Chemical Properties of Hexadecane (CAS 544-76-3)

InChI

InChI=1S/C16H34/c1-3-5-7-9-11-13-15-16-14-12-10-8-6-4-2/h3-16H2,1-2H3

InChI Key

DCAYPVUWAIABOU-UHFFFAOYSA-N

Formula

C16H34

SMILES

CCCCCCCCCCCCCCCC

Molecular Weight¹

226.45

CAS

544-76-3

Other Names

• cetane
• n-Cetane
• n-hexadecane

• ω : Acentric Factor.
• 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).
• C_sat : Molar heat capacity at saturation pressure (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• 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.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boil(P) : Boiling point at given pressure (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_fus(P) : Melting 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_spec : Specific Volume (m³/kg).
• V_COSTALD : COSTALD Characteristic Volume (m³/kmol).
• ω_SRK : SRK acentric factor.
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

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

Physical Properties

Property	Value	Unit	Source
ω	[0.7260; 0.7420]
ω	0.7420		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.7418		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.7260		ChemSep v8.3 pure component data Compiled value
ω	0.7420		KDB
ΔcH°liquid	[-10699.10; -10699.10]	kJ/mol
ΔcH°liquid	-10699.10 ± 1.80	kJ/mol	NIST
ΔcH°liquid	-10699.10 ± 4.10	kJ/mol	NIST
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	[82.16; 83.74]	kJ/mol
ΔfG°	82.16	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	83.74	kJ/mol	KDB
Rg	8.3180		KDB
ΔfH°gas	[-374.90; -373.60]	kJ/mol
ΔfH°gas	-374.17	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-373.60	kJ/mol	KDB
ΔfH°gas	-374.90	kJ/mol	NIST
ΔfH°gas	-374.70	kJ/mol	NIST
ΔfH°liquid	[-456.30; -456.10]	kJ/mol
ΔfH°liquid	-456.30 ± 2.00	kJ/mol	NIST
ΔfH°liquid	-456.10 ± 4.10	kJ/mol	NIST
ΔfusH°	50.04	kJ/mol	Silver incorporated microencapsulation of n-hexadecane and noctadecane appropriate for dynamic thermal management in textiles
ΔsubH°	135.10	kJ/mol	NIST
ΔvapH°	[80.60; 81.80]	kJ/mol
ΔvapH°	81.38	kJ/mol	NIST
ΔvapH°	81.80 ± 1.30	kJ/mol	NIST
ΔvapH°	81.40	kJ/mol	NIST
ΔvapH°	81.40	kJ/mol	NIST
ΔvapH°	81.20	kJ/mol	NIST
ΔvapH°	81.40	kJ/mol	NIST
ΔvapH°	81.40 ± 0.40	kJ/mol	NIST
ΔvapH°	81.10	kJ/mol	NIST
ΔvapH°	Outlier 80.60 ± 1.50	kJ/mol	NIST
IE	9.78	eV	Relay (1.0) Calculated Property
log10WS	[-8.40; -8.40]
log10WS	-8.40		Aq. Solubility Prediction
log10WS	-8.40		Estimated Solubility
logPoct/wat	6.488		Crippen Calculated Property
McVol	236.300	ml/mol	McGowan Calculated Property
NFPA Fire	1		KDB
Pc	[1400.00; 1420.32]	kPa
Pc	1400.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Pc	1401.33	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	Outlier 1420.32	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	1400.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	1400.00	kPa	KDB
Pc	1400.00 ± 200.00	kPa	NIST
Pc	1401.00 ± 50.00	kPa	NIST
Ptriple	9.22e-05	kPa	ChemSep v8.3 pure component data Compiled value
ρc	[218.97; 226.44]	kg/m3
ρc	226.44 ± 45.29	kg/m3	NIST
ρc	218.97 ± 6.79	kg/m3	NIST
Inp	[268.29; 272.02]
Inp	268.29		NIST
Inp	272.02		NIST
S°gas	778.31	J/mol×K	NIST
S°liquid	[586.18; 626.80]	J/mol×K
S°liquid	586.18	J/mol×K	NIST
S°liquid	626.80	J/mol×K	NIST
Tboil	[543.00; 561.00]	K
Tboil	559.98	K	ChemSep v8.3 pure component data Compiled value
Tboil	560.01	K	KDB
Tboil	560.20	K	NIST
Tboil	559.00 ± 2.00	K	NIST
Tboil	559.92 ± 0.20	K	NIST
Tboil	553.00 ± 5.00	K	NIST
Tboil	556.00 ± 6.00	K	NIST
Tboil	561.00 ± 4.00	K	NIST
Tboil	548.00 ± 5.00	K	NIST
Tboil	543.00 ± 8.00	K	NIST
Tboil	547.00 ± 5.00	K	NIST
Tboil	551.00 ± 5.00	K	NIST
Tc	[717.15; 723.00]	K
Tc	723.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Tc	722.40	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	720.54	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	723.00	K	ChemSep v8.3 pure component data Compiled value
Tc	723.00	K	KDB
Tc	723.00 ± 2.00	K	NIST
Tc	723.00 ± 1.90	K	NIST
Tc	722.40 ± 1.10	K	NIST
Tc	723.00 ± 1.20	K	NIST
Tc	722.60	K	NIST
Tc	721.70 ± 2.00	K	NIST
Tc	723.00 ± 2.00	K	NIST
Tc	723.00 ± 3.00	K	NIST
Tc	Outlier 717.15 ± 3.00	K	NIST
Tfus	[288.00; 293.00]	K
Tfus	291.45	K	Phase diagrams of binary systems containing n-alkanes, or cyclohexane, or 1-alkanols and 2,3-pentanedione at atmospheric and high pressure
Tfus	291.50	K	Experimental measurements and thermodynamic modeling of wax disappearance temperature for the binary systems n-C14H30 + n- C16H34, n-C16H34 + n-C18H38 and n-C11H24 + n-C18H38
Tfus	291.10	K	Phase equilibria of didecyldimethylammonium nitrate ionic liquid with water and organic solvents
Tfus	291.00	K	Determination of thermophysical properties of cyclopentane hydrate using a stirred calorimetric cell
Tfus	291.30	K	Solid Liquid Equilibria in the Binary Systems of Saturated Fatty Acids or Triglycerides (C12 to C18) + Hexadecane
Tfus	291.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	291.31	K	ChemSep v8.3 pure component data Compiled value
Tfus	291.34	K	KDB
Tfus	291.17	K	Aq. Solubility Prediction
Tfus	291.27 ± 0.02	K	NIST
Tfus	291.32 ± 0.20	K	NIST
Tfus	291.19 ± 0.05	K	NIST
Tfus	291.15 ± 0.50	K	NIST
Tfus	291.00 ± 0.30	K	NIST
Tfus	291.33 ± 0.10	K	NIST
Tfus	291.25 ± 0.10	K	NIST
Tfus	290.00 ± 1.66	K	NIST
Tfus	291.00 ± 2.00	K	NIST
Tfus	291.29 ± 0.02	K	NIST
Tfus	291.29 ± 0.02	K	NIST
Tfus	291.30 ± 0.01	K	NIST
Tfus	291.30 ± 0.06	K	NIST
Tfus	291.30 ± 0.04	K	NIST
Tfus	291.31 ± 0.02	K	NIST
Tfus	291.00 ± 2.00	K	NIST
Tfus	290.00 ± 3.00	K	NIST
Tfus	291.21 ± 0.15	K	NIST
Tfus	291.24 ± 0.10	K	NIST
Tfus	291.24 ± 0.20	K	NIST
Tfus	290.80 ± 0.50	K	NIST
Tfus	291.29 ± 0.02	K	NIST
Tfus	291.29 ± 0.01	K	NIST
Tfus	291.24 ± 0.10	K	NIST
Tfus	Outlier 293.00 ± 0.60	K	NIST
Tfus	291.30 ± 0.02	K	NIST
Tfus	291.20 ± 0.60	K	NIST
Tfus	290.40 ± 1.50	K	NIST
Tfus	291.20 ± 0.40	K	NIST
Tfus	291.00 ± 2.00	K	NIST
Tfus	291.33 ± 0.20	K	NIST
Tfus	291.30 ± 0.30	K	NIST
Tfus	290.60 ± 0.50	K	NIST
Tfus	291.29 ± 0.10	K	NIST
Tfus	Outlier 293.00 ± 3.00	K	NIST
Tfus	292.40 ± 0.50	K	NIST
Tfus	290.20 ± 2.00	K	NIST
Tfus	291.00 ± 0.60	K	NIST
Tfus	Outlier 288.00 ± 3.00	K	NIST
Tfus	291.05 ± 0.40	K	NIST
Tfus	290.10 ± 0.50	K	NIST
Tfus	290.98 ± 0.30	K	NIST
Tfus	Outlier 288.69 ± 2.00	K	NIST
Tfus	290.70 ± 2.00	K	NIST
Tfus	291.26 ± 0.20	K	NIST
Tfus	290.00 ± 2.00	K	NIST
Tfus	291.26 ± 0.20	K	NIST
Tfus	291.00 ± 2.00	K	NIST
Tfus	Outlier 293.00 ± 2.00	K	NIST
Tfus	Outlier 293.00 ± 2.00	K	NIST
Tfus	291.40 ± 2.00	K	NIST
Tfus	292.00 ± 3.00	K	NIST
Tfus	291.00 ± 3.00	K	NIST
Tfus	291.00 ± 2.00	K	NIST
Ttriple	[291.10; 291.34]	K
Ttriple	291.31	K	ChemSep v8.3 pure component data Compiled value
Ttriple	291.33 ± 0.05	K	NIST
Ttriple	291.32 ± 0.60	K	NIST
Ttriple	291.34 ± 0.02	K	NIST
Ttriple	291.33 ± 0.40	K	NIST
Ttriple	291.32 ± 0.40	K	NIST
Ttriple	291.32 ± 0.20	K	NIST
Ttriple	291.34 ± 0.20	K	NIST
Ttriple	291.33 ± 0.10	K	NIST
Ttriple	Outlier 291.10 ± 0.20	K	NIST
UQi	9.26		ChemSep v8.3 pure component data Compiled value
URi	11.24		ChemSep v8.3 pure component data Compiled value
Vc	[1.034; 1.034]	m3/kmol
Vc	1.034	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Vc	1.034	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	1.034	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	1.034	m3/kmol	KDB
Vc	1.034	m3/kmol	NIST
VCOSTALD	1.05	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.77		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2408100; 0.2410000]
Zc	0.2410000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Zc	0.2410000		ChemSep v8.3 pure component data Compiled value
Zc	0.2408100		KDB
Zra	[0.23; 0.24]
Zra	0.24		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.23		ChemSep v8.3 pure component data Compiled value
Zra	0.24		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[484.90; 512.37]	J/mol×K	[297.79; 313.15]
Cp,liquid	499.00	J/mol×K	297.79	NIST
Cp,liquid	498.30	J/mol×K	298.00	NIST
Cp,liquid	500.21	J/mol×K	298.15	NIST
Cp,liquid	497.16	J/mol×K	298.15	NIST
Cp,liquid	504.20	J/mol×K	298.15	NIST
Cp,liquid	500.21	J/mol×K	298.15	NIST
Cp,liquid	499.62	J/mol×K	298.15	NIST
Cp,liquid	495.73	J/mol×K	298.15	NIST
Cp,liquid	496.45	J/mol×K	298.15	NIST
Cp,liquid	499.62	J/mol×K	298.15	NIST
Cp,liquid	499.97	J/mol×K	298.15	NIST
Cp,liquid	501.60	J/mol×K	298.15	NIST
Cp,liquid	499.72	J/mol×K	298.15	NIST
Cp,liquid	504.58	J/mol×K	298.15	NIST
Cp,liquid	501.45	J/mol×K	298.15	NIST
Cp,liquid	484.90	J/mol×K	311.00	NIST
Cp,liquid	512.37	J/mol×K	313.15	NIST
Csat	[502.50; 572.30]	J/mol×K	[300.00; 400.00]
Csat	502.50	J/mol×K	300.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	508.00	J/mol×K	310.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	514.00	J/mol×K	320.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	520.50	J/mol×K	330.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	527.30	J/mol×K	340.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	534.50	J/mol×K	350.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	541.90	J/mol×K	360.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	549.40	J/mol×K	370.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	557.10	J/mol×K	380.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	564.70	J/mol×K	390.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	572.30	J/mol×K	400.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
η	[0.0001705; 0.0034910]	Pa×s	[293.15; 573.15]
η	0.0034860	Pa×s	293.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0034910	Pa×s	293.15	Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
η	0.0030410	Pa×s	298.15	Studies of mixing properties of binary systems of 2-propanol with hexadecane and squalane at T = (298.15, 303.15, and 308.15) K
η	0.0030410	Pa×s	298.15	Temperature and Composition Dependence of the Densities, Viscosities, and Speeds of Sound of Binary Liquid Mixtures of 1-Butanol with Hexadecane and Squalane
η	0.0030410	Pa×s	298.15	Volumetric, transport, and acoustic properties of binary mixtures of 2-methyl-1-propanol with hexadecane and squalane at T = (298.15, 303.15, and 308.15) K: Experimental results, correlation, and prediction by the ERAS model
η	0.0030940	Pa×s	298.15	Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
η	0.0027060	Pa×s	303.15	Studies of mixing properties of binary systems of 2-propanol with hexadecane and squalane at T = (298.15, 303.15, and 308.15) K
η	0.0027060	Pa×s	303.15	Volumetric, transport, and acoustic properties of binary mixtures of 2-methyl-1-propanol with hexadecane and squalane at T = (298.15, 303.15, and 308.15) K: Experimental results, correlation, and prediction by the ERAS model
η	0.0027780	Pa×s	303.15	Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
η	0.0027720	Pa×s	303.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0027060	Pa×s	303.15	Temperature and Composition Dependence of the Densities, Viscosities, and Speeds of Sound of Binary Liquid Mixtures of 1-Butanol with Hexadecane and Squalane
η	0.0024090	Pa×s	308.15	Studies of mixing properties of binary systems of 2-propanol with hexadecane and squalane at T = (298.15, 303.15, and 308.15) K
η	0.0024090	Pa×s	308.15	Volumetric, transport, and acoustic properties of binary mixtures of 2-methyl-1-propanol with hexadecane and squalane at T = (298.15, 303.15, and 308.15) K: Experimental results, correlation, and prediction by the ERAS model
η	0.0024090	Pa×s	308.15	Temperature and Composition Dependence of the Densities, Viscosities, and Speeds of Sound of Binary Liquid Mixtures of 1-Butanol with Hexadecane and Squalane
η	0.0022610	Pa×s	313.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0018400	Pa×s	323.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0012360	Pa×s	348.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0008927	Pa×s	373.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0006788	Pa×s	398.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0005351	Pa×s	423.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0004256	Pa×s	448.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0003440	Pa×s	473.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0002862	Pa×s	498.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0002360	Pa×s	523.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0001937	Pa×s	548.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
η	0.0001705	Pa×s	573.15	Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
ΔfusH	[47.55; 53.36]	kJ/mol	[290.70; 292.10]
ΔfusH	53.00	kJ/mol	290.70	NIST
ΔfusH	51.46	kJ/mol	291.10	NIST
ΔfusH	51.54	kJ/mol	291.10	NIST
ΔfusH	51.46	kJ/mol	291.10	NIST
ΔfusH	53.35	kJ/mol	291.30	NIST
ΔfusH	53.36	kJ/mol	291.34	NIST
