Decanoic acid, methyl ester (CAS 110-42-9)

InChI

InChI=1S/C11H22O2/c1-3-4-5-6-7-8-9-10-11(12)13-2/h3-10H2,1-2H3

InChI Key

YRHYCMZPEVDGFQ-UHFFFAOYSA-N

Formula

C11H22O2

SMILES

CCCCCCCCCC(=O)OC

Molecular Weight¹

186.30

CAS

110-42-9

Other Names

Capric acid methyl ester
Metholene 2095
Methyl n-decanoate
Methyl tridecanoate
Methyl-n-caprate
Uniphat A30
capric acid, methyl ester
methyl caprate
methyl caprinate
methyl decanoate
n-Capric acid methyl ester

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_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
IE : Ionization energy (eV).
log₁₀WS : Log10 of Water solubility in mol/l.
logP_oct/wat : Octanol/Water partition coefficient.
McVol : McGowan's characteristic volume (ml/mol).
P_c : Critical Pressure (kPa).
P_triple : Triple Point Pressure (kPa).
P_vap : Vapor pressure (kPa).
n₀ : Refractive Index.
ρ_l : Liquid Density (kg/m³).
I_np : Non-polar retention indices.
I : Polar retention indices.
c_sound,fluid : Speed of sound in fluid (m/s).
T_boil : Normal Boiling Point Temperature (K).
T_boilr : Boiling point at reduced 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_triple : Triple Point Temperature (K).
U_Qi : UNIQUAC Qi Parameter.
U_Ri : UNIQUAC Ri Parameter.
V_c : Critical Volume (m³/kmol).
Z_c : Critical Compressibility.
¹: Molecular weight from the IUPAC atomic weights tables.

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Physical Properties
Temperature Dependent Properties
Pressure Dependent Properties
Datasets
Correlations
Similar Compounds
Mixtures
Sources

