Chemical Properties of Octadecane (CAS 593-45-3)

InChI

InChI=1S/C18H38/c1-3-5-7-9-11-13-15-17-18-16-14-12-10-8-6-4-2/h3-18H2,1-2H3

InChI Key

RZJRJXONCZWCBN-UHFFFAOYSA-N

Formula

C18H38

SMILES

CCCCCCCCCCCCCCCCCC

Molecular Weight¹

254.50

CAS

593-45-3

Other Names

• Octadecan
• n-octadecane

• ω : Acentric Factor.
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• Δ_cH°_solid : Standard solid 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_p,solid : Solid 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_fH°_solid : Solid 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).
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• 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°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• γ : Surface Tension (N/m).
• S°_{solid,1 bar} : Solid phase molar entropy at standard conditions (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_boil : Boiling point at given pressure (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_fus : 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).
• 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	[0.7900; 0.8080]
ω	0.8080		ChemSep v8.3 pure component data
ω	0.7900		KDB
ΔcH°liquid	-12008.70 ± 2.40	kJ/mol	NIST
ΔcH°solid	-11946.50 ± 4.80	kJ/mol	NIST
μ	0.00	debye	ChemSep v8.3 pure component data
ΔfG°	[99.21; 100.60]	kJ/mol
ΔfG°	99.21	kJ/mol	ChemSep v8.3 pure component data
ΔfG°	100.60	kJ/mol	KDB
ΔfH°gas	[-414.80; -414.57]	kJ/mol
ΔfH°gas	-414.57	kJ/mol	ChemSep v8.3 pure component data
ΔfH°gas	-414.80	kJ/mol	KDB
ΔfH°gas	-414.60 ± 2.70	kJ/mol	NIST
ΔfH°liquid	-505.40 ± 2.70	kJ/mol	NIST
ΔfH°solid	-567.40 ± 4.80	kJ/mol	NIST
ΔfusH°	[59.30; 61.65]	kJ/mol
ΔfusH°	61.65	kJ/mol	Solid-liquid phase equilibria of (n-octadecane with myristic, and palmitic acid) binary mixtures used as phase change materials (PCMs)
ΔfusH°	59.30	kJ/mol	Silver incorporated microencapsulation of n-hexadecane and noctadecane appropriate for dynamic thermal management in textiles
ΔsubH°	152.70	kJ/mol	NIST
ΔvapH°	[90.60; 92.80]	kJ/mol
ΔvapH°	90.60 ± 1.00	kJ/mol	NIST
ΔvapH°	91.30 ± 2.90	kJ/mol	NIST
ΔvapH°	91.40 ± 1.30	kJ/mol	NIST
ΔvapH°	91.80	kJ/mol	NIST
ΔvapH°	91.80	kJ/mol	NIST
ΔvapH°	Outlier 92.80	kJ/mol	NIST
ΔvapH°	91.40	kJ/mol	NIST
ΔvapH°	90.80	kJ/mol	NIST
IE	9.84	eV	Relay (1.0) Calculated Property
log10WS	-8.13		Relay (1.0) Calculated Property
logPoct/wat	7.268		Crippen Calculated Property
McVol	264.480	ml/mol	McGowan Calculated Property
Pc	[1290.00; 1300.00]	kPa
Pc	1290.00	kPa	ChemSep v8.3 pure component data
Pc	1290.00	kPa	KDB
Pc	1300.00 ± 200.00	kPa	NIST
Pc	1292.00 ± 110.00	kPa	NIST
Ptriple	3.39e-05	kPa	ChemSep v8.3 pure component data
ρc	[203.60; 214.03]	kg/m3
ρc	203.60 ± 50.90	kg/m3	NIST
ρc	214.03 ± 5.09	kg/m3	NIST
Inp	[296.84; 301.71]
Inp	296.84		NIST
Inp	301.71		NIST
S°liquid	696.60	J/mol×K	NIST
S°solid,1 bar	480.20	J/mol×K	NIST
Tboil	[581.00; 589.50]	K
Tboil	588.30	K	ChemSep v8.3 pure component data
Tboil	589.50	K	KDB
Tboil	589.30	K	NIST
Tboil	581.00 ± 3.00	K	NIST
Tboil	581.65 ± 2.50	K	NIST
Tboil	585.65 ± 2.00	K	NIST
Tc	[745.80; 756.15]	K
Tc	747.00	K	ChemSep v8.3 pure component data
Tc	747.00	K	KDB
Tc	747.00 ± 3.00	K	NIST
Tc	745.80 ± 3.40	K	NIST
Tc	747.70 ± 1.00	K	NIST
Tc	747.20	K	NIST
Tc	Outlier 756.15 ± 0.01	K	NIST
Tfus	[299.00; 302.90]	K
Tfus	301.60	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	301.46	K	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Tfus	301.55	K	Fabrication, thermal properties and thermal stabilities of microencapsulated n-alkane with poly(lauryl methacrylate) as shell
Tfus	301.15	K	Development of thermal enhanced n-octadecane/porous nano carbon-based materials using 3-step filtered vacuum impregnation method
Tfus	301.33	K	ChemSep v8.3 pure component data
Tfus	301.30	K	KDB
Tfus	301.65 ± 0.20	K	NIST
Tfus	301.00 ± 0.10	K	NIST
Tfus	301.22 ± 0.15	K	NIST
Tfus	300.95 ± 0.50	K	NIST
Tfus	300.70 ± 0.50	K	NIST
Tfus	301.00 ± 3.00	K	NIST
Tfus	300.30 ± 0.50	K	NIST
Tfus	Outlier 299.00 ± 3.00	K	NIST
Tfus	301.40 ± 0.30	K	NIST
Tfus	301.31 ± 0.02	K	NIST
Tfus	301.31 ± 0.02	K	NIST
Tfus	301.33 ± 0.01	K	NIST
Tfus	301.00 ± 2.00	K	NIST
Tfus	301.35 ± 0.15	K	NIST
Tfus	301.23 ± 0.20	K	NIST
Tfus	301.25 ± 0.20	K	NIST
Tfus	301.25 ± 0.20	K	NIST
Tfus	301.15 ± 1.50	K	NIST
Tfus	301.00 ± 0.50	K	NIST
Tfus	301.00 ± 0.50	K	NIST
Tfus	300.85 ± 0.30	K	NIST
Tfus	301.30 ± 0.60	K	NIST
Tfus	300.15 ± 1.50	K	NIST
Tfus	301.20 ± 0.60	K	NIST
Tfus	300.90 ± 0.60	K	NIST
Tfus	301.20 ± 0.30	K	NIST
Tfus	300.30 ± 0.50	K	NIST
Tfus	300.09 ± 0.50	K	NIST
Tfus	Outlier 302.90 ± 1.00	K	NIST
Tfus	300.00 ± 2.00	K	NIST
Tfus	301.01 ± 0.30	K	NIST
Tfus	301.00 ± 1.50	K	NIST
Tfus	301.00 ± 2.00	K	NIST
Tfus	301.00 ± 2.00	K	NIST
Tfus	301.00 ± 2.00	K	NIST
Tfus	301.00 ± 2.00	K	NIST
Tfus	301.00 ± 3.00	K	NIST
Ttriple	[300.50; 301.33]	K
Ttriple	300.50	K	Solubilities of Some Long-Chain n-Alkanes in Dipropyl Ether, Dibutyl Ether, 1-Chlorobutane, and 1-Chlorooctane as Functions of Temperature
Ttriple	301.33	K	ChemSep v8.3 pure component data
Ttriple	301.00 ± 0.04	K	NIST
Ttriple	301.30 ± 0.20	K	NIST
Ttriple	301.00 ± 0.04	K	NIST
Ttriple	301.30 ± 0.20	K	NIST
UQi	10.34		ChemSep v8.3 pure component data
URi	12.59		ChemSep v8.3 pure component data
Vc	[1.189; 1.189]	m3/kmol
Vc	1.189	m3/kmol	ChemSep v8.3 pure component data
Vc	1.189	m3/kmol	KDB
Vc	1.189	m3/kmol	NIST
Zc	[0.2469530; 0.2470000]
Zc	0.2470000		ChemSep v8.3 pure component data
Zc	0.2469530		KDB
Zra	[0.23; 0.25]
Zra	0.25		ChemSep v8.3 pure component data
Zra	0.23		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[564.40; 568.00]	J/mol×K	[300.00; 325.00]
Cp,liquid	564.40	J/mol×K	300.00	NIST
Cp,liquid	568.00	J/mol×K	325.00	NIST
Cp,solid	485.64	J/mol×K	298.15	NIST
η	[0.0028200; 0.0039500]	Pa×s	[299.75; 318.15]
η	0.0039500	Pa×s	299.75	Intercomparative tests on viscosity measurements of phase change materials
η	0.0039200	Pa×s	299.95	Intercomparative tests on viscosity measurements of phase change materials
η	0.0039100	Pa×s	300.15	Intercomparative tests on viscosity measurements of phase change materials
η	0.0038900	Pa×s	300.35	Intercomparative tests on viscosity measurements of phase change materials
η	0.0038600	Pa×s	300.55	Intercomparative tests on viscosity measurements of phase change materials
η	0.0038400	Pa×s	300.75	Intercomparative tests on viscosity measurements of phase change materials
η	0.0038400	Pa×s	300.85	Intercomparative tests on viscosity measurements of phase change materials
η	0.0038200	Pa×s	300.95	Intercomparative tests on viscosity measurements of phase change materials
η	0.0038100	Pa×s	301.15	Intercomparative tests on viscosity measurements of phase change materials
