Chemical Properties of Squalane (CAS 111-01-3)

InChI

InChI=1S/C30H62/c1-25(2)15-11-19-29(7)23-13-21-27(5)17-9-10-18-28(6)22-14-24-30(8)20-12-16-26(3)4/h25-30H,9-24H2,1-8H3

InChI Key

PRAKJMSDJKAYCZ-UHFFFAOYSA-N

Formula

C30H62

SMILES

CC(C)CCCC(C)CCCC(C)CCCCC(C)CCCC(C)CCCC(C)C

Molecular Weight¹

422.81

CAS

111-01-3

Other Names

• 2,6,10,15,19,23-hexamethyltetracosane
• Cosbiol
• Dodecahydrosqualene
• Hexamethyltetracosane
• NSC 6851
• Perhydrosqualene
• Robane
• Spinacane
• Squalan
• Squalane N
• Tetracosane, 2,6,10,15,19,23-hexamethyl-
• Vitabiosol

• 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).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_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).
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• D^*_i : Self diffusion coefficient (m²/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ : Gas thermal conductivity (W/m×K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

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

Physical Properties

Property	Value	Unit	Source
ω	0.9153		ChemSep v8.3 pure component data Compiled value
ΔcH°liquid	[-19801.30; -19800.60]	kJ/mol
ΔcH°liquid	-19801.30 ± 4.90	kJ/mol	NIST
ΔcH°liquid	-19800.60 ± 1.90	kJ/mol	NIST
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	186.80	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-689.60	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°liquid	[-865.40; -864.70]	kJ/mol
ΔfH°liquid	-864.70 ± 6.40	kJ/mol	NIST
ΔfH°liquid	-865.40 ± 5.90	kJ/mol	NIST
ΔfusH°	52.32	kJ/mol	Joback Calculated Property
ΔvapH°	123.79	kJ/mol	Relay (1.0) Calculated Property
IE	9.72	eV	Relay (1.0) Calculated Property
log10WS	-10.95		Relay (1.0) Calculated Property
logPoct/wat	11.084		Crippen Calculated Property
McVol	433.560	ml/mol	McGowan Calculated Property
Pc	[700.00; 868.00]	kPa
Pc	700.00	kPa	Vapor liquid critical properties of squalane measured by the pulse-heating technique
Pc	868.00	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	0.00	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[2630.00; 2668.00]
Inp	2665.00		NIST
Inp	2666.00		NIST
Inp	2666.00		NIST
Inp	2667.00		NIST
Inp	2665.00		NIST
Inp	2666.00		NIST
Inp	2666.00		NIST
Inp	2666.00		NIST
Inp	2657.00		NIST
Inp	2657.00		NIST
Inp	2658.10		NIST
Inp	2658.50		NIST
Inp	2660.00		NIST
Inp	2664.40		NIST
Inp	2656.10		NIST
Inp	2663.00		NIST
Inp	2657.00		NIST
Inp	2668.00		NIST
Inp	Outlier 2630.00		NIST
Inp	2663.00		NIST
Inp	Outlier 2630.00		NIST
Inp	Outlier 2632.00		NIST
Inp	2668.00		NIST
Inp	2660.00		NIST
Tboil	623.15	K	ChemSep v8.3 pure component data Compiled value
Tc	[805.00; 863.00]	K
Tc	805.00	K	DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
Tc	863.00	K	ChemSep v8.3 pure component data Compiled value
Tfus	235.15	K	ChemSep v8.3 pure component data Compiled value
Ttriple	235.15	K	ChemSep v8.3 pure component data Compiled value
UQi	16.82		ChemSep v8.3 pure component data Compiled value
URi	20.69		ChemSep v8.3 pure component data Compiled value
Vc	1.640	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.1980000		ChemSep v8.3 pure component data Compiled value
Zra	0.20		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[886.36; 931.00]	J/mol×K	[298.15; 400.00]
Cp,liquid	886.36	J/mol×K	298.15	NIST
Cp,liquid	891.00	J/mol×K	300.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	895.00	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
Cp,liquid	899.00	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
Cp,liquid	903.00	J/mol×K	330.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	907.00	J/mol×K	340.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	911.00	J/mol×K	350.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	915.00	J/mol×K	360.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	919.00	J/mol×K	370.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	923.00	J/mol×K	380.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	927.00	J/mol×K	390.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	931.00	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	[0.0037800; 0.0602000]	Pa×s	[283.77; 362.98]
η	0.0602000	Pa×s	283.77	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0461000	Pa×s	288.47	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0355900	Pa×s	293.29	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0279500	Pa×s	298.12	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0282570	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	0.0282570	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	0.0282570	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	0.0224500	Pa×s	303.07	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0220870	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	0.0220870	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	0.0220870	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	0.0183000	Pa×s	308.09	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0177740	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	0.0177740	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	0.0177740	