Chemical Properties of 1-Dodecanol (CAS 112-53-8)

InChI

InChI=1S/C12H26O/c1-2-3-4-5-6-7-8-9-10-11-12-13/h13H,2-12H2,1H3

InChI Key

LQZZUXJYWNFBMV-UHFFFAOYSA-N

Formula

C12H26O

SMILES

CCCCCCCCCCCCO

Molecular Weight¹

186.33

CAS

112-53-8

Other Names

• 1-Dodecyl Alcohol
• 1-Hydroxydodecane
• Adol 10
• Adol 12
• Alcohol C-12
• Alfol 12
• CO-1214
• CO-1214N
• CO-1214S
• Cachalot l-50
• Cachalot l-90
• Conol 20P
• Conol 20PP
• Dodecanol-1
• Duodecyl alcohol
• Dytol J-68
• Epal 12
• Hainol 12SS
• Hydroxydodecane
• Karukoru 20
• Lauric Alcohol
• Laurinic alcohol
• Lauryl 24
• Lorol 11
• Lorol 5
• Lorol 7
• Lorol C12
• MA-1214
• NAA 42
• Nacol 12-96
• Pisol
• S 1298
• Sipol L12
• Siponol 25
• Siponol L2
• Siponol L5
• Undecyl carbinol
• dodecan-1-ol
• dodecanol
• dodecyl alcohol
• lauryl alcohol
• n-Dodecan-1-ol
• n-Dodecanol
• n-Lauryl alcohol
• n-Lauryl alcohol, primary
• n-dodecyl alcohol

