Chemical Properties of Dodecane (CAS 112-40-3)

InChI

InChI=1S/C12H26/c1-3-5-7-9-11-12-10-8-6-4-2/h3-12H2,1-2H3

InChI Key

SNRUBQQJIBEYMU-UHFFFAOYSA-N

Formula

C12H26

SMILES

CCCCCCCCCCCC

Molecular Weight¹

170.33

CAS

112-40-3

Other Names

• Adakane 12
• Ba 51-090453
• Bihexyl
• CH3(CH2)10CH3
• Dihexyl
• Duodecane
• NSC 8714
• n-dodecane

• ω : Acentric Factor.
• α_p : Isobaric thermal expansion coefficient (1/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).
• Δ_fG° : Standard Gibbs free energy of formation (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 standard conditions (kJ/mol).
• Δ_subH : Enthalpy of sublimation at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• D^*_i : Self diffusion coefficient (m²/s).
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• α_diff : Thermal diffusivity (m²/s).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• V_COSTALD : COSTALD Characteristic Volume (m³/kmol).
• ω_SRK : SRK acentric factor.
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

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

Physical Properties

Property	Value	Unit	Source
ω	[0.5620; 0.5750]
ω	0.5620		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.5622		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.5710		ChemSep v8.3 pure component data Compiled value
ω	0.5750		KDB
ΔcH°liquid	[-8090.60; -7901.74]	kJ/mol
ΔcH°liquid	-7901.74	kJ/mol	NIST
ΔcH°liquid	-8086.00 ± 1.20	kJ/mol	NIST
ΔcH°liquid	-8083.20	kJ/mol	NIST
ΔcH°liquid	-8090.60 ± 7.90	kJ/mol	NIST
μ	[0.00; 0.00]	debye
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
μ	0.00	debye	KDB
ΔfG°	[49.81; 50.07]	kJ/mol
ΔfG°	49.81	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	50.07	kJ/mol	KDB
ΔfH°gas	[-291.10; -288.10]	kJ/mol
ΔfH°gas	-290.72	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-291.10	kJ/mol	KDB
ΔfH°gas	-290.90 ± 1.40	kJ/mol	NIST
ΔfH°gas	-288.10 ± 3.30	kJ/mol	NIST
ΔfH°liquid	[-352.10; -349.30]	kJ/mol
ΔfH°liquid	-352.10 ± 1.40	kJ/mol	NIST
ΔfH°liquid	-349.30 ± 3.20	kJ/mol	NIST
ΔfusH°	26.84	kJ/mol	Joback Calculated Property
ΔsubH°	100.20	kJ/mol	NIST
ΔvapH°	[60.30; 62.10]	kJ/mol
ΔvapH°	61.51	kJ/mol	NIST
ΔvapH°	62.10 ± 0.20	kJ/mol	NIST
ΔvapH°	60.30 ± 0.80	kJ/mol	NIST
ΔvapH°	60.70	kJ/mol	NIST
ΔvapH°	61.20	kJ/mol	NIST
ΔvapH°	61.20	kJ/mol	NIST
ΔvapH°	61.50	kJ/mol	NIST
ΔvapH°	61.80 ± 0.50	kJ/mol	NIST
ΔvapH°	61.20 ± 0.20	kJ/mol	NIST
ΔvapH°	60.40 ± 0.30	kJ/mol	NIST
ΔvapH°	61.30	kJ/mol	NIST
ΔvapH°	61.30 ± 0.20	kJ/mol	NIST
IE	9.70	eV	Relay (1.0) Calculated Property
log10WS	-6.48		Relay (1.0) Calculated Property
logPoct/wat	4.927		Crippen Calculated Property
McVol	179.940	ml/mol	McGowan Calculated Property
NFPA Fire	2		KDB
Pc	[1800.00; 1860.00]	kPa
Pc	1820.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Pc	1809.66	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	1820.22	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	1820.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	1820.00	kPa	KDB
Pc	1800.00 ± 100.00	kPa	NIST
Pc	1810.00 ± 20.00	kPa	NIST
Pc	1834.00	kPa	NIST
Pc	Outlier 1860.00 ± 13.78	kPa	NIST
Pc	1824.00 ± 10.00	kPa	NIST
Ptriple	6.15e-04	kPa	ChemSep v8.3 pure component data Compiled value
ρc	[221.44; 226.55]	kg/m3
ρc	221.44 ± 17.03	kg/m3	NIST
ρc	226.55 ± 6.81	kg/m3	NIST
Inp	[200.12; 209.90]
Inp	200.12		NIST
Inp	202.83		NIST
Inp	209.90		NIST
Inp	200.12		NIST
S°gas	622.50	J/mol×K	NIST
S°liquid	[490.66; 497.10]	J/mol×K
S°liquid	490.66	J/mol×K	NIST
S°liquid	497.10	J/mol×K	NIST
Tboil	[479.15; 492.00]	K
Tboil	Outlier 479.15	K	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Tboil	489.48	K	ChemSep v8.3 pure component data Compiled value
Tboil	489.47	K	KDB
Tboil	489.50	K	NIST
Tboil	489.65 ± 0.50	K	NIST
Tboil	489.35 ± 0.50	K	NIST
Tboil	489.25 ± 0.40	K	NIST
Tboil	489.41 ± 0.20	K	NIST
Tboil	489.45 ± 0.20	K	NIST
Tboil	489.41 ± 0.50	K	NIST
Tboil	489.65 ± 0.30	K	NIST
Tboil	492.00 ± 3.00	K	NIST
Tboil	489.79 ± 0.50	K	NIST
Tboil	490.00 ± 2.22	K	NIST
Tboil	489.70 ± 2.00	K	NIST
Tboil	489.49 ± 0.30	K	NIST
Tboil	489.41 ± 0.15	K	NIST
Tboil	489.00 ± 3.00	K	NIST
Tboil	489.41 ± 0.10	K	NIST
Tboil	489.50 ± 2.00	K	NIST
Tboil	488.00 ± 4.00	K	NIST
Tboil	488.30 ± 2.00	K	NIST
Tboil	489.38 ± 0.15	K	NIST
Tboil	487.00 ± 5.00	K	NIST
Tboil	487.00 ± 4.00	K	NIST
Tc	[657.40; 659.00]	K
Tc	658.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Tc	658.80	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	658.26	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	658.00	K	ChemSep v8.3 pure component data Compiled value
Tc	658.00	K	KDB
Tc	658.00 ± 1.00	K	NIST
Tc	658.20 ± 0.30	K	NIST
Tc	658.80 ± 0.60	K	NIST
Tc	658.20 ± 0.40	K	NIST
Tc	658.40	K	NIST
Tc	657.40 ± 0.60	K	NIST
Tc	657.70 ± 0.60	K	NIST
Tc	657.70 ± 0.50	K	NIST
Tc	659.00 ± 0.70	K	NIST
Tc	658.25 ± 0.20	K	NIST
Tfus	[230.90; 273.15]	K
Tfus	263.70	K	Determination of thermophysical properties of cyclopentane hydrate using a stirred calorimetric cell
Tfus	264.95	K	Density, Viscosity, and Freezing Point for Four Binary Systems of n-Dodecane or Methylcyclohexane Mixed with 1-Heptanol or Cyclohexylmethanol
Tfus	263.55	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	263.57	K	ChemSep v8.3 pure component data Compiled value
Tfus	263.50	K	KDB
Tfus	263.49 ± 0.15	K	NIST
Tfus	263.55 ± 0.20	K	NIST
Tfus	263.65 ± 0.50	K	NIST
Tfus	263.30 ± 0.50	K	NIST
Tfus	263.44 ± 0.15	K	NIST
Tfus	265.00 ± 0.83	K	NIST
Tfus	263.44 ± 1.00	K	NIST
Tfus	263.00 ± 1.50	K	NIST
Tfus	263.43 ± 0.10	K	NIST
Tfus	263.53 ± 0.06	K	NIST
Tfus	263.44 ± 0.10	K	NIST
Tfus	263.45 ± 0.10	K	NIST
Tfus	263.46 ± 0.10	K	NIST
Tfus	263.53 ± 0.06	K	NIST
Tfus	263.46 ± 0.10	K	NIST
Tfus	263.53 ± 0.06	K	NIST
Tfus	260.90 ± 1.50	K	NIST
Tfus	263.55 ± 0.02	K	NIST
Tfus	263.55 ± 0.02	K	NIST
Tfus	263.55 ± 0.01	K	NIST
Tfus	263.70 ± 2.00	K	NIST
Tfus	Outlier 230.90 ± 1.50	K	NIST
Tfus	263.09 ± 0.40	K	NIST
Tfus	262.55 ± 0.50	K	NIST
Tfus	263.54 ± 0.20	K	NIST
Tfus	262.70 ± 1.00	K	NIST
Tfus	263.55 ± 0.02	K	NIST
Tfus	263.55 ± 0.02	K	NIST
Tfus	263.55 ± 0.02	K	NIST
Tfus	263.55 ± 0.01	K	NIST
Tfus	263.65 ± 0.30	K	NIST
Tfus	263.65 ± 0.30	K	NIST
Tfus	263.51 ± 0.10	K	NIST
Tfus	263.54 ± 0.06	K	NIST
Tfus	263.55 ± 0.06	K	NIST
Tfus	260.00 ± 4.00	K	NIST
Tfus	261.15 ± 0.30	K	NIST
Tfus	Outlier 273.15 ± 0.50	K	NIST
Tfus	263.15 ± 2.00	K	NIST
Tfus	263.00 ± 1.50	K	NIST
Tfus	262.00 ± 2.00	K	NIST
Tfus	263.54 ± 0.07	K	NIST
Tfus	263.54 ± 0.10	K	NIST
Tfus	263.42 ± 0.08	K	NIST
Tfus	Outlier 273.15 ± 3.00	K	NIST
Ttriple	[263.50; 263.58]	K
Ttriple	263.57	K	ChemSep v8.3 pure component data Compiled value
Ttriple	263.58 ± 0.05	K	NIST
Ttriple	263.58 ± 0.02	K	NIST
Ttriple	263.57 ± 0.20	K	NIST
Ttriple	263.58 ± 0.20	K	NIST
Ttriple	263.58 ± 0.10	K	NIST
Ttriple	263.58 ± 0.06	K	NIST
Ttriple	Outlier 263.50 ± 0.30	K	NIST
UQi	7.10		ChemSep v8.3 pure component data Compiled value
URi	8.55		ChemSep v8.3 pure component data Compiled value
Vc	[0.713; 0.754]	m3/kmol
Vc	0.754	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Vc	0.713	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.754	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.754	m3/kmol	KDB
Vc	0.754	m3/kmol	NIST
VCOSTALD	0.76	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.58		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2508300; 0.2510000]
Zc	0.2510000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Zc	0.2510000		ChemSep v8.3 pure component data Compiled value
Zc	0.2508300		KDB
Zra	[0.25; 0.25]
Zra	0.25		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.25		ChemSep v8.3 pure component data Compiled value
Zra	0.25		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[368.47; 388.29]	J/mol×K	[283.15; 323.15]
Cp,liquid	368.47	J/mol×K	283.15	Heat Capacities, Densities, and Speeds of Sound for {(1,5-Dichloropentane or 1,6-Dichlorohexane) + Dodecane}
Cp,liquid	371.38	J/mol×K	288.15	Thermodynamic Properties of dodecane + 1-butanol and + 2-butanol systems
Cp,liquid	370.48	J/mol×K	288.15	Heat Capacities, Densities, and Speeds of Sound for {(1,5-Dichloropentane or 1,6-Dichlorohexane) + Dodecane}
Cp,liquid	372.74	J/mol×K	293.15	Heat Capacities, Densities, and Speeds of Sound for {(1,5-Dichloropentane or 1,6-Dichlorohexane) + Dodecane}
Cp,liquid	371.10	J/mol×K	297.70	NIST
Cp,liquid	374.50	J/mol×K	298.00	NIST
Cp,liquid	376.91	J/mol×K	298.15	NIST
Cp,liquid	376.00	J/mol×K	298.15	NIST
Cp,liquid	375.04	J/mol×K	298.15	Heat Capacities, Densities, and Speeds of Sound for {(1,5-Dichloropentane or 1,6-Dichlorohexane) + Dodecane}
Cp,liquid	375.93	J/mol×K	298.15	NIST
Cp,liquid	375.94	J/mol×K	298.15	Thermodynamic Properties of dodecane + 1-butanol and + 2-butanol systems
Cp,liquid	370.72	J/mol×K	298.15	NIST
Cp,liquid	374.82	J/mol×K	298.15	NIST
Cp,liquid	376.00	J/mol×K	298.15	NIST
Cp,liquid	372.12	J/mol×K	298.15	NIST
Cp,liquid	376.46	J/mol×K	298.15	NIST
Cp,liquid	376.09	J/mol×K	298.15	NIST
Cp,liquid	376.00	J/mol×K	298.15	NIST
Cp,liquid	375.37	J/mol×K	298.15	NIST
Cp,liquid	374.93	J/mol×K	298.15	NIST
Cp,liquid	373.30	J/mol×K	298.15	NIST
Cp,liquid	375.30	J/mol×K	298.15	NIST
Cp,liquid	373.30	J/mol×K	298.15	NIST
Cp,liquid	375.26	J/mol×K	298.15	NIST
Cp,liquid	377.43	J/mol×K	303.15	Heat Capacities, Densities, and Speeds of Sound for {(1,5-Dichloropentane or 1,6-Dichlorohexane) + Dodecane}
Cp,liquid	380.02	J/mol×K	308.15	Heat Capacities, Densities, and Speeds of Sound for {(1,5-Dichloropentane or 1,6-Dichlorohexane) + Dodecane}
Cp,liquid	380.92	J/mol×K	308.15	Thermodynamic Properties of dodecane + 1-butanol and + 2-butanol systems
Cp,liquid	382.73	J/mol×K	313.15	Heat Capacities, Densities, and Speeds of Sound for {(1,5-Dichloropentane or 1,6-Dichlorohexane) + Dodecane}
Cp,liquid	385.48	J/mol×K	318.15	Heat Capacities, Densities, and Speeds of Sound for {(1,5-Dichloropentane or 1,6-Dichlorohexane) + Dodecane}
Cp,liquid	386.31	J/mol×K	318.15	Thermodynamic Properties of dodecane + 1-butanol and + 2-butanol systems
Cp,liquid	388.29	J/mol×K	323.15	Heat Capacities, Densities, and Speeds of Sound for {(1,5-Dichloropentane or 1,6-Dichlorohexane) + Dodecane}
η	[0.0000551; 0.0015800]	Pa×s	[288.15; 673.20]
η	0.0015800	Pa×s	288.15	Physical properties of phosphonium ionic liquid and its mixtures with dodecane and water
η	0.0014700	Pa×s	293.15	Physical properties of phosphonium ionic liquid and its mixtures with dodecane and water
η	0.0014540	Pa×s	293.15	Dynamic viscosities of 2-butanol with alkanes (C8, C10, and C12) at several temperatures
η	0.0014540	Pa×s	293.15	Dynamic Viscosities of 2-Pentanol with Alkanes (Octane, Decane, and Dodecane) at Three Temperatures T ) (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO Interaction Parameters
η	0.0013360	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of Tributyl Phosphate with Hexane and Dodecane from (298.15 to 328.15) K
η	0.0013500	Pa×s	298.15	Physical properties of phosphonium ionic liquid and its mixtures with dodecane and water
η	0.0013270	Pa×s	298.15	Dynamic Viscosities of 2-Pentanol with Alkanes (Octane, Decane, and Dodecane) at Three Temperatures T ) (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO Interaction Parameters
η	0.0013270	Pa×s	298.15	Dynamic viscosities of 2-butanol with alkanes (C8, C10, and C12) at several temperatures
η	0.0012400	Pa×s	303.15	Physical properties of phosphonium ionic liquid and its mixtures with dodecane and water
η	0.0012190	Pa×s	303.15	Dynamic viscosities of 2-butanol with alkanes (C8, C10, and C12) at several temperatures
η	0.0012190	Pa×s	303.15	Dynamic Viscosities of 2-Pentanol with Alkanes (Octane, Decane, and Dodecane) at Three Temperatures T ) (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO Interaction Parameters
η	0.0012210	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of Tributyl Phosphate with Hexane and Dodecane from (298.15 to 328.15) K
η	0.0013335	Pa×s	303.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0011400	Pa×s	308.15	Physical properties of phosphonium ionic liquid and its mixtures with dodecane and water
η	0.0011250	Pa×s	308.15	Densities and Viscosities of Binary Mixtures of Tributyl Phosphate with Hexane and Dodecane from (298.15 to 328.15) K
η	0.0010600	Pa×s	313.15	Physical properties of phosphonium ionic liquid and its mixtures with dodecane and water
η	0.0010390	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of Tributyl Phosphate with Hexane and Dodecane from (298.15 to 328.15) K
η	0.0011221	Pa×s	313.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0009650	Pa×s	318.15	Densities and Viscosities of Binary Mixtures of Tributyl Phosphate with Hexane and Dodecane from (298.15 to 328.15) K
η	0.0009900	Pa×s	318.15	Physical properties of phosphonium ionic liquid and its mixtures with dodecane and water
η	0.0009700	Pa×s	323.00	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0008980	Pa×s	323.15	Densities and Viscosities of Binary Mixtures of Tributyl Phosphate with Hexane and Dodecane from (298.15 to 328.15) K
η	0.0009225	Pa×s	323.15	Liquid Viscosity and Surface Tension of n-Dodecane, n-Octacosane, Their Mixtures, and a Wax between 323 and 573 K by Surface Light Scattering
η	0.0009300	Pa×s	323.15	Physical properties of phosphonium ionic liquid and its mixtures with dodecane and water
η	0.0008430	Pa×s	328.15	Densities and Viscosities of Binary Mixtures of Tributyl Phosphate with Hexane and Dodecane from (298.15 to 328.15) K
η	0.0008700	Pa×s	328.15	Physical properties of phosphonium ionic liquid and its mixtures with dodecane and water
η	0.0008519	Pa×s	333.10	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0008200	Pa×s	333.15	Physical properties of phosphonium ionic liquid and its mixtures with dodecane and water
η	0.0007442	Pa×s	343.30	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0006763	Pa×s	348.15	Liquid Viscosity and Surface Tension of n-Dodecane, n-Octacosane, Their Mixtures, and a Wax between 323 and 573 K by Surface Light Scattering
η	0.0006736	Pa×s	353.30	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0006075	Pa×s	363.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0005070	Pa×s	373.15	Liquid Viscosity and Surface Tension of n-Dodecane, n-Octacosane, Their Mixtures, and a Wax between 323 and 573 K by Surface Light Scattering
η	0.0005467	Pa×s	373.30	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0004902	Pa×s	383.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0004472	Pa×s	393.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0004003	Pa×s	398.15	Liquid Viscosity and Surface Tension of n-Dodecane, n-Octacosane, Their Mixtures, and a Wax between 323 and 573 K by Surface Light Scattering
η	0.0004112	Pa×s	403.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0003785	Pa×s	413.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0003223	Pa×s	423.15	Liquid Viscosity and Surface Tension of n-Dodecane, n-Octacosane, Their Mixtures, and a Wax between 323 and 573 K by Surface Light Scattering
η	0.0003508	Pa×s	423.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0003277	Pa×s	433.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0002974	Pa×s	443.40	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0002595	Pa×s	448.15	Liquid Viscosity and Surface Tension of n-Dodecane, n-Octacosane, Their Mixtures, and a Wax between 323 and 573 K by Surface Light Scattering
η	0.0002822	Pa×s	453.10	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0002604	Pa×s	463.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0002156	Pa×s	473.15	Liquid Viscosity and Surface Tension of n-Dodecane, n-Octacosane, Their Mixtures, and a Wax between 323 and 573 K by Surface Light Scattering
η	0.0002440	Pa×s	473.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0002250	Pa×s	483.10	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0002250	Pa×s	483.10	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0002076	Pa×s	493.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0001821	Pa×s	498.15	Liquid Viscosity and Surface Tension of n-Dodecane, n-Octacosane, Their Mixtures, and a Wax between 323 and 573 K by Surface Light Scattering
η	0.0001964	Pa×s	503.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0001846	Pa×s	513.10	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0001532	Pa×s	523.15	Liquid Viscosity and Surface Tension of n-Dodecane, n-Octacosane, Their Mixtures, and a Wax between 323 and 573 K by Surface Light Scattering
η	0.0001722	Pa×s	523.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0001608	Pa×s	533.10	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0001489	Pa×s	543.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0001277	Pa×s	548.15	Liquid Viscosity and Surface Tension of n-Dodecane, n-Octacosane, Their Mixtures, and a Wax between 323 and 573 K by Surface Light Scattering