Physical Properties

Property	Value	Unit	Source
ω	0.5491		ChemSep v8.3 pure component data
Δ_cH°_liquid	[-6831.90; -6799.00]	kJ/mol
Δ_cH°_liquid	-6799.00 ± 0.40	kJ/mol	NIST
Δ_cH°_liquid	-6831.90 ± 1.70	kJ/mol	NIST
μ	2.08	debye	ChemSep v8.3 pure component data
Δ_fG°	-256.27	kJ/mol	ChemSep v8.3 pure component data
Δ_fH°_gas	-573.70	kJ/mol	ChemSep v8.3 pure component data
Δ_fusH°	35.92	kJ/mol	Heat Capacity Measurements of 13 Methyl Esters of n-Carboxylic Acids from Methyloctanoate to Methyleicosanoate between 5 K and 350 K
Δ_vapH°	[66.10; 66.90]	kJ/mol
Δ_vapH°	66.10 ± 0.20	kJ/mol	NIST
Δ_vapH°	66.90	kJ/mol	NIST
Δ_vapH°	66.30 ± 0.50	kJ/mol	NIST
Δ_vapH°	66.75 ± 0.57	kJ/mol	NIST
Δ_vapH°	66.80 ± 0.60	kJ/mol	NIST
IE	9.68	eV	Relay (1.0) Calculated Property
log₁₀WS	[-4.69; -4.63]
log₁₀WS	-4.63		Aq. Solubility Prediction
log₁₀WS	-4.69		Estimated Solubility
logP_oct/wat	3.300		Crippen Calculated Property
McVol	173.290	ml/mol	McGowan Calculated Property
P_c	1890.00	kPa	ChemSep v8.3 pure component data
P_triple	5.68e-05	kPa	ChemSep v8.3 pure component data
I_np	[224.56; 1333.00]
I_np	1323.80		NIST
I_np	1319.30		NIST
I_np	1313.00		NIST
I_np	1321.00		NIST
I_np	1312.00		NIST
I_np	1306.00		NIST
I_np	1310.00		NIST
I_np	1307.00		NIST
I_np	1308.00		NIST
I_np	1328.00		NIST
I_np	1324.00		NIST
I_np	1307.00		NIST
I_np	1305.00		NIST
I_np	1324.00		NIST
I_np	1327.00		NIST
I_np	1325.00		NIST
I_np	1325.10		NIST
I_np	1328.00		NIST
I_np	1326.00		NIST
I_np	1326.00		NIST
I_np	1325.00		NIST
I_np	1325.00		NIST
I_np	1309.00		NIST
I_np	1324.00		NIST
I_np	1326.00		NIST
I_np	1306.00		NIST
I_np	1312.00		NIST
I_np	1310.00		NIST
I_np	1311.40		NIST
I_np	1307.00		NIST
I_np	1306.20		NIST
I_np	1306.60		NIST
I_np	1309.00		NIST
I_np	1303.76		NIST
I_np	1309.67		NIST
I_np	1309.08		NIST
I_np	1320.62		NIST
I_np	1311.06		NIST
I_np	1313.09		NIST
I_np	1306.48		NIST
I_np	1324.00		NIST
I_np	1310.00		NIST
I_np	1322.60		NIST
I_np	1328.60		NIST
I_np	1326.00		NIST
I_np	1306.00		NIST
I_np	1307.00		NIST
I_np	1309.00		NIST
I_np	1321.00		NIST
I_np	1305.00		NIST
I_np	1316.00		NIST
I_np	1325.00		NIST
I_np	1325.00		NIST
I_np	1326.00		NIST
I_np	1325.00		NIST
I_np	1326.00		NIST
I_np	1333.00		NIST
I_np	1327.00		NIST
I_np	1326.00		NIST
I_np	1311.00		NIST
I_np	1327.00		NIST
I_np	1326.00		NIST
I_np	1306.00		NIST
I_np	1326.00		NIST
I_np	1305.00		NIST
I_np	1306.00		NIST
I_np	1308.00		NIST
I_np	1313.00		NIST
I_np	1307.00		NIST
I_np	1307.00		NIST
I_np	1308.00		NIST
I_np	1307.00		NIST
I_np	1306.00		NIST
I_np	1323.00		NIST
I_np	1326.00		NIST
I_np	1325.00		NIST
I_np	1328.00		NIST
I_np	1325.00		NIST
I_np	1326.00		NIST
I_np	1322.00		NIST
I_np	1326.00		NIST
I_np	1302.00		NIST
I_np	1324.00		NIST
I_np	1324.00		NIST
I_np	1325.00		NIST
I_np	1307.00		NIST
I_np	1329.00		NIST
I_np	1307.00		NIST
I_np	1328.00		NIST
I_np	1328.00		NIST
I_np	1314.00		NIST
I_np	1309.00		NIST
I_np	1306.00		NIST
I_np	1307.00		NIST
I_np	1308.00		NIST
I_np	1305.00		NIST
I_np	Outlier 224.56		NIST
I_np	Outlier 226.16		NIST
I_np	Outlier 230.80		NIST
I_np	Outlier 226.04		NIST
I_np	Outlier 226.04		NIST
I_np	1324.00		NIST
I_np	1326.00		NIST
I_np	1311.40		NIST
I_np	1303.76		NIST
I_np	1313.09		NIST
I_np	1321.00		NIST
I_np	1307.00		NIST
I_np	1323.00		NIST
I_np	1328.00		NIST
I_np	Outlier 226.04		NIST
I	[1550.00; 1636.00]
I	1597.00		NIST
I	Outlier 1636.00		NIST
I	1624.00		NIST
I	1570.00		NIST
I	1598.30		NIST
I	1603.00		NIST
I	1605.20		NIST
I	1616.30		NIST
I	1592.50		NIST
I	1600.70		NIST
I	1606.90		NIST
I	1613.20		NIST
I	1581.00		NIST
I	1581.00		NIST
I	1592.00		NIST
I	1593.00		NIST
I	1615.00		NIST
I	1586.00		NIST
I	1583.00		NIST
I	1614.00		NIST
I	1597.00		NIST
I	1603.00		NIST
I	1586.00		NIST
I	1590.00		NIST
I	1613.00		NIST
I	1585.00		NIST
I	1594.00		NIST
I	1604.00		NIST
I	1599.00		NIST
I	Outlier 1550.00		NIST
I	Outlier 1552.00		NIST
I	1590.00		NIST
I	1586.00		NIST
I	1596.00		NIST
I	1581.00		NIST
I	1602.00		NIST
I	1583.00		NIST
I	1584.00		NIST
I	1595.00		NIST
I	1593.00		NIST
I	1600.00		NIST
I	1585.00		NIST
I	1628.00		NIST
I	1628.00		NIST
I	1593.00		NIST
I	1628.00		NIST
I	1585.00		NIST
I	1581.00		NIST
I	1573.00		NIST
I	1600.00		NIST
I	1586.00		NIST
I	1593.00		NIST
I	1597.00		NIST
I	1603.00		NIST
I	1606.90		NIST
T_boil	[497.05; 505.00]	K
T_boil	505.00	K	ChemSep v8.3 pure component data
T_boil	497.20	K	NIST
T_boil	497.05 ± 1.00	K	NIST
T_c	681.00	K	ChemSep v8.3 pure component data
T_fus	[255.15; 260.40]	K
T_fus	255.15	K	ChemSep v8.3 pure component data
T_fus	260.40 ± 0.05	K	NIST
T_triple	255.15	K	ChemSep v8.3 pure component data
U_Qi	6.90		ChemSep v8.3 pure component data
U_Ri	8.20		ChemSep v8.3 pure component data
V_c	0.714	m³/kmol	ChemSep v8.3 pure component data
Z_c	0.2430000		ChemSep v8.3 pure component data

