Chemical Properties of Nonadecane (CAS 629-92-5)

InChI

InChI=1S/C19H40/c1-3-5-7-9-11-13-15-17-19-18-16-14-12-10-8-6-4-2/h3-19H2,1-2H3

InChI Key

LQERIDTXQFOHKA-UHFFFAOYSA-N

Formula

C19H40

SMILES

CCCCCCCCCCCCCCCCCCC

Molecular Weight¹

268.52

CAS

629-92-5

Other Names

• n-nonadecane

• 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_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_l : Liquid Density (kg/m³).
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• v_spec : Specific Volume (m³/kg).
• V_COSTALD : COSTALD Characteristic Volume (m³/kmol).
• ω_SRK : SRK acentric factor.
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.8270; 0.8486]
ω	0.8486		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.8271		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.8271		ChemSep v8.3 pure component data Compiled value
ω	0.8270		KDB
ΔcH°liquid	-12662.60 ± 2.60	kJ/mol	NIST
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	[107.50; 109.00]	kJ/mol
ΔfG°	107.50	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	109.00	kJ/mol	KDB
ΔfH°gas	[-435.40; -435.10]	kJ/mol
ΔfH°gas	-435.14	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-435.40	kJ/mol	KDB
ΔfH°gas	-435.10 ± 2.90	kJ/mol	NIST
ΔfH°liquid	-530.90 ± 2.90	kJ/mol	NIST
ΔfusH°	44.97	kJ/mol	Joback Calculated Property
ΔsubH°	143.60	kJ/mol	NIST
ΔvapH°	[95.80; 96.40]	kJ/mol
ΔvapH°	96.40	kJ/mol	NIST
ΔvapH°	95.80	kJ/mol	NIST
IE	9.86	eV	Relay (1.0) Calculated Property
log10WS	-8.40		Relay (1.0) Calculated Property
logPoct/wat	7.658		Crippen Calculated Property
McVol	278.570	ml/mol	McGowan Calculated Property
Pc	[1116.95; 1230.00]	kPa
Pc	1160.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Pc	1160.00	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	1116.95	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	1230.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	1160.00	kPa	KDB
Pc	1200.00 ± 200.00	kPa	NIST
Pc	1160.00 ± 40.00	kPa	NIST
Ptriple	1.59e-05	kPa	ChemSep v8.3 pure component data Compiled value
Tboil	[601.70; 603.75]	K
Tboil	603.75	K	ChemSep v8.3 pure component data Compiled value
Tboil	603.00	K	KDB
Tboil	602.90	K	NIST
Tboil	601.70 ± 1.50	K	NIST
Tc	[755.00; 760.00]	K
Tc	757.00	K	Critical temperatures and pressures of C40, C44, and C60 normal alkanes measured by the pulse-heating technique
Tc	755.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Tc	756.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	755.93	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	Outlier 760.00	K	ChemSep v8.3 pure component data Compiled value
Tc	755.00	K	KDB
Tc	755.00 ± 8.00	K	NIST
Tc	755.30 ± 3.00	K	NIST
Tfus	[300.30; 305.80]	K
Tfus	305.70	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	305.05	K	ChemSep v8.3 pure component data Compiled value
Tfus	305.20	K	KDB
Tfus	304.35 ± 0.50	K	NIST
Tfus	304.00 ± 0.10	K	NIST
Tfus	303.95 ± 0.10	K	NIST
Tfus	305.20 ± 0.30	K	NIST
Tfus	305.80 ± 0.50	K	NIST
Tfus	304.90 ± 0.20	K	NIST
Tfus	304.60 ± 0.50	K	NIST
Tfus	Outlier 300.30 ± 3.00	K	NIST
Tfus	305.00 ± 4.00	K	NIST
Tfus	305.00 ± 3.00	K	NIST
Ttriple	[295.50; 305.04]	K
Ttriple	295.50	K	Solubilities of Some Long-Chain n-Alkanes in Dipropyl Ether, Dibutyl Ether, 1-Chlorobutane, and 1-Chlorooctane as Functions of Temperature
Ttriple	305.04	K	ChemSep v8.3 pure component data Compiled value
UQi	10.88		ChemSep v8.3 pure component data Compiled value
URi	13.27		ChemSep v8.3 pure component data Compiled value
Vc	[1.087; 1.130]	m3/kmol
Vc	1.087	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	1.100	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	1.130	m3/kmol	KDB
VCOSTALD	1.27	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.83		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2088110; 0.2150000]
Zc	0.2150000		ChemSep v8.3 pure component data Compiled value
Zc	0.2088110		KDB
Zra	[0.22; 0.23]
Zra	0.22		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.23		ChemSep v8.3 pure component data Compiled value
Zra	0.22		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[602.60; 640.00]	J/mol×K	[313.15; 353.00]
Cp,liquid	602.60	J/mol×K	313.15	NIST
Cp,liquid	640.00	J/mol×K	353.00	NIST
ΔfusH	[13.67; 47.40]	kJ/mol	[296.00; 305.30]
ΔfusH	13.67	kJ/mol	296.00	NIST
ΔfusH	47.40	kJ/mol	304.00	NIST
ΔfusH	42.70	kJ/mol	304.40	NIST
ΔfusH	47.40	kJ/mol	305.30	NIST
ΔsubH	136.60	kJ/mol	295.50	NIST
ΔvapH	[56.02; 76.20]	kJ/mol	[505.50; 603.20]
ΔvapH	76.20	kJ/mol	505.50	NIST
ΔvapH	73.00	kJ/mol	531.00	NIST
ΔvapH	56.02	kJ/mol	603.20	KDB
ρl	789.00	kg/m3	305.00	KDB
ΔfusS	[46.20; 155.90]	J/mol×K	[296.00; 304.00]
ΔfusS	46.20	J/mol×K	296.00	NIST
ΔfusS	155.90	J/mol×K	304.00	NIST
γ	0.03	N/m	323.20	KDB
vspec	[0.00; 0.00]	m3/kg	[305.45; 576.05]
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	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	321.95	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	323.95	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	326.05	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	328.05	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	330.15	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	332.25	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	334.25	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	336.35	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	338.35	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	340.45	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	342.55	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	344.55	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	346.65	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	348.65	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	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	352.85	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	354.85	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	356.95	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	358.95	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	