Chemical Properties of 1-Tetradecanol (CAS 112-72-1)

InChI

InChI=1S/C14H30O/c1-2-3-4-5-6-7-8-9-10-11-12-13-14-15/h15H,2-14H2,1H3

InChI Key

HLZKNKRTKFSKGZ-UHFFFAOYSA-N

Formula

C14H30O

SMILES

CCCCCCCCCCCCCCO

Molecular Weight¹

214.39

CAS

112-72-1

Other Names

• 1-Hydroxytetradecane
• 150138-88-8
• 8032-14-2
• Alfol 14
• Dehydag wax 14
• Dytol R-52
• Epal 14
• Fatty alcohol (C14)
• Lanette 14
• Lanette K
• Lanette Wax KS
• Lorol C14
• Loxanol V
• NSC 8549
• Philcohol 1400
• Tetradecan-1-ol
• Tetradecanol-1
• myristic alcohol
• myristyl alcohol
• n-Tetradecan-1-ol
• n-Tetradecanol
• n-Tetradecanol-1
• n-Tetradecyl alcohol
• tetradecanol
• tetradecyl alcohol

• ω : Acentric Factor.
• 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_fH°_solid : Solid phase 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_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	[0.7168; 1.0060]
ω	0.7810		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.7168		ChemSep v8.3 pure component data Compiled value
ω	1.0060		KDB
ΔcH°solid	[-9213.00; -9167.00]	kJ/mol
ΔcH°solid	-9168.40 ± 1.20	kJ/mol	NIST
ΔcH°solid	-9213.00 ± 8.00	kJ/mol	NIST
ΔcH°solid	-9167.00 ± 0.60	kJ/mol	NIST
μ	1.60	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	-66.90	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[-481.10; -474.80]	kJ/mol
ΔfH°gas	-481.10	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-474.80 ± 2.60	kJ/mol	NIST
ΔfH°gas	-476.20	kJ/mol	NIST
ΔfH°solid	[-629.60; -628.20]	kJ/mol
ΔfH°solid	-628.20 ± 1.50	kJ/mol	NIST
ΔfH°solid	-629.60 ± 0.60	kJ/mol	NIST
ΔfusH°	[47.60; 98.90]	kJ/mol
ΔfusH°	47.60	kJ/mol	Solid-Liquid Equilibrium of Binary Systems Containing Fatty Acids and Fatty Alcohols Using Differential Scanning Calorimetry
ΔfusH°	98.90	kJ/mol	Evaluation of the Vaporization, Fusion, and Sublimation Enthalpies of the 1-Alkanols: The Vaporization Enthalpy of 1-, 6-, 7-, and 9-Heptadecanol, 1-Octadecanol, 1-Eicosanol, 1-Docosanol, 1-Hexacosanol, and Cholesterol at T ) 298.15 K by Correlation Gas Chromatography
ΔsubH°	[102.20; 153.40]	kJ/mol
ΔsubH°	153.40 ± 1.90	kJ/mol	NIST
ΔsubH°	153.40	kJ/mol	NIST
ΔsubH°	102.20 ± 2.30	kJ/mol	NIST
ΔsubH°	144.00 ± 2.00	kJ/mol	NIST
ΔvapH°	[98.70; 102.20]	kJ/mol
ΔvapH°	102.20	kJ/mol	NIST
ΔvapH°	98.90 ± 2.50	kJ/mol	NIST
ΔvapH°	98.70	kJ/mol	NIST
ΔvapH°	102.20 ± 2.30	kJ/mol	NIST
IE	9.98	eV	Relay (1.0) Calculated Property
log10WS	[-6.11; -5.84]
log10WS	-6.11		Aq. Solubility Prediction
log10WS	-5.84		Estimated Solubility
logPoct/wat	4.680		Crippen Calculated Property
McVol	213.990	ml/mol	McGowan Calculated Property
Pc	[1669.84; 1810.00]	kPa
Pc	1669.84	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	1680.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	1810.00	kPa	KDB
Ptriple	9.16e-05	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[282.29; 1692.00]
Inp	1675.00		NIST
Inp	1664.40		NIST
Inp	1678.20		NIST
Inp	1676.00		NIST
Inp	1669.00		NIST
Inp	1646.00		NIST
Inp	1652.00		NIST
Inp	1655.00		NIST
Inp	1657.00		NIST
Inp	1659.00		NIST
Inp	1653.00		NIST
Inp	1661.00		NIST
Inp	1670.00		NIST
Inp	1658.00		NIST
Inp	1669.00		NIST
Inp	1664.00		NIST
Inp	1680.00		NIST
Inp	1675.00		NIST
Inp	1680.00		NIST
Inp	1673.00		NIST
Inp	1679.00		NIST
Inp	1674.00		NIST
Inp	1686.00		NIST
Inp	1676.00		NIST
Inp	1676.00		NIST
Inp	1675.00		NIST
Inp	1672.00		NIST
Inp	1661.00		NIST
Inp	1647.00		NIST
Inp	1676.00		NIST
Inp	1679.00		NIST
Inp	1681.10		NIST
Inp	1664.00		NIST
Inp	1675.00		NIST
Inp	1647.00		NIST
Inp	1647.00		NIST
Inp	1676.00		NIST
Inp	1675.00		NIST
Inp	1670.00		NIST
Inp	1687.00		NIST
Inp	1680.60		NIST
Inp	1660.00		NIST
Inp	1665.00		NIST