η	0.0001375	Pa×s	553.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0001297	Pa×s	563.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0001051	Pa×s	573.15	Liquid Viscosity and Surface Tension of n-Dodecane, n-Octacosane, Their Mixtures, and a Wax between 323 and 573 K by Surface Light Scattering
η	0.0001201	Pa×s	573.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0001126	Pa×s	583.30	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0001031	Pa×s	593.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0000974	Pa×s	603.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0000913	Pa×s	613.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0000839	Pa×s	623.10	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0000767	Pa×s	633.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0000694	Pa×s	643.10	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0000657	Pa×s	653.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0000605	Pa×s	663.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0000551	Pa×s	673.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
η	0.0000551	Pa×s	673.20	Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
ΔfusH	[35.70; 36.84]	kJ/mol	[263.10; 263.60]
ΔfusH	35.70	kJ/mol	263.10	NIST
ΔfusH	36.58	kJ/mol	263.50	NIST
ΔfusH	36.84	kJ/mol	263.59	NIST
ΔfusH	36.82	kJ/mol	263.60	NIST
ΔfusH	36.82	kJ/mol	263.60	NIST
ΔsubH	101.70	kJ/mol	263.00	NIST
ΔvapH	[43.64; 65.70]	kJ/mol	[299.00; 488.60]
ΔvapH	61.40	kJ/mol	299.00	NIST
ΔvapH	65.70	kJ/mol	317.00	NIST
ΔvapH	58.10	kJ/mol	334.00	NIST
ΔvapH	61.80	kJ/mol	339.00	NIST
ΔvapH	61.10	kJ/mol	343.50	NIST
ΔvapH	57.40	kJ/mol	344.00	NIST
ΔvapH	51.60	kJ/mol	446.00	NIST
ΔvapH	43.64	kJ/mol	488.60	KDB
Pvap	[4.21e-03; 241.00]	kPa	[284.15; 509.15]
Pvap	4.21e-03	kPa	284.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	6.46e-03	kPa	289.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	9.78e-03	kPa	294.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.01	kPa	299.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.02	kPa	304.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.03	kPa	309.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.06	kPa	313.15	Vapor-Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K
Pvap	0.06	kPa	313.15	Vapor Liquid Equilibria of Binary Mixtures Containing 2-Butanol and Hydrocarbons at 313.15 K
Pvap	0.04	kPa	314.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.06	kPa	319.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.20	kPa	323.15	Isothermal Phase Equilibria and Excess Molar Enthalpies for Binary Systems with Dimethyl Ether at 323.15 K
Pvap	0.09	kPa	324.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.12	kPa	329.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.17	kPa	334.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.23	kPa	339.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.36	kPa	342.18	P-x data for binary systems using a novel static total pressure apparatus
Pvap	0.40	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	0.32	kPa	344.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.42	kPa	349.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.75	kPa	352.68	P-x data for binary systems using a novel static total pressure apparatus
Pvap	0.70	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	0.56	kPa	354.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.75	kPa	359.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	1.20	kPa	363.15	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	0.98	kPa	364.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	1.27	kPa	369.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	2.00	kPa	373.15	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	1.64	kPa	374.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	2.10	kPa	379.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	3.20	kPa	383.15	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	2.67	kPa	384.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	3.38	kPa	389.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	4.90	kPa	393.15	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	4.25	kPa	394.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	5.32	kPa	399.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	6.62	kPa	404.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	8.19	kPa	409.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	10.10	kPa	414.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	12.40	kPa	419.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	15.10	kPa	424.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	18.30	kPa	429.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	20.90	kPa	432.23	Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap	22.10	kPa	434.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	26.60	kPa	439.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	31.80	kPa	444.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	31.00	kPa	444.86	Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap	38.00	kPa	449.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	40.08	kPa	453.92	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	40.00	kPa	453.92	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	45.10	kPa	454.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	42.70	kPa	455.87	Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap	43.58	kPa	456.87	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	53.40	kPa	459.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	46.71	kPa	459.31	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	49.93	kPa	461.72	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	50.80	kPa	462.05	Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap	63.00	kPa	464.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	55.35	kPa	465.47	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	58.41	kPa	467.52	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	74.10	kPa	469.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	62.30	kPa	469.67	Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap	63.63	kPa	470.69	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	86.80	kPa	474.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	70.20	kPa	474.19	Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap	69.97	kPa	474.33	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	77.75	kPa	478.47	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	101.00	kPa	479.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	81.00	kPa	479.82	Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap	118.00	kPa	484.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	90.80	kPa	484.34	Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap	100.60	kPa	488.50	Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap	137.00	kPa	489.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	158.00	kPa	494.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	183.00	kPa	499.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	210.00	kPa	504.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	241.00	kPa	509.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
n0	[1.40018; 1.42750]		[293.10; 343.15]
n0	1.42200		293.10	Extraction of propylbenzene or butylbenzene from dodecane using 4-methyl-N-butylpyridinium tetrafluoroborate, [mebupy][BF4], as an ionic liquid at different temperatures
n0	1.42200		293.10	Phase equilibria for the extraction of sec-butylbenzene from dodecane with N,N-dimethylformamide
n0	1.42210		293.10	Extraction of Butylbenzene from Dodecane Using Hexafluorophosphate-Based Ionic Liquids: Effect of Cation Change
n0	1.42200		293.10	Liquid liquid equilibria for n-alkanes (C12, C14, C17) + propylbenzene +NMP mixtures at temperatures between 298 and 328K
n0	1.42200		293.10	Evaluation of [bmim][PF6] as an ionic solvent for the extraction of propylbenzene from aliphatic compounds
n0	1.42180		293.15	Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
n0	1.42180		293.15	Vapor Liquid Equilibrium Data for Binary Systems of n-Dodecane + {Propan-1-ol, Butan-1-ol, 2-Methylpropan-1-ol} at 40 kPa
n0	1.42100		293.15	Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
n0	1.42100		293.15	Activity Coefficients at Infinite Dilution and Excess Molar Volumes in Binary Mixtures Containing Normal Alkanes (Nonane, Decane, Undecane, or Dodecane) and Cresols (2-Methylphenol or 3-Methylphenol)
n0	1.42155		293.15	Liquid Liquid Equilibria of Methanol, Ethanol, and Propan-2-ol with Water and Dodecane
n0	1.41920		293.15	Isothermal Vapor Liquid Equilibrium Data for the Propan-1-ol + Dodecane System at (323.0, 343.4, 353.2, 363.1, and 369.2) K
n0	1.42218		293.15	Thermodynamic modeling and experimental speeds of sound, densities, and refractive indexes of (tetralin + n-dodecane)
n0	1.41720		298.15	Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
n0	1.41920		298.15	Correlation and prediction of mixing thermodynamic properties of ester-containing systems: Ester + alkane and ester + ester binary systems and the ternary dodecane + ethyl pentanoate + ethyl ethanoate
n0	1.41970		298.15	Thermodynamic and acoustic properties of (heptane + dodecane) mixtures under elevated pressures
n0	1.42011		298.15	(Liquid + liquid) equilibria of [C8mim][NTf2] ionic liquid with a sulfur-component and hydrocarbons
n0	1.41960		298.15	Liquid Liquid Equilibrium in N-Methyl-2-hydroxyethylammonium Acetate, Butanoate, or Hexanoate Ionic Liquids + Dibenzothiophene + n-Dodecane Systems at 298.2 K and Atmospheric Pressure
n0	1.41860		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	1.42750		298.15	Liquid-liquid equilibria for mixtures of (Furfural + an Aromatic hydrocarbon + an alkane) at T=298.15 K
n0	1.42750		298.15	Liquid-Liquid Equilibria for Mixtures of (Furfural + a Chlorinated Aromatic Compound + an Alkane) at T = 298.15 K
n0	1.42011		298.15	Thiophene separation from aliphatic hydrocarbons using the 1-ethyl-3-methylimidazolium ethylsulfate ionic liquid
n0	1.41970		298.15	Measurement and Prediction of Excess Properties of Binary Mixtures Methyl Decanoate + an Even-Numbered n-Alkane (C6-C16) at 298.15 K
n0	1.41960		298.20	Liquid-Liquid Equilibria for {1-Ethyl-3-methylimidazolium Diethylphosphate or 1-Ethyl-3-methylimidazolium Ethylsulfate} + 4,6-Dimethyldibenzothiophene + Dodecane Systems at 298.2 K and 313.2 K
n0	1.41640		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	1.41784		303.15	Thermodynamic modeling and experimental speeds of sound, densities, and refractive indexes of (tetralin + n-dodecane)
n0	1.41350		303.15	Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
n0	1.41810		303.15	Liquid liquid equilibria measurements of ternary systems (acetonitrile + a carboxylic acid + dodecane) at 303.15 K
n0	1.41400		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	1.41346		313.15	Thermodynamic modeling and experimental speeds of sound, densities, and refractive indexes of (tetralin + n-dodecane)
n0	1.41310		313.20	Liquid-Liquid Equilibria for {1-Ethyl-3-methylimidazolium Diethylphosphate or 1-Ethyl-3-methylimidazolium Ethylsulfate} + 4,6-Dimethyldibenzothiophene + Dodecane Systems at 298.2 K and 313.2 K
n0	1.40914		323.15	Thermodynamic modeling and experimental speeds of sound, densities, and refractive indexes of (tetralin + n-dodecane)
n0	1.40479		333.15	Thermodynamic modeling and experimental speeds of sound, densities, and refractive indexes of (tetralin + n-dodecane)
n0	1.40018		343.15	Thermodynamic modeling and experimental speeds of sound, densities, and refractive indexes of (tetralin + n-dodecane)
ρl	[610.60; 753.00]	kg/m3	[288.15; 473.15]
ρl	752.44	kg/m3	288.15	Permittivity and density of binary systems of {dimethyl or diethyl carbonate} + n-dodecane from T=(288.15 to 328.15) K
ρl	752.35	kg/m3	288.15	Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl	752.41	kg/m3	288.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Quaternary Mixtures of n-Dodecane (1), n-Butylcyclohexane (2), n-Butylbenzene (3), and 2,2,4,4,6,8,8-Heptamethylnonane (4) at 0.1 MPa as Potential Surrogate Mixtures for Military Jet Fuel, JP-5
ρl	752.44	kg/m3	288.15	Study of the binary mixtures of {monoglyme + (hexane, cyclohexane, octane, dodecane)} by ECM-average and PFP models
ρl	752.44	kg/m3	288.15	On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl	748.00	kg/m3	293.00	KDB
ρl	748.79	kg/m3	293.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Quaternary Mixtures of n-Dodecane (1), n-Butylcyclohexane (2), n-Butylbenzene (3), and 2,2,4,4,6,8,8-Heptamethylnonane (4) at 0.1 MPa as Potential Surrogate Mixtures for Military Jet Fuel, JP-5
ρl	748.80	kg/m3	293.15	On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl	748.73	kg/m3	293.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Binary Mixtures of Ethylcyclohexane or Methylcyclohexane with n-Dodecane or n-Hexadecane at 0.1 MPa
ρl	748.80	kg/m3	293.15	Permittivity and density of binary systems of {dimethyl or diethyl carbonate} + n-dodecane from T=(288.15 to 328.15) K
ρl	748.79	kg/m3	293.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
ρl	748.83	kg/m3	293.15	Densities and Viscosities of Ternary System n-Dodecane (1) + Bicyclohexyl (2) + n-Butanol (3) and Corresponding Binaries at T = (293.15 to 333.15) K
ρl	748.72	kg/m3	293.15	Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl	748.83	kg/m3	293.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρl	753.00	kg/m3	293.15	Volume expansion prediction of supercritical CO 2 + crude oil
ρl	749.00	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	748.81	kg/m3	293.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	748.89	kg/m3	293.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Dodecane with 2,2,4,6,6-Pentamethylheptane or 2,2,4,4,6,8,8-Heptamethylnonane
ρl	745.38	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	745.09	kg/m3	298.15	Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl	745.52	kg/m3	298.15	Thermodynamics of aromatic polar compound (alkanone, alkanal or alkanoate) + hydrocarbon mixtures
ρl	745.11	kg/m3	298.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Binary Mixtures of Ethylcyclohexane or Methylcyclohexane with n-Dodecane or n-Hexadecane at 0.1 MPa
ρl	745.21	kg/m3	298.15	Binary Liquid Liquid Equilibria of ?-Valerolactone with Some Hydrocarbons
ρl	745.52	kg/m3	298.15	Thermodynamics of Mixtures Containing Amines. XV. Liquid Liquid Equilibria for Benzylamine + CH3(CH2)nCH3 (n = 8, 9, 10, 12, 14)
ρl	745.38	kg/m3	298.15	Excess molar enthalpies of the ternary mixtures: {tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether + n-dodecane} at the temperature 298.15 K
ρl	745.32	kg/m3	298.15	Solvent extraction of thiophene from n-alkanes (C7, C12, and C16) using the ionic liquid [C8mim][BF4]
ρl	745.28	kg/m3	298.15	Excess molar enthalpies of binary mixtures containing 2-decanone or dipentyl ether with long-chain n-alkanes at T = 298.15 K
ρl	745.27	kg/m3	298.15	Water/oil/[P6,6,6,14][NTf2] phase equilibria
ρl	745.20	kg/m3	298.15	(Liquid + liquid) equilibria for mixtures of dodecane and ethanol with alkylsulfate-based ionic liquids
ρl	741.52	kg/m3	298.15	Liquid liquid equilibria for acetophenone + n-alkane mixtures and characterization of acetophenone systems using DISQUAC
ρl	745.29	kg/m3	298.15	Study of the binary mixtures of {monoglyme + (hexane, cyclohexane, octane, dodecane)} by ECM-average and PFP models
ρl	745.19	kg/m3	298.15	Permittivity and density of binary systems of {dimethyl or diethyl carbonate} + n-dodecane from T=(288.15 to 328.15) K
ρl	745.62	kg/m3	298.15	Thermodynamics of mixing for binary mixtures of 1-octanol and 1-decanol with n-dodecane and ternary mixture of (TBP + 1-octanol + dodecane) at T = (298.15 to 323.15) K
ρl	745.19	kg/m3	298.15	On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl	745.22	kg/m3	298.15	Densities and Viscosities of Ternary System n-Dodecane (1) + Bicyclohexyl (2) + n-Butanol (3) and Corresponding Binaries at T = (293.15 to 333.15) K
ρl	745.52	kg/m3	298.15	Liquid-liquid equilibria for aqueous sulfuric acid solutions with undecane, dodecane, or 1-dodecanol, trioctylamine or tributyl phosphate and excess and deviation properties for sub-binary systems at 298.15 K
ρl	745.28	kg/m3	298.15	Study of the suitability of two ammonium-based ionic liquids for the extraction of benzene from its mixtures with aliphatic hydrocarbons.
ρl	745.38	kg/m3	298.15	Excess molar enthalpies of the ternary mixtures: methyl tert-butyl ether + 3-methylpentane + (n-decane or n-dodecane) at 298.15K
ρl	745.38	kg/m3	298.15	Excess molar enthalpies of the ternary mixtures: methyl tert-butyl ether +2-methylpentane + (n-decane or n-dodecane) at the temperature 298.15 K
