216.15 ± 1.50	K	NIST
Tfus	216.15 ± 0.50	K	NIST
Tfus	216.31 ± 0.05	K	NIST
Tfus	216.25 ± 0.30	K	NIST
Tfus	216.35 ± 0.40	K	NIST
Tfus	216.65 ± 0.30	K	NIST
Tfus	216.35 ± 0.20	K	NIST
Tfus	217.15 ± 2.00	K	NIST
Tfus	216.00 ± 2.00	K	NIST
Tfus	216.33 ± 0.10	K	NIST
Tfus	216.25 ± 0.50	K	NIST
Tfus	216.25 ± 0.08	K	NIST
Tfus	216.65 ± 0.30	K	NIST
Ttriple	[215.60; 216.38]	K
Ttriple	216.38	K	ChemSep v8.3 pure component data Compiled value
Ttriple	216.37	K	KDB
Ttriple	216.37 ± 0.40	K	NIST
Ttriple	216.37 ± 0.03	K	NIST
Ttriple	216.36 ± 0.20	K	NIST
Ttriple	216.37 ± 0.20	K	NIST
Ttriple	216.36 ± 0.05	K	NIST
Ttriple	216.37 ± 0.02	K	NIST
Ttriple	215.80 ± 0.20	K	NIST
Ttriple	215.85 ± 0.20	K	NIST
Ttriple	Outlier 215.60 ± 0.25	K	NIST
UQi	4.94		ChemSep v8.3 pure component data Compiled value
URi	5.85		ChemSep v8.3 pure component data Compiled value
Vc	[0.492; 0.492]	m3/kmol
Vc	0.492	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Vc	0.492	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.492	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.492	m3/kmol	KDB
Vc	0.492	m3/kmol	NIST
VCOSTALD	0.49	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.40		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2590000; 0.2590860]
Zc	0.2590000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Zc	0.2590000		ChemSep v8.3 pure component data Compiled value
Zc	0.2590860		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	[232.74; 297.00]	J/mol×K	[385.65; 523.15]
Cp,gas	232.74 ± 0.47	J/mol×K	385.65	NIST
Cp,gas	238.95 ± 0.48	J/mol×K	398.15	NIST
Cp,gas	242.67	J/mol×K	405.70	NIST
Cp,gas	250.59 ± 0.50	J/mol×K	423.15	NIST
Cp,gas	263.02 ± 0.53	J/mol×K	448.15	NIST
Cp,gas	270.70	J/mol×K	462.50	NIST
Cp,gas	274.84 ± 0.55	J/mol×K	473.15	NIST
Cp,gas	285.98 ± 0.57	J/mol×K	498.15	NIST
Cp,gas	295.39	J/mol×K	522.70	NIST
Cp,gas	297.00 ± 0.59	J/mol×K	523.15	NIST
Cp,liquid	[232.60; 340.70]	J/mol×K	[220.00; 460.00]
Cp,liquid	232.60	J/mol×K	220.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	233.40	J/mol×K	230.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	235.00	J/mol×K	240.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	237.40	J/mol×K	250.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	240.30	J/mol×K	260.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	243.70	J/mol×K	270.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	244.90	J/mol×K	273.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	247.50	J/mol×K	280.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	248.16	J/mol×K	283.15	Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Cp,liquid	250.10	J/mol×K	288.15	Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Cp,liquid	250.12	J/mol×K	288.15	Thermodynamic behaviour of the binary systems dimethyl carbonate + n-octane or n-nonane
Cp,liquid	251.60	J/mol×K	290.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	252.24	J/mol×K	293.15	Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Cp,liquid	247.70	J/mol×K	293.70	NIST
Cp,liquid	252.40	J/mol×K	297.54	NIST
Cp,liquid	252.40	J/mol×K	298.00	NIST
Cp,liquid	253.20	J/mol×K	298.00	NIST
Cp,liquid	255.68	J/mol×K	298.15	NIST
Cp,liquid	253.72	J/mol×K	298.15	NIST
Cp,liquid	255.68	J/mol×K	298.15	NIST
Cp,liquid	254.11	J/mol×K	298.15	NIST
Cp,liquid	255.68	J/mol×K	298.15	NIST
Cp,liquid	255.68	J/mol×K	298.15	NIST
Cp,liquid	255.10	J/mol×K	298.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	252.92	J/mol×K	298.15	NIST
Cp,liquid	253.98	J/mol×K	298.15	Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Cp,liquid	254.07	J/mol×K	298.15	NIST
Cp,liquid	254.18	J/mol×K	298.15	NIST
Cp,liquid	254.02	J/mol×K	298.15	NIST
Cp,liquid	253.94	J/mol×K	298.15	Thermodynamic behaviour of the binary systems dimethyl carbonate + n-octane or n-nonane
Cp,liquid	254.14	J/mol×K	298.15	NIST
Cp,liquid	253.89	J/mol×K	298.15	NIST
Cp,liquid	251.50	J/mol×K	298.30	NIST
Cp,liquid	254.70	J/mol×K	299.00	NIST
Cp,liquid	253.93	J/mol×K	299.80	NIST
Cp,liquid	255.90	J/mol×K	300.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	256.50	J/mol×K	303.16	Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Cp,liquid	258.03	J/mol×K	308.15	Thermodynamic behaviour of the binary systems dimethyl carbonate + n-octane or n-nonane
Cp,liquid	258.05	J/mol×K	308.15	Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Cp,liquid	260.30	J/mol×K	310.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	260.87	J/mol×K	313.16	Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Cp,liquid	262.20	J/mol×K	318.15	NIST
Cp,liquid	262.70	J/mol×K	318.15	Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Cp,liquid	264.80	J/mol×K	320.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	264.78	J/mol×K	323.15	Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Cp,liquid	267.24	J/mol×K	328.15	Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Cp,liquid	269.40	J/mol×K	330.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	269.31	J/mol×K	333.15	Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Cp,liquid	274.00	J/mol×K	340.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	278.80	J/mol×K	350.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	283.70	J/mol×K	360.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	288.70	J/mol×K	370.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	293.90	J/mol×K	380.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	299.20	J/mol×K	390.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	304.60	J/mol×K	400.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	310.20	J/mol×K	410.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	315.90	J/mol×K	420.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	321.90	J/mol×K	430.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	328.00	J/mol×K	440.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	334.20	J/mol×K	450.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	340.70	J/mol×K	460.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
η	[0.0000325; 0.0007180]	Pa×s	[273.15; 583.10]
η	0.0007180	Pa×s	273.15	Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) K
η	0.0006710	Pa×s	278.15	Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) K
η	0.0006230	Pa×s	283.15	Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) K
η	0.0006247	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	0.0006140	Pa×s	283.15	A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
η	0.0005840	Pa×s	288.15	Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) K
η	0.0005380	Pa×s	293.15	Dynamic Viscosities of 2-Pentanol with Alkanes (Octane, Decane, and Dodecane) at Three Temperatures T ) (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO Interaction Parameters
η	0.0005340	Pa×s	293.15	Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
η	0.0005380	Pa×s	293.15	Dynamic viscosities of 2-butanol with alkanes (C8, C10, and C12) at several temperatures
η	0.0005523	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	0.0005420	Pa×s	293.15	A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
η	0.0005450	Pa×s	293.15	Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) K
η	0.0005439	Pa×s	293.15	Densities and Viscosities of Binary Mixtures of JP-10 with n-Octane or n-Decane at Several Temperatures
η	0.0005374	Pa×s	293.15	Viscosity and Density of Binary Mixtures of Ethyl Alcohol with n-Alkanes (C6, C8, and C10)
η	0.0005177	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of JP-10 with n-Octane or n-Decane at Several Temperatures
η	0.0005206	Pa×s	298.15	Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
η	0.0005060	Pa×s	298.15	Dynamic Viscosities of 2-Pentanol with Alkanes (Octane, Decane, and Dodecane) at Three Temperatures T ) (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO Interaction Parameters
η	0.0005087	Pa×s	298.15	Viscosity and Density of Binary Mixtures of Ethyl Alcohol with n-Alkanes (C6, C8, and C10)
η	0.0005060	Pa×s	298.15	Dynamic viscosities of 2-butanol with alkanes (C8, C10, and C12) at several temperatures
η	0.0005010	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
η	0.0005140	Pa×s	298.15	Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) K
η	0.0005080	Pa×s	298.15	A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
η	0.0004837	Pa×s	303.15	Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
η	0.0004830	Pa×s	303.15	A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
η	0.0004720	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
η	0.0004795	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of JP-10 with n-Octane or n-Decane at Several Temperatures
η	0.0004780	Pa×s	303.15	Dynamic viscosities of 2-butanol with alkanes (C8, C10, and C12) at several temperatures
η	0.0004910	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	0.0004780	Pa×s	303.15	Dynamic Viscosities of 2-Pentanol with Alkanes (Octane, Decane, and Dodecane) at Three Temperatures T ) (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO Interaction Parameters
η	0.0004828	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	0.0004860	Pa×s	303.15	Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) K
η	0.0004911	Pa×s	303.20	Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
η	0.0005014	Pa×s	303.20	Experimental Measurement of JP-10 Viscosity at 242.7-753.3 K under Pressures up to 6.00 MPa
η	0.0004913	Pa×s	303.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0004590	Pa×s	308.15	Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) K
η	0.0004500	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	0.0004340	Pa×s	313.15	Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) K
η	0.0004300	Pa×s	313.15	A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
η	0.0004150	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	0.0004306	Pa×s	313.15	Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
η	0.0004220	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
η	0.0004320	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	0.0004358	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of JP-10 with n-Octane or n-Decane at Several Temperatures
η	0.0004414	Pa×s	313.30	Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
η	0.0004426	Pa×s	313.30	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0004150	Pa×s	318.15	Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) K
η	0.0003864	Pa×s	323.15	Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
η	0.0003800	Pa×s	323.15	Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
η	0.0003870	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	0.0003940	Pa×s	323.15	Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) K
η	0.0003967	Pa×s	323.20	Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
η	0.0003961	Pa×s	323.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0003750	Pa×s	328.15	Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) K
η	0.0003430	Pa×s	333.15	Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
η	0.0003570	Pa×s	333.15	Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) K
η	0.0003495	Pa×s	333.15	Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
η	0.0003634	Pa×s	333.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0003632	Pa×s	333.20	Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
η	0.0003139	Pa×s	343.15	Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
η	0.0003140	Pa×s	343.15	Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
η	0.0003311	Pa×s	343.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0003352	Pa×s	343.20	Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
η	0.0003079	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	0.0003013	Pa×s	353.10	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0003012	Pa×s	353.10	Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
η	0.0003078	Pa×s	353.10	Experimental Measurement of JP-10 Viscosity at 242.7-753.3 K under Pressures up to 6.00 MPa
η	0.0002870	Pa×s	353.15	Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
η	0.0002840	Pa×s	353.15	Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
η	0.0002610	Pa×s	363.15	Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
η	0.0002765	Pa×s	363.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0002766	Pa×s	363.20	Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
η	0.0002487	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	0.0002540	Pa×s	373.30	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0002545	Pa×s	373.30	Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
η	0.0002341	Pa×s	383.00	Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
η	0.0002340	Pa×s	383.00	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0002208	Pa×s	393.10	Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
η	0.0002205	Pa×s	393.10	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0002028	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	0.0002019	Pa×s	403.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0002021	Pa×s	403.20	Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
η	0.0002070	Pa×s	403.20	Experimental Measurement of JP-10 Viscosity at 242.7-753.3 K under Pressures up to 6.00 MPa
η	0.0001924	Pa×s	413.20	Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
η	0.0001905	Pa×s	413.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0001665	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	0.0001762	Pa×s	423.20	Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
η	0.0001761	Pa×s	423.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0001642	Pa×s	433.10	Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
η	0.0001643	Pa×s	433.10	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0001527	Pa×s	443.20	Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
η	0.0001526	Pa×s	443.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0001393	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	0.0001416	Pa×s	453.10	Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
η	0.0001417	Pa×s	453.10	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0001465	Pa×s	453.10	Experimental Measurement of JP-10 Viscosity at 242.7-753.3 K under Pressures up to 6.00 MPa
η	0.0001321	Pa×s	463.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0001322	Pa×s	463.20	Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
η	0.0001228	Pa×s	473.10	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0001228	Pa×s	473.10	Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
η	0.0001168	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
η	0.0001138	Pa×s	483.10	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0001139	Pa×s	483.10	Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
η	0.0001069	Pa×s	493.10	Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
η	0.0001068	Pa×s	493.10	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0000947	Pa×s	498.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0001049	Pa×s	503.00	Experimental Measurement of JP-10 Viscosity at 242.7-753.3 K under Pressures up to 6.00 MPa
η	0.0000993	Pa×s	503.00	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0000995	Pa×s	503.00	Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