Inp	1676.00		NIST
Inp	1680.00		NIST
Inp	1677.00		NIST
Inp	1668.00		NIST
Inp	1652.00		NIST
Inp	1659.00		NIST
Inp	1663.00		NIST
Inp	1665.00		NIST
Inp	1653.00		NIST
Inp	1678.00		NIST
Inp	1685.00		NIST
Inp	1671.00		NIST
Inp	1683.00		NIST
Inp	1692.00		NIST
Inp	1692.00		NIST
Inp	1672.00		NIST
Inp	1684.00		NIST
Inp	1680.00		NIST
Inp	1672.00		NIST
Inp	1673.00		NIST
Inp	1677.00		NIST
Inp	1675.00		NIST
Inp	1680.00		NIST
Inp	1676.00		NIST
Inp	1677.00		NIST
Inp	1673.00		NIST
Inp	1662.00		NIST
Inp	1665.00		NIST
Inp	Outlier 282.29		NIST
Inp	Outlier 283.90		NIST
Inp	Outlier 283.29		NIST
Inp	1679.00		NIST
Inp	1675.00		NIST
Inp	1685.00		NIST
Inp	1672.00		NIST
Inp	1677.00		NIST
Inp	1673.00		NIST
Inp	1676.00		NIST
Inp	1660.00		NIST
Inp	1668.00		NIST
Inp	1653.00		NIST
Ip	[2123.00; 2204.00]
Ip	2137.00		NIST
Ip	2175.00		NIST
Ip	2164.00		NIST
Ip	2161.00		NIST
Ip	2165.00		NIST
Ip	2165.00		NIST
Ip	2177.00		NIST
Ip	2170.00		NIST
Ip	2200.00		NIST
Ip	Outlier 2123.00		NIST
Ip	2174.00		NIST
Ip	2155.00		NIST
Ip	Outlier 2204.00		NIST
Ip	2173.00		NIST
Ip	2157.00		NIST
Ip	2157.00		NIST
Ip	2131.00		NIST
Ip	2152.00		NIST
Ip	2145.00		NIST
Ip	2180.00		NIST
Ip	2169.00		NIST
Ip	2179.00		NIST
Ip	2179.00		NIST
Ip	2152.00		NIST
Ip	2172.00		NIST
Ip	2175.00		NIST
Ip	2157.00		NIST
Ip	2179.00		NIST
Ip	2157.00		NIST
Tboil	[562.00; 564.00]	K
Tboil	564.00	K	ChemSep v8.3 pure component data Compiled value
Tboil	562.00	K	KDB
Tboil	562.20	K	NIST
Tc	[738.70; 747.00]	K
Tc	743.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	738.70	K	ChemSep v8.3 pure component data Compiled value
Tc	747.00	K	KDB
Tfus	[309.15; 312.65]	K
Tfus	310.71	K	Solid-liquid phase equilibrium diagrams of binary mixtures containing fatty acids, fatty alcohol compounds and tripalmitin using differential scanning calorimetry
Tfus	309.15	K	The manufacture of organic carbonate-poly(methyl ethylacrylate) nanowebs with thermal buffering effect
Tfus	310.60	K	High Pressure Solid-Liquid Equilibrium of Fatty Alcohols Binary Systems from 1-Dodecanol, 1-Tetradecanol, 1-Hexadecanol, and 1-Octadecanol
Tfus	312.65	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	310.75	K	ChemSep v8.3 pure component data Compiled value
Tfus	312.60	K	KDB
Tfus	312.65	K	Aq. Solubility Prediction
Tfus	311.00 ± 1.00	K	NIST
Tfus	310.15 ± 0.50	K	NIST
Tfus	311.00 ± 0.05	K	NIST
Tfus	311.21 ± 0.05	K	NIST
Tfus	310.79 ± 0.50	K	NIST
Tfus	310.10 ± 0.60	K	NIST
Tfus	310.20 ± 2.00	K	NIST
Tfus	312.00 ± 1.20	K	NIST
Tfus	309.55 ± 0.50	K	NIST
Tfus	310.75 ± 0.20	K	NIST
Tfus	311.00 ± 1.50	K	NIST
Ttriple	[310.65; 311.35]	K
Ttriple	310.65	K	ChemSep v8.3 pure component data Compiled value
Ttriple	311.35 ± 0.50	K	NIST
UQi	9.07		ChemSep v8.3 pure component data Compiled value
URi	10.67		ChemSep v8.3 pure component data Compiled value
Vc	[0.826; 0.839]	m3/kmol
Vc	0.826	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.826	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.839	m3/kmol	KDB
Zc	[0.2443570; 0.2530000]
Zc	0.2530000		ChemSep v8.3 pure component data Compiled value
Zc	0.2443570		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	516.00	J/mol×K	313.15	NIST
Cp,solid	[388.00; 506.00]	J/mol×K	[298.15; 312.00]
Cp,solid	426.50	J/mol×K	298.15	NIST
Cp,solid	388.00	J/mol×K	298.15	NIST
Cp,solid	506.00	J/mol×K	312.00	NIST
ΔfusH	[1.80; 49.40]	kJ/mol	[306.00; 311.60]
ΔfusH	1.80	kJ/mol	306.00	NIST
ΔfusH	47.29	kJ/mol	308.10	NIST
ΔfusH	25.10	kJ/mol	310.80	NIST
ΔfusH	49.40	kJ/mol	311.00	NIST
ΔfusH	23.81	kJ/mol	311.00	NIST
ΔfusH	49.37	kJ/mol	311.00	NIST
ΔfusH	47.01	kJ/mol	311.20	NIST
ΔfusH	22.01	kJ/mol	311.60	NIST
ΔsubH	143.90	kJ/mol	300.00	NIST
ΔvapH	[72.17; 109.00]	kJ/mol	[319.50; 536.40]
