9-Octadecenoic acid (Z)-, methyl ester (CAS 112-62-9)

InChI

InChI=1S/C19H36O2/c1-3-4-5-6-7-8-9-10-11-12-13-14-15-16-17-18-19(20)21-2/h10-11H,3-9,12-18H2,1-2H3/b11-10-

InChI Key

QYDYPVFESGNLHU-KHPPLWFESA-N

Formula

C19H36O2

SMILES

CCCCCCCCC=CCCCCCCCC(=O)OC

Molecular Weight¹

296.49

CAS

112-62-9

Other Names

(Z)-9-Methyl octadecenoate
(Z)-9-Octadecenoic acid methyl ester
(Z)-9-octadecenoic acid, methyl ester
9-Octadecenoic acid (9Z)-, methyl ester
9-octadecenoic acid, methyl ester (Z)
ADJ 100
CIS-9-OCTADECENOIC ACID
Edenor Me 90/95V
Edenor MeTiO5
Emerest 2801
Emery 2301
Emery oleic acid ester 2301
Emery, oleic acid ester
Esterol 112
Exceparl M-OL
Kemester 205
METHYL ESTER
Methyl (9z)-9-octadecenoate
Methyl (Z)-9-octadecenoate
Methyl (Z)-9-oleate
Methyl 9-octadecenoate, cis-
Methyl-cis-oleate
Nissan Unister M 182A
OLEIC ACID
Oleic acid, methyl ester, cis-
Phytorob 926-67
Priolube 1400
Priolube 1403
Unister M 182A
Witconol 2301
cis-9-Octadecenoic acid, methyl ester
cis-9-Octyldecenoic acid, methyl ester
cis-methyl oleate
methyl cis-9-octadecenoate
methyl oleate
oleic 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).
η : Dynamic viscosity (Pa×s).
Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
IE : Ionization energy (eV).
log₁₀WS : Log10 of Water solubility in mol/l.
logP_oct/wat : Octanol/Water partition coefficient.
McVol : McGowan's characteristic volume (ml/mol).
P_c : Critical Pressure (kPa).
P_triple : Triple Point Pressure (kPa).
P_vap : Vapor pressure (kPa).
ρ_l : Liquid Density (kg/m³).
I_np : Non-polar retention indices.
I_p : 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 : 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).
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	[0.9388; 1.0494]
ω	0.9388		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	1.0494		ChemSep v8.3 pure component data Compiled value
Δ_cH°_liquid	[-11887.00; -11832.40]	kJ/mol
Δ_cH°_liquid	-11832.40 ± 1.50	kJ/mol	NIST
Δ_cH°_liquid	-11887.00 ± 12.00	kJ/mol	NIST
Δ_fG°	-117.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
Δ_fH°_gas	-629.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
Δ_fH°_liquid	-727.64	kJ/mol	NIST
Δ_fusH°	49.54	kJ/mol	Joback Calculated Property
Δ_vapH°	[99.60; 107.80]	kJ/mol
Δ_vapH°	107.80 ± 0.60	kJ/mol	NIST
Δ_vapH°	106.20 ± 0.70	kJ/mol	NIST
Δ_vapH°	102.20	kJ/mol	NIST
Δ_vapH°	103.30	kJ/mol	NIST
Δ_vapH°	99.60	kJ/mol	NIST
Δ_vapH°	106.80 ± 1.00	kJ/mol	NIST
IE	8.95	eV	Relay (1.0) Calculated Property
log₁₀WS	-6.30		Relay (1.0) Calculated Property
logP_oct/wat	6.197		Crippen Calculated Property
McVol	281.710	ml/mol	McGowan Calculated Property
P_c	[1278.30; 1280.00]	kPa
P_c	1278.30	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
P_c	1280.00	kPa	ChemSep v8.3 pure component data Compiled value
P_triple	3.98e-07	kPa	ChemSep v8.3 pure component data Compiled value
I_np	[357.70; 2108.90]
I_np	2074.70		NIST
I_np	2072.00		NIST
I_np	2085.00		NIST
I_np	2081.00		NIST
I_np	2081.00		NIST
I_np	2104.00		NIST
I_np	2086.00		NIST
I_np	2085.00		NIST
I_np	2086.00		NIST
I_np	2082.00		NIST
I_np	2103.00		NIST
I_np	2087.00		NIST
I_np	2077.00		NIST
I_np	2082.00		NIST
I_np	2079.00		NIST
I_np	2082.49		NIST
I_np	2079.00		NIST
I_np	2076.00		NIST
I_np	2078.92		NIST
I_np	2073.44		NIST
I_np	2071.63		NIST
I_np	2086.34		NIST
I_np	2072.42		NIST
I_np	2077.28		NIST
I_np	2072.14		NIST
I_np	2108.90		NIST
I_np	2087.00		NIST
I_np	2085.00		NIST
I_np	2106.00		NIST
I_np	2084.00		NIST
I_np	2095.00		NIST
I_np	2074.00		NIST
I_np	2098.10		NIST
I_np	2106.00		NIST
I_np	2085.00		NIST
I_np	2081.00		NIST
I_np	2082.00		NIST
I_np	2085.00		NIST
I_np	2086.00		NIST
I_np	2100.00		NIST
I_np	2045.00		NIST
I_np	2078.00		NIST
I_np	2080.00		NIST
I_np	2079.00		NIST
I_np	2082.00		NIST
I_np	2083.00		NIST
I_np	2101.00		NIST
I_np	2085.00		NIST
I_np	2102.00		NIST
I_np	2084.00		NIST
I_np	2062.00		NIST
I_np	2105.00		NIST
I_np	2081.00		NIST
I_np	2086.00		NIST
I_np	2086.00		NIST
I_np	Outlier 357.70		NIST
I_np	2085.00		NIST
I_np	2081.00		NIST
I_np	2087.00		NIST
I_np	2098.10		NIST
I_np	2080.00		NIST
I_p	[2400.00; 2476.00]
I_p	2472.00		NIST
I_p	2400.00		NIST
I_p	2403.00		NIST
I_p	2426.00		NIST
I_p	2434.00		NIST
I_p	2436.00		NIST
I_p	2435.00		NIST
I_p	2439.00		NIST
I_p	2455.00		NIST
I_p	2429.00		NIST
I_p	2424.00		NIST
I_p	2426.00		NIST
I_p	2433.00		NIST
I_p	2434.00		NIST
I_p	2439.00		NIST
I_p	2452.00		NIST
I_p	2476.00		NIST
I_p	2472.00		NIST
I_p	2439.00		NIST
I_p	2433.00		NIST
T_boil	617.00	K	ChemSep v8.3 pure component data Compiled value
T_c	[764.00; 777.00]	K
T_c	777.00	K	Vapor-liquid critical point measurements of fifteen compounds by the pulse-heating method
T_c	774.09	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
T_c	764.00	K	ChemSep v8.3 pure component data Compiled value
T_fus	293.05	K	ChemSep v8.3 pure component data Compiled value
T_triple	293.05	K	ChemSep v8.3 pure component data Compiled value
U_Qi	11.00		ChemSep v8.3 pure component data Compiled value
U_Ri	13.36		ChemSep v8.3 pure component data Compiled value
V_c	[1.060; 1.092]	m³/kmol
V_c	1.092	m³/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
V_c	1.060	m³/kmol	ChemSep v8.3 pure component data Compiled value
Z_c	0.2140000		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
η	[0.0018974; 0.0086987]	Pa×s	[283.15; 353.15]