η	0.0038000	Pa×s	301.35	Intercomparative tests on viscosity measurements of phase change materials
η	0.0038000	Pa×s	301.55	Intercomparative tests on viscosity measurements of phase change materials
η	0.0037600	Pa×s	301.75	Intercomparative tests on viscosity measurements of phase change materials
η	0.0037700	Pa×s	301.95	Intercomparative tests on viscosity measurements of phase change materials
η	0.0037600	Pa×s	302.15	Intercomparative tests on viscosity measurements of phase change materials
η	0.0037200	Pa×s	302.35	Intercomparative tests on viscosity measurements of phase change materials
η	0.0037300	Pa×s	302.55	Intercomparative tests on viscosity measurements of phase change materials
η	0.0037100	Pa×s	302.75	Intercomparative tests on viscosity measurements of phase change materials
η	0.0036900	Pa×s	302.95	Intercomparative tests on viscosity measurements of phase change materials
η	0.0036700	Pa×s	303.15	Intercomparative tests on viscosity measurements of phase change materials
η	0.0036700	Pa×s	303.35	Intercomparative tests on viscosity measurements of phase change materials
η	0.0036300	Pa×s	303.55	Intercomparative tests on viscosity measurements of phase change materials
η	0.0036400	Pa×s	303.75	Intercomparative tests on viscosity measurements of phase change materials
η	0.0036500	Pa×s	303.95	Intercomparative tests on viscosity measurements of phase change materials
η	0.0036000	Pa×s	304.15	Intercomparative tests on viscosity measurements of phase change materials
η	0.0035800	Pa×s	304.35	Intercomparative tests on viscosity measurements of phase change materials
η	0.0035700	Pa×s	304.55	Intercomparative tests on viscosity measurements of phase change materials
η	0.0035600	Pa×s	304.75	Intercomparative tests on viscosity measurements of phase change materials
η	0.0035300	Pa×s	304.95	Intercomparative tests on viscosity measurements of phase change materials
η	0.0035500	Pa×s	305.15	Intercomparative tests on viscosity measurements of phase change materials
η	0.0035000	Pa×s	305.35	Intercomparative tests on viscosity measurements of phase change materials
η	0.0035000	Pa×s	305.55	Intercomparative tests on viscosity measurements of phase change materials
η	0.0034800	Pa×s	305.75	Intercomparative tests on viscosity measurements of phase change materials
η	0.0034600	Pa×s	305.95	Intercomparative tests on viscosity measurements of phase change materials
η	0.0034700	Pa×s	306.15	Intercomparative tests on viscosity measurements of phase change materials
η	0.0034700	Pa×s	306.35	Intercomparative tests on viscosity measurements of phase change materials
η	0.0034400	Pa×s	306.55	Intercomparative tests on viscosity measurements of phase change materials
η	0.0034200	Pa×s	306.75	Intercomparative tests on viscosity measurements of phase change materials
η	0.0034300	Pa×s	306.95	Intercomparative tests on viscosity measurements of phase change materials
η	0.0034200	Pa×s	307.15	Intercomparative tests on viscosity measurements of phase change materials
η	0.0034000	Pa×s	307.35	Intercomparative tests on viscosity measurements of phase change materials
η	0.0033900	Pa×s	307.55	Intercomparative tests on viscosity measurements of phase change materials
η	0.0033800	Pa×s	307.75	Intercomparative tests on viscosity measurements of phase change materials
η	0.0033500	Pa×s	307.95	Intercomparative tests on viscosity measurements of phase change materials
η	0.0033400	Pa×s	308.15	Intercomparative tests on viscosity measurements of phase change materials
η	0.0033100	Pa×s	308.35	Intercomparative tests on viscosity measurements of phase change materials
η	0.0032900	Pa×s	308.55	Intercomparative tests on viscosity measurements of phase change materials
η	0.0032900	Pa×s	308.75	Intercomparative tests on viscosity measurements of phase change materials
η	0.0032900	Pa×s	308.95	Intercomparative tests on viscosity measurements of phase change materials
η	0.0032700	Pa×s	309.15	Intercomparative tests on viscosity measurements of phase change materials
η	0.0032600	Pa×s	309.35	Intercomparative tests on viscosity measurements of phase change materials
η	0.0032800	Pa×s	309.55	Intercomparative tests on viscosity measurements of phase change materials
η	0.0032400	Pa×s	309.75	Intercomparative tests on viscosity measurements of phase change materials
η	0.0032200	Pa×s	309.95	Intercomparative tests on viscosity measurements of phase change materials
η	0.0032100	Pa×s	310.15	Intercomparative tests on viscosity measurements of phase change materials
η	0.0032200	Pa×s	310.35	Intercomparative tests on viscosity measurements of phase change materials
η	0.0031800	Pa×s	310.55	Intercomparative tests on viscosity measurements of phase change materials
η	0.0031700	Pa×s	310.75	Intercomparative tests on viscosity measurements of phase change materials
η	0.0031500	Pa×s	310.95	Intercomparative tests on viscosity measurements of phase change materials
η	0.0031400	Pa×s	311.15	Intercomparative tests on viscosity measurements of phase change materials
η	0.0031400	Pa×s	311.35	Intercomparative tests on viscosity measurements of phase change materials
η	0.0031400	Pa×s	311.55	Intercomparative tests on viscosity measurements of phase change materials
η	0.0031200	Pa×s	311.75	Intercomparative tests on viscosity measurements of phase change materials
η	0.0031100	Pa×s	311.95	Intercomparative tests on viscosity measurements of phase change materials
η	0.0031000	Pa×s	312.15	Intercomparative tests on viscosity measurements of phase change materials
η	0.0031000	Pa×s	312.35	Intercomparative tests on viscosity measurements of phase change materials
η	0.0030700	Pa×s	312.55	Intercomparative tests on viscosity measurements of phase change materials
η	0.0030700	Pa×s	312.75	Intercomparative tests on viscosity measurements of phase change materials
η	0.0030700	Pa×s	312.95	Intercomparative tests on viscosity measurements of phase change materials
η	0.0030300	Pa×s	313.15	Intercomparative tests on viscosity measurements of phase change materials
η	0.0030100	Pa×s	313.35	Intercomparative tests on viscosity measurements of phase change materials
η	0.0030100	Pa×s	313.55	Intercomparative tests on viscosity measurements of phase change materials
η	0.0030100	Pa×s	313.75	Intercomparative tests on viscosity measurements of phase change materials
η	0.0030000	Pa×s	313.95	Intercomparative tests on viscosity measurements of phase change materials
η	0.0029900	Pa×s	314.15	Intercomparative tests on viscosity measurements of phase change materials
η	0.0029600	Pa×s	314.35	Intercomparative tests on viscosity measurements of phase change materials
η	0.0029700	Pa×s	314.55	Intercomparative tests on viscosity measurements of phase change materials