ΔfusH	47.55	kJ/mol	292.10	NIST
ΔsubH	[80.00; 134.90]	kJ/mol	[288.00; 291.00]
ΔsubH	80.00 ± 3.00	kJ/mol	288.00	NIST
ΔsubH	83.00 ± 8.00	kJ/mol	289.00	NIST
ΔsubH	134.90	kJ/mol	291.00	NIST
ΔvapH	[51.21; 93.40]	kJ/mol	[300.50; 560.50]
ΔvapH	80.20	kJ/mol	300.50	NIST
ΔvapH	93.40	kJ/mol	311.50	NIST
ΔvapH	66.90	kJ/mol	343.00	NIST
ΔvapH	72.90	kJ/mol	349.80	Synthesis and Physical and Thermodynamic Properties of Lactic Acid and Malic Acid-Based Natural Deep Eutectic Solvents
ΔvapH	74.50	kJ/mol	353.00	Express thermo-gravimetric method for the vaporization enthalpies appraisal for very low volatile molecular and ionic compounds.
ΔvapH	66.20	kJ/mol	353.00	NIST
ΔvapH	65.60	kJ/mol	363.00	NIST
ΔvapH	74.90	kJ/mol	373.00	NIST
ΔvapH	64.90	kJ/mol	373.00	NIST
ΔvapH	64.20	kJ/mol	383.00	NIST
ΔvapH	65.70	kJ/mol	455.50	NIST
ΔvapH	68.50	kJ/mol	488.00	NIST
ΔvapH	61.70	kJ/mol	515.00	NIST
ΔvapH	59.80	kJ/mol	547.00	NIST
ΔvapH	51.21	kJ/mol	560.50	KDB
Pvap	[6.01e-05; 102.04]	kPa	[284.15; 560.90]
Pvap	6.01e-05	kPa	284.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	1.02e-04	kPa	289.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	1.68e-04	kPa	294.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	2.74e-04	kPa	299.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	4.40e-04	kPa	304.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	6.96e-04	kPa	309.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	1.08e-03	kPa	314.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	1.66e-03	kPa	319.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	2.52e-03	kPa	324.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	3.77e-03	kPa	329.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	5.58e-03	kPa	334.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	8.16e-03	kPa	339.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.01	kPa	344.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.02	kPa	349.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.02	kPa	354.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.03	kPa	359.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.05	kPa	364.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.06	kPa	369.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.09	kPa	374.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.12	kPa	379.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.16	kPa	384.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.21	kPa	389.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.28	kPa	394.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.37	kPa	399.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.48	kPa	404.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.63	kPa	409.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	0.81	kPa	414.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	1.03	kPa	419.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	1.32	kPa	424.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	1.67	kPa	429.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	2.10	kPa	434.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	2.63	kPa	439.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	3.28	kPa	444.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	4.07	kPa	449.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	5.02	kPa	454.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	6.18	kPa	459.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	7.56	kPa	464.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	9.21	kPa	469.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	11.20	kPa	474.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	13.50	kPa	479.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	16.30	kPa	484.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	14.78	kPa	486.10	Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
Pvap	19.50	kPa	489.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	23.30	kPa	494.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	27.70	kPa	499.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	32.90	kPa	504.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	38.90	kPa	509.15	Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
Pvap	49.76	kPa	529.60	Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
Pvap	79.60	kPa	549.30	Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
Pvap	101.35	kPa	560.50	Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
Pvap	102.04	kPa	560.90	Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
n0	[1.41450; 1.43520]		[293.10; 343.15]
n0	1.43440		293.10	Liquid-Liquid Equilibria Measurements for Ternary System of Hexadecane + 1,3,5-Trimethylbenzene + N-Methyl-2-pyrrolidone
n0	1.43520		293.15	Densities, Sound Velocities, and Refractive Indexes of Tetralin + n-Hexadecane at (293.15, 303.15, 313.15, 323.15, 333.15, and 343.15) K
n0	1.43460		293.15	Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
n0	1.43232		298.15	Phase behaviour of 1-methyl-3-octylimidazolium bis[trifluoromethylsulfonyl]imide with thiophene and aliphatic hydrocarbons: The influence of n-alkane chain length
n0	1.43230		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	1.43250		298.15	Liquid-liquid equilibria for mixtures of (Furfural + an Aromatic hydrocarbon + an alkane) at T=298.15 K
n0	1.43250		298.15	Liquid-Liquid Equilibria for Mixtures of (Furfural + a Chlorinated Aromatic Compound + an Alkane) at T = 298.15 K
n0	1.43232		298.15	Thiophene separation from aliphatic hydrocarbons using the 1-ethyl-3-methylimidazolium ethylsulfate ionic liquid
n0	1.43400		298.15	Densities, Viscosities, and Refractive Indices of Mixtures of Hexane with Cyclohexane, Decane, Hexadecane, and Squalane at 298.15K
n0	1.43180		298.20	Liquid-Liquid Equilibria for Ternary Mixtures (an Ionic Liquid + Benzene +Heptane or Hexadecane) at T ) 298.2 K and Atmospheric Pressure
n0	1.43110		303.15	Densities, Sound Velocities, and Refractive Indexes of Tetralin + n-Hexadecane at (293.15, 303.15, 313.15, 323.15, 333.15, and 343.15) K
n0	1.42690		313.15	Densities, Sound Velocities, and Refractive Indexes of Tetralin + n-Hexadecane at (293.15, 303.15, 313.15, 323.15, 333.15, and 343.15) K
n0	1.42280		323.15	Densities, Sound Velocities, and Refractive Indexes of Tetralin + n-Hexadecane at (293.15, 303.15, 313.15, 323.15, 333.15, and 343.15) K
n0	1.41870		333.15	Densities, Sound Velocities, and Refractive Indexes of Tetralin + n-Hexadecane at (293.15, 303.15, 313.15, 323.15, 333.15, and 343.15) K
n0	1.41450		343.15	Densities, Sound Velocities, and Refractive Indexes of Tetralin + n-Hexadecane at (293.15, 303.15, 313.15, 323.15, 333.15, and 343.15) K
ρl	[717.50; 773.70]	kg/m3	[293.00; 373.15]
ρl	773.00	kg/m3	293.00	KDB
ρl	773.41	kg/m3	293.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
ρl	773.50	kg/m3	293.15	Liquid-liquid equilibria for the ternary system (water + hexadecane + dipropylene glycol n-propyl ether)
ρl	773.33	kg/m3	293.15	Densities, speeds of sound, refractive indices, viscosities and their related thermodynamic properties for n-hexadecane + two aromatic hydrocarbons binary mixtures at temperatures from 298.15 K to 318.15 K
ρl	773.42	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	773.37	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	773.00	kg/m3	293.15	Volume expansion prediction of supercritical CO 2 + crude oil
ρl	773.70	kg/m3	293.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Direct Sugar to Hydrocarbon Diesel (DSH-76) and Binary Mixtures of N-Hexadecane and 2,2,4,6,6-Pentamethylheptane
ρl	773.49	kg/m3	293.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl	770.31	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	770.22	kg/m3	298.15	Liquid liquid equilibria for acetophenone + n-alkane mixtures and characterization of acetophenone systems using DISQUAC
ρl	771.15	kg/m3	298.15	Solvent extraction of thiophene from n-alkanes (C7, C12, and C16) using the ionic liquid [C8mim][BF4]
ρl	770.31	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	769.91	kg/m3	298.15	Thermodynamics of mixtures containing amines. XI. Liquid + liquid equilibria and molar excess enthalpies at 298.15 K for N-methylaniline + hydrocarbon systems. Characterization in terms of DISQUAC and ERAS models
ρl	770.01	kg/m3	298.15	Liquid-Liquid Equilibrium of Ternary Mixtures Formed by Some Oligooxaethylenes with Ethanol and Hexadecane
ρl	773.19	kg/m3	298.15	Binary Liquid-Liquid Equilibrium (LLE) for N-Methylformamide (NMF) + Hexadecane between (288.15 and 318.15) K and Ternary LLE for Systems of NMF + Heterocyclic Nitrogen Compounds + Hexadecane at 298.15 K
ρl	770.32	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	769.92	kg/m3	298.15	Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
ρl	770.31	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	769.87	kg/m3	298.15	A systematic study on volumetric and transport properties of binary systems 1-propanol + n-hexadecane, 1-butanol + n-hexadecane and 1-propanol + ethyl oleate at different temperatures: Experimental and modeling
ρl	770.14	kg/m3	298.15	Liquid-Liquid Equilibria for Binary System of Ethanol + Hexadecane at Elevated Temperature and the Ternary Systems of Ethanol + Heterocyclic Nitrogen Compounds + Hexadecane at 298.15 K
ρl	769.89	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	770.22	kg/m3	298.15	Thermodynamics of aromatic polar compound (alkanone, alkanal or alkanoate) + hydrocarbon mixtures
ρl	769.86	kg/m3	298.15	Densities, speeds of sound, refractive indices, viscosities and their related thermodynamic properties for n-hexadecane + two aromatic hydrocarbons binary mixtures at temperatures from 298.15 K to 318.15 K
ρl	773.19	kg/m3	298.15	(Liquid + Liquid) Equilibrium for (N,N-Dimethylformamide (DMF) + Hexadecane) at Temperatures between (293.15 and 313.15) K and Ternary Mixtures of (DMF + Hexadecane) with Either Quinoline, or Pyridine, or Pyrrole, or Aniline, or Indole at T = 298.15 K
ρl	771.50	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	769.81	kg/m3	298.15	Densities, speeds of sound, refractive indices, viscosities and their related thermodynamic properties for n-hexadecane + two aromatic hydrocarbons binary mixtures at temperatures from 298.15 K to 318.15 K
ρl	770.22	kg/m3	298.15	Liquid Liquid Equilibria for Systems Containing 4-Phenylbutan-2-one or Benzyl Ethanoate and Selected Alkanes
ρl	770.30	kg/m3	298.15	Liquid liquid equilibria in the ternary systems {hexadecane + BTX aromatics + 2-methoxyethanol or acetonitrile} at 298.15 K
ρl	770.21	kg/m3	298.15	Liquid-liquid equilibria for benzaldehyde + n-alkane mixtures andcharacterization of benzaldehyde + hydrocarbon systems in terms of DISQUAC
ρl	769.93	kg/m3	298.15	Liquid-liquid equilibria for the ternary system (water + hexadecane + dipropylene glycol n-propyl ether)
ρl	770.30	kg/m3	298.20	Ternary Liquid-Liquid Equilibria for Mixtures of 1-Methyl-3-octylimidazolium Chloride + an Alkanol + an Alkane at 298.2 K and 1 bar
ρl	766.47	kg/m3	303.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
ρl	766.55	kg/m3	303.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl	766.40	kg/m3	303.15	A systematic study on volumetric and transport properties of binary systems 1-propanol + n-hexadecane, 1-butanol + n-hexadecane and 1-propanol + ethyl oleate at different temperatures: Experimental and modeling
ρl	766.51	kg/m3	303.15	Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
ρl	766.80	kg/m3	303.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Direct Sugar to Hydrocarbon Diesel (DSH-76) and Binary Mixtures of N-Hexadecane and 2,2,4,6,6-Pentamethylheptane
ρl	766.40	kg/m3	303.15	Densities, speeds of sound, refractive indices, viscosities and their related thermodynamic properties for n-hexadecane + two aromatic hydrocarbons binary mixtures at temperatures from 298.15 K to 318.15 K
ρl	766.43	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	766.47	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	762.94	kg/m3	308.15	Densities, speeds of sound, refractive indices, viscosities and their related thermodynamic properties for n-hexadecane + two aromatic hydrocarbons binary mixtures at temperatures from 298.15 K to 318.15 K
ρl	762.95	kg/m3	308.15	A systematic study on volumetric and transport properties of binary systems 1-propanol + n-hexadecane, 1-butanol + n-hexadecane and 1-propanol + ethyl oleate at different temperatures: Experimental and modeling
ρl	763.06	kg/m3	308.15	Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
