Chemical Properties of Dodecanoic acid, methyl ester (CAS 111-82-0)

InChI

InChI=1S/C13H26O2/c1-3-4-5-6-7-8-9-10-11-12-13(14)15-2/h3-12H2,1-2H3

InChI Key

UQDUPQYQJKYHQI-UHFFFAOYSA-N

Formula

C13H26O2

SMILES

CCCCCCCCCCCC(=O)OC

Molecular Weight¹

214.34

CAS

111-82-0

Other Names

• Lauric acid, methyl ester
• Metholene 2296
• Methyl dodecanoate
• Methyl dodecylate
• Methyl laurate
• Methyl laurinate
• Methyl n-dodecanoate
• NSC 5027
• Uniphat A40

• 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_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_subH : Enthalpy of sublimation at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• 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).
• 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 : Liquid thermal conductivity (W/m×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
ΔcH°liquid	[-8137.80; -8117.00]	kJ/mol
ΔcH°liquid	-8117.00 ± 0.40	kJ/mol	NIST
ΔcH°liquid	-8137.80 ± 1.60	kJ/mol	NIST
ΔfG°	-175.34	kJ/mol	Joback Calculated Property
ΔfH°gas	-556.45	kJ/mol	Joback Calculated Property
ΔfusH°	43.15	kJ/mol	Heat Ca...
ΔvapH°	[76.50; 77.20]	kJ/mol
ΔvapH°	77.17	kJ/mol	NIST
ΔvapH°	76.60 ± 0.40	kJ/mol	NIST
ΔvapH°	76.80	kJ/mol	NIST
ΔvapH°	76.50 ± 0.70	kJ/mol	NIST
ΔvapH°	77.17 ± 0.56	kJ/mol	NIST
ΔvapH°	77.20 ± 0.60	kJ/mol	NIST
log10WS	[-4.69; -4.69]
log10WS	-4.69		Aq. Sol...
log10WS	-4.69		Estimat...
logPoct/wat	4.080		Crippen Calculated Property
McVol	201.470	ml/mol	McGowan Calculated Property
Pc	1707.53	kPa	Joback Calculated Property
Inp	[256.90; 1533.00]
Inp	1514.90		NIST
Inp	1510.00		NIST
Inp	1518.00		NIST
Inp	1508.00		NIST
Inp	1513.00		NIST
Inp	1513.00		NIST
Inp	1527.00		NIST
Inp	1525.00		NIST
Inp	1526.00		NIST
Inp	1527.00		NIST
Inp	1526.00		NIST
Inp	1509.00		NIST
Inp	1507.00		NIST
Inp	1527.00		NIST
Inp	1509.00		NIST
Inp	1505.00		NIST
Inp	1506.00		NIST
Inp	1506.00		NIST
Inp	1506.00		NIST
Inp	1509.00		NIST
Inp	1507.00		NIST
Inp	1524.00		NIST
Inp	1526.00		NIST
Inp	1527.00		NIST
Inp	1513.00		NIST
Inp	1521.30		NIST
Inp	1521.70		NIST
Inp	1526.00		NIST
Inp	1527.00		NIST
Inp	1514.00		NIST
Inp	1506.00		NIST
Inp	1503.00		NIST
Inp	1501.00		NIST
Inp	1523.00		NIST
Inp	1526.00		NIST
Inp	1526.80		NIST
Inp	1525.00		NIST
Inp	1521.00		NIST
Inp	1510.00		NIST
Inp	1533.00		NIST
Inp	1509.00		NIST
Inp	1525.00		NIST
Inp	1508.00		NIST
Inp	1508.00		NIST
Inp	1507.00		NIST
Inp	1505.00		NIST
Inp	1506.00		NIST
Inp	1509.00		NIST
Inp	1507.00		NIST
Inp	1510.00		NIST
Inp	1525.00		NIST
Inp	1526.00		NIST
Inp	1532.00		NIST
Inp	1532.00		NIST
Inp	1508.00		NIST