η	0.0086987	Pa×s	283.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0074518	Pa×s	288.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0063700	Pa×s	293.15	Group Contribution Model for Predicting Viscosity of Fatty Compounds
η	0.0064499	Pa×s	293.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0056336	Pa×s	298.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0049612	Pa×s	303.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0049220	Pa×s	303.15	Group Contribution Model for Predicting Viscosity of Fatty Compounds
η	0.0044012	Pa×s	308.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0039303	Pa×s	313.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0039390	Pa×s	313.15	Group Contribution Model for Predicting Viscosity of Fatty Compounds
η	0.0035306	Pa×s	318.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0031892	Pa×s	323.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0030970	Pa×s	323.15	Group Contribution Model for Predicting Viscosity of Fatty Compounds
η	0.0028944	Pa×s	328.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0026377	Pa×s	333.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0024720	Pa×s	333.15	Group Contribution Model for Predicting Viscosity of Fatty Compounds
η	0.0024160	Pa×s	338.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0022216	Pa×s	343.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0020540	Pa×s	343.15	Group Contribution Model for Predicting Viscosity of Fatty Compounds
η	0.0020499	Pa×s	348.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0018974	Pa×s	353.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
Δ_vapH	[77.20; 106.20]	kJ/mol	[293.00; 498.00]