η	0.0029700	Pa×s	314.75	Intercomparative tests on viscosity measurements of phase change materials
η	0.0029400	Pa×s	314.95	Intercomparative tests on viscosity measurements of phase change materials
η	0.0029600	Pa×s	315.15	Intercomparative tests on viscosity measurements of phase change materials
η	0.0029100	Pa×s	315.35	Intercomparative tests on viscosity measurements of phase change materials
η	0.0029100	Pa×s	315.55	Intercomparative tests on viscosity measurements of phase change materials
η	0.0029000	Pa×s	315.75	Intercomparative tests on viscosity measurements of phase change materials
η	0.0028900	Pa×s	315.95	Intercomparative tests on viscosity measurements of phase change materials
η	0.0028800	Pa×s	316.15	Intercomparative tests on viscosity measurements of phase change materials
η	0.0028800	Pa×s	316.35	Intercomparative tests on viscosity measurements of phase change materials
η	0.0028800	Pa×s	316.55	Intercomparative tests on viscosity measurements of phase change materials
η	0.0028800	Pa×s	316.75	Intercomparative tests on viscosity measurements of phase change materials
η	0.0028800	Pa×s	316.95	Intercomparative tests on viscosity measurements of phase change materials
η	0.0028600	Pa×s	317.15	Intercomparative tests on viscosity measurements of phase change materials
η	0.0028300	Pa×s	317.35	Intercomparative tests on viscosity measurements of phase change materials
η	0.0028200	Pa×s	317.55	Intercomparative tests on viscosity measurements of phase change materials
η	0.0028400	Pa×s	317.75	Intercomparative tests on viscosity measurements of phase change materials
η	0.0028200	Pa×s	317.95	Intercomparative tests on viscosity measurements of phase change materials
η	0.0028300	Pa×s	318.15	Intercomparative tests on viscosity measurements of phase change materials
ΔfusH	[60.10; 61.71]	kJ/mol	[301.00; 301.50]
ΔfusH	60.76	kJ/mol	301.00	NIST
ΔfusH	60.10	kJ/mol	301.10	NIST
ΔfusH	61.50	kJ/mol	301.30	NIST
ΔfusH	61.50	kJ/mol	301.30	NIST
ΔfusH	60.48	kJ/mol	301.30	NIST
ΔfusH	60.48	kJ/mol	301.30	NIST
ΔfusH	61.71	kJ/mol	301.33	NIST
ΔfusH	61.71	kJ/mol	301.33	NIST
ΔfusH	61.50	kJ/mol	301.50	NIST
ΔsubH	[153.00; 153.10]	kJ/mol	[288.00; 293.00]
ΔsubH	153.10 ± 5.00	kJ/mol	288.00	NIST
ΔsubH	153.00 ± 5.00	kJ/mol	293.00	NIST
ΔsubH	153.00 ± 5.00	kJ/mol	293.00	NIST
ΔvapH	[54.48; 84.30]	kJ/mol	[339.50; 589.50]
ΔvapH	84.30	kJ/mol	339.50	NIST
ΔvapH	72.50	kJ/mol	343.00	NIST
ΔvapH	71.80	kJ/mol	353.00	NIST
ΔvapH	71.10	kJ/mol	363.00	NIST
ΔvapH	70.50	kJ/mol	373.00	NIST
ΔvapH	69.80	kJ/mol	383.00	NIST
ΔvapH	80.00	kJ/mol	387.00	NIST
ΔvapH	78.10	kJ/mol	460.50	NIST
ΔvapH	74.40	kJ/mol	500.50	NIST
ΔvapH	69.40	kJ/mol	518.50	NIST
ΔvapH	64.80	kJ/mol	524.50	NIST
ΔvapH	54.48	kJ/mol	589.50	KDB
ρl	[695.00; 777.00]	kg/m3	[301.00; 422.60]
ρl	777.00	kg/m3	301.00	KDB
ρl	755.00	kg/m3	323.10	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ρl	756.00	kg/m3	323.10	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ρl	757.00	kg/m3	323.10	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ρl	758.00	kg/m3	323.10	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ρl	756.00	kg/m3	323.30	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ρl	757.00	kg/m3	323.30	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ρl	733.00	kg/m3	372.80	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ρl	730.00	kg/m3	372.80	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ρl	733.00	kg/m3	372.80	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ρl	731.00	kg/m3	372.80	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ρl	734.00	kg/m3	372.80	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ρl	735.00	kg/m3	372.80	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ρl	736.00	kg/m3	372.80	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ρl	731.00	kg/m3	372.80	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ρl	703.00	kg/m3	422.50	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ρl	704.00	kg/m3	422.50	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ρl	695.00	kg/m3	422.60	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ρl	697.00	kg/m3	422.60	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ρl	699.00	kg/m3	422.60	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ρl	700.00	kg/m3	422.60	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ρl	701.00	kg/m3	422.60	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ρl	702.00	kg/m3	422.60	Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
ΔfusS	[200.70; 204.60]	J/mol×K	[301.00; 301.33]
ΔfusS	201.90	J/mol×K	301.00	NIST
ΔfusS	200.70	J/mol×K	301.30	NIST
ΔfusS	200.70	J/mol×K	301.30	NIST
ΔfusS	204.60	J/mol×K	301.33	NIST
ΔfusS	204.60	J/mol×K	301.33	NIST
vspec	[0.00; 0.00]	m3/kg	[299.25; 568.25]
vspec	0.00	m3/kg	299.25	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	301.35	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	303.35	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	305.45	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	307.55	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	309.55	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	311.65	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	313.65	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	315.75	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	317.75	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	318.65	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	319.85	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	320.65	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	323.55	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	325.45	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	328.35	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	330.35	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	333.25	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	335.15	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	338.05	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	341.05	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	342.95	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	345.85	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	347.85	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	350.75	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	352.65	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	355.55	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	357.55	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	360.45	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	362.35	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	365.25	