Inp	1526.00		NIST
Inp	1521.00		NIST
Inp	1528.00		NIST
Inp	1507.00		NIST
Inp	1525.00		NIST
Inp	1528.00		NIST
Inp	1531.00		NIST
Inp	1517.00		NIST
Inp	1510.00		NIST
Inp	1507.00		NIST
Inp	Outlier 258.35		NIST
Inp	Outlier 260.37		NIST
Inp	Outlier 265.90		NIST
Inp	Outlier 265.80		NIST
Inp	Outlier 265.90		NIST
Inp	Outlier 256.90		NIST
Inp	Outlier 260.05		NIST
Inp	1525.00		NIST
Inp	1526.00		NIST
Inp	1528.00		NIST
Inp	1501.00		NIST
Inp	1521.00		NIST
Inp	1508.00		NIST
Inp	1509.00		NIST
Inp	1514.90		NIST
Inp	1513.00		NIST
Inp	1521.30		NIST
Inp	1506.00		NIST
I	[1770.00; 1834.00]
I	1802.00		NIST
I	Outlier 1834.00		NIST
I	Outlier 1770.00		NIST
I	1798.00		NIST
I	1805.90		NIST
I	1807.10		NIST
I	1813.00		NIST
I	1784.90		NIST
I	1801.50		NIST
I	1806.70		NIST
I	1819.70		NIST
I	1785.00		NIST
I	1801.00		NIST
I	1800.00		NIST
I	1813.00		NIST
I	1785.00		NIST
I	1812.00		NIST
I	1805.00		NIST
I	1810.00		NIST
I	1804.00		NIST
I	1800.00		NIST
I	1804.00		NIST
I	1793.00		NIST
I	1808.00		NIST
I	1806.00		NIST
I	Outlier 1770.00		NIST
I	1814.00		NIST
I	1814.00		NIST
I	1791.00		NIST
I	1808.00		NIST
I	1811.00		NIST
I	1804.00		NIST
I	1793.00		NIST
I	1809.00		NIST
I	1793.00		NIST
I	1785.00		NIST
I	1815.00		NIST
I	1800.00		NIST
I	1800.00		NIST
I	1804.00		NIST
I	1815.00		NIST
I	1802.00		NIST
I	1807.10		NIST
I	1819.70		NIST
I	1808.00		NIST
I	1791.00		NIST
I	1785.00		NIST
Tboil	540.00	K	KDB
Tc	[712.00; 712.15]	K
Tc	712.00	K	KDB
Tc	712.15 ± 3.00	K	NIST
Tfus	[278.00; 278.45]	K
Tfus	278.25	K	Aq. Sol...
Tfus	278.30	K	KDB
Tfus	278.45 ± 0.35	K	NIST
Tfus	278.00 ± 0.05	K	NIST
Vc	0.787	m3/kmol	Joback Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[514.80; 603.14]	J/mol×K	[573.13; 741.92]
Cp,gas	514.80	J/mol×K	573.13	Joback Calculated Property
Cp,gas	531.11	J/mol×K	601.26	Joback Calculated Property
Cp,gas	546.77	J/mol×K	629.39	Joback Calculated Property
Cp,gas	561.79	J/mol×K	657.52	Joback Calculated Property
Cp,gas	576.19	J/mol×K	685.66	Joback Calculated Property
Cp,gas	589.97	J/mol×K	713.79	Joback Calculated Property
Cp,gas	603.14	J/mol×K	741.92	Joback Calculated Property
Cp,liquid	[449.00; 486.80]	J/mol×K	[303.15; 373.15]
Cp,liquid	449.00	J/mol×K	303.15	Heat ca...
Cp,liquid	452.80	J/mol×K	313.15	Heat ca...
Cp,liquid	457.40	J/mol×K	323.15	Heat ca...
Cp,liquid	462.60	J/mol×K	333.15	Heat ca...
Cp,liquid	468.40	J/mol×K	343.15	Heat ca...
Cp,liquid	474.50	J/mol×K	353.15	Heat ca...
Cp,liquid	480.70	J/mol×K	363.15	Heat ca...
Cp,liquid	486.80	J/mol×K	373.15	Heat ca...
η	[0.0011002; 0.0040678]	Pa×s	[283.15; 353.15]
η	0.0040678	Pa×s	283.15	Densiti...