Δ_vapH	84.39	kJ/mol	293.00	NIST
Δ_vapH	106.20	kJ/mol	298.15	the vaporization enthaplies and vapor pressures of a series of unstaurated fatty acid methyl esters by correlation gas chromatography
Δ_vapH	86.30	kJ/mol	425.00	NIST
Δ_vapH	86.70	kJ/mol	429.50	NIST
Δ_vapH	83.00	kJ/mol	457.00	NIST
Δ_vapH	77.20	kJ/mol	498.00	NIST
Δ_vapH	77.20	kJ/mol	498.00	NIST
P_vap	[1.99e-06; 2.42e-04]	kPa	[303.15; 343.15]

P_vap	1.99e-06	kPa	303.15	The Use of Antioxidants to Improve Vapor Pressure Measurements on Compounds with Oxidative Instability: Methyl Oleate with tert-Butylhydroquinone
P_vap	8.13e-06	kPa	313.15	The Use of Antioxidants to Improve Vapor Pressure Measurements on Compounds with Oxidative Instability: Methyl Oleate with tert-Butylhydroquinone
P_vap	2.83e-05	kPa	323.15	The Use of Antioxidants to Improve Vapor Pressure Measurements on Compounds with Oxidative Instability: Methyl Oleate with tert-Butylhydroquinone
P_vap	3.06e-05	kPa	323.15	The Use of Antioxidants to Improve Vapor Pressure Measurements on Compounds with Oxidative Instability: Methyl Oleate with tert-Butylhydroquinone
P_vap	2.83e-05	kPa	323.15	The Use of Antioxidants to Improve Vapor Pressure Measurements on Compounds with Oxidative Instability: Methyl Oleate with tert-Butylhydroquinone
P_vap	3.09e-05	kPa	323.15	The Use of Antioxidants to Improve Vapor Pressure Measurements on Compounds with Oxidative Instability: Methyl Oleate with tert-Butylhydroquinone
P_vap	2.80e-05	kPa	323.15	The Use of Antioxidants to Improve Vapor Pressure Measurements on Compounds with Oxidative Instability: Methyl Oleate with tert-Butylhydroquinone
P_vap	9.19e-05	kPa	333.15	The Use of Antioxidants to Improve Vapor Pressure Measurements on Compounds with Oxidative Instability: Methyl Oleate with tert-Butylhydroquinone
P_vap	2.42e-04	kPa	343.15	The Use of Antioxidants to Improve Vapor Pressure Measurements on Compounds with Oxidative Instability: Methyl Oleate with tert-Butylhydroquinone
c_sound,fluid	[1250.00; 1462.00]	m/s	[278.15; 338.15]

c_sound,fluid	1462.00	m/s	278.15	Density and Speed of Sound Measurements on Five Fatty Acid Methyl Esters at 83 kPa and Temperatures from (278.15 to 338.15) K
c_sound,fluid	1425.00	m/s	288.15	Density and Speed of Sound Measurements on Five Fatty Acid Methyl Esters at 83 kPa and Temperatures from (278.15 to 338.15) K
c_sound,fluid	1389.00	m/s	298.15	Density and Speed of Sound Measurements on Five Fatty Acid Methyl Esters at 83 kPa and Temperatures from (278.15 to 338.15) K
c_sound,fluid	1353.00	m/s	308.15	Density and Speed of Sound Measurements on Five Fatty Acid Methyl Esters at 83 kPa and Temperatures from (278.15 to 338.15) K
c_sound,fluid	1318.00	m/s	318.15	Density and Speed of Sound Measurements on Five Fatty Acid Methyl Esters at 83 kPa and Temperatures from (278.15 to 338.15) K
c_sound,fluid	1284.00	m/s	328.15	Density and Speed of Sound Measurements on Five Fatty Acid Methyl Esters at 83 kPa and Temperatures from (278.15 to 338.15) K
c_sound,fluid	1250.00	m/s	338.15	Density and Speed of Sound Measurements on Five Fatty Acid Methyl Esters at 83 kPa and Temperatures from (278.15 to 338.15) K