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	367.25	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	370.15	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	372.05	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	374.95	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	376.95	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	379.85	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	381.75	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	384.75	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	386.65	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	389.55	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	391.55	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	394.45	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	396.35	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	399.25	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	401.25	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	404.15	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	406.05	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	408.95	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	410.95	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	413.85	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	415.75	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	418.65	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	420.65	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	423.55	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	425.45	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	428.45	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	430.35	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	433.25	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	435.25	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	438.15	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	440.05	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	442.95	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	444.95	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	447.85	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	449.75	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	452.65	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	454.65	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	457.55	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	459.45	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	462.45	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	464.35	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	467.25	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	469.15	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	472.15	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	474.05	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	476.95	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	478.95	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	481.85	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	483.75	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	486.65	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	488.65	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	491.55	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	493.45	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	496.35	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	498.35	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	500.25	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	503.15	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	505.15	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	508.05	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	510.95	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	512.95	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	515.85	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	518.75	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	520.65	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	523.55	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	525.55	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	527.45	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	530.35	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	533.25	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	535.25	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	538.15	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	541.05	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	543.05	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	545.95	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	548.85	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	550.75	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	553.65	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	555.65	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	558.55	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	560.45	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	563.45	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	566.35	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	568.25	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	469.96	K	3.47	Improving a variation of the DSC technique for measuring the boiling points of pure compounds at low pressures
Tfus	[303.15; 353.15]	K	[8860.00; 258230.00]
Tfus	303.15	K	8860.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus	303.15	K	8860.00	Influence of size and shape effects on the high-pressure solubility of n-alkanes: Experimental data, correlation and prediction
Tfus	313.15	K	49600.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus	313.15	K	49600.00	Influence of size and shape effects on the high-pressure solubility of n-alkanes: Experimental data, correlation and prediction
Tfus	323.15	K	94900.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus	323.15	K	94900.00	Influence of size and shape effects on the high-pressure solubility of n-alkanes: Experimental data, correlation and prediction
Tfus	333.15	K	144780.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus	333.15	K	144780.00	Influence of size and shape effects on the high-pressure solubility of n-alkanes: Experimental data, correlation and prediction
Tfus	343.15	K	199220.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus	343.15	K	199220.00	Influence of size and shape effects on the high-pressure solubility of n-alkanes: Experimental data, correlation and prediction
Tfus	353.15	K	258230.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus	353.15	K	258230.00	Influence of size and shape effects on the high-pressure solubility of n-alkanes: Experimental data, correlation and prediction