η	0.0035771	Pa×s	288.15	Densiti...
η	0.0030960	Pa×s	293.15	Group C...
η	0.0031668	Pa×s	293.15	Densiti...
η	0.0028237	Pa×s	298.15	Densiti...
η	0.0025356	Pa×s	303.15	Densiti...
η	0.0024750	Pa×s	303.15	Group C...
η	0.0022893	Pa×s	308.15	Densiti...
η	0.0020776	Pa×s	313.15	Densiti...
η	0.0020440	Pa×s	313.15	Group C...
η	0.0018944	Pa×s	318.15	Densiti...
η	0.0016430	Pa×s	323.15	Group C...
η	0.0017347	Pa×s	323.15	Densiti...
η	0.0015948	Pa×s	328.15	Densiti...
η	0.0013830	Pa×s	333.15	Group C...
η	0.0014714	Pa×s	333.15	Densiti...
η	0.0013621	Pa×s	338.15	Densiti...
η	0.0012651	Pa×s	343.15	Densiti...
η	0.0011730	Pa×s	343.15	Group C...
η	0.0011781	Pa×s	348.15	Densiti...
η	0.0011002	Pa×s	353.15	Densiti...
ΔsubH	121.80 ± 2.10	kJ/mol	267.50	NIST
ΔvapH	[53.30; 83.60]	kJ/mol	[293.00; 498.00]
ΔvapH	80.80	kJ/mol	293.00	NIST
ΔvapH	69.33	kJ/mol	293.00	NIST
ΔvapH	75.80	kJ/mol	298.15	the vap...
ΔvapH	83.60	kJ/mol	310.00	NIST
ΔvapH	71.40	kJ/mol	350.00	NIST
ΔvapH	70.70 ± 0.20	kJ/mol	356.00	NIST
ΔvapH	71.40	kJ/mol	372.50	NIST
ΔvapH	74.90	kJ/mol	373.50	NIST
ΔvapH	62.30	kJ/mol	406.00	NIST
ΔvapH	63.60	kJ/mol	473.50	NIST
ΔvapH	53.30	kJ/mol	498.00	NIST
Pvap	[6.09e-03; 6.00]	kPa	[322.68; 443.30]
Pvap	6.72e-03	kPa	322.68	Experim...
Pvap	6.09e-03	kPa	323.80	Fatty a...
Pvap	7.01e-03	kPa	325.90	Fatty a...
Pvap	8.53e-03	kPa	327.90	Fatty a...
Pvap	9.82e-03	kPa	329.90	Fatty a...
Pvap	0.01	kPa	331.80	Fatty a...
Pvap	0.01	kPa	332.79	Experim...
Pvap	0.01	kPa	333.90	Fatty a...
Pvap	0.02	kPa	335.70	Fatty a...
Pvap	0.02	kPa	338.70	Fatty a...
Pvap	0.02	kPa	340.70	Fatty a...
Pvap	0.03	kPa	342.08	Experim...
Pvap	0.03	kPa	344.10	Fatty a...
Pvap	0.03	kPa	345.90	Fatty a...
Pvap	0.04	kPa	349.30	Fatty a...
Pvap	0.05	kPa	351.30	Fatty a...
Pvap	0.06	kPa	353.15	Isother...
Pvap	0.06	kPa	353.19	Experim...
Pvap	0.06	kPa	354.40	Fatty a...
Pvap	0.07	kPa	356.40	Fatty a...
Pvap	0.08	kPa	359.60	Fatty a...
Pvap	0.10	kPa	361.50	Fatty a...
Pvap	0.12	kPa	362.53	Experim...
Pvap	0.12	kPa	363.15	Isother...
Pvap	0.11	kPa	364.70	Fatty a...
Pvap	0.13	kPa	366.70	Fatty a...
Pvap	0.16	kPa	370.00	Fatty a...
Pvap	0.18	kPa	371.80	Fatty a...
Pvap	0.21	kPa	372.57	Experim...
Pvap	0.22	kPa	373.15	Isother...
Pvap	0.21	kPa	374.70	Fatty a...
Pvap	0.26	kPa	378.60	Fatty a...
Pvap	0.31	kPa	381.70	Fatty a...
Pvap	0.38	kPa	382.62	Experim...
Pvap	0.39	kPa	383.15	Isother...
Pvap	0.41	kPa	386.80	Fatty a...
Pvap	0.49	kPa	389.60	Fatty a...
Pvap	0.53	kPa	391.90	Fatty a...
Pvap	0.64	kPa	392.73	Experim...
Pvap	0.66	kPa	393.15	Isother...
Pvap	0.64	kPa	394.90	Fatty a...