361.05	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	363.15	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	365.15	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	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	369.25	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	371.35	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	373.45	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	375.45	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	377.55	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	379.55	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	381.65	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	383.75	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	385.75	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	387.85	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	389.85	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	391.95	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	393.95	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	396.05	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	398.15	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	400.15	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	402.25	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	404.25	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	406.35	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	408.45	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	410.45	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	412.55	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	414.55	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	416.65	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	418.75	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	420.75	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	422.85	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	424.85	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	426.95	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	429.05	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	431.05	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	433.15	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	435.15	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	437.25	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	439.35	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	441.35	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	443.45	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	445.45	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	447.55	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	449.65	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	451.65	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	453.75	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	455.75	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	457.85	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	459.95	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	461.95	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	464.05	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	466.05	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	468.15	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	470.25	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	472.25	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	474.35	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	476.35	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	478.45	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	480.45	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	482.55	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	484.65	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	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	488.75	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	490.75	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	492.85	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	494.95	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	496.95	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	499.05	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	501.05	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	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	505.25	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	507.25	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	509.35	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	511.35	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	513.45	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	515.55	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	517.55	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	519.65	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	521.65	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	523.75	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	525.85	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	531.35	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	537.15	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	539.15	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	544.95	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	546.85	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	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	552.75	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	554.65	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	556.65	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	562.45	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	564.35	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	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
vspec	0.00	m3/kg	570.25	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	572.15	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	574.05	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	576.05	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

