Chemical Properties of Heptane (CAS 142-82-5)

InChI

InChI=1S/C7H16/c1-3-5-7-6-4-2/h3-7H2,1-2H3

InChI Key

IMNFDUFMRHMDMM-UHFFFAOYSA-N

Formula

C7H16

SMILES

CCCCCCC

Molecular Weight¹

100.20

CAS

142-82-5

Other Names

• Dipropylmethane
• Eptani
• Gettysolve-C
• Heptan
• Heptanen
• Heptyl hydride
• NSC 62784
• Skellysolve C
• n-C7H16
• n-heptane

• ω : Acentric Factor.
• T_ig : Autoignition Temperature (K).
• AP : Aniline Point (K).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• ε_r : Dielectric Constant (Relative permittivity).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_c,grossH : Heat of Combustion, Gross form (kJ/mol).
• Δ_c,netH : Heat of Combustion, Net Form (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_subH : Enthalpy of sublimation at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• ν : Kinematic viscosity (m²/s).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_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_m : Molar Volume (m³/mol).
• 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	[0.3457; 0.3506]
ω	0.3457		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.3506		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.3500		ChemSep v8.3 pure component data Compiled value
ω	0.3490		KDB
Tig	[477.15; 495.93]	K
Tig	495.93	K	KDB
Tig	477.15	K	NCMS SOLV-DB
AP	342.850	K	KDB
ΔcH°liquid	[-4830.00; -4810.30]	kJ/mol
ΔcH°liquid	Outlier -4830.00 ± 120.00	kJ/mol	NIST
ΔcH°liquid	-4818.70	kJ/mol	NIST
ΔcH°liquid	-4816.91 ± 0.63	kJ/mol	NIST
ΔcH°liquid	-4817.16 ± 0.88	kJ/mol	NIST
ΔcH°liquid	-4815.00 ± 1.00	kJ/mol	NIST
ΔcH°liquid	-4810.30	kJ/mol	NIST
ΔcH°liquid	-4817.00 ± 1.50	kJ/mol	NIST
Cp,liquid	223.91	J/mol×K	THERMODYNAMICS OF MIXTURES CONTAINING AMINES. XIV. CpEm OF BENZYLAMINE WITH HEPTANE AT 293.15 K OR WITH METHANOL, 1-PROPANOL OR 1-PENTANOL AT (293.15-308.15) K
μ	[0.00; 0.00]	debye
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
μ	0.00	debye	KDB
εr	1.93		NCMS SOLV-DB
LFL	1.00	% in Air	KDB
UFL	7.00	% in Air	KDB
Tflash,cc	269.15	K	NCMS SOLV-DB
Tflash,oc	269.26	K	KDB
ΔfG°	[8.00; 8.16]	kJ/mol
ΔfG°	8.16	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	8.00	kJ/mol	KDB
Rg	4.2670		KDB
Δc,grossH	4816.91	kJ/mol	KDB
Δc,netH	4464.788	kJ/mol	KDB
ΔfH°gas	[-189.30; -187.34]	kJ/mol
ΔfH°gas	-187.34 ± 0.74	kJ/mol	Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas	-187.65	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-187.90	kJ/mol	KDB
ΔfH°gas	-187.80 ± 0.79	kJ/mol	NIST
ΔfH°gas	-189.30	kJ/mol	NIST
ΔfH°liquid	[-225.90; -224.40]	kJ/mol
ΔfH°liquid	-224.40 ± 0.79	kJ/mol	NIST
ΔfH°liquid	-225.90 ± 1.30	kJ/mol	NIST
ΔfusH°	14.06	kJ/mol	Measurement of Heat Capacity by Adiabatic Calorimetry and Calculation of Thermodynamic Functions of Standard Substances: Copper, Benzoic Acid, and Heptane (For Calibration of an Adiabatic Calorimeter)
ΔvapH°	[32.00; 36.90]	kJ/mol
ΔvapH°	36.57	kJ/mol	NCMS SOLV-DB
ΔvapH°	36.66	kJ/mol	NIST
ΔvapH°	36.60	kJ/mol	NIST
ΔvapH°	36.90	kJ/mol	NIST
ΔvapH°	36.60 ± 0.10	kJ/mol	NIST
ΔvapH°	36.55	kJ/mol	NIST
ΔvapH°	36.54	kJ/mol	NIST
ΔvapH°	Outlier 32.00 ± 0.20	kJ/mol	NIST
IE	[9.83; 10.16]	eV
IE	9.93 ± 0.10	eV	NIST
IE	10.15	eV	NIST
IE	9.93 ± 0.10	eV	NIST
IE	9.83 ± 0.15	eV	NIST
IE	9.91	eV	NIST
IE	9.90 ± 0.05	eV	NIST
IE	10.16	eV	NIST
IE	10.08	eV	NIST
log10WS	[-4.53; -4.53]
log10WS	-4.53		Aq. Solubility Prediction
log10WS	-4.53		Estimated Solubility
logPoct/wat	4.397		NCMS SOLV-DB
McVol	109.490	ml/mol	McGowan Calculated Property
NFPA Fire	3		NCMS SOLV-DB
NFPA Health	1		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	[2723.80; 2801.64]	kPa
Pc	2740.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Pc	2733.75	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	2735.84	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	2740.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	2740.00	kPa	KDB
Pc	2740.00 ± 30.00	kPa	NIST
Pc	2730.00 ± 40.00	kPa	NIST
Pc	2730.00 ± 30.00	kPa	NIST
Pc	2730.00 ± 10.00	kPa	NIST
Pc	2734.00 ± 20.00	kPa	NIST
Pc	2736.00	kPa	NIST
Pc	2734.00 ± 5.00	kPa	NIST
Pc	2775.00 ± 5.00	kPa	NIST
Pc	2760.00 ± 50.66	kPa	NIST
Pc	2736.52 ± 17.23	kPa	NIST
Pc	2736.00 ± 40.53	kPa	NIST
Pc	2770.00 ± 50.66	kPa	NIST
Pc	2750.00 ± 34.50	kPa	NIST
Pc	2730.31 ± 20.68	kPa	NIST
Pc	2730.00 ± 103.42	kPa	NIST
Pc	2735.77 ± 4.05	kPa	NIST
Pc	2735.77 ± 5.06	kPa	NIST
Pc	Outlier 2801.64 ± 20.26	kPa	NIST
Pc	2723.80 ± 26.70	kPa	NIST
Ptriple	1.83e-04	kPa	ChemSep v8.3 pure component data Compiled value
ρc	[232.47; 241.49]	kg/m3
ρc	234.47 ± 3.01	kg/m3	NIST
ρc	232.47 ± 10.02	kg/m3	NIST
ρc	233.47 ± 6.01	kg/m3	NIST
ρc	232.47	kg/m3	NIST
ρc	234.47 ± 5.01	kg/m3	NIST
ρc	232.47 ± 5.01	kg/m3	NIST
ρc	241.49 ± 15.03	kg/m3	NIST
ρc	234.67 ± 1.60	kg/m3	NIST
ρc	234.71 ± 1.60	kg/m3	NIST
ρc	241.49 ± 2.00	kg/m3	NIST
ρc	241.49 ± 5.01	kg/m3	NIST
ρc	234.07 ± 3.01	kg/m3	NIST
S°liquid	[326.40; 330.10]	J/mol×K
S°liquid	328.57	J/mol×K	NIST
S°liquid	327.98	J/mol×K	NIST
S°liquid	328.86	J/mol×K	NIST
S°liquid	330.10	J/mol×K	NIST
S°liquid	326.40	J/mol×K	NIST
Tboil	[370.30; 372.00]	K
Tboil	371.47	K	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Tboil	371.35	K	Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
Tboil	371.64	K	Isobaric vapor-liquid equilibrium for four binary systems of thiophene
Tboil	371.64	K	Isobaric vapor-liquid equilibrium for four binary systems of 3-methylthiophene
Tboil	371.40	K	Isobaric vapor-liquid equilibrium for binary systemsof toluene + o-xylene, benzene + o-xylene, nonane + benzene and nonane + heptane at 101.3 kPa
Tboil	371.64	K	Isobaric vapor-liquid equilibrium for systems containing sulfur compounds
Tboil	371.56	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	371.50	K	Excess molar volumes of the ternary system {methylcyclohexane (1) + cyclohexane (2) + n-alkanes (3)} at T = 298.15 K
Tboil	371.53	K	Isobaric vapor-liquid equilibrium of three binary systems containing dimethyl succinate, dimethyl glutarate and dimethyl adipate at 2, 5.2 and 8.3 kPa
Tboil	371.35	K	Excess volumes, densities, speeds of sound and viscosities for the binary systems of diisopropyl ether with hydrocarbons at 303.15K
Tboil	371.28	K	Vapor Liquid Equilibria Measurements for Di-n-Propyl Ether and Butyl Ethyl Ether with n-Heptane
Tboil	Outlier 370.97	K	A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol
Tboil	371.35	K	Isobaric Vapor-Liquid Equilibria and Excess Properties for the Binary Systems of Methyl Esters + Heptane
Tboil	371.18	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	371.56	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	371.50	K	Vapor-Liquid Equilibrium in the Binary Systems 2-Butanol + tert-Amyl Methyl Ether, 2-Butanol + Heptane, and Heptane + tert-Amyl Methyl Ether
Tboil	371.65	K	Isobaric Vapor-Liquid Equilibria of Heptane + 1-Butanol and Heptane + 1-Pentanol Systems at (53.3 and 91.3) kPa
Tboil	371.57	K	ChemSep v8.3 pure component data Compiled value
Tboil	371.60	K	KDB
Tboil	371.57	K	NCMS SOLV-DB
Tboil	371.50 ± 0.20	K	NIST
Tboil	371.46 ± 0.10	K	NIST
Tboil	371.55 ± 0.10	K	NIST
Tboil	371.80 ± 0.30	K	NIST
Tboil	371.35 ± 0.40	K	NIST
Tboil	371.60	K	NIST
Tboil	371.46 ± 0.10	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.60	K	NIST
Tboil	371.54 ± 0.01	K	NIST
Tboil	371.53 ± 0.30	K	NIST
Tboil	371.60 ± 0.20	K	NIST
Tboil	371.50 ± 0.50	K	NIST
Tboil	371.35 ± 0.30	K	NIST
Tboil	371.64 ± 0.08	K	NIST
Tboil	371.53 ± 0.10	K	NIST
Tboil	Outlier 372.00 ± 2.00	K	NIST
Tboil	371.60 ± 0.30	K	NIST
Tboil	371.60 ± 0.40	K	NIST
Tboil	371.55 ± 0.20	K	NIST
Tboil	371.50 ± 0.50	K	NIST
Tboil	371.55 ± 0.20	K	NIST
Tboil	371.57 ± 0.20	K	NIST
Tboil	371.55 ± 0.10	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.25 ± 0.30	K	NIST
Tboil	371.55 ± 0.20	K	NIST
Tboil	Outlier 371.00 ± 0.30	K	NIST
Tboil	371.45 ± 0.40	K	NIST
Tboil	371.60 ± 0.40	K	NIST
Tboil	371.59 ± 0.10	K	NIST
Tboil	371.55 ± 0.20	K	NIST
Tboil	371.70 ± 0.30	K	NIST
Tboil	371.77 ± 0.15	K	NIST
Tboil	371.46 ± 0.05	K	NIST
Tboil	Outlier 370.65 ± 1.50	K	NIST
Tboil	Outlier 371.00 ± 3.00	K	NIST
Tboil	371.60 ± 0.20	K	NIST
Tboil	371.68 ± 0.20	K	NIST
Tboil	371.65 ± 0.70	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.58 ± 0.20	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.55 ± 0.40	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.65 ± 0.30	K	NIST
Tboil	371.45 ± 0.15	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.60 ± 0.20	K	NIST
Tboil	371.45 ± 0.30	K	NIST
Tboil	371.58 ± 0.08	K	NIST
Tboil	371.60 ± 0.20	K	NIST
Tboil	371.57 ± 0.02	K	NIST
Tboil	371.58 ± 0.20	K	NIST
Tboil	371.55 ± 0.10	K	NIST
Tboil	371.50 ± 0.15	K	NIST
Tboil	371.60 ± 0.30	K	NIST
Tboil	Outlier 370.30 ± 1.00	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.57 ± 0.30	K	NIST
Tboil	371.55 ± 0.20	K	NIST
Tboil	371.57 ± 0.30	K	NIST
Tboil	371.57 ± 0.03	K	NIST
Tboil	371.68 ± 0.15	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.45 ± 0.50	K	NIST
Tboil	371.40 ± 0.50	K	NIST
Tboil	371.65 ± 0.50	K	NIST
Tboil	371.59 ± 0.30	K	NIST
Tboil	371.54 ± 0.20	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.60 ± 0.30	K	NIST
Tboil	371.56 ± 0.15	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.60 ± 0.20	K	NIST
Tboil	371.10 ± 0.70	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.60 ± 0.40	K	NIST
Tboil	371.60 ± 0.30	K	NIST
Tboil	371.55 ± 0.70	K	NIST
Tboil	371.55 ± 0.60	K	NIST
Tboil	371.40 ± 1.00	K	NIST
Tboil	371.54 ± 0.10	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.57 ± 0.01	K	NIST
Tboil	371.57 ± 0.30	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.57 ± 0.30	K	NIST
Tboil	371.70 ± 0.20	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.20 ± 0.70	K	NIST
Tboil	371.54 ± 0.15	K	NIST
Tboil	Outlier 372.00 ± 1.50	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.58 ± 0.05	K	NIST
Tboil	371.15 ± 1.00	K	NIST
Tboil	371.55 ± 0.20	K	NIST
Tboil	371.70 ± 0.20	K	NIST
Tboil	371.15 ± 2.00	K	NIST
Tboil	371.55 ± 0.25	K	NIST
Tboil	371.75 ± 0.40	K	NIST
Tboil	371.55 ± 1.00	K	NIST
Tboil	371.60 ± 0.30	K	NIST
Tboil	371.35 ± 1.00	K	NIST
Tboil	371.58 ± 0.03	K	NIST
Tboil	371.40 ± 0.50	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.65 ± 0.30	K	NIST
Tboil	371.57 ± 0.30	K	NIST
Tboil	371.65 ± 0.50	K	NIST
Tboil	371.65 ± 0.30	K	NIST
Tboil	Outlier 371.00 ± 1.00	K	NIST
Tboil	371.15 ± 1.00	K	NIST
Tboil	371.60 ± 0.20	K	NIST
Tboil	371.57 ± 0.10	K	NIST
Tboil	371.56 ± 0.20	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.55 ± 1.00	K	NIST
Tboil	371.57 ± 0.03	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.15 ± 1.00	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.40 ± 0.40	K	NIST
Tboil	371.73 ± 0.20	K	NIST
Tboil	371.55 ± 0.20	K	NIST
Tboil	371.56 ± 0.15	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.57 ± 0.02	K	NIST
Tboil	371.65 ± 1.50	K	NIST
Tboil	371.54 ± 0.15	K	NIST
Tboil	371.40 ± 1.00	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.56 ± 0.02	K	NIST
Tboil	371.65 ± 1.50	K	NIST
Tboil	371.67 ± 0.03	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.67 ± 0.05	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.30 ± 0.50	K	NIST
Tboil	371.45 ± 0.50	K	NIST
Tboil	371.15 ± 0.60	K	NIST
Tboil	Outlier 370.65 ± 0.60	K	NIST
Tboil	Outlier 370.40 ± 0.50	K	NIST
Tboil	371.50 ± 0.20	K	NIST
Tboil	371.10 ± 0.60	K	NIST
Tboil	371.51 ± 0.05	K	NIST
Tboil	371.51 ± 0.04	K	NIST
Tboil	371.65 ± 1.50	K	NIST
Tboil	371.70 ± 0.50	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.40 ± 1.00	K	NIST
Tboil	Outlier 371.00 ± 1.00	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.50 ± 0.20	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.15 ± 1.00	K	NIST
Tboil	371.60 ± 0.30	K	NIST
Tboil	371.30 ± 1.00	K	NIST
Tboil	371.65 ± 1.00	K	NIST
Tboil	371.45 ± 0.15	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.15 ± 0.50	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.55 ± 0.20	K	NIST
Tboil	371.55 ± 0.20	K	NIST
Tboil	371.53 ± 0.10	K	NIST
Tboil	371.50 ± 0.15	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.53 ± 0.10	K	NIST
Tboil	371.60 ± 0.20	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.55 ± 0.20	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.45 ± 0.30	K	NIST
Tboil	371.65 ± 0.60	K	NIST
Tboil	371.45 ± 0.30	K	NIST
Tboil	371.15 ± 0.30	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.60 ± 0.50	K	NIST
Tboil	371.60 ± 0.20	K	NIST
Tboil	371.55 ± 0.30	K	NIST
Tboil	371.60 ± 0.50	K	NIST
Tboil	371.60 ± 0.20	K	NIST
Tboil	371.71 ± 0.20	K	NIST
Tboil	371.35 ± 0.50	K	NIST
Tboil	371.90 ± 1.50	K	NIST
Tboil	371.46 ± 0.25	K	NIST
Tboil	371.65 ± 0.50	K	NIST
Tboil	371.70 ± 5.00	K	NIST
Tboil	371.55 ± 0.20	K	NIST
Tboil	371.55 ± 0.50	K	NIST
Tboil	371.49 ± 0.30	K	NIST
Tboil	371.30 ± 0.80	K	NIST
Tboil	371.30 ± 1.00	K	NIST
Tboil	371.65 ± 1.50	K	NIST
Tboil	371.45 ± 1.50	K	NIST
Tboil	371.15 ± 1.00	K	NIST
Tboil	371.15 ± 2.00	K	NIST
Tboil	371.90 ± 1.50	K	NIST
Tboil	371.60 ± 0.30	K	NIST
Tboil	371.50 ± 0.40	K	NIST
Tboil	371.59 ± 0.50	K	NIST
Tboil	371.55 ± 1.00	K	NIST
Tboil	371.55 ± 1.00	K	NIST
Tboil	371.58 ± 1.00	K	NIST
Tboil	371.57 ± 1.00	K	NIST
Tboil	371.15 ± 2.00	K	NIST
Tboil	371.65 ± 2.00	K	NIST
Tboil	371.65 ± 2.00	K	NIST
Tboil	371.15 ± 2.00	K	NIST
Tc	[536.70; 542.70]	K
Tc	540.10	K	Measurement of critical properties for binary and ternary mixtures containing potential gasoline additive diethyl carbonate (DEC)
Tc	540.00	K	Measurement of critical temperatures and critical pressures for binary mixtures of methyl tert-butyl ether (MTBE) + alcohol and MTBE + alkane
Tc	540.00	K	Measurement and correlation of critical properties for binary mixtures and ternary mixtures containing gasoline additives
Tc	540.14	K	Experimental determination of critical data of multi-component mixtures containing potential gasoline additives 2-butanol by a flow-type apparatus
Tc	540.60	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	540.10	K	Measurement of Critical Properties for Binary and Ternary Mixtures Containing n-Butanol and n-Alkane
Tc	540.14	K	Determination of the Critical Properties of C6 C10 n-Alkanes and Their Binary Systems Using a Flow Apparatus
Tc	540.20	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Tc	540.30	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	540.26	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	540.20	K	ChemSep v8.3 pure component data Compiled value
Tc	540.20	K	KDB
Tc	540.20 ± 0.30	K	NIST
Tc	Outlier 536.80 ± 2.00	K	NIST
Tc	Outlier 536.70 ± 4.00	K	NIST
Tc	540.00 ± 1.00	K	NIST
Tc	540.40 ± 0.40	K	NIST
Tc	539.80 ± 0.30	K	NIST
Tc	540.30	K	NIST
Tc	540.10	K	NIST
Tc	540.17 ± 0.10	K	NIST
Tc	540.20	K	NIST
Tc	540.68 ± 0.08	K	NIST
Tc	540.20 ± 0.30	K	NIST
Tc	539.86 ± 0.07	K	NIST
Tc	539.90 ± 0.30	K	NIST
Tc	Outlier 542.70 ± 0.70	K	NIST
Tc	541.00 ± 0.50	K	NIST
Tc	540.00 ± 0.30	K	NIST
Tc	540.00 ± 0.40	K	NIST
Tc	540.60 ± 0.40	K	NIST
Tc	540.28 ± 0.20	K	NIST
Tc	540.30 ± 0.33	K	NIST
Tc	540.53 ± 0.27	K	NIST
Tc	540.50 ± 0.55	K	NIST
Tc	540.16 ± 0.05	K	NIST
Tc	540.16 ± 0.06	K	NIST
Tc	Outlier 542.65 ± 0.50	K	NIST
Tc	540.00 ± 1.00	K	NIST
Tfus	[176.05; 183.15]	K
Tfus	182.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	182.57	K	ChemSep v8.3 pure component data Compiled value
Tfus	182.50	K	KDB
Tfus	182.31	K	Aq. Solubility Prediction
Tfus	182.57	K	NCMS SOLV-DB
Tfus	182.55 ± 0.20	K	NIST
Tfus	182.55 ± 0.20	K	NIST
Tfus	182.55 ± 0.20	K	NIST
Tfus	182.55 ± 0.20	K	NIST
Tfus	182.57 ± 0.10	K	NIST
Tfus	182.58 ± 0.05	K	NIST
Tfus	182.55 ± 0.02	K	NIST
Tfus	182.56 ± 0.05	K	NIST
Tfus	183.15 ± 2.00	K	NIST
Tfus	182.12 ± 0.20	K	NIST
Tfus	182.54 ± 0.03	K	NIST
Tfus	182.54 ± 0.02	K	NIST
Tfus	182.65 ± 0.40	K	NIST
Tfus	182.54 ± 0.05	K	NIST
Tfus	182.54 ± 0.03	K	NIST
Tfus	182.50 ± 0.06	K	NIST
Tfus	182.54 ± 0.03	K	NIST
Tfus	182.49 ± 0.08	K	NIST
Tfus	182.45 ± 0.20	K	NIST
Tfus	182.53 ± 0.02	K	NIST
Tfus	182.54 ± 0.01	K	NIST
Tfus	182.45 ± 0.15	K	NIST
Tfus	182.45 ± 0.30	K	NIST
Tfus	182.50 ± 0.15	K	NIST
Tfus	182.55 ± 0.20	K	NIST
Tfus	182.54 ± 0.01	K	NIST
Tfus	182.54 ± 0.03	K	NIST
Tfus	182.54 ± 0.02	K	NIST
Tfus	182.49 ± 0.15	K	NIST
Tfus	182.51 ± 0.20	K	NIST
Tfus	182.55 ± 0.20	K	NIST
Tfus	183.15 ± 1.50	K	NIST
Tfus	182.47 ± 0.20	K	NIST
Tfus	182.55 ± 0.07	K	NIST
Tfus	182.35 ± 0.30	K	NIST
Tfus	182.57 ± 0.08	K	NIST
Tfus	182.35 ± 0.40	K	NIST
Tfus	183.15 ± 2.00	K	NIST
Tfus	183.15 ± 1.50	K	NIST
Tfus	182.34 ± 0.30	K	NIST
Tfus	182.53 ± 0.15	K	NIST
Tfus	182.49 ± 0.20	K	NIST
Tfus	182.53 ± 0.10	K	NIST
Tfus	181.95 ± 1.00	K	NIST
Tfus	182.45 ± 0.50	K	NIST
Tfus	182.55 ± 0.40	K	NIST
Tfus	182.50 ± 0.08	K	NIST
Tfus	182.65 ± 0.50	K	NIST
Tfus	182.65 ± 0.50	K	NIST
Tfus	182.65 ± 0.40	K	NIST
Tfus	183.15 ± 0.30	K	NIST
Tfus	Outlier 176.05 ± 1.00	K	NIST
Ttriple	[182.20; 187.57]	K
Ttriple	182.57	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	182.57	K	ChemSep v8.3 pure component data Compiled value
Ttriple	182.55	K	KDB
Ttriple	183.20 ± 0.10	K	NIST
Ttriple	182.57 ± 0.05	K	NIST
Ttriple	182.59 ± 0.06	K	NIST
Ttriple	182.59 ± 0.02	K	NIST
Ttriple	182.70 ± 0.20	K	NIST
Ttriple	182.56 ± 0.05	K	NIST
Ttriple	182.55 ± 0.03	K	NIST
Ttriple	182.55 ± 0.05	K	NIST
Ttriple	182.55 ± 0.03	K	NIST
Ttriple	182.56 ± 0.04	K	NIST
Ttriple	182.56 ± 0.04	K	NIST
Ttriple	182.55 ± 0.04	K	NIST
Ttriple	182.55 ± 0.02	K	NIST
Ttriple	182.55 ± 0.01	K	NIST
Ttriple	182.53 ± 0.04	K	NIST
Ttriple	182.53 ± 0.02	K	NIST
Ttriple	182.56 ± 0.00	K	NIST
Ttriple	182.56 ± 0.01	K	NIST
Ttriple	182.56 ± 0.01	K	NIST
Ttriple	182.55 ± 0.02	K	NIST
Ttriple	182.56 ± 0.02	K	NIST
Ttriple	182.55 ± 0.04	K	NIST
Ttriple	182.55 ± 0.02	K	NIST
Ttriple	182.56 ± 0.20	K	NIST
Ttriple	182.56 ± 0.20	K	NIST
Ttriple	182.56 ± 0.05	K	NIST
Ttriple	182.56 ± 0.03	K	NIST
Ttriple	183.56 ± 0.06	K	NIST
Ttriple	Outlier 187.57 ± 0.03	K	NIST
Ttriple	182.20 ± 0.20	K	NIST
Ttriple	182.60 ± 0.20	K	NIST
UQi	4.40		ChemSep v8.3 pure component data Compiled value
URi	5.17		ChemSep v8.3 pure component data Compiled value
Vc	[0.425; 0.432]	m3/kmol
Vc	0.428	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Vc	0.432	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.428	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.428	m3/kmol	KDB
Vc	0.428	m3/kmol	NIST
Vc	0.425 ± 0.001	m3/kmol	NIST
Vm	[1.47e-04; 1.47e-04]	m3/mol
Vm	1.47e-04	m3/mol	Thermodynamic study of (heptane + amine) mixtures. II. Excess and partial molar volumes at 298.15 K
Vm	1.47e-04	m3/mol	Thermodynamic Study of Heptane + Silicone Mixtures. Excess Volumes and Enthalpies at 298.15 K
VCOSTALD	0.43	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.35		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2610000; 0.2610980]
Zc	0.2610000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Zc	0.2610000		ChemSep v8.3 pure component data Compiled value
Zc	0.2610980		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	[191.50; 238.49]	J/mol×K	[357.10; 466.10]
Cp,gas	191.50 ± 0.19	J/mol×K	357.10	NIST
Cp,gas	198.78 ± 0.20	J/mol×K	373.15	NIST
Cp,gas	210.75 ± 0.21	J/mol×K	400.40	NIST
Cp,gas	225.31 ± 0.23	J/mol×K	434.35	NIST
Cp,gas	238.49 ± 0.24	J/mol×K	466.10	NIST
Cp,liquid	[201.34; 328.61]	J/mol×K	[190.00; 480.00]
Cp,liquid	201.82	J/mol×K	190.00	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	201.34	J/mol×K	200.00	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	201.69	J/mol×K	210.00	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	202.75	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	201.51	J/mol×K	228.15	Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
Cp,liquid	202.31	J/mol×K	228.15	Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
Cp,liquid	204.43	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	206.22	J/mol×K	238.15	Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
Cp,liquid	205.11	J/mol×K	238.15	Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
Cp,liquid	206.62	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	209.20	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	209.60	J/mol×K	250.00	NIST
Cp,liquid	212.09	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	215.19	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	216.21	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	218.47	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	220.00	J/mol×K	285.00	NIST
Cp,liquid	221.93	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	222.88	J/mol×K	293.15	NIST
Cp,liquid	222.87	J/mol×K	293.15	Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	223.23	J/mol×K	294.15	Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	223.60	J/mol×K	295.15	Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	223.97	J/mol×K	296.15	Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	224.60	J/mol×K	296.50	NIST
Cp,liquid	224.35	J/mol×K	297.15	Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	224.62	J/mol×K	297.86	NIST
Cp,liquid	224.00	J/mol×K	298.00	NIST
Cp,liquid	223.40	J/mol×K	298.00	NIST
Cp,liquid	211.30	J/mol×K	298.00	NIST
Cp,liquid	223.00	J/mol×K	298.00	NIST
Cp,liquid	224.30	J/mol×K	298.10	NIST
Cp,liquid	224.73	J/mol×K	298.15	NIST
Cp,liquid	224.78	J/mol×K	298.15	NIST
Cp,liquid	224.60	J/mol×K	298.15	NIST
Cp,liquid	224.66	J/mol×K	298.15	NIST
Cp,liquid	224.69	J/mol×K	298.15	NIST
Cp,liquid	224.80	J/mol×K	298.15	NIST
Cp,liquid	224.76	J/mol×K	298.15	NIST
Cp,liquid	224.78	J/mol×K	298.15	NIST
Cp,liquid	224.72	J/mol×K	298.15	Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	224.71	J/mol×K	298.15	NIST
Cp,liquid	224.73	J/mol×K	298.15	NIST
Cp,liquid	255.00	J/mol×K	298.15	NIST
Cp,liquid	224.89	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	224.78	J/mol×K	298.15	NIST
Cp,liquid	224.71	J/mol×K	298.15	NIST
Cp,liquid	224.72	J/mol×K	298.15	NIST
Cp,liquid	224.72	J/mol×K	298.15	NIST
Cp,liquid	224.64	J/mol×K	298.15	NIST
Cp,liquid	224.85	J/mol×K	298.15	NIST
Cp,liquid	224.74	J/mol×K	298.15	NIST
Cp,liquid	224.74	J/mol×K	298.15	NIST
Cp,liquid	224.71	J/mol×K	298.15	NIST
Cp,liquid	224.93	J/mol×K	298.15	NIST
Cp,liquid	224.93	J/mol×K	298.15	NIST
Cp,liquid	328.61	J/mol×K	298.15	NIST
Cp,liquid	224.19	J/mol×K	298.15	NIST
Cp,liquid	226.53	J/mol×K	298.15	NIST
Cp,liquid	225.30	J/mol×K	298.15	NIST
Cp,liquid	225.10	J/mol×K	299.15	Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	222.20	J/mol×K	299.20	NIST
Cp,liquid	233.13	J/mol×K	299.80	NIST
Cp,liquid	225.60	J/mol×K	300.00	NIST
Cp,liquid	225.33	J/mol×K	300.00	NIST
Cp,liquid	225.14	J/mol×K	300.00	NIST
Cp,liquid	225.58	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	225.47	J/mol×K	300.15	Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	210.90	J/mol×K	300.80	NIST
Cp,liquid	225.87	J/mol×K	301.15	Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	226.22	J/mol×K	302.15	Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	217.00	J/mol×K	303.00	NIST
Cp,liquid	225.96	J/mol×K	303.15	Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
Cp,liquid	226.53	J/mol×K	303.15	NIST
Cp,liquid	226.61	J/mol×K	303.15	Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	225.25	J/mol×K	303.15	Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
Cp,liquid	227.00	J/mol×K	304.15	Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	227.40	J/mol×K	305.15	Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	227.75	J/mol×K	306.15	Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	228.14	J/mol×K	307.15	Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	228.54	J/mol×K	308.15	Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	228.95	J/mol×K	309.15	Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	229.39	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	229.30	J/mol×K	310.15	Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	229.71	J/mol×K	311.15	Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	230.11	J/mol×K	312.15	Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	229.16	J/mol×K	313.15	Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
Cp,liquid	230.51	J/mol×K	313.15	Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
Cp,liquid	230.87	J/mol×K	313.15	Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
Cp,liquid	230.37	J/mol×K	313.15	Heat Capacities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
Cp,liquid	233.38	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	237.53	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	247.30	J/mol×K	332.00	NIST
Cp,liquid	240.03	J/mol×K	333.15	Heat Capacities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
Cp,liquid	226.50	J/mol×K	333.15	NIST
Cp,liquid	241.85	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	246.32	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	250.94	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	255.71	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	260.62	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	265.68	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	270.87	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	276.20	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	281.80	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	287.60	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	293.80	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	300.50	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	307.80	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
Cp,liquid	315.70	J/mol×K	470.00	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	324.30	J/mol×K	480.00	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	[0.0000745; 0.0005260]	Pa×s	[273.15; 503.20]
η	0.0005260	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	0.0004950	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	0.0004650	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	0.0004410	Pa×s	288.15	Densities and Viscosities of Binary Mixtures of Tri-n-butyl Phosphate + Cyclohexane, + n-Heptane at T ) (288.15, 293.15, 298.15, 303.15, and 308.15) K
η	0.0004380	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	0.0004038	Pa×s	293.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
η	0.0004170	Pa×s	293.15	Densities and Viscosities of Binary Mixtures of Tri-n-butyl Phosphate + Cyclohexane, + n-Heptane at T ) (288.15, 293.15, 298.15, 303.15, and 308.15) K
η	0.0004142	Pa×s	293.15	Densities and Viscosities of Ternary Mixtures of Heptane, Octane, Nonane, and Hexyl Benzene from 293.15 K to 313.15 K
η	0.0004150	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	0.0003928	Pa×s	298.15	Densities and Viscosities of Ternary Mixtures of Heptane, Octane, Nonane, and Hexyl Benzene from 293.15 K to 313.15 K
η	0.0003960	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of Tri-n-butyl Phosphate + Cyclohexane, + n-Heptane at T ) (288.15, 293.15, 298.15, 303.15, and 308.15) K
η	0.0003970	Pa×s	298.15	NCMS SOLV-DB
η	0.0004009	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	0.0004040	Pa×s	298.15	Volumetric and Viscous Properties at Several Temperatures for Binary Mixtures of N-Methylpiperazine with Methylcyclohexane or n-Heptane
η	0.0003831	Pa×s	298.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
η	0.0003920	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	0.0003750	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	0.0003728	Pa×s	303.15	Densities and Viscosities of Ternary Mixtures of Heptane, Octane, Nonane, and Hexyl Benzene from 293.15 K to 313.15 K
η	0.0003720	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	0.0003750	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of Tri-n-butyl Phosphate + Cyclohexane, + n-Heptane at T ) (288.15, 293.15, 298.15, 303.15, and 308.15) K
η	0.0003629	Pa×s	303.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
η	0.0003750	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	0.0003830	Pa×s	303.15	Volumetric and Viscous Properties at Several Temperatures for Binary Mixtures of N-Methylpiperazine with Methylcyclohexane or n-Heptane
η	0.0003848	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	0.0003541	Pa×s	308.15	Densities and Viscosities of Ternary Mixtures of Heptane, Octane, Nonane, and Hexyl Benzene from 293.15 K to 313.15 K
η	0.0003497	Pa×s	308.15	Viscometric and Volumetric Properties of 10 Regular Binary Systems at 308.15 K and 313.15 K
η	0.0003500	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	0.0003560	Pa×s	308.15	Densities and Viscosities of Binary Mixtures of Tri-n-butyl Phosphate + Cyclohexane, + n-Heptane at T ) (288.15, 293.15, 298.15, 303.15, and 308.15) K
η	0.0003540	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	0.0003360	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	0.0003420	Pa×s	313.15	Volumetric and Viscous Properties at Several Temperatures for Binary Mixtures of N-Methylpiperazine with Methylcyclohexane or n-Heptane
η	0.0003250	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	0.0003329	Pa×s	313.15	Viscometric and Volumetric Properties of 10 Regular Binary Systems at 308.15 K and 313.15 K
η	0.0003274	Pa×s	313.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
η	0.0003373	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	0.0003374	Pa×s	313.15	Densities and Viscosities of Ternary Mixtures of Heptane, Octane, Nonane, and Hexyl Benzene from 293.15 K to 313.15 K
η	0.0003422	Pa×s	313.20	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	0.0003097	Pa×s	323.00	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	0.0002980	Pa×s	323.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
η	0.0003074	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	0.0002834	Pa×s	333.10	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	0.0002704	Pa×s	333.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
η	0.0002793	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	0.0002487	Pa×s	343.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
η	0.0002541	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	0.0002562	Pa×s	343.30	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	0.0002382	Pa×s	353.30	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	0.0002207	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	0.0002027	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	0.0001853	Pa×s	383.20	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	0.0001717	Pa×s	393.20	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	0.0001590	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	0.0001488	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	0.0001392	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	0.0001308	Pa×s	433.20	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	0.0001193	Pa×s	443.40	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	0.0001135	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	0.0001047	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	0.0000978	Pa×s	473.20	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	0.0000896	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	0.0000817	Pa×s	493.20	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	0.0000745	Pa×s	503.20	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