ρl	762.89	kg/m3	308.15	Densities, speeds of sound, refractive indices, viscosities and their related thermodynamic properties for n-hexadecane + two aromatic hydrocarbons binary mixtures at temperatures from 298.15 K to 318.15 K
ρl	759.51	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	759.90	kg/m3	313.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Direct Sugar to Hydrocarbon Diesel (DSH-76) and Binary Mixtures of N-Hexadecane and 2,2,4,6,6-Pentamethylheptane
ρl	759.63	kg/m3	313.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl	759.55	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	759.48	kg/m3	313.15	Densities, speeds of sound, refractive indices, viscosities and their related thermodynamic properties for n-hexadecane + two aromatic hydrocarbons binary mixtures at temperatures from 298.15 K to 318.15 K
ρl	759.55	kg/m3	313.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
ρl	759.55	kg/m3	313.15	Experimental high pressure speed of sound and density of (tetralin + n-decane) and (tetralin + n-hexadecane) systems and thermodynamic modeling
ρl	762.90	kg/m3	313.15	Excess Molar Volumes for Three and Four Component Mixtures Simulating the Binary Mixture (Cyclohexane+ Hexadecane)
ρl	759.60	kg/m3	313.15	Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
ρl	755.99	kg/m3	318.15	Densities, speeds of sound, refractive indices, viscosities and their related thermodynamic properties for n-hexadecane + two aromatic hydrocarbons binary mixtures at temperatures from 298.15 K to 318.15 K
ρl	756.14	kg/m3	318.15	Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
ρl	755.98	kg/m3	318.15	Densities, speeds of sound, refractive indices, viscosities and their related thermodynamic properties for n-hexadecane + two aromatic hydrocarbons binary mixtures at temperatures from 298.15 K to 318.15 K
ρl	752.68	kg/m3	323.15	Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
ρl	752.58	kg/m3	323.15	Densities, speeds of sound, refractive indices, viscosities and their related thermodynamic properties for n-hexadecane + two aromatic hydrocarbons binary mixtures at temperatures from 298.15 K to 318.15 K
ρl	752.90	kg/m3	323.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Direct Sugar to Hydrocarbon Diesel (DSH-76) and Binary Mixtures of N-Hexadecane and 2,2,4,6,6-Pentamethylheptane
ρl	752.71	kg/m3	323.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl	752.63	kg/m3	323.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
ρl	752.63	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	752.64	kg/m3	323.15	Experimental high pressure speed of sound and density of (tetralin + n-decane) and (tetralin + n-hexadecane) systems and thermodynamic modeling
ρl	752.60	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	745.71	kg/m3	333.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
ρl	745.69	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	745.73	kg/m3	333.15	Experimental high pressure speed of sound and density of (tetralin + n-decane) and (tetralin + n-hexadecane) systems and thermodynamic modeling
ρl	745.71	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	746.00	kg/m3	333.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Direct Sugar to Hydrocarbon Diesel (DSH-76) and Binary Mixtures of N-Hexadecane and 2,2,4,6,6-Pentamethylheptane
ρl	745.79	kg/m3	333.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl	738.80	kg/m3	343.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
ρl	738.90	kg/m3	343.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl	739.00	kg/m3	343.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Direct Sugar to Hydrocarbon Diesel (DSH-76) and Binary Mixtures of N-Hexadecane and 2,2,4,6,6-Pentamethylheptane
ρl	738.80	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	731.80	kg/m3	353.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl	731.90	kg/m3	353.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Direct Sugar to Hydrocarbon Diesel (DSH-76) and Binary Mixtures of N-Hexadecane and 2,2,4,6,6-Pentamethylheptane
ρl	731.90	kg/m3	353.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
ρl	724.70	kg/m3	363.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl	724.80	kg/m3	363.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Direct Sugar to Hydrocarbon Diesel (DSH-76) and Binary Mixtures of N-Hexadecane and 2,2,4,6,6-Pentamethylheptane
ρl	717.50	kg/m3	373.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl	717.70	kg/m3	373.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Direct Sugar to Hydrocarbon Diesel (DSH-76) and Binary Mixtures of N-Hexadecane and 2,2,4,6,6-Pentamethylheptane
ΔfusS	[176.79; 183.15]	J/mol×K	[291.10; 291.34]
ΔfusS	177.10	J/mol×K	291.10	NIST
ΔfusS	176.79	J/mol×K	291.10	NIST
ΔfusS	183.13	J/mol×K	291.30	NIST
ΔfusS	183.15	J/mol×K	291.34	NIST
csound,fluid	[1074.00; 1367.20]	m/s	[290.65; 373.15]
csound,fluid	1367.20	m/s	290.65	Density and speed of sound measurements of hexadecane
csound,fluid	1365.30	m/s	291.15	Density and speed of sound measurements of hexadecane
csound,fluid	1363.40	m/s	291.65	Density and speed of sound measurements of hexadecane
csound,fluid	1361.50	m/s	292.15	Density and speed of sound measurements of hexadecane
csound,fluid	1359.60	m/s	292.65	Density and speed of sound measurements of hexadecane
csound,fluid	1356.00	m/s	293.00	Fixed-Path Length Laser-Induced Sound Pinging: A Streamlined Method for Sound Speed Determination in Arbitrary Liquids
csound,fluid	1357.70	m/s	293.15	Density and speed of sound measurements of hexadecane
csound,fluid	1357.40	m/s	293.15	Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
csound,fluid	1357.00	m/s	293.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	1340.00	m/s	298.00	Fixed-Path Length Laser-Induced Sound Pinging: A Streamlined Method for Sound Speed Determination in Arbitrary Liquids
csound,fluid	1338.00	m/s	298.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	1338.80	m/s	298.15	Density and speed of sound measurements of hexadecane
csound,fluid	1325.00	m/s	303.00	Fixed-Path Length Laser-Induced Sound Pinging: A Streamlined Method for Sound Speed Determination in Arbitrary Liquids
csound,fluid	1312.00	m/s	303.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	1320.20	m/s	303.15	Density and speed of sound measurements of hexadecane
csound,fluid	1319.60	m/s	303.15	Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
csound,fluid	1301.00	m/s	308.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	1301.70	m/s	308.15	Density and speed of sound measurements of hexadecane
csound,fluid	1287.00	m/s	313.00	Fixed-Path Length Laser-Induced Sound Pinging: A Streamlined Method for Sound Speed Determination in Arbitrary Liquids
csound,fluid	1283.00	m/s	313.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	1282.90	m/s	313.15	Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
csound,fluid	1283.40	m/s	313.15	Density and speed of sound measurements of hexadecane
csound,fluid	1268.00	m/s	318.00	Fixed-Path Length Laser-Induced Sound Pinging: A Streamlined Method for Sound Speed Determination in Arbitrary Liquids
csound,fluid	1265.00	m/s	318.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	1265.30	m/s	318.15	Density and speed of sound measurements of hexadecane
csound,fluid	1248.00	m/s	323.00	Fixed-Path Length Laser-Induced Sound Pinging: A Streamlined Method for Sound Speed Determination in Arbitrary Liquids
csound,fluid	1247.40	m/s	323.15	Density and speed of sound measurements of hexadecane
csound,fluid	1246.00	m/s	323.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	1247.00	m/s	323.15	Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
csound,fluid	1227.00	m/s	328.00	Fixed-Path Length Laser-Induced Sound Pinging: A Streamlined Method for Sound Speed Determination in Arbitrary Liquids
csound,fluid	1228.00	m/s	328.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	1229.80	m/s	328.15	Density and speed of sound measurements of hexadecane
csound,fluid	1210.00	m/s	333.00	Fixed-Path Length Laser-Induced Sound Pinging: A Streamlined Method for Sound Speed Determination in Arbitrary Liquids
csound,fluid	1211.00	m/s	333.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	1212.30	m/s	333.15	Density and speed of sound measurements of hexadecane
csound,fluid	1212.10	m/s	333.15	Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
csound,fluid	1194.90	m/s	338.15	Density and speed of sound measurements of hexadecane
csound,fluid	1193.00	m/s	338.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	1177.90	m/s	343.15	Density and speed of sound measurements of hexadecane
csound,fluid	1176.00	m/s	343.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	1158.00	m/s	348.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	1141.00	m/s	353.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	1124.00	m/s	358.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	1107.00	m/s	363.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	1090.00	m/s	368.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
csound,fluid	1074.00	m/s	373.15	Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
γ	[0.03; 0.03]	N/m	[294.00; 313.20]
γ	0.03	N/m	294.00	Densities and Viscosities at 293.15 373.15 K, Speeds of Sound and Bulk Moduli at 293.15 333.15 K, Surface Tensions, and Flash Points of Binary Mixtures of n-Hexadecane and Alkylbenzenes at 0.1 MPa
γ	0.03	N/m	294.80	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	0.03	N/m	313.20	KDB
vspec	[0.00; 0.00]	m3/kg	[298.00; 573.00]
vspec	0.00	m3/kg	298.00	A simple method to determine the specific volumes of liquids and melts as a function of the temperature. Application to four n-alkanes (C16H34, C18H38, C19H40 and C21H44) under saturating vapour pressure in the 298-573K range
vspec	0.00	m3/kg	323.00	A simple method to determine the specific volumes of liquids and melts as a function of the temperature. Application to four n-alkanes (C16H34, C18H38, C19H40 and C21H44) under saturating vapour pressure in the 298-573K range
vspec	0.00	m3/kg	348.00	A simple method to determine the specific volumes of liquids and melts as a function of the temperature. Application to four n-alkanes (C16H34, C18H38, C19H40 and C21H44) under saturating vapour pressure in the 298-573K range
vspec	0.00	m3/kg	373.00	A simple method to determine the specific volumes of liquids and melts as a function of the temperature. Application to four n-alkanes (C16H34, C18H38, C19H40 and C21H44) under saturating vapour pressure in the 298-573K range
vspec	0.00	m3/kg	398.00	A simple method to determine the specific volumes of liquids and melts as a function of the temperature. Application to four n-alkanes (C16H34, C18H38, C19H40 and C21H44) under saturating vapour pressure in the 298-573K range
vspec	0.00	m3/kg	423.00	A simple method to determine the specific volumes of liquids and melts as a function of the temperature. Application to four n-alkanes (C16H34, C18H38, C19H40 and C21H44) under saturating vapour pressure in the 298-573K range
vspec	0.00	m3/kg	448.00	A simple method to determine the specific volumes of liquids and melts as a function of the temperature. Application to four n-alkanes (C16H34, C18H38, C19H40 and C21H44) under saturating vapour pressure in the 298-573K range
vspec	0.00	m3/kg	473.00	A simple method to determine the specific volumes of liquids and melts as a function of the temperature. Application to four n-alkanes (C16H34, C18H38, C19H40 and C21H44) under saturating vapour pressure in the 298-573K range
vspec	0.00	m3/kg	498.00	A simple method to determine the specific volumes of liquids and melts as a function of the temperature. Application to four n-alkanes (C16H34, C18H38, C19H40 and C21H44) under saturating vapour pressure in the 298-573K range
vspec	0.00	m3/kg	523.00	A simple method to determine the specific volumes of liquids and melts as a function of the temperature. Application to four n-alkanes (C16H34, C18H38, C19H40 and C21H44) under saturating vapour pressure in the 298-573K range
vspec	0.00	m3/kg	548.00	A simple method to determine the specific volumes of liquids and melts as a function of the temperature. Application to four n-alkanes (C16H34, C18H38, C19H40 and C21H44) under saturating vapour pressure in the 298-573K range
vspec	0.00	m3/kg	573.00	A simple method to determine the specific volumes of liquids and melts as a function of the temperature. Application to four n-alkanes (C16H34, C18H38, C19H40 and C21H44) under saturating vapour pressure in the 298-573K range