Datasets

1. Viscosity, Pa*s (1)
2. Mass density, kg/m3 (2)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
325.60	9800.00	0.0026
325.60	16400.00	0.0028
325.60	29600.00	0.0032
325.60	37200.00	0.0036
325.60	51000.00	0.0042
325.60	60500.00	0.0046
325.60	69000.00	0.0050
325.60	70800.00	0.0051
428.90	6800.00	0.0007
428.90	21900.00	0.0008
428.90	42100.00	0.0010
428.90	63400.00	0.0012
428.90	84300.00	0.0014
428.90	104900.00	0.0016
428.90	125500.00	0.0019
428.90	147800.00	0.0021
428.90	168000.00	0.0024
428.90	188600.00	0.0027
428.90	209600.00	0.0029
428.90	230000.00	0.0032
428.90	243100.00	0.0034
533.90	9200.00	0.0003
533.90	9500.00	0.0003
533.90	15200.00	0.0003
533.90	22500.00	0.0004
533.90	44600.00	0.0005
533.90	64000.00	0.0006
533.90	85700.00	0.0007
533.90	105900.00	0.0008
533.90	126600.00	0.0009
533.90	147600.00	0.0010
533.90	147600.00	0.0010
533.90	167700.00	0.0011
533.90	188600.00	0.0012
533.90	209100.00	0.0013
533.90	229300.00	0.0014
533.90	242900.00	0.0015
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
323.65	7000.00	764.0
323.65	14400.00	769.0
323.65	28300.00	778.0
323.65	42200.00	788.0
323.65	55600.00	797.0
323.65	68900.00	800.0
422.85	7700.00	702.0
422.85	15100.00	711.0
422.85	29400.00	724.0
422.85	42500.00	732.0
422.85	56100.00	741.0
422.85	73200.00	752.0
422.85	84500.00	761.0
422.85	110000.00	774.0
422.85	138500.00	787.0
422.85	171700.00	801.0
422.85	206100.00	813.0
422.85	235500.00	823.0
422.85	255900.00	829.0
522.55	15300.00	651.0
522.55	29400.00	668.0
522.55	43200.00	681.0
522.55	56400.00	692.0
522.55	70800.00	703.0
522.55	84400.00	712.0
522.55	110000.00	727.0
522.55	137800.00	742.0
522.55	170400.00	757.0
522.55	205300.00	771.0
522.55	235700.00	782.0
522.55	257000.00	790.0
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
323.00	8090.00	766.0
323.00	9490.00	767.0
323.10	2080.00	763.0
323.10	3570.00	764.0
323.10	5060.00	765.0
323.10	6500.00	766.0
347.90	2090.00	745.0
347.90	3520.00	746.0
347.90	5050.00	747.0
347.90	6530.00	749.0
347.90	8050.00	750.0
347.90	9470.00	751.0
397.20	3470.00	715.0
398.20	2030.00	713.0
398.20	4970.00	716.0
398.20	6480.00	718.0
398.20	9590.00	721.0
398.30	7940.00	719.0
447.50	7920.00	690.0
447.50	9510.00	692.0
447.60	1920.00	681.0
447.60	4900.00	686.0
447.60	6460.00	687.0
447.70	3450.00	684.0
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[314.00; 1103.28]	J/mol×K	[200.00; 1500.00]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			2.58960e+02
Coefficient B			-6.41430e+02
Coefficient C			7.22824e+00
Coefficient D			-6.86020e-05
Coefficient E			1.81400e-08
Comment			ChemSep eq 16, IdealGasHeatCapacityCp
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	314.00	J/mol×K	200.00	Calculated Property
Cp,gas	468.42	J/mol×K	344.44	Calculated Property
Cp,gas	619.29	J/mol×K	488.89	Calculated Property
Cp,gas	741.61	J/mol×K	633.33	Calculated Property
Cp,gas	837.88	J/mol×K	777.78	Calculated Property
Cp,gas	914.12	J/mol×K	922.22	Calculated Property
Cp,gas	975.45	J/mol×K	1066.67	Calculated Property
Cp,gas	1025.70	J/mol×K	1211.11	Calculated Property
Cp,gas	1067.64	J/mol×K	1355.56	Calculated Property
Cp,gas	1103.28	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[563.49; 821.78]	J/mol×K	[300.00; 589.86]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			3.32820e+02
Coefficient B			-1.51760e+01
Coefficient C			4.46124e+00
Coefficient D			3.90660e-03
Coefficient E			-1.57380e-06
Comment			ChemSep eq 16, LiquidHeatCapacityCp
Temperature range, min.			300.00
Temperature range, max.			589.86
Cp,liquid	563.49	J/mol×K	300.00	Calculated Property
Cp,liquid	587.42	J/mol×K	332.21	Calculated Property
Cp,liquid	612.66	J/mol×K	364.41	Calculated Property
Cp,liquid	639.21	J/mol×K	396.62	Calculated Property
Cp,liquid	667.01	J/mol×K	428.83	Calculated Property
Cp,liquid	696.00	J/mol×K	461.03	Calculated Property
Cp,liquid	726.09	J/mol×K	493.24	Calculated Property