ρl	747.00	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	745.28	kg/m3	298.15	Excess Molar Enthalpies of Binary Systems of 2-Octanone or 3-Octanone with Dodecane, Tetradecane, or Hexadecane at 298.15 K
ρl	745.23	kg/m3	298.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρl	745.28	kg/m3	298.15	Excess Molar Enthalpies of Binary Systems of n-Valeric Anhydride or n-Hexanoic Anhydride with n-Dodecane, n-Tetradecane, or n-Hexadecane at 298.15 K
ρl	745.82	kg/m3	298.15	Solid Liquid Equilibria, Excess Molar Volumes, and Deviations in the Molar Refractivity for the Binary Systems of Alamine 304-1 + Decane, Dodecane, or Dodecanol
ρl	741.54	kg/m3	298.15	Thermodynamics of Mixtures Containing a Very Strongly Polar Compound. 10. Liquid Liquid Equilibria for N,N-Dimethylacetamide + Selected Alkanes
ρl	741.54	kg/m3	298.15	Thermodynamics of Mixtures Containing Aromatic Alcohols. 1. Liquid Liquid Equilibria for (Phenylmethanol + Alkane) Systems
ρl	741.54	kg/m3	298.15	Thermodynamics of mixtures containing amines VI. Liquid liquid equilibria for mixtures of o-toluidine + selected alkanes
ρl	745.41	kg/m3	298.15	Mutual Solubilities of Terpene in Methanol and Water and Their Multicomponent Liquid-Liquid Equilibria
ρl	745.43	kg/m3	298.15	Density and Relative Permittivity for 1-Alkanols + Dodecane at 298.15 K
ρl	745.32	kg/m3	298.15	Excess Enthalpies of Binary Mixtures of 1-Hexene with Some n-Alkanes at 298.15 K
ρl	741.54	kg/m3	298.15	Liquid-liquid equilibria for benzaldehyde + n-alkane mixtures andcharacterization of benzaldehyde + hydrocarbon systems in terms of DISQUAC
ρl	745.51	kg/m3	298.15	Liquid Liquid Equilibria for Systems Containing 4-Phenylbutan-2-one or Benzyl Ethanoate and Selected Alkanes
ρl	745.16	kg/m3	298.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Quaternary Mixtures of n-Dodecane (1), n-Butylcyclohexane (2), n-Butylbenzene (3), and 2,2,4,4,6,8,8-Heptamethylnonane (4) at 0.1 MPa as Potential Surrogate Mixtures for Military Jet Fuel, JP-5
ρl	745.51	kg/m3	298.15	Liquid-Liquid Equilibria for 2-Phenylethan-1-ol + Alkane Systems
ρl	746.60	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	745.15	kg/m3	298.20	Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
ρl	741.98	kg/m3	303.15	Thermodynamics of mixing for binary mixtures of 1-octanol and 1-decanol with n-dodecane and ternary mixture of (TBP + 1-octanol + dodecane) at T = (298.15 to 323.15) K
ρl	741.63	kg/m3	303.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Dodecane with 2,2,4,6,6-Pentamethylheptane or 2,2,4,4,6,8,8-Heptamethylnonane
ρl	741.53	kg/m3	303.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Quaternary Mixtures of n-Dodecane (1), n-Butylcyclohexane (2), n-Butylbenzene (3), and 2,2,4,4,6,8,8-Heptamethylnonane (4) at 0.1 MPa as Potential Surrogate Mixtures for Military Jet Fuel, JP-5
ρl	741.42	kg/m3	303.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	741.75	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	741.60	kg/m3	303.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρl	741.57	kg/m3	303.15	On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl	741.77	kg/m3	303.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Binary Mixtures of Ethylcyclohexane or Methylcyclohexane with n-Dodecane or n-Hexadecane at 0.1 MPa
ρl	741.54	kg/m3	303.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
ρl	741.46	kg/m3	303.15	Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl	741.57	kg/m3	303.15	Permittivity and density of binary systems of {dimethyl or diethyl carbonate} + n-dodecane from T=(288.15 to 328.15) K
ρl	741.59	kg/m3	303.15	Densities and Viscosities of Ternary System n-Dodecane (1) + Bicyclohexyl (2) + n-Butanol (3) and Corresponding Binaries at T = (293.15 to 333.15) K
ρl	738.34	kg/m3	308.15	Thermodynamics of mixing for binary mixtures of 1-octanol and 1-decanol with n-dodecane and ternary mixture of (TBP + 1-octanol + dodecane) at T = (298.15 to 323.15) K
ρl	737.95	kg/m3	308.15	Densities and Viscosities of Ternary System n-Dodecane (1) + Bicyclohexyl (2) + n-Butanol (3) and Corresponding Binaries at T = (293.15 to 333.15) K
ρl	737.93	kg/m3	308.15	Study of the binary mixtures of {monoglyme + (hexane, cyclohexane, octane, dodecane)} by ECM-average and PFP models
ρl	737.93	kg/m3	308.15	Permittivity and density of binary systems of {dimethyl or diethyl carbonate} + n-dodecane from T=(288.15 to 328.15) K
ρl	738.12	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	737.93	kg/m3	308.15	On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl	737.97	kg/m3	308.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρl	734.19	kg/m3	313.15	Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl	734.48	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	734.33	kg/m3	313.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρl	734.18	kg/m3	313.15	Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl	734.25	kg/m3	313.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
ρl	734.87	kg/m3	313.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Binary Mixtures of Ethylcyclohexane or Methylcyclohexane with n-Dodecane or n-Hexadecane at 0.1 MPa
ρl	734.35	kg/m3	313.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Dodecane with 2,2,4,6,6-Pentamethylheptane or 2,2,4,4,6,8,8-Heptamethylnonane
ρl	734.69	kg/m3	313.15	Thermodynamics of mixing for binary mixtures of 1-octanol and 1-decanol with n-dodecane and ternary mixture of (TBP + 1-octanol + dodecane) at T = (298.15 to 323.15) K
ρl	734.25	kg/m3	313.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Quaternary Mixtures of n-Dodecane (1), n-Butylcyclohexane (2), n-Butylbenzene (3), and 2,2,4,4,6,8,8-Heptamethylnonane (4) at 0.1 MPa as Potential Surrogate Mixtures for Military Jet Fuel, JP-5
ρl	734.31	kg/m3	313.15	Densities and Viscosities of Ternary System n-Dodecane (1) + Bicyclohexyl (2) + n-Butanol (3) and Corresponding Binaries at T = (293.15 to 333.15) K
ρl	734.08	kg/m3	313.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	734.33	kg/m3	313.20	Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
ρl	730.68	kg/m3	318.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρl	730.66	kg/m3	318.15	Densities and Viscosities of Ternary System n-Dodecane (1) + Bicyclohexyl (2) + n-Butanol (3) and Corresponding Binaries at T = (293.15 to 333.15) K
ρl	731.03	kg/m3	318.15	Thermodynamics of mixing for binary mixtures of 1-octanol and 1-decanol with n-dodecane and ternary mixture of (TBP + 1-octanol + dodecane) at T = (298.15 to 323.15) K
ρl	730.70	kg/m3	318.15	On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl	730.70	kg/m3	318.15	Permittivity and density of binary systems of {dimethyl or diethyl carbonate} + n-dodecane from T=(288.15 to 328.15) K
ρl	726.74	kg/m3	323.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	726.94	kg/m3	323.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Quaternary Mixtures of n-Dodecane (1), n-Butylcyclohexane (2), n-Butylbenzene (3), and 2,2,4,4,6,8,8-Heptamethylnonane (4) at 0.1 MPa as Potential Surrogate Mixtures for Military Jet Fuel, JP-5
ρl	727.01	kg/m3	323.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρl	726.88	kg/m3	323.15	Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl	726.88	kg/m3	323.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Binary Mixtures of Ethylcyclohexane or Methylcyclohexane with n-Dodecane or n-Hexadecane at 0.1 MPa
ρl	727.04	kg/m3	323.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Dodecane with 2,2,4,6,6-Pentamethylheptane or 2,2,4,4,6,8,8-Heptamethylnonane
ρl	726.94	kg/m3	323.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
ρl	727.37	kg/m3	323.15	Thermodynamics of mixing for binary mixtures of 1-octanol and 1-decanol with n-dodecane and ternary mixture of (TBP + 1-octanol + dodecane) at T = (298.15 to 323.15) K
ρl	727.00	kg/m3	323.15	Densities and Viscosities of Ternary System n-Dodecane (1) + Bicyclohexyl (2) + n-Butanol (3) and Corresponding Binaries at T = (293.15 to 333.15) K
ρl	723.35	kg/m3	328.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρl	723.33	kg/m3	328.15	Densities and Viscosities of Ternary System n-Dodecane (1) + Bicyclohexyl (2) + n-Butanol (3) and Corresponding Binaries at T = (293.15 to 333.15) K
ρl	723.32	kg/m3	328.15	Permittivity and density of binary systems of {dimethyl or diethyl carbonate} + n-dodecane from T=(288.15 to 328.15) K
ρl	723.32	kg/m3	328.15	On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl	719.53	kg/m3	333.15	Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl	719.59	kg/m3	333.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Quaternary Mixtures of n-Dodecane (1), n-Butylcyclohexane (2), n-Butylbenzene (3), and 2,2,4,4,6,8,8-Heptamethylnonane (4) at 0.1 MPa as Potential Surrogate Mixtures for Military Jet Fuel, JP-5
ρl	719.67	kg/m3	333.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρl	719.69	kg/m3	333.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Dodecane with 2,2,4,6,6-Pentamethylheptane or 2,2,4,4,6,8,8-Heptamethylnonane
ρl	719.59	kg/m3	333.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
ρl	719.38	kg/m3	333.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	719.53	kg/m3	333.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Binary Mixtures of Ethylcyclohexane or Methylcyclohexane with n-Dodecane or n-Hexadecane at 0.1 MPa
ρl	719.65	kg/m3	333.15	Densities and Viscosities of Ternary System n-Dodecane (1) + Bicyclohexyl (2) + n-Butanol (3) and Corresponding Binaries at T = (293.15 to 333.15) K
ρl	715.98	kg/m3	338.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρl	712.20	kg/m3	343.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Dodecane with 2,2,4,6,6-Pentamethylheptane or 2,2,4,4,6,8,8-Heptamethylnonane
ρl	711.32	kg/m3	343.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	712.20	kg/m3	343.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
ρl	712.28	kg/m3	343.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρl	712.10	kg/m3	344.15	High-pressure densities and interfacial tensions of binary systems containing carbon dioxide + n-alkanes: (n-Dodecane, n-tridecane, n-tetradecane)
ρl	704.62	kg/m3	353.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	704.70	kg/m3	353.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Dodecane with 2,2,4,6,6-Pentamethylheptane or 2,2,4,4,6,8,8-Heptamethylnonane
ρl	697.21	kg/m3	363.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	697.10	kg/m3	363.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Dodecane with 2,2,4,6,6-Pentamethylheptane or 2,2,4,4,6,8,8-Heptamethylnonane
ρl	689.75	kg/m3	373.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	689.60	kg/m3	373.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Dodecane with 2,2,4,6,6-Pentamethylheptane or 2,2,4,4,6,8,8-Heptamethylnonane
ρl	682.25	kg/m3	383.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	674.68	kg/m3	393.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	667.04	kg/m3	403.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	659.32	kg/m3	413.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	651.53	kg/m3	423.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	643.60	kg/m3	433.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	635.55	kg/m3	443.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	627.38	kg/m3	453.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	619.09	kg/m3	463.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	610.60	kg/m3	473.15	Thermophysical properties of fatty acid methyl and ethyl esters
D*i	[0.00; 0.00]	m2/s	[264.14; 364.54]
D*i	0.00	m2/s	264.14	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	266.50	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	268.03	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	278.20	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	278.52	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	278.56	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	278.72	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	288.09	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	288.49	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	288.52	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	298.15	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	298.20	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	298.21	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	308.15	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	308.16	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	318.15	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	318.16	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	323.17	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	328.17	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	328.22	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	328.25	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	333.14	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	337.93	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	337.97	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	337.99	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	348.08	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	352.75	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	352.77	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	364.53	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	364.54	Viscous Calibration Liquids for Self-diffusion Measurements
ΔfusS	[138.80; 139.75]	J/mol×K	[263.50; 263.59]
ΔfusS	138.80	J/mol×K	263.50	NIST
ΔfusS	139.75	J/mol×K	263.59	NIST
γ	[0.02; 0.03]	N/m	[293.15; 323.15]
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	Density, Refractive Index, Viscosity, and Surface Tension of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with Some n-Alkanes from (293.15 to 313.15) K
γ	0.03	N/m	293.20	KDB
γ	0.03	N/m	294.10	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylbenzene + Linear Alkanes (n-Decane, n-Dodecane, n-Tetradecane, n-Hexadecane, or n-Heptadecane) at 0.1 MPa
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	Interfacial tensions of binary mixtures of ethanol with octane, decane, dodecane, and tetradecane
γ	0.02	N/m	303.15	Density, Refractive Index, Viscosity, and Surface Tension of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with Some n-Alkanes from (293.15 to 313.15) K
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	Interfacial tensions of binary mixtures of ethanol with octane, decane, dodecane, and tetradecane
γ	0.02	N/m	308.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.02	N/m	313.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.02	N/m	318.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.02	N/m	323.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
λliquid	[0.13; 0.14]	W/m×K	[318.20; 352.80]
λliquid	0.14	W/m×K	318.20	Thermal conductivity of heavy, even-carbon number n-alkanes (C22 to C32)
λliquid	0.13	W/m×K	323.20	Thermal conductivity of heavy, even-carbon number n-alkanes (C22 to C32)
λliquid	0.13	W/m×K	328.10	Thermal conductivity of heavy, even-carbon number n-alkanes (C22 to C32)
λliquid	0.13	W/m×K	333.10	Thermal conductivity of heavy, even-carbon number n-alkanes (C22 to C32)
λliquid	0.13	W/m×K	337.70	Thermal conductivity of heavy, even-carbon number n-alkanes (C22 to C32)
λliquid	0.13	W/m×K	343.20	Thermal conductivity of heavy, even-carbon number n-alkanes (C22 to C32)
λliquid	0.13	W/m×K	347.90	Thermal conductivity of heavy, even-carbon number n-alkanes (C22 to C32)
λliquid	0.13	W/m×K	352.80	Thermal conductivity of heavy, even-carbon number n-alkanes (C22 to C32)
αdiff	[4.25e-08; 5.83e-08]	m2/s	[423.73; 523.18]
αdiff	5.83e-08	m2/s	423.73	Thermal and Mutual Diffusivity of Binary Mixtures of n-Dodecane and n-Tetracontane with Carbon Monoxide, Hydrogen, and Water from Dynamic Light Scattering (DLS)
αdiff	5.23e-08	m2/s	448.23	Thermal and Mutual Diffusivity of Binary Mixtures of n-Dodecane and n-Tetracontane with Carbon Monoxide, Hydrogen, and Water from Dynamic Light Scattering (DLS)
αdiff	4.87e-08	m2/s	473.10	Thermal and Mutual Diffusivity of Binary Mixtures of n-Dodecane and n-Tetracontane with Carbon Monoxide, Hydrogen, and Water from Dynamic Light Scattering (DLS)
αdiff	4.58e-08	m2/s	498.16	Thermal and Mutual Diffusivity of Binary Mixtures of n-Dodecane and n-Tetracontane with Carbon Monoxide, Hydrogen, and Water from Dynamic Light Scattering (DLS)
αdiff	4.25e-08	m2/s	523.18	Thermal and Mutual Diffusivity of Binary Mixtures of n-Dodecane and n-Tetracontane with Carbon Monoxide, Hydrogen, and Water from Dynamic Light Scattering (DLS)