η	0.0000901	Pa×s	513.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0000755	Pa×s	523.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0000825	Pa×s	523.30	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0000753	Pa×s	533.40	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0000678	Pa×s	543.40	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0000692	Pa×s	553.40	Experimental Measurement of JP-10 Viscosity at 242.7-753.3 K under Pressures up to 6.00 MPa
η	0.0000607	Pa×s	553.40	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0000532	Pa×s	563.30	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0000444	Pa×s	573.30	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0000325	Pa×s	583.10	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
ΔfusH	[20.09; 21.80]	kJ/mol	[215.60; 216.60]
ΔfusH	20.09	kJ/mol	215.60	NIST
ΔfusH	20.65	kJ/mol	215.80	NIST
ΔfusH	20.74	kJ/mol	216.38	NIST
ΔfusH	20.74	kJ/mol	216.40	NIST
ΔfusH	21.80	kJ/mol	216.60	NIST
ΔsubH	68.10	kJ/mol	216.00	NIST
ΔvapH	[34.41; 44.40]	kJ/mol	[247.00; 537.50]
ΔvapH	44.40	kJ/mol	247.00	NIST
ΔvapH	43.00	kJ/mol	257.00	NIST
ΔvapH	41.75	kJ/mol	298.00	Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
ΔvapH	38.00 ± 0.10	kJ/mol	311.00	NIST
ΔvapH	40.50 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	41.90	kJ/mol	315.50	NIST
ΔvapH	36.70 ± 0.10	kJ/mol	328.00	NIST
ΔvapH	39.10 ± 0.10	kJ/mol	333.00	NIST
ΔvapH	35.40 ± 0.10	kJ/mol	344.00	NIST
ΔvapH	41.00	kJ/mol	348.50	NIST
ΔvapH	41.20	kJ/mol	348.50	NIST
ΔvapH	37.80 ± 0.10	kJ/mol	353.00	NIST
ΔvapH	39.20	kJ/mol	363.00	NIST
ΔvapH	34.41	kJ/mol	398.80	NIST
ΔvapH	34.41	kJ/mol	398.80	KDB
ΔvapH	36.30	kJ/mol	414.00	NIST
ΔvapH	39.40	kJ/mol	443.00	NIST
ΔvapH	35.50	kJ/mol	469.00	NIST
ΔvapH	34.90	kJ/mol	537.50	NIST
Pvap	[10.59; 199.97]	kPa	[333.15; 425.20]
Pvap	10.59	kPa	333.15	An equipment for dynamic measurements of vapour liquid equilibria and results in binary systems containing cyclohexylamine
Pvap	16.04	kPa	343.15	An equipment for dynamic measurements of vapour liquid equilibria and results in binary systems containing cyclohexylamine
Pvap	21.09	kPa	350.64	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	23.14	kPa	353.05	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	23.16	kPa	353.15	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)
Pvap	23.61	kPa	353.15	An equipment for dynamic measurements of vapour liquid equilibria and results in binary systems containing cyclohexylamine
Pvap	25.56	kPa	355.76	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	26.70	kPa	356.97	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	28.55	kPa	358.82	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	30.00	kPa	359.76	Measurement and Modeling of Vapor Liquid Equilibria for the Octane + Sulfuric Acid + Water + Ethanol System
Pvap	30.00	kPa	360.06	Measurement and Modeling of Vapor Liquid Equilibria for the Octane + Sulfuric Acid + Water + Ethanol System
Pvap	31.58	kPa	361.59	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	33.91	kPa	363.15	An equipment for dynamic measurements of vapour liquid equilibria and results in binary systems containing cyclohexylamine
Pvap	34.16	kPa	363.86	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	36.53	kPa	365.82	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	38.88	kPa	367.65	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	40.00	kPa	367.97	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	40.00	kPa	368.30	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	40.00	kPa	368.32	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	40.82	kPa	369.09	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	43.19	kPa	370.77	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	45.57	kPa	372.39	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	48.04	kPa	374.01	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	50.59	kPa	375.61	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	52.90	kPa	377.00	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	55.02	kPa	378.25	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	58.20	kPa	380.03	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	60.00	kPa	380.43	Measurement and Modeling of Vapor Liquid Equilibria for the Octane + Sulfuric Acid + Water + Ethanol System
Pvap	60.00	kPa	380.76	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	60.00	kPa	380.78	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	60.00	kPa	380.82	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	60.00	kPa	380.84	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	60.00	kPa	380.85	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	60.00	kPa	380.87	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	60.00	kPa	380.94	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	60.00	kPa	380.94	Measurement and Modeling of Vapor Liquid Equilibria for the Octane + Sulfuric Acid + Water + Ethanol System
Pvap	60.63	kPa	381.34	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	62.68	kPa	382.42	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	65.07	kPa	383.64	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	67.34	kPa	384.76	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	70.52	kPa	386.29	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	73.02	kPa	387.45	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	75.43	kPa	388.55	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	77.94	kPa	389.65	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	80.05	kPa	390.56	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	82.51	kPa	391.60	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	84.94	kPa	392.60	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	87.09	kPa	393.47	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	90.00	kPa	394.09	Measurement and Modeling of Vapor Liquid Equilibria for the Octane + Sulfuric Acid + Water + Ethanol System
Pvap	89.39	kPa	394.37	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	90.00	kPa	394.60	Measurement and Modeling of Vapor Liquid Equilibria for the Octane + Sulfuric Acid + Water + Ethanol System
Pvap	91.38	kPa	395.14	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	93.64	kPa	396.04	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	96.14	kPa	396.95	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	98.73	kPa	397.90	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	99.59	kPa	398.19	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	398.49	Measurement and Modeling of Vapor Liquid Equilibria for the Octane + Sulfuric Acid + Water + Ethanol System
Pvap	101.33	kPa	398.57	Isobaric vapor-liquid equilibrium for binary systemof 2-ethylthiophene + n-octane at 101.33 kPa
Pvap	100.68	kPa	398.59	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	398.74	Measurement and Modeling of Vapor Liquid Equilibria for the Octane + Sulfuric Acid + Water + Ethanol System
Pvap	101.32	kPa	398.83	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	103.61	kPa	399.61	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	106.23	kPa	400.53	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	108.30	kPa	401.23	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	110.71	kPa	402.03	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	113.09	kPa	402.81	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	114.65	kPa	403.32	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	116.17	kPa	403.81	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	117.10	kPa	404.10	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	119.25	kPa	404.79	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	121.60	kPa	405.51	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	124.10	kPa	406.27	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	126.61	kPa	407.03	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	129.50	kPa	407.89	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	132.46	kPa	408.75	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	135.53	kPa	409.62	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	137.42	kPa	410.15	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	139.87	kPa	410.83	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	185.56	kPa	422.10	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	188.02	kPa	422.64	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	190.85	kPa	423.26	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	193.15	kPa	423.76	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	195.02	kPa	424.15	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	197.87	kPa	424.76	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	199.97	kPa	425.20	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
n0	[1.38550; 1.53910]		[277.80; 318.15]
n0	1.40400		277.80	The measurements of coexistence curves and light scattering for {xC6H5CN + (1- x)CH3(CH2)6CH3} in the critical region
n0	1.40320		279.68	The measurements of coexistence curves and light scattering for {xC6H5CN + (1- x)CH3(CH2)6CH3} in the critical region
n0	1.40280		280.36	The measurements of coexistence curves and light scattering for {xC6H5CN + (1- x)CH3(CH2)6CH3} in the critical region
n0	1.40270		280.51	The measurements of coexistence curves and light scattering for {xC6H5CN + (1- x)CH3(CH2)6CH3} in the critical region
n0	1.40210		281.66	The measurements of coexistence curves and light scattering for {xC6H5CN + (1- x)CH3(CH2)6CH3} in the critical region
n0	1.40170		282.65	The measurements of coexistence curves and light scattering for {xC6H5CN + (1- x)CH3(CH2)6CH3} in the critical region
n0	1.40120		283.88	The measurements of coexistence curves and light scattering for {xC6H5CN + (1- x)CH3(CH2)6CH3} in the critical region
n0	1.40070		284.73	The measurements of coexistence curves and light scattering for {xC6H5CN + (1- x)CH3(CH2)6CH3} in the critical region
n0	1.39650		293.15	Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
n0	1.39760		293.15	DIELECTRIC AND REFRACTIVE INDEX MEASUREMENTS FOR THE SYSTEMS 1-PENTANOL + 2,5,8,11,14-PENTAOXAPENTADECANE, OR FOR 2,5,8,11,14-PENTAOXAPENTADECANE + OCTANE AT (293.15-303.15) K.
n0	1.39910		293.15	DIELECTRIC AND REFRACTIVE INDEX MEASUREMENTS FOR THE SYSTEMS 1-PENTANOL + OCTANE, OR + DIBUTYL ETHER OR FOR DIBUTYL ETHER + OCTANE AT DIFFERENT TEMPERATURES
n0	1.39780		293.15	Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
n0	1.39780		293.15	Isothermal Bubble Pressure Data for the Binary System of C2F6 and n-Octane
n0	1.39750		293.15	Infinite Dilution Activity Coefficients of Hydrocarbons in Triethylene Glycol and Tetraethylene Glycol
n0	1.39730		293.15	Vapor-Liquid Equilibria for the Binary Mixture alpha-Pinene + Octane
n0	1.39730		293.15	Limiting Activity Coefficients by Comparative Tensimetry: 1-Propanol and 1-Butanol in Heptane and in Octane
n0	1.39700		293.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene with Some n-Alkanes at T = (293.15 to 313.15) K
n0	1.39650		293.15	Isobaric Vapor-Liquid Equilibria of Hexane + 1-Decene and Octane + 1-Decene Mixtures
n0	1.39780		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	1.39520		298.15	DIELECTRIC AND REFRACTIVE INDEX MEASUREMENTS FOR THE SYSTEMS 1-PENTANOL + 2,5,8,11,14-PENTAOXAPENTADECANE, OR FOR 2,5,8,11,14-PENTAOXAPENTADECANE + OCTANE AT (293.15-303.15) K.
n0	1.39519		298.15	Extraction of Benzene from Aliphatic Compounds Using Commercial Ionic Liquids as Solvents: Study of the Liquid Liquid Equilibrium at T = 298.15 K
n0	1.39519		298.15	Extraction of toluene from aliphatic compounds using an ionic liquid as solvent: Influence of the alkane on the (liquid + liquid) equilibrium
n0	1.39500		298.15	Excess molar volumes of (octane + benzene, or toluene, or 1,3-xylene, or 1,3,5-trimethylbenzene) at temperatures between (298.15 and 328.15) K
n0	1.39500		298.15	(P,Vm,T) Measurements of (octane + 1-chlorohexane) at temperatures from 298.15 K to 328.15 K and at pressures up to 40 MPa
n0	1.39670		298.15	DIELECTRIC AND REFRACTIVE INDEX MEASUREMENTS FOR THE SYSTEMS 1-PENTANOL + OCTANE, OR + DIBUTYL ETHER OR FOR DIBUTYL ETHER + OCTANE AT DIFFERENT TEMPERATURES
n0	1.39505		298.15	KDB
n0	1.39504		298.15	Separation of aromatic hydrocarbons from alkanes using ammonium ionic liquid C2NTf2 at T = 298.15K
n0	1.53910		298.15	(Vapor + liquid) equilibrium of binary mixtures formed by N,N-dimethyl formamide with some compounds at 95.1 kPa
n0	1.39460		298.15	Vapor liquid equilibria in ternary systems of associating components (water, aniline, cyclohexylamine) and hydrocarbons (octane or toluene)
n0	1.39520		298.15	A Study on Alkane + Ester + Ester Systems. Physicochemical Behavior of Binaries and Ternaries of Octane or Iso-octane with Methyl Esters (Ethanoate, Butanoate, Pentanoate)
n0	1.39800		298.15	P-rho-T Data and Modeling for Propan-1-ol + n-Octane or n-Nonane or n-Decane from 313.15 K to 363.15 K and 1 MPa to 20 MPa
n0	1.39520		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	1.39530		298.15	Isothermal Bubble Pressure Data for the Binary System of C2F6 and n-Octane
n0	1.39550		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	1.39470		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	1.39538		298.15	Liquid liquid equilibria of lactam containing binary systems
n0	1.39470		298.15	Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
n0	1.39510		298.15	Density, Surface Tension, and Refractive Index of Octane + 1-Alkanol Mixtures at T ) 298.15 K.
n0	1.39540		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	1.39460		298.15	Activity Coefficients at Infinite Dilution of Cylcohexylamine + Octane, Toluene, Ethylbenzene, or Aniline and Excess Molar Volumes in Binary Mixtures of Cyclohexylamine + Heptane, Octane, Nonane, Decane, Undecane, Aniline, or Water
n0	1.39460		298.15	Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Water + Cyclohexylamine + Aromatic Hydrocarbon (Toluene or Propylbenzene) or Aliphatic Hydrocarbon (Heptane or Octane)
n0	1.39460		298.15	Ternary Liquid-Liquid(-Liquid) Equilibria of Aniline + Cyclohexylamine + Water, Aniline + Cyclohexylamine + Octane, Aniline + Water + Toluene, and Aniline + Water + Octane
n0	1.39519		298.15	Separation of Benzene from Linear Alkanes (C6-C9) Using 1-Ethyl-3-Methylimidazolium Ethylsulfate at T = 298.15 K
n0	1.39519		298.15	Liquid-Liquid Equilibria of the Ternary Systems of Alkane + Aromatic + 1-Ethylpyridinium Ethylsulfate Ionic Liquid at T = (283.15 and 298.15) K
n0	1.39500		298.15	p, Vm, T) measurements of (octane + benzene) at temperatures from (298.15 to 328.15) K and at pressures up to 40 MPa
n0	1.39260		303.15	Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
n0	1.39230		303.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene with Some n-Alkanes at T = (293.15 to 313.15) K
n0	1.39160		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	1.39290		303.15	DIELECTRIC AND REFRACTIVE INDEX MEASUREMENTS FOR THE SYSTEMS 1-PENTANOL + 2,5,8,11,14-PENTAOXAPENTADECANE, OR FOR 2,5,8,11,14-PENTAOXAPENTADECANE + OCTANE AT (293.15-303.15) K.
