Chemical Properties of Tetradecanoic acid (CAS 544-63-8)

InChI

InChI=1S/C14H28O2/c1-2-3-4-5-6-7-8-9-10-11-12-13-14(15)16/h2-13H2,1H3,(H,15,16)

InChI Key

TUNFSRHWOTWDNC-UHFFFAOYSA-N

Formula

C14H28O2

SMILES

CCCCCCCCCCCCCC(=O)O

Molecular Weight¹

228.37

CAS

544-63-8

Other Names

• 1-Tridecanecarboxylic acid
• Acide Myristique
• Crodacid
• Emery 655
• Hydrofol acid 1495
• Hystrene 9014
• Hystrene 9514
• Myristic acid (tetradecanoic acid)
• N-MYRISTIC ACID
• NSC 5028
• Neo-Fat 14
• Philacid 1400
• Prifac 2942
• Prifrac 2942
• Tetradecanoic (Myristic) acid
• Tetradecanoic acid (=Myristic acid)
• Tetradecanoic acid (myristic acid)
• Univol U 316S
• myristic acid
• n-Tetradecan-1-oic acid
• n-Tetradecanoic acid
• n-Tetradecoic acid

• ω : Acentric Factor.
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• Δ_cH°_solid : Standard solid 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).
• C_p,solid : Solid 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_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_subH° : Enthalpy of sublimation 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).
• 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.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• γ : Surface Tension (N/m).
• 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.