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	0.0150000	Pa×s	313.13	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0125000	Pa×s	318.17	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0105700	Pa×s	323.19	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0089900	Pa×s	328.26	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0078000	Pa×s	333.20	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0068100	Pa×s	338.18	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0060000	Pa×s	343.07	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0053200	Pa×s	348.08	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0047200	Pa×s	353.08	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0042000	Pa×s	358.13	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
η	0.0037800	Pa×s	362.98	Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
ΔvapH	[116.20; 134.40]	kJ/mol	[298.15; 438.00]
ΔvapH	134.40	kJ/mol	298.15	The vapor pressure and vaporization enthalpy of squalene and squalane by correlation gas chromatography
ΔvapH	116.20	kJ/mol	438.00	NIST
n0	1.44740		298.15	Densities, Viscosities, and Refractive Indices of Mixtures of Hexane with Cyclohexane, Decane, Hexadecane, and Squalane at 298.15K
ρl	[764.06; 821.58]	kg/m3	[273.15; 363.15]
ρl	821.58	kg/m3	273.15	Temperature and Pressure Dependence of the Viscosities of 2-Ethylhexyl Benzoate, Bis(2-ethylhexyl) Phthalate, 2,6,10,15,19,23-Hexamethyltetracosane (Squalane), and Diisodecyl Phthalate
ρl	815.16	kg/m3	283.15	Temperature and Pressure Dependence of the Viscosities of 2-Ethylhexyl Benzoate, Bis(2-ethylhexyl) Phthalate, 2,6,10,15,19,23-Hexamethyltetracosane (Squalane), and Diisodecyl Phthalate
ρl	811.95	kg/m3	288.15	Temperature and Pressure Dependence of the Viscosities of 2-Ethylhexyl Benzoate, Bis(2-ethylhexyl) Phthalate, 2,6,10,15,19,23-Hexamethyltetracosane (Squalane), and Diisodecyl Phthalate
ρl	808.74	kg/m3	293.15	Temperature and Pressure Dependence of the Viscosities of 2-Ethylhexyl Benzoate, Bis(2-ethylhexyl) Phthalate, 2,6,10,15,19,23-Hexamethyltetracosane (Squalane), and Diisodecyl Phthalate
ρl	805.55	kg/m3	298.15	Temperature and Pressure Dependence of the Viscosities of 2-Ethylhexyl Benzoate, Bis(2-ethylhexyl) Phthalate, 2,6,10,15,19,23-Hexamethyltetracosane (Squalane), and Diisodecyl Phthalate
ρl	802.34	kg/m3	303.15	Temperature and Pressure Dependence of the Viscosities of 2-Ethylhexyl Benzoate, Bis(2-ethylhexyl) Phthalate, 2,6,10,15,19,23-Hexamethyltetracosane (Squalane), and Diisodecyl Phthalate
ρl	795.93	kg/m3	313.15	Temperature and Pressure Dependence of the Viscosities of 2-Ethylhexyl Benzoate, Bis(2-ethylhexyl) Phthalate, 2,6,10,15,19,23-Hexamethyltetracosane (Squalane), and Diisodecyl Phthalate
ρl	789.53	kg/m3	323.15	Temperature and Pressure Dependence of the Viscosities of 2-Ethylhexyl Benzoate, Bis(2-ethylhexyl) Phthalate, 2,6,10,15,19,23-Hexamethyltetracosane (Squalane), and Diisodecyl Phthalate
ρl	783.14	kg/m3	333.15	Temperature and Pressure Dependence of the Viscosities of 2-Ethylhexyl Benzoate, Bis(2-ethylhexyl) Phthalate, 2,6,10,15,19,23-Hexamethyltetracosane (Squalane), and Diisodecyl Phthalate
ρl	776.77	kg/m3	343.15	Temperature and Pressure Dependence of the Viscosities of 2-Ethylhexyl Benzoate, Bis(2-ethylhexyl) Phthalate, 2,6,10,15,19,23-Hexamethyltetracosane (Squalane), and Diisodecyl Phthalate
ρl	770.42	kg/m3	353.15	Temperature and Pressure Dependence of the Viscosities of 2-Ethylhexyl Benzoate, Bis(2-ethylhexyl) Phthalate, 2,6,10,15,19,23-Hexamethyltetracosane (Squalane), and Diisodecyl Phthalate
ρl	764.06	kg/m3	363.15	Temperature and Pressure Dependence of the Viscosities of 2-Ethylhexyl Benzoate, Bis(2-ethylhexyl) Phthalate, 2,6,10,15,19,23-Hexamethyltetracosane (Squalane), and Diisodecyl Phthalate
D*i	[0.00; 0.00]	m2/s	[283.30; 362.88]
D*i	0.00	m2/s	283.30	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	288.28	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	293.13	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	293.19	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	298.19	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	298.44	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	303.00	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	303.18	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	312.99	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	322.69	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	322.72	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	323.16	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	333.03	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	333.49	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	342.81	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	348.20	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	352.82	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	353.15	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	362.60	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	362.82	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	362.88	Viscous Calibration Liquids for Self-diffusion Measurements