n0	1.39450		303.15	DIELECTRIC AND REFRACTIVE INDEX MEASUREMENTS FOR THE SYSTEMS 1-PENTANOL + OCTANE, OR + DIBUTYL ETHER OR FOR DIBUTYL ETHER + OCTANE AT DIFFERENT TEMPERATURES
n0	1.38880		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	1.38550		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	[643.83; 718.25]	kg/m3	[273.15; 363.15]
ρl	718.25	kg/m3	273.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	714.31	kg/m3	278.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	710.76	kg/m3	283.15	Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl	710.61	kg/m3	283.15	Density, viscosity and excess molar volume of binary mixtures of tri-n-octylamine + diluents (n-heptane, n-octane, n-nonane, and n-decane) at various temperatures
ρl	710.34	kg/m3	283.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	706.60	kg/m3	288.15	Study of the binary mixtures of {monoglyme + (hexane, cyclohexane, octane, dodecane)} by ECM-average and PFP models
ρl	706.54	kg/m3	288.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	706.99	kg/m3	288.15	Thermodynamic behavior of thiophene with octane, 1-hexyl-3-methylimidazolium bromide, or 1-octyl-3-methylimidazolium bromide in dilute region at T = (288.15 to 303.15) K
ρl	706.76	kg/m3	288.15	Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl	706.35	kg/m3	288.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	703.00	kg/m3	293.00	KDB
ρl	702.50	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	702.87	kg/m3	293.15	Excess Molar Enthalpies for Binary Mixtures of Ethanol + Acetone, + Octane, + Cyclohexane and 1-Propanol + Acetone, + Octane, + Heptane at 323.15
ρl	702.74	kg/m3	293.15	Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl	702.64	kg/m3	293.15	Liquid liquid equilibria for the ternary system water + octane + 2-butyloxy-ethanol
ρl	702.54	kg/m3	293.15	Volumetric and Transport Properties of Binary Mixtures of n-Octane + Ethanol, + 1-Propanol, + 1-Butanol, and + 1-Pentanol from (293.15 to 323.15) K at Atmospheric Pressure
ρl	702.60	kg/m3	293.15	Density, viscosity and excess molar volume of binary mixtures of tri-n-octylamine + diluents (n-heptane, n-octane, n-nonane, and n-decane) at various temperatures
ρl	703.00	kg/m3	293.15	Thermodynamic behavior of thiophene with octane, 1-hexyl-3-methylimidazolium bromide, or 1-octyl-3-methylimidazolium bromide in dilute region at T = (288.15 to 303.15) K
ρl	702.35	kg/m3	293.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	703.00	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	702.82	kg/m3	293.15	Excess molar volume along with viscosity, refractive index and relative permittivity for binary mixtures of exo-tetrahydrodicyclopentadiene with four octane isomers
ρl	702.53	kg/m3	293.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	702.86	kg/m3	293.15	Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
ρl	702.55	kg/m3	293.15	Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρl	702.93	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	702.50	kg/m3	293.15	Densities and Kinematic Viscosities of a Quinary Regular Liquid System and Its Five Quaternary Subsystems at 293.15A K and 298.15A K
ρl	698.51	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	698.34	kg/m3	298.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	698.73	kg/m3	298.15	Excess molar enthalpies of the ternary mixtures: (tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether + n-octane) at the temperature 298.15 K
ρl	698.50	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	698.58	kg/m3	298.15	Study of the binary mixtures of {monoglyme + (hexane, cyclohexane, octane, dodecane)} by ECM-average and PFP models
ρl	698.92	kg/m3	298.15	Thermodynamic behavior of thiophene with octane, 1-hexyl-3-methylimidazolium bromide, or 1-octyl-3-methylimidazolium bromide in dilute region at T = (288.15 to 303.15) K
ρl	698.64	kg/m3	298.15	Thermodynamics of Mixtures Containing a Strongly Polar Compound. 9. Liquid-Liquid Equilibria for epsilon-Caprolactam + Selected Alkanes
ρl	698.40	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	698.85	kg/m3	298.15	Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
ρl	698.84	kg/m3	298.15	Liquid-liquid equilibria for (2-hydroxy benzaldehyde + n-alkane) mixtures. Intermolecular and proximity effects in systems containing hydroxyl and aldehyde groups
ρl	698.60	kg/m3	298.15	The density, the refractive index and the adjustment of the excess thermodynamic properties by means of the multiple linear regression method for the ternary system ethylbenzene-octane-propylbenzene
ρl	698.50	kg/m3	298.15	Densities and Kinematic Viscosities of a Quinary Regular Liquid System and Its Five Quaternary Subsystems at 293.15A K and 298.15A K
ρl	698.49	kg/m3	298.15	Volumetric and Transport Properties of Binary Mixtures of n-Octane + Ethanol, + 1-Propanol, + 1-Butanol, and + 1-Pentanol from (293.15 to 323.15) K at Atmospheric Pressure
ρl	698.64	kg/m3	298.15	Thermodynamics of mixtures containing amines VI. Liquid liquid equilibria for mixtures of o-toluidine + selected alkanes
ρl	698.53	kg/m3	298.15	Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρl	698.72	kg/m3	298.15	Excess Enthalpies of the Ternary Mixtures: Diisopropyl Ether + 3-Methylpentane + (Octane or Decane) at 298.15 K
ρl	698.76	kg/m3	298.15	Thermodynamics of Mixtures Containing Aromatic Alcohols. 1. Liquid Liquid Equilibria for (Phenylmethanol + Alkane) Systems
ρl	698.61	kg/m3	298.15	Isobaric vapor-liquid equilibrium data of the binary systems of octane with p, o, m-xylene at 20 kPa
ρl	698.86	kg/m3	298.15	Study of the suitability of two ammonium-based ionic liquids for the extraction of benzene from its mixtures with aliphatic hydrocarbons.
ρl	698.86	kg/m3	298.15	Application of the ionic liquid tributylmethylammonium bis(trifluoromethylsulfonyl)imide as solvent for the extraction of benzene from octane and decane at T = 298.15 K and atmospheric pressure
ρl	698.72	kg/m3	298.15	Excess Enthalpies of Binary Mixtures of 1-Hexene with Some n-Alkanes at 298.15 K
ρl	698.81	kg/m3	298.15	Excess molar volume along with viscosity, refractive index and relative permittivity for binary mixtures of exo-tetrahydrodicyclopentadiene with four octane isomers
ρl	698.51	kg/m3	298.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	698.86	kg/m3	298.15	Determination and correlation of (liquid + liquid) equilibria of ternary and quaternary systems with octane, decane, benzene and [BMpyr][DCA] at T = 298.15 K and atmospheric pressure
ρl	698.59	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	698.55	kg/m3	298.15	Density, viscosity and excess molar volume of binary mixtures of tri-n-octylamine + diluents (n-heptane, n-octane, n-nonane, and n-decane) at various temperatures
ρl	698.49	kg/m3	298.15	Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Aliphatic Hydrocarbons (Heptane or Octane) + Phenols + Water
ρl	698.71	kg/m3	298.15	Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl	698.75	kg/m3	298.15	Thermodynamics of mixtures containing amines. XI. Liquid + liquid equilibria and molar excess enthalpies at 298.15 K for N-methylaniline + hydrocarbon systems. Characterization in terms of DISQUAC and ERAS models
ρl	698.60	kg/m3	298.15	Evaluation of ionic liquids as solvent for aromatic extraction: Experimental, correlation and COSMO-RS predictions
ρl	698.64	kg/m3	298.15	Thermodynamics of Mixtures Containing a Strongly Polar Compound. 8. Liquid-Liquid Equilibria for N,N-Dialkylamide + Selected N-Alkanes
ρl	698.55	kg/m3	298.15	Thermodynamics of Mixtures Containing Ethers. Part III. Liquid-Liquid Equilibria for 2,5,8,11-Tetraoxadodecane or 2,5,8,11,14-Pentaoxapentadecane + Selected N-Alkanes
ρl	698.60	kg/m3	298.15	(Liquid + liquid) equilibrium at T = 298.15 K for ternary mixtures of alkane + aromatic compounds + imidazolium-based ionic liquids
ρl	698.71	kg/m3	298.15	Liquid-Liquid Equilibria for 2-Phenylethan-1-ol + Alkane Systems
ρl	698.70	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	698.50	kg/m3	298.15	Viscosities of Dimethyl Carbonate or Diethyl Carbonate with Alkanes at Four Temperatures. New UNIFAC-VISCO Parameters
ρl	698.57	kg/m3	298.20	Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
ρl	698.68	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	694.48	kg/m3	303.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	694.80	kg/m3	303.15	Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
ρl	694.75	kg/m3	303.15	Excess molar volume along with viscosity, refractive index and relative permittivity for binary mixtures of exo-tetrahydrodicyclopentadiene with four octane isomers
ρl	694.50	kg/m3	303.15	Density, viscosity and excess molar volume of binary mixtures of tri-n-octylamine + diluents (n-heptane, n-octane, n-nonane, and n-decane) at various temperatures
ρl	694.88	kg/m3	303.15	Thermodynamic behavior of thiophene with octane, 1-hexyl-3-methylimidazolium bromide, or 1-octyl-3-methylimidazolium bromide in dilute region at T = (288.15 to 303.15) K
ρl	694.49	kg/m3	303.15	Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρl	694.52	kg/m3	303.15	Vapor-Liquid Equilibria in Ternary Systems of Toluene or Octane + Phenols + Water
ρl	694.66	kg/m3	303.15	Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl	694.44	kg/m3	303.15	Volumetric and Transport Properties of Binary Mixtures of n-Octane + Ethanol, + 1-Propanol, + 1-Butanol, and + 1-Pentanol from (293.15 to 323.15) K at Atmospheric Pressure
ρl	694.30	kg/m3	303.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	690.68	kg/m3	308.15	Excess molar volume along with viscosity, refractive index and relative permittivity for binary mixtures of exo-tetrahydrodicyclopentadiene with four octane isomers
ρl	690.58	kg/m3	308.15	Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl	690.73	kg/m3	308.15	Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
ρl	690.44	kg/m3	308.15	Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρl	690.37	kg/m3	308.15	Volumetric and Transport Properties of Binary Mixtures of n-Octane + Ethanol, + 1-Propanol, + 1-Butanol, and + 1-Pentanol from (293.15 to 323.15) K at Atmospheric Pressure
ρl	690.42	kg/m3	308.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	690.48	kg/m3	308.15	Study of the binary mixtures of {monoglyme + (hexane, cyclohexane, octane, dodecane)} by ECM-average and PFP models
ρl	690.50	kg/m3	308.15	The density, the refractive index and the adjustment of the excess thermodynamic properties by means of the multiple linear regression method for the ternary system ethylbenzene-octane-propylbenzene
ρl	690.24	kg/m3	308.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	686.34	kg/m3	313.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	686.36	kg/m3	313.15	Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρl	686.39	kg/m3	313.15	Liquid liquid equilibria for the ternary system water + octane + 2-butyloxy-ethanol
ρl	686.29	kg/m3	313.15	Volumetric and Transport Properties of Binary Mixtures of n-Octane + Ethanol, + 1-Propanol, + 1-Butanol, and + 1-Pentanol from (293.15 to 323.15) K at Atmospheric Pressure
ρl	686.17	kg/m3	313.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	686.59	kg/m3	313.15	Excess molar volume along with viscosity, refractive index and relative permittivity for binary mixtures of exo-tetrahydrodicyclopentadiene with four octane isomers
ρl	686.49	kg/m3	313.15	Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl	686.63	kg/m3	313.15	Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
ρl	686.37	kg/m3	313.20	Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
ρl	682.20	kg/m3	318.15	The density, the refractive index and the adjustment of the excess thermodynamic properties by means of the multiple linear regression method for the ternary system ethylbenzene-octane-propylbenzene
ρl	682.24	kg/m3	318.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	682.37	kg/m3	318.15	Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl	682.19	kg/m3	318.15	Volumetric and Transport Properties of Binary Mixtures of n-Octane + Ethanol, + 1-Propanol, + 1-Butanol, and + 1-Pentanol from (293.15 to 323.15) K at Atmospheric Pressure
ρl	682.26	kg/m3	318.15	Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρl	682.06	kg/m3	318.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	678.08	kg/m3	323.15	Volumetric and Transport Properties of Binary Mixtures of n-Octane + Ethanol, + 1-Propanol, + 1-Butanol, and + 1-Pentanol from (293.15 to 323.15) K at Atmospheric Pressure
ρl	678.13	kg/m3	323.15	Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρl	678.11	kg/m3	323.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	677.94	kg/m3	323.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	673.79	kg/m3	328.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	673.95	kg/m3	328.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	669.61	kg/m3	333.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	669.77	kg/m3	333.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	665.40	kg/m3	338.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	665.55	kg/m3	338.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	661.28	kg/m3	343.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	661.16	kg/m3	343.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	656.88	kg/m3	348.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	652.57	kg/m3	353.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	648.23	kg/m3	358.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	643.83	kg/m3	363.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ΔfusS	[93.19; 95.85]	J/mol×K	[215.60; 216.38]
ΔfusS	93.19	J/mol×K	215.60	NIST
ΔfusS	95.70	J/mol×K	215.80	NIST
ΔfusS	95.85	J/mol×K	216.38	NIST
csound,fluid	[1130.30; 1213.60]	m/s	[288.15; 308.15]
csound,fluid	1213.60	m/s	288.15	Excess Enthalpy, Density, and Speed of Sound for the Ternary Mixture Methyl tert-Butyl Ether (1) + Butan-1-ol (2) + Octane (3)
csound,fluid	1193.00	m/s	293.15	Excess Enthalpy, Density, and Speed of Sound for the Ternary Mixture Methyl tert-Butyl Ether (1) + Butan-1-ol (2) + Octane (3)
csound,fluid	1171.90	m/s	298.15	Excess Enthalpy, Density, and Speed of Sound for the Ternary Mixture Methyl tert-Butyl Ether (1) + Butan-1-ol (2) + Octane (3)
csound,fluid	1151.00	m/s	303.15	Excess Enthalpy, Density, and Speed of Sound for the Ternary Mixture Methyl tert-Butyl Ether (1) + Butan-1-ol (2) + Octane (3)
csound,fluid	1130.30	m/s	308.15	Excess Enthalpy, Density, and Speed of Sound for the Ternary Mixture Methyl tert-Butyl Ether (1) + Butan-1-ol (2) + Octane (3)
γ	[0.02; 0.02]	N/m	[293.20; 318.15]
γ	0.02	N/m	293.20	KDB
γ	0.02	N/m	298.15	Interfacial tensions of binary mixtures of ethanol with octane, decane, dodecane, and tetradecane
γ	0.02	N/m	298.15	Analysis of Surface Tension, Density, and Speed of Sound for the Ternary Mixture Dimethyl Carbonate + p-Xylene + n-Octane
γ	0.02	N/m	308.15	Interfacial tensions of binary mixtures of ethanol with octane, decane, dodecane, and tetradecane
γ	0.02	N/m	308.15	Surface Tension of Dialkyl Carbonates + (Alkanes or 1,4-Dimethylbenzene) and 1,4-Dimethylbenzene + Alkanes Binary Mixtures at T = 308.15 K
γ	0.02	N/m	318.15	Interfacial tensions of binary mixtures of ethanol with octane, decane, dodecane, and tetradecane
λliquid	[0.12; 0.13]	W/m×K	[294.50; 334.80]
λliquid	0.13	W/m×K	294.50	Thermal Conductivities of [bmim][PF6], [hmim][PF6], and [omim][PF6] from 294 to 335 K at Pressures up to 20 MPa.