Cp,liquid	757.17	J/mol×K	525.45	Calculated Property
Cp,liquid	789.12	J/mol×K	557.65	Calculated Property
Cp,liquid	821.78	J/mol×K	589.86	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0040388; 0.0001712]	Pa×s	[301.15; 613.15]	ChemSep v8.3 pure component data
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-8.39560e+01
Coefficient B			4.97870e+03
Coefficient C			1.09900e+01
Coefficient D			-8.98340e-06
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, LiquidViscosity
Temperature range, min.			301.15
Temperature range, max.			613.15
η	0.0040388	Pa×s	301.15	Calculated Property
η	0.0019905	Pa×s	335.82	Calculated Property
η	0.0011745	Pa×s	370.48	Calculated Property
η	0.0007807	Pa×s	405.15	Calculated Property
η	0.0005616	Pa×s	439.82	Calculated Property
η	0.0004253	Pa×s	474.48	Calculated Property
η	0.0003326	Pa×s	509.15	Calculated Property
η	0.0002650	Pa×s	543.82	Calculated Property
η	0.0002129	Pa×s	578.48	Calculated Property
η	0.0001712	Pa×s	613.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[89.30; 25.10]	kJ/mol	[298.15; 723.54]	ChemSep v8.3 pure component data
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			1.21400e+02
Coefficient B			3.63330e-01
Coefficient C			1.28300e+00
Coefficient D			-2.05140e+00
Coefficient E			8.51750e-01
Critical temperature, Tc (K)			7.47000e+02
Comment			ChemSep eq 106, HeatOfVaporization
Temperature range, min.			298.15
Temperature range, max.			723.54
ΔvapH	89.30	kJ/mol	298.15	Calculated Property
ΔvapH	83.54	kJ/mol	345.42	Calculated Property
ΔvapH	77.91	kJ/mol	392.68	Calculated Property
ΔvapH	72.40	kJ/mol	439.95	Calculated Property
ΔvapH	66.93	kJ/mol	487.21	Calculated Property
ΔvapH	61.34	kJ/mol	534.48	Calculated Property
ΔvapH	55.35	kJ/mol	581.74	Calculated Property
ΔvapH	48.46	kJ/mol	629.01	Calculated Property
ΔvapH	39.57	kJ/mol	676.27	Calculated Property
ΔvapH	25.10	kJ/mol	723.54	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[447.10; 623.80]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.50497e+01
Coefficient B			-5.05624e+03
Coefficient C			-1.04586e+02
Temperature range, min.			447.10
Temperature range, max.			623.80
Pvap	1.33	kPa	447.10	Calculated Property
Pvap	2.97	kPa	466.73	Calculated Property
Pvap	6.09	kPa	486.37	Calculated Property
Pvap	11.63	kPa	506.00	Calculated Property
Pvap	20.93	kPa	525.63	Calculated Property
Pvap	35.73	kPa	545.27	Calculated Property
Pvap	58.29	kPa	564.90	Calculated Property
Pvap	91.35	kPa	584.53	Calculated Property
Pvap	138.21	kPa	604.17	Calculated Property
Pvap	202.65	kPa	623.80	Calculated Property
Pvap	[3.26e-05; 1264.10]	kPa	[301.31; 750.15]	ChemSep v8.3 pure component data
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			1.49565e+02
Coefficient B			-1.61203e+04
Coefficient C			-1.87250e+01
Coefficient D			5.38655e-06
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			301.31
Temperature range, max.			750.15
Pvap	3.26e-05	kPa	301.31	Calculated Property
Pvap	4.40e-03	kPa	351.18	Calculated Property
Pvap	0.13	kPa	401.05	Calculated Property
Pvap	1.61	kPa	450.92	Calculated Property
Pvap	10.26	kPa	500.79	Calculated Property
Pvap	42.45	kPa	550.67	Calculated Property
Pvap	129.70	kPa	600.54	Calculated Property
Pvap	319.17	kPa	650.41	Calculated Property
Pvap	672.00	kPa	700.28	Calculated Property
Pvap	1264.10	kPa	750.15	Calculated Property
Pvap	[3.23e-05; 1171.38]	kPa	[301.33; 745.26]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			1.68024e+02
Coefficient B			-1.69988e+04
Coefficient C			-2.14756e+01
Coefficient D			6.99410e-06
Coefficient E			0.00000e+00
Temperature range, min.			301.33
Temperature range, max.			745.26
Pvap	3.23e-05	kPa	301.33	Calculated Property
Pvap	4.36e-03	kPa	350.66	Calculated Property
Pvap	0.13	kPa	399.98	Calculated Property
Pvap	1.55	kPa	449.31	Calculated Property
Pvap	9.67	kPa	498.63	Calculated Property
Pvap	39.37	kPa	547.96	Calculated Property
Pvap	118.98	kPa	597.28	Calculated Property