Datasets

1. Molar heat capacity at constant pressure, J/K/mol (1)
2. Viscosity, Pa*s (5)
3. Mass density, kg/m3 (4)

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
293.15	100.00	879.00
293.15	10000.00	873.50
293.15	20000.00	868.50
293.15	30000.00	865.50
313.15	100.00	904.40
313.15	10000.00	898.90
313.15	20000.00	896.40
313.15	30000.00	893.40
333.15	100.00	943.30
333.15	10000.00	940.80
333.15	20000.00	936.10
333.15	30000.00	929.30
353.15	100.00	978.80
353.15	10000.00	973.70
353.15	20000.00	963.20
353.15	30000.00	959.80
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
273.15	100.00	0.1166
273.15	10000.00	0.1524
273.15	20000.00	0.1994
273.15	30000.00	0.2614
293.15	100.00	0.0353
293.15	10000.00	0.0436
293.15	20000.00	0.0540
293.15	30000.00	0.0656
313.15	100.00	0.0154
313.15	10000.00	0.0183
313.15	20000.00	0.0227
313.15	30000.00	0.0275
333.15	100.00	0.0078
333.15	10000.00	0.0094
333.15	20000.00	0.0110
333.15	30000.00	0.0131
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
338.15	50600.00	0.0156
338.15	102800.00	0.0329
338.15	150200.00	0.0609
338.15	198400.00	0.1089
338.15	249700.00	0.1940
338.15	272700.00	0.2438
338.15	299800.00	0.3276
338.15	349200.00	0.5385
338.15	349200.00	0.5310
348.15	198300.00	0.0708
348.15	200400.00	0.0726
348.15	300600.00	0.2029
348.15	349800.00	0.3276
363.15	10200.00	0.0044
363.15	21000.00	0.0052
363.15	30900.00	0.0060
363.15	40700.00	0.0068
363.15	50600.00	0.0078
363.15	60600.00	0.0089
363.15	70700.00	0.0102
363.15	80600.00	0.0115
363.15	91000.00	0.0131
363.15	100000.00	0.0146
363.15	120400.00	0.0184
363.15	150300.00	0.0256
363.15	200200.00	0.0428
363.15	225600.00	0.0550
363.15	246900.00	0.0662
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.15	10000.00	0.0274
303.15	15000.00	0.0308
303.15	25000.00	0.0382
303.15	50000.00	0.0627
303.15	75000.00	0.0985
303.15	100000.00	0.1508
303.15	125000.00	0.2274
303.15	150000.00	0.3395
313.15	10000.00	0.0184
313.15	15000.00	0.0204
313.15	25000.00	0.0248
313.15	50000.00	0.0391
313.15	75000.00	0.0595
313.15	100000.00	0.0887
313.15	125000.00	0.1303
313.15	150000.00	0.1898
323.15	10000.00	0.0130
323.15	15000.00	0.0143
323.15	25000.00	0.0171
323.15	50000.00	0.0261
323.15	75000.00	0.0387
323.15	100000.00	0.0563
323.15	125000.00	0.0809
323.15	150000.00	0.1154
333.15	10000.00	0.0092
333.15	15000.00	0.0101
333.15	25000.00	0.0121
333.15	50000.00	0.0182
333.15	75000.00	0.0265
333.15	100000.00	0.0378
333.15	125000.00	0.0532
333.15	150000.00	0.0740
343.15	10000.00	0.0070
343.15	15000.00	0.0076
343.15	25000.00	0.0090
343.15	50000.00	0.0133
343.15	75000.00	0.0190
343.15	100000.00	0.0267
343.15	125000.00	0.0370
343.15	150000.00	0.0508
353.15	10000.00	0.0054
353.15	15000.00	0.0059
353.15	25000.00	0.0069
353.15	50000.00	0.0101
353.15	75000.00	0.0142
353.15	100000.00	0.0195
353.15	125000.00	0.0264
353.15	150000.00	0.0355
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.15	10000.00	0.0281
303.15	15000.00	0.0314
303.15	25000.00	0.0387
303.15	50000.00	0.0623
303.15	75000.00	0.0975
303.15	100000.00	0.1497
303.15	125000.00	0.2270
303.15	150000.00	0.3410
313.15	10000.00	0.0182
313.15	15000.00	0.0203
313.15	25000.00	0.0249
313.15	50000.00	0.0398
313.15	75000.00	0.0610
313.15	100000.00	0.0913
313.15	125000.00	0.1346
313.15	150000.00	0.1964
343.15	10000.00	0.0073
343.15	15000.00	0.0079
343.15	25000.00	0.0093
343.15	50000.00	0.0136
343.15	75000.00	0.0193
343.15	100000.00	0.0270
343.15	125000.00	0.0372
343.15	150000.00	0.0510
353.15	10000.00	0.0056
353.15	15000.00	0.0060
353.15	25000.00	0.0070
353.15	50000.00	0.0101
353.15	75000.00	0.0140
353.15	100000.00	0.0193
353.15	125000.00	0.0263
353.15	150000.00	0.0356
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.18	1070.00	0.0220
303.18	5300.00	0.0242
303.18	5740.00	0.0244
303.18	15580.00	0.0303
303.18	25530.00	0.0369
303.18	35790.00	0.0443
303.18	45770.00	0.0546
303.18	55770.00	0.0663
348.13	5270.00	0.0056
348.13	5290.00	0.0056
348.13	25490.00	0.0078
348.13	56280.00	0.0123
348.13	85860.00	0.0184
348.13	115830.00	0.0269
348.13	145930.00	0.0387
348.13	175120.00	0.0556
398.15	5160.00	0.0022
398.15	5230.00	0.0022
398.15	25310.00	0.0029
398.15	56100.00	0.0042
398.15	85890.00	0.0059
398.15	115450.00	0.0079
398.15	145820.00	0.0106
398.15	176100.00	0.0138
448.25	5580.00	0.0012
448.25	5730.00	0.0012
448.25	25470.00	0.0015
448.25	55510.00	0.0022
448.25	85620.00	0.0029
448.25	115510.00	0.0038
448.25	145580.00	0.0048
448.25	176050.00	0.0060
Reference