Pvap	0.69	kPa	397.00	Fatty a...
Pvap	0.77	kPa	399.20	Fatty a...
Pvap	0.90	kPa	401.30	Fatty a...
Pvap	1.06	kPa	402.73	Experim...
Pvap	1.08	kPa	403.15	Isother...
Pvap	1.70	kPa	412.79	Experim...
Pvap	1.73	kPa	413.15	Isother...
Pvap	2.00	kPa	417.53	Isobari...
Pvap	2.65	kPa	422.61	Experim...
Pvap	2.69	kPa	423.15	Isother...
Pvap	4.02	kPa	432.58	Experim...
Pvap	4.10	kPa	433.15	Isother...
Pvap	4.00	kPa	433.71	Isobari...
Pvap	5.92	kPa	442.50	Experim...
Pvap	6.00	kPa	443.30	Isobari...
n0	[1.40513; 1.43836]		[278.15; 358.15]
n0	1.43836		278.15	Thermop...
n0	1.43629		283.15	Thermop...
n0	1.43422		288.15	Thermop...
n0	1.43216		293.15	Thermop...
n0	1.43009		298.15	Thermop...
n0	1.42802		303.15	Thermop...
n0	1.42594		308.15	Thermop...
n0	1.42383		313.15	Thermop...
n0	1.42171		318.15	Thermop...
n0	1.41959		323.15	Thermop...
n0	1.41750		328.15	Thermop...
n0	1.41542		333.15	Thermop...
n0	1.41334		338.15	Thermop...
n0	1.41127		343.15	Thermop...
n0	1.40922		348.15	Thermop...
n0	1.40717		353.15	Thermop...
n0	1.40513		358.15	Thermop...
ρl	[829.90; 869.30]	kg/m3	[293.15; 343.15]
ρl	869.22	kg/m3	293.15	Densiti...
ρl	869.30	kg/m3	293.15	Measure...
ρl	865.39	kg/m3	298.15	Measure...
ρl	865.30	kg/m3	298.15	Densiti...
ρl	861.46	kg/m3	303.15	Measure...
ρl	861.37	kg/m3	303.15	Densiti...
ρl	857.53	kg/m3	308.15	Measure...
ρl	857.44	kg/m3	308.15	Densiti...
ρl	853.61	kg/m3	313.15	Measure...
ρl	853.51	kg/m3	313.15	Densiti...
ρl	849.58	kg/m3	318.15	Densiti...
ρl	849.69	kg/m3	318.15	Measure...
ρl	845.76	kg/m3	323.15	Measure...
ρl	845.65	kg/m3	323.15	Densiti...
ρl	841.72	kg/m3	328.15	Densiti...
ρl	837.78	kg/m3	333.15	Densiti...
ρl	833.84	kg/m3	338.15	Densiti...
ρl	829.90	kg/m3	343.15	Densiti...
λ	[0.12; 0.15]	W/m×K	[283.81; 402.69]
λ	0.15	W/m×K	283.81	Experim...
λ	0.15	W/m×K	284.03	Experim...
λ	0.15	W/m×K	295.89	Experim...
λ	0.15	W/m×K	295.90	Experim...
λ	0.14	W/m×K	306.72	Experim...
λ	0.14	W/m×K	306.79	Experim...
λ	0.14	W/m×K	307.82	Experim...
λ	0.14	W/m×K	307.84	Experim...
λ	0.14	W/m×K	317.62	Experim...
λ	0.14	W/m×K	317.69	Experim...
λ	0.14	W/m×K	327.44	Experim...
λ	0.14	W/m×K	327.69	Experim...
λ	0.14	W/m×K	337.37	Experim...
λ	0.14	W/m×K	337.57	Experim...
λ	0.13	W/m×K	349.53	Experim...
λ	0.13	W/m×K	349.67	Experim...
λ	0.13	W/m×K	359.29	Experim...
λ	0.13	W/m×K	359.31	Experim...
λ	0.13	W/m×K	369.45	Experim...
λ	0.13	W/m×K	369.47	Experim...
λ	0.13	W/m×K	379.17	Experim...
λ	0.13	W/m×K	379.47	Experim...
λ	0.13	W/m×K	390.25	Experim...
λ	0.12	W/m×K	390.33	Experim...
λ	0.12	W/m×K	402.63	Experim...
λ	0.12	W/m×K	402.69	Experim...