• ω : Acentric Factor.
• 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).
• 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°_liquid : Liquid 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).
• NFPA Fire : NFPA Fire Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• γ : Surface Tension (N/m).
• Δ_vapS : Entropy of vaporization at a given temperature (J/mol×K).
• 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	[0.6556; 0.7202]
ω	0.7202		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.6556		ChemSep v8.3 pure component data Compiled value
ΔcH°liquid	[-7950.00; -7909.40]	kJ/mol
ΔcH°liquid	-7950.00 ± 10.00	kJ/mol	NIST
ΔcH°liquid	-7909.40 ± 0.80	kJ/mol	NIST
μ	[1.60; 1.69]	debye
μ	1.69	debye	ChemSep v8.3 pure component data Compiled value
μ	1.60	debye	KDB
ΔfG°	[-87.13; -83.35]	kJ/mol
ΔfG°	-83.35	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	-87.13	kJ/mol	KDB
ΔfH°gas	[-443.10; -436.50]	kJ/mol
ΔfH°gas	-439.60	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-443.10	kJ/mol	KDB
ΔfH°gas	-436.50 ± 1.00	kJ/mol	NIST
ΔfH°gas	-436.50 ± 1.00	kJ/mol	NIST
ΔfH°liquid	-528.50 ± 0.80	kJ/mol	NIST
ΔfusH°	[37.74; 90.80]	kJ/mol
ΔfusH°	40.20	kJ/mol	Solid-Liquid Equilibrium of Binary Systems Containing Fatty Acids and Fatty Alcohols Using Differential Scanning Calorimetry
ΔfusH°	40.31	kJ/mol	Heat capacities and derived thermodynamic functions of 1-dodecanol and 1-tridecanol between 10 K and 370 K and heat capacities of 1-pentadecanol and 1-heptadecanol between 300 K and 380 K and correlationos for the heat capacity and the entropy of liquid n-alcohols
ΔfusH°	90.80	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
ΔfusH°	37.74	kJ/mol	Measurements, Correlations, and Mod. UNIFAC (Do) Prediction of (Solid-Liquid) Phase Equilibria Diagrams in Binary Systems (Aliphatic Ketone + an Alcohol)
ΔsubH°	129.30	kJ/mol	NIST
ΔvapH°	[90.00; 92.00]	kJ/mol
ΔvapH°	90.80 ± 1.20	kJ/mol	NIST
ΔvapH°	Outlier 90.00	kJ/mol	NIST
ΔvapH°	91.70	kJ/mol	NIST
ΔvapH°	91.70	kJ/mol	NIST
ΔvapH°	91.79 ± 0.58	kJ/mol	NIST
ΔvapH°	91.80 ± 0.60	kJ/mol	NIST
ΔvapH°	91.96 ± 0.59	kJ/mol	NIST
ΔvapH°	92.00 ± 0.60	kJ/mol	NIST
IE	9.94	eV	Relay (1.0) Calculated Property
log10WS	[-4.80; -4.67]
log10WS	-4.67		Aq. Solubility Prediction
log10WS	-4.80		Estimated Solubility
logPoct/wat	3.900		Crippen Calculated Property
McVol	185.810	ml/mol	McGowan Calculated Property
NFPA Fire	1		KDB
Pc	[1954.00; 1994.00]	kPa
Pc	1994.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Pc	1994.00	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	Outlier 1954.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	1994.00	kPa	KDB
Pc	1990.00 ± 50.00	kPa	NIST
Pc	1994.00 ± 50.00	kPa	NIST
Pc	1994.00 ± 50.00	kPa	NIST
Ptriple	[9.60e-05; 1.02e-04]	kPa
Ptriple	1.02e-04	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	9.60e-05 ± 2.70e-05	kPa	NIST
Inp	[250.63; 1490.00]
Inp	1455.10		NIST
Inp	1463.10		NIST
Inp	1456.60		NIST
Inp	1461.00		NIST
Inp	1477.00		NIST
Inp	1472.00		NIST
Inp	1473.00		NIST
Inp	1448.00		NIST
Inp	1451.00		NIST
Inp	1451.00		NIST
Inp	1450.00		NIST
Inp	1449.00		NIST
Inp	1442.00		NIST
Inp	1458.00		NIST
Inp	1432.00		NIST
Inp	1453.00		NIST
Inp	1458.00		NIST
Inp	1471.00		NIST
Inp	1435.00		NIST
Inp	1473.00		NIST
Inp	1457.00		NIST
Inp	1459.00		NIST
Inp	1463.00		NIST
Inp	1465.00		NIST
Inp	1471.00		NIST
Inp	1469.00		NIST
Inp	1466.00		NIST
Inp	1474.00		NIST
Inp	1457.10		NIST
Inp	1460.00		NIST
Inp	1474.00		NIST
Inp	1473.00		NIST
Inp	1468.90		NIST
Inp	1473.00		NIST
Inp	1475.00		NIST
Inp	1472.00		NIST
Inp	1473.00		NIST
Inp	1460.00		NIST
Inp	1460.00		NIST
Inp	1487.00		NIST
Inp	1456.50		NIST
Inp	1456.80		NIST
Inp	1442.00		NIST
Inp	1443.00		NIST
Inp	1473.00		NIST
Inp	1478.20		NIST
Inp	1482.80		NIST