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	298.15	804.9
1000.00	298.15	805.4
5000.00	298.15	807.8
10000.00	298.15	810.7
15000.00	298.15	813.4
20000.00	298.15	816.1
30000.00	298.15	821.2
40000.00	298.15	826.0
45000.00	298.15	828.3
50000.00	298.15	830.5
60000.00	298.15	834.8
100.00	323.15	789.0
1000.00	323.15	789.6
5000.00	323.15	792.3
10000.00	323.15	795.5
15000.00	323.15	798.6
20000.00	323.15	801.5
30000.00	323.15	807.1
40000.00	323.15	812.3
45000.00	323.15	814.8
50000.00	323.15	817.2
60000.00	323.15	821.9
100.00	348.15	773.0
1000.00	348.15	773.7
5000.00	348.15	776.7
10000.00	348.15	780.3
15000.00	348.15	783.7
20000.00	348.15	787.0
30000.00	348.15	793.2
40000.00	348.15	799.0
45000.00	348.15	801.7
50000.00	348.15	804.3
60000.00	348.15	809.3
1000.00	373.15	758.0
5000.00	373.15	761.3
10000.00	373.15	765.3
15000.00	373.15	769.1
20000.00	373.15	772.7
30000.00	373.15	779.5
40000.00	373.15	785.8
45000.00	373.15	788.7
50000.00	373.15	791.6
60000.00	373.15	797.1
1000.00	398.15	742.1
5000.00	398.15	745.9
10000.00	398.15	750.4
15000.00	398.15	754.6
20000.00	398.15	758.6
30000.00	398.15	766.1
40000.00	398.15	772.9
45000.00	398.15	776.1
50000.00	398.15	779.1
60000.00	398.15	785.0
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.15	5700.00	798.1
313.15	13500.00	804.3
313.15	23500.00	811.4
313.15	45700.00	822.6
313.15	68000.00	832.5
338.15	7900.00	783.2
338.15	11000.00	785.2
338.15	22500.00	793.3
338.15	45600.00	807.5
338.15	60500.00	814.6
338.15	76300.00	820.5
363.15	10600.00	769.9
363.15	21500.00	777.9
363.15	42500.00	791.1
363.15	63700.00	802.4
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
278.15	100.00	818.1
278.15	1000.00	818.59
278.15	5000.00	820.71
278.15	10000.00	823.31
278.15	15000.00	825.81
278.15	20000.00	828.24
278.15	25000.00	830.59
278.15	30000.00	832.87
278.15	35000.00	835.07
278.15	40000.00	837.21
278.15	45000.00	839.31
283.15	100.00	814.75
283.15	1000.00	815.25
283.15	5000.00	817.45
283.15	10000.00	820.16
283.15	15000.00	822.72
283.15	20000.00	825.21
283.15	25000.00	827.62
283.15	30000.00	829.94
283.15	35000.00	832.23
283.15	40000.00	834.41
283.15	45000.00	836.54
293.15	100.00	808.27
293.15	1000.00	808.81
293.15	5000.00	811.1
293.15	10000.00	813.88
293.15	15000.00	816.58
293.15	20000.00	819.18
293.15	25000.00	821.67
293.15	30000.00	824.14
293.15	35000.00	826.49
293.15	40000.00	828.81
293.15	45000.00	831.04
303.15	100.00	801.88
303.15	1000.00	802.43
303.15	5000.00	804.87
303.15	10000.00	807.78
303.15	15000.00	810.59
303.15	20000.00	813.29
303.15	25000.00	815.92
303.15	30000.00	818.45
303.15	35000.00	820.92
303.15	40000.00	823.29
303.15	45000.00	825.61
313.15	100.00	795.53
313.15	1000.00	796.12
313.15	5000.00	798.64
313.15	10000.00	801.68
313.15	15000.00	804.61
313.15	20000.00	807.43
313.15	25000.00	810.22
313.15	30000.00	812.78
313.15	35000.00	815.35
313.15	40000.00	817.81
313.15	45000.00	820.22
323.15	100.00	789.06
323.15	1000.00	789.69
323.15	5000.00	792.34
323.15	10000.00	795.54
323.15	15000.00	798.63
323.15	20000.00	801.58
323.15	25000.00	804.45
323.15	30000.00	807.17
323.15	35000.00	809.84
323.15	40000.00	812.42
323.15	45000.00	814.91
333.15	100.00	782.73
333.15	1000.00	783.37
333.15	5000.00	786.19
333.15	10000.00	789.56