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	[414.20; 535.20]	K	[2.00; 102.00]
Tboilr	414.20	K	2.00	NIST
Tboilr	535.20	K	102.00	NIST

Datasets

1. Molar heat capacity at constant pressure, J/K/mol (1)
2. Viscosity, Pa*s (1)
3. Mass density, kg/m3 (2)
4. 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	313.97	442.60
4040.00	313.99	441.60
8070.00	314.06	439.50
12160.00	314.09	438.30
16180.00	314.14	436.90
100.00	323.88	449.50
4070.00	323.93	447.20
8060.00	324.01	445.80
12090.00	323.84	444.80
16080.00	323.94	443.30
100.00	333.88	456.40
4050.00	333.96	453.60
8050.00	334.00	452.10
12060.00	334.05	450.50
16170.00	334.11	448.00
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.04	110.00	0.0025
303.04	10512.00	0.0029
302.94	20178.00	0.0032
302.70	30290.00	0.0036
312.63	134.00	0.0021
312.61	10214.00	0.0023
312.50	20279.00	0.0026
312.33	30212.00	0.0029
331.66	132.00	0.0015
331.51	10354.00	0.0017
331.34	20420.00	0.0019
331.07	29762.00	0.0020
351.81	235.00	0.0011
351.74	10090.00	0.0013
351.57	20226.00	0.0014
351.24	29906.00	0.0015
362.23	2921.00	0.0010
361.75	10141.00	0.0011
361.60	19931.00	0.0013
361.57	30100.00	0.0014
Reference