λliquid	0.12	W/m×K	314.70	Thermal Conductivities of [bmim][PF6], [hmim][PF6], and [omim][PF6] from 294 to 335 K at Pressures up to 20 MPa.
λliquid	0.12	W/m×K	334.80	Thermal Conductivities of [bmim][PF6], [hmim][PF6], and [omim][PF6] from 294 to 335 K at Pressures up to 20 MPa.

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil(P)	[352.83; 397.87]	K	[22.95; 99.01]
Tboil(P)	352.83	K	22.95	A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
Tboil(P)	360.22	K	29.98	A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
Tboil(P)	366.89	K	37.87	A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
Tboil(P)	371.89	K	44.82	A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
Tboil(P)	376.93	K	52.81	A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
Tboil(P)	380.87	K	59.85	A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
Tboil(P)	384.36	K	66.66	A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
Tboil(P)	388.38	K	75.23	A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
Tboil(P)	391.59	K	82.72	A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
Tboil(P)	394.32	K	89.51	A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
Tboil(P)	397.87	K	99.01	A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures

Datasets

1. Molar heat capacity at constant pressure, J/K/mol (1)
2. Viscosity, Pa*s (5)
3. Mass density, kg/m3 (4)
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	100.00	263.30
328.15	100.00	265.70
333.15	100.00	267.98
338.15	100.00	270.38
343.15	100.00	272.66
348.15	100.00	275.18
353.15	100.00	277.58
358.15	100.00	280.09
363.15	100.00	282.60
368.15	100.00	285.11
373.15	100.00	287.86
378.15	100.00	290.37
383.15	100.00	293.45
323.15	10130.00	260.90
328.15	10130.00	263.18
333.15	10130.00	265.58
338.15	10130.00	267.75
343.15	10130.00	270.04
348.15	10130.00	272.32
353.15	10130.00	274.49
358.15	10130.00	277.00
363.15	10130.00	279.17
368.15	10130.00	281.57
373.15	10130.00	283.97
378.15	10130.00	286.49
383.15	10130.00	288.88
388.15	10130.00	290.94
393.15	10130.00	292.88
398.15	10130.00	295.97
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
273.15	100.00	0.0007
273.15	10000.00	0.0008
273.15	20000.00	0.0009
273.15	30000.00	0.0010
293.15	100.00	0.0005
293.15	10000.00	0.0006
293.15	20000.00	0.0007
293.15	30000.00	0.0007
313.15	100.00	0.0004
313.15	10000.00	0.0005
313.15	20000.00	0.0005
313.15	30000.00	0.0006
333.15	100.00	0.0004
333.15	10000.00	0.0004
333.15	20000.00	0.0004
333.15	30000.00	0.0005
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.15	101.33	0.0005
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.24	100.00	0.0005
308.72	5000.00	0.0005
308.72	10000.00	0.0005
323.93	100.00	0.0004
348.64	100.00	0.0003
349.46	5000.00	0.0003
349.46	10000.00	0.0003
394.81	5000.00	0.0002
394.81	10000.00	0.0002
436.86	5000.00	0.0002
436.86	10000.00	0.0002
467.46	5000.00	0.0001
467.46	10000.00	0.0001
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
323.15	100.00	0.0004
323.15	10096.00	0.0004
323.15	20701.00	0.0005
323.15	30654.00	0.0005
323.15	41050.00	0.0006
323.15	54543.00	0.0006
323.15	68036.00	0.0007
348.14	100.00	0.0003
348.14	7551.00	0.0003
348.14	13680.00	0.0004
348.14	20500.00	0.0004
348.14	27466.00	0.0004
348.14	27469.00	0.0004
348.14	34305.00	0.0004
348.14	34314.00	0.0004
348.14	41226.00	0.0004
348.14	41227.00	0.0004
348.14	48070.00	0.0005
348.14	55000.00	0.0005
348.14	55004.00	0.0005
348.14	61992.00	0.0005
348.14	61994.00	0.0005
373.12	6723.00	0.0003
373.12	6724.00	0.0003
373.12	20592.00	0.0003
373.12	20599.00	0.0003
373.12	27397.00	0.0003
373.12	27402.00	0.0003
373.12	34317.00	0.0004
373.12	34324.00	0.0004
373.12	41184.00	0.0004
373.12	41207.00	0.0004
373.12	41221.00	0.0004
373.12	48024.00	0.0004
373.12	48032.00	0.0004
373.12	54853.00	0.0004
373.12	54866.00	0.0004
373.12	61686.00	0.0004
373.12	61704.00	0.0004
423.09	14725.00	0.0002
423.09	27159.00	0.0003
423.09	40831.00	0.0003
423.09	54591.00	0.0003
423.09	68420.00	0.0004
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.15	100.00	0.0005
298.15	20900.00	0.0006
298.15	40600.00	0.0008
298.15	60900.00	0.0009
298.15	80000.00	0.0010
298.15	80100.00	0.0010
298.15	100300.00	0.0012
298.15	120100.00	0.0014
298.15	139700.00	0.0016
298.15	139900.00	0.0015
298.15	159500.00	0.0018
298.15	179600.00	0.0020
298.15	197200.00	0.0022
323.15	100.00	0.0004
323.15	20100.00	0.0005
323.15	40000.00	0.0006
323.15	60600.00	0.0007
323.15	80100.00	0.0008
323.15	101000.00	0.0009
323.15	120300.00	0.0010
323.15	141500.00	0.0011
323.15	141600.00	0.0011
323.15	160300.00	0.0013
323.15	180700.00	0.0014
323.15	201800.00	0.0016
323.15	100.00	0.0004
323.15	80100.00	0.0008
348.15	100.00	0.0003
348.15	20400.00	0.0004
348.15	40800.00	0.0005
348.15	60700.00	0.0005
348.15	80100.00	0.0006
348.15	101000.00	0.0007
348.15	120400.00	0.0008
348.15	140200.00	0.0009
348.15	140300.00	0.0009
348.15	160700.00	0.0010
348.15	180800.00	0.0011
348.15	201900.00	0.0012
348.15	100.00	0.0003
348.15	80100.00	0.0006
373.15	100.00	0.0002
373.15	20600.00	0.0003
373.15	39900.00	0.0004
373.15	60000.00	0.0004
373.15	80200.00	0.0005
373.15	101100.00	0.0006
373.15	120000.00	0.0006
373.15	140900.00	0.0007
373.15	160300.00	0.0008
373.15	180500.00	0.0009
373.15	200900.00	0.0010
398.15	21600.00	0.0003
398.15	42000.00	0.0003
398.15	79400.00	0.0004
398.15	80900.00	0.0004
398.15	120900.00	0.0006
398.15	159500.00	0.0007
398.15	160200.00	0.0007
398.15	192300.00	0.0008
398.15	21600.00	0.0003
423.15	21400.00	0.0002
423.15	41100.00	0.0003
423.15	80400.00	0.0004
423.15	80700.00	0.0004
423.15	121500.00	0.0005
423.15	159700.00	0.0006
423.15	161300.00	0.0006
423.15	192500.00	0.0007
423.15	21400.00	0.0002
448.15	21000.00	0.0002
448.15	41200.00	0.0002
448.15	80500.00	0.0003
448.15	81400.00	0.0003
448.15	121500.00	0.0004
448.15	159400.00	0.0005
448.15	160300.00	0.0005
448.15	193000.00	0.0006
448.15	21000.00	0.0002
473.15	19300.00	0.0002
473.15	20000.00	0.0002
473.15	41100.00	0.0002
473.15	81100.00	0.0003
473.15	81500.00	0.0003
473.15	121100.00	0.0004
473.15	160700.00	0.0004
473.15	161300.00	0.0004
473.15	193400.00	0.0005
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
288.15	100.00	706.6
288.15	5000.00	710.9
288.15	10000.00	714.7
288.15	20000.00	721.7
288.15	30000.00	728.1
288.15	40000.00	734.3
298.15	100.00	698.6
298.15	5000.00	703.4
298.15	10000.00	707.0
298.15	20000.00	714.6
298.15	30000.00	721.4
298.15	40000.00	727.7
308.15	100.00	690.5
308.15	5000.00	695.0
308.15	10000.00	699.4
308.15	20000.00	707.3
308.15	30000.00	714.5
308.15	40000.00	720.8
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	101.00	702.58
303.15	101.00	694.48
313.15	101.00	686.32
323.15	101.00	678.09
288.15	100.00	706.5
288.15	1000.00	707.2
288.15	5000.00	710.3
288.15	10000.00	714.1
288.15	15000.00	717.7
288.15	20000.00	721.2
288.15	25000.00	724.5
288.15	30000.00	727.7
288.15	35000.00	730.8
288.15	40000.00	733.7
288.15	45000.00	736.5
288.15	50000.00	739.2
288.15	55000.00	741.7
288.15	60000.00	744.1
293.15	100.00	702.5
293.15	1000.00	703.2
293.15	5000.00	706.4
293.15	10000.00	710.3
293.15	15000.00	714.0
293.15	20000.00	717.6
293.15	25000.00	721.0
293.15	30000.00	724.3
293.15	35000.00	727.5
293.15	40000.00	730.5
293.15	45000.00	733.3
293.15	50000.00	736.0
293.15	55000.00	738.6
293.15	60000.00	741.0
298.15	100.00	698.5
298.15	1000.00	699.2
298.15	5000.00	702.5
298.15	10000.00	706.5
298.15	15000.00	710.3
298.15	20000.00	714.0
298.15	25000.00	717.6
298.15	30000.00	720.9
298.15	35000.00	724.1
298.15	40000.00	727.2
298.15	45000.00	730.1
298.15	50000.00	732.9
298.15	55000.00	735.5
298.15	60000.00	738.0
303.15	100.00	694.4
303.15	1000.00	695.2
303.15	5000.00	698.6
303.15	10000.00	702.7
303.15	15000.00	706.7
303.15	20000.00	710.5
303.15	25000.00	714.1
303.15	30000.00	717.5
303.15	35000.00	720.9
303.15	40000.00	724.0
303.15	45000.00	727.0
303.15	50000.00	729.8
303.15	55000.00	732.5
303.15	60000.00	735.0
308.15	100.00	690.4
308.15	1000.00	691.2
308.15	5000.00	694.7
308.15	10000.00	698.9
308.15	15000.00	703.0
308.15	20000.00	706.9
308.15	25000.00	710.6
308.15	30000.00	714.2
308.15	35000.00	717.5
308.15	40000.00	720.8
308.15	45000.00	723.8
308.15	50000.00	726.7
308.15	55000.00	729.4
308.15	60000.00	731.9
313.15	100.00	686.3
313.15	1000.00	687.1
313.15	5000.00	690.8
313.15	10000.00	695.1
313.15	15000.00	699.3
313.15	20000.00	703.3
313.15	25000.00	707.2
313.15	30000.00	710.8
313.15	35000.00	714.3
313.15	40000.00	717.6
313.15	45000.00	720.7
313.15	50000.00	723.6
313.15	55000.00	726.3
313.15	60000.00	728.9
318.15	100.00	682.2
318.15	1000.00	683.0
318.15	5000.00	686.8
318.15	10000.00	691.3
318.15	15000.00	695.6
318.15	20000.00	699.7
318.15	25000.00	703.6
318.15	30000.00	707.4
318.15	35000.00	711.0
318.15	40000.00	714.3
318.15	45000.00	717.5
318.15	50000.00	720.5
318.15	55000.00	723.3
318.15	60000.00	725.9
323.15	100.00	678.0
323.15	1000.00	678.9
323.15	5000.00	682.8
323.15	10000.00	687.4
323.15	15000.00	691.9
323.15	20000.00	696.1
323.15	25000.00	700.2
323.15	30000.00	704.0
323.15	35000.00	707.7
323.15	40000.00	711.1
323.15	45000.00	714.4
323.15	50000.00	717.4
323.15	55000.00	720.3
323.15	60000.00	722.9
328.15	100.00	673.8
328.15	1000.00	674.7
328.15	5000.00	678.7
328.15	10000.00	683.5
328.15	15000.00	688.1
328.15	20000.00	692.5
328.15	25000.00	696.7
328.15	30000.00	700.7
328.15	35000.00	704.4
328.15	40000.00	707.9