ΔvapH	104.20	kJ/mol	319.50	NIST
ΔvapH	93.60	kJ/mol	329.00	NIST
ΔvapH	106.40	kJ/mol	335.50	NIST
ΔvapH	109.00	kJ/mol	337.50	NIST
ΔvapH	81.80	kJ/mol	385.50	NIST
ΔvapH	76.60	kJ/mol	496.50	NIST
ΔvapH	72.17	kJ/mol	536.40	KDB
Pvap	[8.32; 29.35]	kPa	[479.42; 519.18]
Pvap	8.32	kPa	479.42	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	11.05	kPa	487.56	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	11.05	kPa	487.56	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	13.89	kPa	494.50	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	16.78	kPa	500.44	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	20.26	kPa	506.63	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	24.53	kPa	513.01	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	24.53	kPa	513.07	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	29.35	kPa	519.11	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	29.35	kPa	519.18	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
ΔfusS	[5.86; 158.75]	J/mol×K	[306.00; 311.60]
ΔfusS	5.86	J/mol×K	306.00	NIST
ΔfusS	80.75	J/mol×K	310.80	NIST
ΔfusS	76.57	J/mol×K	311.00	NIST
ΔfusS	158.75	J/mol×K	311.00	NIST
ΔfusS	151.04	J/mol×K	311.20	NIST
ΔfusS	70.71	J/mol×K	311.60	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[333.93; 846.72]	J/mol×K	[298.15; 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			2.33400e+02
Coefficient B			7.27000e+02
Coefficient C			1.56230e+03
Coefficient D			5.42100e+02
Coefficient E			7.23000e+02
Temperature range, min.			298.15
Temperature range, max.			1500.00
Cp,gas	333.93	J/mol×K	298.15	Calculated Property
Cp,gas	460.06	J/mol×K	431.69	Calculated Property
Cp,gas	559.06	J/mol×K	565.23	Calculated Property
Cp,gas	634.48	J/mol×K	698.77	Calculated Property
Cp,gas	693.24	J/mol×K	832.31	Calculated Property
Cp,gas	739.44	J/mol×K	965.84	Calculated Property
Cp,gas	775.93	J/mol×K	1099.38	Calculated Property
Cp,gas	804.90	J/mol×K	1232.92	Calculated Property
Cp,gas	828.05	J/mol×K	1366.46	Calculated Property
Cp,gas	846.72	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[534.43; 687.73]	J/mol×K	[324.00; 569.00]	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			-4.40410e+03
Coefficient B			3.76460e+01
Coefficient C			-1.03060e-01
Coefficient D			1.20780e-04
Coefficient E			-4.97230e-08
Temperature range, min.			324.00
Temperature range, max.			569.00
Cp,liquid	534.43	J/mol×K	324.00	Calculated Property
Cp,liquid	581.08	J/mol×K	351.22	Calculated Property
Cp,liquid	609.01	J/mol×K	378.44	Calculated Property
Cp,liquid	624.04	J/mol×K	405.67	Calculated Property
Cp,liquid	631.36	J/mol×K	432.89	Calculated Property
Cp,liquid	635.50	J/mol×K	460.11	Calculated Property
Cp,liquid	640.31	J/mol×K	487.33	Calculated Property
Cp,liquid	649.03	J/mol×K	514.56	Calculated Property
Cp,liquid	664.20	J/mol×K	541.78	Calculated Property
Cp,liquid	687.73	J/mol×K	569.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0134885; 0.0002416]	Pa×s	[310.65; 569.00]	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			-8.24520e+01
Coefficient B			6.80920e+03
Coefficient C			9.79790e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			310.65
Temperature range, max.			569.00
η	0.0134885	Pa×s	310.65	Calculated Property
η	0.0050213	Pa×s	339.36	Calculated Property
η	0.0023265	Pa×s	368.06	Calculated Property
η	0.0012734	Pa×s	396.77	Calculated Property
η	0.0007932	Pa×s	425.47	Calculated Property
η	0.0005469	Pa×s	454.18	Calculated Property
η	0.0004089	Pa×s	482.88	Calculated Property
η	0.0003264	Pa×s	511.59	Calculated Property
η	0.0002747	Pa×s	540.29	Calculated Property