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil(P)	[444.06; 496.42]	K	[3.47; 22.39]
Tboil(P)	444.06	K	3.47	Improving a variation of the DSC technique for measuring the boiling points of pure compounds at low pressures
Tboil(P)	474.05	K	10.37	Improving a variation of the DSC technique for measuring the boiling points of pure compounds at low pressures
Tboil(P)	486.81	K	15.17	Improving a variation of the DSC technique for measuring the boiling points of pure compounds at low pressures
Tboil(P)	493.60	K	18.66	Improving a variation of the DSC technique for measuring the boiling points of pure compounds at low pressures
Tboil(P)	496.42	K	22.39	Improving a variation of the DSC technique for measuring the boiling points of pure compounds at low pressures
Tfus(P)	[291.50; 343.15]	K	[100.00; 251030.00]
Tfus(P)	291.50	K	100.00	Liquid solid equilibria under high pressure of tetradecane + pentadecane and tetradecane + hexadecane binary systems
Tfus(P)	293.15	K	9210.00	Influence of size and shape effects on the high-pressure solubility of n-alkanes: Experimental data, correlation and prediction
Tfus(P)	293.15	K	9210.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus(P)	296.00	K	20000.00	Liquid solid equilibria under high pressure of tetradecane + pentadecane and tetradecane + hexadecane binary systems
Tfus(P)	300.40	K	40000.00	Liquid solid equilibria under high pressure of tetradecane + pentadecane and tetradecane + hexadecane binary systems
Tfus(P)	303.15	K	50650.00	Influence of size and shape effects on the high-pressure solubility of n-alkanes: Experimental data, correlation and prediction
Tfus(P)	303.15	K	50650.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus(P)	304.80	K	60000.00	Liquid solid equilibria under high pressure of tetradecane + pentadecane and tetradecane + hexadecane binary systems
Tfus(P)	309.70	K	80000.00	Liquid solid equilibria under high pressure of tetradecane + pentadecane and tetradecane + hexadecane binary systems
Tfus(P)	313.15	K	95560.00	Influence of size and shape effects on the high-pressure solubility of n-alkanes: Experimental data, correlation and prediction
Tfus(P)	313.15	K	95560.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus(P)	313.50	K	100000.00	Liquid solid equilibria under high pressure of tetradecane + pentadecane and tetradecane + hexadecane binary systems
Tfus(P)	323.15	K	143920.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus(P)	323.15	K	143920.00	Influence of size and shape effects on the high-pressure solubility of n-alkanes: Experimental data, correlation and prediction
Tfus(P)	333.15	K	195740.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus(P)	333.15	K	195740.00	Influence of size and shape effects on the high-pressure solubility of n-alkanes: Experimental data, correlation and prediction
Tfus(P)	343.15	K	251030.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus(P)	343.15	K	251030.00	Influence of size and shape effects on the high-pressure solubility of n-alkanes: Experimental data, correlation and prediction