328.15	45000.00	711.3
328.15	50000.00	714.4
328.15	55000.00	717.3
328.15	60000.00	719.9
333.15	100.00	669.7
333.15	1000.00	670.6
333.15	5000.00	674.8
333.15	10000.00	679.7
333.15	15000.00	684.5
333.15	20000.00	689.0
333.15	25000.00	693.2
333.15	30000.00	697.3
333.15	35000.00	701.1
333.15	40000.00	704.7
333.15	45000.00	708.1
333.15	50000.00	711.3
333.15	55000.00	714.2
333.15	60000.00	716.9
343.15	100.00	661.2
343.15	1000.00	662.2
343.15	5000.00	666.6
343.15	10000.00	671.9
343.15	15000.00	677.0
343.15	20000.00	681.8
343.15	25000.00	686.3
343.15	30000.00	690.6
343.15	35000.00	694.6
343.15	40000.00	698.4
343.15	45000.00	701.9
343.15	50000.00	705.2
343.15	55000.00	708.2
343.15	60000.00	711.0
353.15	100.00	652.6
353.15	1000.00	653.7
353.15	5000.00	658.4
353.15	10000.00	664.1
353.15	15000.00	669.4
353.15	20000.00	674.5
353.15	25000.00	679.3
353.15	30000.00	683.9
353.15	35000.00	688.1
353.15	40000.00	692.1
353.15	45000.00	695.7
353.15	50000.00	699.1
353.15	55000.00	702.3
353.15	60000.00	705.1
363.15	100.00	643.8
363.15	1000.00	645.0
363.15	5000.00	650.1
363.15	10000.00	656.1
363.15	15000.00	661.9
363.15	20000.00	667.3
363.15	25000.00	672.4
363.15	30000.00	677.2
363.15	35000.00	681.6
363.15	40000.00	685.8
363.15	45000.00	689.6
363.15	50000.00	693.1
363.15	55000.00	696.3
363.15	60000.00	699.2
373.15	100.00	634.7
373.15	1000.00	636.3
373.15	5000.00	641.8
373.15	10000.00	648.2
373.15	15000.00	654.4
373.15	20000.00	660.1
373.15	25000.00	665.5
373.15	30000.00	670.6
373.15	35000.00	675.3
373.15	40000.00	679.6
373.15	45000.00	683.6
373.15	50000.00	687.3
373.15	55000.00	690.5
373.15	60000.00	693.5
393.15	100.00	616.3
393.15	1000.00	618.1
393.15	5000.00	624.3
393.15	10000.00	631.8
393.15	15000.00	638.8
393.15	20000.00	645.3
393.15	25000.00	651.5
393.15	30000.00	657.1
393.15	35000.00	662.3
393.15	40000.00	667.1
393.15	45000.00	671.4
393.15	50000.00	675.3
393.15	55000.00	678.8
393.15	60000.00	681.8
413.15	1000.00	599.3
413.15	5000.00	606.6
413.15	10000.00	615.1
413.15	15000.00	623.1
413.15	20000.00	630.6
413.15	25000.00	637.4
413.15	30000.00	643.8
413.15	35000.00	649.6
413.15	40000.00	654.8
413.15	45000.00	659.5
413.15	50000.00	663.6
413.15	55000.00	667.2
413.15	60000.00	670.2
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	298.15	698.71
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.21	1996.00	703.76
293.22	3994.00	705.71
293.22	6001.00	707.57
293.21	8004.00	709.25
293.22	10009.00	710.88
293.21	13010.00	713.21
293.22	16009.00	715.43
293.22	19011.00	717.57
293.22	22012.00	719.76
293.22	25004.00	721.88
293.22	28004.00	724.19
293.21	30002.00	725.54
313.11	2007.00	688.27
313.11	4000.00	690.26
313.10	5999.00	692.07
313.11	7997.00	693.85
313.11	10009.00	695.59
313.11	13005.00	698.26
313.11	16009.00	700.84
313.10	19006.00	703.5
313.10	21998.00	706.05
313.10	25000.00	708.39
313.10	27998.00	710.67
313.10	30001.00	712.15
333.01	2005.00	672.19
333.01	3993.00	674.49
333.01	5998.00	676.69
333.01	8014.00	678.82
333.01	10007.00	680.8
333.01	13004.00	683.6
333.01	16002.00	686.47
333.01	19006.00	689.24
333.00	22003.00	691.91
333.01	25006.00	694.49
333.01	28003.00	696.99
333.01	30012.00	698.61
353.12	2008.00	655.38
353.12	3999.00	657.99
353.12	6000.00	660.5
353.12	8001.00	663.11
353.12	10006.00	665.45
353.13	13003.00	668.83
353.13	16004.00	672.05
353.12	19000.00	674.99
353.12	22003.00	677.96
353.12	25005.00	680.81
353.12	28008.00	683.56
353.12	30004.00	685.34
Reference

Speed of sound, m/s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
296.97	100.00	1173.0
303.61	100.00	1151.7
318.37	100.00	1089.5
332.50	100.00	1029.1
347.68	100.00	970.1
362.53	100.00	912.3
377.50	100.00	855.4
391.61	100.00	806.4
297.28	4000.00	1196.5
303.53	4000.00	1172.7
318.30	4000.00	1121.2
332.26	4000.00	1066.7
347.40	4000.00	1007.2
362.28	4000.00	955.4
377.03	4000.00	909.7
390.80	4000.00	860.1
407.38	4000.00	802.1
412.59	4000.00	786.2
422.73	4000.00	747.2
431.82	4000.00	720.1
442.23	4000.00	682.1
452.55	4000.00	646.4
462.37	4000.00	614.7
472.05	4000.00	579.7
482.98	4000.00	543.0
493.41	4000.00	503.5
502.54	4000.00	477.8
513.00	4000.00	439.1
522.92	4000.00	407.7
532.23	4000.00	373.2
537.40	4000.00	354.7
542.87	4000.00	337.8
546.68	4000.00	325.7
550.42	4000.00	315.2
557.27	4000.00	290.5
561.20	4000.00	276.7
567.01	4000.00	257.3
570.16	4000.00	245.6
297.34	7000.00	1222.0
303.33	7000.00	1199.7
318.35	7000.00	1141.4
332.33	7000.00	1089.1
347.29	7000.00	1031.9
362.17	7000.00	979.6
377.33	7000.00	933.5
391.00	7000.00	892.3
407.46	7000.00	836.9
412.65	7000.00	818.8
422.88	7000.00	784.5
431.88	7000.00	754.2
442.49	7000.00	723.8
452.64	7000.00	689.9
462.45	7000.00	660.1
472.15	7000.00	631.6
483.04	7000.00	599.7
493.48	7000.00	565.4
502.73	7000.00	537.1
513.26	7000.00	506.5
523.46	7000.00	478.6
532.36	7000.00	450.6
537.75	7000.00	436.8
543.83	7000.00	422.0
547.82	7000.00	406.8
552.01	7000.00	398.1
558.19	7000.00	380.2
561.87	7000.00	372.6
566.82	7000.00	356.5
570.20	7000.00	347.6
573.03	7000.00	341.0
575.57	7000.00	332.6
578.92	7000.00	323.1
297.38	10000.00	1242.7
303.38	10000.00	1213.7
318.11	10000.00	1164.8
332.32	10000.00	1108.6
347.37	10000.00	1053.4
362.12	10000.00	1006.2
377.35	10000.00	960.5
391.09	10000.00	917.4
407.45	10000.00	865.2
412.71	10000.00	846.7
422.61	10000.00	818.2
431.92	10000.00	789.8
442.65	10000.00	755.7
452.77	10000.00	728.1
465.54	10000.00	695.8
472.28	10000.00	676.9
483.12	10000.00	646.1
493.62	10000.00	614.7
502.95	10000.00	590.5
513.46	10000.00	563.1
523.60	10000.00	533.3
532.59	10000.00	511.4
538.10	10000.00	497.5
544.52	10000.00	483.1
548.60	10000.00	471.5
552.52	10000.00	465.1
558.64	10000.00	448.0
562.27	10000.00	441.3
566.96	10000.00	430.4
570.48	10000.00	424.0
573.37	10000.00	414.0
576.28	10000.00	408.7
579.36	10000.00	400.8
297.35	12000.00	1250.8
303.42	12000.00	1233.0
318.37	12000.00	1184.5
332.56	12000.00	1128.3
347.46	12000.00	1072.7
363.67	12000.00	1027.8
379.75	12000.00	973.9
394.67	12000.00	920.8
403.71	12000.00	896.1
414.33	12000.00	864.0
422.69	12000.00	844.3
431.77	12000.00	815.2
442.73	12000.00	779.7
452.88	12000.00	750.8
462.61	12000.00	724.2
472.38	12000.00	693.8
483.14	12000.00	672.7
493.73	12000.00	645.0
503.17	12000.00	616.5
513.67	12000.00	591.5
523.17	12000.00	570.6
532.79	12000.00	545.1
538.41	12000.00	530.4
543.27	12000.00	520.1
549.27	12000.00	505.4
552.88	12000.00	500.8
559.37	12000.00	486.2
562.71	12000.00	477.8
567.10	12000.00	471.0
570.75	12000.00	461.0
573.60	12000.00	454.4
576.53	12000.00	451.3
579.57	12000.00	444.1
Reference

Thermal conductivity, W/m/K

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Thermal conductivity, W/m/K - Liquid
255.43	100.00	0.1386
255.34	5200.00	0.1409
255.48	10100.00	0.1427
255.80	20000.00	0.1458
255.12	30000.00	0.1482
274.91	100.00	0.1318
275.13	5000.00	0.1338
275.12	10200.00	0.1358
274.99	20200.00	0.1400
275.01	30200.00	0.1438
295.39	200.00	0.1265
295.22	5100.00	0.1287
295.33	10200.00	0.1309
295.18	20000.00	0.1351
295.13	30000.00	0.1391
315.13	100.00	0.1201
315.18	5000.00	0.1227
315.06	10000.00	0.1252
315.14	20200.00	0.1299
315.00	30000.00	0.1340
334.94	100.00	0.1143
334.97	5100.00	0.1170
335.05	10000.00	0.1194
334.94	20100.00	0.1245
334.94	30000.00	0.1288
355.08	100.00	0.1084
354.92	5000.00	0.1114
355.03	10000.00	0.1142
355.02	20000.00	0.1194
354.99	30000.00	0.1242
375.06	400.00	0.1019
374.87	5100.00	0.1052
375.08	10200.00	0.1082
374.90	20000.00	0.1147
375.26	30000.00	0.1198
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[144.29; 498.35]	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			1.23360e+02
Coefficient B			-7.00100e+02
Coefficient C			6.57824e+00
Coefficient D			-1.91180e-04
Coefficient E			4.54010e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	144.29	J/mol×K	200.00	Calculated Property
Cp,gas	212.06	J/mol×K	344.44	Calculated Property
Cp,gas	281.52	J/mol×K	488.89	Calculated Property
Cp,gas	338.21	J/mol×K	633.33	Calculated Property
Cp,gas	382.37	J/mol×K	777.78	Calculated Property
Cp,gas	416.72	J/mol×K	922.22	Calculated Property
Cp,gas	443.78	J/mol×K	1066.67	Calculated Property
Cp,gas	465.50	J/mol×K	1211.11	Calculated Property
Cp,gas	483.34	J/mol×K	1355.56	Calculated Property
Cp,gas	498.35	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[230.42; 341.90]	J/mol×K	[216.37; 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			1.84080e+02
Coefficient B			3.62580e+02
Coefficient C			-7.80955e-01
Coefficient D			1.59080e-02
Coefficient E			-1.06970e-05
Temperature range, min.			216.37
Temperature range, max.			460.00
Cp,liquid	230.42	J/mol×K	216.37	Calculated Property
Cp,liquid	235.87	J/mol×K	243.44	Calculated Property
Cp,liquid	243.22	J/mol×K	270.51	Calculated Property
Cp,liquid	252.39	J/mol×K	297.58	Calculated Property
Cp,liquid	263.36	J/mol×K	324.65	Calculated Property
Cp,liquid	276.08	J/mol×K	351.72	Calculated Property
Cp,liquid	290.48	J/mol×K	378.79	Calculated Property
Cp,liquid	306.42	J/mol×K	405.86	Calculated Property
Cp,liquid	323.67	J/mol×K	432.93	Calculated Property
Cp,liquid	341.90	J/mol×K	460.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0025958; 0.0000488]	Pa×s	[211.15; 568.70]	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			-6.70627e+01
Coefficient B			2.93770e+03
Coefficient C			8.93946e+00
Coefficient D			-1.46474e-05
Coefficient E			2.00000e+00
Temperature range, min.			211.15
Temperature range, max.			568.70