Pvap	291.49	kPa	646.61	Calculated Property
Pvap	615.67	kPa	695.93	Calculated Property
Pvap	1171.38	kPa	745.26	Calculated Property
Pvap	[1.48; 101.01]	kPa	[447.70; 590.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.45802e+01
Coefficient B			-4.76396e+03
Coefficient C			-1.11927e+02
Reference			Krafft, 1882
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			447.70
Temperature range, max.			590.00
Pvap	1.48	kPa	447.70	Calculated Property
Pvap	2.80	kPa	463.51	Calculated Property
Pvap	5.02	kPa	479.32	Calculated Property
Pvap	8.57	kPa	495.13	Calculated Property
Pvap	14.03	kPa	510.94	Calculated Property
Pvap	22.11	kPa	526.76	Calculated Property
Pvap	33.71	kPa	542.57	Calculated Property
Pvap	49.87	kPa	558.38	Calculated Property
Pvap	71.84	kPa	574.19	Calculated Property
Pvap	101.01	kPa	590.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[791.56; 238.73]	kg/m3	[273.15; 748.15]	ChemSep v8.3 pure component data
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			5.36958e+01
Coefficient B			2.39010e-01
Coefficient C			7.48160e+02
Coefficient D			2.81530e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			273.15
Temperature range, max.			748.15
ρl	791.56	kg/m3	273.15	Calculated Property
ρl	759.71	kg/m3	325.93	Calculated Property
ρl	726.31	kg/m3	378.71	Calculated Property
ρl	691.01	kg/m3	431.48	Calculated Property
ρl	653.23	kg/m3	484.26	Calculated Property
ρl	612.13	kg/m3	537.04	Calculated Property
ρl	566.21	kg/m3	589.82	Calculated Property
ρl	512.48	kg/m3	642.59	Calculated Property
ρl	442.78	kg/m3	695.37	Calculated Property
ρl	238.73	kg/m3	748.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 3.03e-04]	N/m	[293.15; 723.54]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-5.65680e-03
Coefficient B			5.09500e+01
Coefficient C			-3.34610e+00
Coefficient D			5.47210e-04
Coefficient E			-4.28450e-06
Comment			ChemSep eq 16, SurfaceTension
Temperature range, min.			293.15
Temperature range, max.			723.54
γ	0.03	N/m	293.15	Calculated Property
γ	0.02	N/m	340.97	Calculated Property
γ	0.02	N/m	388.79	Calculated Property
γ	0.02	N/m	436.61	Calculated Property
γ	0.01	N/m	484.43	Calculated Property
γ	0.01	N/m	532.26	Calculated Property
γ	0.01	N/m	580.08	Calculated Property
γ	0.00	N/m	627.90	Calculated Property
γ	0.00	N/m	675.72	Calculated Property
γ	3.03e-04	N/m	723.54	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.01; 0.07]	W/m×K	[301.33; 1000.00]	ChemSep v8.3 pure component data
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K
Coefficient A			-1.98990e+02
Coefficient B			1.10110e+00
Coefficient C			-5.96850e+09
Coefficient D			5.24190e+11
Comment			ChemSep eq 102, VaporThermalConductivity
Temperature range, min.			301.33
Temperature range, max.			1000.00
λ	0.01	W/m×K	301.33	Calculated Property
λ	0.01	W/m×K	378.96	Calculated Property
λ	0.02	W/m×K	456.59	Calculated Property
λ	0.02	W/m×K	534.22	Calculated Property
λ	0.03	W/m×K	611.85	Calculated Property
λ	0.04	W/m×K	689.48	Calculated Property
λ	0.04	W/m×K	767.11	Calculated Property
λ	0.05	W/m×K	844.74	Calculated Property
λ	0.06	W/m×K	922.37	Calculated Property
λ	0.07	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.15; 0.08]	W/m×K	[301.15; 589.86]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λ in W/m×K, T in K
Coefficient A			-4.66270e-02
Coefficient B			-1.30560e+02
Coefficient C			-6.48420e-01
Coefficient D			-1.71820e-03
Coefficient E			-4.69950e-07
Comment			ChemSep eq 16, LiquidThermalConductivity
Temperature range, min.			301.15
Temperature range, max.			589.86
λ	0.15	W/m×K	301.15	Calculated Property
λ	0.14	W/m×K	333.23	Calculated Property
λ	0.14	W/m×K	365.31	Calculated Property
λ	0.13	W/m×K	397.39	Calculated Property
λ	0.12	W/m×K	429.47	Calculated Property
λ	0.11	W/m×K	461.54	Calculated Property
λ	0.11	W/m×K	493.62	Calculated Property
λ	0.10	W/m×K	525.70	Calculated Property
λ	0.09	W/m×K	557.78	Calculated Property
λ	0.08	W/m×K	589.86	Calculated Property