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	283.15	876.58
1000.00	283.15	877.29
3000.00	283.15	879.12
5000.00	283.15	880.29
10000.00	283.15	883.41
15000.00	283.15	886.29
20000.00	283.15	889.1
25000.00	283.15	891.75
30000.00	283.15	894.31
35000.00	283.15	896.95
40000.00	283.15	899.33
50000.00	283.15	904.05
60000.00	283.15	909.85
100.00	293.15	869.3
1000.00	293.15	869.79
3000.00	293.15	871.19
5000.00	293.15	872.09
10000.00	293.15	875.46
15000.00	293.15	878.42
20000.00	293.15	881.47
25000.00	293.15	884.32
30000.00	293.15	887.1
35000.00	293.15	889.69
40000.00	293.15	892.27
50000.00	293.15	897.52
60000.00	293.15	901.95
100.00	303.15	860.98
1000.00	303.15	861.67
3000.00	303.15	863.19
5000.00	303.15	864.57
10000.00	303.15	867.78
15000.00	303.15	871.1
20000.00	303.15	874.06
25000.00	303.15	876.92
30000.00	303.15	879.85
35000.00	303.15	882.66
40000.00	303.15	885.34
50000.00	303.15	890.6
60000.00	303.15	895.49
100.00	313.15	853.31
1000.00	313.15	853.78
3000.00	313.15	855.32
5000.00	313.15	856.78
10000.00	313.15	860.3
15000.00	313.15	863.63
20000.00	313.15	866.74
25000.00	313.15	870.04
30000.00	313.15	872.94
35000.00	313.15	875.68
40000.00	313.15	878.33
50000.00	313.15	883.95
60000.00	313.15	888.91
100.00	323.15	845.42
1000.00	323.15	846.17
3000.00	323.15	847.65
5000.00	323.15	849.19
10000.00	323.15	852.91
15000.00	323.15	856.38
20000.00	323.15	859.88
25000.00	323.15	863.01
30000.00	323.15	866.2
35000.00	323.15	869.19
40000.00	323.15	872.15
50000.00	323.15	877.67
60000.00	323.15	883.06
100.00	333.15	837.89
1000.00	333.15	838.44
3000.00	333.15	840.13
5000.00	333.15	841.69
10000.00	333.15	845.49
15000.00	333.15	849.14
20000.00	333.15	852.7
25000.00	333.15	856.12
30000.00	333.15	859.27
35000.00	333.15	862.4
40000.00	333.15	865.66
50000.00	333.15	871.36
60000.00	333.15	876.77
100.00	343.15	829.64
1000.00	343.15	830.6
3000.00	343.15	832.28
5000.00	343.15	834.04
10000.00	343.15	837.93
15000.00	343.15	841.71
20000.00	343.15	845.7
25000.00	343.15	848.98
30000.00	343.15	852.48
35000.00	343.15	855.72
40000.00	343.15	858.94
50000.00	343.15	864.79
60000.00	343.15	870.31
100.00	353.15	821.96
1000.00	353.15	822.7
3000.00	353.15	824.65
5000.00	353.15	826.36
10000.00	353.15	830.59
15000.00	353.15	834.55
20000.00	353.15	838.32
25000.00	353.15	842.04
30000.00	353.15	845.62
35000.00	353.15	849.06
40000.00	353.15	853.14
50000.00	353.15	858.49
60000.00	353.15	864.35
100.00	363.15	813.95
1000.00	363.15	814.97
3000.00	363.15	816.88
5000.00	363.15	818.64
10000.00	363.15	822.93
15000.00	363.15	827.44
20000.00	363.15	831.22
25000.00	363.15	834.95
30000.00	363.15	838.64
35000.00	363.15	842.26
40000.00	363.15	845.87
50000.00	363.15	852.24
60000.00	363.15	858.43
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
303.10	100.00	861.8
303.11	3010.00	863.7
303.13	6030.00	865.7
303.16	9050.00	867.9
303.20	12030.00	869.8
303.20	15040.00	871.7
312.95	100.00	853.4
313.11	3030.00	855.3
313.08	6050.00	857.4
313.06	9040.00	859.2
313.12	12030.00	861.2
312.95	15050.00	863.4
323.05	100.00	845.5
323.17	3030.00	847.4
323.30	6050.00	849.3
323.33	9050.00	851.6
323.27	12040.00	853.8
323.40	15020.00	855.9
333.15	100.00	837.8
333.15	3040.00	840.3
333.15	6040.00	842.3
333.18	9050.00	844.7
333.16	12020.00	846.9
333.14	15030.00	849.0
343.18	100.00	829.4
343.22	3020.00	831.9
343.22	6020.00	833.9
343.21	9040.00	836.6
343.19	12060.00	838.5
343.19	15050.00	841.1
353.27	100.00	821.6
353.28	3040.00	824.4
353.23	6050.00	826.8
353.26	9030.00	829.5
353.18	12030.00	831.6
353.16	15040.00	834.1
Reference