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[331.90; 1163.55]	J/mol×K	[200.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			2.74480e+02
Coefficient B			-6.48390e+02
Coefficient C			7.31324e+00
Coefficient D			-1.10950e-04
Coefficient E			3.36070e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	331.90	J/mol×K	200.00	Calculated Property
Cp,gas	495.13	J/mol×K	344.44	Calculated Property
Cp,gas	654.71	J/mol×K	488.89	Calculated Property
Cp,gas	783.60	J/mol×K	633.33	Calculated Property
Cp,gas	884.59	J/mol×K	777.78	Calculated Property
Cp,gas	964.30	J/mol×K	922.22	Calculated Property
Cp,gas	1028.39	J/mol×K	1066.67	Calculated Property
Cp,gas	1081.06	J/mol×K	1211.11	Calculated Property
Cp,gas	1125.37	J/mol×K	1355.56	Calculated Property
Cp,gas	1163.55	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[589.54; 866.90]	J/mol×K	[305.00; 603.05]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			2.44790e+02
Coefficient B			4.25400e+01
Coefficient C			4.53824e+00
Coefficient D			4.63340e-03
Coefficient E			-2.66680e-06
Temperature range, min.			305.00
Temperature range, max.			603.05
Cp,liquid	589.54	J/mol×K	305.00	Calculated Property
Cp,liquid	619.37	J/mol×K	338.12	Calculated Property
Cp,liquid	650.40	J/mol×K	371.23	Calculated Property
Cp,liquid	682.23	J/mol×K	404.35	Calculated Property
Cp,liquid	714.48	J/mol×K	437.47	Calculated Property
Cp,liquid	746.73	J/mol×K	470.58	Calculated Property
Cp,liquid	778.55	J/mol×K	503.70	Calculated Property
Cp,liquid	809.48	J/mol×K	536.82	Calculated Property
Cp,liquid	839.08	J/mol×K	569.93	Calculated Property
Cp,liquid	866.90	J/mol×K	603.05	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0044672; 0.0000693]	Pa×s	[303.15; 760.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-8.47610e+01
Coefficient B			5.10100e+03
Coefficient C			1.10820e+01
Coefficient D			-8.72390e-06
Coefficient E			2.00000e+00
Temperature range, min.			303.15
Temperature range, max.			760.00
η	0.0044672	Pa×s	303.15	Calculated Property
η	0.0016620	Pa×s	353.91	Calculated Property
η	0.0008603	Pa×s	404.67	Calculated Property
η	0.0005343	Pa×s	455.43	Calculated Property
η	0.0003662	Pa×s	506.19	Calculated Property
η	0.0002632	Pa×s	556.96	Calculated Property
η	0.0001922	Pa×s	607.72	Calculated Property
η	0.0001398	Pa×s	658.48	Calculated Property
η	0.0000998	Pa×s	709.24	Calculated Property
η	0.0000693	Pa×s	760.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[94.95; 6.95]	kJ/mol	[298.15; 758.00]	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			1.54040e+02
Coefficient B			1.22150e+00
Coefficient C			-3.28990e-01
Coefficient D			-1.05410e+00
Coefficient E			6.82100e-01
Critical temperature, Tc (K)			7.60000e+02
Temperature range, min.			298.15
Temperature range, max.			758.00
ΔvapH	94.95	kJ/mol	298.15	Calculated Property
ΔvapH	87.78	kJ/mol	349.24	Calculated Property
ΔvapH	81.23	kJ/mol	400.34	Calculated Property
ΔvapH	75.09	kJ/mol	451.43	Calculated Property
ΔvapH	69.13	kJ/mol	502.53	Calculated Property
ΔvapH	62.97	kJ/mol	553.62	Calculated Property
ΔvapH	56.11	kJ/mol	604.72	Calculated Property
ΔvapH	47.60	kJ/mol	655.81	Calculated Property
ΔvapH	35.41	kJ/mol	706.91	Calculated Property
ΔvapH	6.95	kJ/mol	758.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[455.49; 639.03]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.47703e+01
Coefficient B			-5.00471e+03
Coefficient C			-1.09923e+02
Temperature range, min.			455.49
Temperature range, max.			639.03
Pvap	1.33	kPa	455.49	Calculated Property