Inp	1486.00		NIST
Inp	1490.00		NIST
Inp	1456.00		NIST
Inp	1462.00		NIST
Inp	1471.00		NIST
Inp	1475.00		NIST
Inp	1472.00		NIST
Inp	1472.00		NIST
Inp	1476.00		NIST
Inp	1477.00		NIST
Inp	1475.00		NIST
Inp	1474.00		NIST
Inp	1472.00		NIST
Inp	1476.00		NIST
Inp	1475.00		NIST
Inp	1472.00		NIST
Inp	1430.00		NIST
Inp	1464.00		NIST
Inp	1451.00		NIST
Inp	1474.00		NIST
Inp	1475.00		NIST
Inp	1458.00		NIST
Inp	1473.00		NIST
Inp	1466.00		NIST
Inp	1466.00		NIST
Inp	1466.00		NIST
Inp	1466.00		NIST
Inp	1479.00		NIST
Inp	1476.00		NIST
Inp	1478.00		NIST
Inp	1465.00		NIST
Inp	1457.00		NIST
Inp	1460.00		NIST
Inp	1461.00		NIST
Inp	1468.00		NIST
Inp	1462.00		NIST
Inp	1458.00		NIST
Inp	1462.00		NIST
Inp	1488.00		NIST
Inp	1468.00		NIST
Inp	1468.00		NIST
Inp	1469.00		NIST
Inp	1477.00		NIST
Inp	1479.00		NIST
Inp	1483.00		NIST
Inp	1484.00		NIST
Inp	1484.00		NIST
Inp	1474.00		NIST
Inp	1470.00		NIST
Inp	1457.00		NIST
Inp	1484.00		NIST
Inp	1487.00		NIST
Inp	1474.00		NIST
Inp	1476.00		NIST
Inp	1471.00		NIST
Inp	1476.00		NIST
Inp	1480.00		NIST
Inp	1485.00		NIST
Inp	1471.00		NIST
Inp	1468.00		NIST
Inp	1470.00		NIST
Inp	1468.00		NIST
Inp	1468.00		NIST
Inp	1476.00		NIST
Inp	1475.00		NIST
Inp	1465.00		NIST
Inp	1458.00		NIST
Inp	1460.00		NIST
Inp	Outlier 250.63		NIST
Inp	Outlier 252.06		NIST
Inp	Outlier 251.68		NIST
Inp	1469.00		NIST
Inp	1474.00		NIST
Inp	1472.00		NIST
Inp	1456.50		NIST
Inp	1468.00		NIST
Inp	1483.00		NIST
Inp	1457.00		NIST
Inp	1471.00		NIST
Inp	1475.00		NIST
Inp	1455.10		NIST
Inp	1450.00		NIST
Inp	1453.00		NIST
Ip	[1919.00; 1984.00]
Ip	1935.00		NIST
Ip	1942.00		NIST
Ip	Outlier 1924.00		NIST
Ip	1962.00		NIST
Ip	1957.00		NIST
Ip	1960.00		NIST
Ip	1960.00		NIST
Ip	1979.00		NIST
Ip	1950.00		NIST
Ip	1940.00		NIST
Ip	1980.00		NIST
Ip	1943.00		NIST
Ip	1952.00		NIST
Ip	Outlier 1925.00		NIST
Ip	Outlier 1925.00		NIST
Ip	1940.00		NIST
Ip	1970.00		NIST
Ip	1961.00		NIST
Ip	1981.00		NIST
Ip	1970.00		NIST
Ip	1930.00		NIST
Ip	1970.00		NIST
Ip	1981.00		NIST
Ip	1977.00		NIST
Ip	1977.00		NIST
Ip	1948.00		NIST
Ip	1962.00		NIST
Ip	1977.00		NIST
Ip	1977.00		NIST
Ip	1975.00		NIST
Ip	1950.00		NIST
Ip	1950.00		NIST
Ip	Outlier 1920.00		NIST
Ip	1973.00		NIST
Ip	1957.00		NIST
Ip	1964.00		NIST
Ip	1969.00		NIST
Ip	1955.00		NIST
Ip	1953.00		NIST
Ip	1983.00		NIST
Ip	1968.00		NIST
Ip	1963.00		NIST
Ip	1956.00		NIST
Ip	1956.00		NIST
Ip	1959.00		NIST
Ip	1961.00		NIST
Ip	1956.00		NIST
Ip	1977.00		NIST
Ip	1953.00		NIST
Ip	1969.00		NIST
Ip	1973.00		NIST
Ip	1961.00		NIST
Ip	Outlier 1919.00		NIST
Ip	1946.00		NIST
Ip	Outlier 1920.00		NIST
Ip	Outlier 1925.00		NIST
Ip	1973.00		NIST
Ip	1973.00		NIST
Ip	1977.00		NIST
Ip	1983.00		NIST
Ip	1984.00		NIST
Ip	1973.00		NIST
Ip	1957.00		NIST
Ip	1981.00		NIST
Ip	1981.00		NIST
Ip	1973.00		NIST
Ip	1973.00		NIST
Ip	1973.00		NIST
Ip	1973.00		NIST
Ip	1973.00		NIST
Ip	1973.00		NIST
Ip	1973.00		NIST
Ip	1973.00		NIST
Ip	Outlier 1925.00		NIST
Ip	1973.00		NIST
Ip	1973.00		NIST
Ip	1973.00		NIST
Ip	1973.00		NIST
Ip	1973.00		NIST
Ip	1974.00		NIST
Ip	1947.00		NIST
Ip	1950.00		NIST
Ip	1983.00		NIST
Ip	1953.00		NIST
Ip	1956.00		NIST
Ip	1946.00		NIST
Ip	1935.00		NIST
Ip	1960.00		NIST
Ip	1980.00		NIST
Ip	1973.00		NIST
Ip	1950.00		NIST
Ip	Outlier 1925.00		NIST
Tboil	[532.00; 537.10]	K
Tboil	532.50	K	(Liquid + liquid) equilibria of (water + propionic acid + alcohol) ternary systems
Tboil	537.10	K	ChemSep v8.3 pure component data Compiled value
Tboil	532.00	K	KDB
Tboil	534.20	K	NIST
Tc	[717.00; 719.40]	K
Tc	719.40	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Tc	Outlier 717.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	718.70	K	ChemSep v8.3 pure component data Compiled value
Tc	719.40	K	KDB
Tc	719.40 ± 1.50	K	NIST
Tc	719.40 ± 0.80	K	NIST
Tc	719.40 ± 0.80	K	NIST