εr	[1.92; 1.94]		[288.15; 308.15]
εr	1.94		288.15	Permittivity and density of the systems (monoglyme, diglyme, triglyme, or tetraglyme + n-heptane) at several temperatures
εr	1.93		298.15	Permittivity and density of the systems (monoglyme, diglyme, triglyme, or tetraglyme + n-heptane) at several temperatures
εr	1.92		308.15	Permittivity and density of the systems (monoglyme, diglyme, triglyme, or tetraglyme + n-heptane) at several temperatures
ΔfusH	[13.99; 14.16]	kJ/mol	[182.20; 182.70]
ΔfusH	14.16	kJ/mol	182.20	NIST
ΔfusH	14.16	kJ/mol	182.20	NIST
ΔfusH	14.04	kJ/mol	182.52	NIST
ΔfusH	14.04	kJ/mol	182.55	NIST
ΔfusH	14.04	kJ/mol	182.55	NIST
ΔfusH	14.02	kJ/mol	182.56	NIST
ΔfusH	14.02	kJ/mol	182.56	NIST
ΔfusH	14.06	kJ/mol	182.56	NIST
ΔfusH	14.03	kJ/mol	182.56	NIST
ΔfusH	13.99	kJ/mol	182.57	NIST
ΔfusH	14.05	kJ/mol	182.59	NIST
ΔfusH	14.04	kJ/mol	182.60	NIST
ΔfusH	14.04	kJ/mol	182.60	NIST
ΔfusH	14.06	kJ/mol	182.70	NIST
ΔsubH	57.90	kJ/mol	183.00	NIST
ΔvapH	[31.70; 36.72]	kJ/mol	[298.00; 371.60]
ΔvapH	36.72	kJ/mol	298.00	Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
ΔvapH	35.60 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	36.10	kJ/mol	318.00	NIST
ΔvapH	36.40	kJ/mol	318.00	NIST
ΔvapH	36.10	kJ/mol	330.50	NIST
ΔvapH	34.50 ± 0.10	kJ/mol	331.00	NIST
ΔvapH	34.40 ± 0.10	kJ/mol	333.00	NIST
ΔvapH	36.00	kJ/mol	335.50	NIST
ΔvapH	36.10	kJ/mol	336.00	NIST
ΔvapH	33.20 ± 0.10	kJ/mol	350.00	NIST
ΔvapH	34.70	kJ/mol	350.50	NIST
ΔvapH	33.10 ± 0.10	kJ/mol	353.00	NIST
ΔvapH	35.50	kJ/mol	353.50	NIST
ΔvapH	35.40	kJ/mol	355.50	NIST
ΔvapH	35.20	kJ/mol	360.50	NIST
ΔvapH	32.00	kJ/mol	371.00	NIST
ΔvapH	31.77	kJ/mol	371.60	NIST
ΔvapH	31.70	kJ/mol	371.60	KDB
ν	[0.0000005; 0.0000007]	m2/s	[283.15; 313.15]
ν	0.0000007	m2/s	283.15	Kinematic Viscosities for Ether + Alkane Mixtures: Experimental Results and UNIFAC-VISCO Parameters
ν	0.0000007	m2/s	283.15	Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
ν	0.0000006	m2/s	298.15	Kinematic Viscosities for Ether + Alkane Mixtures: Experimental Results and UNIFAC-VISCO Parameters
ν	0.0000006	m2/s	298.15	Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
ν	0.0000005	m2/s	313.15	Kinematic Viscosities for Ether + Alkane Mixtures: Experimental Results and UNIFAC-VISCO Parameters
ν	0.0000005	m2/s	313.15	Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
Pvap	[0.82; 2621.76]	kPa	[263.45; 537.20]
Pvap	0.82	kPa	263.45	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	1.53	kPa	273.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Pvap	1.54	kPa	273.15	Excess Properties and Vapor Pressure of 2-Diethylaminoethylamine + n-Heptane
Pvap	1.55	kPa	273.27	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	2.76	kPa	283.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Pvap	2.77	kPa	283.21	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	3.63	kPa	288.15	Experimental and predicted vapour-liquid equilibrium of the binary mixtures n-heptane + chlorobutane isomers
Pvap	4.74	kPa	293.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Pvap	4.76	kPa	293.15	Excess Properties and Vapor Pressure of 2-Diethylaminoethylamine + n-Heptane
Pvap	4.77	kPa	293.25	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	6.14	kPa	298.15	Excess Properties and Vapor Pressure of 2-Diethylaminoethylamine + n-Heptane
Pvap	6.10	kPa	298.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Pvap	6.09	kPa	298.15	NCMS SOLV-DB
Pvap	6.09	kPa	298.15	Experimental and predicted vapour-liquid equilibrium of the binary mixtures n-heptane + chlorobutane isomers
Pvap	6.10	kPa	298.15	Thermophysical Study of the n-Hexane or n-Heptane with 1- Chloropropane Systems
Pvap	7.79	kPa	303.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap	7.83	kPa	303.15	Excess Properties and Vapor Pressure of 2-Diethylaminoethylamine + n-Heptane
Pvap	7.79	kPa	303.15	Excess properties and vapour pressure of (3-diethylaminopropylamine + n-alkanes)
Pvap	7.90	kPa	303.15	Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
Pvap	7.92	kPa	303.15	Measurement and correlation of (vapor + liquid) equilibria for the {2-propoxyethanol (C3E1) + n-hexane} and the {2-propoxyethanol (C3E1) + n-heptane} systems
Pvap	7.87	kPa	303.15	Phase equilibria for mixtures containing nonionic surfactant systems: Modeling and experiments
Pvap	7.79	kPa	303.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Pvap	7.81	kPa	303.15	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	8.32	kPa	305.26	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	9.85	kPa	308.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap	9.87	kPa	308.15	Experimental and predicted vapour-liquid equilibrium of the binary mixtures n-heptane + chlorobutane isomers
Pvap	10.55	kPa	310.22	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	12.41	kPa	313.12	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	12.33	kPa	313.15	Vapor Liquid Equilibria of Binary Mixtures Containing 2-Butanol and Hydrocarbons at 313.15 K
Pvap	12.32	kPa	313.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Pvap	12.33	kPa	313.15	Phase equilibria for mixtures containing nonionic surfactant systems: Modeling and experiments
Pvap	12.39	kPa	313.15	Excess Properties and Vapor Pressure of 2-Diethylaminoethylamine + n-Heptane
Pvap	12.40	kPa	313.15	Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
Pvap	12.24	kPa	313.15	Measurement and correlation of (vapor + liquid) equilibria for the {2-propoxyethanol (C3E1) + n-hexane} and the {2-propoxyethanol (C3E1) + n-heptane} systems
Pvap	12.32	kPa	313.15	Excess properties and vapour pressure of (3-diethylaminopropylamine + n-alkanes)
Pvap	12.34	kPa	313.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap	12.33	kPa	313.15	Vapor-Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K
Pvap	12.34	kPa	313.15	Phase equilibrium properties of the ternary mixture dibutyl ether + toluene + heptane at 313.15 K
Pvap	12.31	kPa	313.15	Thermodynamic behaviour of second generation biofuels: Vapour liquid equilibria and excess enthalpies of the binary mixtures 2-pentanol and n-heptane or 2,2,4-trimethylpentane
Pvap	13.09	kPa	314.93	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	14.07	kPa	316.50	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	15.33	kPa	318.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap	16.19	kPa	319.71	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	18.98	kPa	323.10	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	18.85	kPa	323.15	Excess properties and vapour pressure of (3-diethylaminopropylamine + n-alkanes)
Pvap	18.85	kPa	323.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Pvap	18.95	kPa	323.15	Phase equilibria for mixtures containing nonionic surfactant systems: Modeling and experiments
Pvap	18.91	kPa	323.15	Measurement and correlation of (vapor + liquid) equilibria for the {2-propoxyethanol (C3E1) + n-hexane} and the {2-propoxyethanol (C3E1) + n-heptane} systems
Pvap	18.96	kPa	323.15	Excess Properties and Vapor Pressure of 2-Diethylaminoethylamine + n-Heptane
Pvap	19.00	kPa	323.15	Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
Pvap	18.90	kPa	323.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap	19.10	kPa	323.62	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	20.00	kPa	324.56	Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
Pvap	21.45	kPa	326.44	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	23.04	kPa	328.15	Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap	23.79	kPa	329.04	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	26.15	kPa	331.39	Vapor Liquid Equilibria Measurements for Di-n-Propyl Ether and Butyl Ethyl Ether with n-Heptane
Pvap	26.14	kPa	331.48	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	26.49	kPa	331.82	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	28.13	kPa	333.07	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	27.99	kPa	333.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Pvap	27.98	kPa	333.15	Excess properties and vapour pressure of (3-diethylaminopropylamine + n-alkanes)
Pvap	28.20	kPa	333.15	Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
Pvap	28.14	kPa	333.15	Excess Properties and Vapor Pressure of 2-Diethylaminoethylamine + n-Heptane
Pvap	27.97	kPa	333.21	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	29.69	kPa	334.81	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	30.59	kPa	335.45	Vapor Liquid Equilibria Measurements for Di-n-Propyl Ether and Butyl Ethyl Ether with n-Heptane
Pvap	30.51	kPa	335.50	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	32.24	kPa	336.95	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	32.84	kPa	337.48	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	35.53	kPa	339.56	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	35.66	kPa	339.70	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	37.87	kPa	341.35	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	38.89	kPa	341.94	Vapor Liquid Equilibria Measurements for Di-n-Propyl Ether and Butyl Ethyl Ether with n-Heptane
Pvap	40.00	kPa	342.77	Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
Pvap	40.12	kPa	342.96	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	40.62	kPa	343.04	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	40.43	kPa	343.15	Excess properties and vapour pressure of (3-diethylaminopropylamine + n-alkanes)
Pvap	40.64	kPa	343.15	Excess Properties and Vapor Pressure of 2-Diethylaminoethylamine + n-Heptane
Pvap	40.43	kPa	343.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Pvap	40.60	kPa	343.15	Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
Pvap	42.35	kPa	344.47	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	42.88	kPa	344.76	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	44.75	kPa	346.04	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	46.80	kPa	347.16	Vapor Liquid Equilibria Measurements for Di-n-Propyl Ether and Butyl Ethyl Ether with n-Heptane
Pvap	46.71	kPa	347.28	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	47.80	kPa	347.85	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	49.09	kPa	348.72	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	50.62	kPa	349.53	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	50.97	kPa	349.68	Vapor Liquid Equilibria Measurements for Di-n-Propyl Ether and Butyl Ethyl Ether with n-Heptane
Pvap	51.49	kPa	350.12	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	53.33	kPa	351.08	Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
Pvap	53.30	kPa	351.14	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	53.41	kPa	351.21	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	55.76	kPa	352.49	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	56.20	kPa	352.58	Vapor Liquid Equilibria Measurements for Di-n-Propyl Ether and Butyl Ethyl Ether with n-Heptane
Pvap	57.56	kPa	353.01	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	57.27	kPa	353.15	Excess Properties and Vapor Pressure of 2-Diethylaminoethylamine + n-Heptane
Pvap	56.99	kPa	353.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Pvap	57.09	kPa	353.15	Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
Pvap	57.10	kPa	353.15	Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
Pvap	57.88	kPa	353.62	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	58.57	kPa	353.90	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	60.00	kPa	354.63	Vapor Liquid Equilibria Measurements for Di-n-Propyl Ether and Butyl Ethyl Ether with n-Heptane
Pvap	60.00	kPa	354.72	Isobaric vapor liquid equilibria for the n-hexane + 2-isopropoxyethanol and n-heptane + 2-isopropoxyethanol systems
Pvap	60.18	kPa	354.79	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	63.11	kPa	356.25	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	63.98	kPa	356.61	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	64.60	kPa	356.78	Vapor Liquid Equilibria Measurements for Di-n-Propyl Ether and Butyl Ethyl Ether with n-Heptane
Pvap	66.42	kPa	357.84	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	66.66	kPa	357.85	Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
Pvap	67.99	kPa	358.49	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	68.27	kPa	358.68	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	70.24	kPa	359.38	Vapor Liquid Equilibria Measurements for Di-n-Propyl Ether and Butyl Ethyl Ether with n-Heptane
Pvap	71.15	kPa	359.98	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	74.25	kPa	361.33	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	75.87	kPa	362.03	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	76.47	kPa	362.11	Vapor Liquid Equilibria Measurements for Di-n-Propyl Ether and Butyl Ethyl Ether with n-Heptane
Pvap	76.55	kPa	362.30	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	78.59	kPa	363.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Pvap	78.94	kPa	363.15	Excess Properties and Vapor Pressure of 2-Diethylaminoethylamine + n-Heptane
Pvap	79.00	kPa	363.32	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	79.55	kPa	363.44	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	79.99	kPa	363.64	Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
Pvap	80.00	kPa	363.67	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	80.00	kPa	363.74	Isobaric vapor liquid equilibria for the n-hexane + 2-isopropoxyethanol and n-heptane + 2-isopropoxyethanol systems
Pvap	81.28	kPa	364.24	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	81.76	kPa	364.36	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	83.45	kPa	364.95	Vapor Liquid Equilibria Measurements for Di-n-Propyl Ether and Butyl Ethyl Ether with n-Heptane
Pvap	84.05	kPa	365.32	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	85.00	kPa	365.65	Experimental Vapor-Liquid Equilibria and Thermodynamic Modeling of the Methanol + n-Heptane and 1-Butanol + Aniline Binary Systems
Pvap	86.30	kPa	366.20	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	86.56	kPa	366.23	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	88.10	kPa	366.87	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	88.40	kPa	366.87	Vapor Liquid Equilibria Measurements for Di-n-Propyl Ether and Butyl Ethyl Ether with n-Heptane
Pvap	91.09	kPa	367.97	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	93.32	kPa	368.70	Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
Pvap	93.46	kPa	368.83	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	94.00	kPa	368.85	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	96.33	kPa	369.84	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	98.98	kPa	370.85	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	370.97	A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol
Pvap	100.00	kPa	371.11	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	100.00	kPa	371.20	Isobaric vapor liquid equilibria for the n-hexane + 2-isopropoxyethanol and n-heptane + 2-isopropoxyethanol systems
Pvap	101.30	kPa	371.28	Vapor Liquid Equilibria Measurements for Di-n-Propyl Ether and Butyl Ethyl Ether with n-Heptane
Pvap	101.30	kPa	371.35	Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
Pvap	100.68	kPa	371.35	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	101.30	kPa	371.47	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	101.30	kPa	371.53	Isobaric vapor-liquid equilibrium of three binary systems containing dimethyl succinate, dimethyl glutarate and dimethyl adipate at 2, 5.2 and 8.3 kPa
Pvap	101.32	kPa	371.56	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	100.00	kPa	371.58	Isobaric Vapor-Liquid Equilibrium for Two Binary Systems of n-Heptane + sec-Butyl Acetate and Methylcyclohexane + sec-Butyl Acetate under Atmosphere
Pvap	101.46	kPa	371.66	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	102.90	kPa	372.08	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	103.92	kPa	372.42	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	106.48	kPa	373.25	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	108.71	kPa	373.98	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	110.39	kPa	374.50	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	111.77	kPa	374.93	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	113.35	kPa	375.41	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	116.21	kPa	376.29	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	119.14	kPa	377.17	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	120.32	kPa	377.51	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	120.89	kPa	377.68	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	123.70	kPa	378.49	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	126.80	kPa	379.37	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	130.00	kPa	380.26	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	132.04	kPa	380.83	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	145.56	kPa	384.39	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	166.41	kPa	389.41	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	182.39	kPa	392.89	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	185.50	kPa	393.58	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	186.60	kPa	393.79	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	189.67	kPa	394.43	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	192.97	kPa	395.10	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	196.04	kPa	395.73	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	197.85	kPa	396.09	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	199.97	kPa	396.50	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	200.79	kPa	396.70	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	224.89	kPa	401.26	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	248.92	kPa	405.44	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	275.09	kPa	409.66	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	302.76	kPa	413.80	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	341.76	kPa	419.17	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	378.80	kPa	423.85	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	420.15	kPa	428.69	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	477.00	kPa	433.15	In Situ Determination of Phase Equilibria of Methyl Benzoate + Alkane Mixtures Using an Infrared Absorption Method. Comparison with Polar GC-SAFT Predictions
Pvap	467.65	kPa	433.81	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	518.27	kPa	438.86	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	587.00	kPa	443.15	In Situ Determination of Phase Equilibria of Methyl Benzoate + Alkane Mixtures Using an Infrared Absorption Method. Comparison with Polar GC-SAFT Predictions
Pvap	568.27	kPa	443.50	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	619.76	kPa	447.95	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	666.97	kPa	451.80	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	703.00	kPa	453.15	In Situ Determination of Phase Equilibria of Methyl Benzoate + Alkane Mixtures Using an Infrared Absorption Method. Comparison with Polar GC-SAFT Predictions
Pvap	726.16	kPa	456.35	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	773.29	kPa	459.78	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	850.62	kPa	465.07	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	925.23	kPa	469.84	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	980.00	kPa	473.10	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	980.00	kPa	473.20	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	960.00	kPa	473.30	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	983.90	kPa	473.39	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	1030.55	kPa	476.11	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	1092.41	kPa	479.57	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	1169.38	kPa	483.67	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	1242.28	kPa	487.36	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	1313.39	kPa	490.81	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	1384.19	kPa	494.11	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	1443.40	kPa	496.77	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	1460.00	kPa	498.20	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	1470.00	kPa	498.20	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	1490.00	kPa	498.20	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	1518.18	kPa	500.01	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	1604.13	kPa	503.59	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	1699.51	kPa	507.39	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	1793.01	kPa	510.95	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	1911.60	kPa	515.27	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	2019.09	kPa	518.99	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	2116.11	kPa	522.22	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	2180.00	kPa	523.20	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	2190.00	kPa	523.20	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	2170.00	kPa	523.20	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	2219.70	kPa	525.53	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	2309.81	kPa	528.30	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	2416.50	kPa	531.47	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	2525.68	kPa	534.57	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
Pvap	2621.76	kPa	537.20	Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
n0	[1.37197; 1.53800]		[293.10; 323.15]
n0	1.50240		293.10	(Liquid + liquid) equilibria of {heptane + xylene + N-formylmorpholine} ternary system
n0	1.38820		293.10	(Liquid + liquid) equilibria of three ternary systems: (heptane + benzene + N-formylmorpholine), (heptane + toluene + N-formylmorpholine), (heptane + xylene + N-formylmorpholine) from T = (298.15 to 353.15) K
n0	1.38760		293.15	Bubble points of some binary mixtures formed by o-cresol at 95.75 kPa
n0	1.38760		293.15	Limiting Activity Coefficients by Comparative Tensimetry: 1-Propanol and 1-Butanol in Heptane and in Octane
n0	1.38780		293.15	Infinite Dilution Activity Coefficients of Hydrocarbons in Triethylene Glycol and Tetraethylene Glycol
n0	1.38780		293.15	Isothermal vapour-liquid equilibrium data for the binary systems of (CHF3 or C2F6) and n-heptane
n0	1.38780		293.15	A novel static analytical apparatus for phase equilibrium measurements
n0	1.38770		293.15	Vapor Liquid Equilibrium Data for the Morpholine-4-carbaldehyde + n-Hexane or n-Heptane Binary Systems Using a Static-Synthetic Apparatus
n0	1.38720		293.15	Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
n0	1.38776		293.15	Mixing properties of binary mixtures presenting azeotropes at several temperatures
n0	1.38730		293.20	Liquid phase equilibria for mixtures of (an aliphatic hydrocarbon + toluene + gamma-butyrolactone)
n0	1.38850		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	1.38520		298.15	Molar heat capacities for (2-methyl-2-butanol + heptane) mixtures and cyclopentanol at temperatures from (284 to 353) K
n0	1.38520		298.15	Isothermal vapour-liquid equilibrium data for the binary systems of (CHF3 or C2F6) and n-heptane
n0	1.38600		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	1.38511		298.15	KDB
n0	1.38517		298.15	Mixing properties of binary mixtures presenting azeotropes at several temperatures
n0	1.38530		298.15	Improvements in the Experimentation and the Representation of Thermodynamic Properties (iso-p VLE and yE) of Alkyl Propanoate + Alkane Binaries
n0	1.38550		298.15	Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
n0	1.38530		298.15	Thermodynamic and acoustic properties of (heptane + dodecane) mixtures under elevated pressures
n0	1.38515		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	1.38515		298.15	Extraction of toluene from aliphatic compounds using an ionic liquid as solvent: Influence of the alkane on the (liquid + liquid) equilibrium
n0	1.38529		298.15	Application of [HMim][NTf2], [HMim][TfO] and [BMim][TfO] ionic liquids on the extraction of toluene from alkanes: Effect of the anion and the alkyl chain length of the cation on the LLE
n0	1.38529		298.15	1-Alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ionic liquids as solvents in the separation of azeotropic mixtures
n0	1.38530		298.15	Measurements and Correlations of the Isobaric Vapor Liquid Equilibria of Binary Mixtures and Excess Properties for Mixtures Containing an Alkyl (Methyl, Ethyl) Butanoate with an Alkane (Heptane, Nonane) at 101.3 kPa
n0	1.38500		298.15	NCMS SOLV-DB
n0	1.38517		298.15	Thiophene separation from aliphatic hydrocarbons using the 1-ethyl-3-methylimidazolium ethylsulfate ionic liquid
n0	1.53800		298.15	Thermodynamic and Acoustic Properties of Mixtures of Dibromomethane + Heptane
n0	1.38527		298.15	Measurement of VLE Data by Using an Experimental Installation with Automatic Control: Modeling of Binary Systems of Methyl Acetate or Ethyl Acetate with n-Heptane or 2,2,4-Trimethylpentane at Both 0.1 and 1.5 MPa
n0	1.38517		298.15	A study on the liquid liquid equilibria of 1-alkyl-3-methylimidazolium hexafluorophosphate with ethanol and alkanes
n0	1.38510		298.15	Bubble Temperature Measurements on the Binary Mixtures of n-Heptane or Nitrobenzene or Chlorobenzene with Some Chloroethanes and Chloroethylenes at (94.6 to 95.8) kPa
n0	1.38510		298.15	Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
n0	1.38517		298.15	Phase behaviour of 1-methyl-3-octylimidazolium bis[trifluoromethylsulfonyl]imide with thiophene and aliphatic hydrocarbons: The influence of n-alkane chain length
n0	1.38540		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	1.38530		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	1.38520		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	1.38530		298.15	Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Water + Cyclohexylamine + Aromatic Hydrocarbon (Toluene or Propylbenzene) or Aliphatic Hydrocarbon (Heptane or Octane)
n0	1.38530		298.15	Vapor-Liquid Equilibrium for Binary System of Diethyl Sulfide + n-Heptane and Diethyl Sulfide + 2,2,4-Trimethylpentane at (363.15 and 353.15) K
n0	1.38515		298.15	Separation of Benzene from Linear Alkanes (C6-C9) Using 1-Ethyl-3-Methylimidazolium Ethylsulfate at T = 298.15 K
n0	1.38500		298.20	Liquid-Liquid Equilibria for Ternary Mixtures (an Ionic Liquid + Benzene +Heptane or Hexadecane) at T ) 298.2 K and Atmospheric Pressure
n0	1.38510		298.20	(Liquid + liquid) equilibria of aqueous solutions of butyric acid with n-heptane and toluene at T = (298.2, 308.2, and 318.2) K
n0	1.38360		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	1.38259		303.15	Experimental Determination of Densities and Refractive Indices of the Ternary Mixture 2-Methyl-2-propanol + Cyclohexylamine + n-Heptane at T = (303.15 to 323.15) K
n0	1.38440		303.15	(Liquid + liquid) equilibria measurements for ternary systems (sulfolane + a carboxylic acid + n-heptane) at T = 303.15 K and at 0.1 MPa
n0	1.38258		303.15	Mixing properties of binary mixtures presenting azeotropes at several temperatures
n0	1.38270		303.15	Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
n0	1.37995		308.15	Experimental Determination of Densities and Refractive Indices of the Ternary Mixture 2-Methyl-2-propanol + Cyclohexylamine + n-Heptane at T = (303.15 to 323.15) K
n0	1.38100		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	1.37731		313.15	Experimental Determination of Densities and Refractive Indices of the Ternary Mixture 2-Methyl-2-propanol + Cyclohexylamine + n-Heptane at T = (303.15 to 323.15) K
n0	1.37463		318.15	Experimental Determination of Densities and Refractive Indices of the Ternary Mixture 2-Methyl-2-propanol + Cyclohexylamine + n-Heptane at T = (303.15 to 323.15) K
n0	1.37480		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
n0	1.37480		318.15	Thermodynamic properties of (an ester + an alkane). XVI. Experimental HEm and V Em values and a new correlation method for (an alkyl ethanoate + an n-alkane) at 318.15 K
n0	1.37197		323.15	Experimental Determination of Densities and Refractive Indices of the Ternary Mixture 2-Methyl-2-propanol + Cyclohexylamine + n-Heptane at T = (303.15 to 323.15) K
ρl	[626.26; 700.67]	kg/m3	[273.15; 358.15]
ρl	700.67	kg/m3	273.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	696.57	kg/m3	278.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	692.40	kg/m3	283.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	692.44	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	688.13	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	687.95	kg/m3	288.15	Densities and Excess Molar Volumes of 2-Butanol + Cyclohexanamine + Heptane and 2-Butanol + n-Heptane at Temperatures between (288.15 and 323.15) K
ρl	688.25	kg/m3	288.15	Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
ρl	688.20	kg/m3	288.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	689.00	kg/m3	288.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	687.95	kg/m3	288.15	Experimental determination and modelling of densities and excess molar volumes of ternary system (1-butanol + cyclohexylamine + n-heptane) and corresponding binaries from 288.15 to 323.15K
ρl	688.59	kg/m3	288.15	Excess molar volumes of (1-chlorobutane +heptane + 2-butanone or 2-pentanone) at 288.15 , 303.15 and 313.15 K . Measurements and correlations.
ρl	684.00	kg/m3	293.00	KDB
ρl	683.99	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	683.78	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	683.67	kg/m3	293.15	Density of Working Liquids for Diffusion Vacuum Pumps
ρl	683.89	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	683.91	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	683.73	kg/m3	293.15	Experimental determination and modelling of densities and excess molar volumes of ternary system (1-butanol + cyclohexylamine + n-heptane) and corresponding binaries from 288.15 to 323.15K