Similar Compounds

Find more compounds similar to Octadecane.

Mixtures

• Pentane, 3-methyl- + Octadecane
• Butane, 2,2-dimethyl- + Octadecane
• Benzene + Octadecane
• Methane + Octadecane
• Benzonitrile + Octadecane
• Hydrogen + Octadecane
• Hexadecane + Octadecane
• Undecane + Octadecane
• Tetradecanoic acid + Octadecane
• n-Hexadecanoic acid + Octadecane
• n-Hexane + Octadecane
• Decane + Octadecane
• Carbon dioxide + Decane + Octadecane
• Carbon dioxide + Octadecane
• Ethane + Octadecane
• Methane + Decane + Octadecane
• Tetradecane + Octadecane
• Tetradecane + Cyclohexane + Octadecane
• Di-n-propyl ether + Octadecane
• n-Butyl ether + Octadecane

Find more mixtures with Octadecane.

Sources

• KDB Vapor Pressure Data
• 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
• High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
• 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
• Measurement and equation of state prediction of vapor-liquid equilibrium and physical properties for the system methane + n-octadecane
• Experimental results and thermodynamic investigation of carbon dioxide solubility in heavy liquid hydrocarbons and corresponding phase properties
• 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
• Influence of size and shape effects on the high-pressure solubility of n-alkanes: Experimental data, correlation and prediction
• Universal critical amplitude ratios in binary mixtures of {benzonitrile + alkane}
• Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
• Viscosity of n-hexadecane, n-octadecane and n-eicosane at pressures up to 243 MPa and temperatures up to 534 K
• Improving a variation of the DSC technique for measuring the boiling points of pure compounds at low pressures
• Solid-liquid phase equilibria of (n-octadecane with myristic, and palmitic acid) binary mixtures used as phase change materials (PCMs)
• 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
• Silver incorporated microencapsulation of n-hexadecane and noctadecane appropriate for dynamic thermal management in textiles
• Fabrication, thermal properties and thermal stabilities of microencapsulated n-alkane with poly(lauryl methacrylate) as shell
• Development of thermal enhanced n-octadecane/porous nano carbon-based materials using 3-step filtered vacuum impregnation method
• Intercomparative tests on viscosity measurements of phase change materials
• Excess Molar Volumes for Three and Four Component Mixtures Simulating the Binary Mixture (Cyclohexane+ Hexadecane)
• Interfacial Tension Measurement and Calculation of (Carbon Dioxide + n-Alkane) Binary Mixtures
• Solubilities of Some Long-Chain n-Alkanes in Dipropyl Ether, Dibutyl Ether, 1-Chlorobutane, and 1-Chlorooctane as Functions of Temperature
• Experimental Measurement and Equation of State Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n- Octadecane) Binary Systems
• Solubility Measurements and Saturated Liquid Properties of Ternary Systems (Methane + Decane + Octadecane) at 295 K
• Equilibrium Properties of (Carbon Dioxide + n-Decane + n-Octadecane) Systems: Experiments and Thermodynamic Modeling
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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