Pvap	2.99	kPa	475.88	Calculated Property
Pvap	6.15	kPa	496.28	Calculated Property
Pvap	11.78	kPa	516.67	Calculated Property
Pvap	21.19	kPa	537.06	Calculated Property
Pvap	36.14	kPa	557.46	Calculated Property
Pvap	58.84	kPa	577.85	Calculated Property
Pvap	91.97	kPa	598.24	Calculated Property
Pvap	138.71	kPa	618.64	Calculated Property
Pvap	202.66	kPa	639.03	Calculated Property
Pvap	[1.74e-05; 1206.90]	kPa	[305.04; 760.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			1.75493e+02
Coefficient B			-1.78436e+04
Coefficient C			-2.24873e+01
Coefficient D			7.34961e-06
Coefficient E			2.00000e+00
Temperature range, min.			305.04
Temperature range, max.			760.15
Pvap	1.74e-05	kPa	305.04	Calculated Property
Pvap	2.90e-03	kPa	355.61	Calculated Property
Pvap	0.10	kPa	406.18	Calculated Property
Pvap	1.28	kPa	456.74	Calculated Property
Pvap	8.46	kPa	507.31	Calculated Property
Pvap	35.96	kPa	557.88	Calculated Property
Pvap	112.50	kPa	608.45	Calculated Property
Pvap	284.02	kPa	659.01	Calculated Property
Pvap	616.93	kPa	709.58	Calculated Property
Pvap	1206.90	kPa	760.15	Calculated Property
Pvap	[1.97e-05; 1113.31]	kPa	[305.33; 755.93]	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			1.75641e+02
Coefficient B			-1.78211e+04
Coefficient C			-2.25095e+01
Coefficient D			7.24611e-06
Coefficient E			0.00000e+00
Temperature range, min.			305.33
Temperature range, max.			755.93
Pvap	1.97e-05	kPa	305.33	Calculated Property
Pvap	3.05e-03	kPa	355.40	Calculated Property
Pvap	0.10	kPa	405.46	Calculated Property
Pvap	1.26	kPa	455.53	Calculated Property
Pvap	8.23	kPa	505.60	Calculated Property
Pvap	34.58	kPa	555.66	Calculated Property
Pvap	107.07	kPa	605.73	Calculated Property
Pvap	267.64	kPa	655.80	Calculated Property
Pvap	575.42	kPa	705.86	Calculated Property
Pvap	1113.31	kPa	755.93	Calculated Property
Pvap	[1.85e-05; 2.06e-04]	kPa	[306.00; 328.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			7.46686e+01
Coefficient B			-6.49271e+04
Coefficient C			4.52785e+02
Reference			Morecroft, 1964
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			306.00
Temperature range, max.			328.00
Pvap	1.85e-05	kPa	306.00	Calculated Property
Pvap	2.43e-05	kPa	308.44	Calculated Property
Pvap	3.20e-05	kPa	310.89	Calculated Property
Pvap	4.19e-05	kPa	313.33	Calculated Property
Pvap	5.49e-05	kPa	315.78	Calculated Property
Pvap	7.18e-05	kPa	318.22	Calculated Property
Pvap	9.36e-05	kPa	320.67	Calculated Property
Pvap	1.22e-04	kPa	323.11	Calculated Property
Pvap	1.59e-04	kPa	325.56	Calculated Property
Pvap	2.06e-04	kPa	328.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[796.68; 382.55]	kg/m3	[273.15; 734.16]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			5.41043e+01
Coefficient B			2.38310e-01
Coefficient C			7.60000e+02
Coefficient D			2.99030e-01
Temperature range, min.			273.15
Temperature range, max.			734.16
ρl	796.68	kg/m3	273.15	Calculated Property
ρl	764.64	kg/m3	324.37	Calculated Property
ρl	731.30	kg/m3	375.60	Calculated Property
ρl	696.35	kg/m3	426.82	Calculated Property
ρl	659.37	kg/m3	478.04	Calculated Property
ρl	619.70	kg/m3	529.27	Calculated Property
ρl	576.30	kg/m3	580.49	Calculated Property
ρl	527.20	kg/m3	631.71	Calculated Property
ρl	468.01	kg/m3	682.94	Calculated Property
ρl	382.55	kg/m3	734.16	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 3.78e-06]	N/m	[293.15; 751.03]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-3.89050e-03
Coefficient B			1.02440e+02
Coefficient C			-3.87930e+00