ρl	684.00	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	685.00	kg/m3	293.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	683.82	kg/m3	293.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
ρl	683.93	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	684.05	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	683.85	kg/m3	293.15	Thermodynamics of Mixtures Containing Amines. XII. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for N-Methylaniline + Hydrocarbon Systems
ρl	683.73	kg/m3	293.15	Densities and Excess Molar Volumes of 2-Butanol + Cyclohexanamine + Heptane and 2-Butanol + n-Heptane at Temperatures between (288.15 and 323.15) K
ρl	683.99	kg/m3	293.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	683.85	kg/m3	293.15	Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρl	683.53	kg/m3	293.20	Isobaric vapour liquid equilibria for binary mixtures of n-heptane with bromobenzene, chlorobenzene and fluorobenzene at atmospheric pressure
ρl	683.82	kg/m3	293.22	Thermodynamic and acoustic properties of binary mixtures of alcohols and alkanes. II. Density and heat capacity of (ethanol + n-heptane) under elevated pressures
ρl	679.50	kg/m3	298.15	Vapor-Liquid Equilibrium Data for the Binary Decafluoropentane (HFC-43-10meec) + Heptane, Decafluoropentane + Butyl Ethyl Ether, Octafluorobutane (HFC-338pcc) + Butyl Ethyl Ether, and Heptafluoro Propyl Methyl Ether (HFE-347mcc) + HFC-338pcc Systems at 101.3 kPa
ρl	679.57	kg/m3	298.15	Application of 1-alkyl-3-methylpyridinium bis(trifluoromethylsulfonyl)imide ionic liquids for the ethanol removal from its mixtures with alkanes
ρl	679.70	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	679.63	kg/m3	298.15	Thermodynamics of Mixtures Containing a Strongly Polar Compound. 9. Liquid-Liquid Equilibria for epsilon-Caprolactam + Selected Alkanes
ρl	679.49	kg/m3	298.15	Densities and Excess Molar Volumes of 2-Butanol + Cyclohexanamine + Heptane and 2-Butanol + n-Heptane at Temperatures between (288.15 and 323.15) K
ρl	683.80	kg/m3	298.15	Liquid-liquid equilibria for ternary mixtures of 2,2-dimethyl-1,3-dioxolane-4-methanol with n-heptane, toluene, ethanol and water
ρl	679.75	kg/m3	298.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	679.54	kg/m3	298.15	Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
ρl	679.63	kg/m3	298.15	Thermodynamics of mixtures containing amines VI. Liquid liquid equilibria for mixtures of o-toluidine + selected alkanes
ρl	680.00	kg/m3	298.15	Effect of Temperature on Phase Equilibrium of the Mixed-Solvent System of (2,2,2-Trifluoroethanol + Methanol + Cyclohexane)
ρl	680.00	kg/m3	298.15	Liquid-Liquid Equilibrium of (Cyclohexane + 2,2,2-Trifluoroethanol) and (Cyclohexane + Methanol) from (278.15 to 318.15) K
ρl	680.02	kg/m3	298.15	Binary Liquid Liquid Equilibria of ?-Valerolactone with Some Hydrocarbons
ρl	679.61	kg/m3	298.15	Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρl	679.79	kg/m3	298.15	Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
ρl	679.74	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	679.54	kg/m3	298.15	Excess Enthalpy and Excess Volume for Pyridine + Methyldiethanolamine and Pyridine + Ethanolamine Mixtures
ρl	679.60	kg/m3	298.15	Thermodynamics of Mixtures Containing Amines. XII. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for N-Methylaniline + Hydrocarbon Systems
ρl	679.71	kg/m3	298.15	Thermodynamics of Mixtures Containing Aromatic Alcohols. 1. Liquid Liquid Equilibria for (Phenylmethanol + Alkane) Systems
ρl	679.51	kg/m3	298.15	Solvation of N-methyl-2-pyrrolidone and N,N-dimethylpropanamide in cyclohexane, heptane, n-alkan-1-ols(C1-C4) and water at 298.15K
ρl	679.69	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	679.47	kg/m3	298.15	Solvent extraction of thiophene from n-alkanes (C7, C12, and C16) using the ionic liquid [C8mim][BF4]
ρl	679.54	kg/m3	298.15	Experimental and theoretical study of surface tension of binary mixtures of (n-alkyl acetates + heptane, benzene, and toluene)
ρl	680.00	kg/m3	298.15	Phase diagrams of (hexane + methanol + 2,2,2-trifluoroethanol) at three temperatures: Measurement and correlation
ρl	679.55	kg/m3	298.15	Thermodynamic properties of solvation of aromatic compounds in cyclohexane, heptane, benzene, 1,4-dioxane, and chloroform at 298.15 K
ρl	679.71	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	679.91	kg/m3	298.15	Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
ρl	679.43	kg/m3	298.15	Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Aliphatic Hydrocarbons (Heptane or Octane) + Phenols + Water
ρl	679.59	kg/m3	298.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
ρl	679.63	kg/m3	298.15	Thermodynamics of Mixtures Containing a Strongly Polar Compound. 8. Liquid-Liquid Equilibria for N,N-Dialkylamide + Selected N-Alkanes
ρl	679.50	kg/m3	298.15	Vapor-Liquid Equilibria for the Ternary Systems of Methyl tert-Butyl Ether + Methanol + Methylcyclohexane and Methyl tert-Butyl Ether + Methanol + n-Heptane and Constituent Binary Systems at 313.15 K
ρl	679.54	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	679.49	kg/m3	298.15	Excess molar volumes and isentropic compressibilities changes of mixing of tetrahydropyran + benzene + cyclo or n-alkanes ternary mixtures at 308.15 K
ρl	679.60	kg/m3	298.15	Cation effect of ammonium imide based ionic liquids in alcohols extraction from alcohol-alkane azeotropic mixtures
ρl	679.66	kg/m3	298.15	Thermodynamic and acoustic properties of binary mixtures of alcohols and alkanes. I. Speed of sound in (ethanol + n-heptane) under elevated pressures
ρl	690.60	kg/m3	298.15	Ternary (liquid + liquid) equilibria for mixtures of 1-hexyl-3-methylimidazolium (tetrafluoroborate or hexafluorophosphate) + benzene + an alkane at T = 298.2 K and p = 0.1 MPa
ρl	680.17	kg/m3	298.15	Excess Enthalpies of Binary Mixtures of 1-Hexene with Some n-Alkanes at 298.15 K
ρl	679.78	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	679.48	kg/m3	298.15	Separation of sulfur compounds from alkanes with 1-alkylcyanopyridinium-based ionic liquids
ρl	679.54	kg/m3	298.15	Effect of the alkyl side chain of the 1-alkylpiperidinium-based ionic liquids on desulfurization of fuels
ρl	679.57	kg/m3	298.15	Quaternary (liquid + liquid) equilibrium data for the extraction of toluene from alkanes using the ionic liquid [EMim][MSO4]
ρl	679.54	kg/m3	298.15	Extraction desulfurization process of fuels with ionic liquids
ρl	679.57	kg/m3	298.15	(Liquid + liquid) equilibrium of ternary and quaternary systems containing heptane, cyclohexane, toluene and the ionic liquid [EMim][N(CN)2]. Experimental data and correlation
ρl	679.50	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	681.48	kg/m3	298.15	Quaternary isothermal vapor-liquid equilibrium of the model biofuel 2-butanone + n-heptane + tetrahydrofuran + cyclohexane using Raman spectroscopic characterization
ρl	679.46	kg/m3	298.15	Conformational analysis of branched alkanes using limiting partial molar volumes
ρl	679.48	kg/m3	298.15	Separation of pyridine from heptane with tricyanomethanide-based ionic liquids
ρl	679.57	kg/m3	298.15	Capacity of two 1-butyl-1-methylpyrrolidinium-based ionic liquidsfor the extraction of ethanol from its mixtures with heptane and hexane
ρl	680.00	kg/m3	298.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	679.40	kg/m3	298.15	Viscosities of Dimethyl Carbonate or Diethyl Carbonate with Alkanes at Four Temperatures. New UNIFAC-VISCO Parameters
ρl	679.00	kg/m3	298.15	Liquid-Liquid Equilibrium Data for Ternary Systems Containing Alkanes (n-Pentane, n-Hexane, n-Heptane, and n-Octane) + Alcohol (Methanol and Ethanol) + Protic Ionic Liquid (2-HEAF)
ρl	679.64	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	683.80	kg/m3	298.15	Liquid-liquid equilibria for multicomponent mixtures of 2,2-dimethyl-1,3-dioxolane with n-heptane, toluene, ethanol and water
ρl	679.71	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	679.71	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	679.49	kg/m3	298.15	Topological and thermodynamic investigations of binary mixtures: Molar excess volumes, molar excess enthalpies and isentropic compressibility changes of mixing
ρl	679.55	kg/m3	298.15	Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
ρl	679.60	kg/m3	298.15	Vapour liquid equilibrium at T = 308.15 K for binary systems: Dibromomethane + n-heptane, bromotrichloromethane + n-heptane, bromotrichloromethane + dibromomethane, bromotrichloromethane + bromochloromethane and dibromomethane + bromochloromethane. Experimental data and modelling
ρl	679.49	kg/m3	298.15	Experimental determination and modelling of densities and excess molar volumes of ternary system (1-butanol + cyclohexylamine + n-heptane) and corresponding binaries from 288.15 to 323.15K
ρl	679.75	kg/m3	298.16	Thermodynamic and acoustic properties of binary mixtures of alcohols and alkanes. II. Density and heat capacity of (ethanol + n-heptane) under elevated pressures
ρl	682.30	kg/m3	298.20	Ternary Liquid-Liquid Equilibria for Mixtures of 1-Methyl-3-octylimidazolium Chloride + an Alkanol + an Alkane at 298.2 K and 1 bar
ρl	679.86	kg/m3	298.20	Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
ρl	675.75	kg/m3	301.62	Density of Working Liquids for Diffusion Vacuum Pumps
ρl	675.31	kg/m3	303.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
ρl	675.40	kg/m3	303.15	Effect of polarity and temperature on the binary interaction between D2EHPA extractant and organic solvents (kerosene, n-heptane, chlorobenzene and 1-octanol): Experimental and thermodynamics
ρl	675.49	kg/m3	303.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	675.84	kg/m3	303.15	Excess molar volumes of (1-chlorobutane +heptane + 2-butanone or 2-pentanone) at 288.15 , 303.15 and 313.15 K . Measurements and correlations.
ρl	675.23	kg/m3	303.15	Densities and Excess Molar Volumes of 2-Butanol + Cyclohexanamine + Heptane and 2-Butanol + n-Heptane at Temperatures between (288.15 and 323.15) K
ρl	675.54	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	675.41	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	675.23	kg/m3	303.15	Experimental determination and modelling of densities and excess molar volumes of ternary system (1-butanol + cyclohexylamine + n-heptane) and corresponding binaries from 288.15 to 323.15K
ρl	675.37	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	675.47	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	675.63	kg/m3	303.15	Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
ρl	675.53	kg/m3	303.15	Thermodynamics of Mixtures Containing Amines. XII. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for N-Methylaniline + Hydrocarbon Systems
ρl	676.00	kg/m3	303.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	675.35	kg/m3	303.15	Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρl	675.51	kg/m3	303.17	Thermodynamic and acoustic properties of binary mixtures of alcohols and alkanes. II. Density and heat capacity of (ethanol + n-heptane) under elevated pressures
ρl	670.94	kg/m3	308.15	Densities and Excess Molar Volumes of 2-Butanol + Cyclohexanamine + Heptane and 2-Butanol + n-Heptane at Temperatures between (288.15 and 323.15) K
ρl	671.07	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	671.20	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	670.94	kg/m3	308.15	Experimental determination and modelling of densities and excess molar volumes of ternary system (1-butanol + cyclohexylamine + n-heptane) and corresponding binaries from 288.15 to 323.15K
ρl	671.02	kg/m3	308.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
ρl	671.33	kg/m3	308.15	Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
ρl	671.19	kg/m3	308.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	671.12	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	671.05	kg/m3	308.15	Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρl	671.21	kg/m3	308.17	Thermodynamic and acoustic properties of binary mixtures of alcohols and alkanes. II. Density and heat capacity of (ethanol + n-heptane) under elevated pressures
ρl	667.37	kg/m3	310.71	Density of Working Liquids for Diffusion Vacuum Pumps
ρl	666.74	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	666.73	kg/m3	313.15	Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρl	666.92	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	666.87	kg/m3	313.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	666.89	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	666.89	kg/m3	313.15	Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
ρl	666.80	kg/m3	313.15	Effect of polarity and temperature on the binary interaction between D2EHPA extractant and organic solvents (kerosene, n-heptane, chlorobenzene and 1-octanol): Experimental and thermodynamics
ρl	668.00	kg/m3	313.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	666.62	kg/m3	313.15	Densities and Excess Molar Volumes of 2-Butanol + Cyclohexanamine + Heptane and 2-Butanol + n-Heptane at Temperatures between (288.15 and 323.15) K
ρl	667.01	kg/m3	313.15	Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
ρl	666.68	kg/m3	313.15	Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
ρl	666.62	kg/m3	313.15	Experimental determination and modelling of densities and excess molar volumes of ternary system (1-butanol + cyclohexylamine + n-heptane) and corresponding binaries from 288.15 to 323.15K
ρl	665.84	kg/m3	313.15	Excess molar volumes of (1-chlorobutane +heptane + 2-butanone or 2-pentanone) at 288.15 , 303.15 and 313.15 K . Measurements and correlations.
ρl	666.97	kg/m3	313.17	Thermodynamic and acoustic properties of binary mixtures of alcohols and alkanes. II. Density and heat capacity of (ethanol + n-heptane) under elevated pressures
ρl	662.65	kg/m3	318.15	Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
ρl	662.27	kg/m3	318.15	Densities and Excess Molar Volumes of 2-Butanol + Cyclohexanamine + Heptane and 2-Butanol + n-Heptane at Temperatures between (288.15 and 323.15) K
ρl	662.27	kg/m3	318.15	Experimental determination and modelling of densities and excess molar volumes of ternary system (1-butanol + cyclohexylamine + n-heptane) and corresponding binaries from 288.15 to 323.15K
ρl	662.38	kg/m3	318.15	Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρl	662.38	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	662.52	kg/m3	318.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	662.55	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	662.67	kg/m3	318.18	Thermodynamic and acoustic properties of binary mixtures of alcohols and alkanes. II. Density and heat capacity of (ethanol + n-heptane) under elevated pressures
ρl	659.85	kg/m3	319.85	Density of Working Liquids for Diffusion Vacuum Pumps
ρl	658.19	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	657.70	kg/m3	323.15	Effect of polarity and temperature on the binary interaction between D2EHPA extractant and organic solvents (kerosene, n-heptane, chlorobenzene and 1-octanol): Experimental and thermodynamics
ρl	657.98	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	657.90	kg/m3	323.15	Densities and Excess Molar Volumes of 2-Butanol + Cyclohexanamine + Heptane and 2-Butanol + n-Heptane at Temperatures between (288.15 and 323.15) K
ρl	658.13	kg/m3	323.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	657.99	kg/m3	323.15	Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρl	658.26	kg/m3	323.15	Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
ρl	657.90	kg/m3	323.15	Experimental determination and modelling of densities and excess molar volumes of ternary system (1-butanol + cyclohexylamine + n-heptane) and corresponding binaries from 288.15 to 323.15K
ρl	660.00	kg/m3	323.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	653.79	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	653.71	kg/m3	328.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	653.72	kg/m3	328.15	Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
ρl	653.57	kg/m3	328.15	Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρl	651.92	kg/m3	329.04	Density of Working Liquids for Diffusion Vacuum Pumps
ρl	649.24	kg/m3	333.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	651.00	kg/m3	333.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	648.40	kg/m3	333.15	Effect of polarity and temperature on the binary interaction between D2EHPA extractant and organic solvents (kerosene, n-heptane, chlorobenzene and 1-octanol): Experimental and thermodynamics
ρl	649.33	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	649.11	kg/m3	333.15	Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρl	644.84	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	644.74	kg/m3	338.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	644.77	kg/m3	338.15	Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
ρl	644.60	kg/m3	338.15	Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρl	644.32	kg/m3	338.26	Density of Working Liquids for Diffusion Vacuum Pumps
ρl	640.29	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	640.19	kg/m3	343.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	642.00	kg/m3	343.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	635.91	kg/m3	347.53	Density of Working Liquids for Diffusion Vacuum Pumps
ρl	635.63	kg/m3	348.15	Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
ρl	635.60	kg/m3	348.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	630.95	kg/m3	353.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ρl	627.85	kg/m3	356.84	Density of Working Liquids for Diffusion Vacuum Pumps
ρl	626.26	kg/m3	358.15	Experimental measurements and prediction of liquid densities for n-alkane mixtures
ΔfusS	[76.81; 78.81]	J/mol×K	[182.20; 182.70]
ΔfusS	77.73	J/mol×K	182.20	NIST
ΔfusS	77.73	J/mol×K	182.20	NIST
ΔfusS	76.93	J/mol×K	182.52	NIST
ΔfusS	76.89	J/mol×K	182.55	NIST
ΔfusS	76.89	J/mol×K	182.55	NIST
ΔfusS	78.81	J/mol×K	182.56	NIST
ΔfusS	76.81	J/mol×K	182.56	NIST
ΔfusS	77.02	J/mol×K	182.56	NIST
ΔfusS	76.81	J/mol×K	182.56	NIST
ΔfusS	76.96	J/mol×K	182.59	NIST
ΔfusS	77.00	J/mol×K	182.70	NIST
csound,fluid	[111.10; 1154.11]	m/s	[292.70; 536.15]
csound,fluid	1154.11	m/s	292.70	Thermodynamic and Acoustic Properties of Mixtures of 1,6-Dichlorohexane with Heptane from (293 to 313) K
csound,fluid	1151.92	m/s	293.13	Excess molar heat capacities for (decan-1-ol + n-heptane) at temperatures from (290 to 318) K. Experimental results and theoretical description using the ERAS model
csound,fluid	1152.60	m/s	293.15	Excess Molar Volumes and Speed of Sound in Bromotrichloromethane + n-Heptane, Dibromomethane + n-Heptane, Bromotrichloromethane + Dibromomethane, and Bromotrichloromethane + Bromochloromethane at Temperatures from (293.15 to 313.15) K
csound,fluid	1152.20	m/s	293.15	Excess Molar Volumes and Speed of Sound in Bromotrichloromethane + n-Heptane, Dibromomethane + n-Heptane, Bromotrichloromethane + Dibromomethane, and Bromotrichloromethane + Bromochloromethane at Temperatures from (293.15 to 313.15) K
csound,fluid	1131.06	m/s	298.00	Thermodynamic and Acoustic Properties of Mixtures of 1,6-Dichlorohexane with Heptane from (293 to 313) K
csound,fluid	1130.26	m/s	298.12	Excess molar heat capacities for (decan-1-ol + n-heptane) at temperatures from (290 to 318) K. Experimental results and theoretical description using the ERAS model
csound,fluid	1130.90	m/s	298.15	Excess Molar Volumes and Speed of Sound in Bromotrichloromethane + n-Heptane, Dibromomethane + n-Heptane, Bromotrichloromethane + Dibromomethane, and Bromotrichloromethane + Bromochloromethane at Temperatures from (293.15 to 313.15) K
csound,fluid	1131.00	m/s	298.15	Excess Molar Volumes and Speed of Sound in Bromotrichloromethane + n-Heptane, Dibromomethane + n-Heptane, Bromotrichloromethane + Dibromomethane, and Bromotrichloromethane + Bromochloromethane at Temperatures from (293.15 to 313.15) K
csound,fluid	1108.00	m/s	302.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	1109.45	m/s	302.98	Thermodynamic and Acoustic Properties of Mixtures of 1,6-Dichlorohexane with Heptane from (293 to 313) K
csound,fluid	1108.78	m/s	303.10	Excess molar heat capacities for (decan-1-ol + n-heptane) at temperatures from (290 to 318) K. Experimental results and theoretical description using the ERAS model
csound,fluid	1109.60	m/s	303.15	Excess Molar Volumes and Speed of Sound in Bromotrichloromethane + n-Heptane, Dibromomethane + n-Heptane, Bromotrichloromethane + Dibromomethane, and Bromotrichloromethane + Bromochloromethane at Temperatures from (293.15 to 313.15) K
csound,fluid	1109.10	m/s	303.15	Excess Molar Volumes and Speed of Sound in Bromotrichloromethane + n-Heptane, Dibromomethane + n-Heptane, Bromotrichloromethane + Dibromomethane, and Bromotrichloromethane + Bromochloromethane at Temperatures from (293.15 to 313.15) K
csound,fluid	1087.42	m/s	308.06	Thermodynamic and Acoustic Properties of Mixtures of 1,6-Dichlorohexane with Heptane from (293 to 313) K
csound,fluid	1087.47	m/s	308.07	Excess molar heat capacities for (decan-1-ol + n-heptane) at temperatures from (290 to 318) K. Experimental results and theoretical description using the ERAS model
csound,fluid	1088.20	m/s	308.15	Excess Molar Volumes and Speed of Sound in Bromotrichloromethane + n-Heptane, Dibromomethane + n-Heptane, Bromotrichloromethane + Dibromomethane, and Bromotrichloromethane + Bromochloromethane at Temperatures from (293.15 to 313.15) K
csound,fluid	1088.10	m/s	308.15	Excess Molar Volumes and Speed of Sound in Bromotrichloromethane + n-Heptane, Dibromomethane + n-Heptane, Bromotrichloromethane + Dibromomethane, and Bromotrichloromethane + Bromochloromethane at Temperatures from (293.15 to 313.15) K
csound,fluid	1066.28	m/s	313.03	Excess molar heat capacities for (decan-1-ol + n-heptane) at temperatures from (290 to 318) K. Experimental results and theoretical description using the ERAS model
csound,fluid	1067.10	m/s	313.15	Excess Molar Volumes and Speed of Sound in Bromotrichloromethane + n-Heptane, Dibromomethane + n-Heptane, Bromotrichloromethane + Dibromomethane, and Bromotrichloromethane + Bromochloromethane at Temperatures from (293.15 to 313.15) K
csound,fluid	1066.90	m/s	313.15	Excess Molar Volumes and Speed of Sound in Bromotrichloromethane + n-Heptane, Dibromomethane + n-Heptane, Bromotrichloromethane + Dibromomethane, and Bromotrichloromethane + Bromochloromethane at Temperatures from (293.15 to 313.15) K
csound,fluid	1064.29	m/s	313.45	Thermodynamic and Acoustic Properties of Mixtures of 1,6-Dichlorohexane with Heptane from (293 to 313) K
csound,fluid	1042.00	m/s	318.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	1043.90	m/s	318.33	Excess molar heat capacities for (decan-1-ol + n-heptane) at temperatures from (290 to 318) K. Experimental results and theoretical description using the ERAS model
csound,fluid	981.50	m/s	333.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	921.10	m/s	348.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	861.20	m/s	363.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	801.60	m/s	378.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	742.30	m/s	393.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	683.10	m/s	408.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	643.50	m/s	418.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	603.90	m/s	428.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	564.00	m/s	438.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	523.90	m/s	448.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	503.60	m/s	453.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	483.30	m/s	458.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	462.80	m/s	463.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	442.20	m/s	468.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	421.30	m/s	473.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	400.30	m/s	478.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	379.00	m/s	483.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	357.40	m/s	488.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	335.40	m/s	493.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	313.00	m/s	498.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	290.10	m/s	503.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	266.60	m/s	508.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	242.40	m/s	513.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	217.30	m/s	518.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	190.90	m/s	523.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	162.70	m/s	528.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	131.90	m/s	533.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	111.10	m/s	536.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
γ	[0.01; 0.02]	N/m	[277.93; 358.12]
γ	0.02	N/m	277.93	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.02	N/m	282.83	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.02	N/m	283.15	Experimental and theoretical study of surface tension of n-pentane, n-heptane, and some of their mixtures at different temperatures
γ	0.02	N/m	287.81	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.02	N/m	288.15	Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
γ	0.02	N/m	288.15	Interfacial Tensions of Imidazolium-Based Ionic Liquids with N-Alkanes and Cyclohexane
γ	0.02	N/m	292.81	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.02	N/m	293.15	Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ	0.02	N/m	293.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.02	N/m	293.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.02	N/m	293.15	Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
γ	0.02	N/m	293.15	Experimental and theoretical study of surface tension of n-pentane, n-heptane, and some of their mixtures at different temperatures
γ	0.02	N/m	293.20	KDB
γ	0.02	N/m	297.82	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.02	N/m	298.13	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.02	N/m	298.15	Interfacial Tensions of Imidazolium-Based Ionic Liquids with N-Alkanes and Cyclohexane
γ	0.02	N/m	298.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.02	N/m	298.15	Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ	0.02	N/m	298.15	NCMS SOLV-DB
γ	0.02	N/m	298.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.02	N/m	298.15	Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
γ	0.02	N/m	302.83	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.02	N/m	303.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.02	N/m	303.15	Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
γ	0.02	N/m	303.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.02	N/m	303.15	Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ	0.02	N/m	303.15	Experimental and theoretical study of surface tension of n-pentane, n-heptane, and some of their mixtures at different temperatures
γ	0.02	N/m	303.18	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.02	N/m	303.49	Surface Tension of 2,2-Dimethylbutane from (233 to 378) K
γ	0.02	N/m	307.86	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.02	N/m	308.12	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.02	N/m	308.15	Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ	0.02	N/m	308.15	Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
γ	0.02	N/m	308.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.02	N/m	308.15	Interfacial Tensions of Imidazolium-Based Ionic Liquids with N-Alkanes and Cyclohexane
γ	0.02	N/m	308.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.02	N/m	312.86	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.02	N/m	313.13	Surface Tension of 2,2-Dimethylbutane from (233 to 378) K
γ	0.02	N/m	313.15	Experimental and theoretical study of surface tension of n-pentane, n-heptane, and some of their mixtures at different temperatures
γ	0.02	N/m	313.15	Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ	0.02	N/m	313.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.02	N/m	313.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.02	N/m	313.18	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.02	N/m	317.86	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.02	N/m	318.15	Interfacial Tensions of Imidazolium-Based Ionic Liquids with N-Alkanes and Cyclohexane
γ	0.02	N/m	318.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.02	N/m	318.15	Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ	0.02	N/m	318.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.02	N/m	318.17	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.02	N/m	318.49	Surface Tension of 2,2-Dimethylbutane from (233 to 378) K
γ	0.02	N/m	322.86	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.02	N/m	323.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.02	N/m	323.15	Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ	0.02	N/m	323.15	Experimental and theoretical study of surface tension of n-pentane, n-heptane, and some of their mixtures at different temperatures
γ	0.02	N/m	323.15	Surface Tension of 2,2-Dimethylbutane from (233 to 378) K
γ	0.02	N/m	323.20	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.02	N/m	327.88	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.02	N/m	328.12	Surface Tension of 2,2-Dimethylbutane from (233 to 378) K
γ	0.02	N/m	328.15	Interfacial Tensions of Imidazolium-Based Ionic Liquids with N-Alkanes and Cyclohexane
γ	0.02	N/m	328.15	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.02	N/m	332.91	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.02	N/m	333.13	Surface Tension of 2,2-Dimethylbutane from (233 to 378) K
γ	0.02	N/m	337.88	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.02	N/m	338.14	Surface Tension of 2,2-Dimethylbutane from (233 to 378) K
γ	0.02	N/m	342.92	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.02	N/m	343.12	Surface Tension of 2,2-Dimethylbutane from (233 to 378) K
γ	0.01	N/m	348.13	Surface Tension of 2,2-Dimethylbutane from (233 to 378) K
γ	0.01	N/m	358.12	Surface Tension of 2,2-Dimethylbutane from (233 to 378) K