Tc	719.40	K	NIST
Tfus	[296.15; 298.00]	K
Tfus	297.78	K	Solid-liquid phase equilibrium diagrams of binary mixtures containing fatty acids, fatty alcohol compounds and tripalmitin using differential scanning calorimetry
Tfus	297.22	K	Thermodynamics of organic mixtures containing amines. VIII. Systems with quinoline
Tfus	296.15	K	The manufacture of organic carbonate-poly(methyl ethylacrylate) nanowebs with thermal buffering effect
Tfus	296.90	K	High Pressure Solid-Liquid Equilibrium of Fatty Alcohols Binary Systems from 1-Dodecanol, 1-Tetradecanol, 1-Hexadecanol, and 1-Octadecanol
Tfus	296.51	K	Solid-Liquid Equilibria in Three Binary Mixtures Containing Diphenyl Carbonate
Tfus	297.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	296.95	K	ChemSep v8.3 pure component data Compiled value
Tfus	297.00	K	KDB
Tfus	297.65	K	Aq. Solubility Prediction
Tfus	Outlier 298.00 ± 1.00	K	NIST
Tfus	296.65 ± 0.50	K	NIST
Tfus	296.60 ± 0.60	K	NIST
Tfus	297.15 ± 1.00	K	NIST
Tfus	296.65 ± 0.50	K	NIST
Tfus	296.65 ± 1.50	K	NIST
Tfus	297.30 ± 0.15	K	NIST
Tfus	297.00 ± 3.00	K	NIST
Tfus	297.15 ± 1.00	K	NIST
Tfus	297.15 ± 1.00	K	NIST
Tfus	296.55 ± 0.50	K	NIST
Ttriple	[296.95; 296.95]	K
Ttriple	296.95	K	ChemSep v8.3 pure component data Compiled value
Ttriple	296.95 ± 0.50	K	NIST
UQi	7.99		ChemSep v8.3 pure component data Compiled value
URi	9.32		ChemSep v8.3 pure component data Compiled value
Vc	[0.718; 0.787]	m3/kmol
Vc	0.718	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.787	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	[0.2393550; 0.2570000]
Zc	0.2570000		ChemSep v8.3 pure component data Compiled value
Zc	0.2393550		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[438.42; 462.00]	J/mol×K	[298.15; 316.00]
Cp,liquid	438.42	J/mol×K	298.15	NIST
Cp,liquid	439.40	J/mol×K	303.15	NIST
Cp,liquid	462.00	J/mol×K	316.00	NIST
ΔfusH	[40.17; 40.31]	kJ/mol	[297.30; 300.20]
ΔfusH	40.31	kJ/mol	297.30	NIST
ΔfusH	40.17	kJ/mol	300.20	NIST
ΔfusH	40.17	kJ/mol	300.20	NIST
ΔsubH	130.10 ± 1.20	kJ/mol	289.50	NIST
ΔvapH	[57.10; 95.40]	kJ/mol	[297.00; 533.10]
ΔvapH	95.00 ± 2.00	kJ/mol	297.00	NIST
ΔvapH	95.40	kJ/mol	305.00	NIST
ΔvapH	85.80	kJ/mol	325.50	NIST
ΔvapH	92.50	kJ/mol	330.00	NIST
ΔvapH	83.30	kJ/mol	333.00	NIST
ΔvapH	84.70 ± 0.50	kJ/mol	343.00	NIST
ΔvapH	84.76	kJ/mol	343.15	NIST
ΔvapH	80.50	kJ/mol	358.00	NIST
ΔvapH	73.80	kJ/mol	410.50	NIST
ΔvapH	67.60	kJ/mol	449.00	NIST
ΔvapH	67.60	kJ/mol	449.00	NIST
ΔvapH	71.50	kJ/mol	469.00	NIST
ΔvapH	66.70	kJ/mol	487.50	NIST
ΔvapH	57.10	kJ/mol	527.50	NIST
ΔvapH	67.70	kJ/mol	533.10	KDB
n0	[1.39640; 1.44120]		[298.15; 298.20]
n0	1.44058		298.15	Liquid Liquid Phase Equilibria of 1-Propanol + Water + n-Alcohol Ternary Systems at 298.15 K and Atmospheric Pressure
n0	1.39640		298.20	(Liquid + liquid) equilibria of the (water + butyric acid + dodecanol) ternary system
n0	1.44120		298.20	Solubility and Tie Line Data of the Water - Phosphoric Acid Solvents at T = (303.2 and 313.2) K: An Experimental and Correlational Study
ρl	[802.10; 835.00]	kg/m3	[293.00; 338.15]
ρl	835.00	kg/m3	293.00	KDB
ρl	831.10	kg/m3	297.15	Distribution of Butyric Acid between Water and Several Solvents
ρl	830.37	kg/m3	298.15	Liquid-liquid equilibria for aqueous sulfuric acid solutions with undecane, dodecane, or 1-dodecanol, trioctylamine or tributyl phosphate and excess and deviation properties for sub-binary systems at 298.15 K
ρl	823.35	kg/m3	298.15	Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
ρl	829.60	kg/m3	298.15	Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl	830.90	kg/m3	298.15	Solid Liquid Equilibria, Excess Molar Volumes, and Deviations in the Molar Refractivity for the Binary Systems of Alamine 304-1 + Decane, Dodecane, or Dodecanol