Coefficient D			2.11930e-03
Coefficient E			-6.02260e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 758 K.
Temperature range, min.			293.15
Temperature range, max.			751.03
γ	0.03	N/m	293.15	Calculated Property
γ	0.02	N/m	344.03	Calculated Property
γ	0.02	N/m	394.90	Calculated Property
γ	0.02	N/m	445.78	Calculated Property
γ	0.01	N/m	496.65	Calculated Property
γ	0.01	N/m	547.53	Calculated Property
γ	0.01	N/m	598.40	Calculated Property
γ	0.00	N/m	649.28	Calculated Property
γ	0.00	N/m	700.15	Calculated Property
γ	3.78e-06	N/m	751.03	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.07]	W/m×K	[305.04; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			4.33330e-05
Coefficient B			1.27100e+00
Coefficient C			2.79960e+03
Coefficient D			1.38170e+05
Temperature range, min.			305.04
Temperature range, max.			1000.00
λgas	0.01	W/m×K	305.04	Calculated Property
λgas	0.01	W/m×K	382.26	Calculated Property
λgas	0.01	W/m×K	459.48	Calculated Property
λgas	0.02	W/m×K	536.69	Calculated Property
λgas	0.03	W/m×K	613.91	Calculated Property
λgas	0.03	W/m×K	691.13	Calculated Property
λgas	0.04	W/m×K	768.35	Calculated Property
λgas	0.05	W/m×K	845.56	Calculated Property
λgas	0.06	W/m×K	922.78	Calculated Property
λgas	0.07	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.08]	W/m×K	[305.04; 603.05]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			-5.70190e-02
Coefficient B			7.31110e+01
Coefficient C			-2.15180e+00
Coefficient D			2.16180e-03
Coefficient E			-3.51710e-06
Temperature range, min.			305.04
Temperature range, max.			603.05
λliquid	0.15	W/m×K	305.04	Calculated Property
λliquid	0.14	W/m×K	338.15	Calculated Property
λliquid	0.14	W/m×K	371.26	Calculated Property
λliquid	0.13	W/m×K	404.38	Calculated Property
λliquid	0.12	W/m×K	437.49	Calculated Property
λliquid	0.12	W/m×K	470.60	Calculated Property
λliquid	0.11	W/m×K	503.71	Calculated Property
λliquid	0.10	W/m×K	536.83	Calculated Property
λliquid	0.09	W/m×K	569.94	Calculated Property
λliquid	0.08	W/m×K	603.05	Calculated Property

Similar Compounds

Find more compounds similar to Nonadecane.

Mixtures

• Carbon dioxide + Nonadecane
• Di-n-propyl ether + Nonadecane
• n-Butyl ether + Nonadecane
• Butane, 1-chloro- + Nonadecane
• Octane, 1-chloro- + Nonadecane

Sources

• KDB Vapor Pressure Data
• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• Hankinson and Thomson (1979), COSTALD parameters ChEDL chemicals 1.5.2, from Hankinson, R. W.; Thomson, G. H. A New Correlation for Saturated Densities of Liquids and Their Mixtures. AIChE J. 1979, 25, 653-663.
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 ChEDL chemicals 1.5.2, from Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 2. Normal Alkanes. J. Chem. Eng. Data 1995, 40, 531-546.
• Passut and Danner (1973), critical constants and acentric factors ChEDL chemicals 1.5.2, from Passut, C. A.; Danner, R. P. Acentric Factor. A Valuable Correlating Parameter for the Properties of Hydrocarbons. Ind. Eng. Chem. Process Des. Dev. 1973, 12, 365-368.
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• Cheméo Relay (1.0)
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Crippen Method
• Critical temperatures and pressures of C40, C44, and C60 normal alkanes measured by the pulse-heating technique
• 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
• 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
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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