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,liquid	[382.80; 417.20]	J/mol×K	[298.15; 373.15]

C_p,liquid	382.80	J/mol×K	298.15	NIST
C_p,liquid	384.70	J/mol×K	303.15	Heat capacities and thermal diffusivities of some n-alkanoic acid methyl esters
C_p,liquid	387.60	J/mol×K	313.15	Heat capacities and thermal diffusivities of some n-alkanoic acid methyl esters
C_p,liquid	391.80	J/mol×K	323.15	Heat capacities and thermal diffusivities of some n-alkanoic acid methyl esters
C_p,liquid	396.70	J/mol×K	333.15	Heat capacities and thermal diffusivities of some n-alkanoic acid methyl esters
C_p,liquid	401.90	J/mol×K	343.15	Heat capacities and thermal diffusivities of some n-alkanoic acid methyl esters
C_p,liquid	407.30	J/mol×K	353.15	Heat capacities and thermal diffusivities of some n-alkanoic acid methyl esters
C_p,liquid	412.40	J/mol×K	363.15	Heat capacities and thermal diffusivities of some n-alkanoic acid methyl esters
C_p,liquid	417.20	J/mol×K	373.15	Heat capacities and thermal diffusivities of some n-alkanoic acid methyl esters
η	[0.0007421; 0.0029888]	Pa×s	[278.15; 363.15]

η	0.0029888	Pa×s	278.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0026543	Pa×s	283.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0023733	Pa×s	288.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0021360	Pa×s	293.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0019335	Pa×s	298.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0017601	Pa×s	303.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0016091	Pa×s	308.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0014773	Pa×s	313.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0013613	Pa×s	318.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0012589	Pa×s	323.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0011675	Pa×s	328.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0010864	Pa×s	333.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0010133	Pa×s	338.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0009477	Pa×s	343.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0008886	Pa×s	348.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0008342	Pa×s	353.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0007859	Pa×s	358.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0007421	Pa×s	363.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
Δ_vapH	[49.90; 63.05]	kJ/mol	[293.00; 498.00]

Δ_vapH	63.05	kJ/mol	293.00	NIST
Δ_vapH	62.90 ± 0.10	kJ/mol	337.00	NIST
Δ_vapH	63.00	kJ/mol	347.00	NIST
Δ_vapH	62.00	kJ/mol	350.00	NIST
Δ_vapH	57.10	kJ/mol	439.50	NIST
Δ_vapH	49.90	kJ/mol	498.00	NIST
P_vap	[4.73e-04; 12.80]	kPa	[273.35; 432.65]