Physical Properties

Property	Value	Unit	Source
ω	[0.8740; 0.9535]
ω	0.8740		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.9535		ChemSep v8.3 pure component data Compiled value
ΔcH°liquid	-8676.70 ± 1.40	kJ/mol	NIST
ΔcH°solid	-8675.90 ± 9.60	kJ/mol	NIST
μ	1.68	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	-278.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-681.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfusH°	[43.70; 44.75]	kJ/mol
ΔfusH°	44.75	kJ/mol	Solid-liquid phase equilibria of (n-octadecane with myristic, and palmitic acid) binary mixtures used as phase change materials (PCMs)
ΔfusH°	43.70	kJ/mol	Solid-Liquid Equilibrium of Binary Systems Containing Fatty Acids and Fatty Alcohols Using Differential Scanning Calorimetry
ΔsubH°	169.00 ± 9.00	kJ/mol	NIST
ΔvapH°	107.40	kJ/mol	Relay (1.0) Calculated Property
IE	9.95	eV	Relay (1.0) Calculated Property
log10WS	-5.33		Aq. Solubility Prediction
logPoct/wat	4.772		Crippen Calculated Property
McVol	215.560	ml/mol	McGowan Calculated Property
Pc	[1644.20; 2150.00]	kPa
Pc	1915.04	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	2150.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	1644.20 ± 85.00	kPa	NIST
Ptriple	[2.13e-05; 3.76e-05]	kPa
Ptriple	3.76e-05	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	2.13e-05 ± 1.07e-05	kPa	NIST
Inp	[288.93; 1800.00]
Inp	1763.00		NIST
Inp	1767.00		NIST
Inp	1738.00		NIST
Inp	1778.00		NIST
Inp	1735.00		NIST
Inp	1784.00		NIST
Inp	1765.00		NIST
Inp	1740.00		NIST
Inp	1750.00		NIST
Inp	1762.00		NIST
Inp	1763.00		NIST
Inp	1763.00		NIST
Inp	1761.00		NIST
Inp	1768.00		NIST
Inp	1769.00		NIST
Inp	1775.00		NIST
Inp	1748.00		NIST
Inp	1780.00		NIST
Inp	1770.00		NIST
Inp	1767.10		NIST
Inp	1762.00		NIST
Inp	1772.00		NIST
Inp	1765.00		NIST
Inp	1787.00		NIST
Inp	1787.00		NIST
Inp	1769.70		NIST
Inp	1770.00		NIST
Inp	1748.00		NIST
Inp	1748.00		NIST
Inp	1768.00		NIST
Inp	1776.00		NIST
Inp	1780.00		NIST
Inp	1798.00		NIST
Inp	1770.00		NIST
Inp	1771.00		NIST
Inp	1771.00		NIST
Inp	1770.00		NIST
Inp	1762.00		NIST
Inp	1772.00		NIST
Inp	1767.00		NIST
Inp	1759.00		NIST
Inp	1752.00		NIST
Inp	1771.00		NIST
Inp	1777.00		NIST
Inp	1767.00		NIST
Inp	1771.00		NIST
Inp	1752.00		NIST
Inp	1743.00		NIST
Inp	1762.00		NIST
Inp	1743.00		NIST
Inp	1743.00		NIST
Inp	1769.00		NIST
Inp	1772.71		NIST
Inp	1774.64		NIST
Inp	1769.00		NIST
Inp	1751.00		NIST
Inp	1731.00		NIST
Inp	1737.00		NIST
Inp	1740.00		NIST
Inp	1737.27		NIST
Inp	1763.00		NIST
Inp	1779.00		NIST
Inp	1758.20		NIST
Inp	1767.00		NIST
Inp	1770.00		NIST
Inp	1752.10		NIST
Inp	1756.00		NIST
Inp	1739.00		NIST
Inp	1762.00		NIST
Inp	1747.00		NIST
Inp	1747.00		NIST
Inp	1761.00		NIST
Inp	1751.00		NIST
Inp	1762.00		NIST
Inp	1763.00		NIST
Inp	1766.00		NIST
Inp	1744.00		NIST
Inp	1774.00		NIST
Inp	1767.00		NIST
Inp	1761.00		NIST
Inp	1765.00		NIST