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil(P)	[308.91; 371.21]	K	[10.23; 100.11]
Tboil(P)	308.91	K	10.23	A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
Tboil(P)	320.43	K	16.91	A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
Tboil(P)	328.58	K	23.50	A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
Tboil(P)	339.42	K	35.39	A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
Tboil(P)	352.66	K	56.16	A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
Tboil(P)	358.24	K	67.57	A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
Tboil(P)	361.37	K	74.44	A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
Tboil(P)	363.45	K	79.37	A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
Tboil(P)	366.31	K	86.51	A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
Tboil(P)	371.21	K	100.11	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 (6)
3. Mass density, kg/m3 (13)
4. Speed of sound, m/s (2)
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
273.15	100.00	216.20
273.15	5000.00	213.10
273.15	10000.00	210.90
273.15	15000.00	208.10
273.15	20000.00	207.20
293.15	100.00	224.10
293.15	5000.00	223.00
293.15	10000.00	218.20
293.15	15000.00	216.80
293.15	20000.00	214.40
313.15	100.00	233.80
313.15	5000.00	230.30
313.15	10000.00	226.20
313.15	15000.00	223.10
313.15	20000.00	221.60
333.15	100.00	241.90
333.15	5000.00	238.70
333.15	10000.00	235.00
333.15	15000.00	232.00
333.15	20000.00	229.30
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.15	98.00	0.0004
298.15	24510.00	0.0005
298.15	49030.00	0.0006
298.15	98060.00	0.0008
298.15	147100.00	0.0011
298.15	196130.00	0.0015
298.15	245160.00	0.0019
303.15	98.00	0.0004
303.15	24510.00	0.0005
303.15	49030.00	0.0006
303.15	98060.00	0.0008
303.15	147100.00	0.0011
303.15	196130.00	0.0014
303.15	245160.00	0.0017
323.11	49030.00	0.0005
323.13	24510.00	0.0004
323.20	98060.00	0.0007
323.20	147100.00	0.0009
323.21	196130.00	0.0011
323.25	98.00	0.0003
323.25	245160.00	0.0014
362.80	147100.00	0.0006
362.83	98060.00	0.0005
362.85	49030.00	0.0004
362.87	196130.00	0.0008
362.92	98.00	0.0002
362.98	245160.00	0.0010
363.07	24510.00	0.0003
391.93	147100.00	0.0005
392.00	196130.00	0.0007
392.00	245160.00	0.0008
392.04	98060.00	0.0004
393.01	24510.00	0.0002
393.14	49030.00	0.0003
422.17	196130.00	0.0006
422.24	98060.00	0.0003
422.26	147100.00	0.0004
422.58	24510.00	0.0002
422.60	49030.00	0.0002
423.04	245160.00	0.0007
452.91	245160.00	0.0006
453.04	196130.00	0.0005
453.10	147100.00	0.0004
453.16	98060.00	0.0003
453.24	49030.00	0.0002
453.40	24510.00	0.0002
470.10	49030.00	0.0002
470.19	24510.00	0.0002
470.19	98060.00	0.0003
470.19	147100.00	0.0004
470.57	196130.00	0.0005
470.61	245160.00	0.0005
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
293.15	20000.00	0.0005
293.15	40000.00	0.0006
293.15	60000.00	0.0007
293.15	80000.00	0.0008
293.15	100000.00	0.0009
313.15	20000.00	0.0004
313.15	40000.00	0.0005
313.15	60000.00	0.0006
313.15	80000.00	0.0007
313.15	100000.00	0.0008
333.15	20000.00	0.0003
333.15	40000.00	0.0004
333.15	60000.00	0.0005
333.15	80000.00	0.0005
333.15	100000.00	0.0006
353.15	20000.00	0.0003
353.15	40000.00	0.0003
353.15	60000.00	0.0004
353.15	80000.00	0.0005
353.15	100000.00	0.0005
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.15	101.33	0.0004
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.24	100.00	0.0004
306.79	5000.00	0.0004
306.79	10000.00	0.0004
323.93	100.00	0.0003
337.54	5000.00	0.0003
337.54	10000.00	0.0003
348.64	100.00	0.0002
369.35	5000.00	0.0002
369.35	10000.00	0.0002
407.85	5000.00	0.0002
407.85	10000.00	0.0002
449.64	5000.00	0.0001
449.64	10000.00	0.0001
473.54	5000.00	0.0001
473.54	10000.00	0.0001
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
293.15	5000.00	0.0004
293.15	10000.00	0.0005
293.15	20000.00	0.0005
293.15	30000.00	0.0006
293.15	40000.00	0.0006
293.15	60000.00	0.0007
293.15	80000.00	0.0008
293.15	100000.00	0.0009
293.15	120000.00	0.0010
313.15	5000.00	0.0004
313.15	10000.00	0.0004
313.15	20000.00	0.0004
313.15	30000.00	0.0005
313.15	40000.00	0.0005
313.15	60000.00	0.0006
313.15	80000.00	0.0006
313.15	100000.00	0.0007
313.15	120000.00	0.0008
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.15	100.00	0.0004
303.15	1000.00	0.0004
303.15	5000.00	0.0004
303.15	10000.00	0.0004
303.15	15000.00	0.0004
303.15	20000.00	0.0004
303.15	25000.00	0.0005
303.15	30000.00	0.0005
303.15	35000.00	0.0005
303.15	40000.00	0.0005
303.15	45000.00	0.0006
303.15	50000.00	0.0006
303.15	55000.00	0.0006
303.15	60000.00	0.0006
313.15	100.00	0.0003
313.15	1000.00	0.0003
313.15	5000.00	0.0003
313.15	10000.00	0.0004
313.15	15000.00	0.0004
313.15	20000.00	0.0004
313.15	25000.00	0.0004
313.15	30000.00	0.0004
313.15	35000.00	0.0005
313.15	40000.00	0.0005
313.15	45000.00	0.0005
313.15	50000.00	0.0005
313.15	55000.00	0.0005
313.15	60000.00	0.0006
323.15	100.00	0.0003
323.15	1000.00	0.0003
323.15	5000.00	0.0003
323.15	10000.00	0.0003
323.15	15000.00	0.0004
323.15	20000.00	0.0004
323.15	25000.00	0.0004
323.15	30000.00	0.0004
323.15	35000.00	0.0004
323.15	40000.00	0.0004
323.15	45000.00	0.0005
323.15	50000.00	0.0005
323.15	55000.00	0.0005
323.15	60000.00	0.0005
333.15	100.00	0.0003
333.15	1000.00	0.0003
333.15	5000.00	0.0003
333.15	10000.00	0.0003
333.15	15000.00	0.0003
333.15	20000.00	0.0003
333.15	25000.00	0.0004
333.15	30000.00	0.0004
333.15	35000.00	0.0004
333.15	40000.00	0.0004
333.15	45000.00	0.0004
333.15	50000.00	0.0004
333.15	55000.00	0.0005
333.15	60000.00	0.0005
343.15	100.00	0.0002
343.15	1000.00	0.0002
343.15	5000.00	0.0003
343.15	10000.00	0.0003
343.15	15000.00	0.0003
343.15	20000.00	0.0003
343.15	25000.00	0.0003
343.15	30000.00	0.0003
343.15	35000.00	0.0004
343.15	40000.00	0.0004
343.15	45000.00	0.0004
343.15	50000.00	0.0004
343.15	55000.00	0.0004
343.15	60000.00	0.0004
353.15	100.00	0.0002
353.15	1000.00	0.0002
353.15	5000.00	0.0002
353.15	10000.00	0.0003
353.15	15000.00	0.0003
353.15	20000.00	0.0003
353.15	25000.00	0.0003
353.15	30000.00	0.0003
353.15	35000.00	0.0003
353.15	40000.00	0.0003
353.15	45000.00	0.0004
353.15	50000.00	0.0004
353.15	55000.00	0.0004
353.15	60000.00	0.0004
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.00	2100.00	687.2
293.00	3000.00	688.1
293.00	4000.00	688.9
293.00	5000.00	689.8
293.00	10000.00	694.0
293.00	20000.00	701.8
293.00	30000.00	708.7
293.00	40000.00	714.8
293.00	49900.00	720.8
293.00	59900.00	726.4
293.00	69900.00	731.6
293.00	79900.00	736.8
293.00	89900.00	741.5
293.00	99900.00	746.1
293.00	109900.00	750.6
293.00	119900.00	754.9
293.00	129900.00	759.2
293.00	134900.00	761.2
293.00	137400.00	762.2
313.00	2100.00	671.9
313.00	3000.00	672.9
313.00	4000.00	673.9
313.00	5000.00	674.8
313.00	10000.00	679.4
313.00	20000.00	688.0
313.00	30000.00	695.4
313.00	40000.00	702.2
313.00	49900.00	708.5
313.00	59900.00	714.3
313.00	69900.00	720.0
313.00	79900.00	725.2
313.00	89900.00	730.3
313.00	99900.00	735.1
313.00	109900.00	739.9
313.00	119900.00	744.3
313.00	129900.00	748.7
313.00	134900.00	751.0
313.00	137400.00	751.9
333.00	2100.00	654.8
333.00	3000.00	656.0
333.00	4000.00	657.7
333.00	5000.00	658.4
333.00	10000.00	663.9
333.00	20000.00	673.8
333.00	30000.00	682.3
333.00	40000.00	689.5
333.00	49900.00	696.5
333.00	59900.00	703.1
333.00	69900.00	708.9
333.00	79900.00	714.5
333.00	89900.00	720.0
333.00	99900.00	725.2
333.00	109900.00	729.8
333.00	119900.00	734.7
333.00	129900.00	739.3
333.00	134900.00	741.4
333.00	137400.00	742.6
353.00	2100.00	636.1
353.00	3000.00	637.6
353.00	4000.00	639.1
353.00	5000.00	640.4
353.00	10000.00	647.1
353.00	20000.00	658.5
353.00	30000.00	668.0
353.00	40000.00	676.7
353.00	49900.00	684.5
353.00	59900.00	691.3
353.00	69900.00	697.9
353.00	79900.00	703.8
353.00	89900.00	709.7
353.00	99900.00	715.0
353.00	109900.00	720.3
353.00	119900.00	725.3
353.00	129900.00	730.1
353.00	134900.00	732.4
353.00	137400.00	733.5
373.00	2100.00	616.9
373.00	3000.00	618.6
373.00	4000.00	620.3
373.00	5000.00	622.0
373.00	10000.00	629.9
373.00	20000.00	643.2
373.00	30000.00	654.1
373.00	40000.00	663.6
373.00	49900.00	672.0
373.00	59900.00	679.6
373.00	69900.00	686.7
373.00	79900.00	693.3
373.00	89900.00	699.4
373.00	99900.00	705.2
373.00	109900.00	710.7
373.00	119900.00	716.0
373.00	129900.00	720.9
373.00	134900.00	723.3
373.00	137400.00	724.5
393.00	2100.00	596.5
393.00	3000.00	598.7
393.00	4000.00	600.8
393.00	5000.00	602.8
393.00	10000.00	612.2
393.00	20000.00	627.8
393.00	30000.00	640.2
393.00	40000.00	650.8
393.00	49900.00	659.9
393.00	59900.00	668.3
393.00	69900.00	675.9
393.00	79900.00	682.9
393.00	89900.00	689.5
393.00	99900.00	695.7
393.00	109900.00	701.4
393.00	119900.00	706.8
393.00	129900.00	712.1
393.00	134900.00	714.7
393.00	137400.00	715.8
413.00	2100.00	574.1
413.00	3000.00	577.0
413.00	4000.00	579.6
413.00	5000.00	582.1
413.00	10000.00	593.6
413.00	20000.00	611.9
413.00	30000.00	626.0
413.00	40000.00	637.6
413.00	49900.00	647.8
413.00	59900.00	656.9
413.00	69900.00	664.7
413.00	79900.00	672.4
413.00	89900.00	679.3
413.00	99900.00	685.8
413.00	109900.00	692.2
413.00	119900.00	698.0
413.00	129900.00	703.6
413.00	134900.00	706.2
413.00	137400.00	707.4
433.00	2100.00	550.1
433.00	3000.00	553.9
433.00	4000.00	557.5
433.00	5000.00	560.7
433.00	10000.00	574.6
433.00	20000.00	595.4
433.00	30000.00	611.5
433.00	40000.00	624.3
433.00	49900.00	635.2
433.00	59900.00	644.7
433.00	69900.00	653.5
433.00	79900.00	661.6
433.00	89900.00	669.0
433.00	99900.00	676.0
433.00	109900.00	682.3
433.00	119900.00	688.5
433.00	129900.00	694.3
433.00	134900.00	697.2
433.00	137400.00	698.6
448.00	2100.00	531.1
448.00	3000.00	535.6
448.00	4000.00	539.8
448.00	5000.00	543.6
448.00	10000.00	560.0
448.00	20000.00	583.0
448.00	30000.00	600.3
448.00	40000.00	614.4
448.00	49900.00	626.2
448.00	59900.00	636.6
448.00	69900.00	646.2
448.00	79900.00	654.4
448.00	89900.00	661.8
448.00	99900.00	669.2
448.00	109900.00	675.8
448.00	119900.00	682.3
448.00	129900.00	688.4
448.00	134900.00	691.4
448.00	137400.00	692.6
468.00	2100.00	501.1
468.00	3000.00	507.8
468.00	4000.00	513.4
468.00	5000.00	518.6
468.00	10000.00	539.1
468.00	20000.00	566.5
468.00	30000.00	586.2
468.00	40000.00	601.3
468.00	49900.00	614.2
468.00	59900.00	625.3
468.00	69900.00	635.2
468.00	79900.00	644.1
468.00	89900.00	652.3
468.00	99900.00	659.9
468.00	109900.00	667.2
468.00	119900.00	673.9
468.00	129900.00	679.9
468.00	134900.00	682.8
468.00	137400.00	684.3
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
233.15	101.68	733.289
233.15	1104.14	733.918
233.15	2003.32	734.481
233.15	4006.02	735.714
233.15	6004.84	736.928
233.15	8009.54	738.125
233.15	9956.83	739.277
233.15	11864.20	740.377
233.15	13984.20	741.588
233.15	15994.70	742.722
233.15	17888.30	743.774
233.15	20074.10	744.977
233.15	22023.80	746.029
233.15	24017.60	747.094
233.15	25954.00	748.113
233.15	27944.50	749.147
233.15	29979.30	750.192
253.15	98.99	717.086
253.15	1101.50	717.807
253.15	2000.52	718.446
253.15	4006.34	719.85
253.15	6005.44	721.223
253.15	8147.76	722.669
253.15	10096.20	723.959
253.15	11827.30	725.088
253.15	13955.10	726.459
253.15	16060.20	727.785
253.15	18039.50	729.014
253.15	20020.00	730.22
253.15	22093.30	731.465
253.15	23827.70	732.495
253.15	25891.20	733.701
253.15	27738.70	734.762
253.15	29899.80	735.987
273.15	102.15	700.687
273.15	1101.26	701.507
273.15	2006.30	702.244
273.15	4005.43	703.841
273.15	6005.46	705.403
273.15	8197.47	707.077
273.15	10109.30	708.507
273.15	12113.70	709.976
273.15	14092.30	711.403
273.15	16115.70	712.831
273.15	18076.00	714.19
273.15	20096.30	715.565
273.15	22068.90	716.883
273.15	24101.50	718.226
273.15	25917.60	719.397
273.15	27991.30	720.718
273.15	29444.50	721.633
293.15	98.89	683.986
293.15	1104.28	684.937
293.15	2003.35	685.779
293.15	4003.02	687.611
293.15	6003.71	689.394
293.15	8007.44	691.14
293.15	10027.90	692.854
293.15	12138.70	694.603
293.15	14007.80	696.118
293.15	16160.30	697.827
293.15	18149.30	699.368
293.15	19992.10	700.756
293.15	22123.00	702.362
293.15	24036.20	703.766
293.15	25999.00	705.175
293.15	27982.80	706.576
293.15	29985.70	707.965
313.15	101.45	666.898
313.15	1102.20	667.995
313.15	2005.49	668.973
313.15	4004.53	671.086
313.15	6106.94	673.238
313.15	7941.18	675.062
313.15	9944.39	676.997
313.15	11841.20	678.793
313.15	13782.40	680.575
313.15	16032.40	682.588
313.15	17876.00	684.2
313.15	19748.40	685.804
313.15	21802.90	687.518
313.15	23828.70	689.172
313.15	25813.90	690.765
313.15	27801.40	692.324
313.15	29818.40	693.872
333.15	103.00	649.298
333.15	1105.97	650.588
333.15	2004.12	651.723
333.15	4003.59	654.18
333.15	6004.59	656.549
333.15	8005.55	658.837
333.15	9901.48	660.933
333.15	12083.40	663.274
333.15	14040.10	665.309
333.15	16005.20	667.293
333.15	17854.30	669.109
333.15	19984.70	671.149
333.15	21966.60	672.997
333.15	23925.50	674.778
333.15	25823.40	676.467
333.15	27822.80	678.205
333.15	30009.20	680.058
353.15	99.37	631.037
353.15	1182.85	632.68
353.15	2156.26	634.131
353.15	4140.73	636.982
353.15	6175.55	639.78
353.15	8138.91	642.37
353.15	10095.00	644.851
353.15	12083.30	647.284
353.15	14039.80	649.596
353.15	16039.20	651.883
353.15	18008.20	654.064
353.15	19996.30	656.201
353.15	21955.50	658.247
353.15	23925.40	660.247
353.15	25887.20	662.188
353.15	27855.00	664.084
353.15	29976.00	666.077
373.15	1164.33	613.877
373.15	2149.21	615.631
373.15	4123.49	618.999
373.15	5987.02	622.014
373.15	8094.82	625.262
373.15	10059.80	628.151
373.15	12066.30	630.972
373.15	14017.80	633.61
373.15	16044.40	636.241
373.15	18058.00	638.765
373.15	19975.60	641.085
373.15	21959.60	643.408
373.15	23948.00	645.665
373.15	25804.80	647.712
373.15	27898.40	649.952
373.15	29818.70	651.952
393.15	1101.93	593.952
393.15	2001.51	595.905
393.15	4002.83	600.027
393.15	6004.29	603.884
393.15	8005.48	607.511
393.15	10007.10	610.942
393.15	12110.90	614.361
393.15	14116.50	617.466
393.15	16097.20	620.399
393.15	18029.00	623.142
393.15	20054.00	625.904
393.15	22015.90	628.483
393.15	24005.50	631.008
393.15	25986.10	633.434
393.15	27951.60	635.769
393.15	29842.80	638.037
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.18	1000.00	668.09
313.18	2000.00	669.03
313.18	3000.00	669.97
313.18	4000.00	670.93
313.18	5010.00	671.9
313.18	6000.00	672.87
313.18	7000.00	673.86
313.18	8000.00	674.87
313.18	9000.00	675.87
313.18	10000.00	676.86
313.18	11000.00	677.85
313.18	12000.00	678.83
313.18	13000.00	679.81
313.18	14000.00	680.76
313.18	15000.00	681.7
313.18	16000.00	682.62
313.18	17000.00	683.53
313.18	18000.00	684.41
313.18	19000.00	685.26
313.18	20000.00	686.11
313.18	21000.00	686.92
313.18	22000.00	687.67
313.18	23000.00	688.42
313.18	23910.00	689.07
313.18	25000.00	689.85
333.04	1000.00	650.66
333.04	2000.00	651.8
333.04	3000.00	652.94
333.04	4000.00	654.08
333.04	5000.00	655.23
333.04	6000.00	656.38
333.04	7000.00	657.54
333.04	8000.00	658.65
333.04	9000.00	659.81
333.04	10000.00	660.92
333.04	11000.00	662.03
333.04	12000.00	663.1
333.04	13000.00	664.2
333.04	14000.00	665.25
333.04	15000.00	666.31
333.04	16000.00	667.33
333.04	17000.00	668.33
333.04	18030.00	669.34
333.04	19000.00	670.26
333.04	20000.00	671.2
333.04	22000.00	673.01
333.04	23000.00	673.86
333.04	24000.00	674.7
333.04	25000.00	675.52
333.04	23000.00	673.86
353.06	1010.00	632.6
353.06	2000.00	634.02
353.06	3000.00	635.41
353.06	4000.00	636.78
353.06	5000.00	638.15
353.06	6000.00	639.47
353.06	7000.00	640.8
353.06	8000.00	642.1
353.06	9010.00	643.4
353.06	10000.00	644.66
353.06	11000.00	645.92
353.06	12000.00	647.13
353.06	13000.00	648.37
353.06	14000.00	649.56
353.06	15000.00	650.72
353.06	16000.00	651.88
353.06	17000.00	653.0
353.06	18030.00	654.12
353.06	19000.00	655.16
353.06	20000.00	656.22
353.06	21000.00	657.27
353.06	22000.00	658.25
353.06	23000.00	659.24
353.06	24000.00	660.2
353.06	25000.00	661.14
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	679.5
298.15	1000.00	680.4
298.15	5000.00	684.2
298.15	10000.00	688.6
298.15	15000.00	692.8
298.15	20000.00	696.7
298.15	25000.00	700.4
298.15	30000.00	704.0
298.15	35000.00	707.4
298.15	40000.00	710.7
298.15	45000.00	713.8
298.15	50000.00	716.8
298.15	55000.00	719.7
298.15	60000.00	722.5
298.15	65000.00	725.2
298.15	70000.00	727.9
298.15	80000.00	732.9
298.15	90000.00	737.7
298.15	100000.00	742.3
298.15	110000.00	746.6
298.15	120000.00	750.7
298.15	130000.00	754.6
298.15	140000.00	758.4
313.15	100.00	666.6
313.15	1000.00	667.6
313.15	5000.00	671.8
313.15	10000.00	676.7
313.15	15000.00	681.3
313.15	20000.00	685.6
313.15	25000.00	689.5
313.15	30000.00	693.5
313.15	35000.00	697.1
313.15	40000.00	700.5
313.15	45000.00	703.9
313.15	50000.00	707.2
313.15	55000.00	710.3
313.15	60000.00	713.3
313.15	65000.00	716.1
313.15	70000.00	718.9
313.15	80000.00	724.2
313.15	90000.00	729.3
313.15	100000.00	734.0
313.15	110000.00	738.6
313.15	120000.00	742.8
313.15	130000.00	747.0
313.15	140000.00	751.1
333.15	100.00	648.9
333.15	1000.00	650.0
333.15	5000.00	655.0
333.15	10000.00	660.6
333.15	15000.00	665.8
333.15	20000.00	670.6
333.15	25000.00	675.1
333.15	30000.00	679.4
333.15	35000.00	683.4
333.15	40000.00	687.3
333.15	45000.00	690.9
333.15	50000.00	694.4
333.15	55000.00	697.7
333.15	60000.00	701.0
333.15	65000.00	704.1
333.15	70000.00	707.1
333.15	80000.00	712.8
333.15	90000.00	718.2
333.15	100000.00	723.2
333.15	110000.00	728.1
333.15	120000.00	732.6
333.15	130000.00	737.0
333.15	140000.00	741.1
353.15	100.00	631.2
353.15	1000.00	632.1
353.15	5000.00	637.8
353.15	10000.00	644.3
353.15	15000.00	650.3
353.15	20000.00	655.7
353.15	25000.00	660.8
353.15	30000.00	665.5
353.15	35000.00	670.0
353.15	40000.00	674.1
353.15	45000.00	678.1
353.15	50000.00	682.0
353.15	55000.00	685.5
353.15	60000.00	689.1
353.15	65000.00	692.4
353.15	70000.00	695.7
353.15	80000.00	701.7
353.15	90000.00	707.5
353.15	100000.00	712.8
353.15	110000.00	717.9
353.15	120000.00	722.7
353.15	130000.00	727.3
353.15	140000.00	731.6
373.15	1000.00	613.3
373.15	5000.00	620.1
373.15	10000.00	627.7
373.15	15000.00	634.5
373.15	20000.00	640.7
373.15	25000.00	646.3
373.15	30000.00	651.6
373.15	35000.00	656.5
373.15	40000.00	661.1
373.15	45000.00	665.5
373.15	50000.00	669.6
373.15	55000.00	673.5
373.15	60000.00	677.3
373.15	65000.00	680.8
373.15	70000.00	684.3
373.15	80000.00	690.8
373.15	90000.00	696.9
373.15	100000.00	702.6
373.15	110000.00	708.0
373.15	120000.00	713.0
373.15	130000.00	717.9
373.15	140000.00	722.3
393.15	1000.00	593.5
393.15	5000.00	601.7
393.15	10000.00	610.6
393.15	15000.00	618.4
393.15	20000.00	625.4
393.15	25000.00	631.7
393.15	30000.00	637.5
393.15	35000.00	643.0
393.15	40000.00	648.0
393.15	45000.00	652.8
393.15	50000.00	657.2
393.15	55000.00	661.5
393.15	60000.00	665.5
393.15	65000.00	669.3
393.15	70000.00	673.1
393.15	80000.00	680.1
393.15	90000.00	686.5
393.15	100000.00	692.5
393.15	110000.00	698.2
393.15	120000.00	703.4
393.15	130000.00	708.5
393.15	140000.00	713.4
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
288.15	101.00	688.33
293.15	101.00	684.11
298.15	101.00	679.87
303.15	101.00	675.6
308.15	101.00	671.31
313.15	101.00	667.0
288.15	100.00	688.4
288.15	1000.00	689.2
288.15	5000.00	692.5
288.15	10000.00	696.5
288.15	15000.00	700.4
288.15	20000.00	704.1
288.15	25000.00	707.7
288.15	30000.00	711.1
288.15	35000.00	714.3
288.15	40000.00	717.4
288.15	45000.00	720.3
288.15	50000.00	723.1
288.15	55000.00	725.8
288.15	60000.00	728.2
293.15	100.00	684.2
293.15	1000.00	685.0
293.15	5000.00	688.4
293.15	10000.00	692.6
293.15	15000.00	696.5
293.15	20000.00	700.4
293.15	25000.00	704.0
293.15	30000.00	707.5
293.15	35000.00	710.9
293.15	40000.00	714.0
293.15	45000.00	717.0
293.15	50000.00	719.9
293.15	55000.00	722.5
293.15	60000.00	725.1
298.15	100.00	679.9
298.15	1000.00	680.7
298.15	5000.00	684.3
298.15	10000.00	688.6
298.15	15000.00	692.7
298.15	20000.00	696.6
298.15	25000.00	700.4
298.15	30000.00	704.0
298.15	35000.00	707.4
298.15	40000.00	710.7
298.15	45000.00	713.8
298.15	50000.00	716.7
298.15	55000.00	719.4
298.15	60000.00	721.9
303.15	100.00	675.7
303.15	1000.00	676.5
303.15	5000.00	680.2
303.15	10000.00	684.6
303.15	15000.00	688.9
303.15	20000.00	693.0
303.15	25000.00	696.8
303.15	30000.00	700.5
303.15	35000.00	704.0
303.15	40000.00	707.4
303.15	45000.00	710.5
303.15	50000.00	713.5
303.15	55000.00	716.2
303.15	60000.00	718.8
308.15	100.00	671.4
308.15	1000.00	672.2
308.15	5000.00	676.0
308.15	10000.00	680.6
308.15	15000.00	685.0
308.15	20000.00	689.2
308.15	25000.00	693.2
308.15	30000.00	697.0
308.15	35000.00	700.6
308.15	40000.00	704.0
308.15	45000.00	707.2
308.15	50000.00	710.3
308.15	55000.00	713.1
308.15	60000.00	715.7
313.15	100.00	667.1
313.15	1000.00	668.0
313.15	5000.00	672.0
313.15	10000.00	676.7
313.15	15000.00	681.2
313.15	20000.00	685.5
313.15	25000.00	689.6
313.15	30000.00	693.5
313.15	35000.00	697.2
313.15	40000.00	700.7
313.15	45000.00	704.0
313.15	50000.00	707.1
313.15	55000.00	709.9
313.15	60000.00	712.6
318.15	100.00	662.7
318.15	1000.00	663.6
318.15	5000.00	667.7
318.15	10000.00	672.6
318.15	15000.00	677.3
318.15	20000.00	681.8
318.15	25000.00	686.0
318.15	30000.00	690.0
318.15	35000.00	693.8
318.15	40000.00	697.4
318.15	45000.00	700.7
318.15	50000.00	703.9
318.15	55000.00	706.8
318.15	60000.00	709.5
323.15	100.00	658.3
323.15	1000.00	659.3
323.15	5000.00	663.5
323.15	10000.00	668.6
323.15	15000.00	673.4
323.15	20000.00	678.0
323.15	25000.00	682.4
323.15	30000.00	686.5
323.15	35000.00	690.4
323.15	40000.00	694.1
323.15	45000.00	697.5
323.15	50000.00	700.7
323.15	55000.00	703.7
323.15	60000.00	706.4
328.15	100.00	653.9
328.15	1000.00	654.9
328.15	5000.00	659.3
328.15	10000.00	664.5
328.15	15000.00	669.5
328.15	20000.00	674.3
328.15	25000.00	678.8
328.15	30000.00	683.0
328.15	35000.00	687.0
328.15	40000.00	690.8
328.15	45000.00	694.3
328.15	50000.00	697.6
328.15	55000.00	700.6
328.15	60000.00	703.3
333.15	100.00	649.5
333.15	1000.00	650.6
333.15	5000.00	655.1
333.15	10000.00	660.5
333.15	15000.00	665.7
333.15	20000.00	670.6
333.15	25000.00	675.2
333.15	30000.00	679.6
333.15	35000.00	683.7
333.15	40000.00	687.5
333.15	45000.00	691.1
333.15	50000.00	694.4
333.15	55000.00	697.4
333.15	60000.00	700.2
343.15	100.00	640.5
343.15	1000.00	641.6
343.15	5000.00	646.5
343.15	10000.00	652.3
343.15	15000.00	657.8
343.15	20000.00	663.1
343.15	25000.00	668.0
343.15	30000.00	672.6
343.15	35000.00	676.9
343.15	40000.00	681.0
343.15	45000.00	684.7
343.15	50000.00	688.1
343.15	55000.00	691.3
343.15	60000.00	694.1
353.15	100.00	631.3
353.15	1000.00	632.5
353.15	5000.00	637.8
353.15	10000.00	644.0
353.15	15000.00	649.9
353.15	20000.00	655.5
353.15	25000.00	660.7
353.15	30000.00	665.6
353.15	35000.00	670.2
353.15	40000.00	674.4
353.15	45000.00	678.3
353.15	50000.00	681.9
353.15	55000.00	685.1
353.15	60000.00	688.0
363.15	100.00	621.9
363.15	1000.00	623.2
363.15	5000.00	628.9
363.15	10000.00	635.6
363.15	15000.00	641.9
363.15	20000.00	647.9
363.15	25000.00	653.4
363.15	30000.00	658.6
363.15	35000.00	663.5
363.15	40000.00	667.9
363.15	45000.00	672.0
363.15	50000.00	675.7
363.15	55000.00	679.0
363.15	60000.00	681.9
373.15	1000.00	614.2
373.15	5000.00	620.2
373.15	10000.00	627.4
373.15	15000.00	634.1
373.15	20000.00	640.4
373.15	25000.00	646.3
373.15	30000.00	651.8
373.15	35000.00	656.9
373.15	40000.00	661.5
373.15	45000.00	665.8
373.15	50000.00	669.6
373.15	55000.00	673.1
373.15	60000.00	676.1
393.15	1000.00	594.6
393.15	5000.00	601.7
393.15	10000.00	610.0
393.15	15000.00	617.8
393.15	20000.00	625.0
393.15	25000.00	631.7
393.15	30000.00	637.9
393.15	35000.00	643.6
393.15	40000.00	648.7
393.15	45000.00	653.3
393.15	50000.00	657.4
393.15	55000.00	660.9
393.15	60000.00	663.9
413.15	1000.00	574.1
413.15	5000.00	582.3
413.15	10000.00	592.0
413.15	15000.00	600.9
413.15	20000.00	609.2
413.15	25000.00	616.9
413.15	30000.00	623.9
413.15	35000.00	630.2
413.15	40000.00	635.9
413.15	45000.00	640.9
413.15	50000.00	645.2
413.15	55000.00	648.9
413.15	60000.00	651.9
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	298.15	679.71
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	692.57
288.15	100.00	688.55
293.15	100.00	684.19
298.15	100.00	679.95
303.15	100.00	675.68
308.15	100.00	671.39
313.15	100.00	667.06
318.15	100.00	662.54
323.15	100.00	658.32
328.15	100.00	653.81
283.15	2000.00	694.49
288.15	2000.00	690.28
293.15	2000.00	686.15
298.15	2000.00	682.02
303.15	2000.00	677.75
308.15	2000.00	673.45
313.15	2000.00	669.26
318.15	2000.00	664.87
323.15	2000.00	660.53
328.15	2000.00	656.27
283.15	5000.00	697.06
288.15	5000.00	693.01
293.15	5000.00	688.99
298.15	5000.00	684.8
303.15	5000.00	680.76
308.15	5000.00	676.49
313.15	5000.00	672.35
318.15	5000.00	668.35
323.15	5000.00	664.05
328.15	5000.00	659.84
283.15	7000.00	698.8
288.15	7000.00	694.77
293.15	7000.00	690.74
298.15	7000.00	686.68
303.15	7000.00	682.65
308.15	7000.00	678.48
313.15	7000.00	674.51
318.15	7000.00	670.32