333.15	15000.00	792.76
333.15	20000.00	795.83
333.15	25000.00	798.79
333.15	30000.00	801.62
333.15	35000.00	804.39
333.15	40000.00	807.03
333.15	45000.00	809.62
343.15	100.00	776.31
343.15	1000.00	777.0
343.15	5000.00	779.93
343.15	10000.00	783.45
343.15	15000.00	786.81
343.15	20000.00	790.03
343.15	25000.00	793.12
343.15	30000.00	796.08
343.15	35000.00	798.94
343.15	40000.00	801.71
343.15	45000.00	804.4
353.15	100.00	770.03
353.15	1000.00	770.73
353.15	5000.00	773.84
353.15	10000.00	777.5
353.15	15000.00	781.02
353.15	20000.00	784.36
353.15	25000.00	787.57
353.15	30000.00	790.66
353.15	35000.00	793.62
353.15	40000.00	796.47
353.15	45000.00	799.24
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
338.19	1050.00	779.26
338.19	21210.00	792.77
338.20	40640.00	803.93
338.20	60420.00	814.29
338.20	79830.00	822.46
338.20	100230.00	831.55
338.21	119820.00	837.96
338.20	140240.00	845.12
338.20	161300.00	851.46
338.22	940.00	778.91
373.12	780.00	756.09
373.12	20350.00	771.55
373.12	39970.00	784.5
373.12	60030.00	795.89
373.12	80950.00	806.36
373.12	101160.00	815.48
373.12	120420.00	823.57
373.12	140640.00	831.1
373.12	159510.00	837.61
373.12	180460.00	843.98
373.12	201380.00	850.63
373.12	620.00	756.02
388.14	1100.00	746.78
388.13	20290.00	762.98
388.14	40380.00	776.95
388.14	59850.00	788.53
388.13	80490.00	799.25
388.13	101530.00	809.12
388.13	120960.00	817.16
388.13	139900.00	824.59
388.14	160800.00	832.35
388.14	180610.00	838.96
388.14	201470.00	845.55
388.13	890.00	746.65
413.17	1050.00	730.56
413.18	20110.00	748.65
413.18	40280.00	763.94
413.18	60200.00	776.68
413.21	80740.00	788.16
413.22	100350.00	797.82
413.22	120460.00	806.56
413.24	140200.00	815.07
413.25	160570.00	822.8
413.25	181450.00	829.85
413.25	202090.00	836.75
413.24	610.00	730.1
433.36	680.00	717.22
433.31	600.00	717.04
433.35	20500.00	737.74
433.36	40310.00	753.83
433.19	60430.00	767.55
433.20	80190.00	779.13
433.21	100280.00	789.84
433.21	120040.00	798.72
433.21	140200.00	807.55
433.19	160660.00	815.65
433.19	180700.00	823.09
433.19	200370.00	830.05
433.18	1120.00	717.8
453.15	1150.00	704.74
453.16	20190.00	726.4
453.17	40450.00	744.09
453.18	60480.00	758.43
453.18	80140.00	770.59
453.18	100410.00	781.58
453.20	120790.00	791.61
453.20	140400.00	800.32
453.19	160150.00	808.49
453.20	180710.00	816.55
338.29	1010.00	779.46
452.95	163170.00	809.3
452.95	180270.00	815.84
452.85	201770.00	823.37
473.05	150.00	690.19
472.81	1050.00	691.59
473.05	20040.00	715.2
473.05	39890.00	733.71
473.06	60230.00	749.17
473.06	79910.00	761.86
473.07	100370.00	773.42
473.05	120200.00	783.48
473.05	140440.00	792.71
473.05	160340.00	801.0
473.05	180470.00	808.83
473.03	200210.00	815.83
473.04	1050.00	691.45
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[634.77; 1822.54]	J/mol×K	[273.00; 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			3.69830e+02
Coefficient B			-5.53390e+02
Coefficient C			7.58124e+00
Coefficient D			1.03190e-04
Coefficient E			-3.81860e-08
Comment			ChemSep eq 16, IdealGasHeatCapacityCp
Temperature range, min.			273.00
Temperature range, max.			1500.00
Cp,gas	634.77	J/mol×K	273.00	Calculated Property
Cp,gas	895.75	J/mol×K	409.33	Calculated Property
Cp,gas	1113.82	J/mol×K	545.67	Calculated Property