P_vap	4.73e-04	kPa	273.35	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	4.98e-04	kPa	273.84	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	5.25e-04	kPa	274.32	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	5.54e-04	kPa	274.80	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	5.88e-04	kPa	275.29	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	6.15e-04	kPa	275.77	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	6.49e-04	kPa	276.26	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	6.85e-04	kPa	276.74	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	7.23e-04	kPa	277.23	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	7.60e-04	kPa	277.71	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	8.03e-04	kPa	278.20	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	8.44e-04	kPa	278.69	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	8.87e-04	kPa	279.18	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	9.34e-04	kPa	279.66	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	9.82e-04	kPa	280.15	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	1.03e-03	kPa	280.64	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	1.09e-03	kPa	281.12	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	1.13e-03	kPa	281.47	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	1.31e-03	kPa	282.96	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	1.39e-03	kPa	283.48	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	1.53e-03	kPa	284.46	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	1.61e-03	kPa	284.96	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	1.69e-03	kPa	285.43	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	1.73e-03	kPa	285.64	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	1.74e-03	kPa	285.74	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	1.78e-03	kPa	285.95	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	1.87e-03	kPa	286.44	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	1.97e-03	kPa	286.95	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	2.06e-03	kPa	287.44	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	2.17e-03	kPa	287.94	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	2.17e-03	kPa	287.94	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	2.39e-03	kPa	288.93	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	2.49e-03	kPa	289.31	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	2.51e-03	kPa	289.43	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	2.76e-03	kPa	290.42	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	2.79e-03	kPa	290.53	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	2.89e-03	kPa	290.92	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	3.15e-03	kPa	291.81	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	3.18e-03	kPa	291.92	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	3.34e-03	kPa	292.42	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	3.49e-03	kPa	292.87	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
P_vap	3.50e-03	kPa	292.90	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	3.67e-03	kPa	293.41	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	3.84e-03	kPa	293.91	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	3.99e-03	kPa	294.30	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	4.22e-03	kPa	294.90	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	4.41e-03	kPa	295.40	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	4.44e-03	kPa	295.51	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	4.62e-03	kPa	295.90	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	4.84e-03	kPa	296.39	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	4.99e-03	kPa	296.77	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	5.30e-03	kPa	297.39	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	5.53e-03	kPa	297.89	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	5.57e-03	kPa	297.98	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	6.06e-03	kPa	298.88	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	6.34e-03	kPa	299.38	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	6.92e-03	kPa	300.37	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	6.95e-03	kPa	300.46	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	7.24e-03	kPa	300.87	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	7.89e-03	kPa	301.87	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	8.24e-03	kPa	302.37	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	8.52e-03	kPa	302.84	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	8.63e-03	kPa	302.94	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	8.40e-03	kPa	302.97	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
P_vap	8.98e-03	kPa	303.36	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	9.24e-03	kPa	303.76	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	9.30e-03	kPa	303.81	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	9.29e-03	kPa	303.82	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	9.29e-03	kPa	303.82	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	9.37e-03	kPa	303.86	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	0.01	kPa	304.85	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	0.01	kPa	304.85	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	0.01	kPa	305.24	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	0.01	kPa	305.26	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	0.01	kPa	305.29	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	0.01	kPa	305.35	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	0.01	kPa	305.42	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
P_vap	0.02	kPa	313.01	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
P_vap	0.04	kPa	323.04	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
P_vap	0.09	kPa	333.13	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
P_vap	0.17	kPa	343.30	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
P_vap	0.31	kPa	352.40	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
P_vap	0.56	kPa	362.72	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
P_vap	0.93	kPa	372.54	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
P_vap	1.56	kPa	382.62	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
P_vap	2.00	kPa	389.10	Isobaric vapor-liquid equilibrium for binary system of methyl caprylate + methyl caprate at 2, 6 and 10 kPa
P_vap	2.00	kPa	389.10	Isobaric vapor-liquid equilibrium for binary system of methyl caprate + methyl laurate at 2, 4 and 6 kPa
P_vap	2.52	kPa	392.75	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
P_vap	3.92	kPa	402.71	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
P_vap	4.00	kPa	404.15	Isobaric vapor-liquid equilibrium for binary system of methyl caprate + methyl laurate at 2, 4 and 6 kPa
P_vap	6.01	kPa	412.79	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
P_vap	6.00	kPa	412.93	Isobaric vapor-liquid equilibrium for binary system of methyl caprylate + methyl caprate at 2, 6 and 10 kPa
P_vap	6.00	kPa	413.57	Isobaric vapor-liquid equilibrium for binary system of methyl caprate + methyl laurate at 2, 4 and 6 kPa
P_vap	8.89	kPa	422.71	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
P_vap	10.00	kPa	424.43	Isobaric vapor-liquid equilibrium for binary system of methyl caprylate + methyl caprate at 2, 6 and 10 kPa
P_vap	12.80	kPa	432.65	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
n₀	[1.39819; 1.43209]		[278.15; 358.15]

n₀	1.43209		278.15	Thermophysical properties of fatty acid methyl and ethyl esters
n₀	1.42995		283.15	Thermophysical properties of fatty acid methyl and ethyl esters
n₀	1.42783		288.15	Thermophysical properties of fatty acid methyl and ethyl esters
n₀	1.42571		293.15	Thermophysical properties of fatty acid methyl and ethyl esters
n₀	1.42350		298.15	Measurement and Prediction of Excess Properties of Binary Mixtures Methyl Decanoate + an Even-Numbered n-Alkane (C6-C16) at 298.15 K
n₀	1.42359		298.15	Thermophysical properties of fatty acid methyl and ethyl esters
n₀	1.42148		303.15	Thermophysical properties of fatty acid methyl and ethyl esters
n₀	1.41938		308.15	Thermophysical properties of fatty acid methyl and ethyl esters
n₀	1.41726		313.15	Thermophysical properties of fatty acid methyl and ethyl esters
n₀	1.41510		318.15	Thermophysical properties of fatty acid methyl and ethyl esters
n₀	1.41295		323.15	Thermophysical properties of fatty acid methyl and ethyl esters
n₀	1.41083		328.15	Thermophysical properties of fatty acid methyl and ethyl esters
n₀	1.40871		333.15	Thermophysical properties of fatty acid methyl and ethyl esters
n₀	1.40659		338.15	Thermophysical properties of fatty acid methyl and ethyl esters
n₀	1.40448		343.15	Thermophysical properties of fatty acid methyl and ethyl esters
n₀	1.40237		348.15	Thermophysical properties of fatty acid methyl and ethyl esters
n₀	1.40028		353.15	Thermophysical properties of fatty acid methyl and ethyl esters
n₀	1.39819		358.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρ_l	[847.62; 872.25]	kg/m³	[293.15; 323.15]