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
T_boilr	491.70	K	2.70	NIST

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
270.00	490.00	892.3
270.00	990.00	892.6
270.00	1990.00	893.2
270.00	2990.00	893.7
270.00	3990.00	894.3
270.00	4990.00	894.8
270.00	9990.00	897.4
270.00	19990.00	902.4
270.00	29990.00	907.1
270.00	39990.00	911.7
270.00	49830.00	915.9
290.00	490.00	877.7
290.00	1000.00	878.0
290.00	2000.00	878.6
290.00	3000.00	879.2
290.00	3990.00	879.8
290.00	4990.00	880.4
290.00	10000.00	883.3
290.00	19990.00	888.7
290.00	29990.00	893.8
290.00	39990.00	898.7
290.00	49960.00	903.4
310.00	490.00	863.3
310.00	990.00	863.6
310.00	2000.00	864.3
310.00	3000.00	865.0
310.00	4000.00	865.6
310.00	5000.00	866.2
310.00	9990.00	869.3
310.00	20000.00	875.3
310.00	29990.00	880.8
310.00	39990.00	886.1
310.00	49990.00	891.1
330.00	500.00	849.0
330.00	1000.00	849.3
330.00	2000.00	850.1
330.00	3000.00	850.8
330.00	3990.00	851.5
330.00	4990.00	852.2
330.00	10000.00	855.6
330.00	19990.00	862.0
330.00	29990.00	868.0
330.00	39990.00	873.6
330.00	49990.00	878.9
350.00	500.00	834.6
350.00	990.00	835.0
350.00	2000.00	835.8
350.00	2990.00	836.6
350.00	3990.00	837.3
350.00	5000.00	838.1
350.00	9990.00	841.8
350.00	20000.00	848.8
350.00	30000.00	855.3
350.00	40000.00	861.3
350.00	49980.00	867.0
370.00	500.00	820.1
370.00	990.00	820.6
370.00	1990.00	821.4
370.00	2990.00	822.3
370.00	3990.00	823.2
370.00	5010.00	824.0
370.00	10000.00	828.1
370.00	20010.00	835.7
370.00	29990.00	842.6
370.00	39990.00	849.1
370.00	49970.00	855.1
390.00	490.00	805.7
390.00	990.00	806.2
390.00	2000.00	807.1
390.00	3000.00	808.1
390.00	3990.00	809.0
390.00	5000.00	810.0
390.00	10000.00	814.5
390.00	19990.00	822.7
390.00	29980.00	830.2
390.00	40000.00	837.2
390.00	49990.00	843.6
410.00	490.00	791.0
410.00	990.00	791.6
410.00	2000.00	792.7
410.00	3000.00	793.7
410.00	3990.00	794.8
410.00	5000.00	795.8
410.00	10000.00	800.8
410.00	20000.00	809.8
410.00	30000.00	817.9
410.00	39990.00	825.3
410.00	50000.00	832.2
430.00	500.00	776.2
430.00	1000.00	776.8
430.00	1990.00	778.0
430.00	3000.00	779.2
430.00	3990.00	780.3
430.00	4990.00	781.5
430.00	9990.00	786.9
430.00	19990.00	796.7
430.00	29990.00	805.5
430.00	39990.00	813.5
430.00	49990.00	820.8
450.00	490.00	761.2
450.00	1000.00	761.9
450.00	1990.00	763.2
450.00	2990.00	764.5
450.00	3990.00	765.8
450.00	5000.00	767.1
450.00	10000.00	773.1
450.00	20000.00	783.9
450.00	29990.00	793.3
450.00	39990.00	801.9
450.00	50010.00	809.7
470.00	490.00	746.3
470.00	990.00	747.0
470.00	2000.00	748.6
470.00	2990.00	750.0
470.00	3990.00	751.5
470.00	5010.00	752.9
470.00	10000.00	759.5
470.00	19990.00	771.2
470.00	29990.00	781.5
470.00	39990.00	790.6
470.00	49970.00	798.8
Reference