ρl	822.80	kg/m3	308.15	Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl	816.00	kg/m3	318.15	Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl	809.10	kg/m3	328.15	Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl	802.10	kg/m3	338.15	Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ΔvapS	246.74	J/mol×K	343.15	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[288.77; 734.06]	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			2.01500e+02
Coefficient B			6.32700e+02
Coefficient C			1.56250e+03
Coefficient D			4.67330e+02
Coefficient E			7.21200e+02
Temperature range, min.			298.15
Temperature range, max.			1500.00
Cp,gas	288.77	J/mol×K	298.15	Calculated Property
Cp,gas	397.58	J/mol×K	431.69	Calculated Property
Cp,gas	483.03	J/mol×K	565.23	Calculated Property
Cp,gas	548.41	J/mol×K	698.77	Calculated Property
Cp,gas	599.57	J/mol×K	832.31	Calculated Property
Cp,gas	639.95	J/mol×K	965.84	Calculated Property
Cp,gas	671.91	J/mol×K	1099.38	Calculated Property
Cp,gas	697.32	J/mol×K	1232.92	Calculated Property
Cp,gas	717.65	J/mol×K	1366.46	Calculated Property
Cp,gas	734.06	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[428.06; 582.44]	J/mol×K	[296.95; 537.10]	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			-1.24210e+03
Coefficient B			1.04400e+01
Coefficient C			-2.00550e-02
Coefficient D			1.29250e-05
Coefficient E			0.00000e+00
Temperature range, min.			296.95
Temperature range, max.			537.10
Cp,liquid	428.06	J/mol×K	296.95	Calculated Property
Cp,liquid	474.22	J/mol×K	323.63	Calculated Property
Cp,liquid	509.69	J/mol×K	350.32	Calculated Property
Cp,liquid	535.94	J/mol×K	377.00	Calculated Property
Cp,liquid	554.45	J/mol×K	403.68	Calculated Property
Cp,liquid	566.69	J/mol×K	430.37	Calculated Property
Cp,liquid	574.14	J/mol×K	457.05	Calculated Property
Cp,liquid	578.26	J/mol×K	483.73	Calculated Property
Cp,liquid	580.54	J/mol×K	510.42	Calculated Property
Cp,liquid	582.44	J/mol×K	537.10	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0195173; 0.0002539]	Pa×s	[293.15; 537.10]	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			-7.64970e+01
Coefficient B			6.31280e+03
Coefficient C			8.98240e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			293.15
Temperature range, max.			537.10
η	0.0195173	Pa×s	293.15	Calculated Property
η	0.0069800	Pa×s	320.26	Calculated Property
η	0.0031101	Pa×s	347.36	Calculated Property
η	0.0016390	Pa×s	374.47	Calculated Property
η	0.0009841	Pa×s	401.57	Calculated Property
η	0.0006548	Pa×s	428.68	Calculated Property
η	0.0004731	Pa×s	455.78	Calculated Property
η	0.0003653	Pa×s	482.89	Calculated Property
η	0.0002978	Pa×s	509.99	Calculated Property
η	0.0002539	Pa×s	537.10	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[92.88; 0.00]	kJ/mol	[296.95; 718.70]	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			9.00700e+01
Coefficient B			-1.62490e+00
Coefficient C			5.11330e+00
Coefficient D			-3.19490e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			7.18700e+02
Temperature range, min.			296.95
Temperature range, max.			718.70
ΔvapH	92.88	kJ/mol	296.95	Calculated Property
ΔvapH	84.94	kJ/mol	343.81	Calculated Property
ΔvapH	76.36	kJ/mol	390.67	Calculated Property
ΔvapH	67.72	kJ/mol	437.53	Calculated Property
ΔvapH	59.49	kJ/mol	484.39	Calculated Property
ΔvapH	51.98	kJ/mol	531.26	Calculated Property
ΔvapH	45.32	kJ/mol	578.12	Calculated Property
ΔvapH	39.42	kJ/mol	624.98	Calculated Property
ΔvapH	33.42	kJ/mol	671.84	Calculated Property
ΔvapH	0.00	kJ/mol	718.70	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[416.56; 561.39]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.66246e+01
Coefficient B			-5.32811e+03
Coefficient C			-9.04220e+01
Temperature range, min.			416.56