Datasets

1. Molar heat capacity at constant pressure, J/K/mol (1)
2. Viscosity, Pa*s (4)
3. Mass density, kg/m3 (6)

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	130.00	513.57
328.15	130.00	517.19
333.15	130.00	520.81
338.15	130.00	524.66
343.15	130.00	528.51
348.15	130.00	532.82
353.15	130.00	536.44
358.15	130.00	540.74
363.15	130.00	544.59
368.15	130.00	548.67
373.15	130.00	553.20
378.15	130.00	557.27
383.15	130.00	561.57
388.15	130.00	565.65
393.15	130.00	569.73
398.15	130.00	574.03
403.15	130.00	578.56
408.15	130.00	583.09
413.15	130.00	586.94
418.15	130.00	591.46
423.15	130.00	595.77
428.15	130.00	599.62
433.15	130.00	603.92
438.15	130.00	608.67
443.15	130.00	613.20
448.15	130.00	617.28
453.15	130.00	622.26
323.15	10090.00	512.21
328.15	10090.00	515.83
333.15	10090.00	519.46
338.15	10090.00	523.31
343.15	10090.00	526.48
348.15	10090.00	530.10
353.15	10090.00	534.40
358.15	10090.00	538.48
363.15	10090.00	542.10
368.15	10090.00	546.40
373.15	10090.00	550.70
378.15	10090.00	554.55
383.15	10090.00	558.86
388.15	10090.00	563.16
393.15	10090.00	567.24
398.15	10090.00	571.31
403.15	10090.00	575.61
408.15	10090.00	579.92
413.15	10090.00	584.44
418.15	10090.00	588.97
423.15	10090.00	593.05
428.15	10090.00	596.45
433.15	10090.00	600.30
438.15	10090.00	604.60
443.15	10090.00	609.35
448.15	10090.00	613.66
453.15	10090.00	617.05
458.15	10090.00	621.35
463.15	10090.00	625.43
468.15	10090.00	630.19
473.15	10090.00	634.94
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.90	3300.00	0.0028
303.90	7300.00	0.0030
303.90	12900.00	0.0032
303.90	19000.00	0.0035
303.90	26800.00	0.0038
303.90	33600.00	0.0041
325.70	8100.00	0.0019
325.70	8300.00	0.0020
325.70	21500.00	0.0023
325.70	35600.00	0.0027
325.70	49300.00	0.0031
325.70	63600.00	0.0036
325.70	77500.00	0.0041
325.70	91800.00	0.0046
325.70	104100.00	0.0052
325.70	119200.00	0.0059
325.70	122700.00	0.0061
429.10	12800.00	0.0006
429.10	12800.00	0.0006
429.10	22200.00	0.0006
429.10	22700.00	0.0006
429.10	35800.00	0.0007
429.10	70500.00	0.0010
429.10	91600.00	0.0012
429.10	118800.00	0.0014
429.10	140300.00	0.0016
429.10	167800.00	0.0018
429.10	188000.00	0.0020
429.10	222900.00	0.0025
533.70	14100.00	0.0003
533.70	14300.00	0.0003
533.70	29900.00	0.0003
533.70	30100.00	0.0003
533.70	50400.00	0.0004
533.70	50500.00	0.0004
533.70	77100.00	0.0005
533.70	104600.00	0.0006
533.70	125000.00	0.0007
533.70	152800.00	0.0008
533.70	188400.00	0.0010
533.70	210000.00	0.0011
533.70	226600.00	0.0012
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.36	1080.00	0.0031
298.36	10010.00	0.0035
298.36	21090.00	0.0040
298.36	30500.00	0.0045
298.36	1060.00	0.0031
323.21	1250.00	0.0019
323.21	21100.00	0.0024
323.21	40990.00	0.0030
323.21	60490.00	0.0036
323.21	80320.00	0.0044
323.21	102810.00	0.0051
323.21	1090.00	0.0019
348.20	1010.00	0.0013
348.20	20050.00	0.0016
348.20	40520.00	0.0019
348.20	60680.00	0.0024
348.20	80450.00	0.0028
348.20	100940.00	0.0033
348.20	1070.00	0.0013
373.12	1240.00	0.0009
373.12	20080.00	0.0011
373.12	40700.00	0.0014
373.12	60760.00	0.0017
373.12	80760.00	0.0020
373.12	100220.00	0.0023
373.12	1210.00	0.0009
398.21	1230.00	0.0007
398.21	20450.00	0.0009
398.21	40750.00	0.0011
398.21	60560.00	0.0013
398.21	80390.00	0.0015
398.21	100460.00	0.0017
398.21	1670.00	0.0007
423.26	1420.00	0.0005
423.26	20790.00	0.0007
423.26	40900.00	0.0008
423.26	60040.00	0.0010
423.26	80490.00	0.0012
423.26	100020.00	0.0013
423.26	1360.00	0.0005
448.23	1170.00	0.0004
448.23	20220.00	0.0006
448.23	40500.00	0.0007
448.23	60460.00	0.0008
448.23	80430.00	0.0010
448.23	100270.00	0.0011
448.23	1100.00	0.0004
473.54	1250.00	0.0004
473.54	20770.00	0.0005
473.54	40980.00	0.0006
473.54	60770.00	0.0007
473.54	80500.00	0.0008
473.54	101080.00	0.0009
473.54	1270.00	0.0004
298.61	970.00	0.0031
298.61	10340.00	0.0036
298.61	20570.00	0.0040
298.61	30370.00	0.0046
323.22	990.00	0.0019
323.22	20960.00	0.0024
323.22	42100.00	0.0030
323.22	61170.00	0.0037
323.22	81170.00	0.0045
348.20	610.00	0.0013
348.20	20370.00	0.0016
348.20	40780.00	0.0020
348.20	62000.00	0.0024
348.20	80380.00	0.0028
373.25	1370.00	0.0009
373.25	19850.00	0.0011
373.25	40190.00	0.0014
373.25	59970.00	0.0017
373.25	81310.00	0.0020
398.28	1050.00	0.0007
398.28	21190.00	0.0009
398.28	41290.00	0.0011
398.28	59990.00	0.0013
398.28	80670.00	0.0015
423.31	1460.00	0.0006
423.31	20610.00	0.0007
423.31	40760.00	0.0009
423.31	60120.00	0.0010
423.31	80990.00	0.0012
448.48	1230.00	0.0004
448.48	20750.00	0.0006
448.48	40680.00	0.0007
448.48	60650.00	0.0008
448.48	80720.00	0.0010
473.85	1400.00	0.0004
473.85	21260.00	0.0005
473.85	41040.00	0.0006
473.85	61190.00	0.0007
473.85	81710.00	0.0008
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
323.70	970.00	0.0019
322.70	1940.00	0.0019
323.80	1980.00	0.0019
323.70	3000.00	0.0019
323.80	3910.00	0.0019
372.70	990.00	0.0009
372.70	1960.00	0.0009
372.80	2970.00	0.0009
372.80	3950.00	0.0009
373.90	980.00	0.0009
373.90	2000.00	0.0009
373.90	2980.00	0.0009
373.90	3900.00	0.0009
422.90	1990.00	0.0006
422.90	2970.00	0.0006
422.90	3840.00	0.0006
471.90	1000.00	0.0004
472.00	2010.00	0.0004
472.10	2910.00	0.0004
472.10	3870.00	0.0004
473.70	3990.00	0.0004
521.90	970.00	0.0002
521.90	1960.00	0.0003
521.90	2950.00	0.0003
522.00	3830.00	0.0003
572.20	2000.00	0.0002
572.10	2930.00	0.0002
572.20	3850.00	0.0002
621.90	2010.00	0.0001
622.00	2890.00	0.0001
622.10	3820.00	0.0001
623.20	3990.00	0.0001
673.20	2000.00	0.0001
673.60	3000.00	0.0001
672.60	3990.00	0.0001
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
318.15	6895.00	0.0022
318.15	13790.00	0.0023
318.15	20680.00	0.0025
318.15	27580.00	0.0027
318.15	34470.00	0.0029
318.15	41370.00	0.0032
318.15	48260.00	0.0034
318.15	55160.00	0.0036
318.15	62050.00	0.0039
333.15	6895.00	0.0017
333.15	13790.00	0.0018
333.15	20680.00	0.0020
333.15	27580.00	0.0021
333.15	34470.00	0.0022
333.15	41370.00	0.0024
333.15	48260.00	0.0026
333.15	55160.00	0.0028
333.15	62050.00	0.0030
348.15	6895.00	0.0013
348.15	13790.00	0.0014
348.15	20680.00	0.0016
348.15	27580.00	0.0017
348.15	34470.00	0.0018
348.15	41370.00	0.0019
348.15	48260.00	0.0021
348.15	55160.00	0.0022
348.15	62050.00	0.0024
363.15	6895.00	0.0011
363.15	13790.00	0.0012
363.15	20680.00	0.0013
363.15	27580.00	0.0014
363.15	34470.00	0.0015
363.15	41370.00	0.0016
363.15	48260.00	0.0017
363.15	55160.00	0.0018
363.15	62050.00	0.0019
388.15	6895.00	0.0008
388.15	13790.00	0.0009
388.15	20680.00	0.0010
388.15	27580.00	0.0010
388.15	34470.00	0.0012
388.15	41370.00	0.0012
388.15	48260.00	0.0013
388.15	55160.00	0.0013
388.15	62050.00	0.0014
413.15	6895.00	0.0006
413.15	13790.00	0.0007
413.15	20680.00	0.0007
413.15	27580.00	0.0008
413.15	34470.00	0.0008
413.15	41370.00	0.0009
413.15	48260.00	0.0009
413.15	55160.00	0.0010
413.15	62050.00	0.0010
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
323.65	14900.00	758.0
323.65	27900.00	769.0
323.65	41500.00	779.0
323.65	55500.00	787.0
323.65	69400.00	792.0
323.65	81300.00	799.0
323.65	109700.00	807.0
422.85	14100.00	700.0
422.85	27900.00	713.0
422.85	41200.00	724.0
422.85	55500.00	734.0
422.85	69800.00	743.0
422.85	82800.00	750.0
422.85	108800.00	765.0
422.85	136900.00	778.0
422.85	170700.00	792.0
422.85	204300.00	804.0
422.85	236500.00	815.0
422.85	262300.00	823.0
522.55	15100.00	643.0
522.55	27100.00	660.0
522.55	42000.00	675.0
522.55	55400.00	687.0
522.55	69100.00	698.0
522.55	82100.00	707.0
522.55	107900.00	723.0
522.55	135800.00	738.0
522.55	170100.00	755.0
522.55	203300.00	769.0
522.55	235800.00	782.0
522.55	255000.00	788.0
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	769.98
313.15	100.00	759.6
333.15	100.00	745.81
373.15	100.00	717.79
393.15	100.00	703.59
433.15	100.00	674.64
298.15	10100.00	776.41
313.15	10100.00	766.44
373.15	10100.00	727.21
393.15	10100.00	714.02
433.15	10100.00	687.77
298.15	20100.00	782.34
313.15	20100.00	772.76
333.15	20100.00	760.5
373.15	20100.00	735.47
393.15	20100.00	723.09
433.15	20100.00	698.82
313.15	30100.00	778.65
373.15	30100.00	742.97
313.15	40100.00	784.24
333.15	40100.00	773.01
373.15	40100.00	749.88
393.15	40100.00	738.85
433.15	40100.00	717.04
333.15	50100.00	778.56
373.15	50100.00	756.25
313.15	60100.00	794.38
333.15	60100.00	783.47
373.15	60100.00	762.2
393.15	60100.00	752.0
433.15	60100.00	731.95
313.15	80100.00	803.42
333.15	80100.00	793.1
373.15	80100.00	773.03
393.15	80100.00	763.28
433.15	80100.00	744.68
333.15	100100.00	801.83
373.15	100100.00	782.74
393.15	100100.00	773.48
433.15	100100.00	755.89
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	770.5
298.15	1000.00	771.1
298.15	5000.00	773.6
298.15	10000.00	776.9