Datasets

1. Isobaric coefficient of expansion, 1/K (1)
2. Molar heat capacity at constant pressure, J/K/mol (1)
3. Viscosity, Pa*s (3)
4. Mass density, kg/m3 (9)
5. Speed of sound, m/s (1)

Isobaric coefficient of expansion, 1/K

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Isobaric coefficient of expansion, 1/K - Liquid
278.15	5000.00	0.0009
278.15	10000.00	0.0009
278.15	15000.00	0.0009
278.15	20000.00	0.0009
278.15	25000.00	0.0008
278.15	30000.00	0.0008
278.15	35000.00	0.0008
278.15	40000.00	0.0008
278.15	45000.00	0.0008
278.15	50000.00	0.0008
278.15	55000.00	0.0008
288.15	5000.00	0.0009
288.15	10000.00	0.0009
288.15	15000.00	0.0009
288.15	20000.00	0.0009
288.15	25000.00	0.0008
288.15	30000.00	0.0008
288.15	35000.00	0.0008
288.15	40000.00	0.0008
288.15	45000.00	0.0008
288.15	50000.00	0.0008
288.15	55000.00	0.0007
298.15	5000.00	0.0009
298.15	10000.00	0.0009
298.15	15000.00	0.0009
298.15	20000.00	0.0009
298.15	25000.00	0.0008
298.15	30000.00	0.0008
298.15	35000.00	0.0008
298.15	40000.00	0.0008
298.15	45000.00	0.0008
298.15	50000.00	0.0008
298.15	55000.00	0.0007
308.15	5000.00	0.0010
308.15	10000.00	0.0009
308.15	15000.00	0.0009
308.15	20000.00	0.0009
308.15	25000.00	0.0009
308.15	30000.00	0.0008
308.15	35000.00	0.0008
308.15	40000.00	0.0008
308.15	45000.00	0.0008
308.15	50000.00	0.0008
308.15	55000.00	0.0007
318.15	5000.00	0.0010
318.15	10000.00	0.0009
318.15	15000.00	0.0009
318.15	20000.00	0.0009
318.15	25000.00	0.0009
318.15	30000.00	0.0008
318.15	35000.00	0.0008
318.15	40000.00	0.0008
318.15	45000.00	0.0008
318.15	50000.00	0.0008
318.15	55000.00	0.0007
328.15	5000.00	0.0010
328.15	10000.00	0.0009
328.15	15000.00	0.0009
328.15	20000.00	0.0009
328.15	25000.00	0.0009
328.15	30000.00	0.0008
328.15	35000.00	0.0008
328.15	40000.00	0.0008
328.15	45000.00	0.0008
328.15	50000.00	0.0008
328.15	55000.00	0.0007
338.15	5000.00	0.0010
338.15	10000.00	0.0010
338.15	15000.00	0.0009
338.15	20000.00	0.0009
338.15	25000.00	0.0009
338.15	30000.00	0.0008
338.15	35000.00	0.0008
338.15	40000.00	0.0008
338.15	45000.00	0.0008
338.15	50000.00	0.0008
338.15	55000.00	0.0007
348.15	5000.00	0.0010
348.15	10000.00	0.0010
348.15	15000.00	0.0009
348.15	20000.00	0.0009
348.15	25000.00	0.0009
348.15	30000.00	0.0008
348.15	35000.00	0.0008
348.15	40000.00	0.0008
348.15	45000.00	0.0008
348.15	50000.00	0.0008
348.15	55000.00	0.0007
Reference