Temperature range, max.			561.39
Pvap	1.33	kPa	416.56	Calculated Property
Pvap	2.87	kPa	432.65	Calculated Property
Pvap	5.78	kPa	448.74	Calculated Property
Pvap	10.96	kPa	464.84	Calculated Property
Pvap	19.70	kPa	480.93	Calculated Property
Pvap	33.80	kPa	497.02	Calculated Property
Pvap	55.67	kPa	513.11	Calculated Property
Pvap	88.38	kPa	529.21	Calculated Property
Pvap	135.81	kPa	545.30	Calculated Property
Pvap	202.65	kPa	561.39	Calculated Property
Pvap	[1.03e-04; 1962.29]	kPa	[296.95; 718.70]	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			1.80082e+02
Coefficient B			-1.79270e+04
Coefficient C			-2.26400e+01
Coefficient D			9.84390e-18
Coefficient E			6.00000e+00
Temperature range, min.			296.95
Temperature range, max.			718.70
Pvap	1.03e-04	kPa	296.95	Calculated Property
Pvap	0.01	kPa	343.81	Calculated Property
Pvap	0.41	kPa	390.67	Calculated Property
Pvap	4.49	kPa	437.53	Calculated Property
Pvap	25.01	kPa	484.39	Calculated Property
Pvap	88.89	kPa	531.26	Calculated Property
Pvap	233.95	kPa	578.12	Calculated Property
Pvap	510.17	kPa	624.98	Calculated Property
Pvap	1009.46	kPa	671.84	Calculated Property
Pvap	1962.29	kPa	718.70	Calculated Property
Pvap	[9.08e-05; 1905.88]	kPa	[296.95; 721.00]	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			2.84704e+02
Coefficient B			-2.24029e+04
Coefficient C			-3.86309e+01
Coefficient D			1.56516e-05
Coefficient E			0.00000e+00
Temperature range, min.			296.95
Temperature range, max.			721.00
Pvap	9.08e-05	kPa	296.95	Calculated Property
Pvap	0.02	kPa	344.07	Calculated Property
Pvap	0.47	kPa	391.18	Calculated Property
Pvap	5.00	kPa	438.30	Calculated Property
Pvap	27.33	kPa	485.42	Calculated Property
Pvap	95.91	kPa	532.53	Calculated Property
Pvap	251.64	kPa	579.65	Calculated Property
Pvap	546.80	kPa	626.77	Calculated Property
Pvap	1056.06	kPa	673.88	Calculated Property
Pvap	1905.88	kPa	721.00	Calculated Property
Pvap	[0.18; 4.49]	kPa	[376.54; 437.61]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.57656e+01
Coefficient B			-4.73802e+03
Coefficient C			-1.05421e+02
Reference			Ambrose, Ellender, et al., 1974
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			376.54
Temperature range, max.			437.61
Pvap	0.18	kPa	376.54	Calculated Property
Pvap	0.28	kPa	383.33	Calculated Property
Pvap	0.42	kPa	390.11	Calculated Property
Pvap	0.61	kPa	396.90	Calculated Property
Pvap	0.89	kPa	403.68	Calculated Property
Pvap	1.26	kPa	410.47	Calculated Property
Pvap	1.77	kPa	417.25	Calculated Property
Pvap	2.45	kPa	424.04	Calculated Property
Pvap	3.34	kPa	430.82	Calculated Property
Pvap	4.49	kPa	437.61	Calculated Property
Pvap	[2.65; 132.46]	kPa	[425.72; 549.67]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.35507e+01
Coefficient B			-3.45333e+03
Coefficient C			-1.51106e+02
Reference			Ambrose and Sprake, 1970
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			425.72
Temperature range, max.			549.67
Pvap	2.65	kPa	425.72	Calculated Property
Pvap	4.84	kPa	439.49	Calculated Property
Pvap	8.35	kPa	453.26	Calculated Property
Pvap	13.74	kPa	467.04	Calculated Property
Pvap	21.68	kPa	480.81	Calculated Property
Pvap	33.00	kPa	494.58	Calculated Property
Pvap	48.63	kPa	508.35	Calculated Property
Pvap	69.62	kPa	522.13	Calculated Property
Pvap	97.14	kPa	535.90	Calculated Property
Pvap	132.46	kPa	549.67	Calculated Property
Pvap	[0.70; 102.42]	kPa	[399.70; 538.60]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.33815e+01
Coefficient B			-3.34942e+03
Coefficient C			-1.55915e+02
Reference			Kemme and Kreps, 1969
Temperature range, min.			399.70
Temperature range, max.			538.60
Pvap	0.70	kPa	399.70	Calculated Property
Pvap	1.58	kPa	415.13	Calculated Property
Pvap	3.28	kPa	430.57	Calculated Property