Inp	1763.00		NIST
Inp	1763.00		NIST
Inp	1746.00		NIST
Inp	1761.00		NIST
Inp	1762.00		NIST
Inp	1747.00		NIST
Inp	1763.00		NIST
Inp	1780.00		NIST
Inp	1765.00		NIST
Inp	1771.00		NIST
Inp	1762.00		NIST
Inp	1748.00		NIST
Inp	1742.00		NIST
Inp	1742.00		NIST
Inp	1741.00		NIST
Inp	1771.00		NIST
Inp	1765.00		NIST
Inp	1769.00		NIST
Inp	1782.00		NIST
Inp	1769.00		NIST
Inp	1769.00		NIST
Inp	1771.00		NIST
Inp	1750.00		NIST
Inp	1765.00		NIST
Inp	1764.00		NIST
Inp	1769.00		NIST
Inp	1765.00		NIST
Inp	1768.00		NIST
Inp	1757.00		NIST
Inp	1782.00		NIST
Inp	1769.00		NIST
Inp	1760.00		NIST
Inp	1769.00		NIST
Inp	1770.00		NIST
Inp	1771.00		NIST
Inp	1768.00		NIST
Inp	1773.00		NIST
Inp	1795.00		NIST
Inp	1777.00		NIST
Inp	1780.00		NIST
Inp	1770.00		NIST
Inp	1765.00		NIST
Inp	1776.00		NIST
Inp	1783.00		NIST
Inp	1741.00		NIST
Inp	1768.00		NIST
Inp	1755.00		NIST
Inp	1751.00		NIST
Inp	1783.00		NIST
Inp	1786.00		NIST
Inp	1747.00		NIST
Inp	1770.00		NIST
Inp	1764.00		NIST
Inp	1748.00		NIST
Inp	1748.00		NIST
Inp	1760.00		NIST
Inp	1760.00		NIST
Inp	1773.00		NIST
Inp	1769.00		NIST
Inp	1776.00		NIST
Inp	1756.00		NIST
Inp	1763.00		NIST
Inp	1765.00		NIST
Inp	1763.00		NIST
Inp	1772.00		NIST
Inp	1760.00		NIST
Inp	1758.00		NIST
Inp	1751.00		NIST
Inp	1761.00		NIST
Inp	1767.00		NIST
Inp	1765.00		NIST
Inp	1769.00		NIST
Inp	1756.00		NIST
Inp	1768.00		NIST
Inp	1772.00		NIST
Inp	1769.00		NIST
Inp	1738.00		NIST
Inp	1768.00		NIST
Inp	1777.00		NIST
Inp	1780.00		NIST
Inp	1755.00		NIST
Inp	1743.00		NIST
Inp	1757.00		NIST
Inp	1759.00		NIST
Inp	1717.00		NIST
Inp	1750.00		NIST
Inp	1731.00		NIST
Inp	1758.00		NIST
Inp	1768.00		NIST
Inp	1758.00		NIST
Inp	1778.00		NIST
Inp	1770.00		NIST
Inp	1768.00		NIST
Inp	1760.00		NIST
Inp	1800.00		NIST
Inp	1761.00		NIST
Inp	1777.00		NIST
Inp	1768.00		NIST
Inp	1750.00		NIST
Inp	1780.00		NIST
Inp	1774.00		NIST
Inp	1748.00		NIST
Inp	1767.00		NIST
Inp	1745.00		NIST
Inp	1758.00		NIST
Inp	1762.00		NIST
Inp	1749.00		NIST
Inp	1750.00		NIST
Inp	1786.00		NIST
Inp	1754.00		NIST
Inp	Outlier 293.98		NIST
Inp	Outlier 303.00		NIST
Inp	Outlier 291.80		NIST
Inp	Outlier 288.93		NIST
Inp	1762.00		NIST
Inp	1769.00		NIST
Inp	1763.00		NIST
Inp	1761.00		NIST
Inp	1768.00		NIST
Inp	1777.00		NIST
Inp	1759.00		NIST
Inp	1760.00		NIST
Inp	1750.00		NIST
Inp	1745.00		NIST
Inp	1786.00		NIST
Inp	1784.00		NIST
Inp	1758.20		NIST
Inp	1739.00		NIST
Inp	Outlier 293.98		NIST
Ip	[2648.00; 2734.00]
Ip	2681.00		NIST
Ip	2715.00		NIST
Ip	2687.00		NIST
Ip	2679.00		NIST
Ip	2694.00		NIST
Ip	2694.00		NIST
Ip	2716.00		NIST
Ip	2712.00		NIST
Ip	2714.00		NIST
Ip	2734.00		NIST
Ip	2680.00		NIST
Ip	2712.00		NIST
Ip	2714.00		NIST
Ip	2656.00		NIST
Ip	2656.00		NIST
Ip	2679.00		NIST
Ip	2724.00		NIST
Ip	2733.00		NIST
Ip	2660.00		NIST
Ip	2698.00		NIST
Ip	2692.00		NIST
Ip	2692.00		NIST
Ip	2692.00		NIST
Ip	2675.00		NIST
Ip	2692.00		NIST