ρ_l	872.25	kg/m³	293.15	Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
ρ_l	868.16	kg/m³	298.15	Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
ρ_l	864.06	kg/m³	303.15	Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
ρ_l	859.96	kg/m³	308.15	Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
ρ_l	855.85	kg/m³	313.15	Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
ρ_l	851.74	kg/m³	318.15	Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
ρ_l	847.62	kg/m³	323.15	Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
λ	[0.12; 0.15]	W/m×K	[267.10; 399.95]

λ	0.15	W/m×K	267.10	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.15	W/m×K	267.11	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.15	W/m×K	277.00	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.15	W/m×K	277.07	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	288.82	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	288.84	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	300.83	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	300.86	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	311.66	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	311.87	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	324.72	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	324.92	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	336.71	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	336.71	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	348.66	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	348.81	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	354.58	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	354.59	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	360.11	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	360.61	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	368.98	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	369.47	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.12	W/m×K	379.50	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.12	W/m×K	379.65	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.12	W/m×K	389.35	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.12	W/m×K	389.39	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.12	W/m×K	399.87	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.12	W/m×K	399.95	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
T_boilr	[381.20; 387.20]	K	[1.30; 2.00]
T_boilr	381.20	K	1.30	NIST
T_boilr	387.20	K	2.00	NIST

Datasets

Molar heat capacity at constant pressure, J/K/mol (1)
Viscosity, Pa*s (1)
Mass density, kg/m3 (1)
Speed of sound, m/s (1)

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

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
100.00	313.71	383.90
4070.00	313.82	382.10
8030.00	313.83	380.50
12010.00	313.99	378.50
16140.00	314.01	376.60
100.00	324.79	387.60
4070.00	324.79	386.00
8030.00	325.01	384.40
12010.00	325.06	382.50
16140.00	325.20	379.30
100.00	334.12	393.20
4070.00	334.53	390.30
8030.00	334.33	388.30
12010.00	334.60	386.20
16140.00	334.84	384.20
Reference

Viscosity, Pa*s

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
101.30	293.15	0.0022
20000.00	293.15	0.0027
40000.00	293.15	0.0032
60000.00	293.15	0.0039
80000.00	293.15	0.0047
100000.00	293.15	0.0055
120000.00	293.15	0.0065
140000.00	293.15	0.0077
160000.00	293.15	0.0090
101.30	313.15	0.0015
20000.00	313.15	0.0018
40000.00	313.15	0.0022
60000.00	313.15	0.0027
80000.00	313.15	0.0031
100000.00	313.15	0.0036
120000.00	313.15	0.0042
140000.00	313.15	0.0049
160000.00	313.15	0.0056
180000.00	313.15	0.0063
200000.00	313.15	0.0072
101.30	333.15	0.0011
20000.00	333.15	0.0013
40000.00	333.15	0.0016
60000.00	333.15	0.0019
80000.00	333.15	0.0022
100000.00	333.15	0.0025
120000.00	333.15	0.0029
140000.00	333.15	0.0033
160000.00	333.15	0.0037
180000.00	333.15	0.0042
200000.00	333.15	0.0047
101.30	353.15	0.0008
20000.00	353.15	0.0010
40000.00	353.15	0.0012
60000.00	353.15	0.0014
80000.00	353.15	0.0016
100000.00	353.15	0.0019
120000.00	353.15	0.0021
140000.00	353.15	0.0024
160000.00	353.15	0.0027
180000.00	353.15	0.0030
200000.00	353.15	0.0034
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	868.0
298.15	3000.00	870.0
298.15	6000.00	872.0
298.15	9000.00	874.0
298.15	12000.00	877.0
298.15	15000.00	878.0
308.15	100.00	860.0
308.15	3010.00	862.0
308.15	6000.00	864.0
308.15	9000.00	866.0
308.15	12000.00	869.0
308.15	15000.00	871.0
318.15	100.00	853.0
318.15	3000.00	854.0
318.15	6000.00	856.0
318.15	9000.00	859.0
318.15	12000.00	861.0
318.15	15000.00	863.0
Reference