323.15	7000.00	666.33
328.15	7000.00	661.99
283.15	10000.00	701.2
288.15	10000.00	697.23
293.15	10000.00	693.41
298.15	10000.00	689.23
303.15	10000.00	685.52
308.15	10000.00	681.37
313.15	10000.00	677.42
318.15	10000.00	673.52
323.15	10000.00	669.41
328.15	10000.00	665.25
283.15	20000.00	709.08
288.15	20000.00	705.18
293.15	20000.00	701.57
298.15	20000.00	697.65
303.15	20000.00	694.07
308.15	20000.00	690.12
313.15	20000.00	686.53
318.15	20000.00	682.85
323.15	20000.00	679.17
328.15	20000.00	675.25
283.15	30000.00	716.12
288.15	30000.00	712.38
293.15	30000.00	708.99
298.15	30000.00	705.17
303.15	30000.00	701.86
308.15	30000.00	698.22
313.15	30000.00	694.65
318.15	30000.00	691.31
323.15	30000.00	687.64
328.15	30000.00	684.02
283.15	40000.00	722.63
288.15	40000.00	719.01
293.15	40000.00	715.7
298.15	40000.00	712.11
303.15	40000.00	708.87
308.15	40000.00	705.32
313.15	40000.00	702.08
318.15	40000.00	698.89
323.15	40000.00	695.38
328.15	40000.00	691.84
283.15	50000.00	728.63
288.15	50000.00	725.2
293.15	50000.00	722.03
298.15	50000.00	718.54
303.15	50000.00	715.5
308.15	50000.00	712.12
313.15	50000.00	708.98
318.15	50000.00	705.82
323.15	50000.00	702.5
328.15	50000.00	699.13
283.15	60000.00	734.33
288.15	60000.00	731.01
293.15	60000.00	728.02
298.15	60000.00	724.73
303.15	60000.00	721.67
308.15	60000.00	718.41
313.15	60000.00	715.39
318.15	60000.00	712.36
323.15	60000.00	709.15
328.15	60000.00	706.05
283.15	65000.00	736.99
288.15	65000.00	733.73
293.15	65000.00	730.72
298.15	65000.00	727.65
303.15	65000.00	724.56
308.15	65000.00	721.43
313.15	65000.00	718.32
318.15	65000.00	715.32
323.15	65000.00	712.32
328.15	65000.00	709.3
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	680.0
298.15	3000.00	683.0
298.15	6000.00	686.0
298.15	9000.00	689.0
298.15	12000.00	691.0
298.15	15000.00	694.0
308.15	100.00	670.0
308.15	3000.00	674.0
308.15	6000.00	677.0
308.15	9000.00	680.0
308.15	12000.00	683.0
308.15	15000.00	685.0
318.15	100.00	662.0
318.15	3000.00	666.0
318.15	6000.00	669.0
318.15	9000.00	672.0
318.15	12000.00	675.0
318.15	15000.00	678.0
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.25	2103.00	685.58
293.25	3666.00	687.27
293.25	6195.00	689.52
293.25	10385.00	693.22
293.25	14421.00	696.48
293.25	17447.00	698.88
293.25	20472.00	701.01
293.25	23543.00	703.3
293.25	26611.00	705.5
313.08	2050.00	669.15
313.08	4083.00	671.15
313.08	6733.00	673.77
313.07	11204.00	678.28
313.08	14195.00	681.03
313.07	17225.00	683.61
313.07	20247.00	686.13
313.08	23266.00	688.54
313.08	26286.00	691.26
313.07	29805.00	693.98
332.78	2084.00	652.25
332.77	4091.00	654.57
332.78	7031.00	658.26
332.78	11151.00	662.67
332.78	14177.00	665.56
332.78	17172.00	668.79
332.78	20193.00	671.47
332.78	23214.00	674.57
332.78	26231.00	677.28
352.39	2184.00	635.33
352.39	4102.00	637.96
352.40	7146.00	641.83
352.39	11159.00	646.85
352.39	14169.00	650.4
352.39	17199.00	653.84
352.40	20204.00	657.05
352.40	23212.00	660.04
352.40	26228.00	663.06
352.39	29758.00	666.6
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	278.15	696.3
100.00	283.15	692.1
100.00	293.15	683.7
100.00	303.15	675.3
100.00	313.15	666.6
100.00	323.15	657.6
100.00	333.15	648.9
100.00	343.15	639.8
100.00	353.15	630.6
1000.00	278.15	697.0
1000.00	283.15	692.9
1000.00	293.15	684.6
1000.00	303.15	676.2
1000.00	313.15	667.6
1000.00	323.15	658.7
1000.00	333.15	650.0
1000.00	343.15	641.1
1000.00	353.15	632.0
2500.00	278.15	698.3
2500.00	283.15	694.2
2500.00	293.15	685.9
2500.00	303.15	677.7
2500.00	313.15	669.1
2500.00	323.15	660.4
2500.00	333.15	651.8
2500.00	343.15	643.1
2500.00	353.15	634.2
5000.00	278.15	700.3
5000.00	283.15	696.3
5000.00	293.15	688.2
5000.00	303.15	680.1
5000.00	313.15	671.7
5000.00	323.15	663.1
5000.00	333.15	654.8
5000.00	343.15	646.3
5000.00	353.15	637.8
7500.00	278.15	702.3
7500.00	283.15	698.3
7500.00	293.15	690.4
7500.00	303.15	682.4
7500.00	313.15	674.2
7500.00	323.15	665.8
7500.00	333.15	657.6
7500.00	343.15	649.4
7500.00	353.15	641.1
10000.00	278.15	704.2
10000.00	283.15	700.2
10000.00	293.15	692.5
10000.00	303.15	684.7
10000.00	313.15	676.6
10000.00	323.15	668.4
10000.00	333.15	660.4
10000.00	343.15	652.4
10000.00	353.15	644.3
15000.00	278.15	707.9
15000.00	283.15	704.0
15000.00	293.15	696.6
15000.00	303.15	689.0
15000.00	313.15	681.2
15000.00	323.15	673.3
15000.00	333.15	665.6
15000.00	343.15	658.0
15000.00	353.15	650.3
20000.00	278.15	711.4
20000.00	283.15	707.6
20000.00	293.15	700.4
20000.00	303.15	693.0
20000.00	313.15	685.5
20000.00	323.15	677.9
20000.00	333.15	670.4
20000.00	343.15	663.1
20000.00	353.15	655.7
25000.00	278.15	714.7
25000.00	283.15	711.1
25000.00	293.15	703.9
25000.00	303.15	696.9
25000.00	313.15	689.5
25000.00	323.15	682.1
25000.00	333.15	674.9
25000.00	343.15	667.9
25000.00	353.15	660.8
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
278.15	100.00	696.36
278.15	1000.00	697.01
278.15	5000.00	700.47
278.15	10000.00	704.35
278.15	15000.00	708.03
278.15	20000.00	711.54
278.15	25000.00	714.88
278.15	30000.00	718.17
278.15	35000.00	721.23
278.15	40000.00	724.19
278.15	45000.00	727.05
283.15	100.00	692.23
283.15	1000.00	693.01
283.15	5000.00	696.39
283.15	10000.00	700.44
283.15	15000.00	704.24
283.15	20000.00	707.85
283.15	25000.00	711.27
283.15	30000.00	714.56
283.15	35000.00	717.81
283.15	40000.00	720.8
283.15	45000.00	723.72
293.15	100.00	683.79
293.15	1000.00	684.6
293.15	5000.00	688.22
293.15	10000.00	692.49
293.15	15000.00	696.52
293.15	20000.00	700.34
293.15	25000.00	703.98
293.15	30000.00	707.62
293.15	35000.00	710.9
293.15	40000.00	714.1
293.15	45000.00	717.14
303.15	100.00	675.35
303.15	1000.00	676.16
303.15	5000.00	680.06
303.15	10000.00	684.63
303.15	15000.00	688.92
303.15	20000.00	692.96
303.15	25000.00	696.8
303.15	30000.00	700.52
303.15	35000.00	704.0
303.15	40000.00	707.3
303.15	45000.00	710.51
313.15	100.00	666.86
313.15	1000.00	667.7
313.15	5000.00	671.91
313.15	10000.00	676.8
313.15	15000.00	681.35
313.15	20000.00	685.63
313.15	25000.00	689.69
313.15	30000.00	693.53
313.15	35000.00	697.19
313.15	40000.00	700.67
313.15	45000.00	704.02
323.15	100.00	657.9
323.15	1000.00	658.85
323.15	5000.00	663.24
323.15	10000.00	668.53
323.15	15000.00	673.44
323.15	20000.00	677.94
323.15	25000.00	682.25
323.15	30000.00	686.3
323.15	35000.00	690.15
323.15	40000.00	693.83
323.15	45000.00	697.33
333.15	100.00	648.77
333.15	1000.00	649.92
333.15	5000.00	654.8
333.15	10000.00	660.46
333.15	15000.00	665.66
333.15	20000.00	670.49
333.15	25000.00	675.03
333.15	30000.00	679.3
333.15	35000.00	683.35
333.15	40000.00	687.19
333.15	45000.00	690.85
343.15	100.00	639.69
343.15	1000.00	640.93
343.15	5000.00	646.23
343.15	10000.00	652.33
343.15	15000.00	657.9
343.15	20000.00	663.04
343.15	25000.00	667.86
343.15	30000.00	672.37
343.15	35000.00	676.61
343.15	40000.00	680.63
343.15	45000.00	684.47
353.15	100.00	630.49
353.15	1000.00	631.83
353.15	5000.00	637.6
353.15	10000.00	644.13
353.15	15000.00	650.11
353.15	20000.00	655.53
353.15	25000.00	660.64
353.15	30000.00	665.38
353.15	35000.00	669.83
353.15	40000.00	674.08
353.15	45000.00	678.04
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.15	340.00	667.1
313.15	690.00	667.5
313.15	1030.00	667.8
313.15	1380.00	668.2
313.15	1720.00	668.64
313.15	2070.00	669.0
313.15	2410.00	669.3
313.15	2760.00	669.8
313.15	3100.00	670.1
313.15	3450.00	670.4
313.15	3800.00	670.8
313.15	4140.00	671.2
313.15	4480.00	671.6
313.15	4830.00	671.9
313.15	5170.00	672.2
313.15	5510.00	672.6
313.15	5860.00	672.9
313.15	6200.00	673.3
313.15	6550.00	673.6
313.15	6890.00	674.0
313.15	7240.00	674.3
333.15	340.00	649.7
333.15	690.00	650.2
333.15	1030.00	650.6
333.15	1380.00	651.0
333.15	1720.00	651.4
333.15	2070.00	651.9
333.15	2410.00	652.3
333.15	2760.00	652.7
333.15	3100.00	653.2
333.15	3450.00	653.6
333.15	3800.00	654.0
333.15	4140.00	654.4
333.15	4480.00	654.8
333.15	4830.00	655.2
333.15	5170.00	655.6
333.15	5510.00	656.0
333.15	5860.00	656.4
333.15	6200.00	656.8
333.15	6550.00	657.2
333.15	6890.00	657.6
333.15	7240.00	658.0
333.15	7580.00	658.4
333.15	7930.00	658.8
333.15	8270.00	659.2
353.15	340.00	631.8
353.15	690.00	632.3
353.15	1030.00	632.8
353.15	1380.00	633.3
353.15	1720.00	633.9
353.15	2070.00	634.4
353.15	2410.00	634.9
353.15	2760.00	635.3
353.15	3100.00	635.8
353.15	3450.00	636.3
353.15	3800.00	636.8
353.15	4140.00	637.3
353.15	4480.00	637.7
353.15	4830.00	638.2
353.15	5170.00	638.7
353.15	5510.00	639.2
353.15	5860.00	639.6
353.15	6200.00	640.1
353.15	6550.00	640.6
353.15	6890.00	641.0
353.15	7240.00	641.5
353.15	7580.00	641.9
353.15	7930.00	642.3
353.15	8270.00	642.8
353.15	8620.00	643.2
353.15	8960.00	643.9
353.15	9310.00	644.1
353.15	9650.00	644.5
373.15	340.00	613.1
373.15	690.00	613.7
373.15	1030.00	614.3
373.15	1380.00	614.9
373.15	1720.00	615.5
373.15	2070.00	616.1
373.15	2410.00	616.7
373.15	2760.00	617.3
373.15	3100.00	618.2
373.15	3450.00	618.5
373.15	3800.00	619.0
373.15	4140.00	619.6
373.15	4480.00	620.2
373.15	4830.00	620.7
373.15	5170.00	621.2
373.15	5510.00	621.8
373.15	5860.00	622.3
373.15	6200.00	622.9
373.15	6550.00	623.4
373.15	6890.00	623.9
373.15	7240.00	624.4
373.15	7580.00	625.0
373.15	7930.00	625.5
373.15	8270.00	626.0
373.15	8620.00	626.5
373.15	8960.00	627.0
373.15	9310.00	627.5
373.15	9650.00	628.0
393.15	340.00	593.4
393.15	690.00	594.1
393.15	1030.00	594.9
393.15	1380.00	595.6
393.15	1720.00	596.3
393.15	2070.00	597.0
393.15	2410.00	597.8
393.15	2760.00	598.5
393.15	3100.00	599.2
393.15	3450.00	599.9
393.15	3800.00	600.5
393.15	4140.00	601.2
393.15	4480.00	601.9
393.15	4830.00	602.5
393.15	5170.00	603.2
393.15	5510.00	603.8
393.15	5860.00	604.4
393.15	6200.00	605.1
393.15	6550.00	605.7
393.15	6890.00	606.3
393.15	7240.00	606.9
393.15	7580.00	607.5
393.15	7930.00	608.1
393.15	8270.00	608.7
393.15	8620.00	609.3
393.15	8960.00	609.9
393.15	9310.00	610.8
393.15	9650.00	611.1
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	101.00	692.398
283.15	267.60	692.646
283.15	550.80	692.799
283.15	878.60	693.177
283.15	991.30	693.192
283.15	2020.20	694.161
283.15	2914.80	694.997
283.15	4946.50	696.597
283.15	7034.80	698.638
283.15	9021.60	700.052
283.15	9991.90	700.869
283.15	11958.70	702.48
283.15	15011.20	704.783
283.15	18047.40	706.965
283.15	20045.40	708.637
283.15	22056.50	709.841
283.15	25044.10	712.0
283.15	28046.30	714.05
283.15	30051.70	715.435
283.15	32054.80	716.688
283.15	32971.30	717.342
283.15	32999.60	717.432
283.15	34016.50	718.012
283.15	34959.50	718.734
283.15	37943.00	720.455
283.15	40004.00	721.755
283.15	42057.90	723.102
283.15	44939.90	724.839
283.15	48022.40	726.526
283.15	49996.40	727.851
283.15	51981.80	728.904
283.15	54965.00	730.736
283.15	57949.30	732.407
283.15	59996.40	733.467
283.15	62025.40	734.345
283.15	64997.50	735.98
283.16	65971.00	736.499
288.15	102.00	688.224
288.15	391.30	688.682
288.15	554.40	688.232
288.15	882.70	689.214
288.15	989.10	688.618
288.15	2057.50	689.559
288.15	2917.80	690.931
288.15	5041.40	692.738
288.15	7088.80	693.96
288.15	9018.60	695.614
288.15	10039.90	696.278
288.15	12071.60	698.584
288.15	15001.40	700.836
288.15	17968.20	703.23
288.15	20067.60	704.758
288.15	22019.60	705.649
288.15	25001.50	707.645
288.15	28025.70	709.735
288.15	30034.70	711.006
288.15	32084.00	712.959
288.15	33050.00	713.818
288.15	33096.20	713.93
288.15	34035.60	714.067
288.15	35077.00	714.575
288.15	37992.90	716.378
288.15	40040.80	717.608
288.15	42022.80	718.735
288.15	44979.30	720.398
288.15	48045.10	723.18
288.15	50067.60	724.245
288.15	52032.00	724.841
288.15	55076.90	726.211
288.15	58004.00	729.214
288.15	59987.50	729.723
288.15	61973.60	731.101
288.15	64941.60	731.745
288.15	66025.40	732.751
293.15	100.50	683.714
293.16	305.20	684.504
293.16	476.40	684.708
293.15	825.10	684.796
293.16	1045.20	685.167
293.15	1971.70	685.978
293.15	3060.60	686.787
293.15	5011.00	688.859
293.16	7096.80	690.796
293.15	9042.10	692.394
293.15	10035.70	693.252
293.15	11946.50	694.459
293.15	14940.60	697.266
293.16	17888.60	698.789
293.16	19991.60	701.345
293.15	21987.10	701.769
293.16	24983.20	704.2
293.15	27986.00	706.659
293.16	29975.80	708.599
293.16	32232.40	710.098
293.15	33150.80	710.425
293.15	33149.70	710.401
293.15	34098.90	710.557
293.15	34999.60	711.53
293.16	38026.50	712.948
293.15	40081.00	714.898
293.15	42099.20	716.347
293.15	45068.20	718.234
293.16	48021.50	720.258
293.16	50084.50	721.322
293.16	52032.40	722.789
293.15	54965.50	724.479
293.15	58071.90	726.215
293.16	60018.30	727.31
293.16	61962.20	728.261
293.16	64991.00	729.973
293.15	66045.20	730.5
298.15	102.30	679.807
298.15	305.40	680.336
298.16	493.70	680.581
298.15	854.50	680.896
298.16	1012.60	680.891
298.15	1980.90	681.933
298.15	3167.80	682.97
298.15	5067.60	684.841
298.15	7065.30	686.383
298.16	9120.90	688.48
298.15	10106.60	689.119
298.16	11970.20	689.977
298.16	15219.70	693.294
298.16	17984.10	694.869
298.15	20127.80	696.696
298.15	22004.20	699.062
298.15	25080.50	701.29
298.16	28040.20	703.578
298.16	30089.10	704.725
298.16	32033.90	706.093
298.15	33112.80	707.026
298.16	33092.70	706.936
298.15	33924.30	706.971
298.16	35216.60	707.884
298.15	38096.90	709.948
298.15	40161.30	711.975
298.15	42028.50	713.324
298.15	45020.90	715.087
298.15	48106.60	717.001
298.15	50068.10	718.317
298.16	52019.70	719.461
298.15	55016.00	721.123
298.15	57930.90	723.027
298.15	59914.40	724.031
298.15	62036.30	725.393
298.15	65017.50	726.954
298.16	66118.40	727.501
303.15	100.70	675.559
303.15	304.10	675.598
303.15	498.90	675.77
303.15	900.60	675.904
303.15	979.10	676.053
303.15	1977.60	677.27
303.16	2964.90	678.337
303.15	4930.40	680.06
303.16	7045.60	682.343
303.16	8858.20	683.448
303.16	10013.90	684.334
303.15	11975.10	686.61
303.15	15043.60	689.15
303.16	18021.30	692.198
303.15	19974.40	693.813
303.15	21919.60	695.403
303.15	24991.70	697.736
303.16	27933.40	699.906
303.16	29990.40	701.007
303.15	31957.80	702.727
303.15	32862.10	703.514
303.15	33111.70	703.9
303.15	34080.70	704.468
303.15	34979.90	705.109
303.15	37951.00	707.216
303.15	39903.50	708.418
303.15	42013.80	709.635
303.15	44896.20	711.236
303.15	47951.40	713.224
303.15	50065.30	714.711
303.15	52072.60	715.915
303.15	55074.50	717.452
303.15	57989.30	719.654
303.15	59978.60	720.537
303.15	62052.40	721.855
303.15	64988.20	723.925
303.15	66029.70	724.328
308.15	105.00	671.006
308.15	274.30	671.143
308.15	494.10	671.318
308.15	803.30	671.687
308.15	1039.50	672.093
308.15	1916.70	672.909
308.15	2980.70	674.097
308.15	4990.20	676.132
308.15	6964.90	678.143
308.15	8864.30	679.887
308.15	9863.10	680.761
308.15	12008.60	682.857
308.16	15068.70	685.368
308.15	17849.80	687.815
308.15	19930.20	689.488
308.15	21988.30	691.177
308.15	25012.20	693.658
308.15	27955.20	695.718
308.15	29906.20	696.905
308.15	31928.70	698.302
308.15	32941.40	698.96
308.15	32885.90	699.002
308.15	34010.80	700.438
308.16	34949.30	701.078
308.15	37971.20	703.176
308.15	40011.40	704.309
308.15	41998.10	705.614
308.15	45016.60	707.854
308.15	48033.40	709.906
308.15	50043.60	711.265
308.15	51977.40	712.584
308.15	54981.90	714.563
308.15	58008.90	716.265
308.15	60030.00	717.688
308.15	61984.80	718.959
308.15	64980.50	720.569
308.16	66087.80	721.543
313.15	100.80	666.87
313.15	316.00	667.185
313.15	569.60	667.234
313.16	860.70	667.671
313.15	1088.80	668.002
313.15	2109.70	669.053
313.15	3137.00	670.192
313.15	5111.80	672.198
313.15	6921.80	674.169
313.15	9210.70	676.379
313.15	10209.30	677.309
313.15	12019.70	679.079
313.15	15058.60	681.665
313.15	17921.10	684.308
313.15	19931.90	686.1
313.15	22058.20	687.733
313.15	24861.60	690.068
313.15	27868.70	692.385
313.15	29956.80	693.806
313.15	32107.10	695.43
313.15	32980.30	696.141
313.15	33002.20	696.147
313.15	33981.20	697.086
313.15	35045.40	697.948
313.15	38126.60	700.098
313.16	39996.90	701.327
313.15	41978.40	702.778
313.15	44946.30	704.758
313.15	47879.70	706.851
313.16	50020.80	708.33
313.15	52097.40	709.812
313.15	54924.00	711.549
313.15	58081.50	713.474
313.15	59932.20	714.707
313.15	62004.00	716.103
313.15	64954.10	717.814
313.15	66113.10	718.367
318.15	100.70	662.812
318.15	336.30	663.228
318.16	590.90	663.443
318.16	891.00	663.766
318.15	1105.70	663.94
318.15	1929.10	664.905
318.15	2933.20	665.972
318.16	5020.80	668.355
318.16	6926.70	670.309
318.15	8989.00	672.331
318.15	10074.50	673.533
318.15	11896.00	675.253
318.16	14800.10	678.075
318.15	18102.40	681.046
318.15	19985.10	682.727
318.15	22093.70	684.679
318.16	24872.80	686.865
318.16	27909.40	689.38
318.15	29997.50	691.196
318.16	31957.10	692.414
318.15	33015.60	693.259
318.15	33179.60	693.331
318.16	34110.30	694.119
318.16	35047.60	694.934
318.15	37838.40	697.046
318.15	40092.50	698.439
318.16	41996.00	699.6
318.15	44884.00	701.561
318.15	47944.40	703.663
318.16	49950.20	705.2
318.16	52037.30	706.412
318.15	54944.20	708.215
318.15	57972.30	710.506
318.15	59922.50	711.605
318.16	61930.00	712.85
318.15	65021.80	714.898
318.15	66027.50	715.438
323.15	102.30	658.378
323.15	296.10	658.71
323.15	528.40	658.782
323.16	920.70	659.343
323.15	994.20	659.429
323.15	2006.90	660.61
323.15	2966.60	661.806
323.15	4996.20	663.968
323.15	7042.10	666.276
323.15	9029.90	667.858
323.15	10089.70	669.742
323.15	11913.70	670.973
323.15	15110.70	674.373
323.15	17980.70	677.251
323.15	20037.80	678.71
323.15	21994.90	680.737
323.15	24993.40	683.213
323.16	27958.40	685.975
323.16	30054.60	687.083
323.15	32079.20	689.177
323.16	33067.40	689.946
323.15	33103.20	689.972
323.15	34080.80	690.434
323.15	35113.00	691.624
323.15	37952.80	693.659
323.16	40047.00	695.097
323.15	42011.10	696.516
323.16	44936.90	698.783
323.15	48025.40	700.814
323.15	49933.50	702.105
323.15	52114.30	703.681
323.15	54963.50	705.509
323.15	58044.90	707.475
323.15	60049.80	708.827
323.15	62131.00	710.008
323.15	64998.70	711.842
323.16	66131.20	712.551
328.15	100.80	653.868
328.15	289.90	654.182
328.16	501.00	654.211
328.15	897.50	654.815
328.15	994.10	655.012
328.15	1988.80	656.162
328.15	2996.70	657.408
328.15	5013.40	659.794
328.15	6974.90	662.023
328.15	9017.00	664.204
328.15	10040.00	665.257
328.16	12209.60	667.562
328.16	15054.80	670.204
328.16	18061.30	673.216
328.16	20279.00	675.247
328.16	22012.90	676.775
328.15	24924.10	679.489
328.15	27979.20	682.036
328.15	29958.30	683.395
328.15	32059.50	685.102
328.15	33065.50	685.969
328.15	33107.20	685.992
328.15	34013.40	687.01
328.15	35029.60	687.796
328.15	38009.80	690.025
328.15	39969.00	691.415
328.15	41958.80	692.865
328.15	44952.60	695.094
328.15	47977.50	697.371
328.15	49926.50	698.804
328.15	51996.90	700.259
328.15	54946.60	702.284
328.15	57938.70	704.221
328.15	59990.90	705.64
328.15	61981.50	707.057
328.15	65031.60	708.835
328.15	66046.20	709.499
333.15	100.40	649.302
333.16	303.50	649.622
333.15	532.60	649.653
333.15	897.80	650.259
333.16	1003.00	650.554
333.15	1987.20	651.687
333.15	3023.40	653.063
333.15	4997.40	655.338
333.15	7002.40	657.844
333.15	9032.00	660.047
333.15	10209.50	661.268
333.16	12011.10	663.322
333.15	15008.40	666.206
333.16	17991.90	669.217
333.16	20035.90	671.108
333.15	22033.60	672.882
333.16	25027.10	675.678
333.15	28039.90	678.188
333.15	30015.60	679.579
333.15	32067.10	681.185
333.15	32976.90	681.946
333.16	33072.70	682.004
333.15	34085.90	683.474
333.15	35075.40	684.235
333.15	37893.70	686.324
333.15	40110.90	687.848
333.15	41946.80	689.191
333.15	44974.00	691.567
333.15	47935.60	693.899
333.15	49919.60	695.372
333.15	51953.30	696.893
333.15	54875.90	699.008
333.15	58057.20	700.988
333.15	59992.70	702.482
333.15	62048.60	703.927
333.15	64970.40	705.65
333.15	66005.00	706.481
338.15	100.40	644.915
338.15	309.80	645.161
338.15	561.60	645.341
338.15	898.50	645.924
338.15	1014.10	646.212
338.16	2000.20	647.409
338.15	2936.10	648.694
338.15	5018.60	651.205
338.16	6917.30	653.552
338.16	9046.90	656.063
338.15	10033.60	657.126
338.16	11959.40	659.361
338.15	14884.90	662.203
338.15	17955.80	665.481
338.15	19927.00	667.369
338.15	22041.10	669.319
338.15	25026.20	672.169
338.16	27975.50	674.704
338.15	29993.70	676.134
338.16	31948.90	677.899
338.15	32881.50	678.515
338.16	32881.50	678.499
338.15	33937.40	679.921
338.15	35012.40	680.879
338.16	37962.10	683.24
338.15	39986.90	684.582
338.15	41989.90	686.092
338.15	44978.20	688.463
338.15	47971.40	690.744
338.15	49998.60	692.38
338.15	52127.20	693.976
338.16	54992.20	696.066
338.15	57939.90	697.82
338.15	60013.80	699.459
338.16	62073.50	700.918
338.15	65011.90	702.688
338.15	66056.80	703.55
343.15	105.10	640.758
343.15	297.30	640.918
343.15	520.30	641.218
343.15	911.70	641.765
343.15	1017.70	641.938
343.15	1994.60	643.242
343.15	2968.30	644.553
343.15	4994.80	647.152
343.15	6976.60	649.726
343.15	9002.60	652.141
343.15	10060.40	653.267
343.15	12024.50	655.625
343.15	14927.50	658.769
343.15	17975.20	661.975
343.15	19985.00	664.0
343.15	22032.80	666.001
343.15	25090.50	668.93
343.15	28044.70	671.724
343.15	30082.00	673.379
343.15	32169.60	675.296
343.15	33053.30	676.043
343.15	33096.80	676.076
343.16	34034.10	676.976
343.15	35030.10	677.808
343.15	37943.20	680.185
343.15	40012.30	681.817
343.15	41972.20	683.353
343.15	44927.30	685.751
343.15	47907.90	688.0
343.15	50058.90	689.668
343.15	52026.20	691.103
343.16	54918.50	693.158
343.16	57986.20	695.23
343.15	59944.40	696.69
343.15	61966.50	697.921
343.15	65069.90	699.939
343.15	66059.20	700.533
348.15	100.30	636.109
348.16	291.70	636.475
348.15	462.20	636.505
348.15	859.80	637.192
348.15	974.20	637.393
348.15	1974.90	638.781
348.15	3051.10	640.295
348.15	5094.00	643.002
348.16	7050.20	645.632
348.16	9003.20	648.038
348.15	10025.40	649.256
348.16	12186.90	651.83
348.15	14792.00	654.622
348.16	17899.00	658.098
348.15	20111.40	660.386
348.15	22163.40	662.539
348.16	25099.80	665.329
348.15	28080.10	668.108
348.15	30148.90	670.002
348.15	32161.30	671.799
348.16	32941.60	672.463
348.15	32935.20	672.452
348.15	33958.60	673.504
348.15	35044.60	674.428
348.15	37937.40	676.834
348.15	40025.60	678.502
348.16	42065.80	680.23
348.15	45050.60	682.511
348.15	47914.70	684.825
348.15	49949.80	686.336
348.15	52166.80	688.088
348.15	55021.90	690.168
348.15	57945.30	692.261
348.16	60030.00	693.748
348.15	62063.30	695.106
348.15	64941.60	696.91
348.15	66153.40	697.788
353.15	100.50	631.649
353.15	336.00	631.995
353.15	572.60	632.233
353.15	926.00	632.774
353.15	1016.40	632.95
353.16	2113.40	634.631
353.15	2992.10	635.919
353.15	4963.90	638.644
353.15	7000.90	641.284
353.15	9062.30	643.911
353.15	10005.00	645.176
353.15	12127.50	647.788
353.15	14954.20	651.028
353.15	17977.40	654.406
353.15	19937.00	656.492
353.15	21893.60	658.507
353.15	24908.20	661.562
353.15	27850.30	664.482
353.15	29936.20	666.345
353.15	31876.00	668.022
353.15	32911.00	668.934
353.15	32960.80	669.075
353.16	33963.70	670.126
353.15	34945.40	670.985
353.15	37913.10	673.509
353.15	40142.80	675.336
353.15	42067.30	677.003
353.15	45001.70	679.292
353.15	48029.20	681.775
353.15	50145.10	683.478
353.15	52082.20	685.052
353.15	55132.20	687.213
353.15	57980.30	689.013
353.15	60098.40	690.731
353.16	62042.50	692.223
353.15	65062.70	694.154
353.16	66024.30	694.802
358.15	100.40	626.935
358.15	264.10	627.168
358.15	508.40	627.316
358.15	926.80	628.098
358.15	1013.90	628.327
358.16	2083.90	629.903
358.15	3021.20	631.365
358.15	4930.00	634.077
358.16	6993.50	637.086
358.16	9030.20	639.755
358.15	10072.70	641.066
358.15	12136.80	643.735
358.15	14904.90	646.944
358.15	17965.40	650.491
358.16	20162.00	652.87
358.15	22174.60	654.965
358.15	25059.40	657.993
358.15	28035.20	660.974
358.15	30001.90	662.532
358.15	31977.70	664.488
358.15	32792.60	665.093
358.15	33039.30	665.404
358.15	33850.00	666.525
358.15	35026.50	667.567
358.15	37872.30	669.996
358.15	40037.40	671.748
358.15	42100.10	673.454
358.16	45054.00	675.954
358.15	47958.10	678.424
358.15	50037.90	680.129
358.15	52080.70	681.85
358.15	55073.40	684.059
358.15	57918.40	685.685
358.15	60042.70	687.68
358.15	62066.50	689.111
358.15	64986.10	691.283
358.15	66108.60	692.023
363.15	104.10	622.138
363.15	334.00	622.474
363.15	601.70	622.649
363.15	892.90	623.267
363.15	1034.70	623.668
363.15	1986.00	625.081
363.15	2940.40	626.678
363.15	4979.20	629.757
363.16	6920.20	632.642
363.16	8964.80	635.395
363.15	9959.50	636.563
363.15	11970.70	639.421
363.15	14935.50	642.887
363.15	17973.30	646.544
363.15	19939.90	648.708
363.16	21932.90	650.806
363.15	24872.20	654.024
363.15	27992.70	657.078
363.15	30062.30	659.006
363.15	31961.10	660.63
363.15	33053.30	661.633
363.15	33032.60	661.606
363.15	33999.50	663.017
363.15	35028.30	664.03
363.15	37919.20	666.495
363.15	39916.00	668.059
363.15	42015.50	669.917
363.16	44986.80	672.551
363.15	47947.20	675.063
363.15	50050.30	676.807
363.15	52022.60	678.457
363.15	54940.40	680.815
363.15	57916.50	682.78
363.15	59980.00	684.625
363.15	62042.90	686.168
363.15	64924.10	688.267
363.15	66088.40	689.169
Reference