Cp,gas	1288.05	J/mol×K	682.00	Calculated Property
Cp,gas	1427.56	J/mol×K	818.33	Calculated Property
Cp,gas	1540.45	J/mol×K	954.67	Calculated Property
Cp,gas	1632.70	J/mol×K	1091.00	Calculated Property
Cp,gas	1708.57	J/mol×K	1227.33	Calculated Property
Cp,gas	1771.11	J/mol×K	1363.67	Calculated Property
Cp,gas	1822.54	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[828.01; 1476.30]	J/mol×K	[300.00; 720.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			-3.82760e+01
Coefficient B			-1.13460e+02
Coefficient C			6.82024e+00
Coefficient D			1.18600e-03
Coefficient E			-3.73630e-07
Comment			ChemSep eq 16, LiquidHeatCapacityCp
Temperature range, min.			300.00
Temperature range, max.			720.00
Cp,liquid	828.01	J/mol×K	300.00	Calculated Property
Cp,liquid	914.33	J/mol×K	346.67	Calculated Property
Cp,liquid	994.99	J/mol×K	393.33	Calculated Property
Cp,liquid	1071.47	J/mol×K	440.00	Calculated Property
Cp,liquid	1144.72	J/mol×K	486.67	Calculated Property
Cp,liquid	1215.31	J/mol×K	533.33	Calculated Property
Cp,liquid	1283.61	J/mol×K	580.00	Calculated Property
Cp,liquid	1349.82	J/mol×K	626.67	Calculated Property
Cp,liquid	1414.04	J/mol×K	673.33	Calculated Property
Cp,liquid	1476.30	J/mol×K	720.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[117.63; 0.00]	kJ/mol	[235.15; 863.00]	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			1.32740e+02
Coefficient B			3.80000e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			8.63000e+02
Comment			ChemSep eq 106, HeatOfVaporization
Temperature range, min.			235.15
Temperature range, max.			863.00
ΔvapH	117.63	kJ/mol	235.15	Calculated Property
ΔvapH	112.48	kJ/mol	304.91	Calculated Property
ΔvapH	106.91	kJ/mol	374.67	Calculated Property
ΔvapH	100.83	kJ/mol	444.43	Calculated Property
ΔvapH	94.08	kJ/mol	514.19	Calculated Property
ΔvapH	86.43	kJ/mol	583.96	Calculated Property
ΔvapH	77.48	kJ/mol	653.72	Calculated Property
ΔvapH	66.42	kJ/mol	723.48	Calculated Property
ΔvapH	51.04	kJ/mol	793.24	Calculated Property
ΔvapH	0.00	kJ/mol	863.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[556.00; 747.17]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.62095e+01
Coefficient B			-6.60264e+03
Coefficient C			-1.41310e+02
Temperature range, min.			556.00
Temperature range, max.			747.17
Pvap	1.33	kPa	556.00	Calculated Property
Pvap	2.90	kPa	577.24	Calculated Property
Pvap	5.85	kPa	598.48	Calculated Property
Pvap	11.12	kPa	619.72	Calculated Property
Pvap	19.99	kPa	640.96	Calculated Property
Pvap	34.26	kPa	662.21	Calculated Property
Pvap	56.29	kPa	683.45	Calculated Property
Pvap	89.10	kPa	704.69	Calculated Property
Pvap	136.39	kPa	725.93	Calculated Property
Pvap	202.66	kPa	747.17	Calculated Property
Pvap	[0.00; 864.87]	kPa	[235.15; 863.00]	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			5.11542e+02
Coefficient B			-4.03420e+04
Coefficient C			-7.04910e+01
Coefficient D			2.48600e-05
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			235.15
Temperature range, max.			863.00
Pvap	0.00	kPa	235.15	Calculated Property
Pvap	3.90e-10	kPa	304.91	Calculated Property
Pvap	3.12e-05	kPa	374.67	Calculated Property
Pvap	0.02	kPa	444.43	Calculated Property
Pvap	0.68	kPa	514.19	Calculated Property
Pvap	6.82	kPa	583.96	Calculated Property
