Chemical Properties of 9-Octadecenoic acid, 12-hydroxy-, methyl ester, [R-(Z)]- (CAS 141-24-2)

InChI

InChI=1S/C19H36O3/c1-3-4-5-12-15-18(20)16-13-10-8-6-7-9-11-14-17-19(21)22-2/h10,13,18,20H,3-9,11-12,14-17H2,1-2H3/b13-10-/t18-/m0/s1

InChI Key

XKGDWZQXVZSXAO-GFBZKKKVSA-N

Formula

C19H36O3

SMILES

CCCCCCC(O)CC=CCCCCCCCC(=O)OC

Molecular Weight¹

312.49

CAS

141-24-2

Other Names

• 12-Hydroxy-9-octadecenoic acid methyl ester
• 9-octadecenoic acid, 12-hydroxy-, [R]-, methyl ester
• Flexricin P-1
• Methyl ricinolate
• Ricinoleic acid methyl ester
• [R]-methyl 12-hydroxy-9-octadecenoate
• methyl ricinoleate

• 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_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).
• ρ_l : Liquid Density (kg/m³).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Cheméo can also estimate Critical Volume, Standard Gibbs free energy of formation, Acentric Factor for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
ΔvapH	89.30	kJ/mol	498.00	NIST
ρl	[857.50; 928.50]	kg/m3	[293.16; 383.23]
ρl	928.50	kg/m3	293.16	Measurements and Correlations of the Density, Viscosity, and Vapor Pressure for Methyl Ricinoleate
ρl	921.20	kg/m3	303.17	Measurements and Correlations of the Density, Viscosity, and Vapor Pressure for Methyl Ricinoleate
ρl	916.70	kg/m3	313.33	Measurements and Correlations of the Density, Viscosity, and Vapor Pressure for Methyl Ricinoleate
ρl	910.30	kg/m3	323.05	Measurements and Correlations of the Density, Viscosity, and Vapor Pressure for Methyl Ricinoleate
ρl	904.00	kg/m3	333.25	Measurements and Correlations of the Density, Viscosity, and Vapor Pressure for Methyl Ricinoleate
ρl	895.80	kg/m3	343.32	Measurements and Correlations of the Density, Viscosity, and Vapor Pressure for Methyl Ricinoleate
ρl	883.30	kg/m3	353.06	Measurements and Correlations of the Density, Viscosity, and Vapor Pressure for Methyl Ricinoleate
ρl	875.00	kg/m3	363.38	Measurements and Correlations of the Density, Viscosity, and Vapor Pressure for Methyl Ricinoleate
ρl	865.80	kg/m3	373.26	Measurements and Correlations of the Density, Viscosity, and Vapor Pressure for Methyl Ricinoleate
ρl	857.50	kg/m3	383.23	Measurements and Correlations of the Density, Viscosity, and Vapor Pressure for Methyl Ricinoleate

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[423.06; 996.29]	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			4.53000e-01
Coefficient B			1.81394e+00
Coefficient C			-1.03260e-03
Coefficient D			2.14500e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	423.06	J/mol×K	273.00	Calculated Property
Cp,gas	522.44	J/mol×K	353.78	Calculated Property
Cp,gas	611.32	J/mol×K	434.56	Calculated Property
Cp,gas	690.37	J/mol×K	515.33	Calculated Property
Cp,gas	760.27	J/mol×K	596.11	Calculated Property
Cp,gas	821.70	J/mol×K	676.89	Calculated Property
Cp,gas	875.34	J/mol×K	757.67	Calculated Property
Cp,gas	921.86	J/mol×K	838.44	Calculated Property
Cp,gas	961.96	J/mol×K	919.22	Calculated Property
Cp,gas	996.29	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0027683; 0.0000257]	Pa×s	[386.96; 677.31]	Joback Predicted correlation
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.68024e+01
Coefficient B			4.22285e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc.
Temperature range, min.			386.96
Temperature range, max.			677.31
η	0.0027683	Pa×s	386.96	Calculated Property
η	0.0011953	Pa×s	419.22	Calculated Property
η	0.0005820	Pa×s	451.48	Calculated Property
η	0.0003119	Pa×s	483.74	Calculated Property
η	0.0001807	Pa×s	516.00	Calculated Property
η	0.0001116	Pa×s	548.27	Calculated Property
η	0.0000728	Pa×s	580.53	Calculated Property
η	0.0000496	Pa×s	612.79	Calculated Property
η	0.0000352	Pa×s	645.05	Calculated Property
η	0.0000257	Pa×s	677.31	Calculated Property

Similar Compounds

Find more compounds similar to 9-Octadecenoic acid, 12-hydroxy-, methyl ester, [R-(Z)]-.

Sources

• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Energies of combustion and standard molar enthalpies of formation of ricinoleic acid and methyl ricinoleate
• Measurements and Correlations of the Density, Viscosity, and Vapor Pressure for Methyl Ricinoleate
• Joback Method
• McGowan Method
• NIST Webbook

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