Chemical Properties of 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).
• 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_vap : Vapor pressure (kPa).
• 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).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

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

Physical Properties

Property	Value	Unit	Source
ω	0.8479		Relay (1.0) Calculated Property
ΔcH°liquid	[-11887.00; -11832.40]	kJ/mol
ΔcH°liquid	-11832.40 ± 1.50	kJ/mol	NIST
ΔcH°liquid	-11887.00 ± 12.00	kJ/mol	NIST
ΔfG°	-121.05	kJ/mol	Joback Calculated Property
ΔfH°gas	-681.74	kJ/mol	Relay (1.0) Calculated Property
ΔfH°liquid	-727.64	kJ/mol	NIST
ΔfusH°	49.54	kJ/mol	Joback Calculated Property
ΔvapH°	[99.60; 107.80]	kJ/mol
ΔvapH°	107.80 ± 0.60	kJ/mol	NIST
ΔvapH°	106.20 ± 0.70	kJ/mol	NIST
ΔvapH°	102.20	kJ/mol	NIST
ΔvapH°	103.30	kJ/mol	NIST
ΔvapH°	99.60	kJ/mol	NIST
ΔvapH°	106.80 ± 1.00	kJ/mol	NIST
IE	8.95	eV	Relay (1.0) Calculated Property
log10WS	-6.30		Relay (1.0) Calculated Property
logPoct/wat	6.197		Crippen Calculated Property
McVol	281.710	ml/mol	McGowan Calculated Property
Pc	1122.31	kPa	Joback Calculated Property
Inp	[357.70; 2108.90]
Inp	2074.70		NIST
Inp	2072.00		NIST
Inp	2085.00		NIST
Inp	2081.00		NIST
Inp	2081.00		NIST
Inp	2104.00		NIST
Inp	2086.00		NIST
Inp	2085.00		NIST
Inp	2086.00		NIST
Inp	2082.00		NIST
Inp	2103.00		NIST
Inp	2087.00		NIST
Inp	2077.00		NIST
Inp	2082.00		NIST
Inp	2079.00		NIST
Inp	2082.49		NIST
Inp	2079.00		NIST
Inp	2076.00		NIST
Inp	2078.92		NIST
Inp	2073.44		NIST
Inp	2071.63		NIST
Inp	2086.34		NIST
Inp	2072.42		NIST
Inp	2077.28		NIST
Inp	2072.14		NIST
Inp	2108.90		NIST
Inp	2087.00		NIST
Inp	2085.00		NIST
Inp	2106.00		NIST
Inp	2084.00		NIST
Inp	2095.00		NIST
Inp	2074.00		NIST
Inp	2098.10		NIST
Inp	2106.00		NIST
Inp	2085.00		NIST
Inp	2081.00		NIST
Inp	2082.00		NIST
Inp	2085.00		NIST
Inp	2086.00		NIST
Inp	2100.00		NIST
Inp	2045.00		NIST
Inp	2078.00		NIST
Inp	2080.00		NIST
Inp	2079.00		NIST
Inp	2082.00		NIST
Inp	2083.00		NIST
Inp	2101.00		NIST
Inp	2085.00		NIST
Inp	2102.00		NIST
Inp	2084.00		NIST
Inp	2062.00		NIST
Inp	2105.00		NIST
Inp	2081.00		NIST
Inp	2086.00		NIST
Inp	2086.00		NIST
Inp	Outlier 357.70		NIST
Inp	2085.00		NIST
Inp	2081.00		NIST
Inp	2087.00		NIST
Inp	2098.10		NIST
Inp	2080.00		NIST
I	[2400.00; 2476.00]
I	2472.00		NIST
I	2400.00		NIST
I	2403.00		NIST
I	2426.00		NIST
I	2434.00		NIST
I	2436.00		NIST
I	2435.00		NIST
I	2439.00		NIST
I	2455.00		NIST
I	2429.00		NIST
I	2424.00		NIST
I	2426.00		NIST
I	2433.00		NIST
I	2434.00		NIST
I	2439.00		NIST
I	2452.00		NIST
I	2476.00		NIST
I	2472.00		NIST
I	2439.00		NIST
I	2433.00		NIST
Tboil	585.22	K	Relay (1.0) Calculated Property
Tc	777.00	K	Vapor-liquid critical point measurements of fifteen compounds by the pulse-heating method
Tfus	279.03	K	Relay (1.0) Calculated Property
Vc	1.068	m3/kmol	Relay (1.0) Calculated Property