η	0.0025958	Pa×s	211.15	Calculated Property
η	0.0010233	Pa×s	250.88	Calculated Property
η	0.0005606	Pa×s	290.61	Calculated Property
η	0.0003641	Pa×s	330.33	Calculated Property
η	0.0002573	Pa×s	370.06	Calculated Property
η	0.0001884	Pa×s	409.79	Calculated Property
η	0.0001387	Pa×s	449.52	Calculated Property
η	0.0001007	Pa×s	489.24	Calculated Property
η	0.0000713	Pa×s	528.97	Calculated Property
η	0.0000488	Pa×s	568.70	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[46.98; 0.00]	kJ/mol	[216.38; 568.70]	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			6.50910e+01
Coefficient B			9.06328e-01
Coefficient C			-6.18290e-01
Coefficient D			2.51605e-02
Coefficient E			1.14898e-01
Critical temperature, Tc (K)			5.68700e+02
Temperature range, min.			216.38
Temperature range, max.			568.70
ΔvapH	46.98	kJ/mol	216.38	Calculated Property
ΔvapH	44.33	kJ/mol	255.53	Calculated Property
ΔvapH	41.74	kJ/mol	294.67	Calculated Property
ΔvapH	39.14	kJ/mol	333.82	Calculated Property
ΔvapH	36.43	kJ/mol	372.97	Calculated Property
ΔvapH	33.49	kJ/mol	412.11	Calculated Property
ΔvapH	30.10	kJ/mol	451.26	Calculated Property
ΔvapH	25.86	kJ/mol	490.41	Calculated Property
ΔvapH	19.78	kJ/mol	529.55	Calculated Property
ΔvapH	0.00	kJ/mol	568.70	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[291.19; 425.47]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.44378e+01
Coefficient B			-3.45148e+03
Coefficient C			-4.72760e+01
Temperature range, min.			291.19
Temperature range, max.			425.47
Pvap	1.33	kPa	291.19	Calculated Property
Pvap	3.01	kPa	306.11	Calculated Property
Pvap	6.23	kPa	321.03	Calculated Property
Pvap	11.96	kPa	335.95	Calculated Property
Pvap	21.52	kPa	350.87	Calculated Property
Pvap	36.66	kPa	365.79	Calculated Property
Pvap	59.53	kPa	380.71	Calculated Property
Pvap	92.74	kPa	395.63	Calculated Property
Pvap	139.32	kPa	410.55	Calculated Property
Pvap	202.67	kPa	425.47	Calculated Property
Pvap	[2.08e-03; 2443.01]	kPa	[216.00; 568.74]	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			8.05529e+01
Coefficient B			-7.57820e+03
Coefficient C			-9.65721e+00
Coefficient D			5.66482e-06
Coefficient E			2.00000e+00
Temperature range, min.			216.00
Temperature range, max.			568.74
Pvap	2.08e-03	kPa	216.00	Calculated Property
Pvap	0.10	kPa	255.19	Calculated Property
Pvap	1.49	kPa	294.39	Calculated Property
Pvap	10.57	kPa	333.58	Calculated Property
Pvap	46.10	kPa	372.77	Calculated Property
Pvap	144.56	kPa	411.97	Calculated Property
Pvap	359.85	kPa	451.16	Calculated Property
Pvap	759.61	kPa	490.35	Calculated Property
Pvap	1422.97	kPa	529.55	Calculated Property
Pvap	2443.01	kPa	568.74	Calculated Property
Pvap	[2.46e-03; 2417.19]	kPa	[216.38; 568.83]	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			6.57782e+01
Coefficient B			-6.98194e+03
Coefficient C			-7.37874e+00
Coefficient D			3.38092e-06
Coefficient E			0.00000e+00
Temperature range, min.			216.38
Temperature range, max.			568.83
Pvap	2.46e-03	kPa	216.38	Calculated Property
Pvap	0.11	kPa	255.54	Calculated Property
Pvap	1.53	kPa	294.70	Calculated Property
Pvap	10.66	kPa	333.86	Calculated Property
Pvap	46.40	kPa	373.02	Calculated Property
Pvap	145.90	kPa	412.19	Calculated Property
Pvap	364.04	kPa	451.35	Calculated Property
Pvap	767.43	kPa	490.51	Calculated Property
Pvap	1427.60	kPa	529.67	Calculated Property
Pvap	2417.19	kPa	568.83	Calculated Property
Pvap	[2.21e-03; 1.62]	kPa	[216.59; 297.10]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.65814e+01
Coefficient B			-4.45845e+03
Coefficient C			-2.01430e+01
Reference			Carruth and Kobayashi, 1973
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			216.59
Temperature range, max.			297.10
Pvap	2.21e-03	kPa	216.59	Calculated Property
Pvap	5.94e-03	kPa	225.54	Calculated Property
Pvap	0.01	kPa	234.48	Calculated Property
Pvap	0.03	kPa	243.43	Calculated Property
Pvap	0.07	kPa	252.37	Calculated Property
Pvap	0.15	kPa	261.32	Calculated Property
Pvap	0.29	kPa	270.26	Calculated Property
Pvap	0.53	kPa	279.21	Calculated Property
Pvap	0.95	kPa	288.15	Calculated Property
Pvap	1.62	kPa	297.10	Calculated Property
Pvap	[7.68; 103.90]	kPa	[326.08; 399.72]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39276e+01
Coefficient B			-3.12029e+03
Coefficient C			-6.36330e+01
Reference			Williamham, Taylor, et al., 1945
Temperature range, min.			326.08
Temperature range, max.			399.72
Pvap	7.68	kPa	326.08	Calculated Property
Pvap	11.00	kPa	334.26	Calculated Property
Pvap	15.43	kPa	342.44	Calculated Property
Pvap	21.23	kPa	350.63	Calculated Property
Pvap	28.69	kPa	358.81	Calculated Property
Pvap	38.16	kPa	366.99	Calculated Property
Pvap	49.99	kPa	375.17	Calculated Property
Pvap	64.60	kPa	383.36	Calculated Property
Pvap	82.41	kPa	391.54	Calculated Property
Pvap	103.90	kPa	399.72	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[758.96; 233.06]	kg/m3	[216.38; 568.76]	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			5.06718e+01
Coefficient B			2.38180e-01
Coefficient C			5.68770e+02
Coefficient D			2.51710e-01
Temperature range, min.			216.38
Temperature range, max.			568.76
ρl	758.96	kg/m3	216.38	Calculated Property
ρl	731.28	kg/m3	255.53	Calculated Property
ρl	702.04	kg/m3	294.69	Calculated Property
ρl	670.85	kg/m3	333.84	Calculated Property
ρl	637.17	kg/m3	372.99	Calculated Property
ρl	600.12	kg/m3	412.15	Calculated Property
ρl	558.19	kg/m3	451.30	Calculated Property
ρl	508.32	kg/m3	490.45	Calculated Property
ρl	442.17	kg/m3	529.61	Calculated Property
ρl	233.06	kg/m3	568.76	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.01]	N/m	[216.35; 398.85]	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			4.94966e-02
Coefficient B			-9.51000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			216.35
Temperature range, max.			398.85
γ	0.03	N/m	216.35	Calculated Property
γ	0.03	N/m	236.63	Calculated Property
γ	0.03	N/m	256.91	Calculated Property
γ	0.02	N/m	277.18	Calculated Property
γ	0.02	N/m	297.46	Calculated Property
γ	0.02	N/m	317.74	Calculated Property
γ	0.02	N/m	338.02	Calculated Property
γ	0.02	N/m	358.29	Calculated Property
γ	0.01	N/m	378.57	Calculated Property
γ	0.01	N/m	398.85	Calculated Property
γ	[0.03; 1.43e-05]	N/m	[216.38; 565.18]	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			-1.02820e-02
Coefficient B			1.55570e+01
Coefficient C			-3.03830e+00
Coefficient D			-2.67640e-04
Coefficient E			-4.42650e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 568.7 K.
Temperature range, min.			216.38
Temperature range, max.			565.18
γ	0.03	N/m	216.38	Calculated Property
γ	0.03	N/m	255.14	Calculated Property
γ	0.02	N/m	293.89	Calculated Property
γ	0.02	N/m	332.65	Calculated Property
γ	0.01	N/m	371.40	Calculated Property
γ	0.01	N/m	410.16	Calculated Property
γ	0.01	N/m	448.91	Calculated Property
γ	0.00	N/m	487.67	Calculated Property
γ	0.00	N/m	526.42	Calculated Property
γ	1.43e-05	N/m	565.18	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.11]	W/m×K	[216.38; 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			-8.96850e+03
Coefficient B			8.44080e-01
Coefficient C			-2.75640e+10
Coefficient D			-6.50970e+10
Temperature range, min.			216.38
Temperature range, max.			1000.00
λgas	0.01	W/m×K	216.38	Calculated Property
λgas	0.01	W/m×K	303.45	Calculated Property
λgas	0.02	W/m×K	390.52	Calculated Property
λgas	0.03	W/m×K	477.59	Calculated Property
λgas	0.04	W/m×K	564.66	Calculated Property
λgas	0.05	W/m×K	651.72	Calculated Property
λgas	0.06	W/m×K	738.79	Calculated Property
λgas	0.08	W/m×K	825.86	Calculated Property
λgas	0.09	W/m×K	912.93	Calculated Property
λgas	0.11	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.10]	W/m×K	[216.38; 398.83]	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			-3.31600e-02
Coefficient B			1.78410e+01
Coefficient C			-1.63670e+00
Coefficient D			-4.77370e-05
Coefficient E			-2.65010e-06
Temperature range, min.			216.38
Temperature range, max.			398.83
λliquid	0.15	W/m×K	216.38	Calculated Property
λliquid	0.15	W/m×K	236.65	Calculated Property
λliquid	0.14	W/m×K	256.92	Calculated Property
λliquid	0.13	W/m×K	277.20	Calculated Property
λliquid	0.13	W/m×K	297.47	Calculated Property
λliquid	0.12	W/m×K	317.74	Calculated Property
λliquid	0.12	W/m×K	338.01	Calculated Property
λliquid	0.11	W/m×K	358.29	Calculated Property
λliquid	0.10	W/m×K	378.56	Calculated Property
λliquid	0.10	W/m×K	398.83	Calculated Property

Similar Compounds

Find more compounds similar to Octane.

Mixtures

• Acetonitrile + Octane + Water
• Octane + Acetone + Water
• Octane + Acetone
• Acetonitrile + Octane
• Octane + Heptane
• Octane + Oxygen
• Carbon dioxide + Octane
• Hexane, tetradecafluoro- + Octane
• Octane + Octadecafluorooctane
• Ethanol, 2-propoxy- + Octane
• Toluene + 1,2-Ethanediol + Octane
• Octane + Dibenzothiophene
• Benzene + Octane
• Toluene + Octane
• Benzene, 1,3-dimethyl- + Octane
• Octane + Mesitylene
• Ethanol + Octane
• Octane + 1-Decanol
• 1-Dodecanol + Octane
• Octane + 1-Tetradecanol

Find more mixtures with Octane.

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.
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Measurements of the Liquid Viscosities of Mixtures of n-Butane, n-Hexane, and n-Octane with Squalane to 30MPa
• Thermal Conductivities of [bmim][PF6], [hmim][PF6], and [omim][PF6] from 294 to 335 K at Pressures up to 20 MPa.