Ip	2674.00		NIST
Ip	2684.00		NIST
Ip	2651.00		NIST
Ip	Outlier 2649.00		NIST
Ip	2703.00		NIST
Ip	2685.00		NIST
Ip	2693.00		NIST
Ip	2693.00		NIST
Ip	2708.00		NIST
Ip	2710.00		NIST
Ip	2715.00		NIST
Ip	2715.00		NIST
Ip	2733.00		NIST
Ip	2706.00		NIST
Ip	2704.00		NIST
Ip	2674.00		NIST
Ip	Outlier 2648.00		NIST
Ip	2682.00		NIST
Ip	2717.00		NIST
Ip	2713.00		NIST
Ip	2713.00		NIST
Ip	2713.00		NIST
Ip	2713.00		NIST
Ip	2672.00		NIST
Ip	2695.00		NIST
Ip	2713.00		NIST
Ip	2684.00		NIST
Ip	2691.00		NIST
Ip	2670.00		NIST
Ip	2670.00		NIST
Ip	2702.00		NIST
Ip	2692.00		NIST
Ip	2695.00		NIST
Ip	2679.00		NIST
Ip	2713.00		NIST
Ip	2722.00		NIST
Ip	2672.00		NIST
Ip	2701.00		NIST
Ip	2724.00		NIST
Ip	2689.00		NIST
Ip	2713.00		NIST
Ip	2670.00		NIST
Ip	2670.00		NIST
Ip	2670.00		NIST
Ip	2670.00		NIST
Ip	2670.00		NIST
Ip	2670.00		NIST
Ip	2713.00		NIST
Ip	2670.00		NIST
Ip	2713.00		NIST
Ip	2670.00		NIST
Ip	2670.00		NIST
Ip	2660.00		NIST
Ip	2670.00		NIST
Ip	2713.00		NIST
Ip	2713.00		NIST
Ip	2719.00		NIST
Ip	2713.00		NIST
Ip	2670.00		NIST
Ip	2713.00		NIST
Ip	2713.00		NIST
Ip	2713.00		NIST
Ip	2713.00		NIST
Ip	2713.00		NIST
Ip	2713.00		NIST
Ip	2682.00		NIST
Ip	2660.00		NIST
Ip	2670.00		NIST
Ip	2679.00		NIST
Ip	2724.00		NIST
Ip	2713.00		NIST
Ip	2681.00		NIST
Ip	2694.00		NIST
Ip	2680.00		NIST
Ip	2651.00		NIST
Ip	2693.00		NIST
Ip	2733.00		NIST
Ip	2682.00		NIST
Ip	2691.00		NIST
Tboil	599.35	K	ChemSep v8.3 pure component data Compiled value
Tc	[765.19; 784.00]	K
Tc	784.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	770.00	K	ChemSep v8.3 pure component data Compiled value
Tc	765.19 ± 3.00	K	NIST
Tfus	[326.15; 329.05]	K
Tfus	327.50	K	High pressure solid liquid equilibria of fatty acids
Tfus	327.03	K	Measurement and PC-SAFT modeling of solid-liquid equilibrium of deep eutectic solvents of quaternary ammonium chlorides and carboxylic acids
Tfus	Outlier 329.05	K	Solid-liquid phase equilibrium diagrams of binary mixtures containing fatty acids, fatty alcohol compounds and tripalmitin using differential scanning calorimetry
Tfus	328.88	K	The solid liquid phase diagrams of binary mixtures of even saturated fatty acids differing by six carbon atoms
Tfus	326.15	K	Preparation of paraffin and fatty acid phase changing nanoemulsions for heat transfer
Tfus	327.85	K	Prediction of the properties of eutectic fatty acid phase change materials
Tfus	327.60	K	Solid Liquid Equilibria in the Binary Systems of Saturated Fatty Acids or Triglycerides (C12 to C18) + Hexadecane
Tfus	327.48	K	Solid-Liquid Equilibrium of Binary Fatty Acid Mixtures
Tfus	327.50	K	Study of the Effect of Pressure on Melting Behavior of Saturated Fatty Acids in Liquid or Supercritical Carbon Dioxide
Tfus	328.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	326.70	K	ChemSep v8.3 pure component data Compiled value
Tfus	327.82	K	Aq. Solubility Prediction