Pvap	32.59	kPa	653.72	Calculated Property
Pvap	107.30	kPa	723.48	Calculated Property
Pvap	305.16	kPa	793.24	Calculated Property
Pvap	864.87	kPa	863.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[842.59; 257.92]	kg/m3	[235.15; 863.00]	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			6.76332e+01
Coefficient B			2.62230e-01
Coefficient C			8.63000e+02
Coefficient D			3.86040e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			235.15
Temperature range, max.			863.00
ρl	842.59	kg/m3	235.15	Calculated Property
ρl	799.40	kg/m3	304.91	Calculated Property
ρl	755.23	kg/m3	374.67	Calculated Property
ρl	709.78	kg/m3	444.43	Calculated Property
ρl	662.59	kg/m3	514.19	Calculated Property
ρl	612.95	kg/m3	583.96	Calculated Property
ρl	559.64	kg/m3	653.72	Calculated Property
ρl	500.22	kg/m3	723.48	Calculated Property
ρl	428.17	kg/m3	793.24	Calculated Property
ρl	257.92	kg/m3	863.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 4.52e-06]	N/m	[235.15; 839.77]	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			-6.80440e-02
Coefficient B			-2.04250e+01
Coefficient C			-1.86680e+00
Coefficient D			-1.54380e-03
Coefficient E			7.09040e-07
Comment			ChemSep eq 16, SurfaceTension, ChemSep Tmax 863 K
Temperature range, min.			235.15
Temperature range, max.			839.77
γ	0.03	N/m	235.15	Calculated Property
γ	0.03	N/m	302.33	Calculated Property
γ	0.02	N/m	369.51	Calculated Property
γ	0.02	N/m	436.69	Calculated Property
γ	0.01	N/m	503.87	Calculated Property
γ	0.01	N/m	571.05	Calculated Property
γ	0.01	N/m	638.23	Calculated Property
γ	0.00	N/m	705.41	Calculated Property
γ	0.00	N/m	772.59	Calculated Property
γ	4.52e-06	N/m	839.77	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.00; 0.05]	W/m×K	[235.15; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K
Coefficient A			5.67140e-05
Coefficient B			1.06250e+00
Coefficient C			5.51790e+02
Coefficient D			7.55790e+04
Comment			ChemSep eq 102, VaporThermalConductivity
Temperature range, min.			235.15
Temperature range, max.			1000.00
λ	0.00	W/m×K	235.15	Calculated Property
λ	0.01	W/m×K	320.13	Calculated Property
λ	0.01	W/m×K	405.12	Calculated Property
λ	0.02	W/m×K	490.10	Calculated Property
λ	0.02	W/m×K	575.08	Calculated Property
λ	0.03	W/m×K	660.07	Calculated Property
λ	0.03	W/m×K	745.05	Calculated Property
λ	0.04	W/m×K	830.03	Calculated Property
λ	0.05	W/m×K	915.02	Calculated Property
λ	0.05	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.10; 0.05]	W/m×K	[235.15; 720.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λ in W/m×K, T in K
Coefficient A			-4.54270e-02
Coefficient B			7.61980e+00
Coefficient C			-1.89820e+00
Coefficient D			-2.60510e-04
Coefficient E			-5.95570e-07
Comment			ChemSep eq 16, LiquidThermalConductivity
Temperature range, min.			235.15
Temperature range, max.			720.00
λ	0.10	W/m×K	235.15	Calculated Property
λ	0.09	W/m×K	289.02	Calculated Property
λ	0.09	W/m×K	342.89	Calculated Property
λ	0.08	W/m×K	396.77	Calculated Property
λ	0.07	W/m×K	450.64	Calculated Property
λ	0.07	W/m×K	504.51	Calculated Property
λ	0.06	W/m×K	558.38	Calculated Property
λ	0.06	W/m×K	612.26	Calculated Property
λ	0.05	W/m×K	666.13	Calculated Property
λ	0.05	W/m×K	720.00	Calculated Property