η	0.0002416	Pa×s	569.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[95.76; 0.00]	kJ/mol	[310.65; 738.70]	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			1.01670e+02
Coefficient B			-1.16650e+00
Coefficient C			4.16700e+00
Coefficient D			-2.69220e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			7.38700e+02
Comment			Range stopped at Tc; ChemSep gives it to 745.3 K.
Temperature range, min.			310.65
Temperature range, max.			738.70
ΔvapH	95.76	kJ/mol	310.65	Calculated Property
ΔvapH	87.80	kJ/mol	358.21	Calculated Property
ΔvapH	79.41	kJ/mol	405.77	Calculated Property
ΔvapH	71.05	kJ/mol	453.33	Calculated Property
ΔvapH	63.07	kJ/mol	500.89	Calculated Property
ΔvapH	55.72	kJ/mol	548.46	Calculated Property
ΔvapH	49.07	kJ/mol	596.02	Calculated Property
ΔvapH	42.95	kJ/mol	643.58	Calculated Property
ΔvapH	36.30	kJ/mol	691.14	Calculated Property
ΔvapH	0.00	kJ/mol	738.70	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[442.04; 589.72]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.69720e+01
Coefficient B			-5.71881e+03
Coefficient C			-9.92760e+01
Temperature range, min.			442.04
Temperature range, max.			589.72
Pvap	1.33	kPa	442.04	Calculated Property
Pvap	2.86	kPa	458.45	Calculated Property
Pvap	5.73	kPa	474.86	Calculated Property
Pvap	10.84	kPa	491.27	Calculated Property
Pvap	19.47	kPa	507.68	Calculated Property
Pvap	33.45	kPa	524.08	Calculated Property
Pvap	55.18	kPa	540.49	Calculated Property
Pvap	87.82	kPa	556.90	Calculated Property
Pvap	135.36	kPa	573.31	Calculated Property
Pvap	202.66	kPa	589.72	Calculated Property
Pvap	[9.20e-05; 1537.73]	kPa	[310.65; 738.70]	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			1.73942e+02
Coefficient B			-1.83180e+04
Coefficient C			-2.16560e+01
Coefficient D			7.56370e-18
Coefficient E			6.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 745.3 K.
Temperature range, min.			310.65
Temperature range, max.			738.70
Pvap	9.20e-05	kPa	310.65	Calculated Property
Pvap	0.01	kPa	358.21	Calculated Property
Pvap	0.29	kPa	405.77	Calculated Property
Pvap	3.12	kPa	453.33	Calculated Property
Pvap	17.62	kPa	500.89	Calculated Property
Pvap	64.21	kPa	548.46	Calculated Property
Pvap	174.10	kPa	596.02	Calculated Property
Pvap	390.20	kPa	643.58	Calculated Property
Pvap	787.01	kPa	691.14	Calculated Property
Pvap	1537.73	kPa	738.70	Calculated Property
Pvap	[8.63e-05; 1801.78]	kPa	[310.65; 741.00]	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			2.83615e+02
Coefficient B			-2.31007e+04
Coefficient C			-3.83547e+01
Coefficient D			1.54882e-05
Coefficient E			0.00000e+00
Temperature range, min.			310.65
Temperature range, max.			741.00
Pvap	8.63e-05	kPa	310.65	Calculated Property
Pvap	0.01	kPa	358.47	Calculated Property
Pvap	0.34	kPa	406.28	Calculated Property
Pvap	3.57	kPa	454.10	Calculated Property
Pvap	19.80	kPa	501.92	Calculated Property
Pvap	72.08	kPa	549.73	Calculated Property
Pvap	198.56	kPa	597.55	Calculated Property
Pvap	456.38	kPa	645.37	Calculated Property
Pvap	936.72	kPa	693.18	Calculated Property
Pvap	1801.78	kPa	741.00	Calculated Property
Pvap	[0.77; 99.62]	kPa	[424.80; 569.10]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.29151e+01
Coefficient B			-3.25334e+03
Coefficient C			-1.77782e+02
Reference			Kemme and Kreps, 1969
Temperature range, min.			424.80
Temperature range, max.			569.10
Pvap	0.77	kPa	424.80	Calculated Property
Pvap	1.73	kPa	440.83	Calculated Property
Pvap	3.52	kPa	456.87	Calculated Property
Pvap	6.63	kPa	472.90	Calculated Property
Pvap	11.70	kPa	488.93	Calculated Property
Pvap	19.53	kPa	504.97	Calculated Property
Pvap	31.07	kPa	521.00	Calculated Property
Pvap	47.43	kPa	537.03	Calculated Property