Speed of sound, m/s

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
101.30	283.15	1443.2
101.30	363.15	1170.9
101.30	303.15	1370.5
101.30	383.15	1108.9
101.30	323.15	1301.9
101.30	393.15	1078.5
101.30	343.15	1235.8
10000.00	283.15	1486.1
10000.00	363.15	1228.2
10000.00	303.15	1416.8
10000.00	383.15	1170.4
10000.00	323.15	1352.1
10000.00	393.15	1142.4
10000.00	343.15	1289.0
20000.00	363.15	1280.6
20000.00	283.15	1526.5
20000.00	303.15	1460.0
20000.00	383.15	1226.5
20000.00	323.15	1397.7
20000.00	393.15	1200.0
20000.00	343.15	1338.1
30000.00	363.15	1329.3
30000.00	303.15	1502.0
30000.00	283.15	1564.5
30000.00	383.15	1277.8
30000.00	323.15	1441.1
30000.00	393.15	1252.0
30000.00	343.15	1383.7
40000.00	303.15	1540.9
40000.00	383.15	1324.6
40000.00	283.15	1600.5
40000.00	363.15	1374.0
40000.00	323.15	1482.3
40000.00	393.15	1299.9
40000.00	343.15	1426.0
50000.00	303.15	1578.3
50000.00	383.15	1367.4
50000.00	323.15	1521.2
50000.00	283.15	1634.5
50000.00	363.15	1414.4
50000.00	393.15	1343.8
50000.00	343.15	1466.7
60000.00	303.15	1613.7
60000.00	383.15	1407.7
60000.00	323.15	1558.5
60000.00	393.15	1384.5
60000.00	283.15	1668.6
60000.00	363.15	1454.6
60000.00	343.15	1505.4
70000.00	283.15	1701.0
70000.00	383.15	1446.1
70000.00	323.15	1593.5
70000.00	363.15	1492.2
70000.00	393.15	1423.6
70000.00	303.15	1647.0
70000.00	343.15	1542.2
80000.00	303.15	1678.8
80000.00	363.15	1527.5
80000.00	383.15	1481.7
80000.00	283.15	1732.7
80000.00	323.15	1627.2
80000.00	393.15	1460.2
80000.00	343.15	1575.4
90000.00	303.15	1709.5
90000.00	383.15	1516.9
90000.00	363.15	1563.5
90000.00	323.15	1659.3
90000.00	393.15	1495.7
90000.00	283.15	1762.7
90000.00	343.15	1609.4
100000.00	383.15	1550.2
100000.00	363.15	1597.2
100000.00	303.15	1739.7
100000.00	323.15	1690.2
100000.00	393.15	1529.7
100000.00	283.15	1790.8
100000.00	343.15	1641.6
110000.00	283.15	1819.3
110000.00	363.15	1629.1
110000.00	383.15	1583.4
110000.00	323.15	1719.3
110000.00	303.15	1768.5
110000.00	393.15	1562.8
110000.00	343.15	1672.6
120000.00	323.15	1747.7
120000.00	283.15	1846.0
120000.00	363.15	1659.3
120000.00	303.15	1796.4
120000.00	383.15	1615.8
120000.00	393.15	1593.9
120000.00	343.15	1701.9
130000.00	323.15	1775.4
130000.00	393.15	1624.5
130000.00	283.15	1872.5
130000.00	363.15	1687.5
130000.00	303.15	1821.2
130000.00	383.15	1645.9
130000.00	343.15	1729.9
140000.00	393.15	1654.6
140000.00	363.15	1715.4
140000.00	303.15	1848.1
140000.00	283.15	1897.8
140000.00	323.15	1801.6
140000.00	383.15	1674.2
140000.00	343.15	1757.3
150000.00	363.15	1741.8
150000.00	303.15	1874.2
150000.00	393.15	1683.0
150000.00	283.15	1923.3
150000.00	383.15	1701.5
150000.00	323.15	1827.1
150000.00	343.15	1783.8
160000.00	323.15	1853.0
160000.00	383.15	1729.4
160000.00	393.15	1710.3
160000.00	283.15	1947.8
160000.00	303.15	1899.0
160000.00	363.15	1766.9
160000.00	343.15	1809.7
170000.00	393.15	1736.2
170000.00	323.15	1878.4
170000.00	303.15	1923.1
170000.00	383.15	1755.3
170000.00	363.15	1793.1
170000.00	283.15	1971.2
170000.00	343.15	1834.3
180000.00	393.15	1761.2
180000.00	283.15	1994.3
180000.00	323.15	1902.6
180000.00	363.15	1817.7
180000.00	383.15	1781.4
180000.00	303.15	1947.0
180000.00	343.15	1859.7
190000.00	393.15	1785.3
190000.00	383.15	1805.7
190000.00	303.15	1970.3
190000.00	283.15	2016.8
190000.00	363.15	1841.2
190000.00	323.15	1925.8
190000.00	343.15	1883.4
200000.00	283.15	2036.4
200000.00	323.15	1949.2
200000.00	303.15	1992.7
200000.00	343.15	1905.8
200000.00	363.15	1864.9
200000.00	383.15	1828.3
200000.00	393.15	1809.7
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[444.96; 1122.36]	J/mol×K	[300.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
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			3.29970e+02
Coefficient B			9.71600e+02
Coefficient C			1.64560e+03
Coefficient D			6.74480e+02
Coefficient E			7.48000e+02
Temperature range, min.			300.00
Temperature range, max.			1500.00