Speed of sound, m/s

Operational condition: Frequency, MHz = 2 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
293.15	100.00	1351.3
293.15	10000.00	1400.9
293.15	20000.00	1445.1
293.15	30000.00	1486.4
293.15	40000.00	1526.9
293.15	50000.00	1563.8
293.15	60000.00	1600.0
293.15	70000.00	1628.6
293.15	80000.00	1660.5
293.15	90000.00	1690.9
313.15	100.00	1276.4
313.15	10000.00	1328.0
313.15	20000.00	1375.3
313.15	30000.00	1420.0
313.15	40000.00	1461.6
313.15	50000.00	1500.9
313.15	60000.00	1537.0
313.15	70000.00	1573.3
313.15	80000.00	1607.4
313.15	90000.00	1637.8
313.15	100000.00	1671.1
313.15	120000.00	1728.6
313.15	140000.00	1784.4
333.15	100.00	1205.5
333.15	10000.00	1259.6
333.15	20000.00	1311.0
333.15	30000.00	1357.5
333.15	40000.00	1401.0
333.15	50000.00	1441.3
333.15	60000.00	1480.9
333.15	70000.00	1515.7
333.15	80000.00	1550.8
333.15	90000.00	1585.9
333.15	100000.00	1621.9
333.15	120000.00	1682.0
333.15	140000.00	1739.2
333.15	160000.00	1791.8
333.15	180000.00	1843.5
333.15	200000.00	1893.2
353.15	100.00	1133.5
353.15	10000.00	1192.2
353.15	20000.00	1247.2
353.15	30000.00	1295.9
353.15	40000.00	1342.5
353.15	50000.00	1386.1
353.15	60000.00	1426.2
353.15	70000.00	1463.8
353.15	80000.00	1500.1
353.15	90000.00	1534.8
353.15	100000.00	1568.3
353.15	120000.00	1632.8
353.15	140000.00	1690.8
353.15	160000.00	1744.4
353.15	180000.00	1802.7
353.15	200000.00	1851.2
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[409.00; 565.34]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.55217e+01
Coefficient B			-4.84033e+03
Coefficient C			-9.12700e+01
Temperature range, min.			409.00
Temperature range, max.			565.34
Pvap	1.33	kPa	409.00	Calculated Property
Pvap	2.94	kPa	426.37	Calculated Property
Pvap	5.98	kPa	443.74	Calculated Property
Pvap	11.41	kPa	461.11	Calculated Property
Pvap	20.52	kPa	478.48	Calculated Property
Pvap	35.09	kPa	495.86	Calculated Property
Pvap	57.43	kPa	513.23	Calculated Property
Pvap	90.39	kPa	530.60	Calculated Property
Pvap	137.44	kPa	547.97	Calculated Property
Pvap	202.66	kPa	565.34	Calculated Property
Pvap	[5.30e-05; 1771.68]	kPa	[278.15; 712.00]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			1.80226e+02
Coefficient B			-1.60241e+04
Coefficient C			-2.36787e+01
Coefficient D			1.04209e-05
Temperature range, min.			278.15
Temperature range, max.			712.00
Pvap	5.30e-05	kPa	278.15	Calculated Property
Pvap	8.10e-03	kPa	326.36	Calculated Property
Pvap	0.24	kPa	374.56	Calculated Property
Pvap	2.73	kPa	422.77	Calculated Property
Pvap	16.06	kPa	470.97	Calculated Property
Pvap	61.91	kPa	519.18	Calculated Property
Pvap	179.71	kPa	567.38	Calculated Property
Pvap	431.09	kPa	615.59	Calculated Property
Pvap	910.66	kPa	663.79	Calculated Property
Pvap	1771.68	kPa	712.00	Calculated Property

Similar Compounds

Find more compounds similar to Dodecanoic acid, methyl ester.