298.15	20000.00	782.6
298.15	30000.00	788.1
323.15	100.00	753.1
323.15	1000.00	753.9
323.15	5000.00	756.8
323.15	10000.00	760.4
323.15	20000.00	766.9
323.15	30000.00	772.9
323.15	40000.00	778.5
323.15	50000.00	783.8
323.15	60000.00	788.7
348.15	100.00	735.6
348.15	1000.00	736.5
348.15	5000.00	739.8
348.15	10000.00	743.8
348.15	20000.00	751.1
348.15	30000.00	757.8
348.15	40000.00	763.9
348.15	50000.00	769.7
348.15	60000.00	775.1
373.15	100.00	717.8
373.15	1000.00	719.4
373.15	5000.00	723.2
373.15	10000.00	727.7
373.15	20000.00	735.9
373.15	30000.00	743.4
373.15	40000.00	750.3
373.15	50000.00	756.5
373.15	60000.00	762.4
423.15	100.00	680.8
423.15	1000.00	684.1
423.15	5000.00	689.2
423.15	10000.00	695.1
423.15	20000.00	705.5
423.15	30000.00	714.7
423.15	40000.00	722.9
423.15	50000.00	730.4
423.15	60000.00	737.2
463.15	100.00	651.6
463.15	1000.00	654.5
463.15	5000.00	661.0
463.15	10000.00	668.5
463.15	20000.00	681.2
463.15	30000.00	692.0
463.15	40000.00	701.4
463.15	50000.00	709.8
463.15	60000.00	717.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.20	10000.00	775.86
303.20	10000.00	773.66
313.20	10000.00	764.59
323.20	10000.00	759.8
333.20	10000.00	753.38
348.20	10000.00	744.11
353.20	10000.00	740.03
373.20	10000.00	727.81
393.20	10000.00	713.25
413.20	10000.00	700.27
423.20	10000.00	694.3
433.20	10000.00	687.01
453.20	10000.00	674.02
463.20	10000.00	669.34
473.20	10000.00	660.45
298.20	20000.00	782.89
303.20	20000.00	779.38
313.20	20000.00	773.09
323.20	20000.00	766.48
333.20	20000.00	760.44
348.20	20000.00	751.32
353.20	20000.00	748.27
373.20	20000.00	736.02
393.20	20000.00	723.64
413.20	20000.00	711.23
423.20	20000.00	705.01
433.20	20000.00	698.74
453.20	20000.00	686.53
463.20	20000.00	680.32
473.20	20000.00	673.95
298.20	30000.00	788.75
303.20	30000.00	785.01
313.20	30000.00	778.81
323.20	30000.00	773.19
333.20	30000.00	767.3
348.20	30000.00	758.67
353.20	30000.00	755.72
373.20	30000.00	744.18
393.20	30000.00	732.3
413.20	30000.00	720.49
423.20	30000.00	714.62
433.20	30000.00	708.69
453.20	30000.00	696.77
463.20	30000.00	690.8
473.20	30000.00	685.23
298.20	40000.00	793.81
303.20	40000.00	790.38
313.20	40000.00	784.36
323.20	40000.00	778.83
333.20	40000.00	773.53
348.20	40000.00	765.1
353.20	40000.00	762.19
373.20	40000.00	751.02
393.20	40000.00	739.4
413.20	40000.00	728.42
423.20	40000.00	722.88
433.20	40000.00	717.4
453.20	40000.00	706.13
463.20	40000.00	700.49
473.20	40000.00	695.19
298.20	50000.00	799.18
303.20	50000.00	795.64
313.20	50000.00	789.46
323.20	50000.00	784.38
333.20	50000.00	779.1
348.20	50000.00	770.98
353.20	50000.00	768.11
373.20	50000.00	757.42
393.20	50000.00	746.41
413.20	50000.00	735.85
423.20	50000.00	730.73
433.20	50000.00	725.14
453.20	50000.00	714.59
463.20	50000.00	709.18
473.20	50000.00	704.05
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
318.15	6895.00	760.3
318.15	13789.00	765.0
318.15	20684.00	769.6
318.15	27579.00	773.9
318.15	34474.00	777.7
318.15	41369.00	781.5
318.15	48263.00	785.2
318.15	55158.00	788.7
318.15	62053.00	791.7
333.15	6895.00	750.7
333.15	13789.00	755.8
333.15	20684.00	760.4
333.15	27579.00	765.1
333.15	34474.00	769.7
333.15	41369.00	773.9
333.15	48263.00	777.6
333.15	55158.00	781.2
333.15	62053.00	784.3
348.15	6895.00	741.7
348.15	13789.00	747.2
348.15	20684.00	752.5
348.15	27579.00	757.2
348.15	34474.00	761.9
348.15	41369.00	766.1
348.15	48263.00	770.2
348.15	55158.00	774.1
348.15	62053.00	777.6
363.15	6895.00	732.0
363.15	13789.00	738.1
363.15	20684.00	743.9
363.15	27579.00	748.6
363.15	34474.00	753.7
363.15	41369.00	758.4
363.15	48263.00	762.6
363.15	55158.00	766.7
363.15	62053.00	770.5
388.15	6895.00	714.7
388.15	13789.00	721.7
388.15	20684.00	728.1
388.15	27579.00	733.9
388.15	34474.00	739.2
388.15	41369.00	744.1
388.15	48263.00	748.8
388.15	55158.00	753.3
388.15	62053.00	757.5
413.15	6895.00	696.2
413.15	13789.00	704.3
413.15	20684.00	711.0
413.15	27579.00	717.9
413.15	34474.00	723.7
413.15	41369.00	729.4
413.15	48263.00	734.5
413.15	55158.00	739.5
413.15	62053.00	743.8
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.15	340.00	759.52
313.15	690.00	759.83
313.15	1030.00	760.08
313.15	1380.00	760.33
313.15	1720.00	760.65
313.15	2070.00	760.88
313.15	2410.00	761.08
313.15	2760.00	761.33
313.15	3100.00	761.65
313.15	3450.00	761.83
313.15	3800.00	762.08
313.15	4140.00	762.33
313.15	4480.00	762.49
313.15	4830.00	762.83
313.15	5170.00	763.08
313.15	5510.00	763.33
313.15	5860.00	763.58
313.15	6200.00	763.83
313.15	6550.00	764.08
313.15	6890.00	764.33
313.15	7240.00	764.65
313.15	7580.00	764.83
313.15	7930.00	765.08
313.15	8270.00	765.33
313.15	8620.00	765.58
313.15	8960.00	765.74
313.15	9310.00	765.99
313.15	9650.00	766.24
313.15	10000.00	766.49
313.15	10340.00	766.74
313.15	10690.00	766.98
313.15	11030.00	767.22
313.15	11380.00	767.48
333.15	340.00	746.8
333.15	690.00	747.1
333.15	1030.00	747.4
333.15	1380.00	747.7
333.15	1720.00	748.0
333.15	2070.00	748.2
333.15	2410.00	748.5
333.15	2760.00	748.7
333.15	3100.00	749.0
333.15	3450.00	749.2
333.15	3800.00	749.5
333.15	4140.00	749.8
333.15	4480.00	750.0
333.15	4830.00	750.2
333.15	5170.00	750.5
333.15	5510.00	750.7
333.15	5860.00	751.0
333.15	6200.00	751.2
333.15	6550.00	751.4
333.15	6890.00	751.6
333.15	7240.00	752.0
333.15	7580.00	752.4
333.15	7930.00	752.6
333.15	8270.00	752.8
333.15	8620.00	753.0
333.15	8960.00	753.2
333.15	9310.00	753.5
333.15	9650.00	753.8
333.15	10000.00	754.0
333.15	10340.00	754.3
333.15	10690.00	754.5
333.15	11030.00	754.8
333.15	11380.00	755.0
353.15	340.00	736.2
353.15	690.00	736.4
353.15	1030.00	736.6
353.15	1380.00	736.9
353.15	1720.00	737.1
353.15	2070.00	737.4
353.15	2410.00	737.7
353.15	2760.00	738.0
353.15	3100.00	738.3
353.15	3450.00	738.7
353.15	3800.00	739.1
353.15	4140.00	739.3
353.15	4480.00	739.5
353.15	4830.00	739.8
353.15	5170.00	740.0
353.15	5510.00	740.2
353.15	5860.00	740.4
353.15	6200.00	740.5
353.15	6550.00	740.7
353.15	6890.00	741.0
353.15	7240.00	741.2
353.15	7580.00	741.5
353.15	7930.00	741.7
353.15	8270.00	742.0
353.15	8620.00	742.2
353.15	8960.00	742.5
353.15	9310.00	742.7
353.15	9650.00	742.9
353.15	10000.00	743.1
353.15	10340.00	743.5
353.15	10690.00	743.9
353.15	11030.00	744.1
353.15	11380.00	744.3
373.15	340.00	723.1
373.15	690.00	723.3
373.15	1030.00	723.6
373.15	1380.00	723.8
373.15	1720.00	724.0
373.15	2070.00	724.3
373.15	2410.00	724.6
373.15	2760.00	724.9
373.15	3100.00	725.1
373.15	3450.00	725.4
373.15	3800.00	725.6
373.15	4140.00	725.9
373.15	4480.00	726.1
373.15	4830.00	726.4
373.15	5170.00	726.7
373.15	5510.00	726.9
373.15	5860.00	727.2
373.15	6200.00	727.5
373.15	6550.00	727.8
373.15	6890.00	728.1
373.15	7240.00	728.4
373.15	7580.00	728.5
373.15	7930.00	728.9
373.15	8270.00	729.4
373.15	8620.00	729.9
373.15	8960.00	730.2
373.15	9310.00	730.6
373.15	9650.00	730.8
373.15	10000.00	731.0
373.15	10340.00	731.4
373.15	10690.00	731.6
373.15	11030.00	731.9
373.15	11380.00	732.1
393.15	340.00	710.0
393.15	690.00	710.3
393.15	1030.00	710.6
393.15	1380.00	710.9
393.15	1720.00	711.1
393.15	2070.00	711.4
393.15	2410.00	711.7
393.15	2760.00	712.0
393.15	3100.00	712.2
393.15	3450.00	712.3
393.15	3800.00	712.5
393.15	4140.00	712.8
393.15	4480.00	713.0
393.15	4830.00	713.3
393.15	5170.00	713.5
393.15	5510.00	713.8
393.15	5860.00	714.0
393.15	6200.00	714.3
393.15	6550.00	714.6
393.15	6890.00	714.9
393.15	7240.00	715.1
393.15	7580.00	715.3
393.15	7930.00	715.5
393.15	8270.00	715.8
393.15	8620.00	716.0
393.15	8960.00	716.3
393.15	9310.00	716.6
393.15	9650.00	716.8
393.15	10000.00	717.1
393.15	10340.00	717.4
393.15	10690.00	717.6
393.15	11030.00	717.9
393.15	11380.00	718.1
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[280.52; 983.80]	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			2.32700e+02
Coefficient B			-6.55340e+02
Coefficient C			7.17124e+00
Coefficient D			-1.45100e-04
Coefficient E			4.65970e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	280.52	J/mol×K	200.00	Calculated Property
Cp,gas	418.41	J/mol×K	344.44	Calculated Property
Cp,gas	553.55	J/mol×K	488.89	Calculated Property
Cp,gas	662.49	J/mol×K	633.33	Calculated Property
Cp,gas	747.61	J/mol×K	777.78	Calculated Property
Cp,gas	814.69	J/mol×K	922.22	Calculated Property
Cp,gas	868.64	J/mol×K	1066.67	Calculated Property
Cp,gas	913.15	J/mol×K	1211.11	Calculated Property
Cp,gas	950.89	J/mol×K	1355.56	Calculated Property
Cp,gas	983.80	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[496.87; 715.80]	J/mol×K	[291.31; 560.01]	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			3.87360e+02
Coefficient B			-1.23610e+02
Coefficient C			3.83024e+00
Coefficient D			5.00000e-03