Speed of sound, m/s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
283.15	101.30	1362.6
283.15	10000.00	1408.9
283.15	20000.00	1452.2
283.15	30000.00	1493.2
283.15	40000.00	1531.7
283.15	50000.00	1568.0
283.15	60000.00	1602.6
283.15	70000.00	1634.5
283.15	80000.00	1666.4
283.15	90000.00	1696.9
283.15	100000.00	1726.9
283.15	110000.00	1755.2
283.15	120000.00	1783.4
283.15	130000.00	1809.5
283.15	140000.00	1835.9
303.15	101.30	1287.7
303.15	10000.00	1339.2
303.15	20000.00	1385.8
303.15	30000.00	1429.6
303.15	40000.00	1470.3
303.15	50000.00	1508.7
303.15	60000.00	1544.9
303.15	70000.00	1580.2
303.15	80000.00	1614.1
303.15	90000.00	1646.1
303.15	100000.00	1676.9
303.15	110000.00	1706.8
303.15	120000.00	1735.1
303.15	130000.00	1762.8
303.15	140000.00	1789.2
303.15	150000.00	1815.2
303.15	170000.00	1864.9
303.15	190000.00	1912.7
303.15	210000.00	1957.6
323.15	101.30	1214.8
323.15	10000.00	1269.1
323.15	20000.00	1319.3
323.15	30000.00	1365.7
323.15	40000.00	1409.0
323.15	50000.00	1449.5
323.15	60000.00	1487.8
323.15	70000.00	1524.0
323.15	80000.00	1558.3
323.15	90000.00	1591.2
323.15	100000.00	1623.3
323.15	110000.00	1653.9
323.15	120000.00	1684.6
323.15	130000.00	1711.9
323.15	140000.00	1739.6
323.15	150000.00	1765.9
323.15	170000.00	1817.0
323.15	190000.00	1864.8
323.15	210000.00	1910.9
343.15	101.30	1142.8
343.15	10000.00	1202.4
343.15	20000.00	1255.9
343.15	30000.00	1304.9
343.15	40000.00	1350.5
343.15	50000.00	1393.5
343.15	60000.00	1433.7
343.15	70000.00	1471.7
343.15	80000.00	1508.2
343.15	90000.00	1541.7
343.15	100000.00	1574.1
343.15	110000.00	1606.0
343.15	120000.00	1636.2
343.15	130000.00	1665.9
343.15	140000.00	1694.0
343.15	150000.00	1721.2
343.15	170000.00	1773.2
343.15	190000.00	1822.0
343.15	210000.00	1868.7
363.15	10000.00	1138.5
363.15	20000.00	1195.9
363.15	30000.00	1247.9
363.15	40000.00	1296.3
363.15	50000.00	1341.1
363.15	60000.00	1382.7
363.15	70000.00	1421.6
363.15	80000.00	1458.4
363.15	90000.00	1493.8
363.15	100000.00	1527.4
363.15	110000.00	1559.7
363.15	120000.00	1590.9
363.15	130000.00	1620.7
363.15	140000.00	1649.4
363.15	150000.00	1677.2
363.15	170000.00	1730.6
363.15	190000.00	1780.4
363.15	210000.00	1827.2
383.15	10000.00	1077.4
383.15	20000.00	1138.6
383.15	30000.00	1193.5
383.15	40000.00	1244.5
383.15	50000.00	1291.3
383.15	60000.00	1334.9
383.15	70000.00	1375.4
383.15	80000.00	1414.2
383.15	90000.00	1450.6
383.15	100000.00	1485.3
383.15	110000.00	1518.9
383.15	120000.00	1550.9
383.15	130000.00	1581.2
383.15	140000.00	1610.8
383.15	150000.00	1641.0
383.15	170000.00	1692.7
383.15	190000.00	1743.0
383.15	210000.00	1791.1
403.15	10000.00	1017.7
403.15	20000.00	1083.2
403.15	30000.00	1141.7
403.15	40000.00	1194.7
403.15	50000.00	1242.9
403.15	60000.00	1288.1
403.15	70000.00	1330.6
403.15	80000.00	1370.3
403.15	90000.00	1407.7
403.15	100000.00	1442.8
403.15	110000.00	1476.6
403.15	120000.00	1509.7
403.15	130000.00	1541.7
403.15	140000.00	1571.6
403.15	150000.00	1600.1
403.15	170000.00	1655.5
403.15	190000.00	1706.6
403.15	210000.00	1754.5
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[271.79; 687.64]	J/mol×K	[298.15; 1500.00]	ChemSep v8.3 pure component data
Equation			Y = A + B·((C/T)/sinh(C/T))² + D·((E/T)/cosh(E/T))² Y is C_p,gas in J/mol×K, T in K
Coefficient A			2.09900e+02
Coefficient B			4.13910e+02
Coefficient C			7.77290e+02
Coefficient D			2.61610e+02
Coefficient E			2.44530e+03
Comment			ChemSep eq 107, IdealGasHeatCapacityCp
Temperature range, min.			298.15
Temperature range, max.			1500.00