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
ΔvapH	[77.20; 106.20]	kJ/mol	[293.00; 498.00]
ΔvapH	84.39	kJ/mol	293.00	NIST
ΔvapH	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
ΔvapH	86.30	kJ/mol	425.00	NIST
ΔvapH	86.70	kJ/mol	429.50	NIST
ΔvapH	83.00	kJ/mol	457.00	NIST
ΔvapH	77.20	kJ/mol	498.00	NIST
ΔvapH	77.20	kJ/mol	498.00	NIST
Pvap	[1.99e-06; 2.42e-04]	kPa	[303.15; 343.15]
Pvap	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
Pvap	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
Pvap	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
Pvap	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
Pvap	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
Pvap	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
Pvap	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
Pvap	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
Pvap	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
csound,fluid	[1250.00; 1462.00]	m/s	[278.15; 338.15]
csound,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
csound,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
csound,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
csound,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
csound,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
csound,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
csound,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
Tboilr	491.70	K	2.70	NIST

Datasets

1. Mass density, kg/m3 (1)
2. Speed of sound, m/s (1)

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
Cp,gas	[410.88; 977.08]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			-3.15600e+00
Coefficient B			1.77404e+00
Coefficient C			-9.99000e-04
Coefficient D			2.05200e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	410.88	J/mol×K	273.00	Calculated Property
Cp,gas	508.51	J/mol×K	353.78	Calculated Property
Cp,gas	595.95	J/mol×K	434.56	Calculated Property
Cp,gas	673.85	J/mol×K	515.33	Calculated Property
Cp,gas	742.84	J/mol×K	596.11	Calculated Property
Cp,gas	803.59	J/mol×K	676.89	Calculated Property
Cp,gas	856.74	J/mol×K	757.67	Calculated Property
Cp,gas	902.94	J/mol×K	838.44	Calculated Property
Cp,gas	942.84	J/mol×K	919.22	Calculated Property
Cp,gas	977.08	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[480.72; 693.87]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap 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
Pvap	1.33	kPa	480.72	Calculated Property
Pvap	3.03	kPa	504.40	Calculated Property
Pvap	6.29	kPa	528.09	Calculated Property
Pvap	12.08	kPa	551.77	Calculated Property
Pvap	21.73	kPa	575.45	Calculated Property
Pvap	36.98	kPa	599.14	Calculated Property
Pvap	59.96	kPa	622.82	Calculated Property
Pvap	93.22	kPa	646.50	Calculated Property
Pvap	139.69	kPa	670.19	Calculated Property
Pvap	202.66	kPa	693.87	Calculated Property
Pvap	[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 Pvap 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
Pvap	3.84e-07	kPa	293.05	Calculated Property
Pvap	2.38e-04	kPa	345.38	Calculated Property
Pvap	0.02	kPa	397.71	Calculated Property
Pvap	0.40	kPa	450.03	Calculated Property
Pvap	3.85	kPa	502.36	Calculated Property
Pvap	21.24	kPa	554.69	Calculated Property
Pvap	80.69	kPa	607.02	Calculated Property
Pvap	237.04	kPa	659.34	Calculated Property
Pvap	582.90	kPa	711.67	Calculated Property
Pvap	1269.01	kPa	764.00	Calculated Property
Pvap	[0.14; 2.01]	kPa	[428.72; 485.22]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap 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
Temperature range, min.			428.72
Temperature range, max.			485.22
Pvap	0.14	kPa	428.72	Calculated Property
Pvap	0.19	kPa	435.00	Calculated Property
Pvap	0.27	kPa	441.28	Calculated Property
Pvap	0.37	kPa	447.55	Calculated Property
Pvap	0.50	kPa	453.83	Calculated Property
Pvap	0.68	kPa	460.11	Calculated Property
Pvap	0.90	kPa	466.39	Calculated Property
Pvap	1.19	kPa	472.66	Calculated Property
Pvap	1.55	kPa	478.94	Calculated Property
Pvap	2.01	kPa	485.22	Calculated Property

Similar Compounds

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

Mixtures

• 9-Octadecenoic acid (Z)-, methyl ester + Methyl Alcohol
• Glycerin + 9-Octadecenoic acid (Z)-, methyl ester
• 9-Octadecenoic acid (Z)-, methyl ester + Methyl Alcohol + Water
• Glycerin + 9-Octadecenoic acid (Z)-, methyl ester + Methyl Alcohol
• Carbon dioxide + 9-Octadecenoic acid (Z)-, methyl ester
• 9-Octadecenoic acid (Z)-, methyl ester + Water
• Benzene + 9-Octadecenoic acid (Z)-, methyl ester + Water
• Toluene + 9-Octadecenoic acid (Z)-, methyl ester + Water
• 9-Octadecenoic acid (Z)-, methyl ester + Phenol + Water
• Thiophene + 9-Octadecenoic acid (Z)-, methyl ester + Water
• Pyridine + 9-Octadecenoic acid (Z)-, methyl ester + Water
• Glycerin + 9-Octadecenoic acid (Z)-, methyl ester + Water
• 9-Octadecenoic acid (Z)-, methyl ester + Hexadecanoic acid, methyl ester + Methyl tetradecanoate

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• 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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