C_p,gas	444.96	J/mol×K	300.00	Calculated Property
C_p,gas	597.40	J/mol×K	433.33	Calculated Property
C_p,gas	721.26	J/mol×K	566.67	Calculated Property
C_p,gas	819.39	J/mol×K	700.00	Calculated Property
C_p,gas	899.03	J/mol×K	833.33	Calculated Property
C_p,gas	963.91	J/mol×K	966.67	Calculated Property
C_p,gas	1016.59	J/mol×K	1100.00	Calculated Property
C_p,gas	1059.30	J/mol×K	1233.33	Calculated Property
C_p,gas	1094.02	J/mol×K	1366.67	Calculated Property
C_p,gas	1122.36	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
C_p,liquid	[595.95; 896.58]	J/mol×K	[293.05; 617.00]	ChemSep v8.3 pure component data Compiled value
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			3.24000e+02
Coefficient B			9.28000e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			293.05
Temperature range, max.			617.00

C_p,liquid	595.95	J/mol×K	293.05	Calculated Property
C_p,liquid	629.35	J/mol×K	329.04	Calculated Property
C_p,liquid	662.76	J/mol×K	365.04	Calculated Property
C_p,liquid	696.16	J/mol×K	401.03	Calculated Property
C_p,liquid	729.56	J/mol×K	437.03	Calculated Property
C_p,liquid	762.96	J/mol×K	473.02	Calculated Property
C_p,liquid	796.37	J/mol×K	509.02	Calculated Property
C_p,liquid	829.77	J/mol×K	545.01	Calculated Property
C_p,liquid	863.17	J/mol×K	581.01	Calculated Property
C_p,liquid	896.58	J/mol×K	617.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0060769; 0.0001677]	Pa×s	[293.05; 617.00]	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			-1.19410e+01
Coefficient B			2.00380e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			293.05
Temperature range, max.			617.00

η	0.0060769	Pa×s	293.05	Calculated Property
η	0.0028763	Pa×s	329.04	Calculated Property
η	0.0015778	Pa×s	365.04	Calculated Property
η	0.0009640	Pa×s	401.03	Calculated Property
η	0.0006388	Pa×s	437.03	Calculated Property
η	0.0004506	Pa×s	473.02	Calculated Property
η	0.0003340	Pa×s	509.02	Calculated Property
η	0.0002575	Pa×s	545.01	Calculated Property
η	0.0002051	Pa×s	581.01	Calculated Property
η	0.0001677	Pa×s	617.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Δ_vapH	[100.78; 0.00]	kJ/mol	[293.05; 764.00]	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 Δ_vapH in kJ/mol, T in K
Coefficient A			1.22000e+02
Coefficient B			3.95000e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			7.64000e+02
Temperature range, min.			293.05
Temperature range, max.			764.00

Δ_vapH	100.78	kJ/mol	293.05	Calculated Property
Δ_vapH	96.20	kJ/mol	345.38	Calculated Property
Δ_vapH	91.25	kJ/mol	397.71	Calculated Property
Δ_vapH	85.86	kJ/mol	450.03	Calculated Property
Δ_vapH	79.90	kJ/mol	502.36	Calculated Property
Δ_vapH	73.16	kJ/mol	554.69	Calculated Property
Δ_vapH	65.30	kJ/mol	607.02	Calculated Property
Δ_vapH	55.63	kJ/mol	659.34	Calculated Property
Δ_vapH	42.31	kJ/mol	711.67	Calculated Property
Δ_vapH	0.00	kJ/mol	764.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
P_vap	[1.33; 202.66]	kPa	[480.72; 693.87]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is P_vap in kPa, T in K
Coefficient A			1.42421e+01
Coefficient B			-5.28740e+03
Coefficient C			-1.01816e+02
Temperature range, min.			480.72
Temperature range, max.			693.87