• A Digital Variable-Angle Rolling-Ball Viscometer for Measurement of Viscosity, Density, and Bubble-Point Pressure of CO2 and Organic Liquid Mixtures
• Densities and Kinematic Viscosities of One Quinary Regular Liquid System and Its Five Quaternary Sub-Systems at Temperatures (293.15 and 298.15) K
• Densities and Kinematic Viscosities of a Quinary Regular Liquid System and Its Five Quaternary Subsystems at 293.15A K and 298.15A K
• Measurement and correlation of liquid liquid equilibria and partition coefficients of benzothyophene and benzothyophene 1,1-dioxide for acetonitrile + n-octane system
• 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
• An equipment for dynamic measurements of vapour liquid equilibria and results in binary systems containing cyclohexylamine
• 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
• Experimental and predicted excess molar enthalpies for 1,4-dioxane + octane + cyclohexane at 303.15 K
• Excess enthalpies of binary mixtures of 2-ethoxyethanol with four hydrocarbons at 298.15, 308.15, and 318.15K An experimental and theoretical study
• Experimental determination and calculation of thermodynamic properties of CO2 + octane to high temperatures and high pressures
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• Measurement of infinite dilution activity coefficients of n-alkanes in 4-methyl-n-butylpyridinium tetrafluoroborate using gas liquid chromatography
• Effect of bromine substitution on the solubility of gases in hydrocarbons and fluorocarbons
• Thermodynamics of mixtures containing amines VI. Liquid liquid equilibria for mixtures of o-toluidine + selected alkanes
• (Vapor + liquid) equilibrium of binary mixtures formed by N,N-dimethyl formamide with some compounds at 95.1 kPa
• Determination and correlation of liquid liquid equilibria for four binary N,N-dimethylformamide + hydrocarbon systems
• 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
• Vapor liquid equilibria in ternary systems of associating components (water, aniline, cyclohexylamine) and hydrocarbons (octane or toluene)
• Measurement and prediction of pyrene solubility in pure, binary, ternary and quaternary solvent systems
• Liquid liquid equilibria of lactam containing binary systems
• Experimental and predicted phase equilibria and excess properties for systems with ionic liquids
• liquid-liquid equilibrium of substituted perfluoro-n-octane + n-octane systems
• 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)
• 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}
• Vapor liquid equilibrium data for the nitrogen + n-octane system from (344.5 to 543.5)K and at pressures up to 50MPa
• Activity coefficients at infinite dilution of alkanes and alkenes in 1-alkyl-3-methylimidazolium tetrafluoroborate
• 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
• (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}
• Isomer effect in the separation of octane and xylenes using the ionic liquid 1-ethyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}amide
• Measurements of different thermodynamic properties of systems containing ionic liquids and correlation of these properties using modified UNIFAC (Dortmund)
• Liquid-liquid equilibrium data for binary perfluoroalkane (C6 and C8) + n-alkane systems
• Isobaric vapor-liquid equilibria for the n-heptane + ethylene glycol monopropyl ether and n-octane + ethylene glycol monopropyl ether systems
• Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Viscosity of the binary systems 2-methyl-2-propanol with n-alkanes at T = (303.15, 308.15, 313.15, 318.15 and 323.15) K: Prediction and correlation - New UNIFAC-VISCO interaction parameters
• Determination and correlation of liquid-liquid equilibria for nine binary acetonitrile + n-alkane systems
• Perfluoroalkanes and perfluoroalkylalkane surfactants in solution: Partial molar volumes in n-octane and hetero-SAFT-VR modelling
• 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
• Experimental determination and calculation of the critical curves for the binary systems of CO2 containing ketone, alkane, ester and alcohol, respectively
• Liquid-liquid equilibria of mixtures with ethyl lactate and various hydrocarbons
• Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
• Liquid-liquid equilibrium (LLE) data for ternary mixtures of {aliphatic + p-xylene + [EMpy][ESO4]} at T = 313.15 K
• Ternary (liquid liquid) equilibria of nitrate based ionic liquid + alkane + benzene at 298.15 K: Experiments and correlation
• Isobaric vapor-liquid equilibrium data of the binary systems of octane with p, o, m-xylene at 20 kPa
• Measurement and correlation of vapor-liquid equilibria for alkane + alkanol andalkane + alkanediol systems with group contribution COSMOSPACE model
• Using binary mixtures of dicationic ionic liquids for determination ofactivity coefficients at infinite dilution by gas-liquid chromatography
• Enthalpies and Gibbs free energies of solvation in ethylene glycol at298 K: Influence of the solvophobic effect
• Liquid-liquid equilibria for ternary systems acetic acid + n-butylacetate + hydrocarbons at 293.15 K
• A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
• 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
• Study of critical and maximum temperatures of coexistence of liquid and gas phase in hydrocarbons binary mixtures of aromatic hydrocarbons with alkanes and cycloalkanes
• Isobaric vapor-liquid equilibrium for binary systemof 2-ethylthiophene + n-octane at 101.33 kPa
• tert-Butyl chloride as a probe of the solvophobic effects
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• Liquid liquid equilibria for the ternary system water + octane + 2-butyloxy-ethanol
• Solutions of alkyl methanoates and alkanes: Simultaneous modeling of phase equilibria and mixing properties. Estimation of behavior by UNIFAC with recalculation of parameters
• The ionic liquid 1-ethyl-3-methylimidazolium tris(pentafluoroethyl) trifluorophosphate as alternative extractant for BTEX separation
• Speed of sound and thermodynamic properties of ternary liquid mixture octane + dodecane + hexadecane
• 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 extraction of p-xylene from their mixtures with alkanes using 1-butyl-1-methylmorpholinium tricyanomethanide and 1- butyl-3-methylimidazolium tricyanomethanide ionic liquids
• Anomalous nucleation near a fluid phase boundary created by a rapid heat pulse
• 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
• Study of the suitability of two ammonium-based ionic liquids for the extraction of benzene from its mixtures with aliphatic hydrocarbons.
• Application of the ionic liquid tributylmethylammonium bis(trifluoromethylsulfonyl)imide as solvent for the extraction of benzene from octane and decane at T = 298.15 K and atmospheric pressure
• Preferential solvation and mixing behaviour of the essential oil 1,8-cineole with short-chain hydrocarbons
• Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 K
• 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
• Oil desulfurization using deep eutectic solvents as sustainable and economical extractants via liquid-liquid extraction: Experimental and PC-SAFT predictions
• 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
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
• 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
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Phase equilibria of 1-hexyl-3-methylimidazolium acetate with water and oil
• Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
• Dynamic viscosities of 2-butanol with alkanes (C8, C10, and C12) at several temperatures
• Isothermal and isobaric (vapour + liquid) equilibria of (alpha-pinene + n-butanol + n-octane)
• 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
• Liquid + liquid equilibria for ternary mixtures of (solvent + aromatic hydrocarbon + alkane)
• 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
• Coexistence curves of critical nonaqueous microemulsions of (AOT + DMA + nonane) and (AOT + DMA + octane)
• 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
• 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)
• 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
• Excess molar enthalpies of the ternary mixtures: (tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether + n-octane) at the temperature 298.15 K
• (P,Vm,T) Measurements of (octane + 1-chlorohexane) at temperatures from 298.15 K to 328.15 K and at pressures up to 40 MPa
• 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
• (p,rho,T,x) and viscosity measurements of {x1 n-heptane + (1 - x1) n-octane} mixtures at high temperatures and high pressures
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• 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
• Ternary (liquid + liquid) equilibria for mixtures of (methanol + aniline + n-octane or n-dodecane) at T = 298.15 K
• Excess molar volumes of (octane + benzene, or toluene, or 1,3-xylene, or 1,3,5-trimethylbenzene) at temperatures between (298.15 and 328.15) K
• p, Vm, T) measurements of (octane + benzene) at temperatures from (298.15 to 328.15) K and at pressures up to 40 MPa
• Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
• 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
• (Liquid + liquid) equilibria for ternary mixtures of (ethylene glycol + toluene + n-octane)
• 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
• The measurements of coexistence curves and light scattering for {xC6H5CN + (1- x)CH3(CH2)6CH3} in the critical region
• Activity coefficients at infinite dilution of hydrocarbons, alkylbenzenes, and alcohols in the paramagnetic ionic liquid 1-butyl-3-methyl-imidazolium tetrachloridoferrate(III) using gas liquid chromatography
• 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
• 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
• Separation of benzene from alkanes using 1-ethyl-3-methylpyridinium ethylsulfate ionic liquid at several temperatures and atmospheric pressure: Effect of the size of the aliphatic hydrocarbons
• Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
• 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
• Separation of toluene from alkanes using 1-ethyl-3-methylpyridinium ethylsulfate ionic liquid at T = 298.15 K and atmospheric pressure
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate [EMIM][TCB] using gas liquid chromatography
• 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.
• Activity coefficients at infinite dilution of organic solutes in N-alkylpyridinium bis(trifluoromethylsulfonyl)imide ([CnPY][NTf2], n = 2, 4, 5) using gas liquid chromatography
• 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
• Interfacial tensions of binary mixtures of ethanol with octane, decane, dodecane, and tetradecane
• 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
• Thermophysical properties for (diethyl carbonate + p-xylene + octane) ternary system
• Compressed liquid densities for the (n-heptane + n-decane) and (n-octane + n-decane) systems from T = (313 to 363) K
• Interactions of volatile organic compounds with 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 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
• 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
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
• 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
• Thermodynamics of mixtures containing amines. XI. Liquid + liquid equilibria and molar excess enthalpies at 298.15 K for N-methylaniline + hydrocarbon systems. Characterization in terms of DISQUAC and ERAS models
• 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
• Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• Volumetric properties of dialkyl carbonate + n-alkane mixtures at high pressures: Experimental measurement and Nitta-Chao model prediction
• 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
• 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
• 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
• Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Evaluation of ionic liquids as solvent for aromatic extraction: Experimental, correlation and COSMO-RS predictions
• 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
• Density, viscosity and excess molar volume of binary mixtures of tri-n-octylamine + diluents (n-heptane, n-octane, n-nonane, and n-decane) at various temperatures
• Experimental and Nitta-Chao model prediction of high pressure density of p-xylene with dialkyl carbonates or n-alkanes
• 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
• (Liquid + liquid) equilibrium at T = 298.15 K for ternary mixtures of alkane + aromatic compounds + imidazolium-based ionic liquids
• 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
• Excess molar volume along with viscosity, refractive index and relative permittivity for binary mixtures of exo-tetrahydrodicyclopentadiene with four octane isomers
• 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 of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
• 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
• (Liquid + liquid) equilibria for (water + 1-propanol + diisopropyl ether + octane, or methylbenzene, or heptane) systems at T = 298.15 K
• 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
• 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
• Determination and correlation of (liquid + liquid) equilibria of ternary and quaternary systems with octane, decane, benzene and [BMpyr][DCA] at T = 298.15 K and atmospheric pressure
• Thermodynamic behavior of thiophene with octane, 1-hexyl-3-methylimidazolium bromide, or 1-octyl-3-methylimidazolium bromide in dilute region at T = (288.15 to 303.15) K
• Selective recovery of aliphatics from aromatics in the presence of the {[4empy][Tf2N] + [emim][DCA]} ionic liquid mixture
• Solvation of hydrocarbons in aqueous-organic mixtures
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
• Comparative study of the LLE of the quaternary and ternary systems involving benzene, n-octane, n-decane and the ionic liquid [BMpyr] [NTf2]
• Densities and derived thermodynamic properties for the (n-heptane + n-octane), (n-heptane + ethanol) and (n-octane + ethanol) systems at high pressures
• 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
• Liquid-liquid extraction of toluene from alkane with pyridinium based ionic liquid ([BPy][NO3] and [HPy][NO3]) at 298.15 K and atmospheric pressure
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• 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
• High pressure densities and derived thermodynamic properties for the (n-heptane + n-octane + ethanol) ternary system
• Experimental solubility of diosgenin and estriol in various solvents between T = (293.2-328.2) K
• Surface tension and density of mixtures of m-xylene + n-alkane at 293.15 K: Analysis under the extended Langmuir and Shereshefsky models
• 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
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• Thermodynamics of mixtures containing aromatic nitriles
• 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
• Solubility of dibenzothiophene in nine organic solvents: Experimental measurement and thermodynamic modelling
• Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
• Ternary liquid-liquid phase equilibria of {ionic liquid + thiophene + (octane/hexadecane)}
• Liquid-liquid equilibria for (2-hydroxy benzaldehyde + n-alkane) mixtures. Intermolecular and proximity effects in systems containing hydroxyl and aldehyde groups
• Thermodynamic behaviour of the binary systems dimethyl carbonate + n-octane or n-nonane
• Excess volumes, densities, speeds of sound and viscosities for the binary systems of diisopropyl ether with hydrocarbons at 303.15K
• THERMODYNAMICS OF MIXTURES CONTAINING ALKOXYETHANOLS. XXVIII. LIQUID-LIQUID EQUILIBRIA FOR 2-PHENOXYETHANOL + SELECTED ALKANES
• DIELECTRIC AND REFRACTIVE INDEX MEASUREMENTS FOR THE SYSTEMS 1-PENTANOL + OCTANE, OR + DIBUTYL ETHER OR FOR DIBUTYL ETHER + OCTANE AT DIFFERENT TEMPERATURES
• DIELECTRIC AND REFRACTIVE INDEX MEASUREMENTS FOR THE SYSTEMS 1-PENTANOL + 2,5,8,11,14-PENTAOXAPENTADECANE, OR FOR 2,5,8,11,14-PENTAOXAPENTADECANE + OCTANE AT (293.15-303.15) K.