Coefficient E			-1.96170e-06
Temperature range, min.			291.31
Temperature range, max.			560.01
Cp,liquid	496.87	J/mol×K	291.31	Calculated Property
Cp,liquid	514.95	J/mol×K	321.17	Calculated Property
Cp,liquid	534.52	J/mol×K	351.02	Calculated Property
Cp,liquid	555.62	J/mol×K	380.88	Calculated Property
Cp,liquid	578.31	J/mol×K	410.73	Calculated Property
Cp,liquid	602.62	J/mol×K	440.59	Calculated Property
Cp,liquid	628.54	J/mol×K	470.44	Calculated Property
Cp,liquid	656.08	J/mol×K	500.30	Calculated Property
Cp,liquid	685.18	J/mol×K	530.15	Calculated Property
Cp,liquid	715.80	J/mol×K	560.01	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0051219; 0.0000667]	Pa×s	[278.15; 723.00]	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			-8.47006e+01
Coefficient B			4.84191e+03
Coefficient C			1.11516e+01
Coefficient D			-9.61734e-06
Coefficient E			2.00000e+00
Temperature range, min.			278.15
Temperature range, max.			723.00
η	0.0051219	Pa×s	278.15	Calculated Property
η	0.0017211	Pa×s	327.58	Calculated Property
η	0.0008499	Pa×s	377.01	Calculated Property
η	0.0005172	Pa×s	426.43	Calculated Property
η	0.0003518	Pa×s	475.86	Calculated Property
η	0.0002526	Pa×s	525.29	Calculated Property
η	0.0001847	Pa×s	574.72	Calculated Property
η	0.0001345	Pa×s	624.14	Calculated Property
η	0.0000961	Pa×s	673.57	Calculated Property
η	0.0000667	Pa×s	723.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[81.61; 0.00]	kJ/mol	[291.31; 723.00]	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			1.27750e+02
Coefficient B			9.26120e-01
Coefficient C			5.25830e-01
Coefficient D			-2.14150e+00
Coefficient E			1.20390e+00
Critical temperature, Tc (K)			7.23000e+02
Temperature range, min.			291.31
Temperature range, max.			723.00
ΔvapH	81.61	kJ/mol	291.31	Calculated Property
ΔvapH	75.72	kJ/mol	339.28	Calculated Property
ΔvapH	70.32	kJ/mol	387.24	Calculated Property
ΔvapH	65.25	kJ/mol	435.21	Calculated Property
ΔvapH	60.29	kJ/mol	483.17	Calculated Property
ΔvapH	55.09	kJ/mol	531.14	Calculated Property
ΔvapH	49.12	kJ/mol	579.10	Calculated Property
ΔvapH	41.50	kJ/mol	627.07	Calculated Property
ΔvapH	30.32	kJ/mol	675.03	Calculated Property
ΔvapH	0.00	kJ/mol	723.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[421.88; 585.67]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.54069e+01
Coefficient B			-4.97629e+03
Coefficient C			-9.27430e+01
Temperature range, min.			421.88
Temperature range, max.			585.67
Pvap	1.33	kPa	421.88	Calculated Property
Pvap	2.94	kPa	440.08	Calculated Property
Pvap	6.01	kPa	458.28	Calculated Property
Pvap	11.46	kPa	476.48	Calculated Property
Pvap	20.61	kPa	494.68	Calculated Property
Pvap	35.24	kPa	512.87	Calculated Property
Pvap	57.63	kPa	531.07	Calculated Property
Pvap	90.61	kPa	549.27	Calculated Property
Pvap	137.62	kPa	567.47	Calculated Property
Pvap	202.65	kPa	585.67	Calculated Property
Pvap	[7.59e-05; 1373.82]	kPa	[288.95; 723.00]	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			1.31110e+02
Coefficient B			-1.41511e+04
Coefficient C			-1.62438e+01
Coefficient D			5.02761e-06
Coefficient E			2.00000e+00
Temperature range, min.			288.95
Temperature range, max.			723.00
Pvap	7.59e-05	kPa	288.95	Calculated Property
Pvap	7.93e-03	kPa	337.18	Calculated Property
Pvap	0.21	kPa	385.41	Calculated Property
Pvap	2.19	kPa	433.63	Calculated Property
Pvap	12.95	kPa	481.86	Calculated Property
Pvap	50.83	kPa	530.09	Calculated Property
Pvap	149.77	kPa	578.32	Calculated Property
Pvap	359.12	kPa	626.54	Calculated Property
Pvap	741.66	kPa	674.77	Calculated Property
Pvap	1373.82	kPa	723.00	Calculated Property
Pvap	[8.83e-05; 1413.13]	kPa	[291.32; 720.60]	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			1.60137e+02
Coefficient B			-1.55289e+04
Coefficient C			-2.05917e+01
Coefficient D			8.01493e-06
Coefficient E			0.00000e+00
Temperature range, min.			291.32
Temperature range, max.			720.60
Pvap	8.83e-05	kPa	291.32	Calculated Property
Pvap	8.95e-03	kPa	339.02	Calculated Property
Pvap	0.22	kPa	386.72	Calculated Property
Pvap	2.29	kPa	434.41	Calculated Property
Pvap	13.07	kPa	482.11	Calculated Property
Pvap	50.12	kPa	529.81	Calculated Property
Pvap	145.97	kPa	577.51	Calculated Property
Pvap	350.91	kPa	625.20	Calculated Property
Pvap	737.67	kPa	672.90	Calculated Property
Pvap	1413.13	kPa	720.60	Calculated Property
Pvap	[6.94; 101.24]	kPa	[463.20; 559.90]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42141e+01
Coefficient B			-4.24982e+03
Coefficient C			-1.17054e+02
Reference			Camin, Forziati, et al., 1954
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			463.20
Temperature range, max.			559.90
Pvap	6.94	kPa	463.20	Calculated Property
Pvap	10.04	kPa	473.94	Calculated Property
Pvap	14.21	kPa	484.69	Calculated Property
Pvap	19.74	kPa	495.43	Calculated Property
Pvap	26.91	kPa	506.18	Calculated Property
Pvap	36.09	kPa	516.92	Calculated Property
Pvap	47.66	kPa	527.67	Calculated Property
Pvap	62.06	kPa	538.41	Calculated Property
Pvap	79.75	kPa	549.16	Calculated Property
Pvap	101.24	kPa	559.90	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[773.45; 222.56]	kg/m3	[291.31; 723.00]	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			5.26181e+01
Coefficient B			2.36420e-01
Coefficient C			7.23000e+02
Coefficient D			2.84030e-01
Temperature range, min.			291.31
Temperature range, max.			723.00
ρl	773.45	kg/m3	291.31	Calculated Property
ρl	742.39	kg/m3	339.28	Calculated Property
ρl	709.84	kg/m3	387.24	Calculated Property
ρl	675.43	kg/m3	435.21	Calculated Property
ρl	638.63	kg/m3	483.17	Calculated Property
ρl	598.60	kg/m3	531.14	Calculated Property
ρl	553.89	kg/m3	579.10	Calculated Property
ρl	501.59	kg/m3	627.07	Calculated Property
ρl	433.79	kg/m3	675.03	Calculated Property
ρl	222.56	kg/m3	723.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.00]	N/m	[291.35; 559.95]	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			5.25070e-02
Coefficient B			-8.54000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			291.35
Temperature range, max.			559.95
γ	0.03	N/m	291.35	Calculated Property
γ	0.03	N/m	321.19	Calculated Property
γ	0.02	N/m	351.04	Calculated Property
γ	0.02	N/m	380.88	Calculated Property
γ	0.02	N/m	410.73	Calculated Property
γ	0.01	N/m	440.57	Calculated Property
γ	0.01	N/m	470.42	Calculated Property
γ	0.01	N/m	500.26	Calculated Property
γ	0.01	N/m	530.11	Calculated Property
γ	0.00	N/m	559.95	Calculated Property
γ	[0.03; 8.91e-06]	N/m	[291.31; 716.09]	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			-3.66440e-03
Coefficient B			2.20160e+02
Coefficient C			-4.82090e+00
Coefficient D			4.54190e-03
Coefficient E			-8.47450e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 723 K.
Temperature range, min.			291.31
Temperature range, max.			716.09
γ	0.03	N/m	291.31	Calculated Property
γ	0.02	N/m	338.51	Calculated Property
γ	0.02	N/m	385.71	Calculated Property
γ	0.02	N/m	432.90	Calculated Property
γ	0.01	N/m	480.10	Calculated Property
γ	0.01	N/m	527.30	Calculated Property
γ	0.01	N/m	574.50	Calculated Property
γ	0.00	N/m	621.70	Calculated Property
γ	0.00	N/m	668.89	Calculated Property
γ	8.91e-06	N/m	716.09	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.08]	W/m×K	[291.31; 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			3.59610e-06
Coefficient B			1.51180e+00
Coefficient C			5.10880e+02
Coefficient D			2.38140e+04
Temperature range, min.			291.31
Temperature range, max.			1000.00
λgas	0.01	W/m×K	291.31	Calculated Property
λgas	0.01	W/m×K	370.05	Calculated Property
λgas	0.02	W/m×K	448.80	Calculated Property
λgas	0.02	W/m×K	527.54	Calculated Property
λgas	0.03	W/m×K	606.28	Calculated Property
λgas	0.04	W/m×K	685.03	Calculated Property
λgas	0.05	W/m×K	763.77	Calculated Property
λgas	0.06	W/m×K	842.51	Calculated Property
λgas	0.07	W/m×K	921.26	Calculated Property
λgas	0.08	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.14; 0.09]	W/m×K	[291.31; 560.01]	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			6.80700e-03
Coefficient B			-1.52970e+02
Coefficient C			-4.40960e-01
Coefficient D			-3.88920e-03
Coefficient E			1.22450e-06
Temperature range, min.			291.31
Temperature range, max.			560.01
λliquid	0.14	W/m×K	291.31	Calculated Property
λliquid	0.14	W/m×K	321.17	Calculated Property
λliquid	0.13	W/m×K	351.02	Calculated Property
λliquid	0.12	W/m×K	380.88	Calculated Property
λliquid	0.12	W/m×K	410.73	Calculated Property
λliquid	0.11	W/m×K	440.59	Calculated Property
λliquid	0.10	W/m×K	470.44	Calculated Property
λliquid	0.10	W/m×K	500.30	Calculated Property
λliquid	0.09	W/m×K	530.15	Calculated Property
λliquid	0.09	W/m×K	560.01	Calculated Property