Speed of sound, m/s

Fixed		Measured
Temperature, K - Fluid (supercritical or subcritical phases)	Pressure, kPa - Fluid (supercritical or subcritical phases)	Speed of sound, m/s - Fluid (supercritical or subcritical phases)
513.92	2500.00	266.66
525.23	2500.00	196.31
528.93	2500.00	167.01
534.12	2500.00	121.38
538.13	2500.00	101.28
544.09	2500.00	100.71
547.02	2500.00	107.6
552.59	2500.00	118.66
559.91	2500.00	129.19
564.02	2500.00	135.46
572.57	2500.00	144.47
584.19	2500.00	156.26
590.48	2500.00	161.58
601.60	2500.00	170.4
612.58	2500.00	179.23
620.87	2500.00	183.77
632.18	2500.00	189.44
640.72	2500.00	192.85
650.07	2500.00	195.77
513.59	3000.00	293.56
523.83	3000.00	242.56
528.41	3000.00	218.56
532.76	3000.00	193.81
538.36	3000.00	152.7
544.95	3000.00	115.6
549.04	3000.00	105.27
553.93	3000.00	110.64
574.87	5000.00	160.49
577.04	5000.00	154.18
582.31	5000.00	142.67
588.17	5000.00	139.88
592.28	5000.00	136.41
597.48	5000.00	135.43
602.30	5000.00	135.26
607.65	5000.00	136.72
615.11	5000.00	142.58
623.25	5000.00	150.58
632.29	5000.00	156.55
643.51	5000.00	165.41
513.58	6000.00	394.15
524.62	6000.00	357.73
529.10	6000.00	344.17
533.77	6000.00	331.99
539.09	6000.00	316.72
543.60	6000.00	300.59
548.98	6000.00	283.97
553.05	6000.00	270.32
557.86	6000.00	255.8
563.84	6000.00	236.54
574.85	6000.00	211.93
583.18	6000.00	191.45
592.57	6000.00	176.14
604.10	6000.00	161.83
613.73	6000.00	158.49
559.74	3000.00	116.03
563.09	3000.00	119.84
574.33	3000.00	134.46
582.39	3000.00	142.99
591.77	3000.00	152.87
602.84	3000.00	161.38
612.37	3000.00	167.57
623.42	3000.00	174.58
632.04	3000.00	179.96
641.53	3000.00	186.21
650.90	3000.00	189.41
513.65	4000.00	333.84
524.25	4000.00	291.43
528.90	4000.00	269.01
533.55	4000.00	252.16
537.58	4000.00	231.06
541.47	4000.00	208.26
549.16	4000.00	178.39
553.43	4000.00	160.12
560.41	4000.00	132.63
563.94	4000.00	124.51
575.28	4000.00	113.58
584.60	4000.00	122.55
591.62	4000.00	127.84
603.68	4000.00	143.88
612.08	4000.00	149.82
621.22	4000.00	157.32
631.85	4000.00	163.15
641.95	4000.00	173.32
622.48	6000.00	158.77
632.41	6000.00	159.42
643.04	6000.00	164.74
513.40	8000.00	451.65
524.62	8000.00	417.84
528.95	8000.00	403.55
533.57	8000.00	391.25
538.84	8000.00	376.34
542.55	8000.00	364.39
548.66	8000.00	346.4
553.19	8000.00	335.76
557.81	8000.00	325.48
563.58	8000.00	312.82
574.41	8000.00	287.41
583.10	8000.00	270.69
593.19	8000.00	249.19
604.67	8000.00	226.0
613.93	8000.00	218.01
620.20	8000.00	211.6
632.86	8000.00	201.03
642.59	8000.00	195.65
515.30	10000.00	481.16
523.19	10000.00	459.31
533.40	10000.00	437.12
543.16	10000.00	413.25
553.20	10000.00	388.87
563.03	10000.00	363.89
573.39	10000.00	345.21
579.18	10000.00	331.94
515.23	5000.00	363.89
521.41	5000.00	337.01
534.45	5000.00	293.97
543.50	5000.00	262.34
553.42	5000.00	225.17
565.65	5000.00	187.87
582.86	10000.00	325.02
587.85	10000.00	315.79
592.71	10000.00	307.49
603.51	10000.00	291.2
614.03	10000.00	272.94
623.13	10000.00	260.67
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
100.00	293.15	1151.69
100.00	298.16	1129.87
100.00	303.06	1108.88
100.00	308.08	1087.42
100.00	313.10	1066.12
100.00	318.18	1044.54
15200.00	293.20	1256.33
15200.00	303.17	1218.64
15200.00	308.08	1200.43
15200.00	313.10	1182.05
15200.00	318.18	1163.39
30400.00	293.18	1341.5
30400.00	303.13	1306.98
30400.00	308.07	1290.28
30400.00	313.12	1273.35
30400.00	318.18	1256.47
45590.00	293.19	1416.6
45590.00	298.18	1400.09
45590.00	303.07	1384.42
45590.00	308.07	1368.71
45590.00	313.12	1352.98
45590.00	318.17	1337.39
60790.00	293.20	1484.48
60790.00	298.19	1468.69
60790.00	303.18	1453.68
60790.00	308.12	1438.95
60790.00	313.12	1424.3
60790.00	318.17	1409.63
75990.00	293.20	1546.46
75990.00	298.11	1531.64
75990.00	303.17	1517.17
75990.00	308.12	1503.23
75990.00	313.10	1489.21
75990.00	318.09	1475.54
91190.00	293.20	1603.69
91190.00	298.15	1589.43
91190.00	303.18	1575.68
91190.00	308.11	1562.39
91190.00	313.13	1549.03
91190.00	318.15	1535.72
101320.00	293.20	1639.7
101320.00	298.16	1625.72
101320.00	303.10	1612.63
101320.00	308.24	1599.12
101320.00	313.21	1586.17
101320.00	318.18	1573.59
111450.00	293.10	1674.29
111450.00	298.13	1660.46
111450.00	298.16	1660.43
111450.00	303.15	1647.6
111450.00	308.21	1634.64
111450.00	313.20	1622.05
111450.00	318.18	1609.77
121580.00	293.16	1707.09
121580.00	298.14	1692.38
121580.00	303.10	1681.25
121580.00	308.17	1668.58
121580.00	313.13	1656.4
121580.00	318.17	1644.27
Reference

Thermal conductivity, W/m/K

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Thermal conductivity, W/m/K - Liquid
77.00	295.00	0.1190
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[127.29; 443.49]	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			1.09310e+02
Coefficient B			-7.04200e+02
Coefficient C			6.44424e+00
Coefficient D			-1.79220e-04
Coefficient E			4.69920e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	127.29	J/mol×K	200.00	Calculated Property
Cp,gas	186.30	J/mol×K	344.44	Calculated Property
Cp,gas	247.34	J/mol×K	488.89	Calculated Property
Cp,gas	297.55	J/mol×K	633.33	Calculated Property
Cp,gas	336.98	J/mol×K	777.78	Calculated Property
Cp,gas	367.92	J/mol×K	922.22	Calculated Property
Cp,gas	392.57	J/mol×K	1066.67	Calculated Property
Cp,gas	412.59	J/mol×K	1211.11	Calculated Property
Cp,gas	429.26	J/mol×K	1355.56	Calculated Property
Cp,gas	443.49	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[198.94; 370.88]	J/mol×K	[182.55; 520.00]	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			1.34750e+02
Coefficient B			1.49370e+01
Coefficient C			3.69524e+00
Coefficient D			1.43800e-03
Coefficient E			3.67110e-06
Temperature range, min.			182.55
Temperature range, max.			520.00
Cp,liquid	198.94	J/mol×K	182.55	Calculated Property
Cp,liquid	205.37	J/mol×K	220.04	Calculated Property
Cp,liquid	213.56	J/mol×K	257.54	Calculated Property
Cp,liquid	223.84	J/mol×K	295.03	Calculated Property
Cp,liquid	236.68	J/mol×K	332.53	Calculated Property
Cp,liquid	252.71	J/mol×K	370.02	Calculated Property
Cp,liquid	272.79	J/mol×K	407.52	Calculated Property
Cp,liquid	298.07	J/mol×K	445.01	Calculated Property
Cp,liquid	330.09	J/mol×K	482.51	Calculated Property
Cp,liquid	370.88	J/mol×K	520.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0040835; 0.0000481]	Pa×s	[180.15; 540.20]	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			-6.10886e+01
Coefficient B			2.53230e+03
Coefficient C			8.09167e+00
Coefficient D			-1.52585e-05
Coefficient E			2.00000e+00
Temperature range, min.			180.15
Temperature range, max.			540.20
η	0.0040835	Pa×s	180.15	Calculated Property
η	0.0012599	Pa×s	220.16	Calculated Property
η	0.0006189	Pa×s	260.16	Calculated Property
η	0.0003822	Pa×s	300.17	Calculated Property
η	0.0002638	Pa×s	340.17	Calculated Property
η	0.0001909	Pa×s	380.18	Calculated Property
η	0.0001396	Pa×s	420.18	Calculated Property
η	0.0001008	Pa×s	460.19	Calculated Property
η	0.0000709	Pa×s	500.19	Calculated Property
η	0.0000481	Pa×s	540.20	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[43.46; 0.00]	kJ/mol	[182.57; 540.20]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			4.27576e+01
Coefficient B			-1.05124e+00
Coefficient C			4.60171e+00
Coefficient D			-5.55895e+00
Coefficient E			2.36950e+00
Critical temperature, Tc (K)			5.40200e+02
Temperature range, min.			182.57
Temperature range, max.			540.20
ΔvapH	43.46	kJ/mol	182.57	Calculated Property
ΔvapH	41.28	kJ/mol	222.31	Calculated Property
ΔvapH	38.88	kJ/mol	262.04	Calculated Property
ΔvapH	36.37	kJ/mol	301.78	Calculated Property
ΔvapH	33.80	kJ/mol	341.52	Calculated Property
ΔvapH	31.09	kJ/mol	381.25	Calculated Property
ΔvapH	27.99	kJ/mol	420.99	Calculated Property
ΔvapH	24.07	kJ/mol	460.73	Calculated Property
ΔvapH	18.31	kJ/mol	500.46	Calculated Property
ΔvapH	0.00	kJ/mol	540.20	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[271.34; 396.62]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42106e+01
Coefficient B			-3.08981e+03
Coefficient C			-4.94170e+01
Temperature range, min.			271.34
Temperature range, max.			396.62
Pvap	1.33	kPa	271.34	Calculated Property
Pvap	3.03	kPa	285.26	Calculated Property
Pvap	6.29	kPa	299.18	Calculated Property
Pvap	12.09	kPa	313.10	Calculated Property
Pvap	21.77	kPa	327.02	Calculated Property
Pvap	37.03	kPa	340.94	Calculated Property
Pvap	60.03	kPa	354.86	Calculated Property
Pvap	93.29	kPa	368.78	Calculated Property
Pvap	139.74	kPa	382.70	Calculated Property
Pvap	202.65	kPa	396.62	Calculated Property
Pvap	[1.72e-04; 2714.64]	kPa	[182.57; 540.20]	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			8.28968e+01
Coefficient B			-7.08485e+03
Coefficient C			-1.01792e+01
Coefficient D			7.44171e-06
Coefficient E			2.00000e+00
Temperature range, min.			182.57
Temperature range, max.			540.20
Pvap	1.72e-04	kPa	182.57	Calculated Property
Pvap	0.03	kPa	222.31	Calculated Property
Pvap	0.73	kPa	262.04	Calculated Property
Pvap	7.23	kPa	301.78	Calculated Property
Pvap	38.10	kPa	341.52	Calculated Property
Pvap	133.74	kPa	381.25	Calculated Property
Pvap	357.06	kPa	420.99	Calculated Property
Pvap	789.97	kPa	460.73	Calculated Property
Pvap	1533.15	kPa	500.46	Calculated Property
Pvap	2714.64	kPa	540.20	Calculated Property
Pvap	[1.26e-04; 2783.13]	kPa	[182.56; 540.26]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			1.08146e+02
Coefficient B			-8.03007e+03
Coefficient C			-1.41239e+01
Coefficient D			1.20486e-05
Coefficient E			0.00000e+00
Temperature range, min.			182.56
Temperature range, max.			540.26
Pvap	1.26e-04	kPa	182.56	Calculated Property
Pvap	0.02	kPa	222.30	Calculated Property
Pvap	0.73	kPa	262.05	Calculated Property
Pvap	7.33	kPa	301.79	Calculated Property
Pvap	38.43	kPa	341.54	Calculated Property
Pvap	133.10	kPa	381.28	Calculated Property
Pvap	351.76	kPa	421.03	Calculated Property
Pvap	777.67	kPa	460.77	Calculated Property
Pvap	1528.31	kPa	500.52	Calculated Property
Pvap	2783.13	kPa	540.26	Calculated Property
Pvap	[2.91e-04; 5.27]	kPa	[185.29; 295.60]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.56991e+01
Coefficient B			-3.76567e+03
Coefficient C			-2.73380e+01
Reference			Carruth and Kobayashi, 1973
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			185.29
Temperature range, max.			295.60
Pvap	2.91e-04	kPa	185.29	Calculated Property
Pvap	1.62e-03	kPa	197.55	Calculated Property
Pvap	7.16e-03	kPa	209.80	Calculated Property
Pvap	0.03	kPa	222.06	Calculated Property
Pvap	0.08	kPa	234.32	Calculated Property
Pvap	0.23	kPa	246.57	Calculated Property
Pvap	0.57	kPa	258.83	Calculated Property
Pvap	1.28	kPa	271.09	Calculated Property
Pvap	2.69	kPa	283.34	Calculated Property
Pvap	5.27	kPa	295.60	Calculated Property
Pvap	[6.38; 103.89]	kPa	[299.07; 372.43]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38807e+01
Coefficient B			-2.92114e+03
Coefficient C			-5.61990e+01
Reference			Williamham, Taylor, et al., 1945
Temperature range, min.			299.07
Temperature range, max.			372.43
Pvap	6.38	kPa	299.07	Calculated Property
Pvap	9.43	kPa	307.22	Calculated Property
Pvap	13.60	kPa	315.37	Calculated Property
Pvap	19.17	kPa	323.52	Calculated Property
Pvap	26.49	kPa	331.67	Calculated Property
Pvap	35.93	kPa	339.83	Calculated Property
Pvap	47.90	kPa	347.98	Calculated Property
Pvap	62.88	kPa	356.13	Calculated Property
Pvap	81.37	kPa	364.28	Calculated Property
Pvap	103.89	kPa	372.43	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[771.03; 225.89]	kg/m3	[182.57; 540.20]	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			5.71582e+01
Coefficient B			2.53040e-01
Coefficient C			5.40200e+02
Coefficient D			2.73350e-01
Temperature range, min.			182.57
Temperature range, max.			540.20
ρl	771.03	kg/m3	182.57	Calculated Property
ρl	741.61	kg/m3	222.31	Calculated Property
ρl	710.68	kg/m3	262.04	Calculated Property
ρl	677.85	kg/m3	301.78	Calculated Property
ρl	642.59	kg/m3	341.52	Calculated Property
ρl	604.04	kg/m3	381.25	Calculated Property
ρl	560.74	kg/m3	420.99	Calculated Property
ρl	509.72	kg/m3	460.73	Calculated Property
ρl	442.92	kg/m3	500.46	Calculated Property
ρl	225.89	kg/m3	540.20	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.01]	N/m	[182.15; 371.15]	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			4.88687e-02
Coefficient B			-9.80000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			182.15
Temperature range, max.			371.15
γ	0.03	N/m	182.15	Calculated Property
γ	0.03	N/m	203.15	Calculated Property
γ	0.03	N/m	224.15	Calculated Property
γ	0.02	N/m	245.15	Calculated Property
γ	0.02	N/m	266.15	Calculated Property
γ	0.02	N/m	287.15	Calculated Property
γ	0.02	N/m	308.15	Calculated Property
γ	0.02	N/m	329.15	Calculated Property
γ	0.01	N/m	350.15	Calculated Property
γ	0.01	N/m	371.15	Calculated Property
γ	[0.03; 1.37e-05]	N/m	[182.57; 536.27]	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			-7.74100e-03
Coefficient B			6.54050e+01
Coefficient C			-3.64780e+00
Coefficient D			1.89400e-03
Coefficient E			-8.16920e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 540.2 K.
Temperature range, min.			182.57
Temperature range, max.			536.27
γ	0.03	N/m	182.57	Calculated Property
γ	0.03	N/m	221.87	Calculated Property
γ	0.02	N/m	261.17	Calculated Property
γ	0.02	N/m	300.47	Calculated Property
γ	0.02	N/m	339.77	Calculated Property
γ	0.01	N/m	379.07	Calculated Property
γ	0.01	N/m	418.37	Calculated Property
γ	0.01	N/m	457.67	Calculated Property
γ	0.00	N/m	496.97	Calculated Property
γ	1.37e-05	N/m	536.27	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.11]	W/m×K	[182.57; 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			-7.63330e-02
Coefficient B			3.80250e-01
Coefficient C			-7.53990e+03
Coefficient D			-2.64680e+06
Temperature range, min.			182.57
Temperature range, max.			1000.00
λgas	0.00	W/m×K	182.57	Calculated Property
λgas	0.01	W/m×K	273.40	Calculated Property
λgas	0.02	W/m×K	364.22	Calculated Property
λgas	0.03	W/m×K	455.05	Calculated Property
λgas	0.04	W/m×K	545.87	Calculated Property
λgas	0.05	W/m×K	636.70	Calculated Property
λgas	0.07	W/m×K	727.52	Calculated Property
λgas	0.08	W/m×K	818.35	Calculated Property
λgas	0.10	W/m×K	909.17	Calculated Property
λgas	0.11	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.16; 0.10]	W/m×K	[182.57; 393.15]	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			8.36570e-02
Coefficient B			4.91110e+01
Coefficient C			-3.45360e+00
Coefficient D			7.79890e-03
Coefficient E			-2.51120e-05
Temperature range, min.			182.57
Temperature range, max.			393.15
λliquid	0.16	W/m×K	182.57	Calculated Property
λliquid	0.15	W/m×K	205.97	Calculated Property
λliquid	0.15	W/m×K	229.37	Calculated Property
λliquid	0.14	W/m×K	252.76	Calculated Property
λliquid	0.13	W/m×K	276.16	Calculated Property
λliquid	0.12	W/m×K	299.56	Calculated Property
λliquid	0.12	W/m×K	322.96	Calculated Property
λliquid	0.11	W/m×K	346.35	Calculated Property
λliquid	0.10	W/m×K	369.75	Calculated Property
λliquid	0.10	W/m×K	393.15	Calculated Property

Similar Compounds

Find more compounds similar to Heptane.