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

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
323.15	100.00	386.32
328.15	100.00	389.56
333.15	100.00	392.79
338.15	100.00	395.86
343.15	100.00	399.09
348.15	100.00	402.33
353.15	100.00	405.57
358.15	100.00	408.80
363.15	100.00	412.04
368.15	100.00	415.28
373.15	100.00	418.85
378.15	100.00	422.09
383.15	100.00	425.50
388.15	100.00	428.73
393.15	100.00	432.31
398.15	100.00	435.38
403.15	100.00	438.78
408.15	100.00	442.53
413.15	100.00	445.77
418.15	100.00	449.34
423.15	100.00	452.92
428.15	100.00	456.50
433.15	100.00	460.59
438.15	100.00	465.35
323.15	10180.00	385.13
328.15	10180.00	388.02
333.15	10180.00	391.26
338.15	10180.00	394.33
343.15	10180.00	397.39
348.15	10180.00	400.46
353.15	10180.00	403.52
358.15	10180.00	406.93
363.15	10180.00	410.00
368.15	10180.00	413.23
373.15	10180.00	416.13
378.15	10180.00	419.36
383.15	10180.00	422.60
388.15	10180.00	426.01
393.15	10180.00	429.07
398.15	10180.00	433.16
403.15	10180.00	435.89
408.15	10180.00	438.78
413.15	10180.00	441.68
418.15	10180.00	444.06
423.15	10180.00	447.64
428.15	10180.00	450.88
433.15	10180.00	454.28
438.15	10180.00	458.20
443.15	10180.00	462.12
448.15	10180.00	465.70
453.15	10180.00	469.95
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
293.15	100.00	0.0015
293.15	1000.00	0.0015
293.15	5000.00	0.0016
293.15	10000.00	0.0017
293.15	20000.00	0.0019
293.15	30000.00	0.0021
293.15	40000.00	0.0023
293.15	50000.00	0.0026
293.15	60000.00	0.0028
293.15	70000.00	0.0031
293.15	80000.00	0.0034
293.15	100000.00	0.0041
293.15	120000.00	0.0050
293.15	140000.00	0.0058
313.15	100.00	0.0011
313.15	1000.00	0.0011
313.15	5000.00	0.0011
313.15	10000.00	0.0012
313.15	20000.00	0.0013
313.15	30000.00	0.0015
313.15	40000.00	0.0016
313.15	50000.00	0.0018
313.15	60000.00	0.0019
313.15	70000.00	0.0021
313.15	80000.00	0.0023
313.15	100000.00	0.0028
313.15	120000.00	0.0032
313.15	140000.00	0.0038
333.15	100.00	0.0008
333.15	1000.00	0.0008
333.15	5000.00	0.0009
333.15	10000.00	0.0009
333.15	20000.00	0.0010
333.15	30000.00	0.0011
333.15	40000.00	0.0012
333.15	50000.00	0.0013
333.15	60000.00	0.0014
333.15	70000.00	0.0016
333.15	80000.00	0.0017
333.15	100000.00	0.0020
333.15	120000.00	0.0023
333.15	140000.00	0.0027
353.15	100.00	0.0006
353.15	1000.00	0.0006
353.15	5000.00	0.0007
353.15	10000.00	0.0007
353.15	20000.00	0.0008
353.15	30000.00	0.0009
353.15	40000.00	0.0010
353.15	50000.00	0.0010
353.15	60000.00	0.0011
353.15	70000.00	0.0012
353.15	80000.00	0.0013
353.15	100000.00	0.0015
353.15	120000.00	0.0018
353.15	140000.00	0.0020
373.15	100.00	0.0005
373.15	1000.00	0.0005
373.15	5000.00	0.0005
373.15	10000.00	0.0006
373.15	20000.00	0.0006
373.15	30000.00	0.0007
373.15	40000.00	0.0008
373.15	50000.00	0.0008
373.15	60000.00	0.0009
373.15	70000.00	0.0010
373.15	80000.00	0.0011
373.15	100000.00	0.0012
373.15	120000.00	0.0014
373.15	140000.00	0.0016
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.20	6020.00	0.0015
298.20	8050.00	0.0015
298.20	10020.00	0.0015
304.90	6020.00	0.0013
303.40	8050.00	0.0014
303.30	10020.00	0.0014
314.50	5990.00	0.0011
313.40	8000.00	0.0012
313.30	10020.00	0.0012
323.40	6050.00	0.0010
323.10	8010.00	0.0010
323.40	10000.00	0.0010
334.10	6010.00	0.0009
333.30	8030.00	0.0009
333.40	10000.00	0.0009
343.30	5990.00	0.0008
343.20	8070.00	0.0008
343.30	10010.00	0.0008
353.40	6080.00	0.0007
353.60	8020.00	0.0007
353.40	9980.00	0.0007
364.00	6040.00	0.0006
363.70	8020.00	0.0006
363.30	10050.00	0.0006
374.00	6000.00	0.0005
373.90	8020.00	0.0006
373.10	10070.00	0.0006
383.00	6010.00	0.0005
383.40	8050.00	0.0005
383.20	10000.00	0.0005
393.10	6080.00	0.0005
393.60	8030.00	0.0005
393.00	10020.00	0.0005
403.00	6040.00	0.0004
404.10	8020.00	0.0004
403.10	10040.00	0.0004
413.20	6080.00	0.0004
413.70	7990.00	0.0004
412.90	10010.00	0.0004
423.00	6080.00	0.0004
423.90	8050.00	0.0004
423.40	10000.00	0.0004
433.20	6010.00	0.0003
433.30	8000.00	0.0003
432.90	10020.00	0.0004
443.50	6020.00	0.0003
443.50	8010.00	0.0003
443.20	10050.00	0.0003
453.30	6020.00	0.0003
454.00	8040.00	0.0003
453.30	9950.00	0.0003
463.40	6040.00	0.0003
464.10	8020.00	0.0003
463.30	10010.00	0.0003
473.40	6040.00	0.0003
473.50	8010.00	0.0003
473.30	10050.00	0.0003
483.40	6050.00	0.0002
483.40	8080.00	0.0002
483.40	10000.00	0.0002
493.40	6040.00	0.0002
493.40	8010.00	0.0002
493.20	10050.00	0.0002
503.40	6080.00	0.0002
502.70	7960.00	0.0002
503.20	10010.00	0.0002
514.20	6050.00	0.0002
513.00	8040.00	0.0002
513.00	10000.00	0.0002
523.70	5970.00	0.0002
523.00	8000.00	0.0002
523.70	10040.00	0.0002
533.50	6040.00	0.0002
533.30	8040.00	0.0002
533.50	10070.00	0.0002
542.90	6010.00	0.0002
542.90	8060.00	0.0002
542.90	9950.00	0.0002
552.90	6070.00	0.0001
553.20	8010.00	0.0002
552.90	10020.00	0.0002
563.00	6050.00	0.0001
563.00	8020.00	0.0001
563.00	10020.00	0.0002
573.00	6010.00	0.0001
573.00	8020.00	0.0001
573.00	10040.00	0.0001
582.80	6000.00	0.0001
582.90	7960.00	0.0001
582.80	10010.00	0.0001
593.00	6020.00	0.0001
592.90	8070.00	0.0001
593.00	10000.00	0.0001
603.10	6010.00	0.0001
602.90	8020.00	0.0001
603.10	10010.00	0.0001
613.10	6040.00	0.0001
612.90	8020.00	0.0001
613.10	10010.00	0.0001
623.20	6050.00	0.0001
623.00	7990.00	0.0001
623.20	10050.00	0.0001
633.50	6020.00	0.0001
632.80	8040.00	0.0001
633.50	10010.00	0.0001
643.40	6020.00	0.0001
643.00	8050.00	0.0001
643.40	10010.00	0.0001
653.40	6070.00	0.0001
652.90	8020.00	0.0001
653.40	10040.00	0.0001
663.20	6010.00	0.0001
663.10	8010.00	0.0001
663.20	10050.00	0.0001
673.50	6040.00	0.0001
672.90	8010.00	0.0001
673.50	9980.00	0.0001
683.30	6010.00	0.0001
683.20	8050.00	0.0001
683.20	10040.00	0.0001
693.20	6010.00	0.0001
693.20	8020.00	0.0001
693.20	10010.00	0.0001
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
284.60	670.00	0.0018
284.70	2710.00	0.0018
284.70	4240.00	0.0018
350.50	690.00	0.0007
350.50	4250.00	0.0007
350.50	8310.00	0.0007
294.00	8310.00	0.0016
322.30	4240.00	0.0010
284.60	2190.00	0.0018
353.10	8320.00	0.0007
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.09	1022.00	735.79
313.09	2023.00	736.6
313.09	3017.00	737.36
313.09	4026.00	738.14
313.09	5023.00	738.89
313.09	6032.00	739.66
313.09	7011.00	740.38
313.09	8009.00	741.15
313.09	9026.00	741.91
313.09	10008.00	742.66
313.09	11022.00	743.39
313.09	12012.00	744.09
313.09	13019.00	744.82
313.09	14017.00	745.55
313.09	15025.00	746.22
313.09	16025.00	746.91
313.09	17015.00	747.58
313.09	18022.00	748.26
313.09	19025.00	748.93
313.09	20013.00	749.59
313.09	21015.00	750.23
313.09	22011.00	750.9
313.09	23021.00	751.53
313.09	24015.00	752.21
313.09	24354.00	752.42
322.97	1025.00	728.33
322.97	2028.00	729.17
322.97	3026.00	729.97
322.97	4034.00	730.78
322.97	5021.00	731.59
322.97	6017.00	732.37
322.97	7017.00	733.17
322.97	8041.00	733.99
322.97	9015.00	734.73
322.97	10016.00	735.5
322.97	11019.00	736.28
322.97	12011.00	737.01
322.97	13028.00	737.78
322.97	14041.00	738.53
322.97	14994.00	739.22
322.97	16027.00	739.96
322.97	17001.00	740.64
322.97	18015.00	741.35
322.97	19032.00	742.07
322.97	20004.00	742.74
322.97	21009.00	743.43
322.97	22023.00	744.14
322.97	23009.00	744.8
322.97	24013.00	745.5
322.97	24507.00	745.83
332.80	1023.00	721.08
332.80	2019.00	721.96
332.80	3022.00	722.81
332.80	4030.00	723.69
332.80	5026.00	724.53
332.80	6035.00	725.36
332.80	7014.00	726.16
332.80	8025.00	727.03
332.80	9017.00	727.84
332.80	10020.00	728.67
332.80	11023.00	729.46
332.80	12022.00	730.26
332.80	13004.00	731.04
332.80	14008.00	731.81
332.80	15018.00	732.57
332.80	16023.00	733.35
332.80	17014.00	734.08
332.80	18006.00	734.82
332.80	19024.00	735.59
332.80	20023.00	736.32
332.80	21009.00	737.01
332.80	22009.00	737.73
332.80	23018.00	738.45
332.80	24018.00	739.17
332.80	24665.00	739.63
342.69	1019.00	713.8
342.69	2025.00	714.75
342.69	3025.00	715.67
342.69	4014.00	716.58
342.69	5015.00	717.47
342.69	6017.00	718.36
342.69	7021.00	719.25
342.69	8007.00	720.13
342.69	9019.00	721.03
342.69	10018.00	721.86
342.69	11016.00	722.71
342.69	12013.00	723.56
342.69	13021.00	724.39
342.69	14020.00	725.21
342.69	15030.00	726.04
342.69	16024.00	726.83
342.69	17011.00	727.58
342.69	18025.00	728.36
342.69	19023.00	729.15
342.69	20013.00	729.88
342.69	21006.00	730.67
342.69	22021.00	731.41
342.69	23014.00	732.15
342.69	24013.00	732.89
342.69	24725.00	733.44
352.51	1021.00	706.54
352.51	2027.00	707.55
352.51	3013.00	708.48
352.51	4019.00	709.46
352.51	5027.00	710.45
352.51	6014.00	711.35
352.51	7020.00	712.33
352.51	8000.00	713.23
352.51	9024.00	714.18
352.51	10009.00	715.07
352.51	11022.00	715.96
352.51	12012.00	716.84
352.51	13026.00	717.71
352.51	14017.00	718.6
352.51	15021.00	719.45
352.51	16022.00	720.3
352.51	17012.00	721.08
352.51	18027.00	721.95
352.51	19013.00	722.74
352.51	20028.00	723.53
352.51	21021.00	724.33
352.51	22023.00	725.14
352.51	23008.00	725.88
352.51	24020.00	726.65
352.51	24813.00	727.31
362.29	1015.00	699.21
362.29	2020.00	700.31
362.29	3015.00	701.33
362.29	4012.00	702.34
362.29	5029.00	703.4
362.29	6009.00	704.36
362.29	7029.00	705.38
362.29	8013.00	706.3
362.29	9012.00	707.31
362.29	10038.00	708.31
362.29	11027.00	709.22
362.29	12009.00	710.09
362.29	13007.00	711.04
362.29	14015.00	711.96
362.29	15008.00	712.81
362.29	16034.00	713.71
362.29	17030.00	714.59
362.29	18011.00	715.43
362.29	19021.00	716.29
362.29	20007.00	717.15
362.29	21017.00	717.94
362.29	22032.00	718.77
362.29	23002.00	719.6
362.29	24005.00	720.38
362.29	24809.00	721.05
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	745.23
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.00	2100.00	752.3
293.00	3100.00	752.9
293.00	4100.00	753.6
293.00	5000.00	754.2
293.00	10100.00	757.5
293.00	20000.00	763.5
293.00	30000.00	769.0
293.00	40000.00	774.3
293.00	50000.00	779.0
293.00	60000.00	783.8
293.00	69900.00	788.0
293.00	79900.00	792.5
293.00	89900.00	796.7
293.00	99900.00	800.8
293.00	109900.00	804.8
293.00	119900.00	808.7
293.00	129900.00	812.4
293.00	134900.00	814.4
293.00	137400.00	815.2
313.00	2100.00	737.7
313.00	3100.00	738.5
313.00	4100.00	739.2
313.00	5000.00	739.9
313.00	10100.00	743.4
313.00	20000.00	750.1
313.00	30000.00	756.3
313.00	40000.00	761.8
313.00	50000.00	767.1
313.00	60000.00	772.1
313.00	69900.00	777.0
313.00	79900.00	781.6
313.00	89900.00	786.1
313.00	99900.00	790.4
313.00	109900.00	794.6
313.00	119900.00	798.7
313.00	129900.00	802.7
313.00	134900.00	804.6
313.00	137400.00	805.4
333.00	2100.00	722.8
333.00	3100.00	723.6
333.00	4100.00	724.5
333.00	5000.00	725.3
333.00	10100.00	729.4
333.00	20000.00	736.6
333.00	30000.00	743.4
333.00	40000.00	749.6
333.00	50000.00	755.3
333.00	60000.00	760.8
333.00	69900.00	766.0