• 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
• Viscosity measurements of hydrocarbon fuel at temperatures from (303.2 to 513.2) K and pressures up to 5.1 MPa using a two-capillary viscometer
• 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
• The density, the refractive index and the adjustment of the excess thermodynamic properties by means of the multiple linear regression method for the ternary system ethylbenzene-octane-propylbenzene
• Standard molar Gibbs free energy and enthalpy of solvation of lowpolar solutes in formamide derivatives at 298 K
• Mutual diffusion behavior of short chain alcohols + n-octane mixtures
• Thermodynamics of hydrogen bonding and van der Waals interactions of organic solutes in solutions of imidazolium based ionic liquids: "structure-property" relationships
• Thermodynamic of dissolution and hydrogen bond of the pyrrole, N-methylpyrrole with proton acceptors
• Thermochemistry of hydrogen bonding of proton acceptors in the media of linear and cyclic amides. Cooperativity effects in multi-particle complexes of amides
• Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
• Phase Equilibria in Systems of Morpholine, Acetonitrile, and n-Alkanes
• Bubble Point Measurements of n-Butane + n-Octane and n-Butane + n-Nonane Binary Mixtures
• Excess Molar Volumes for Three and Four Component Mixtures Simulating the Binary Mixture (Cyclohexane+ Hexadecane)
• A Study on Alkane + Ester + Ester Systems. Physicochemical Behavior of Binaries and Ternaries of Octane or Iso-octane with Methyl Esters (Ethanoate, Butanoate, Pentanoate)
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
• 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
• Solubility of Mercury in Liquid Hydrocarbons and Hydrocarbon Mixtures
• 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
• Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
• Diffusion Coefficients of Carbon Dioxide in Eight Hydrocarbon Liquids at Temperatures between (298.15 and 423.15) K at Pressures up to 69 MPa
• Liquid Liquid Equilibria Data for Ethylbenzene or p-Xylene with Alkane and 1-Butylpyridinium Nitrate Ionic Liquid at 298.15 K
• Liquid Liquid Equilibria of Binary, Ternary, and Quaternary Systems Involving Monoethylene Glycol, Water, Toluene, p-Xylene, Hexane, and Octane
• Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
• 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 Measurement of JP-10 Viscosity at 242.7-753.3 K under Pressures up to 6.00 MPa
• Measurement and Correlation of High Pressure Phase Equilibria for CO2 + Alkanes and CO2 + Crude Oil Systems
• Extraction of Citric Acid and Maleic Acid from Their Aqueous Solutions Using a Phosphorus-Bonded Extractant, Tri-n-octylphosphineoxide, and a Secondary Amine, Dioctylamine
• 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
• Simultaneous Measurement of Dynamic Viscosity and Density of n-Alkanes at High Pressures
• Measurements of the Speed of Sound in Liquid and Supercritical n-Octane and Isooctane
• Measurement and Prediction of Vapor-Liquid Equilibria in Ternary Systems Containing an Organic Component, Cyclohexylamine, and Cyclohexanol
• Liquid-Liquid Equilibria for 2-Phenylethan-1-ol + Alkane Systems
• 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
• Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
• 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
• P-rho-T Data and Modeling for Propan-1-ol + n-Octane or n-Nonane or n-Decane from 313.15 K to 363.15 K and 1 MPa to 20 MPa
• Measurement of Critical Properties for Binary and Ternary Mixtures Containing n-Butanol and n-Alkane
• Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
• Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
• Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
• Liquid Extraction of Toluene from Heptane, Octane, or Nonane Using Mixed Ionic Solvents of 1-Ethyl-3-methylimidazolium Methylsulfate and 1-Hexyl-3-methylimidazolium Hexafluorophosphate
• Isothermal Bubble Pressure Data for the Binary System of C2F6 and n-Octane
• Twenty Years of Experimental Determinations of Thermophysical Properties with High Accuracy: Thermodynamics Laboratory, ESIQIE-IPN, Mexico
• Comparison of Extractability of Oxalic Acid from Dilute Aqueous Solutions Using Dioctylamine and Trioctylphosphine Oxide
• Thermodynamic Studies of Solubility for Naphthalene in 12 Solvents from 279 to 330 K
• Measuring Activity Coefficient at Infinite Dilution of Hydrocarbons in Ionic Liquids and Evaluation of Other Thermodynamic Properties using Gas Chromatography
• Measurement and Prediction of Excess Properties of Binary Mixtures Methyl Decanoate + an Even-Numbered n-Alkane (C6-C16) at 298.15 K
• 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)
• Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
• Measurements of the Thermal Conductivity of n-Octane, Isooctane, 1-Octene, and 1-Octanol in the Temperature Range from 253 to 393 K at Pressures up to 30 MPa
• Thermodynamic Properties of Mixtures Containing Precursors of Vitamin B5
• 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 Molar Enthalpies for Binary Mixtures of Ethanol + Acetone, + Octane, + Cyclohexane and 1-Propanol + Acetone, + Octane, + Heptane at 323.15
• Infinite Dilution Activity Coefficients of Hydrocarbons in Triethylene Glycol and Tetraethylene Glycol
• Vapor-Liquid Equilibria for the Binary Mixture alpha-Pinene + Octane
• 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.
• Excess Enthalpies of the Ternary Mixtures: Diisopropyl Ether + 3-Methylpentane + (Octane or Decane) at 298.15 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
• 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
• Excess Enthalpies of Binary Mixtures of 1-Hexene with Some n-Alkanes at 298.15 K
• Limiting Activity Coefficients by Comparative Tensimetry: 1-Propanol and 1-Butanol in Heptane and in Octane
• A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
• Measurement and Correlation of Mutual Solubilities for High Viscosity Binary Systems: Aniline + Methylcyclohexane, Phenol + Heptane, Phenol + Octane, and Glycerol + 1-Pentanol
• Solubility of Benzophenone in Binary Alkane + Carbon Tetrachloride Solvent Mixtures
• Density, Surface Tension, and Refractive Index of Octane + 1-Alkanol Mixtures at T ) 298.15 K.
• 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
• Dynamic Viscosities of 2-Pentanol with Alkanes (Octane, Decane, and Dodecane) at Three Temperatures T ) (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO Interaction Parameters
• Liquid-Liquid Equilibria of Methyl Acetate + Methanol + Octane or Nonane
• Liquid-Liquid Equilibria for Monoethylene Glycol + Water + Alkane Systems in the Range (273 to 313) K and Atmospheric Pressure
• Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
• Phase Separation in Binary Mixtures Containing Linear Perfluoroalkanes
• Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
• 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
• Thermodynamics of Mixtures Containing Ethers. Part III. Liquid-Liquid Equilibria for 2,5,8,11-Tetraoxadodecane or 2,5,8,11,14-Pentaoxapentadecane + Selected N-Alkanes
• 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
• 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
• Activity Coefficients at Infinite Dilution of Cylcohexylamine + Octane, Toluene, Ethylbenzene, or Aniline and Excess Molar Volumes in Binary Mixtures of Cyclohexylamine + Heptane, Octane, Nonane, Decane, Undecane, Aniline, or Water
• A Vibrating Edge Supported Plate, Fabricated by the Methods of Micro Electro Mechanical System for the Simultaneous Measurement of Density and Viscosity: Results for Methylbenzene and Octane at Temperatures between (323 and 423) K and Pressures in the Range (0.1 to 68) MPa
• 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
• 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
• Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Water + Cyclohexylamine + Aromatic Hydrocarbon (Toluene or Propylbenzene) or Aliphatic Hydrocarbon (Heptane or Octane)
• Ternary Liquid-Liquid(-Liquid) Equilibria of Aniline + Cyclohexylamine + Water, Aniline + Cyclohexylamine + Octane, Aniline + Water + Toluene, and Aniline + Water + Octane
• Vapor-Liquid Equilibrium of Binary Mixtures. 1. Ethanol + 1-Butanol, Ethanol + Octane, 1-Butanol + Octane
• 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
• Experimental Vapor-Liquid Equilibria for the Carbon Dioxide + Octane and Carbon Dioxide + Decane Systems
• Ternary Liquid-Liquid Equilibria for Systems of (Sulfolane + Toluene or Chloronaphthalene + Octane)
• 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
• Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
• Infinite Dilution Activity Coefficients for Trihexyltetradecyl Phosphonium Ionic Liquids: Measurements and COSMO-RS Prediction
• 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
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
• Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
• Separation of Benzene from Linear Alkanes (C6-C9) Using 1-Ethyl-3-Methylimidazolium Ethylsulfate at T = 298.15 K
• 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
• Liquid-Liquid Equilibria of the Ternary Systems of Alkane + Aromatic + 1-Ethylpyridinium Ethylsulfate Ionic Liquid at T = (283.15 and 298.15) K
• Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Aliphatic Hydrocarbons (Heptane or Octane) + Phenols + Water
• Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
• Vapor-Liquid Equilibria in Ternary Systems of Toluene or Octane + Phenols + Water
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
• Dynamic Interfacial Tension between Water and n-Octane plus Sorbitan Monolaurate at (274.2 to 293.2) K
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Butyl-3-methylimidazolium Nitrate Using Gas-Liquid Chromatography
• 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
• 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
• Extraction of Benzene from Aliphatic Compounds Using Commercial Ionic Liquids as Solvents: Study of the Liquid Liquid Equilibrium at T = 298.15 K
• Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
• Interfacial Tension between Methane and Octane at Elevated Pressure at Five Temperatures from (274.2 to 282.2) K
• 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
• Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
• 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 Mixtures Containing Aromatic Alcohols. 1. Liquid Liquid Equilibria for (Phenylmethanol + Alkane) Systems
• Isobaric Vapor Liquid Equilibrium of Binary Systems of Hexane or Octane with 1,2-Dimethylbenzene or 1,3-Dimethylbenzene at 101.3 kPa
• 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
• Densities, Viscosities, and Refractive Indices of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene with Some n-Alkanes at T = (293.15 to 313.15) K
• Liquid Liquid Equilibria for Dipropylene Glycol Hydrocarbon Binary Systems: Experimental Data and Regression
• Multiproperty Correlation of Experimental Data of the Binaries Propyl Ethanoate + Alkanes (Pentane to Decane). New Experimental Information for Vapor Liquid Equilibrium and Mixing Properties
• Surface Tension of Dialkyl Carbonates + (Alkanes or 1,4-Dimethylbenzene) and 1,4-Dimethylbenzene + Alkanes Binary Mixtures at T = 308.15 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
• Measurement and Modeling of Vapor Liquid Equilibria for the Octane + Sulfuric Acid + Water + Ethanol System
• Volumetric and Transport Properties of Binary Mixtures of n-Octane + Ethanol, + 1-Propanol, + 1-Butanol, and + 1-Pentanol from (293.15 to 323.15) K at Atmospheric Pressure
• Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
• Liquid Liquid Equilibria for the Ternary Systems of 4-Methyl-1,3-dioxolan-2-one + 1,4-Dimethylbenzene + Octane, Decane, or Dodecane and the Ternary Systems of Acetonitrile + Morpholine + Octane, Decane, or Dodecane at 313.15 K or 298.15 K
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Determination of the Relative Permittivity of Octane at Temperatures between (303 and 393) K and Pressures below 25 MPa with a Concentric Cylinder Capacitor at a Frequency of 1 kHz
• 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
• Liquid Liquid Extraction of Toluene from n-Alkanes using {[4empy][Tf2N] + [emim][DCA]} Ionic Liquid Mixtures
• Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
• 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
• Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
• Determination of the Critical Properties of C6 C10 n-Alkanes and Their Binary Systems Using a Flow Apparatus
• Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
• 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
• Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) 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
• Measurement of Activity Coefficient at Infinite Dilution of Hydrocarbons in Sulfolane Using Gas-Liquid Chromatography
• Liquid - Liquid Equilibria for the Binary Systems of Sulfolane with Alkanes
• Densities and Viscosities of Ternary Mixtures of Heptane, Octane, Nonane, and Hexyl Benzene from 293.15 K to 313.15 K
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• 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
• Isobaric Vapor-Liquid Equilibria of Hexane + 1-Decene and Octane + 1-Decene Mixtures
• Phase Equilibria of (1-Ethyl-3-methylimidazolium Ethylsulfate + Hydrocarbon, + Ketone, and + Ether) Binary Systems
• 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
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Hexyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• 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
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Liquid-Liquid Equilibria of Ternary Systems Sulfide + Octane + Solvents at Different Temperatures
• Densities and Viscosities of Binary Mixtures of JP-10 with n-Octane or n-Decane at Several Temperatures
• Viscosity and Density of Five Hydrocarbon Liquids at Pressures up to 200 MPa and Temperatures up to 473 K
• Excess Enthalpy, Density, and Speed of Sound for the Ternary Mixture Methyl tert-Butyl Ether (1) + Butan-1-ol (2) + Octane (3)
• Analysis of Surface Tension, Density, and Speed of Sound for the Ternary Mixture Dimethyl Carbonate + p-Xylene + n-Octane
• 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
• Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
• Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
• Viscosity and Density of Binary Mixtures of Ethyl Alcohol with n-Alkanes (C6, C8, and C10)
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Phase Equilibria of (1-Hexyl-3-methylimidazolium Thiocyanate + Water, Alcohol, or Hydrocarbon) Binary Systems
• 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
• Thermodynamics of Mixtures Containing a Strongly Polar Compound. 9. Liquid-Liquid Equilibria for epsilon-Caprolactam + Selected Alkanes
• 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
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
• Miscibility of Trihexyl(tetradecyl)phosphonium Chloride with Alkanes
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure
• Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD

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