Mixtures

• Dodecanoic acid, methyl ester + Decanoic acid, methyl ester
• Dodecanoic acid, methyl ester + Cyclohexane, methyl-
• Dodecanoic acid, methyl ester + Tetradecane
• Dodecanoic acid, methyl ester + 4,7-Methano-1H-indene, octahydro-
• Cyclohexane, (1-methylethyl)- + Dodecanoic acid, methyl ester
• Cyclohexane, (1-methylethyl)- + Dodecanoic acid, methyl ester + 4,7-Methano-1H-indene, octahydro-
• Dodecanoic acid, methyl ester + Methyl Alcohol
• Ethane + Dodecanoic acid, methyl ester
• Dodecanoic acid, methyl ester + Glycerin + Methyl Alcohol
• 1-Propanol + Dodecanoic acid, methyl ester
• Dodecanoic acid, methyl ester + 1-Butanol
• Dodecanoic acid, methyl ester + 1-Pentanol
• Dodecanoic acid, methyl ester + Octanoic acid, ethyl ester
• Ethanol + Dodecanoic acid, methyl ester + Glycerin
• Dodecanoic acid, methyl ester + Glycerin + Water

Sources

• KDB Vapor Pressure Data
• Crippen Method
• Measurement and correlation of vapor liquid equilibria for methanol + methyl laurate and methanol + methyl myristate systems near critical temperature of methanol
• Phase behaviour of high molecular mass methyl esters in supercritical ethane
• Measurement and correlation of ternary vapor-liquid equilibria for methanol + glycerol + fatty acid methyl ester (methyl laurate, methyl myristate, methyl palmitate) systems at elevated temperatures and pressures
• 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
• High-pressure liquid densities and derived thermodynamic properties for methyl laurate and ethyl laurate
• Isobaric vapor-liquid equilibrium for binary system of methyl caprate + methyl laurate at 2, 4 and 6 kPa
• Measurement of speed of sound, density compressibility and viscosity in liquid methyl laurate and ethyl laurate up to 200 MPa by using acoustic wave sensors
• Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
• Heat capacities and thermal diffusivities of some n-alkanoic acid methyl esters
• Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
• Thermophysical properties of fatty acid methyl and ethyl esters
• Liquid viscosities for methyl hexanoate, methyl heptanoate, methyl caprylate, and methyl nonanoate at high pressures
• Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
• Experimental studies on the thermal conductivity of methyl laurate component of biodiesel with three alcohols
• the vaporization enthaplies and vapor pressures of a series of unstaurated fatty acid methyl esters by correlation gas chromatography
• Isobaric molar heat capacities of binary mixtures containing methyl caprate and methyl laurate at pressures up to 16.2 MPa
• Measurement and correlation of viscosities and densities of methyl dodecanoate and ethyl dodecanoate at elevated pressures
• Liquid Liquid Equilibrium for the Ternary System of Methyl Laurate/Methyl Myristate + Ethanol + Glycerol at 318.15 and 333.15 K
• Isothermal Vapor Pressures of Three Binary Systems: n-Tetradecane + Methyl Dodecanoate, Methyl Tetradecanoate, or Methyl Hexadecanoate between 353.15 and 453.15 K
• Densities and Viscosities of Mixtures of Methyl Dodecanoate + Ethyl Octanoate at Pressures up to 15 MPa
• Densities and Viscosities for the Ternary Mixtures of exo-Tetrahydrodicyclopentadiene (1) + Isopropylcyclohexane (2) + Methyl Laurate (3) and Corresponding Binaries
• Heat Capacity Measurements of 13 Methyl Esters of n-Carboxylic Acids from Methyloctanoate to Methyleicosanoate between 5 K and 350 K
• Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
• Article Ternary Liquid Liquid Equilibrium of Biodiesel Compounds for Systems Consisting of a Methyl Ester + Glycerin + Water
• Group Contribution Model for Predicting Viscosity of Fatty Compounds
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.
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