333.00	79900.00	770.9
333.00	89900.00	775.7
333.00	99900.00	780.1
333.00	109900.00	784.6
333.00	119900.00	788.8
333.00	129900.00	793.2
333.00	134900.00	795.1
333.00	137400.00	796.0
353.00	2100.00	708.1
353.00	3100.00	709.0
353.00	4100.00	710.0
353.00	5000.00	710.9
353.00	10100.00	715.6
353.00	20000.00	723.9
353.00	30000.00	731.3
353.00	40000.00	737.7
353.00	50000.00	744.1
353.00	60000.00	750.1
353.00	69900.00	755.6
353.00	79900.00	760.7
353.00	89900.00	765.7
353.00	99900.00	770.5
353.00	109900.00	775.1
353.00	119900.00	779.6
353.00	129900.00	784.0
353.00	134900.00	786.0
353.00	137400.00	787.0
373.00	2100.00	693.2
373.00	3100.00	694.3
373.00	4100.00	695.3
373.00	5000.00	696.3
373.00	10100.00	701.5
373.00	20000.00	710.8
373.00	30000.00	718.7
373.00	40000.00	726.0
373.00	50000.00	733.1
373.00	60000.00	739.4
373.00	69900.00	745.2
373.00	79900.00	750.7
373.00	89900.00	756.0
373.00	99900.00	761.0
373.00	109900.00	765.9
373.00	119900.00	770.6
373.00	129900.00	775.1
373.00	134900.00	777.4
373.00	137400.00	778.5
393.00	2100.00	678.1
393.00	3100.00	679.2
393.00	4100.00	680.4
393.00	5000.00	681.6
393.00	10100.00	687.5
393.00	20000.00	697.8
393.00	30000.00	706.6
393.00	40000.00	714.7
393.00	50000.00	722.2
393.00	60000.00	728.7
393.00	69900.00	735.1
393.00	79900.00	741.1
393.00	89900.00	746.8
393.00	99900.00	752.2
393.00	109900.00	757.2
393.00	119900.00	762.0
393.00	129900.00	766.8
393.00	134900.00	769.0
393.00	137400.00	770.2
413.00	2100.00	662.8
413.00	3100.00	664.2
413.00	4100.00	665.6
413.00	5000.00	666.9
413.00	10100.00	673.7
413.00	20000.00	685.1
413.00	30000.00	694.9
413.00	40000.00	703.6
413.00	50000.00	711.4
413.00	60000.00	718.7
413.00	69900.00	725.4
413.00	79900.00	731.7
413.00	89900.00	737.3
413.00	99900.00	743.2
413.00	109900.00	748.5
413.00	119900.00	753.7
413.00	129900.00	758.5
413.00	134900.00	760.9
413.00	137400.00	762.0
433.00	2100.00	646.8
433.00	3100.00	648.5
433.00	4100.00	650.0
433.00	5000.00	651.6
433.00	10100.00	659.5
433.00	20000.00	672.0
433.00	30000.00	682.8
433.00	40000.00	692.1
433.00	50000.00	700.6
433.00	60000.00	708.3
433.00	69900.00	715.6
433.00	79900.00	722.1
433.00	89900.00	728.3
433.00	99900.00	734.3
433.00	109900.00	739.8
433.00	119900.00	745.1
433.00	129900.00	750.3
433.00	134900.00	752.7
433.00	137400.00	753.9
448.00	2100.00	634.6
448.00	3100.00	636.7
448.00	4100.00	638.2
448.00	5000.00	640.0
448.00	10100.00	648.5
448.00	20000.00	662.4
448.00	30000.00	674.0
448.00	40000.00	684.0
448.00	50000.00	692.9
448.00	60000.00	701.0
448.00	69900.00	708.3
448.00	79900.00	715.3
448.00	89900.00	721.9
448.00	99900.00	727.9
448.00	109900.00	733.5
448.00	119900.00	739.0
448.00	129900.00	744.2
448.00	134900.00	746.7
448.00	137400.00	747.9
468.00	2100.00	617.8
468.00	3100.00	619.9
468.00	4100.00	622.0
468.00	5000.00	624.1
468.00	10100.00	634.1
468.00	20000.00	649.5
468.00	30000.00	661.8
468.00	40000.00	672.8
468.00	50000.00	682.6
468.00	60000.00	691.0
468.00	69900.00	698.9
468.00	79900.00	706.3
468.00	89900.00	712.9
468.00	99900.00	719.2
468.00	109900.00	725.1
468.00	119900.00	731.0
468.00	129900.00	736.3
468.00	134900.00	738.9
468.00	137400.00	740.2
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.29	100.00	756.0
283.29	1000.00	757.0
283.29	3000.00	758.0
283.30	5000.00	760.0
283.30	10000.00	763.0
283.31	20000.00	769.0
283.30	30000.00	775.0
283.30	40000.00	780.0
283.30	50000.00	785.0
283.30	60000.00	790.0
283.31	70000.00	795.0
283.32	80000.00	799.0
283.32	90000.00	803.0
293.17	100.00	749.0
293.18	1000.00	750.0
293.19	5000.00	753.0
293.19	10000.00	756.0
293.19	20000.00	763.0
293.19	30000.00	769.0
293.19	40000.00	774.0
293.19	50000.00	780.0
293.20	60000.00	785.0
293.19	70000.00	789.0
293.19	80000.00	794.0
293.19	90000.00	798.0
293.19	100000.00	802.0
303.05	100.00	742.0
303.05	1000.00	743.0
303.05	5000.00	746.0
303.06	10000.00	749.0
303.05	20000.00	756.0
303.04	30000.00	762.0
303.06	40000.00	768.0
303.05	50000.00	774.0
303.05	60000.00	779.0
303.05	70000.00	784.0
303.05	80000.00	789.0
303.05	90000.00	793.0
303.04	100000.00	797.0
312.89	100.00	736.0
312.89	1000.00	737.0
312.90	5000.00	740.0
312.90	10000.00	744.0
312.90	20000.00	751.0
312.90	30000.00	757.0
312.90	40000.00	763.0
312.90	50000.00	769.0
312.90	60000.00	774.0
312.90	70000.00	780.0
312.90	80000.00	784.0
312.90	90000.00	789.0
312.90	100000.00	793.0
322.83	100.00	727.0
322.83	1000.00	728.0
322.83	5000.00	732.0
322.83	10000.00	736.0
322.83	20000.00	743.0
322.83	30000.00	750.0
322.83	40000.00	756.0
322.83	50000.00	762.0
322.83	60000.00	768.0
322.83	70000.00	773.0
322.83	80000.00	778.0
322.83	90000.00	783.0
322.83	100000.00	787.0
332.74	100.00	720.0
332.74	1000.00	721.0
332.74	5000.00	725.0
332.74	10000.00	729.0
332.74	20000.00	737.0
332.74	30000.00	744.0
332.74	40000.00	750.0
332.74	50000.00	757.0
332.74	60000.00	762.0
332.74	70000.00	768.0
332.74	80000.00	773.0
332.74	90000.00	778.0
332.75	100000.00	782.0
342.67	100.00	713.0
342.67	1000.00	714.0
342.67	5000.00	718.0
342.67	10000.00	722.0
342.67	20000.00	731.0
342.67	30000.00	738.0
342.67	40000.00	745.0
342.67	50000.00	751.0
342.67	60000.00	757.0
342.67	69990.00	763.0
342.67	80000.00	768.0
342.67	90000.00	773.0
342.67	100000.00	778.0
352.58	100.00	707.0
352.58	1000.00	708.0
352.58	5000.00	712.0
352.58	10000.00	716.0
352.58	20000.00	725.0
352.58	30000.00	733.0
352.58	40000.00	740.0
352.58	50000.00	747.0
352.58	60000.00	753.0
352.58	70000.00	759.0
352.58	80000.00	764.0
352.58	90000.00	769.0
352.58	100000.00	774.0
362.49	100.00	699.0
362.49	1000.00	700.0
362.48	5000.00	704.0
362.48	10000.00	709.0
362.48	20000.00	718.0
362.48	30000.00	726.0
362.49	40000.00	734.0
362.48	50000.00	741.0
362.49	60000.00	747.0
362.49	70000.00	753.0
362.48	80000.00	759.0
362.48	90000.00	764.0
362.49	100000.00	769.0
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
278.15	100.00	759.2
278.15	1000.00	760.5
278.15	5000.00	763.1
278.15	10000.00	766.2
278.15	20000.00	771.9
278.15	30000.00	777.3
278.15	40000.00	782.3
278.15	50000.00	787.1
278.15	60000.00	791.7
298.15	100.00	745.6
298.15	1000.00	746.2
298.15	5000.00	749.0
298.15	10000.00	752.4
298.15	20000.00	758.7
298.15	30000.00	764.7
298.15	40000.00	770.1
298.15	50000.00	775.3
298.15	60000.00	780.2
323.15	100.00	727.2
323.15	1000.00	728.2
323.15	5000.00	731.4
323.15	10000.00	735.3
323.15	20000.00	742.6
323.15	30000.00	749.2
323.15	40000.00	755.2
323.15	50000.00	760.9
323.15	60000.00	766.3
348.15	100.00	708.7
348.15	1000.00	709.6
348.15	5000.00	713.4
348.15	10000.00	717.8
348.15	20000.00	726.1
348.15	30000.00	733.5
348.15	40000.00	740.2
348.15	50000.00	746.4
348.15	60000.00	752.3
373.15	1000.00	690.8
373.15	5000.00	695.2
373.15	10000.00	700.4
373.15	20000.00	709.8
373.15	30000.00	718.1
373.15	40000.00	725.6
373.15	50000.00	732.5
373.15	60000.00	738.9
423.15	1000.00	652.6
423.15	5000.00	658.7
423.15	10000.00	665.6
423.15	20000.00	677.6
423.15	30000.00	688.0
423.15	40000.00	697.0
423.15	50000.00	705.3
423.15	60000.00	712.8
463.15	5000.00	627.9
463.15	10000.00	636.9
463.15	20000.00	651.8
463.15	30000.00	664.2
463.15	40000.00	674.8
463.15	50000.00	684.1
463.15	60000.00	692.6
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.21	2007.00	750.58
293.21	3977.00	752.18
293.21	5979.00	753.71
293.21	7982.00	755.06
293.22	9987.00	756.38
293.21	12987.00	758.27
293.22	15986.00	760.07
293.22	18994.00	761.82
293.22	21995.00	763.63
293.22	24987.00	765.5
293.22	27987.00	767.37
293.21	29985.00	768.5
313.10	1990.00	736.16
313.10	4017.00	737.72
313.10	6016.00	739.14
313.10	8014.00	740.64
313.10	10011.00	742.11
313.10	13007.00	744.26
313.10	16011.00	746.36
313.10	19017.00	748.61
313.10	22017.00	750.69
313.10	25019.00	752.63
313.10	28017.00	754.52
313.10	30020.00	755.75
333.01	2024.00	721.82
333.00	3976.00	723.61
333.01	5981.00	725.32
333.01	7987.00	726.99
333.01	10019.00	728.35
333.01	13016.00	730.73
333.01	16014.00	733.04
333.01	19018.00	735.29
333.01	22015.00	737.46
333.01	25018.00	739.58
333.01	28015.00	741.65
333.01	30024.00	742.99
353.12	2000.00	706.86
353.12	3991.00	708.83
353.12	5996.00	710.75
353.12	8009.00	712.81
353.12	10014.00	714.63
353.12	13006.00	717.28
353.12	16007.00	719.83
353.12	19003.00	722.16
353.12	22006.00	724.55
353.12	25008.00	726.87
353.12	28011.00	729.13
353.12	30007.00	730.59
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	745.29
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.53	8012.00	740.43
313.50	9962.00	741.88
313.50	12011.00	743.35
313.52	13987.00	744.76
313.48	16030.00	746.15
313.48	17972.00	747.51
323.46	7994.00	733.56
323.48	9968.00	735.18
323.57	11960.00	736.57
323.52	13993.00	738.13
323.49	16021.00	739.64
323.49	18018.00	741.06
333.55	8003.00	726.32
333.51	9996.00	727.99
333.55	11980.00	729.56
333.56	13998.00	731.15
333.53	15975.00	732.68
333.52	17973.00	734.22
343.50	7959.00	719.25
343.50	10036.00	721.04
343.48	11000.00	721.9
343.48	11993.00	722.72
343.47	12998.00	723.59
343.52	13977.00	724.32
343.54	14989.00	725.15
343.55	15979.00	725.97
343.56	16970.00	726.72
343.56	18004.00	727.54
353.57	8022.00	712.16
353.57	10035.00	713.95
353.58	11021.00	714.86
353.58	12000.00	715.73
353.56	13021.00	716.67
353.56	13976.00	717.47
353.52	15037.00	718.45
353.55	15991.00	719.22
353.59	17027.00	720.07
353.53	17993.00	720.9
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	283.15	756.0
100.00	288.15	752.4
100.00	293.15	748.8
100.00	298.15	745.3
100.00	303.15	741.7
100.00	308.15	738.1
100.00	313.15	734.4
100.00	318.15	730.8
100.00	323.15	727.1
10000.00	283.15	762.4
10000.00	288.15	758.9
10000.00	293.15	755.5
10000.00	298.15	752.1
10000.00	303.15	748.7
10000.00	308.15	745.3
10000.00	313.15	741.8
10000.00	318.15	738.4
10000.00	323.15	734.9
20000.00	283.15	768.3
20000.00	288.15	765.1
20000.00	293.15	761.7
20000.00	298.15	758.5
20000.00	303.15	755.2
20000.00	308.15	752.0
20000.00	313.15	748.7
20000.00	318.15	745.4
20000.00	323.15	742.0
30000.00	283.15	773.9
30000.00	288.15	770.7
30000.00	293.15	767.6
30000.00	298.15	764.4
30000.00	303.15	761.3
30000.00	308.15	758.2
30000.00	313.15	755.0
30000.00	318.15	751.9
30000.00	323.15	748.6
40000.00	283.15	779.2
40000.00	288.15	776.1
40000.00	293.15	773.1
40000.00	298.15	770.0
40000.00	303.15	767.0
40000.00	308.15	764.0
40000.00	313.15	760.9
40000.00	318.15	757.9
40000.00	323.15	754.8
50000.00	283.15	784.1
50000.00	288.15	781.2
50000.00	293.15	778.2
50000.00	298.15	775.3
50000.00	303.15	772.4
50000.00	308.15	769.4
50000.00	313.15	766.4
50000.00	318.15	763.5
50000.00	323.15	760.5
60000.00	283.15	788.6
60000.00	288.15	786.0
60000.00	293.15	783.2
60000.00	298.15	780.3
60000.00	303.15	777.5
60000.00	308.15	774.6
60000.00	313.15	771.7
60000.00	318.15	768.8
60000.00	323.15	765.9
Reference