Tfus	327.05 ± 0.35	K	NIST
Tfus	327.40 ± 0.05	K	NIST
Tfus	327.10 ± 1.00	K	NIST
Tfus	328.70 ± 1.50	K	NIST
Tfus	327.00 ± 3.00	K	NIST
Tfus	327.00 ± 3.00	K	NIST
Ttriple	[327.05; 327.37]	K
Ttriple	327.37	K	ChemSep v8.3 pure component data Compiled value
Ttriple	327.32 ± 0.02	K	NIST
Ttriple	327.05 ± 0.50	K	NIST
Ttriple	327.32 ± 0.02	K	NIST
UQi	8.55		ChemSep v8.3 pure component data Compiled value
URi	10.30		ChemSep v8.3 pure component data Compiled value
Vc	[0.836; 0.890]	m3/kmol
Vc	0.836	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.890	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2300000		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,solid	[432.01; 523.00]	J/mol×K	[298.00; 298.15]
Cp,solid	523.00	J/mol×K	298.00	NIST
Cp,solid	432.01	J/mol×K	298.15	NIST
ΔfusH	[36.28; 45.75]	kJ/mol	[317.00; 327.00]
ΔfusH	36.28	kJ/mol	317.00	NIST
ΔfusH	45.75	kJ/mol	326.20	NIST
ΔfusH	45.00	kJ/mol	326.50	NIST
ΔfusH	40.10	kJ/mol	326.60	NIST
ΔfusH	45.10	kJ/mol	327.00	NIST
ΔfusH	45.10	kJ/mol	327.00	NIST
ΔsubH	[139.70; 140.00]	kJ/mol	[311.85; 318.50]
ΔsubH	140.00 ± 4.00	kJ/mol	311.85	NIST
ΔsubH	139.70 ± 3.80	kJ/mol	318.50	NIST
ΔvapH	[88.90; 111.20]	kJ/mol	[298.00; 511.00]
ΔvapH	111.20	kJ/mol	298.00	Vapor Pressures and Vaporization, Sublimation, and Fusion Enthalpies of Some Fatty Acids
ΔvapH	104.10 ± 2.00	kJ/mol	348.50	NIST
ΔvapH	100.40	kJ/mol	421.00	NIST
ΔvapH	88.90	kJ/mol	455.00	NIST
ΔvapH	91.60	kJ/mol	511.00	NIST
Pvap	[1.33; 9.33]	kPa	[464.60; 512.60]
Pvap	1.33	kPa	464.60	Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique
Pvap	2.67	kPa	480.80	Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique
Pvap	4.00	kPa	489.50	Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique
Pvap	5.33	kPa	497.20	Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique
Pvap	6.67	kPa	503.10	Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique
Pvap	8.00	kPa	508.20	Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique
Pvap	9.33	kPa	512.60	Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique
ρl	[758.00; 861.30]	kg/m3	[332.10; 473.20]
ρl	861.30	kg/m3	332.10	Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K
ρl	846.90	kg/m3	352.10	Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K
ρl	835.60	kg/m3	368.20	Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K
ρl	821.40	kg/m3	388.20	Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K
ρl	806.70	kg/m3	408.20	Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K
ρl	791.70	kg/m3	427.90	Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K
ρl	780.90	kg/m3	443.20	Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K
ρl	769.30	kg/m3	458.20	Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K
ρl	758.00	kg/m3	473.20	Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K
ΔfusS	114.00	J/mol×K	317.00	NIST