C_p,gas	271.79	J/mol×K	298.15	Calculated Property
C_p,gas	365.14	J/mol×K	431.69	Calculated Property
C_p,gas	441.66	J/mol×K	565.23	Calculated Property
C_p,gas	499.95	J/mol×K	698.77	Calculated Property
C_p,gas	547.08	J/mol×K	832.31	Calculated Property
C_p,gas	586.82	J/mol×K	965.84	Calculated Property
C_p,gas	620.38	J/mol×K	1099.38	Calculated Property
C_p,gas	648.15	J/mol×K	1232.92	Calculated Property
C_p,gas	670.41	J/mol×K	1366.46	Calculated Property
C_p,gas	687.64	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
C_p,liquid	[346.77; 488.59]	J/mol×K	[255.15; 505.00]	ChemSep v8.3 pure component data
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is C_p,liquid in J/mol×K, T in K
Coefficient A			2.01940e+02
Coefficient B			5.67630e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			ChemSep eq 100, LiquidHeatCapacityCp
Temperature range, min.			255.15
Temperature range, max.			505.00

C_p,liquid	346.77	J/mol×K	255.15	Calculated Property
C_p,liquid	362.53	J/mol×K	282.91	Calculated Property
C_p,liquid	378.29	J/mol×K	310.67	Calculated Property
C_p,liquid	394.04	J/mol×K	338.43	Calculated Property
C_p,liquid	409.80	J/mol×K	366.19	Calculated Property
C_p,liquid	425.56	J/mol×K	393.96	Calculated Property
C_p,liquid	441.32	J/mol×K	421.72	Calculated Property
C_p,liquid	457.08	J/mol×K	449.48	Calculated Property
C_p,liquid	472.84	J/mol×K	477.24	Calculated Property
C_p,liquid	488.59	J/mol×K	505.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0049544; 0.0002018]	Pa×s	[255.15; 505.00]	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			-1.17770e+01
Coefficient B			1.65070e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			ChemSep eq 101, LiquidViscosity
Temperature range, min.			255.15
Temperature range, max.			505.00

η	0.0049544	Pa×s	255.15	Calculated Property
η	0.0026260	Pa×s	282.91	Calculated Property
η	0.0015590	Pa×s	310.67	Calculated Property
η	0.0010083	Pa×s	338.43	Calculated Property
η	0.0006966	Pa×s	366.19	Calculated Property
η	0.0005070	Pa×s	393.96	Calculated Property
η	0.0003848	Pa×s	421.72	Calculated Property
η	0.0003022	Pa×s	449.48	Calculated Property
η	0.0002440	Pa×s	477.24	Calculated Property
η	0.0002018	Pa×s	505.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Δ_vapH	[69.13; 0.00]	kJ/mol	[255.15; 681.00]	ChemSep v8.3 pure component data
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is Δ_vapH in kJ/mol, T in K
Coefficient A			8.78330e+01
Coefficient B			5.92850e-01
Coefficient C			-2.70010e-01
Coefficient D			1.31770e-01
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			6.81000e+02
Comment			ChemSep eq 106, HeatOfVaporization, ChemSep Tmax 686.9 K
Temperature range, min.			255.15
Temperature range, max.			681.00

Δ_vapH	69.13	kJ/mol	255.15	Calculated Property
Δ_vapH	65.53	kJ/mol	302.47	Calculated Property
Δ_vapH	61.75	kJ/mol	349.78	Calculated Property
Δ_vapH	57.70	kJ/mol	397.10	Calculated Property
Δ_vapH	53.28	kJ/mol	444.42	Calculated Property
Δ_vapH	48.33	kJ/mol	491.73	Calculated Property
Δ_vapH	42.58	kJ/mol	539.05	Calculated Property
Δ_vapH	35.57	kJ/mol	586.37	Calculated Property
Δ_vapH	26.06	kJ/mol	633.68	Calculated Property
Δ_vapH	0.00	kJ/mol	681.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
P_vap	[1.33; 202.67]	kPa	[381.00; 520.45]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is P_vap in kPa, T in K
Coefficient A			1.61003e+01
Coefficient B			-4.73527e+03
Coefficient C			-8.15400e+01
Temperature range, min.			381.00
Temperature range, max.			520.45

P_vap	1.33	kPa	381.00	Calculated Property
P_vap	2.90	kPa	396.49	Calculated Property
P_vap	5.87	kPa	411.99	Calculated Property
P_vap	11.16	kPa	427.48	Calculated Property
P_vap	20.07	kPa	442.98	Calculated Property
P_vap	34.39	kPa	458.47	Calculated Property
P_vap	56.47	kPa	473.97	Calculated Property
P_vap	89.30	kPa	489.46	Calculated Property
P_vap	136.56	kPa	504.96	Calculated Property
P_vap	202.67	kPa	520.45	Calculated Property
P_vap	[5.69e-05; 1943.65]	kPa	[255.15; 686.90]	ChemSep v8.3 pure component data
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is P_vap in kPa, T in K
Coefficient A			8.59832e+01
Coefficient B			-1.07940e+04
Coefficient C			-9.64540e+00
Coefficient D			2.93910e-18
Coefficient E			6.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			255.15
Temperature range, max.			686.90