Speed of sound, m/s

Operational condition: Frequency, MHz = 3 (Liquid)

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
10000.00	303.15	1318.5
20000.00	303.15	1372.4
30000.00	303.15	1421.4
40000.00	303.15	1468.5
50000.00	303.15	1512.3
60000.00	303.15	1553.7
70000.00	303.15	1593.3
10000.00	313.15	1281.7
20000.00	313.15	1337.9
30000.00	313.15	1389.6
40000.00	313.15	1436.8
50000.00	313.15	1481.5
60000.00	313.15	1524.2
70000.00	313.15	1564.6
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[220.50; 744.64]	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			1.93680e+02
Coefficient B			-7.32610e+02
Coefficient C			6.99424e+00
Coefficient D			-2.22840e-04
Coefficient E			6.22570e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	220.50	J/mol×K	200.00	Calculated Property
Cp,gas	314.94	J/mol×K	344.44	Calculated Property
Cp,gas	415.45	J/mol×K	488.89	Calculated Property
Cp,gas	498.99	J/mol×K	633.33	Calculated Property
Cp,gas	564.85	J/mol×K	777.78	Calculated Property
Cp,gas	616.65	J/mol×K	922.22	Calculated Property
Cp,gas	657.99	J/mol×K	1066.67	Calculated Property
Cp,gas	691.77	J/mol×K	1211.11	Calculated Property
Cp,gas	720.11	J/mol×K	1355.56	Calculated Property
Cp,gas	744.64	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[362.49; 497.07]	J/mol×K	[263.57; 433.15]	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			2.03950e+02
Coefficient B			6.27310e+02
Coefficient C			-6.28155e-01
Coefficient D			1.46760e-02
Coefficient E			-7.97580e-06
Temperature range, min.			263.57
Temperature range, max.			433.15
Cp,liquid	362.49	J/mol×K	263.57	Calculated Property
Cp,liquid	368.24	J/mol×K	282.41	Calculated Property
Cp,liquid	376.65	J/mol×K	301.25	Calculated Property
Cp,liquid	387.43	J/mol×K	320.10	Calculated Property
Cp,liquid	400.45	J/mol×K	338.94	Calculated Property
Cp,liquid	415.62	J/mol×K	357.78	Calculated Property
Cp,liquid	432.89	J/mol×K	376.62	Calculated Property
Cp,liquid	452.24	J/mol×K	395.47	Calculated Property
Cp,liquid	473.64	J/mol×K	414.31	Calculated Property
Cp,liquid	497.07	J/mol×K	433.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0029471; 0.0000535]	Pa×s	[262.15; 658.00]	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			-8.32111e+01
Coefficient B			4.23831e+03
Coefficient C			1.11464e+01
Coefficient D			-1.24656e-05
Coefficient E			2.00000e+00
Temperature range, min.			262.15
Temperature range, max.			658.00
η	0.0029471	Pa×s	262.15	Calculated Property
η	0.0011915	Pa×s	306.13	Calculated Property
η	0.0006522	Pa×s	350.12	Calculated Property
η	0.0004200	Pa×s	394.10	Calculated Property
η	0.0002940	Pa×s	438.08	Calculated Property
η	0.0002133	Pa×s	482.07	Calculated Property
η	0.0001558	Pa×s	526.05	Calculated Property
η	0.0001122	Pa×s	570.03	Calculated Property
η	0.0000788	Pa×s	614.02	Calculated Property
η	0.0000535	Pa×s	658.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[65.06; 0.00]	kJ/mol	[263.57; 658.00]	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			9.81298e+01
Coefficient B			9.39672e-01
Coefficient C			-4.12509e-02
Coefficient D			-9.49322e-01
Coefficient E			5.01567e-01
Critical temperature, Tc (K)			6.58000e+02
Temperature range, min.			263.57
Temperature range, max.			658.00
ΔvapH	65.06	kJ/mol	263.57	Calculated Property
ΔvapH	60.65	kJ/mol	307.40	Calculated Property
ΔvapH	56.50	kJ/mol	351.22	Calculated Property
ΔvapH	52.53	kJ/mol	395.05	Calculated Property
ΔvapH	48.62	kJ/mol	438.87	Calculated Property
ΔvapH	44.58	kJ/mol	482.70	Calculated Property
ΔvapH	40.09	kJ/mol	526.52	Calculated Property
ΔvapH	34.59	kJ/mol	570.35	Calculated Property
ΔvapH	26.59	kJ/mol	614.17	Calculated Property
ΔvapH	0.00	kJ/mol	658.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[6.30e-04; 1753.46]	kPa	[263.57; 658.00]	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			1.20980e+02
Coefficient B			-1.15821e+04
Coefficient C			-1.52254e+01
Coefficient D			6.68003e-06
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 658.15 K.
Temperature range, min.			263.57
Temperature range, max.			658.00
Pvap	6.30e-04	kPa	263.57	Calculated Property
Pvap	0.04	kPa	307.40	Calculated Property
Pvap	0.66	kPa	351.22	Calculated Property
Pvap	5.32	kPa	395.05	Calculated Property
Pvap	25.57	kPa	438.87	Calculated Property
Pvap	86.32	kPa	482.70	Calculated Property
Pvap	227.59	kPa	526.52	Calculated Property
Pvap	503.53	kPa	570.35	Calculated Property
Pvap	982.71	kPa	614.17	Calculated Property
Pvap	1753.46	kPa	658.00	Calculated Property
Pvap	[6.62e-04; 1746.95]	kPa	[263.57; 658.20]	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			1.12723e+02
Coefficient B			-1.12005e+04
Coefficient C			-1.39838e+01
Coefficient D			5.78857e-06
Coefficient E			0.00000e+00
Temperature range, min.			263.57
Temperature range, max.			658.20
Pvap	6.62e-04	kPa	263.57	Calculated Property
Pvap	0.04	kPa	307.42	Calculated Property
Pvap	0.66	kPa	351.27	Calculated Property
Pvap	5.30	kPa	395.11	Calculated Property
Pvap	25.51	kPa	438.96	Calculated Property
Pvap	86.39	kPa	482.81	Calculated Property
Pvap	228.37	kPa	526.66	Calculated Property
Pvap	505.56	kPa	570.50	Calculated Property
Pvap	984.52	kPa	614.35	Calculated Property
Pvap	1746.95	kPa	658.20	Calculated Property
Pvap	[6.37; 103.91]	kPa	[399.53; 490.49]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40584e+01
Coefficient B			-3.74384e+03
Coefficient C			-9.28390e+01
Reference			Williamham, Taylor, et al., 1945
Temperature range, min.			399.53
Temperature range, max.			490.49
Pvap	6.37	kPa	399.53	Calculated Property
Pvap	9.40	kPa	409.64	Calculated Property
Pvap	13.54	kPa	419.74	Calculated Property
Pvap	19.10	kPa	429.85	Calculated Property
Pvap	26.39	kPa	439.96	Calculated Property
Pvap	35.80	kPa	450.06	Calculated Property
Pvap	47.77	kPa	460.17	Calculated Property
Pvap	62.76	kPa	470.28	Calculated Property
Pvap	81.29	kPa	480.38	Calculated Property
Pvap	103.91	kPa	490.49	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[768.93; 218.78]	kg/m3	[263.15; 658.00]	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			5.16694e+01
Coefficient B			2.36170e-01
Coefficient C			6.58000e+02
Coefficient D			2.70600e-01
Temperature range, min.			263.15
Temperature range, max.			658.00
ρl	768.93	kg/m3	263.15	Calculated Property
ρl	739.20	kg/m3	307.02	Calculated Property
ρl	707.94	kg/m3	350.89	Calculated Property
ρl	674.78	kg/m3	394.77	Calculated Property
ρl	639.17	kg/m3	438.64	Calculated Property
ρl	600.25	kg/m3	482.51	Calculated Property
ρl	556.55	kg/m3	526.38	Calculated Property
ρl	505.09	kg/m3	570.26	Calculated Property
ρl	437.75	kg/m3	614.13	Calculated Property
ρl	218.78	kg/m3	658.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.01]	N/m	[263.15; 489.15]	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			5.12665e-02
Coefficient B			-8.84000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			263.15
Temperature range, max.			489.15
γ	0.03	N/m	263.15	Calculated Property
γ	0.03	N/m	288.26	Calculated Property
γ	0.02	N/m	313.37	Calculated Property
γ	0.02	N/m	338.48	Calculated Property
γ	0.02	N/m	363.59	Calculated Property
γ	0.02	N/m	388.71	Calculated Property
γ	0.01	N/m	413.82	Calculated Property
γ	0.01	N/m	438.93	Calculated Property
γ	0.01	N/m	464.04	Calculated Property
γ	0.01	N/m	489.15	Calculated Property
γ	[0.03; 4.41e-06]	N/m	[263.57; 653.27]	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			-4.94040e-03
Coefficient B			1.62060e+02
Coefficient C			-4.43540e+00
Coefficient D			3.78650e-03
Coefficient E			-8.42560e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 658 K.
Temperature range, min.			263.57
Temperature range, max.			653.27
γ	0.03	N/m	263.57	Calculated Property
γ	0.02	N/m	306.87	Calculated Property
γ	0.02	N/m	350.17	Calculated Property
γ	0.02	N/m	393.47	Calculated Property
γ	0.01	N/m	436.77	Calculated Property
γ	0.01	N/m	480.07	Calculated Property
γ	0.01	N/m	523.37	Calculated Property
γ	0.00	N/m	566.67	Calculated Property
γ	0.00	N/m	609.97	Calculated Property
γ	4.41e-06	N/m	653.27	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.09]	W/m×K	[263.57; 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			5.55040e-06
Coefficient B			1.47260e+00
Coefficient C			5.58150e+02
Coefficient D			3.56360e+03
Temperature range, min.			263.57
Temperature range, max.			1000.00
λgas	0.01	W/m×K	263.57	Calculated Property
λgas	0.01	W/m×K	345.39	Calculated Property
λgas	0.02	W/m×K	427.22	Calculated Property
λgas	0.03	W/m×K	509.05	Calculated Property
λgas	0.03	W/m×K	590.87	Calculated Property
λgas	0.04	W/m×K	672.70	Calculated Property
λgas	0.05	W/m×K	754.52	Calculated Property
λgas	0.07	W/m×K	836.35	Calculated Property
λgas	0.08	W/m×K	918.17	Calculated Property
λgas	0.09	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.09]	W/m×K	[263.44; 489.47]	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			2.93640e-02
Coefficient B			-1.08040e+02
Coefficient C			-7.00700e-01
Coefficient D			-4.07910e-03
Coefficient E			6.13770e-07
Temperature range, min.			263.44
Temperature range, max.			489.47
λliquid	0.15	W/m×K	263.44	Calculated Property
λliquid	0.14	W/m×K	288.55	Calculated Property
λliquid	0.13	W/m×K	313.67	Calculated Property
λliquid	0.13	W/m×K	338.78	Calculated Property
λliquid	0.12	W/m×K	363.90	Calculated Property
λliquid	0.11	W/m×K	389.01	Calculated Property
λliquid	0.11	W/m×K	414.13	Calculated Property
λliquid	0.10	W/m×K	439.24	Calculated Property
λliquid	0.10	W/m×K	464.36	Calculated Property
λliquid	0.09	W/m×K	489.47	Calculated Property

Similar Compounds

Find more compounds similar to Dodecane.

Mixtures

• Dodecane + Propane, 2-methoxy-2-methyl- + Pentane, 3-methyl-
• Dodecane + 2,5,8,11,14-Pentaoxapentadecane
• Dodecane + 1-Octanol
• Dodecane + 1-Decanol
• Dodecane + Tri-n-butylphosphate + 1-Octanol
• Pentanoic acid, ethyl ester + Dodecane
• Dodecane + Ethyl Acetate
• Pentanoic acid, ethyl ester + Dodecane + Ethyl Acetate
• Benzo[b]thiophene + Dodecane
• Carbon dioxide + Dodecane + 1-Decanol
• Dodecane + Anisole
• Dodecane + Heptane
• Hexadecane + Dodecane + Octane
• Dodecane + Isopropyl acetate
• Benzonitrile + Dodecane
• Dodecane + Naphthalene, 1,2,3,4-tetrahydro-
• Dodecane + Acetophenone
• 2,5,8,11-Tetraoxadodecane + Dodecane
• Dodecane + Methyl Alcohol
• Dodecane + Acetic acid, methyl ester + Methyl Alcohol

Find more mixtures with Dodecane.