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	523.20	K	13.30	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[335.01; 864.54]	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 Cp,gas in J/mol×K, T in K
Coefficient A			2.46920e+02
Coefficient B			7.55330e+02
Coefficient C			1.64680e+03
Coefficient D			5.27980e+02
Coefficient E			7.53550e+02
Temperature range, min.			300.00
Temperature range, max.			1500.00
Cp,gas	335.01	J/mol×K	300.00	Calculated Property
Cp,gas	454.29	J/mol×K	433.33	Calculated Property
Cp,gas	551.96	J/mol×K	566.67	Calculated Property
Cp,gas	629.16	J/mol×K	700.00	Calculated Property
Cp,gas	691.48	J/mol×K	833.33	Calculated Property
Cp,gas	741.98	J/mol×K	966.67	Calculated Property
Cp,gas	782.84	J/mol×K	1100.00	Calculated Property
Cp,gas	815.89	J/mol×K	1233.33	Calculated Property
Cp,gas	842.69	J/mol×K	1366.67	Calculated Property
Cp,gas	864.54	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[501.52; 880.27]	J/mol×K	[327.37; 599.35]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K
Coefficient A			3.25720e+02
Coefficient B			6.96850e-02
Coefficient C			1.42750e-03
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			327.37
Temperature range, max.			599.35
Cp,liquid	501.52	J/mol×K	327.37	Calculated Property
Cp,liquid	533.17	J/mol×K	357.59	Calculated Property
Cp,liquid	567.44	J/mol×K	387.81	Calculated Property
Cp,liquid	604.30	J/mol×K	418.03	Calculated Property
Cp,liquid	643.78	J/mol×K	448.25	Calculated Property
Cp,liquid	685.86	J/mol×K	478.47	Calculated Property
Cp,liquid	730.56	J/mol×K	508.69	Calculated Property
Cp,liquid	777.85	J/mol×K	538.91	Calculated Property
Cp,liquid	827.76	J/mol×K	569.13	Calculated Property
Cp,liquid	880.27	J/mol×K	599.35	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0089566; 0.0002191]	Pa×s	[327.37; 599.35]	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			-3.44890e+01
Coefficient B			3.99960e+03
Coefficient C			3.03160e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			327.37
Temperature range, max.			599.35
η	0.0089566	Pa×s	327.37	Calculated Property
η	0.0041686	Pa×s	357.59	Calculated Property
η	0.0022299	Pa×s	387.81	Calculated Property
η	0.0013283	Pa×s	418.03	Calculated Property
η	0.0008611	Pa×s	448.25	Calculated Property
η	0.0005973	Pa×s	478.47	Calculated Property
η	0.0004377	Pa×s	508.69	Calculated Property
η	0.0003355	Pa×s	538.91	Calculated Property
η	0.0002669	Pa×s	569.13	Calculated Property
η	0.0002191	Pa×s	599.35	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[106.65; 22.84]	kJ/mol	[327.37; 763.00]	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 ΔvapH in kJ/mol, T in K
Coefficient A			1.31070e+02
Coefficient B			-2.71890e-01
Coefficient C			2.16630e+00
Coefficient D			-1.53070e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			7.70000e+02
Temperature range, min.			327.37
Temperature range, max.			763.00
ΔvapH	106.65	kJ/mol	327.37	Calculated Property
ΔvapH	98.89	kJ/mol	375.77	Calculated Property
ΔvapH	90.92	kJ/mol	424.18	Calculated Property
ΔvapH	82.94	kJ/mol	472.58	Calculated Property
ΔvapH	75.12	kJ/mol	520.98	Calculated Property
ΔvapH	67.53	kJ/mol	569.39	Calculated Property
ΔvapH	60.11	kJ/mol	617.79	Calculated Property
ΔvapH	52.50	kJ/mol	666.19	Calculated Property
ΔvapH	43.38	kJ/mol	714.60	Calculated Property
ΔvapH	22.84	kJ/mol	763.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[461.48; 631.79]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.57451e+01
Coefficient B			-5.46750e+03
Coefficient C			-1.07769e+02
Temperature range, min.			461.48
Temperature range, max.			631.79
Pvap	1.33	kPa	461.48	Calculated Property
Pvap	2.92	kPa	480.40	Calculated Property
Pvap	5.94	kPa	499.33	Calculated Property
Pvap	11.31	kPa	518.25	Calculated Property
Pvap	20.34	kPa	537.17	Calculated Property
Pvap	34.81	kPa	556.10	Calculated Property
Pvap	57.04	kPa	575.02	Calculated Property
Pvap	89.94	kPa	593.94	Calculated Property
Pvap	137.07	kPa	612.87	Calculated Property
Pvap	202.63	kPa	631.79	Calculated Property
Pvap	[3.75e-05; 1639.70]	kPa	[327.37; 763.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			1.71152e+02
Coefficient B			-1.96490e+04
Coefficient C			-2.09510e+01
Coefficient D			5.36980e-18
Coefficient E			6.00000e+00
Temperature range, min.			327.37
Temperature range, max.			763.00
Pvap	3.75e-05	kPa	327.37	Calculated Property
Pvap	4.79e-03	kPa	375.77	Calculated Property
Pvap	0.15	kPa	424.18	Calculated Property
Pvap	1.85	kPa	472.58	Calculated Property
Pvap	11.95	kPa	520.98	Calculated Property
Pvap	49.47	kPa	569.39	Calculated Property
Pvap	150.09	kPa	617.79	Calculated Property
Pvap	369.67	kPa	666.19	Calculated Property
Pvap	801.57	kPa	714.60	Calculated Property
Pvap	1639.70	kPa	763.00	Calculated Property
Pvap	[4.19e-05; 1535.46]	kPa	[327.55; 756.00]	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			2.20853e+02