Pvap	6.27	kPa	446.00	Calculated Property
Pvap	11.23	kPa	461.43	Calculated Property
Pvap	19.02	kPa	476.87	Calculated Property
Pvap	30.70	kPa	492.30	Calculated Property
Pvap	47.52	kPa	507.73	Calculated Property
Pvap	70.90	kPa	523.17	Calculated Property
Pvap	102.42	kPa	538.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[824.28; 236.76]	kg/m3	[296.95; 718.70]	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			5.63232e+01
Coefficient B			2.37890e-01
Coefficient C			7.18700e+02
Coefficient D			2.64000e-01
Temperature range, min.			296.95
Temperature range, max.			718.70
ρl	824.28	kg/m3	296.95	Calculated Property
ρl	793.39	kg/m3	343.81	Calculated Property
ρl	760.84	kg/m3	390.67	Calculated Property
ρl	726.24	kg/m3	437.53	Calculated Property
ρl	688.97	kg/m3	484.39	Calculated Property
ρl	648.13	kg/m3	531.26	Calculated Property
ρl	602.11	kg/m3	578.12	Calculated Property
ρl	547.68	kg/m3	624.98	Calculated Property
ρl	476.02	kg/m3	671.84	Calculated Property
ρl	236.76	kg/m3	718.70	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.01]	N/m	[297.15; 532.15]	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			5.16816e-02
Coefficient B			-7.48000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			297.15
Temperature range, max.			532.15
γ	0.03	N/m	297.15	Calculated Property
γ	0.03	N/m	323.26	Calculated Property
γ	0.03	N/m	349.37	Calculated Property
γ	0.02	N/m	375.48	Calculated Property
γ	0.02	N/m	401.59	Calculated Property
γ	0.02	N/m	427.71	Calculated Property
γ	0.02	N/m	453.82	Calculated Property
γ	0.02	N/m	479.93	Calculated Property
γ	0.01	N/m	506.04	Calculated Property
γ	0.01	N/m	532.15	Calculated Property
γ	[0.03; 0.00]	N/m	[293.15; 718.70]	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			5.30340e-02
Coefficient B			1.10080e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			7.18700e+02
Temperature range, min.			293.15
Temperature range, max.			718.70
γ	0.03	N/m	293.15	Calculated Property
γ	0.03	N/m	340.43	Calculated Property
γ	0.02	N/m	387.72	Calculated Property
γ	0.02	N/m	435.00	Calculated Property
γ	0.02	N/m	482.28	Calculated Property
γ	0.01	N/m	529.57	Calculated Property
γ	0.01	N/m	576.85	Calculated Property
γ	0.01	N/m	624.13	Calculated Property
γ	0.00	N/m	671.42	Calculated Property
γ	0.00	N/m	718.70	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.03; 0.09]	W/m×K	[537.10; 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			-2.83000e-03
Coefficient B			9.12610e-01
Coefficient C			-1.91810e+04
Coefficient D			0.00000e+00
Temperature range, min.			537.10
Temperature range, max.			1000.00
λgas	0.03	W/m×K	537.10	Calculated Property
λgas	0.03	W/m×K	588.53	Calculated Property
λgas	0.04	W/m×K	639.97	Calculated Property
λgas	0.04	W/m×K	691.40	Calculated Property
λgas	0.05	W/m×K	742.83	Calculated Property
λgas	0.05	W/m×K	794.27	Calculated Property
λgas	0.06	W/m×K	845.70	Calculated Property
λgas	0.07	W/m×K	897.13	Calculated Property
λgas	0.08	W/m×K	948.57	Calculated Property
λgas	0.09	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.09]	W/m×K	[296.95; 537.10]	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			2.28040e-01
Coefficient B			-2.50000e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			296.95
Temperature range, max.			537.10
λliquid	0.15	W/m×K	296.95	Calculated Property
λliquid	0.15	W/m×K	323.63	Calculated Property
λliquid	0.14	W/m×K	350.32	Calculated Property
λliquid	0.13	W/m×K	377.00	Calculated Property
λliquid	0.13	W/m×K	403.68	Calculated Property
λliquid	0.12	W/m×K	430.37	Calculated Property
λliquid	0.11	W/m×K	457.05	Calculated Property
λliquid	0.11	W/m×K	483.73	Calculated Property
λliquid	0.10	W/m×K	510.42	Calculated Property
λliquid	0.09	W/m×K	537.10	Calculated Property