Sources

• KDB Vapor Pressure Data
• 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.
• Cheméo Relay (1.0)
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Crippen Method
• Activity coefficient at infinite dilution, azeotropic data, excess enthalpies and solid liquid-equilibria for binary systems of alkanes and aromatics with esters
• Liquid liquid equilibria for n-alkanes (C12, C14, C17) + propylbenzene +NMP mixtures at temperatures between 298 and 328K
• Phase equilibria for the extraction of sec-butylbenzene from dodecane with N,N-dimethylformamide
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• Thermodynamics of mixtures containing amines VI. Liquid liquid equilibria for mixtures of o-toluidine + selected alkanes
• High-pressure vapor liquid equilibria for CO2 + alkanol systems and densities of n-dodecane and n-tridecane
• Solution thermodynamics near the liquid liquid critical point I. First-order excess derivatives
• Thiophene separation from aliphatic hydrocarbons using the 1-ethyl-3-methylimidazolium ethylsulfate ionic liquid
• Ionic liquids on desulfurization of fuel oils
• Determination and correlation of liquid-liquid equilibria for nine binary acetonitrile + n-alkane systems
• Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
• P-x data for binary systems using a novel static total pressure apparatus
• Liquid-liquid equilibria of mixtures with ethyl lactate and various hydrocarbons
• Liquid-liquid equilibria for aqueous sulfuric acid solutions with undecane, dodecane, or 1-dodecanol, trioctylamine or tributyl phosphate and excess and deviation properties for sub-binary systems at 298.15 K
• Liquid-liquid equilibria for ternary systems acetic acid + n-butylacetate + hydrocarbons at 293.15 K
• Interfacial tension of binary mixtures exhibiting azeotropic behavior: Measurement and modeling with PCP-SAFT combined with Density Gradient Theory
• Liquid-liquid equilibria for benzaldehyde + n-alkane mixtures andcharacterization of benzaldehyde + hydrocarbon systems in terms of DISQUAC
• Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
• High-pressure densities and interfacial tensions of binary systems containing carbon dioxide + n-alkanes: (n-Dodecane, n-tridecane, n-tetradecane)
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• Liquid liquid equilibria measurements of ternary systems (acetonitrile + a carboxylic acid + dodecane) at 303.15 K
• Liquid liquid equilibria for acetophenone + n-alkane mixtures and characterization of acetophenone systems using DISQUAC
• Speed of sound and thermodynamic properties of ternary liquid mixture octane + dodecane + hexadecane
• High pressure phase behaviour of the CO2 + 1-decanol + n-dodecane system
• Liquid-liquid-liquid equilibria for water + [P6 6 6 14][DCA] + dodecane ternary system
• Study of the suitability of two ammonium-based ionic liquids for the extraction of benzene from its mixtures with aliphatic hydrocarbons.
• Thermodynamics of aromatic polar compound (alkanone, alkanal or alkanoate) + hydrocarbon mixtures
• An experimental investigation on the solubility of methane in 1-octanol and n-dodecane at ambient temperatures
• Determination of solubility parameters from density measurements for non-polar hydrocarbons at temperatures from (298 to 433) K and pressures up to 137 MPa
• Volume expansion prediction of supercritical CO 2 + crude oil
• Compressed liquid densities of binary mixtures of n-decane + n-dodecane at temperatures from 283 K to 363 K and pressures up to 100 MPa
• High temperature and pressure water/oil interfacial tension benchmark data for the Ninth Industrial Fluid Properties Simulation Challenge
• Thermal conductivity of heavy, even-carbon number n-alkanes (C22 to C32)
• Permittivity and density of binary systems of {dimethyl or diethyl carbonate} + n-dodecane from T=(288.15 to 328.15) K
• Liquid--liquid equilibria for mixtures of {methyl acetate + methanol + n-alkane (C10--C12)} at several temperatures and 1 atm
• Dynamic viscosities of 2-butanol with alkanes (C8, C10, and C12) at several temperatures
• 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
• Excess molar enthalpies of the ternary mixtures: methyl tert-butyl ether +2-methylpentane + (n-decane or n-dodecane) at the temperature 298.15 K
• On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
• Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
• Excess molar enthalpies of the ternary mixtures: {tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether + n-dodecane} at the temperature 298.15 K
• Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
• (Liquid + liquid) equilibria for ternary mixtures of (methanol or ethanol + toluene or m-xylene + n-dodecane)
• On the permittivity and density of the systems {tetraglyme + (n-nonane or n-dodecane)} at various temperatures
• Ternary (liquid + liquid) equilibria for mixtures of (methanol + aniline + n-octane or n-dodecane) at T = 298.15 K
• (Liquid + liquid) equilibria of [C8mim][NTf2] ionic liquid with a sulfur-component and hydrocarbons
• 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]
• Thermodynamic and acoustic properties of (heptane + dodecane) mixtures under elevated pressures
• Partition behaviour of benzoic acid in (water + n-dodecane) solutions at T = (293.15 and 298.15) K
• Activity coefficients at infinite dilution of hydrocarbons, alkylbenzenes, and alcohols in the paramagnetic ionic liquid 1-butyl-3-methyl-imidazolium tetrachloridoferrate(III) using gas liquid chromatography
• Excess molar enthalpies of binary mixtures containing 2-decanone or dipentyl ether with long-chain n-alkanes at T = 298.15 K
• Interfacial tensions of binary mixtures of ethanol with octane, decane, dodecane, and tetradecane
• Extraction of propylbenzene or butylbenzene from dodecane using 4-methyl-N-butylpyridinium tetrafluoroborate, [mebupy][BF4], as an ionic liquid at different temperatures
• (Liquid + liquid) equilibria for the ternary system (water + dodecane + propylene glycol n-propyl ether)
• Correlation and prediction of mixing thermodynamic properties of ester-containing systems: Ester + alkane and ester + ester binary systems and the ternary dodecane + ethyl pentanoate + ethyl ethanoate
• Evaluation of [bmim][PF6] as an ionic solvent for the extraction of propylbenzene from aliphatic compounds
• Thermodynamic modeling and experimental speeds of sound, densities, and refractive indexes of (tetralin + n-dodecane)
• Universal critical amplitude ratios in binary mixtures of {benzonitrile + alkane}
• Physical properties of phosphonium ionic liquid and its mixtures with dodecane and water
• Water/oil/[P6,6,6,14][NTf2] phase equilibria
• (Liquid + liquid) equilibria for mixtures of dodecane and ethanol with alkylsulfate-based ionic liquids
• Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
• Study of the binary mixtures of {monoglyme + (hexane, cyclohexane, octane, dodecane)} by ECM-average and PFP models
• Thermodynamics of mixing for binary mixtures of 1-octanol and 1-decanol with n-dodecane and ternary mixture of (TBP + 1-octanol + dodecane) at T = (298.15 to 323.15) K
• Contributing to accurate high pressure viscosity measurements: Vibrating wire viscometer and falling body viscometer techniques
• Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
• Experimental solubility of diosgenin and estriol in various solvents between T = (293.2-328.2) K
• Heat capacity and Joule-Thomson coefficient of selected n-alkanes at 0.1 and 10 MPa in broad temperature ranges
• Phase equilibrium measurements and thermodynamic modeling of binary mixtures containing a diesel compound n-dodecane + biodiesel compounds: Ethyl dodecanoate and ethyl octanoate
• Determination of thermophysical properties of cyclopentane hydrate using a stirred calorimetric cell
• Thermophysical properties of fatty acid methyl and ethyl esters
• Excess molar enthalpies of the ternary mixtures: methyl tert-butyl ether + 3-methylpentane + (n-decane or n-dodecane) at 298.15K
• Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
• Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
• 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
• Viscous Calibration Liquids for Self-diffusion Measurements
• Prediction and Experimental Measurement of Refractive Index in Ternary Hydrocarbon Mixtures
• Mass Diffusion Coefficient and Soret Coefficient of o-Dichlorobenzene Solutions of PCBM and [60]Fullerene by the Soret Forced Rayleigh Scattering Method
• Experimental and Computational Study on Liquid Liquid Equilibrium in Ternary Systems of -Valerolactone, Toluene, and Hydrocarbons
• Densities of the binary systems n-hexane + n-decane and nhexane + n-hexadecane up to 60 MPa and 463 K
• Thermal and Mutual Diffusivity of Binary Mixtures of n-Dodecane and n-Tetracontane with Carbon Monoxide, Hydrogen, and Water from Dynamic Light Scattering (DLS)
• Liquid Liquid Equilibria of Binary and Ternary Systems Methanol/Water + n-Hexane, + n-Octane, + n-Dodecane, and + n-Hexadecane in the Temperature Range between T = 283.15 K and T = 333.15 K
• Equilibrium Study on the Extraction of Levulinic Acid from Aqueous Solution with Aliquat 336 Dissolved in Different Diluents: Solvent s Polarity Effect and Column Design
• Phase Equilibria for the Hydroesterification of 10-Undecenoic Acid Methyl Ester
• Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
• Liquid Liquid Equilibria for the Ternary Systems Dodecane + Toluene or Thiophene or Pyridine + 1-Ethyl-3-methylimidazolium Methyl Sulfate
• Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylbenzene + Linear Alkanes (n-Decane, n-Dodecane, n-Tetradecane, n-Hexadecane, or n-Heptadecane) at 0.1 MPa
• Density, Viscosity, and Freezing Point for Four Binary Systems of n-Dodecane or Methylcyclohexane Mixed with 1-Heptanol or Cyclohexylmethanol
• 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 for Systems Containing 4-Phenylbutan-2-one or Benzyl Ethanoate and Selected Alkanes
• Solvent Polarity Effect when Amberlite-LA2 Is Used in the Extraction of Picric Acid
• Density, Viscosity, and Structure of Equilibrium Solvent Phases in Butyric Acid Extraction by Phosphonium Ionic Liquid
• Interfacial Tension Measurement and Calculation of (Carbon Dioxide + n-Alkane) Binary Mixtures
• Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
• Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
• Liquid Viscosity and Surface Tension of n-Dodecane, n-Octacosane, Their Mixtures, and a Wax between 323 and 573 K by Surface Light Scattering
• Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
• Measurement and Correlation of High Pressure Phase Equilibria for CO2 + Alkanes and CO2 + Crude Oil Systems
• Simultaneous Measurement of Dynamic Viscosity and Density of n-Alkanes at High Pressures
• Density and Compressibility of Multicomponent n-Alkane Mixtures up to 463 K and 140 MPa
• Viscosity Measurements of n-Dodecane at Temperatures between 303 K and 693 K and Pressures up to 10 MPa
• Liquid-Liquid Equilibria for 2-Phenylethan-1-ol + Alkane Systems
• Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Binary Mixtures of Ethylcyclohexane or Methylcyclohexane with n-Dodecane or n-Hexadecane at 0.1 MPa
• Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
• Liquid-Liquid Equilibria of Formic Acid and Furfural in a Biphasic Aqueous-Organic System: Optimization of Solvent and Amine Extractant
• Densities and Viscosities of Ternary System n-Dodecane (1) + Bicyclohexyl (2) + n-Butanol (3) and Corresponding Binaries at T = (293.15 to 333.15) K
• Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
• Liquid-Liquid Equilibria of Lactic Acid/Water Solutions in Tri-iso-octylamine/Dodecane/1-Dodecanol at 306.1, 310.1, and 316.1 K. Experimental Data and Prediction
• Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
• Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Quaternary Mixtures of n-Dodecane (1), n-Butylcyclohexane (2), n-Butylbenzene (3), and 2,2,4,4,6,8,8-Heptamethylnonane (4) at 0.1 MPa as Potential Surrogate Mixtures for Military Jet Fuel, JP-5
• Thermodynamic Studies of Solubility for Naphthalene in 12 Solvents from 279 to 330 K
• Measurement and Prediction of Excess Properties of Binary Mixtures Methyl Decanoate + an Even-Numbered n-Alkane (C6-C16) at 298.15 K
• Phase Equilibrium and Liquid Viscosity of CO2 + n-Dodecane Mixtures between 283 and 353 K
• Liquid-Liquid Equilibrium for Ternary Systems of N-Methylformamide + Pyrrole/Indole + Alkanes at 298.15 K: Phase Equilibrium Measurement and Correlation
• Density, Speed of Sound, Compressibility, and Excess Properties of Carbon Dioxide + n-Dodecane Binary Mixtures from 10 to 70 MPa
• Experimental Investigation of the Thermophysical Properties of the Bio-Aviation Fuel Surrogates: Binary and Ternary Mixtures of n-Dodecane, Methyl Butyrate, and Methyl Decanoate
• Liquid-liquid equilibria for mixtures of (Furfural + an Aromatic hydrocarbon + an alkane) at T=298.15 K
• Liquid-Liquid Equilibria for Mixtures of (Furfural + a Chlorinated Aromatic Compound + an Alkane) at T = 298.15 K
• Excess molar volumes and enthalpies of mixing for the ternary system (butyl butyrate + 1-octanol + dodecane) at the temperature 308.15 K.
• Ternary Liquid-Liquid Equilibria for Mixtures of 1-Methyl-3-octylimidazolium Chloride + an Alkanol + an Alkane at 298.2 K and 1 bar
• Excess Enthalpies of Binary Mixtures of 1-Hexene with Some n-Alkanes at 298.15 K
• Solubility of Benzophenone in Binary Alkane + Carbon Tetrachloride Solvent Mixtures
• Heat Capacities, Densities, and Speeds of Sound for {(1,5-Dichloropentane or 1,6-Dichlorohexane) + Dodecane}
• Dynamic Viscosities of 2-Pentanol with Alkanes (Octane, Decane, and Dodecane) at Three Temperatures T ) (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO Interaction Parameters
• Activity Coefficients at Infinite Dilution and Excess Molar Volumes in Binary Mixtures Containing Normal Alkanes (Nonane, Decane, Undecane, or Dodecane) and Cresols (2-Methylphenol or 3-Methylphenol)
• Thermodynamic Properties of dodecane + 1-butanol and + 2-butanol systems
• Density and Relative Permittivity for 1-Alkanols + Dodecane at 298.15 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
• Measurement and Correlation of Phase Equilibria for Dodecane + sec-Butylbenzene + N-Methyl-2-pyrrolidone
• Mutual Solubilities of Terpene in Methanol and Water and Their Multicomponent Liquid-Liquid Equilibria
• 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
• 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
• Densities and Viscosities of Binary Mixtures of Tributyl Phosphate with Hexane and Dodecane from (298.15 to 328.15) K
• Vapor-Liquid Equilibria of Binary Systems of Ethene Oxide + Dodecane, Ethene Oxide + 1-Decanol, and Ethene Oxide + 1-Dodecanol and Prediction with the Predictive Soave-Redlich-Kwong (PSRK) Equation of State
• Liquid-Liquid Equilibria for {1-Ethyl-3-methylimidazolium Diethylphosphate or 1-Ethyl-3-methylimidazolium Ethylsulfate} + 4,6-Dimethyldibenzothiophene + Dodecane Systems at 298.2 K and 313.2 K
• Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
• Vapor-Liquid Equilibrium Data for the Nitrogen + Dodecane System at Temperatures from (344 to 593) K and at Pressures up to 60 MPa
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Liquid Liquid Equilibria of Alkane (C10 C14) + sec-Butylbenzene + Sulfolane
• Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
• Vapor Liquid Equilibria of Binary and Ternary Systems Containing Carbon Dioxide, Alkane, and Benzothiophene
• Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
• Liquid Liquid Equilibria of Methanol, Ethanol, and Propan-2-ol with Water and Dodecane
• Density, Refractive Index, Viscosity, and Surface Tension of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with Some n-Alkanes from (293.15 to 313.15) K
• Liquid Liquid Equilibrium in N-Methyl-2-hydroxyethylammonium Acetate, Butanoate, or Hexanoate Ionic Liquids + Dibenzothiophene + n-Dodecane Systems at 298.2 K and Atmospheric Pressure
• Vapor-Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K
• Isothermal Vapor Liquid Equilibrium Data for the Propan-1-ol + Dodecane System at (323.0, 343.4, 353.2, 363.1, and 369.2) K
• 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
• Thermodynamics of Mixtures Containing Aromatic Alcohols. 1. Liquid Liquid Equilibria for (Phenylmethanol + Alkane) Systems
• Extraction of Butylbenzene from Dodecane Using Hexafluorophosphate-Based Ionic Liquids: Effect of Cation Change
• Liquid Liquid Equilibria for the Ternary System Water + Dodecane + 1-(1-Methyl-2-propoxyethoxy)-2-propanol
• 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
• Thermodynamics of Mixtures Containing a Very Strongly Polar Compound. 10. Liquid Liquid Equilibria for N,N-Dimethylacetamide + Selected Alkanes
• Density, Viscosity, and Interfacial Tension of Binary Mixture of Tri-iso-amyl Phosphate (TiAP) and n-Dodecane: Effect of Compositions and Gamma Absorbed Doses
• Solid Liquid Equilibria, Excess Molar Volumes, and Deviations in the Molar Refractivity for the Binary Systems of Alamine 304-1 + Decane, Dodecane, or Dodecanol
• Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
• Liquid Liquid Equilibria for the Ternary Systems of 4-Methyl-1,3-dioxolan-2-one + 1,4-Dimethylbenzene + Octane, Decane, or Dodecane and the Ternary Systems of Acetonitrile + Morpholine + Octane, Decane, or Dodecane at 313.15 K or 298.15 K
• Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Dodecane with 2,2,4,6,6-Pentamethylheptane or 2,2,4,4,6,8,8-Heptamethylnonane
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Vapor Liquid Equilibrium Data for Binary Systems of n-Dodecane + {Propan-1-ol, Butan-1-ol, 2-Methylpropan-1-ol} at 40 kPa
• Thermodynamics of Mixtures Containing Amines. XV. Liquid Liquid Equilibria for Benzylamine + CH3(CH2)nCH3 (n = 8, 9, 10, 12, 14)
• Measurement and Modeling of the Densities for CO2 + Dodecane System from 313.55 K to 353.55 K and Pressures up to 18 MPa
• Binary Liquid Liquid Equilibria of ?-Valerolactone with Some Hydrocarbons
• Liquid-Liquid Equilibria of Alkane (C10-C14) + Hexylbenzene + Sulfolane
• Isothermal Phase Equilibria and Excess Molar Enthalpies for Binary Systems with Dimethyl Ether at 323.15 K
• Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
• Thermophysical Characterization of Liquids Using Precise Density and Isobaric Heat Capacity Measurements As a Function of Pressure
• Comparison between Experimental and Theoretical Estimations of the Thermal Expansion, Concentration Expansion Coefficients, and Viscosity for Binary Mixtures under Pressures up to 20 MPa
• Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
• Excess Molar Enthalpies of Binary Systems of 2-Octanone or 3-Octanone with Dodecane, Tetradecane, or Hexadecane at 298.15 K
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Excess Molar Enthalpies of Binary Systems of n-Valeric Anhydride or n-Hexanoic Anhydride with n-Dodecane, n-Tetradecane, or n-Hexadecane at 298.15 K
• Isobaric Thermal Expansivity for Nonpolar Compounds
• Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
• Miscibility of Trihexyl(tetradecyl)phosphonium Chloride with Alkanes
• Joback Method
• KDB
• McGowan Method
• NIST Webbook

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