P_vap	1.33	kPa	480.72	Calculated Property
P_vap	3.03	kPa	504.40	Calculated Property
P_vap	6.29	kPa	528.09	Calculated Property
P_vap	12.08	kPa	551.77	Calculated Property
P_vap	21.73	kPa	575.45	Calculated Property
P_vap	36.98	kPa	599.14	Calculated Property
P_vap	59.96	kPa	622.82	Calculated Property
P_vap	93.22	kPa	646.50	Calculated Property
P_vap	139.69	kPa	670.19	Calculated Property
P_vap	202.66	kPa	693.87	Calculated Property
P_vap	[3.98e-07; 1269.45]	kPa	[293.05; 764.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is P_vap in kPa, T in K
Coefficient A			1.80582e+02
Coefficient B			-1.91530e+04
Coefficient C			-2.29890e+01
Coefficient D			7.27690e-06
Coefficient E			2.00000e+00
Temperature range, min.			293.05
Temperature range, max.			764.00

P_vap	3.98e-07	kPa	293.05	Calculated Property
P_vap	2.32e-04	kPa	345.38	Calculated Property
P_vap	0.02	kPa	397.71	Calculated Property
P_vap	0.39	kPa	450.03	Calculated Property
P_vap	3.73	kPa	502.36	Calculated Property
P_vap	20.86	kPa	554.69	Calculated Property
P_vap	80.20	kPa	607.02	Calculated Property
P_vap	237.45	kPa	659.34	Calculated Property
P_vap	585.35	kPa	711.67	Calculated Property
P_vap	1269.45	kPa	764.00	Calculated Property
P_vap	[3.84e-07; 1269.01]	kPa	[293.05; 764.00]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is P_vap in kPa, T in K
Coefficient A			1.94662e+02
Coefficient B			-1.98622e+04
Coefficient C			-2.50644e+01
Coefficient D			8.34958e-06
Coefficient E			0.00000e+00
Temperature range, min.			293.05
Temperature range, max.			764.00

P_vap	3.84e-07	kPa	293.05	Calculated Property
P_vap	2.38e-04	kPa	345.38	Calculated Property
P_vap	0.02	kPa	397.71	Calculated Property
P_vap	0.40	kPa	450.03	Calculated Property
P_vap	3.85	kPa	502.36	Calculated Property
P_vap	21.24	kPa	554.69	Calculated Property
P_vap	80.69	kPa	607.02	Calculated Property
P_vap	237.04	kPa	659.34	Calculated Property
P_vap	582.90	kPa	711.67	Calculated Property
P_vap	1269.01	kPa	764.00	Calculated Property
P_vap	[0.14; 2.01]	kPa	[428.72; 485.22]	NIST
Equation			ln(Y) = A + B/(T + C) Y is P_vap in kPa, T in K
Coefficient A			1.66366e+01
Coefficient B			-6.27036e+03
Coefficient C			-9.18220e+01
Reference			Rose and Schrodt, 1964
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			428.72
Temperature range, max.			485.22

P_vap	0.14	kPa	428.72	Calculated Property
P_vap	0.19	kPa	435.00	Calculated Property
P_vap	0.27	kPa	441.28	Calculated Property
P_vap	0.37	kPa	447.55	Calculated Property
P_vap	0.50	kPa	453.83	Calculated Property
P_vap	0.68	kPa	460.11	Calculated Property
P_vap	0.90	kPa	466.39	Calculated Property
P_vap	1.19	kPa	472.66	Calculated Property
P_vap	1.55	kPa	478.94	Calculated Property
P_vap	2.01	kPa	485.22	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρ_l	[873.80; 279.71]	kg/m³	[293.05; 764.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρ_l in kg/m³, T in K
Coefficient A			7.33956e+01
Coefficient B			2.62400e-01
Coefficient C			7.64000e+02
Coefficient D			3.32470e-01
Temperature range, min.			293.05
Temperature range, max.			764.00