Coefficient B			-2.15189e+04
Coefficient C			-2.86975e+01
Coefficient D			9.02023e-06
Coefficient E			0.00000e+00
Temperature range, min.			327.55
Temperature range, max.			756.00
Pvap	4.19e-05	kPa	327.55	Calculated Property
Pvap	4.81e-03	kPa	375.16	Calculated Property
Pvap	0.14	kPa	422.76	Calculated Property
Pvap	1.66	kPa	470.37	Calculated Property
Pvap	10.72	kPa	517.97	Calculated Property
Pvap	45.19	kPa	565.58	Calculated Property
Pvap	141.42	kPa	613.18	Calculated Property
Pvap	358.30	kPa	660.79	Calculated Property
Pvap	781.64	kPa	708.39	Calculated Property
Pvap	1535.46	kPa	756.00	Calculated Property
Pvap	[7.22e-03; 1.16]	kPa	[385.03; 465.10]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			7.93904e+00
Coefficient B			-1.57952e+03
Coefficient C			-2.62300e+02
Reference			Hammer and Lydersen, 1957
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			385.03
Temperature range, max.			465.10
Pvap	7.22e-03	kPa	385.03	Calculated Property
Pvap	0.02	kPa	393.93	Calculated Property
Pvap	0.04	kPa	402.82	Calculated Property
Pvap	0.07	kPa	411.72	Calculated Property
Pvap	0.13	kPa	420.62	Calculated Property
Pvap	0.22	kPa	429.51	Calculated Property
Pvap	0.36	kPa	438.41	Calculated Property
Pvap	0.55	kPa	447.31	Calculated Property
Pvap	0.81	kPa	456.20	Calculated Property
Pvap	1.16	kPa	465.10	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[864.08; 256.60]	kg/m3	[327.37; 763.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			6.17150e+01
Coefficient B			2.40510e-01
Coefficient C			7.63000e+02
Coefficient D			2.85710e-01
Temperature range, min.			327.37
Temperature range, max.			763.00
ρl	864.08	kg/m3	327.37	Calculated Property
ρl	830.05	kg/m3	375.77	Calculated Property
ρl	794.36	kg/m3	424.18	Calculated Property
ρl	756.61	kg/m3	472.58	Calculated Property
ρl	716.20	kg/m3	520.98	Calculated Property
ρl	672.21	kg/m3	569.39	Calculated Property
ρl	623.02	kg/m3	617.79	Calculated Property
ρl	565.41	kg/m3	666.19	Calculated Property
ρl	490.59	kg/m3	714.60	Calculated Property
ρl	256.60	kg/m3	763.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.01]	N/m	[327.15; 523.15]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			5.93576e-02
Coefficient B			-9.32000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			327.15
Temperature range, max.			523.15
γ	0.03	N/m	327.15	Calculated Property
γ	0.03	N/m	348.93	Calculated Property
γ	0.02	N/m	370.71	Calculated Property
γ	0.02	N/m	392.48	Calculated Property
γ	0.02	N/m	414.26	Calculated Property
γ	0.02	N/m	436.04	Calculated Property
γ	0.02	N/m	457.82	Calculated Property
γ	0.01	N/m	479.59	Calculated Property
γ	0.01	N/m	501.37	Calculated Property
γ	0.01	N/m	523.15	Calculated Property
γ	[0.03; 1.65e-04]	N/m	[327.37; 763.00]	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 γ in N/m, T in K
Coefficient A			5.78220e-02
Coefficient B			1.24620e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			7.70000e+02
Temperature range, min.			327.37
Temperature range, max.			763.00
γ	0.03	N/m	327.37	Calculated Property
γ	0.03	N/m	375.77	Calculated Property
γ	0.02	N/m	424.18	Calculated Property
γ	0.02	N/m	472.58	Calculated Property
γ	0.01	N/m	520.98	Calculated Property
γ	0.01	N/m	569.39	Calculated Property
γ	0.01	N/m	617.79	Calculated Property
γ	0.00	N/m	666.19	Calculated Property
γ	0.00	N/m	714.60	Calculated Property
γ	1.65e-04	N/m	763.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.03; 0.11]	W/m×K	[599.35; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			6.60860e-08
Coefficient B			2.15320e+00
Coefficient C			7.65270e+02
Coefficient D			0.00000e+00
Temperature range, min.			599.35
Temperature range, max.			1000.00
λgas	0.03	W/m×K	599.35	Calculated Property
λgas	0.03	W/m×K	643.87	Calculated Property
λgas	0.04	W/m×K	688.38	Calculated Property
λgas	0.05	W/m×K	732.90	Calculated Property
λgas	0.06	W/m×K	777.42	Calculated Property
λgas	0.06	W/m×K	821.93	Calculated Property
λgas	0.07	W/m×K	866.45	Calculated Property
λgas	0.08	W/m×K	910.97	Calculated Property
λgas	0.10	W/m×K	955.48	Calculated Property
λgas	0.11	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.10]	W/m×K	[327.37; 599.35]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λliquid in W/m×K, T in K
Coefficient A			2.18000e-01
Coefficient B			-2.00000e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			327.37
Temperature range, max.			599.35
λliquid	0.15	W/m×K	327.37	Calculated Property
λliquid	0.15	W/m×K	357.59	Calculated Property
λliquid	0.14	W/m×K	387.81	Calculated Property
λliquid	0.13	W/m×K	418.03	Calculated Property
λliquid	0.13	W/m×K	448.25	Calculated Property
λliquid	0.12	W/m×K	478.47	Calculated Property
λliquid	0.12	W/m×K	508.69	Calculated Property
λliquid	0.11	W/m×K	538.91	Calculated Property
λliquid	0.10	W/m×K	569.13	Calculated Property
λliquid	0.10	W/m×K	599.35	Calculated Property