Similar Compounds

Find more compounds similar to 1-Dodecanol.

Mixtures

• 1-Dodecanol + Propanoic acid + Water
• n-Hexane + 1-Dodecanol
• 1-Dodecanol + Octane
• 1-Dodecanol + Decane
• 1-Dodecanol + Quinoline
• 1-Dodecanol + Butanoic acid + Water
• 1-Dodecanol + Ethanol
• 1-Dodecanol + Ethanol + Water
• 1-Dodecanol + Tri-n-butylphosphate
• 1-Dodecanol + 1-Octanamine, N,N-dioctyl-
• 1-Dodecanol + Carbon dioxide
• 1-Dodecanol + Tripalmitin
• Propane + 1-Dodecanol
• 1-Dodecanol + 1-Octanol
• 1-Dodecanol + 1-Octadecanol
• 1-Dodecanol + Water + Phosphoric Acid
• 1-Dodecanol + Water
• 1-Dodecanol + Phenol + Water
• 1-Dodecanol + 1,4-Butanediol
• 1-Propanol + 1-Dodecanol + Water

Find more mixtures with 1-Dodecanol.

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).
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 ChEDL chemicals 1.5.2, from Gude, M.; Teja, A. S. Vapor-Liquid Critical Properties of Elements and Compounds. 4. Aliphatic Alkanols. J. Chem. Eng. Data 1995, 40, 1025-1036.
• 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
• The influence of temperature on the liquid liquid solid equilibria of the ternary system water + ethanol + 1-dodecanol
• Phase equilibria of high molecular mass 1-alcohols in supercritical propane
• (Solid + liquid) and (liquid + liquid) phase equilibria measurements and correlation of the binary systems {tri-iso-butyl(methyl)phosphonium tosylate + alcohol, or +hydrocarbon}
• The solid-liquid phase diagrams of binary mixtures of even saturated fatty alcohols
• Liquid-liquid equilibria for aqueous sulfuric acid solutions with undecane, dodecane, or 1-dodecanol, trioctylamine or tributyl phosphate and excess and deviation properties for sub-binary systems at 298.15 K
• Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
• Measurement and correlation of vapor-liquid equilibria for alkane + alkanol andalkane + alkanediol systems with group contribution COSMOSPACE model
• Phase behavior of the carbon dioxide p 1-dodecanol system at high pressures
• Solid-liquid phase equilibrium diagrams of binary mixtures containing fatty acids, fatty alcohol compounds and tripalmitin using differential scanning calorimetry
• (Liquid + liquid) equilibria of the (water + butyric acid + dodecanol) ternary system
• (Liquid + liquid) equilibria of (water + propionic acid + alcohol) ternary systems
• Thermodynamics of organic mixtures containing amines. VIII. Systems with quinoline
• Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
• Thermophysical properties and thermodynamic phase behavior of ionic liquids
• Solubility and Tie Line Data of the Water - Phosphoric Acid Solvents at T = (303.2 and 313.2) K: An Experimental and Correlational Study
• 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
• Solvent Polarity Effect when Amberlite-LA2 Is Used in the Extraction of Picric Acid
• High Pressure Phase Behavior of the Homologous Series CO2 + 1-Alcohols
• Liquid-Liquid Equilibria of Lactic Acid/Water Solutions in Tri-iso-octylamine/Dodecane/1-Dodecanol at 306.1, 310.1, and 316.1 K. Experimental Data and Prediction
• Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
• Solid-Liquid Equilibrium of Binary Systems Containing Fatty Acids and Fatty Alcohols Using Differential Scanning Calorimetry
• Liquid Viscosity and Interfacial Tension of Binary and Ternary Mixtures Containing n-Octacosane by Surface Light Scattering
• Effect of Diluents on Extraction Equilibrium of trans-Aconitic Acid
• Experimental Measurement and Thermodynamic Model of Liquid-Liquid Equilibrium for the Ternary System of 1-Dodecanol-Phenol-Water
• Heat capacities and derived thermodynamic functions of 1-dodecanol and 1-tridecanol between 10 K and 370 K and heat capacities of 1-pentadecanol and 1-heptadecanol between 300 K and 380 K and correlationos for the heat capacity and the entropy of liquid n-alcohols
• Density-Pressure Relationship in Hydrogen-Bonded Mixtures: 1,4-Butanediol + 1-Dodecanol
• 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
• Distribution of Butyric Acid between Water and Several Solvents
• Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Vapor-Liquid Equilibria of Binary Systems of Ethene Oxide + Dodecane, Ethene Oxide + 1-Decanol, and Ethene Oxide + 1-Dodecanol and Prediction with the Predictive Soave-Redlich-Kwong (PSRK) Equation of State
• Liquid-Liquid Phase Behavior of Solutions of 1-Dodecyl-3-methylimidazolium Bis(trifluoromethylsulphonyl)imide (C12mimNTf2) in n- Alkyl Alcohols
• Measurements, Correlations, and Mod. UNIFAC (Do) Prediction of (Solid-Liquid) Phase Equilibria Diagrams in Binary Systems (Aliphatic Ketone + an Alcohol)
• Liquid-Liquid Phase Behavior of Solutions of 1-Hexyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C6mimNTf2) in n-Alkyl Alcohols
• Solid-Liquid Equilibria in Three Binary Mixtures Containing Diphenyl Carbonate
• Liquid Liquid Phase Equilibria of 1-Propanol + Water + n-Alcohol Ternary Systems at 298.15 K and Atmospheric Pressure
• Solid Liquid Equilibria, Excess Molar Volumes, and Deviations in the Molar Refractivity for the Binary Systems of Alamine 304-1 + Decane, Dodecane, or Dodecanol
• Solubility Determination and Correlation of (2R,3S,4S,5S)-6-(Hydroxymethyl)-tetrahydro-2H-pyran-2,3,4, 5-tetraol in Fatty Alcohol
• 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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