ρ_l	873.80	kg/m³	293.05	Calculated Property
ρ_l	836.40	kg/m³	345.38	Calculated Property
ρ_l	797.54	kg/m³	397.71	Calculated Property
ρ_l	756.87	kg/m³	450.03	Calculated Property
ρ_l	713.83	kg/m³	502.36	Calculated Property
ρ_l	667.58	kg/m³	554.69	Calculated Property
ρ_l	616.65	kg/m³	607.02	Calculated Property
ρ_l	558.14	kg/m³	659.34	Calculated Property
ρ_l	484.16	kg/m³	711.67	Calculated Property
ρ_l	279.71	kg/m³	764.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ_gas	[0.02; 0.05]	W/m×K	[617.00; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λ_gas in W/m×K, T in K
Coefficient A			1.41600e-04
Coefficient B			9.31000e-01
Coefficient C			7.99400e+02
Coefficient D			0.00000e+00
Temperature range, min.			617.00
Temperature range, max.			1000.00

λ_gas	0.02	W/m×K	617.00	Calculated Property
λ_gas	0.03	W/m×K	659.56	Calculated Property
λ_gas	0.03	W/m×K	702.11	Calculated Property
λ_gas	0.03	W/m×K	744.67	Calculated Property
λ_gas	0.03	W/m×K	787.22	Calculated Property
λ_gas	0.04	W/m×K	829.78	Calculated Property
λ_gas	0.04	W/m×K	872.33	Calculated Property
λ_gas	0.04	W/m×K	914.89	Calculated Property
λ_gas	0.05	W/m×K	957.44	Calculated Property
λ_gas	0.05	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ_liquid	[0.10; 0.06]	W/m×K	[293.05; 609.20]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λ_liquid in W/m×K, T in K
Coefficient A			1.40150e-01
Coefficient B			-1.33160e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			293.05
Temperature range, max.			609.20

λ_liquid	0.10	W/m×K	293.05	Calculated Property
λ_liquid	0.10	W/m×K	328.18	Calculated Property
λ_liquid	0.09	W/m×K	363.31	Calculated Property
λ_liquid	0.09	W/m×K	398.43	Calculated Property
λ_liquid	0.08	W/m×K	433.56	Calculated Property
λ_liquid	0.08	W/m×K	468.69	Calculated Property
λ_liquid	0.07	W/m×K	503.82	Calculated Property
λ_liquid	0.07	W/m×K	538.94	Calculated Property
λ_liquid	0.06	W/m×K	574.07	Calculated Property
λ_liquid	0.06	W/m×K	609.20	Calculated Property

Similar Compounds

7-Hexadecenoic acid, methyl ester, (Z)-.

9-Octadecenoic acid, methyl ester, (E)-.

Find more compounds similar to 9-Octadecenoic acid (Z)-, methyl ester.

Mixtures

Sources

KDB Vapor Pressure Data
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
Vapor liquid equilibria and densities of CO2 with four unsaturated fatty acid esters at elevated pressures
Liquid-liquid equilibria for mixtures containing water, methanol, fatty acid methyl esters, and glycerol
Vapor-liquid critical point measurements of fifteen compounds by the pulse-heating method
Phase equilibria of triolein to biodiesel reactor systems
the vaporization enthaplies and vapor pressures of a series of unstaurated fatty acid methyl esters by correlation gas chromatography
The Use of Antioxidants to Improve Vapor Pressure Measurements on Compounds with Oxidative Instability: Methyl Oleate with tert-Butylhydroquinone
Experimental Measurements and Modeling Study of Liquid-Liquid Equilibrium [(Water + Methyl Oleate + Model Molecules of Tar Issued from the Biomass Gasification Process (Benzene, Toluene, Phenol, Thiophene, and Pyridine)]
Phase Equilibria for the Ternary System Methyl Oleate + Tocopherol + Supercritical CO2
Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
Compressed-Liquid Density Measurements of Methyl Oleate and Methyl Linoleate
Article Ternary Liquid Liquid Equilibrium of Biodiesel Compounds for Systems Consisting of a Methyl Ester + Glycerin + Water
Speed of Sound, Density, and Derivative Properties of Methyl Oleate and Methyl Linoleate under High Pressure
Group Contribution Model for Predicting Viscosity of Fatty Compounds
Viscosities of Fatty Mixtures: Experimental Data and Prediction
Density and Speed of Sound Measurements on Five Fatty Acid Methyl Esters at 83 kPa and Temperatures from (278.15 to 338.15) K
Joback Method
KDB
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure

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Chemical Properties of 9-Octadecenoic acid (Z)-, methyl ester (CAS 112-62-9)

Contents