Similar Compounds

Find more compounds similar to Tetradecanoic acid.

Mixtures

• TETRAMETHYLAMMONIUM CHLORIDE + Tetradecanoic acid
• Triolein + Tetradecanoic acid + 1-Hexanol
• Triolein + 1-Butanol + Tetradecanoic acid
• 1-Propanol + Triolein + Tetradecanoic acid
• Triolein + 2-Propanol + Tetradecanoic acid
• Tetradecanoic acid + n-Hexadecanoic acid
• Octadecanoic acid + Tetradecanoic acid
• Tetradecanoic acid + Octadecane
• Dodecanoic acid + Tetradecanoic acid
• Tetradecanoic acid + Octanoic acid
• Tripalmitin + Tetradecanoic acid
• Trichloromethane + Tetradecanoic acid
• Trichloroethylene + Tetradecanoic acid
• Benzene, chloro- + Tetradecanoic acid
• Tetradecanoic acid + Ethane, 1,2-dichloro-
• Tetradecanoic acid + Benzene, (chloromethyl)-
• Tetradecanoic acid + Ethyl Acetate
• Tetradecanoic acid + Acetone
• Tetradecanoic acid + Anisole
• n-Hexane + Tetradecanoic acid

Find more mixtures with Tetradecanoic acid.

Sources

• KDB Vapor Pressure Data
• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• 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
• High pressure solid liquid equilibria of fatty acids
• Measurement and PC-SAFT modeling of solid-liquid equilibrium of deep eutectic solvents of quaternary ammonium chlorides and carboxylic acids
• Solid-liquid phase equilibrium diagrams of binary mixtures containing fatty acids, fatty alcohol compounds and tripalmitin using differential scanning calorimetry
• Experimental determination of the (vapor + liquid) equilibrium data of binary mixtures of fatty acids by differential scanning calorimetry
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
• Solid-liquid phase equilibria of (n-octadecane with myristic, and palmitic acid) binary mixtures used as phase change materials (PCMs)
• Physical properties of systems of interest to the edible oil industry: Viscosities and densities of model systems formed by (triacylglycerol + fatty acid + solvent)
• The solid liquid phase diagrams of binary mixtures of even saturated fatty acids differing by six carbon atoms
• Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique
• Preparation of paraffin and fatty acid phase changing nanoemulsions for heat transfer
• Prediction of the properties of eutectic fatty acid phase change materials
• Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K
• Solid Liquid Equilibria in the Binary Systems of Saturated Fatty Acids or Triglycerides (C12 to C18) + Hexadecane
• Solid-Liquid Equilibrium of Binary Systems Containing Fatty Acids and Fatty Alcohols Using Differential Scanning Calorimetry
• Solid-Liquid Equilibrium of Binary Fatty Acid Mixtures
• Solubilities of Fatty Acids and Triglycerides in 1-Bromopropane
• Vapor Pressures and Vaporization, Sublimation, and Fusion Enthalpies of Some Fatty Acids
• Study of the Effect of Pressure on Melting Behavior of Saturated Fatty Acids in Liquid or Supercritical Carbon Dioxide
• Solubilities of Dodecanoic and Tetradecanoic Acids in Supercritical CO2 with and without Entrainers
• Joback Method
• Aqueous Solubility Prediction Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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