Mixtures

• Octane + Heptane
• Diethyl malonate + Heptane
• Ethanol, 2-butoxy- + Heptane
• Ethanol, 2-propoxy- + Heptane
• Carbon dioxide + Heptane
• Thiophene + Heptane + Ethanol, 2,2'-oxybis-
• Benzo[b]thiophene + Heptane + Ethanol, 2,2'-oxybis-
• Thiophene + Triethylene glycol + Heptane
• Benzo[b]thiophene + Triethylene glycol + Heptane
• Heptane + Ethanol, 2,2'-oxybis-
• Triethylene glycol + Heptane
• 1,2-Ethanediol + TETRAMETHYLAMMONIUM CHLORIDE + Heptane
• 1-Dodecanamine + Heptane
• Heptane + 1-Tetradecanamine
• Propylamine + Heptane
• 2-Propanamine + Heptane
• 1-Butanamine + Heptane
• Isobutylamine + Heptane
• 2-Propanamine, 2-methyl- + Heptane
• 1-Pentanamine + Heptane

Find more mixtures with Heptane.

Sources

• KDB Vapor Pressure Data
• Active Thermochemical Tables 1.112, gas-phase enthalpies of formation ChEDL chemicals 1.5.2, from Active Thermochemical Tables (ATcT), version 1.112, Argonne National Laboratory; Ruscic, B. et al. Active Thermochemical Tables: Thermochemistry for the 21st Century. J. Phys.: Conf. Ser. 2005, 16, 561.
• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• Hankinson and Thomson (1979), COSTALD parameters ChEDL chemicals 1.5.2, from Hankinson, R. W.; Thomson, G. H. A New Correlation for Saturated Densities of Liquids and Their Mixtures. AIChE J. 1979, 25, 653-663.
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 ChEDL chemicals 1.5.2, from Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 2. Normal Alkanes. J. Chem. Eng. Data 1995, 40, 531-546.
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• Passut and Danner (1973), critical constants and acentric factors ChEDL chemicals 1.5.2, from Passut, C. A.; Danner, R. P. Acentric Factor. A Valuable Correlating Parameter for the Properties of Hydrocarbons. Ind. Eng. Chem. Process Des. Dev. 1973, 12, 365-368.
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Kinematic Viscosities for Ether + Alkane Mixtures: Experimental Results and UNIFAC-VISCO Parameters
• Viscometric and Volumetric Properties of 10 Regular Binary Systems at 308.15 K and 313.15 K
• Thermodynamic and Acoustic Properties of Mixtures of Dibromomethane + Heptane
• Experimental Study of the Density and Viscosity of n-Heptane at Temperatures from 298 K to 470 K and Pressure up to 245 MPa
• Densities and Kinematic Viscosities of a Quinary Regular Liquid System and Its Five Quaternary Subsystems at 293.15A K and 298.15A K
• Experimental solubility data of various n-alkane waxes: effects of alkane chain length, alkane odd versus even carbon number structures, and solvent chemistry on solubility
• Activity coefficient at infinite dilution, azeotropic data, excess enthalpies and solid liquid-equilibria for binary systems of alkanes and aromatics with esters
• Liquid-liquid equilibrium data of water with neohexane, methylcyclohexane, tert-butyl methyl ether, n-heptane and vapor -liquid-liquid equilibrium with methane
• Vapour pressures and excess functions of (3,5; 2,6)dimethylpyridine + n-hexane, n-heptane and n-octane measurement and prediction
• Establishing benchmarks for the Second Industrial Fluids Simulation Challenge
• Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, trihexyl(tetradecyl)-phosphonium tris(pentafluoroethyl) trifluorophosphate, by gas liquid chromatography
• Bubble points of some binary mixtures formed by o-cresol at 95.75 kPa
• Solubility of CO2 in branched alkanes in order to extend the PPR78 model (predictive 1978, Peng Robinson EOS with temperature-dependent kij calculated through a group contribution method) to such systems
• Isobaric vapour liquid equilibria for binary mixtures of n-heptane with bromobenzene, chlorobenzene and fluorobenzene at atmospheric pressure
• Comparative experimental and modeling studies of the viscosity behavior of ethanol +C7 hydrocarbon mixtures versus pressure and temperature
• Liquid liquid equilibrium of (perfluoroalkane + alkane) binary mixtures
• Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
• Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, tributylmethylphosphonium methylsulphate by gas liquid chromatography
• Ternary liquid liquid equilibria for mixtures of toluene + n-heptane + an ionic liquid
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• Vapour liquid liquid and vapour liquid equilibrium of the system water + ethanol + heptane at 101.3 kPa
• Vapour liquid equilibrium data for the hydrogen sulphide + n-heptane system at temperatures from 293.25 to 373.22K and pressures up to about 6.9MPa
• Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
• Thermodynamics of mixtures containing amines VI. Liquid liquid equilibria for mixtures of o-toluidine + selected alkanes
• Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
• Determination and correlation of liquid liquid equilibria for four binary N,N-dimethylformamide + hydrocarbon systems
• Determination of partial molar excess enthalpies at infinite dilution for the systems four alcohols + [bmim]PF6 at different temperatures by isothermal titration calorimeter
• Phase behaviour of 1-methyl-3-octylimidazolium bis[trifluoromethylsulfonyl]imide with thiophene and aliphatic hydrocarbons: The influence of n-alkane chain length
• Thermodynamics of fuels with a biosynthetic component (III): Vapor liquid equilibrium data for the ternary mixture ethyl 1, 1-dimethylethyl ether, n-heptane and 1-hexene at T = 313.15K
• Determination and correlation of molar excess enthalpies of binary systems 2,4-pentanedione + (1-butanol, + 2-methyl-1-propanol, + 1-pentanol, + 1-heptane, + ethyl acetate, and + water)
• A study on the liquid liquid equilibria of 1-alkyl-3-methylimidazolium hexafluorophosphate with ethanol and alkanes
• Thiophene separation from aliphatic hydrocarbons using the 1-ethyl-3-methylimidazolium ethylsulfate ionic liquid
• Isobaric vapor liquid equilibria for the n-hexane + 2-isopropoxyethanol and n-heptane + 2-isopropoxyethanol 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}
• Activity coefficients at infinite dilution of alkanes and alkenes in 1-alkyl-3-methylimidazolium tetrafluoroborate
• Binary, ternary and quaternary liquid liquid equilibria in 1-butanol, oleic acid, water and n-heptane mixtures
• 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
• Liquid phase equilibria for mixtures of (an aliphatic hydrocarbon + toluene + gamma-butyrolactone)
• Phase equilibrium for the systems diisopropyl ether, isopropyl alcohol + 2,2,4-trimethylpentane and + n-heptane at 101.3 kPa
• Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
• Alkylsulfate-based ionic liquids to separate azeotropic mixtures
• (Solid + liquid) and (liquid + liquid) phase equilibria study and correlation of the binary systems {N-butyl-3-methylpyridinium tosylate + water, or + an alcohol, or + a hydrocarbon}
• Measurements of different thermodynamic properties of systems containing ionic liquids and correlation of these properties using modified UNIFAC (Dortmund)
• Alkylsulfate-based ionic liquids to separate azeotropic mixtures
• 1-Butanol + hexylamine + n-heptane at temperature range (288.15 323.15 K): Experimental density data, excess molar volumes determination and modeling with cubic EOS
• Isobaric vapor-liquid equilibria for the n-heptane + ethylene glycol monopropyl ether and n-octane + ethylene glycol monopropyl ether systems
• Liquid-liquid equilibrium and interfacial tension of the ternary system heptane + thiophene + 1-ethyl-3-methylimidazolium bis(trifluoromethanesulfonyl)imide
• Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
• Experimental and predicted excess molar enthalpies of binary mixtures containing 2,2'-oxybis[propane], benzene, butan-1-ol, 2-methylpropan-1-ol, 2-methyl-2-ene-1-propanol at 303.15 K
• 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
• Liquid densities of acetone and n-heptane and excess volumes of the binary system in a wide temperature and pressure range
• N-butylpyridinium bis-(trifluoromethylsulfonyl)imide ionic liquids as solvents for the liquid-liquid extraction of aromatics from their mixtures with alkanes: isomeric effect of the cation
• Influence of anion structure on the liquid-liquid equilibria of 1-(3-hydroxypropyl)pyridinium cation based ionic liquid-hydrocarbon binary systems
• Solubility of decanedioic acid in binary solvent mixtures
• Physical properties of 3-methyl-N-butylpyridinium tricyanomethanide and ternary LLE data with an aromatic and an aliphatic hydrocarbon at T = (303.2 and 328.2) K and p = 0.1 MPa
• Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
• Experimental determination and calculation of the critical curves for the binary systems of CO2 containing ketone, alkane, ester and alcohol, respectively
• Liquid-liquid equilibria of {n-heptane + toluene + aniline} ternary system: Experimental data and correlation
• Capacity of ionic liquids [EMim][NTf2] and [EMpy][NTf2] for extraction of toluene from mixtures with alkanes: Comparative study of the effect of the cation
• Isobaric vapor-liquid equilibrium for four binary systems of thiophene
• Phase equilibrium properties of the ternary mixture dibutyl ether + toluene + heptane at 313.15 K
• Ternary liquid-liquid equilibria of bis(trifluoromethylsulfonyl)-amide based ionic liquids + methanol + heptane
• Liquid-liquid equilibria of mixtures with ethyl lactate and various hydrocarbons
• Isobaric vapor-liquid equilibrium for four binary systems of 3-methylthiophene
• Ternary liquid-liquid equilibria of bis(trifluoromethylsulfonyl)-amide based ionic liquids + thiophene + n-heptane. The influence of cation structure
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid ethyl(2-hydroxyethyl)dimethyl-ammonium diethylphosphate using gas liquid chromatography
• Validation of a new apparatus using the dynamic method for determining the critical properties of binary mixtures containing CO2 and a n-alkane
• 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
• Vapour liquid equilibria and excess enthalpies of the binary mixtures 1-pentanol with 2,2,4-trimethylpentane or n-heptane
• A novel static analytical apparatus for phase equilibrium measurements
• Ternary liquid liquid equilibria of trifluorotris(perfluoroethyl)phosphate based ionic liquids + methanol + heptane
• Ternary (liquid liquid) equilibria of nitrate based ionic liquid + alkane + benzene at 298.15 K: Experiments and correlation
• Separation of toluene from n-heptane using monocationic and dicationic ionic liquids
• Liquid-liquid equilibria containing fluorous solvents as environmentally benign solvent
• (Liquid-liquid) equilibria for ternary and quaternary systems of representative compounds of gasoline + methanol at 293.15 K: Experimental data and correlation
• Isobaric vapor-liquid equilibrium for binary systemsof toluene + o-xylene, benzene + o-xylene, nonane + benzene and nonane + heptane at 101.3 kPa
• Isobaric vapor-liquid equilibrium for systems containing sulfur compounds
• Using binary mixtures of dicationic ionic liquids for determination ofactivity coefficients at infinite dilution by gas-liquid chromatography
• Capacity of two 1-butyl-1-methylpyrrolidinium-based ionic liquidsfor the extraction of ethanol from its mixtures with heptane and hexane
• Enthalpies and Gibbs free energies of solvation in ethylene glycol at298 K: Influence of the solvophobic effect
• A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
• Liquid-liquid equilibrium in binary systems of isomeric C8 aliphatic monoethers with nitromethane
• A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
• Interfacial tension of binary mixtures exhibiting azeotropic behavior: Measurement and modeling with PCP-SAFT combined with Density Gradient Theory
• Ternary liquid-liquid equilibria of trifluorotris(perfluoroethyl)phosphate based ionic liquids + benzothiophene + heptane
• Extraction of toluene from alkane using [Bmim][NO3] or [Omim][NO3] ionic liquid at 298.15 K and atmospheric pressure
• Prediction and measurement of phase equilibria for the extraction of BTX from naphtha reformate using BMIMPF6 ionic liquid
• Liquid-liquid extraction of toluene from n-heptane by {[emim][TCM] + [emim][DCA]} binary ionic liquid mixtures
• Extraction of benzene, ethylbenzene, and xylenes from n-heptane using binary mixtures of [4empy][Tf2N] and [emim][DCA] ionic liquids
• Liquid-liquid equilibria for multicomponent mixtures of 2,2-dimethyl-1,3-dioxolane with n-heptane, toluene, ethanol and water
• tert-Butyl chloride as a probe of the solvophobic effects
• Thermodynamic behaviour of second generation biofuels: Vapour liquid equilibria and excess enthalpies of the binary mixtures 2-pentanol and n-heptane or 2,2,4-trimethylpentane
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
• Liquid liquid equilibria for ternary systems ethanol + heptane + phosphoric-based ionic liquids
• Thermodynamic study of heptane + amine mixtures. V. Excess and solvation Gibbs energies
• Vapor liquid equilibria of {n-heptane + toluene + [emim][DCA]} system by headspace gas chromatography
• Separation of azeotropic mixtures using high ionicity ionic liquid based on 1-ethyl-3- methylimidazolium thiocyanate
• Vapour liquid equilibrium at T = 308.15 K for binary systems: Dibromomethane + n-heptane, bromotrichloromethane + n-heptane, bromotrichloromethane + dibromomethane, bromotrichloromethane + bromochloromethane and dibromomethane + bromochloromethane. Experimental data and modelling
• Separation of pyridine from heptane with tricyanomethanide-based ionic liquids
• Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
• Extraction of aromatic nitrogen compounds from heptane quinolinium and isoquinolinium based ionic liquids
• Phase equilibrium for ternary liquid systems of water + di-(2- ethylhexyl)phosphoric acid + organic diluents: Thermodynamic study
• 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
• Liquid-liquid equilibria for ternary mixtures of 2,2-dimethyl-1,3-dioxolane-4-methanol with n-heptane, toluene, ethanol and water
• Vapour-liquid equilibria of the ternary mixture (1-pentanol + 2,2,4-trimethylpentane + heptane) and the binary mixture (2,2,4-trimethylpentane + heptane) at T = 313.15 K for the characterization of second generation biofuels.
• Solution thermodynamics of simvastatin in pure solvents and binary solvent mixtures
• Experimental study on liquid - liquid equilibria of ionic liquids + alkane + ethyl benzene or p-xylene at 298.15 K
• Experimental and predicted vapour-liquid equilibrium of the binary mixtures n-heptane + chlorobutane isomers
• Extraction of benzene from heptane with pyridinium based ionic liquid at (298.15, 308.15 and 318.15) K
• Liquid-liquid equilibria in the ternary and multicomponent systems involving hydrocarbons, thiophene or pyridine and ionic liquid (1-benzyl-3-metylimidazolium bis(trifluorometylsulfonyl)imide)
• Solubility of heptane in aqueous solutions of methyldiethanolamine (MDEA)
• 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
• Vapor-liquid equilibria for n-heptane + (benzene, toluene, pxylene, or ethylbenzene) + {[4empy][Tf2N] (0.3) + [emim][DCA] (0.7)} binary ionic liquid mixture
• Liquid-liquid equilibria for the extraction of phenols from alkane using ethylene glycol
• Effect of cation alkyl chain length on liquid-liquid equilibria of {ionic liquids + thiophene + heptane}: COSMO-RS prediction and experimental verification
• Quantitative comparison between predicted and experimental binary n-alkane p benzene phase behaviors using cubic and PC-SAFT EOS
• Determination of solubility parameters from density measurements for non-polar hydrocarbons at temperatures from (298 to 433) K and pressures up to 137 MPa
• Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 K
• Effect of polarity and temperature on the binary interaction between D2EHPA extractant and organic solvents (kerosene, n-heptane, chlorobenzene and 1-octanol): Experimental and thermodynamics
• Measurement and prediction of liquid-liquid equilibria in ternary systems containing water, an organic component, and cyclohexanol
• Application of 1-hexyl-3-methylimidazolium trifluoromethanesulfonate to the removal of alcohol from mixtures with heptane
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
• Quaternary isothermal vapor-liquid equilibrium of the model biofuel 2-butanone + n-heptane + tetrahydrofuran + cyclohexane using Raman spectroscopic characterization
• 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
• Extraction of benzothiazole and thiophene from their mixtures with n-heptane using tetrahexylammonium bromide-based deep eutectic solvents as extractive denitrogenation and desulfurization agents
• New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
• Liquid-liquid equilibria of n-heptane, methanol and deep eutectic solvents composed of carboxylic acid and monocyclic terpenes
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Separation of thiophene, or benzothiophene from model fuel using glycols. Liquid-liquid phase equilibria and oxidative desulfurization study
• Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
• Density of biofuel mixtures (Dibutyl ether + Heptane) at temperatures from (298.15-393.15) K and at pressures up to 140 MPa: Experimental data and PC-SAFT modeling
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• The determination of activity coefficients at infinite dilution using g.l.c. for hydrocarbons in furfural at T = 278:15 K and T = 298:15 K
• Thermodynamic properties of (an ester + an alkane). XVI. Experimental HEm and V Em values and a new correlation method for (an alkyl ethanoate + an n-alkane) at 318.15 K
• Activity coefficients at infinite dilution for hydrocarbons in furfuryl alcohol at T=(278.15 and 298.15) K, determined by g.l.c.
• Ternary (liquid + liquid) equilibria for mixtures of 1-hexyl-3-methylimidazolium (tetrafluoroborate or hexafluorophosphate) + benzene + an alkane at T = 298.2 K and p = 0.1 MPa
• Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
• Thermodynamic and acoustic properties of binary mixtures of alcohols and alkanes. I. Speed of sound in (ethanol + n-heptane) under elevated pressures
• Thermodynamic and acoustic properties of binary mixtures of alcohols and alkanes. II. Density and heat capacity of (ethanol + n-heptane) under elevated pressures
• Thermodynamic properties of (an ester + and alkane). XVII. Experimental He and Ve values for (an alkyl propanoate + an alkane) at 318.15K
• 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
• 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)
• Experimental measurements and prediction of liquid densities for n-alkane mixtures
• Measurement of activity coefficients at infinite dilution using polar and non-polar solutes in the ionic liquid 1-methyl-3-octyl-imidazolium diethyleneglycolmonomethylethersulfate at T = (288.15, 298.15, and 313.15) K
• Excess molar heat capacities for (decan-1-ol + n-heptane) at temperatures from (290 to 318) K. Experimental results and theoretical description using the ERAS model
• 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
• High-pressure (vapor + liquid) equilibria in the (nitrogen + n-heptane) system
• (Liquid + liquid) equilibria of three ternary systems: (heptane + benzene + N-formylmorpholine), (heptane + toluene + N-formylmorpholine), (heptane + xylene + N-formylmorpholine) from T = (298.15 to 353.15) K
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• Mixing properties of binary mixtures presenting azeotropes at several temperatures
• Thermodynamic study of (perfluoroalkane + alkane) mixtures: Excess and solvation enthalpies
• (Liquid + liquid) equilibria of {heptane + xylene + N-formylmorpholine} ternary system
• Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
• Excess properties and vapour pressure of (3-diethylaminopropylamine + n-alkanes)
• Solvent extraction of thiophene from n-alkanes (C7, C12, and C16) using the ionic liquid [C8mim][BF4]
• Phase equilibria for mixtures containing nonionic surfactant systems: Modeling and experiments
• Measurement and correlation of the (p, ?, T) relation of liquid n-heptane, n-nonane, 2,4-dichlorotoluene, and bromobenzene in the temperature range from (233.15 to 473.15) K at pressures up to 30 MPa for use as density reference liquids
• 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
• Thermodynamic and acoustic properties of (heptane + dodecane) mixtures under elevated pressures
• Measurement and correlation of (vapor + liquid) equilibria for the {2-propoxyethanol (C3E1) + n-hexane} and the {2-propoxyethanol (C3E1) + n-heptane} systems
• Experimental and theoretical study of surface tension of binary mixtures of (n-alkyl acetates + heptane, benzene, and toluene)
• Molar heat capacities for (2-methyl-2-butanol + heptane) mixtures and cyclopentanol at temperatures from (284 to 353) K
• Phase diagrams of (hexane + methanol + 2,2,2-trifluoroethanol) at three temperatures: Measurement and correlation
• Thermodynamics of biofuels: Excess enthalpies for binary mixtures involving ethyl 1,1-dimethylethyl ether and hydrocarbons at different temperatures using a new flow calorimeter
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
• Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
• Experimental densities, refractive indices, and speeds of sound of 12 binary mixtures containing alkanes and aromatic compounds at T = 313.15 K
• (Liquid + liquid) equilibria for ternary mixtures of (alkane + benzene + [EMpy] [ESO4]) at several temperatures and atmospheric pressure
• Thermodynamic properties of solvation of aromatic compounds in cyclohexane, heptane, benzene, 1,4-dioxane, and chloroform at 298.15 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
• Excess enthalpies of binary and ternary mixtures containing dibutyl ether (DBE), 1-butanol, and heptane at T = 298.15 K and 313.15 K
• Experimental and theoretical study of surface tension of n-pentane, n-heptane, and some of their mixtures at different temperatures
• (Liquid + liquid) equilibria in the binary systems (aliphatic, or aromatic hydrocarbons + 1-ethyl-3-methylimidazolium ethylsulfate, or 1-butyl-3-methylimidazolium methylsulfate ionic liquids)
• Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
• Speed of sound, density, and heat capacity for (2-methyl-2-butanol + heptane) at pressures up to 100 MPa and temperatures from (293 to 318) K. Experimental results and theoretical investigations
• (Liquid + liquid) equilibria of (heptane, or hexane, or cyclohexane + toluene + 1,3- dimethyl-2-imidazolidinone) ternary systems at T = 298.15 K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-octyl-3-methylimidazolium hexafluorophosphate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
• Evaluation of the polysubstituted pyridinium ionic liquid [hmmpy][Ntf2] as a suitable solvent for desulfurization: Phase equilibria
• 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
• Separation of toluene and heptane by liquid liquid extraction using z-methyl-N-butylpyridinium tetrafluoroborate isomers (z = 2, 3, or 4) at T = 313.2 K
• Separation of benzene from alkanes by solvent extraction with 1-ethylpyridinium ethylsulfate ionic liquid
• Separation of aromatic hydrocarbons (toluene or benzene) from aliphatic hydrocarbon (n-heptane) by extraction with ethylene carbonate
• Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
• Volumetric and acoustic behaviour of systems containing n-hexane, or n-heptane and isomeric chlorobutanes
• Activity coefficients at infinite dilution of organic solutes in N-alkylpyridinium bis(trifluoromethylsulfonyl)imide ([CnPY][NTf2], n = 2, 4, 5) using gas liquid chromatography
• Permittivity and density of the systems (monoglyme, diglyme, triglyme, or tetraglyme + n-heptane) at several temperatures
• 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
• Thermodynamic study of (heptane + amine) mixtures. II. Excess and partial molar volumes at 298.15 K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Quaternary isobaric (vapor + liquid + liquid) equilibrium and (vapor + liquid) equilibrium for the system (water + ethanol + cyclohexane + heptane) at 101.3 kPa
• Thermodynamic study of (heptane + amine) mixtures. III: Excess and partial molar volumes in mixtures with secondary, tertiary, and cyclic amines at 298.15 K
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
• (Liquid + liquid) equilibrium for ternary mixtures of {heptane + aromatic compounds + [EMpy][ESO4]} at T = 298.15 K
• 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
• (Liquid + liquid) equilibrium for the ternary systems {heptane + toluene + 1-allyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide} and {heptane + toluene + 1-methyl-3-propylimidazolium bis(trifluoromethylsulfonyl)imide} ionic liquids
• Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
• Thermodynamic properties of biofuels: Heat capacities of binary mixtures containing ethanol and hydrocarbons up to 20 MPa and the pure compounds using a new flow calorimeter
• Compressed liquid densities for the (n-heptane + n-decane) and (n-octane + n-decane) systems from T = (313 to 363) K
• Alkylsulfate-based ionic liquids in the liquid-liquid extraction of aromatic hydrocarbons
• Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• (Liquid + liquid) equilibrium for binary systems of N-formylmorpholine with alkanes
• Solubilities of some organic solutes in 1-ethyl-3-methylimidazolium acetate. Chromatographic measurements and predictions from COSMO-RS
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
• (Liquid + liquid) equilibria for the ternary mixtures (alkane + toluene + ionic liquid) at T = 298.15 K: Influence of the anion on the phase equilibria
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium hexafluorophosphate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 363.15) K
• Determination of infinite dilution activity coefficients using HS-SPME/GC/FID for hydrocarbons in furfural at temperatures of (298.15, 308.15, and 318.15) K
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
• Ternary (liquid + liquid) equilibria of {trifluorotris(perfluoroethyl)phosphate based ionic liquids + thiophene + heptane}
• 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
• Application of [HMim][NTf2], [HMim][TfO] and [BMim][TfO] ionic liquids on the extraction of toluene from alkanes: Effect of the anion and the alkyl chain length of the cation on the LLE
• 1-Alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ionic liquids as solvents in the separation of azeotropic mixtures
• Liquid-liquid extraction of aromatics from their mixtures with alkanes using 1-methyl 3-octylimidazolium thiocyanate ionic liquid
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
• 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
• (Liquid + liquid) equilibria of aqueous solutions of butyric acid with n-heptane and toluene at T = (298.2, 308.2, and 318.2) K
• Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
• 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
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
• Application of 1-alkyl-3-methylpyridinium bis(trifluoromethylsulfonyl)imide ionic liquids for the ethanol removal from its mixtures with alkanes
• Liquid liquid equilibria for ternary systems of (ethylene glycol + toluene + heptane) at temperatures (303.15, 308.15, and 313.15) K and atmospheric pressure: Experimental results and correlation with UNIQUAC and NRTL models
• 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
• Separation of thiophene from heptane with ionic liquids
• Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
• Activity coefficients at infinite dilution of organic solutes in N-formylmorpholine and N-methylpyrrolidone from gas-liquid chromatography
• Measurement of critical temperatures and critical pressures for binary mixtures of methyl tert-butyl ether (MTBE) + alcohol and MTBE + alkane
• Phase equilibria study of the (N-octylisoquinolinium thiocyanate ionic liquid + aliphatic and aromatic hydrocarbon, or thiophene) binary systems
• Thermodynamics of solvation and solvophobic effect in formamide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
• Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
• Solvent extraction of aromatic sulfur compounds from n-heptane using the 1-ethyl-3-methylimidazolium tricyanomethanide ionic liquid
• Liquid density of biofuel mixtures: 1-Heptanol + heptane system at pressures up to 140 MPa and temperatures from 298.15 K to 393.15 K
• Experimental and theoretical excess molar enthalpies of ternary and binary mixtures containing 2-Methoxy-2-Methylpropane, 1-propanol, heptane
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Cation effect of ammonium imide based ionic liquids in alcohols extraction from alcohol-alkane azeotropic mixtures
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
• The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
• 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
• Separation of sulfur compounds from alkanes with 1-alkylcyanopyridinium-based ionic liquids
• 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
• Selective extraction of toluene from n-heptane using [emim][SCN] and [bmim][SCN] ionic liquids as solvents
• Effect of the alkyl side chain of the 1-alkylpiperidinium-based ionic liquids on desulfurization of fuels
• Measurement and correlation of critical properties for binary mixtures and ternary mixtures containing gasoline additives
• Quaternary (liquid + liquid) equilibrium data for the extraction of toluene from alkanes using the ionic liquid [EMim][MSO4]
• Application of 1-pentyl-3-methylimidazolium bis(trifluoromethylsulfonyl) imide for desulfurization, denitrification and dearomatization of FCC gasoline
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium methyl sulfate
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Extraction desulfurization process of fuels with ionic liquids
• Thermodynamics of solvation in propylene glycol and methyl cellosolve
• Ternary (liquid + liquid) equilibria of {trifluorotris(perfluoroethyl) phosphate based ionic liquids + thiophene + heptane}: Part 2
• Phase equilibria study of binary systems comprising an (ionic liquid + hydrocarbon)
• Solvation parameter model and thermodynamic parameters in a dicationic ionic liquid based on pyrrolidinium
• Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Refractive indices and static permittivities of systems containing n-hexane or n-heptane and isomeric chlorobutanes
• (Liquid + liquid) extraction of methanol from alkanes using dialkylphosphate-based ionic liquids as solvents
• Thermodynamic models for determination of the solubility of (-)-shikimic acid in different pure solvents and in (H2O + ethanol) binary solvent mixtures
• 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
• Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
• Use of selective ionic liquids and ionic liquid/salt mixtures as entrainer in a (vapor + liquid) system to separate n-heptane from toluene
• 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
• (Liquid + liquid) equilibrium of ternary and quaternary systems containing heptane, cyclohexane, toluene and the ionic liquid [EMim][N(CN)2]. Experimental data and correlation
• (Liquid + liquid) equilibria measurements for ternary systems (sulfolane + a carboxylic acid + n-heptane) at T = 303.15 K and at 0.1 MPa
• Contributing to accurate high pressure viscosity measurements: Vibrating wire viscometer and falling body viscometer techniques
• Mutual diffusion coefficients of isopropanol + n-heptane and isobutanol + n-heptane
• Selective recovery of aliphatics from aromatics in the presence of the {[4empy][Tf2N] + [emim][DCA]} ionic liquid mixture
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• 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
• Isothermal vapour-liquid equilibrium data for the binary systems of (CHF3 or C2F6) and n-heptane
• 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
• Surface tension and density of mixtures of m-xylene + n-alkane at 293.15 K: Analysis under the extended Langmuir and Shereshefsky models
• Liquid-liquid equilibrium measurements and correlation for phase behaviors of alcohols + heptane + ILs ternary systems
• Determination of melting temperatures in hydrocarbon mixtures by differential scanning calorimetry
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Mutual diffusion coefficients of n-butanol + n-heptane and n-pentanol + n-heptane from 288.15 K to 318.15 K
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• Conformational analysis of branched alkanes using limiting partial molar volumes
• Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
• 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]
• Removal of 2- and 3-methylthiophene from their mixtures with n-heptane using tetrahexylammonium bromide-based deep eutectic solvents as extractive desulfurization agents
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Improving the method of solution calorimetry for evaluation of the enthalpies of phase transitions and condensed state enthalpies of formation
• Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
• Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
• Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
• Liquid-liquid extraction of sulfur compounds from heptane with tricyanomethanide based ionic liquids
• Mutual diffusion coefficients of 3-methyl-1-butanol + n-heptane and 2-methyl-1-butanol + n-heptane from 288.15 K to 318.15 K
• Isobaric vapor-liquid equilibrium of three binary systems containing dimethyl succinate, dimethyl glutarate and dimethyl adipate at 2, 5.2 and 8.3 kPa
• Determination and correlation of solubility and solution thermodynamics of musk xylene in different pure solvents
• Liquid-liquid equilibria for (2-hydroxy benzaldehyde + n-alkane) mixtures. Intermolecular and proximity effects in systems containing hydroxyl and aldehyde groups
• Excess volumes, densities, speeds of sound and viscosities for the binary systems of diisopropyl ether with hydrocarbons at 303.15K
• Thermophysical properties and thermodynamic phase behavior of ionic liquids
• Topological and thermodynamic investigations of binary mixtures: Molar excess volumes, molar excess enthalpies and isentropic compressibility changes of mixing
• Experimental determination and modelling of densities and excess molar volumes of ternary system (1-butanol + cyclohexylamine + n-heptane) and corresponding binaries from 288.15 to 323.15K
• Excess molar volumes and isentropic compressibilities changes of mixing of tetrahydropyran + benzene + cyclo or n-alkanes ternary mixtures at 308.15 K
• Thermodynamic properties of binary mixtures containing Tetrahydropyran: Excess molar volumes, Excess molar enthalpies and isentropic compressibilities changes of mixing
• THERMODYNAMICS OF MIXTURES CONTAINING ALKOXYETHANOLS. XXVIII. LIQUID-LIQUID EQUILIBRIA FOR 2-PHENOXYETHANOL + SELECTED ALKANES
• Thermophysical Study of the n-Hexane or n-Heptane with 1- Chloropropane Systems
• Excess molar volumes of (1-chlorobutane +heptane + 2-butanone or 2-pentanone) at 288.15 , 303.15 and 313.15 K . Measurements and correlations.
• Determination of the solubility, dissolution enthalpy and entropy of 3-pentadecylphenyl acrylate in different organic solvents
• Correlation and prediction of the phase behavior and thermal properties of binary and ternary systems of 2,2 -oxybis[propane] + benzene, toluene, cyclohexane or n-heptane
• Solvation of N-methyl-2-pyrrolidone and N,N-dimethylpropanamide in cyclohexane, heptane, n-alkan-1-ols(C1-C4) and water at 298.15K
• THERMODYNAMICS OF MIXTURES CONTAINING AMINES. XIV. CpEm OF BENZYLAMINE WITH HEPTANE AT 293.15 K OR WITH METHANOL, 1-PROPANOL OR 1-PENTANOL AT (293.15-308.15) 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
• Excess properties from p.rho.T data for n-heptane + isomeric chlorobutane mixtures
• 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
• Standard molar Gibbs free energy and enthalpy of solvation of lowpolar solutes in formamide derivatives at 298 K
• 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
• Thermal transport properties of heptane-isooctane mixtures
• Temperature and pressure dependence of densities and viscosities for binary mixtures of methyl decanoate plus n-heptane
• 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
• Capillary Viscometer and Vibrating Tube Densimeter for Simultaneous Measurements up to 70 MPa and 423 K
• Phase Equilibria in Systems of Morpholine, Acetonitrile, and n-Alkanes
• Solubility Measurement and Correlation for 2- Naphthaldehyde in Pure Organic Solvents and Methanol + Ethanol Mixtures
• Experimental and Computational Study on Liquid Liquid Equilibrium in Ternary Systems of -Valerolactone, Toluene, and Hydrocarbons
• Experimental and Modeling Study of the Phase Behavior of (Heptane + Carbon Dioxide + Water) Mixtures
• Vapor Liquid Equilibria of n-Heptane + Toluene +1-Ethyl-4-methylpyridinium Bis(trifluoromethylsulfonyl)imide Ionic Liquid
• Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
• Solubility of Ethene in n-Hexane and n-Heptane as Common Slurry-Phase Polymerization Solvents: Experimental Measurement and Modeling
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
• 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
• Vapor Liquid Equilibria Measurements for Di-n-Propyl Ether and Butyl Ethyl Ether with n-Heptane
• 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
• Measurement and Correlation of Liquid Liquid Equilibrium for Quaternary Systems of Water + Methanol or Ethanol + Ethyl Methyl Carbonate + Heptane at 25 deg C
• L(+)-tartaric Acid Separations Using Aliquat 336 in n-Heptane, Kerosene, and 1-Octanol at 300 +- 1 K
• Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
• Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
• Phase Behavior of the System (Carbon Dioxide + n-Heptane + Methylbenzene): A Comparison between Experimental Data and SAFT-gamma-Mie Predictions
• 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
• Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
• Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
• Extraction of Low Concentration Aqueous Solution of Methylal: Liquid Liquid Equilibrium in Water + Methylal + (Cyclohexane and n-Heptane) Ternary Systems
• Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
• Liquid-Liquid Extraction of Butanol from Heptane + Butanol Mixture by Ionic Liquids
• Experimental Vapor-Liquid Equilibria and Thermodynamic Modeling of the Methanol + n-Heptane and 1-Butanol + Aniline Binary Systems
• Isobaric Vapor-Liquid Equilibrium for Two Binary Systems of n-Heptane + sec-Butyl Acetate and Methylcyclohexane + sec-Butyl Acetate under Atmosphere
• Density of Working Liquids for Diffusion Vacuum Pumps
• 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
• Measurement of the Speed of Sound in Near-Critical and Supercritical n-Heptane at Temperatures from (513.40 to 650.90) K and Pressures from (2.5 to 10.0) MPa
• Liquid Density of Mixtures of Methyl Nonafluorobutyl Ether (HFE-7100) + n-Heptane at Pressures up to 80 MPa and Temperatures from 298.15 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
• Solubilities of Organic Semiconductors and Nonsteroidal Anti-inflammatory Drugs in Pure and Mixed Organic Solvents: Measurement and Modeling with Hansen Solubility Parameter
• Measurement of Critical Properties for Binary and Ternary Mixtures Containing n-Butanol and n-Alkane
• 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
• A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol
• Experimental Study on Reactive Extraction of Malonic Acid with Validation by Fourier Transform Infrared Spectroscopy
• Solubility Determination and Correlation of Warfarin Sodium 2-Propanol Solvate in Pure, Binary, and Ternary Solvent Mixtures
• Separation of Alkylbenzenes from n-Heptane Using Binary Mixtures of Ionic Solvents
• Liquid Liquid Equilibrium Data for the Separation of Acetone from n-Heptane Using Four Imidazolium-Based Ionic Liquids
• Solubilities of 2,6-Dimethylnaphthalene in Six Pure Solvents and Two Binary Solvent Systems
• Effect of Diluents on Extraction Equilibrium of trans-Aconitic Acid
• Measuring Activity Coefficient at Infinite Dilution of Hydrocarbons in Ionic Liquids and Evaluation of Other Thermodynamic Properties using Gas Chromatography
• Liquid-Liquid Equilibrium for Ternary Systems of N-Methylformamide + Pyrrole/Indole + Alkanes at 298.15 K: Phase Equilibrium Measurement and Correlation
• (r, VE, T) Measurements of the Ternary Mixture (Dibutyl Ether + 1-Heptanol + Heptane) at Temperatures up to 393.15 K and Pressures up to 140 MPa and Modeling Using the Peng-Robinson and PC-SAFT Equations of State
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• Liquid-Liquid Equilibrium Data for Ternary Systems Containing Alkanes (n-Pentane, n-Hexane, n-Heptane, and n-Octane) + Alcohol (Methanol and Ethanol) + Protic Ionic Liquid (2-HEAF)
• Liquid-Liquid Equilibrium Measurements for the Extraction of Pyridine and Benzothiazole from n-Alkanes Using Deep Eutectic Solvents
• Measurement of VLE Data by Using an Experimental Installation with Automatic Control: Modeling of Binary Systems of Methyl Acetate or Ethyl Acetate with n-Heptane or 2,2,4-Trimethylpentane at Both 0.1 and 1.5 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
• Surface Tension of Pure Liquids and Binary Liquid Mixtures
• 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
• Determination of Isobaric Thermal Expansivity of Organic Compounds from 0.1 to 30 MPa at 30 C with an Isothermal Pressure Scanning Microcalorimeter
• Ternary Liquid-Liquid Equilibria for Mixtures of 1-Methyl-3-octylimidazolium Chloride + an Alkanol + an Alkane at 298.2 K and 1 bar
• 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.
• Bubble Temperature Measurements on the Binary Mixtures of n-Heptane or Nitrobenzene or Chlorobenzene with Some Chloroethanes and Chloroethylenes at (94.6 to 95.8) kPa
• Isobaric Vapor-Liquid Equilibria and Excess Properties for the Binary Systems of Methyl Esters + Heptane
• Measurement of Activity Coefficients of Solutes at Infinite Dilution in (Dimethyl Sulfoxide + Acetamide, or Formamide, or Urea) Using Gas Liquid Chromatography at the Temperature 298.15 K
• Speed of Sound in Propan-1-ol + Heptane Mixtures under Elevated Pressures
• Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
• 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
• 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
• Volumetric Properties of Binary Tetraethylene Glycol Dimethyl Ether + Heptane Mixtures between (278.15 and 353.15) K and up to 25 MPa
• Surface Tension and Interfacial Tension of Binary Organic Liquid Mixtures
• Isothermal Vapor-Liquid Equilibria for the 2-Propanol + n-Heptane System near the Critical Region
• Analysis and Evaluation of the Liquid-Liquid Equilibrium Data of the Extraction of Aromatics from Hydrocarbons by Tetraethylene Glycol
• Determination and Study on the Solubility of Methane in Heptane + Cyclohexane and Heptane + Ethanol at High Pressures
• Solubilities of Bis (2,2,6,6-Tetramethyl-4-Piperidinyl) Maleate in Hexane, Heptane, Octane, m-Xylene and Tetrahydrofuran from (253.15 to 310.15) K
• Liquid-Liquid Equilibria for Monoethylene Glycol + Water + Alkane Systems in the Range (273 to 313) K and Atmospheric Pressure
• Vapor Pressures of n-Heptane Determined by Comparative Ebulliometry
• Compressed Liquid Densities of Squalane and Pentaerythritol Tetra(2-ethylhexanoate)
• Liquid-Liquid Equilibrium for the System Heptane + o-Xylene + Diethylene Glycol over the Temperature Range of 288.15 K to 318.15 K
• Phase Separation in Binary Mixtures Containing Linear Perfluoroalkanes
• Experimental Dynamic Viscosities of 2,3-Dimethylpentane up to 60 MPa and from (303.15 to 353.15) K Using a Rolling-Ball Viscometer
• Vapor-Liquid Equilibrium Data for the Binary Decafluoropentane (HFC-43-10meec) + Heptane, Decafluoropentane + Butyl Ethyl Ether, Octafluorobutane (HFC-338pcc) + Butyl Ethyl Ether, and Heptafluoro Propyl Methyl Ether (HFE-347mcc) + HFC-338pcc Systems at 101.3 kPa
• Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
• Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
• Determination of Activity Coefficients at Infinite Dilution of Polar and Nonpolar Solutes in the Ionic Liquid 1-Ethyl-3-methyl- imidazolium Bis(trifluoromethylsulfonyl) Imidate Using Gas-Liquid Chromatography at the Temperature 303.15 K or 318.15 K
• 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
• Surface and interfacial tension of the ternary system heptane + toluene + N,N-dimethylformamide
• Vapor-Liquid Equilibria for the Ternary Systems of Methyl tert-Butyl Ether + Methanol + Methylcyclohexane and Methyl tert-Butyl Ether + Methanol + n-Heptane and Constituent Binary Systems at 313.15 K
• 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
• Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
• Ternary and Quaternary Liquid-Liquid Equilibria of Water + Methanol + Diisopropyl Ether and Water + Methanol + Diisopropyl Ether + Toluene Mixtures
• High-Pressure Density Measurements for the Binary System Ethanol + Heptane
• 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
• 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 Equilibria for Ternary Mixtures (an Ionic Liquid + Benzene +Heptane or Hexadecane) at T ) 298.2 K and Atmospheric Pressure
• Determination and Study of the Solubility of Methane in Mixtures of Methanol plus Various Hydrocarbons at High Pressures
• Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Water + Cyclohexylamine + Aromatic Hydrocarbon (Toluene or Propylbenzene) or Aliphatic Hydrocarbon (Heptane or Octane)
• Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• 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
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
• Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
• Heat Capacity, Speed of Ultrasound, and Density for 1,5-Dibromopentane + Heptane within the Temperature Range from 293.15 K to 313.15 K
• Thermodynamics of Fuels with a Biosynthetic Component: Vapor-Liquid Equilibrium Data for Binary and Ternary Mixtures Containing Ethyl 1,1-Dimethylethyl Ether, n-Heptane, and Toluene at T ) 313.15 K
• Excess Molar Volumes at 298.15 K and Isothermal Vapor-Liquid Equilibria at 333.15 K for the Binary Mixtures of Dimethyl Carbonate with Benzene, Toluene, n-Heptane, and Isooctane
• Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Binary Mixtures at 298.15 K
• Infinite Dilution Activity Coefficients for Trihexyltetradecyl Phosphonium Ionic Liquids: Measurements and COSMO-RS Prediction
• Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K
• Vapor-Liquid Equilibrium for Binary System of Diethyl Sulfide + n-Heptane and Diethyl Sulfide + 2,2,4-Trimethylpentane at (363.15 and 353.15) K
• Solubility of Anthracene in Binary Diisopropyl Ether + Alkane Solvent Mixtures at 298.15 K
• Solubility of 5-(Dithiolan-3-yl)pentanoic Acid in the Mixed Solvents of Cyclohexane + Ethyl Acetate, Heptane + Ethyl Acetate, and Hexane + Ethyl Acetate
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
• Solubility of Artemisinin in Different Single and Binary Solvent Mixtures Between (284.15 and 323.15) K and NRTL Interaction Parameters
• Separation of Benzene from Linear Alkanes (C6-C9) Using 1-Ethyl-3-Methylimidazolium Ethylsulfate at T = 298.15 K
• Interfacial Tension of n-Alkane and Ionic Liquid Systems
• Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
• Experimental Determination of Densities and Refractive Indices of the Ternary Mixture 2-Methyl-2-propanol + Cyclohexylamine + n-Heptane at T = (303.15 to 323.15) K
• Solvent Extraction of Toluene from Heptane with the Ionic Liquids N-Ethylpyridinium Bis(trifluoromethylsulfonyl)imide and z-Methyl-N-ethylpyridinium Bis(trifluoromethylsulfonyl)imide (z = 2, 3, or 4) at T = 313.2 K
• Thermodynamic and Acoustic Properties of Mixtures of 1,6-Dichlorohexane with Heptane from (293 to 313) K
• Measurement of Heat Capacity by Adiabatic Calorimetry and Calculation of Thermodynamic Functions of Standard Substances: Copper, Benzoic Acid, and Heptane (For Calibration of an Adiabatic Calorimeter)
• Solubility of Benzoic Acid in Pure Solvents and Binary Mixtures
• Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Aliphatic Hydrocarbons (Heptane or Octane) + Phenols + Water
• Influence of Compressed Carbon Dioxide on the Capillarity of the Gas-Crude Oil-Reservoir Water System
• Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
• Liquid-Liquid Equilibria Measurement of Systems Involving Alkanes (Heptane and Dodecane), Aromatics (Benzene or Toluene), and Furfural
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Solubilities of Phenylphosphinic Acid, Methylphenylphosphinic Acid, Hexachlorocyclotriphosphazene, and Hexaphenoxycyclotriphosphazene in Selected Solvents
• Liquid-Liquid Extraction of Toluene from Heptane Using 1-Alkyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide Ionic Liquids
• Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
• Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
• Measurement and Correlation for the Solubilities of Dihydrocapsaicin in n-Heptane, n-Hexane, n-Pentane, Ethyl Acetate, Acetone, Ethanol, and Water
• Influence of Anion Structure on the Liquid-Liquid Equilibria of 1-Ethyl-3-methyl-imidazolium Cation Based Ionic Liquid-Hydrocarbon Binary Systems
• Vapor-Liquid Equilibrium in the Binary Systems 2-Butanol + tert-Amyl Methyl Ether, 2-Butanol + Heptane, and Heptane + tert-Amyl Methyl Ether
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Butyl-3-methylimidazolium Nitrate Using Gas-Liquid Chromatography
• Solubility of 2-(2,4,6-Trichlorophenoxy)ethyl Bromide in Methanol, Ethanol, Propanol, Isopropanol, Acetonitrile, n-Heptane, and Acetone
• Solubilities of 1-Hexyl-3-methylimidazole Nitrate and 1-Octyl-3-methylimidazole Nitrate in Selected Solvents
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Ethyl-3-methylimidazolium Diethylphosphate Using Gas Liquid Chromatography
• Sulfonate-Based Ionic Liquids in the Liquid Liquid Extraction of Aromatic Hydrocarbons
• 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
• Interfacial Tensions of Imidazolium-Based Ionic Liquids with N-Alkanes and Cyclohexane
• Extraction of n-Alcohols from n-Heptane Using Ionic Liquids.
• 1-Alkyl-2,3-dimethylimidazolium Bis(trifluoromethylsulfonyl)imide Ionic Liquids for the Liquid Liquid Extraction of Toluene from Heptane
• 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
• Thermodynamic Study of Heptane + Silicone Mixtures. Excess Volumes and Enthalpies at 298.15 K
• Excess Properties and Vapor Pressure of 2-Diethylaminoethylamine + n-Heptane
• Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
• Vapor-Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K
• 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
• Vapor Liquid Equilibria of Binary Mixtures Containing 2-Butanol and Hydrocarbons at 313.15 K
• 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 Equilibria of Tertiary Amine and n-Alkane/Alkanol Binary Mixtures: Experimental Measurements and Modeling with GC-PPC-SAFT
• Measurements and Correlations of Liquid.Liquid Equilibria for Water + Ethanol + 1,1'-Oxybis(butane) + Methylbenzene or Heptane Mixtures at 298.15 K
• 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
• Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
• Excess Molar Volumes and Speed of Sound in Bromotrichloromethane + n-Heptane, Dibromomethane + n-Heptane, Bromotrichloromethane + Dibromomethane, and Bromotrichloromethane + Bromochloromethane at Temperatures from (293.15 to 313.15) K
• Measurements and Correlations of the Isobaric Vapor Liquid Equilibria of Binary Mixtures and Excess Properties for Mixtures Containing an Alkyl (Methyl, Ethyl) Butanoate with an Alkane (Heptane, Nonane) at 101.3 kPa
• 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
• Temperature and Composition Effect on CO2 Miscibility by Interfacial Tension Measurement
• Densities of Cresols and Linear Alkane Mixtures at High Pressure
• (p, rho, T) Behavior for the Binary Mixtures Carbon Dioxide + Heptane and Carbon Dioxide + Tridecane
• Liquid Liquid Equilibrium Data for {Heptane + Aromatic + 1-(2-Hydroxyethyl)-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide ([hemim][NTf2])} Ternary Systems
• A Promising Ionic Liquid [BMIM][FeCl4] for the Extractive Separation of Aromatic and Aliphatic Hydrocarbons
• Thermodynamics of Mixtures Containing Amines. XII. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for N-Methylaniline + Hydrocarbon Systems
• Excess Enthalpy and Excess Volume for Pyridine + Methyldiethanolamine and Pyridine + Ethanolamine Mixtures
• 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
• Vapor Liquid Equilibrium Data for the Morpholine-4-carbaldehyde + n-Hexane or n-Heptane Binary Systems Using a Static-Synthetic Apparatus
• Determination of the Relative Permittivity of Heptane at Temperatures between (303 and 363) K and Pressures below 60 MPa with a Concentric Cylinder Capacitor at a Frequency of 1 kHz
• Liquid Liquid Equilibria of Benzene + n-Heptane + N,N-Dimethylformamide and Benzene + n-Heptane + N,N-Dimethylformamide + Ammonium Thiocyanate
• Solubility and Dissolution Thermodynamic Data of Mefenamic Acid Crystals in Different Classes of Organic Solvents
• 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
• Improvements in the Experimentation and the Representation of Thermodynamic Properties (iso-p VLE and yE) of Alkyl Propanoate + Alkane Binaries
• Solubility of Dichloronitrobenzene in Eight Organic Solvents from T = (278.15 to 303.15) K: Measurement and Thermodynamic Modeling
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Experimental and Modeling of the Propene Solubility in the Heptane and Methylbenzene Solvents
• Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
• Liquid Liquid Equilibria for the Systems: Heptane + Benzene + Solvent (Propylene carbonate, N,N-Dimethylformamide, or Mixtures) at Temperatures from (303.2 to 323.2) K
• 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
• Oxygenated Compounds + Hydrocarbon Mixtures in Fuels and Biofuels: Excess Enthalpies of Ternary Mixtures Containing 1-Butoxybutane + Propan-1-ol +1-Hex-1-ene, or Heptane, or 2,2,4-Trimethylpentane at (298.15 and 313.15) K
• Liquid Liquid Equilibria for Quaternary Systems of Water + Ethanol + Diethyl Carbonate + Methylbenzene or Heptane
• Liquid Liquid Equilibrium in Mixtures Containing Propane-1,2,3-triol and Mixtures Containing Vegetable Oils at Atmospheric Pressure
• Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
• Determination of the Critical Properties of C6 C10 n-Alkanes and Their Binary Systems Using a Flow Apparatus
• Experimental Study: The Impact of Dissolved Water on the Viscosity of Reservoir Fluids at HPHT Conditions
• Selective Separation of Aromatics from Paraffins and Cycloalkanes Using Morpholinium-Based Ionic Liquid
• P ? T Data for 1-Butanol and Isobutyl Alcohol from (283.15 to 363.15) K at Pressures up to 66 MPa
• Solubility Determination and Thermodynamic Models for 2-Methylnaphthalene in Different Solvents from T = (278.15 to 303.15) K
• Binary Liquid Liquid Equilibria of ?-Valerolactone with Some Hydrocarbons
• Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
• Measurement of the Critical Properties of the Ternary Systems Hexane + Heptane + Octane and Octane + Nonane + Decane Using a Flow Apparatus
• Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
• Dialkylphosphate-Based Ionic Liquids as Solvents to Extract Toluene from Heptane
• 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
• Measurements and Calculation of Vapor-Liquid Equilibria for the Binary Mixtures of Fluorobenzene and Alkanes at a Pressure of 101.4 kPa
• 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
• Liquid Liquid Equilibria of Mixtures Containing Methyl Acetate + Methanol + Hexane or Heptane
• Diffusion Coefficients of Organic Compounds at Infinite Dilution in Mixtures Involving Associating Compounds. Experimental Determination and Modeling by Group Contribution Methods
• Influence of the Temperature on the Liquid Liquid Equilibria of Heptane + Toluene + Sulfolane and Heptane + m-Xylene + Sulfolane
• Solubilities of Stearic Acid in Organic Solvents and in Azeotropic Solvent Mixtures
• Liquid Liquid Equilibria for the Ternary Systems Water + n-Pentanoic Acid with n-Heptane or Dichloromethane at 298.2 K
• 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
• Phase Equilibrium Properties of Binary and Ternary Mixtures Containing Dibutyl Ether, Cyclohexane, and Heptane or 1-Hexene at T ) 313.15 K
• Measurements and Correlation of Liquid Liquid Equilibria of (Water + Ethanol + Dimethyl Carbonate + 2,2,4-Trimethylpentane or n-Heptane) and (Water + Dimethyl Carbonate + n-Heptane + Toluene)
• 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
• Liquid-Liquid Equilibrium of (Cyclohexane + 2,2,2-Trifluoroethanol) and (Cyclohexane + Methanol) from (278.15 to 318.15) K
• Determination and Correlation of Excess Molar Enthalpies of Eight Binary Systems Containing Acetophenone at Different Temperatures
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Solubility of Diamantane, Trimantane, Tetramantane, and Their Derivatives in Organic Solvents
• Effect of Temperature on Phase Equilibrium of the Mixed-Solvent System of (2,2,2-Trifluoroethanol + Methanol + Cyclohexane)
• Densities and Viscosities of Binary Mixtures of Tri-n-butyl Phosphate + Cyclohexane, + n-Heptane at T ) (288.15, 293.15, 298.15, 303.15, and 308.15) K
• Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
• Solubility of the Antimicrobial Agent Triclosan in Organic Solvents of Different Hydrogen Bonding Capabilities at Several Temperatures
• Solubilities of Palmitic Acid in Pure Solvents and Its Mixtures
• Mass Diffusion Coefficients of Dimethyl Carbonate in Heptane and in Air at T ) (278.15 to 338.15) K
• Measurement and Correlation for Solubilities of Naphthalene in Acetone, Toluene, Xylene, Ethanol, Heptane, and 1-Butanol
• 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
• Mass Diffusion Coefficients of Oxygenated Fuel Additives in Diesel Oil and in Heptane at T ) (276 to 333) K
• Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
• In Situ Determination of Phase Equilibria of Methyl Benzoate + Alkane Mixtures Using an Infrared Absorption Method. Comparison with Polar GC-SAFT Predictions
• Surface Tension of 2,2-Dimethylbutane from (233 to 378) K
• Mutual Diffusion Coefficients of Diethyl Carbonate and Diethyl Adipate in Heptane at T = (278.15 to 338.15) K under Atmospheric Pressure
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Measurement and Correlation of Bubble Point Pressure in (CO2 + C6H6), (CO2 + CH3C6H5), (CO2 + C6H14), and (CO2 + C7H16) at Temperatures from (293.15 to 313.15) K
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Liquid-Liquid Equilibria for the Three Ternary Systems (3-Methyl-N-butylpyridinium Dicyanamide + Toluene + Heptane), (1-Butyl-3-methylimidazolium Dicyanamide + Toluene + Heptane) and (1-Butyl-3-methylimidazolium Thiocyanate + Toluene + Heptane) at T = (313.15 and 348.15) K and p = 0.1 MPa
• Phase Equilibria of (1-Hexyl-3-methylimidazolium Thiocyanate + Water, Alcohol, or Hydrocarbon) Binary Systems
• Experimental Measurement and Correlation of the Solubilities of 2,4-Dichloro-5-methoxypyrimidine in Ethyl Ethanoate, Methanol, Ethanol, Acetone, Tetrachloromethane, and Heptane at Temperatures between (295 and 320) K
• Phase Equilibria for Liquid Mixtures of (an Alkane + Toluene + Dimethyl Phthalate)
• Heat Capacities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
• 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
• Isobaric Vapor-Liquid Equilibria of Heptane + 1-Butanol and Heptane + 1-Pentanol Systems at (53.3 and 91.3) kPa
• Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
• Densities and Excess Molar Volumes of 2-Butanol + Cyclohexanamine + Heptane and 2-Butanol + n-Heptane at Temperatures between (288.15 and 323.15) K
• 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
• Volumetric and Viscous Properties at Several Temperatures for Binary Mixtures of N-Methylpiperazine with Methylcyclohexane or n-Heptane
• Solubility of Triadimefon in Organic Solvents at Temperatures between (288.15 and 333.15) K
• Liquid-Liquid Equilibria for the Ternary Systems {Heptane + Toluene + N-Butylpyridinium Tetrafluoroborate or N-Hexylpyridinium Tetrafluoroborate} at T = 313.2 K
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• 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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