Pvap	69.84	kPa	553.07	Calculated Property
Pvap	99.62	kPa	569.10	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[822.61; 340.52]	kg/m3	[310.65; 738.70]	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			5.21003e+01
Coefficient B			2.26740e-01
Coefficient C			7.45300e+02
Coefficient D			2.80910e-01
Comment			Range stopped at Tc; ChemSep gives it to 745.3 K.
Temperature range, min.			310.65
Temperature range, max.			738.70
ρl	822.61	kg/m3	310.65	Calculated Property
ρl	789.68	kg/m3	358.21	Calculated Property
ρl	755.21	kg/m3	405.77	Calculated Property
ρl	718.82	kg/m3	453.33	Calculated Property
ρl	679.97	kg/m3	500.89	Calculated Property
ρl	637.82	kg/m3	548.46	Calculated Property
ρl	590.95	kg/m3	596.02	Calculated Property
ρl	536.59	kg/m3	643.58	Calculated Property
ρl	467.60	kg/m3	691.14	Calculated Property
ρl	340.52	kg/m3	738.70	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.01]	N/m	[312.65; 562.15]	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			5.19224e-02
Coefficient B			-7.03000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			312.65
Temperature range, max.			562.15
γ	0.03	N/m	312.65	Calculated Property
γ	0.03	N/m	340.37	Calculated Property
γ	0.03	N/m	368.09	Calculated Property
γ	0.02	N/m	395.82	Calculated Property
γ	0.02	N/m	423.54	Calculated Property
γ	0.02	N/m	451.26	Calculated Property
γ	0.02	N/m	478.98	Calculated Property
γ	0.02	N/m	506.71	Calculated Property
γ	0.01	N/m	534.43	Calculated Property
γ	0.01	N/m	562.15	Calculated Property
γ	[0.03; 0.00]	N/m	[310.65; 738.70]	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			5.94800e-02
Coefficient B			1.30100e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			7.38700e+02
Comment			Range stopped at Tc; ChemSep gives it to 745.3 K.
Temperature range, min.			310.65
Temperature range, max.			738.70
γ	0.03	N/m	310.65	Calculated Property
γ	0.03	N/m	358.21	Calculated Property
γ	0.02	N/m	405.77	Calculated Property
γ	0.02	N/m	453.33	Calculated Property
γ	0.01	N/m	500.89	Calculated Property
γ	0.01	N/m	548.46	Calculated Property
γ	0.01	N/m	596.02	Calculated Property
γ	0.00	N/m	643.58	Calculated Property
γ	0.00	N/m	691.14	Calculated Property
γ	0.00	N/m	738.70	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.03; 0.08]	W/m×K	[568.80; 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			-3.00400e+00
Coefficient B			-3.48740e-02
Coefficient C			-1.76630e+03
Coefficient D			-2.84780e+07
Temperature range, min.			568.80
Temperature range, max.			1000.00
λgas	0.03	W/m×K	568.80	Calculated Property
λgas	0.03	W/m×K	616.71	Calculated Property
λgas	0.04	W/m×K	664.62	Calculated Property
λgas	0.04	W/m×K	712.53	Calculated Property
λgas	0.05	W/m×K	760.44	Calculated Property
λgas	0.05	W/m×K	808.36	Calculated Property
λgas	0.06	W/m×K	856.27	Calculated Property
λgas	0.07	W/m×K	904.18	Calculated Property
λgas	0.07	W/m×K	952.09	Calculated Property
λgas	0.08	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.17; 0.12]	W/m×K	[310.65; 569.00]	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			2.31500e-01
Coefficient B			-1.98700e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			310.65
Temperature range, max.			569.00
λliquid	0.17	W/m×K	310.65	Calculated Property
λliquid	0.16	W/m×K	339.36	Calculated Property
λliquid	0.16	W/m×K	368.06	Calculated Property
λliquid	0.15	W/m×K	396.77	Calculated Property
λliquid	0.15	W/m×K	425.47	Calculated Property
λliquid	0.14	W/m×K	454.18	Calculated Property
λliquid	0.14	W/m×K	482.88	Calculated Property
λliquid	0.13	W/m×K	511.59	Calculated Property
λliquid	0.12	W/m×K	540.29	Calculated Property
λliquid	0.12	W/m×K	569.00	Calculated Property

