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).
• 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_vap : Vapor pressure (kPa).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• 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	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
ΔfG°	-69.82	kJ/mol	Joback Calculated Property
ΔfH°gas	[-476.20; -474.80]	kJ/mol
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	1810.00	kPa	KDB
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
I	[2123.00; 2204.00]
I	2137.00		NIST
I	2175.00		NIST
I	2164.00		NIST
I	2161.00		NIST
I	2165.00		NIST
I	2165.00		NIST
I	2177.00		NIST
I	2170.00		NIST
I	2200.00		NIST
I	Outlier 2123.00		NIST
I	2174.00		NIST
I	2155.00		NIST
I	Outlier 2204.00		NIST
I	2173.00		NIST
I	2157.00		NIST
I	2157.00		NIST
I	2131.00		NIST
I	2152.00		NIST
I	2145.00		NIST
I	2180.00		NIST
I	2169.00		NIST
I	2179.00		NIST
I	2179.00		NIST
I	2152.00		NIST
I	2172.00		NIST
I	2175.00		NIST
I	2157.00		NIST
I	2179.00		NIST
I	2157.00		NIST
Tboil	[562.00; 562.20]	K
Tboil	562.00	K	KDB
Tboil	562.20	K	NIST
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	312.60	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	311.35 ± 0.50	K	NIST
Vc	0.839	m3/kmol	KDB
Zc	0.2443570		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[582.76; 668.73]	J/mol×K	[612.10; 770.20]
Cp,gas	582.76	J/mol×K	612.10	Joback Calculated Property
Cp,gas	598.60	J/mol×K	638.45	Joback Calculated Property
Cp,gas	613.81	J/mol×K	664.80	Joback Calculated Property
Cp,gas	628.40	J/mol×K	691.15	Joback Calculated Property
Cp,gas	642.41	J/mol×K	717.50	Joback Calculated Property
Cp,gas	655.85	J/mol×K	743.85	Joback Calculated Property
Cp,gas	668.73	J/mol×K	770.20	Joback Calculated Property
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
η	[0.0000596; 0.0130512]	Pa×s	[308.36; 612.10]
η	0.0130512	Pa×s	308.36	Joback Calculated Property
η	0.0028226	Pa×s	358.98	Joback Calculated Property
η	0.0008913	Pa×s	409.61	Joback Calculated Property
η	0.0003627	Pa×s	460.23	Joback Calculated Property
η	0.0001764	Pa×s	510.85	Joback Calculated Property
η	0.0000977	Pa×s	561.48	Joback Calculated Property
η	0.0000596	Pa×s	612.10	Joback Calculated Property
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
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	[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

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
• Cheméo Relay (1.0)
• 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
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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