P_vap	5.69e-05	kPa	255.15	Calculated Property
P_vap	8.75e-03	kPa	303.12	Calculated Property
P_vap	0.28	kPa	351.09	Calculated Property
P_vap	3.25	kPa	399.07	Calculated Property
P_vap	20.06	kPa	447.04	Calculated Property
P_vap	79.46	kPa	495.01	Calculated Property
P_vap	230.83	kPa	542.98	Calculated Property
P_vap	538.43	kPa	590.96	Calculated Property
P_vap	1077.07	kPa	638.93	Calculated Property
P_vap	1943.65	kPa	686.90	Calculated Property
P_vap	[1.41; 31.13]	kPa	[380.50; 461.40]	NIST
Equation			ln(Y) = A + B/(T + C) Y is P_vap in kPa, T in K
Coefficient A			1.53721e+01
Coefficient B			-4.69188e+03
Coefficient C			-6.82460e+01
Reference			Rose and Supina, 1961
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			380.50
Temperature range, max.			461.40

P_vap	1.41	kPa	380.50	Calculated Property
P_vap	2.15	kPa	389.49	Calculated Property
P_vap	3.20	kPa	398.48	Calculated Property
P_vap	4.67	kPa	407.47	Calculated Property
P_vap	6.67	kPa	416.46	Calculated Property
P_vap	9.36	kPa	425.44	Calculated Property
P_vap	12.93	kPa	434.43	Calculated Property
P_vap	17.57	kPa	443.42	Calculated Property
P_vap	23.55	kPa	452.41	Calculated Property
P_vap	31.13	kPa	461.40	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρ_l	[900.39; 260.76]	kg/m³	[255.15; 686.90]	ChemSep v8.3 pure component data
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρ_l in kg/m³, T in K
Coefficient A			6.33445e+01
Coefficient B			2.42920e-01
Coefficient C			6.86900e+02
Coefficient D			2.85710e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			255.15
Temperature range, max.			686.90

ρ_l	900.39	kg/m³	255.15	Calculated Property
ρ_l	864.21	kg/m³	303.12	Calculated Property
ρ_l	826.31	kg/m³	351.09	Calculated Property
ρ_l	786.25	kg/m³	399.07	Calculated Property
ρ_l	743.41	kg/m³	447.04	Calculated Property
ρ_l	696.83	kg/m³	495.01	Calculated Property
ρ_l	644.83	kg/m³	542.98	Calculated Property
ρ_l	584.03	kg/m³	590.96	Calculated Property
ρ_l	505.26	kg/m³	638.93	Calculated Property
ρ_l	260.76	kg/m³	686.90	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.02; 0.06]	W/m×K	[505.00; 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			2.20890e-06
Coefficient B			1.47900e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Comment			ChemSep eq 102, VaporThermalConductivity
Temperature range, min.			505.00
Temperature range, max.			1000.00

λ	0.02	W/m×K	505.00	Calculated Property
λ	0.03	W/m×K	560.00	Calculated Property
λ	0.03	W/m×K	615.00	Calculated Property
λ	0.03	W/m×K	670.00	Calculated Property
λ	0.04	W/m×K	725.00	Calculated Property
λ	0.04	W/m×K	780.00	Calculated Property
λ	0.05	W/m×K	835.00	Calculated Property
λ	0.05	W/m×K	890.00	Calculated Property
λ	0.06	W/m×K	945.00	Calculated Property
λ	0.06	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.14; 0.09]	W/m×K	[255.15; 537.00]	ChemSep v8.3 pure component data
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λ in W/m×K, T in K
Coefficient A			1.97420e-01
Coefficient B			-2.07730e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			ChemSep eq 100, LiquidThermalConductivity
Temperature range, min.			255.15
Temperature range, max.			537.00

λ	0.14	W/m×K	255.15	Calculated Property
λ	0.14	W/m×K	286.47	Calculated Property
λ	0.13	W/m×K	317.78	Calculated Property
λ	0.12	W/m×K	349.10	Calculated Property
λ	0.12	W/m×K	380.42	Calculated Property
λ	0.11	W/m×K	411.73	Calculated Property
λ	0.11	W/m×K	443.05	Calculated Property
λ	0.10	W/m×K	474.37	Calculated Property
λ	0.09	W/m×K	505.68	Calculated Property
λ	0.09	W/m×K	537.00	Calculated Property

Similar Compounds

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Chemical Properties of Decanoic acid, methyl ester (CAS 110-42-9)

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