Similar Compounds

Find more compounds similar to 1-Tetradecanol.

Mixtures

• n-Hexane + 1-Tetradecanol
• Octane + 1-Tetradecanol
• Decane + 1-Tetradecanol
• Tripalmitin + 1-Tetradecanol
• 1-Octanol + 1-Tetradecanol
• 1-Decanol + 1-Tetradecanol
• 1-Octadecanol + 1-Tetradecanol
• 1-Dodecanol + 1-Tetradecanol
• 1-Hexadecanol + 1-Tetradecanol
• Carbon dioxide + 1-Tetradecanol
• Tetradecanoic acid + 1-Tetradecanol

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
• Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
• The solid-liquid phase diagrams of binary mixtures of even saturated fatty alcohols
• Measurement and correlation of vapor-liquid equilibria for alkane + alkanol andalkane + alkanediol systems with group contribution COSMOSPACE model
• Solid-liquid phase equilibrium diagrams of binary mixtures containing fatty acids, fatty alcohol compounds and tripalmitin using differential scanning calorimetry
• The manufacture of organic carbonate-poly(methyl ethylacrylate) nanowebs with thermal buffering effect
• High Pressure Solid-Liquid Equilibrium of Fatty Alcohols Binary Systems from 1-Dodecanol, 1-Tetradecanol, 1-Hexadecanol, and 1-Octadecanol
• High Pressure Phase Behavior of the Homologous Series CO2 + 1-Alcohols
• Solid-Liquid Equilibrium of Binary Systems Containing Fatty Acids and Fatty Alcohols Using Differential Scanning Calorimetry
• Evaluation of the Vaporization, Fusion, and Sublimation Enthalpies of the 1-Alkanols: The Vaporization Enthalpy of 1-, 6-, 7-, and 9-Heptadecanol, 1-Octadecanol, 1-Eicosanol, 1-Docosanol, 1-Hexacosanol, and Cholesterol at T ) 298.15 K by Correlation Gas Chromatography
• Liquid-Liquid Phase Behavior of Solutions of 1-Dodecyl-3-methylimidazolium Bis(trifluoromethylsulphonyl)imide (C12mimNTf2) in n- Alkyl Alcohols
• Liquid-Liquid Phase Behavior of Solutions of 1-Hexyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C6mimNTf2) in n-Alkyl Alcohols
• Liquid-Liquid Phase Behavior of Solutions of 1-Octyl- and 1-Decyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide (C8,10mimNTf2) in n-Alkyl Alcohols
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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