Similar Compounds

Find more compounds similar to Hexadecane.

Mixtures

• Hexadecane + Acetone
• Hexadecane + Ethanol
• Benzene + Hexadecane
• Hexadecane + 1-Butanol
• Hexadecane + Cyclohexane
• n-Hexane + Hexadecane
• Hexadecane + Methyl Alcohol
• Hexadecane + Pentane, 3-methyl-
• Hexadecane + Butane, 2,2-dimethyl-
• Hexadecane + Tetradecane
• Hexadecane + Water
• Triacetin + Hexadecane
• Triacetin + Hexadecane + Water
• Benzene + Hexadecane + Ethanol, 2-methoxy-
• Toluene + Hexadecane + Ethanol, 2-methoxy-
• p-Xylene + Hexadecane + Ethanol, 2-methoxy-
• Benzene + Acetonitrile + Hexadecane
• Toluene + Acetonitrile + Hexadecane
• Acetonitrile + p-Xylene + Hexadecane
• Acetonitrile + Hexadecane

Find more mixtures with Hexadecane.

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
• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Densities, Viscosities, and Refractive Indices of Mixtures of Hexane with Cyclohexane, Decane, Hexadecane, and Squalane at 298.15K
• Excess Volumes, Densities, Speeds of Sound, and Viscosities for the Binary Systems of 1-Octanol with Hexadecane and Squalane at (298.15, 303.15 and 308.15) K
• High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
• Solubility of 9-fluorenone, thianthrene and xanthene in organic solvents
• Liquid solid equilibria under high pressure of tetradecane + pentadecane and tetradecane + hexadecane binary systems
• Phase diagrams of binary systems containing n-alkanes, or cyclohexane, or 1-alkanols and 2,3-pentanedione at atmospheric and high pressure
• Measurement and correlation of liquid liquid equilibria for acetonitrile + n-alkane systems
• Phase behaviour of 1-methyl-3-octylimidazolium bis[trifluoromethylsulfonyl]imide with thiophene and aliphatic hydrocarbons: The influence of n-alkane chain length
• Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
• 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
• Separation of propylbenzene and n-alkanes from their mixtures using 4-methyl-N-butylpyridinium tetrafluoroborate as an ionic solvent at several temperatures
• Experimental measurements and equation of state modeling of liquid densities for long-chain n-alkanes at pressures to 265 MPa and temperatures to 523 K
• Liquid-liquid equilibria for the ternary system (water + hexadecane + dipropylene glycol n-propyl ether)
• Liquid-liquid equilibria for ternary systems acetic acid + n-butylacetate + hydrocarbons at 293.15 K
• Liquid-liquid equilibria for benzaldehyde + n-alkane mixtures andcharacterization of benzaldehyde + hydrocarbon systems in terms of DISQUAC
• A modified continuous flow apparatus for gas solubility measurements at high pressure and temperature with camera system
• Experimental measurements and thermodynamic modeling of wax disappearance temperature for the binary systems n-C14H30 + n- C16H34, n-C16H34 + n-C18H38 and n-C11H24 + n-C18H38
• Liquid liquid equilibria in the ternary systems {hexadecane + BTX aromatics + 2-methoxyethanol or acetonitrile} at 298.15 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
• Extraction of nitrogen compounds from diesel fuel using imidazolium- and pyridinium- based ionic liquids: Experiments, COSMO-RS prediction and NRTL correlation
• Isobaric vapor-liquid equilibrium for the three binary systems of C14 - C16 n-alkane + methyl myristate at 5.00 kPa
• Measurements and prediction of ternary liquid-liquid equilibria for mixtures of IL + sulfur compound + hexadecane
• Thermodynamics of aromatic polar compound (alkanone, alkanal or alkanoate) + hydrocarbon mixtures
• Volume expansion prediction of supercritical CO 2 + crude oil
• Evaluation of 1-ethyl-3-methylimidazolium methylsulfate and 1,3-dimethylimidazolium methylsulfate as solvents for extraction of alkylbenzenes from hexadecane at 313 and 333 K
• Liquid density measurements of cumene, tert-butylbenzene, and hexadecane over wide ranges of temperature and pressure
• A systematic study on volumetric and transport properties of binary systems 1-propanol + n-hexadecane, 1-butanol + n-hexadecane and 1-propanol + ethyl oleate at different temperatures: Experimental and modeling
• Experimental measurement and thermodynamic modeling of phase equilibria of {CO2 + tetralin + n-alkanes (with n = 6, 16)} and its binary systems
• 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
• Influence of size and shape effects on the high-pressure solubility of n-alkanes: Experimental data, correlation and prediction
• Phase equilibria of didecyldimethylammonium nitrate ionic liquid with water and organic solvents
• Solvent extraction of thiophene from n-alkanes (C7, C12, and C16) using the ionic liquid [C8mim][BF4]
• Studies of mixing properties of binary systems of 2-propanol with hexadecane and squalane at T = (298.15, 303.15, and 308.15) K
• Volumetric, transport, and acoustic properties of binary mixtures of 2-methyl-1-propanol with hexadecane and squalane at T = (298.15, 303.15, and 308.15) K: Experimental results, correlation, and prediction by the ERAS model
• Density and speed of sound measurements of hexadecane
• Relation between characteristic molecular volume and hydrophobicity of nonpolar molecules
• Excess molar enthalpies of binary mixtures containing 2-decanone or dipentyl ether with long-chain n-alkanes at T = 298.15 K
• Thermodynamics of mixtures containing amines. XI. Liquid + liquid equilibria and molar excess enthalpies at 298.15 K for N-methylaniline + hydrocarbon systems. Characterization in terms of DISQUAC and ERAS models
• Universal critical amplitude ratios in binary mixtures of {benzonitrile + alkane}
• Viscosity of n-hexadecane, n-octadecane and n-eicosane at pressures up to 243 MPa and temperatures up to 534 K
• Experimental high pressure speed of sound and density of (tetralin + n-decane) and (tetralin + n-hexadecane) systems and thermodynamic modeling
• Experimental measurement and prediction of (liquid + liquid + liquid) equilibrium for the system (n-hexadecane + water + triacetin)
• High pressure speed of sound and density of (decalin + n-decane), (decalin + n-hexadecane) and (n-decane + n-hexadecane) systems and thermodynamic modeling with PHCT equation of state
• Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
• Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
• Improving a variation of the DSC technique for measuring the boiling points of pure compounds at low pressures
• Experimental solubility of diosgenin and estriol in various solvents between T = (293.2-328.2) K
• Determination of melting temperatures in hydrocarbon mixtures by differential scanning calorimetry
• Heat capacity and Joule-Thomson coefficient of selected n-alkanes at 0.1 and 10 MPa in broad temperature ranges
• Determination of thermophysical properties of cyclopentane hydrate using a stirred calorimetric cell
• Densities, speeds of sound, refractive indices, viscosities and their related thermodynamic properties for n-hexadecane + two aromatic hydrocarbons binary mixtures at temperatures from 298.15 K to 318.15 K
• Ternary liquid-liquid phase equilibria of {ionic liquid + thiophene + (octane/hexadecane)}
• Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
• A simple method to determine the specific volumes of liquids and melts as a function of the temperature. Application to four n-alkanes (C16H34, C18H38, C19H40 and C21H44) under saturating vapour pressure in the 298-573K range
• Thermodynamic functions of hydrogen bonding of amines in methanol: head space analysis and solution calorimetry
• Express thermo-gravimetric method for the vaporization enthalpies appraisal for very low volatile molecular and ionic compounds.
• Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
• Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
• Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
• Silver incorporated microencapsulation of n-hexadecane and noctadecane appropriate for dynamic thermal management in textiles
• Excess Molar Volumes for Three and Four Component Mixtures Simulating the Binary Mixture (Cyclohexane+ Hexadecane)
• Densities of the binary systems n-hexane + n-decane and nhexane + n-hexadecane up to 60 MPa and 463 K
• 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
• Solid Liquid Equilibria in the Binary Systems of Saturated Fatty Acids or Triglycerides (C12 to C18) + Hexadecane
• Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
• 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
• Diffusion Coefficients of Carbon Dioxide in Eight Hydrocarbon Liquids at Temperatures between (298.15 and 423.15) K at Pressures up to 69 MPa
• Viscosities and Densities of Binary Mixtures of Hexadecane with Dissolved Methane or Carbon Dioxide at Temperatures from (298 to 473) K and at Pressures up to 120 MPa
• Liquid Liquid Equilibria for Systems Containing 4-Phenylbutan-2-one or Benzyl Ethanoate and Selected Alkanes
• Densities and Viscosities at 293.15 373.15 K, Speeds of Sound and Bulk Moduli at 293.15 333.15 K, Surface Tensions, and Flash Points of Binary Mixtures of n-Hexadecane and Alkylbenzenes at 0.1 MPa
• Interfacial Tension Measurement and Calculation of (Carbon Dioxide + n-Alkane) Binary Mixtures
• 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
• Synthesis and Physical and Thermodynamic Properties of Lactic Acid and Malic Acid-Based Natural Deep Eutectic Solvents
• 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
• Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
• Viscosities of Liquid Hexadecane at Temperatures between 323 K and 673 K and Pressures up to 4 MPa Measured Using a Dual-Capillary Viscometer
• Density and Volumetric Properties of Binary Mixtures of CO2 + Hexadecane from (303.2 to 473.2) K and Pressures up to 50.0 MPa
• Measurement and Prediction of Excess Properties of Binary Mixtures Methyl Decanoate + an Even-Numbered n-Alkane (C6-C16) at 298.15 K
• Liquid-Liquid Equilibria for Benzene/Thiophene + Cyclohexane/Hexadecane + Deep Eutectic Solvents: Data and Correlation
• Fixed-Path Length Laser-Induced Sound Pinging: A Streamlined Method for Sound Speed Determination in Arbitrary Liquids
• Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
• 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
• Ternary Liquid-Liquid Equilibria for Mixtures of 1-Methyl-3-octylimidazolium Chloride + an Alkanol + an Alkane at 298.2 K and 1 bar
• Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
• Liquid-Liquid Equilibria for Ternary Mixtures (an Ionic Liquid + Benzene +Heptane or Hexadecane) at T ) 298.2 K and Atmospheric Pressure
• Liquid-Liquid Equilibria Measurements for Ternary System of Hexadecane + 1,3,5-Trimethylbenzene + N-Methyl-2-pyrrolidone
• High-Pressure Density Measurements for the Binary System Cyclohexane + n-Hexadecane in the Temperature Range of (318.15 to 413.15) K
• Liquid-Liquid Equilibria for the Ternary System Water + Hexadecane + Propylene Glycol n-Propyl Ether
• Densities, Sound Velocities, and Refractive Indexes of Tetralin + n-Hexadecane at (293.15, 303.15, 313.15, 323.15, 333.15, and 343.15) K
• Vapor Liquid Phase Equilibria and Physical Properties Measurements for Ternary Systems (Methane + Decane + Hexadecane)
• Temperature and Composition Effect on CO2 Miscibility by Interfacial Tension Measurement
• Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Direct Sugar to Hydrocarbon Diesel (DSH-76) and Binary Mixtures of N-Hexadecane and 2,2,4,6,6-Pentamethylheptane
• Thermodynamics of Mixtures Containing Amines. XV. Liquid Liquid Equilibria for Benzylamine + CH3(CH2)nCH3 (n = 8, 9, 10, 12, 14)
• Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
• Liquid-Liquid Equilibria for Binary System of Ethanol + Hexadecane at Elevated Temperature and the Ternary Systems of Ethanol + Heterocyclic Nitrogen Compounds + Hexadecane at 298.15 K
• Solid-Liquid Equilibria of Dibenzothiophene and Dibenzothiophene Sulfone in Organic Solvents
• Temperature and Composition Dependence of the Densities, Viscosities, and Speeds of Sound of Binary Liquid Mixtures of 1-Butanol with Hexadecane and Squalane
• Liquid-Liquid Equilibrium of Ternary Mixtures Formed by Some Oligooxaethylenes with Ethanol and Hexadecane
• Binary Liquid-Liquid Equilibrium (LLE) for N-Methylformamide (NMF) + Hexadecane between (288.15 and 318.15) K and Ternary LLE for Systems of NMF + Heterocyclic Nitrogen Compounds + Hexadecane at 298.15 K
• Solubility of Carbon Dioxide in Water and Hexadecane: Experimental Measurement and Thermodynamic Modeling
• High-Pressure Viscosity Measurements for the Binary System Cyclohexane + n-Hexadecane in the Temperature Range of (318.15 to 413.15) K
• Excess Molar Enthalpies of Binary Systems of 2-Octanone or 3-Octanone with Dodecane, Tetradecane, or Hexadecane at 298.15 K
• 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
• (Liquid + Liquid) Equilibrium for (N,N-Dimethylformamide (DMF) + Hexadecane) at Temperatures between (293.15 and 313.15) K and Ternary Mixtures of (DMF + Hexadecane) with Either Quinoline, or Pyridine, or Pyrrole, or Aniline, or Indole at T = 298.15 K
• Experimental Measurement and Thermodynamic Modeling for the Solubility of Methane in Water and Hexadecane
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure
• Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD

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