Similar Compounds

Find more compounds similar to Squalane.

Mixtures

• Squalane + 1-Propanol, 2-methyl-
• Squalane + 2-Propanol
• Squalane + 1-Octanol
• Squalane + Isobutane
• Squalane + Butane
• n-Hexane + Squalane
• Squalane + Octane
• Squalane + Carbon dioxide
• Squalane + Carbon dioxide + Ethanol
• Squalane + Norflurane
• Propane + Squalane
• Squalane + 1-Butanol
• Hydrogen + Squalane
• Hydrogen + Squalane + Carbon dioxide
• Squalane + Ethane

Sources

• Cheméo Relay (1.0)
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Crippen Method
• Densities, Viscosities, and Refractive Indices of Mixtures of Hexane with Cyclohexane, Decane, Hexadecane, and Squalane at 298.15K
• Measurements of the Liquid Viscosities of Mixtures of n-Butane, n-Hexane, and n-Octane with Squalane to 30MPa
• Measurements of the Liquid Viscosities of Mixtures of Isobutane with Squalane to 30 MPa
• 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
• Vapor liquid critical properties of squalane measured by the pulse-heating technique
• 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
• Temperature and pressure dependences of volumetric properties of two poly(propylene glycol) dimethyl ether lubricants
• An experimental setup for isobaric heat capacities for viscous fluids at high pressure: Squalane, bis(2-ethylhexyl) sebacate and bis(2-ethylhexyl) phthalate
• Viscosity measurements for squalane at high pressures to 350 MPa from T = (293.15 to 363.15) K
• On the viscosity of two 1-butyl-1-methylpyrrolidinium ionic liquids: Effect of the temperature and pressure
• The vapor pressure and vaporization enthalpy of squalene and squalane by correlation gas chromatography
• High pressure viscosity behaviour of tris(2-ethylhexyl) trimellitate up to 150 MPa
• Viscous Calibration Liquids for Self-diffusion Measurements
• Diffusion Coefficients of Carbon Dioxide in Eight Hydrocarbon Liquids at Temperatures between (298.15 and 423.15) K at Pressures up to 69 MPa
• Vapor Liquid Equilibrium Measurements for Carbon Dioxide + Cyclohexene + Squalane at High Pressures Using a Synthetic Method
• DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
• Measurements and Modeling of Phase Behavior, Density, and Viscosity of Oil + Carbon Dioxide: Squalane + CO2 at Temperatures (313 to 363) K and Pressures up to 77 MPa
• Fluid Phase Equilibria of Binary n-Alkane + Squalane Systems
• Compressed Liquid Densities of Squalane and Pentaerythritol Tetra(2-ethylhexanoate)
• Solubility Measurements of 1,1,1,2-Tetrafluoroethane (R134a) and of Propane in Squalane at Temperatures from (325 to 400) K and Pressures from (0.1 to 1) MPa
• Measurements of the Viscosity of Bis(2-ethylhexyl) Sebacate, Squalane, and Bis(2-ethylhexyl) Phthalate between (283 and 363) K at 0.1 MPa
• New Experimental Data and Reference Models for the Viscosity and Density of Squalane
• Temperature and Composition Dependence of the Densities, Viscosities, and Speeds of Sound of Binary Liquid Mixtures of 1-Butanol with Hexadecane and Squalane
• Viscosity and Density of Carbon Dioxide + 2,6,10,15,19,23-Hexamethyltetracosane (Squalane)
• Phase Equilibrium of Hydrogen, Carbon Dioxide, Squalene, and Squalane
• Temperature and Pressure Dependence of the Viscosities of 2-Ethylhexyl Benzoate, Bis(2-ethylhexyl) Phthalate, 2,6,10,15,19,23-Hexamethyltetracosane (Squalane), and Diisodecyl Phthalate
• Joback 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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