Chemical Properties of 2-Methyl-1-butanol (CAS 137-32-6)

InChI

InChI=1S/C5H12O/c1-3-5(2)4-6/h5-6H,3-4H2,1-2H3

InChI Key

QPRQEDXDYOZYLA-UHFFFAOYSA-N

Formula

C5H12O

SMILES

CCC(C)CO

Molecular Weight¹

88.15

CAS

137-32-6

Other Names

• 1-butanol, 2-methyl-

• ω : Acentric Factor.
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• IE : Ionization energy (eV).
• ν : Kinematic viscosity (m²/s).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• γ : Surface Tension (N/m).
• 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).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.5628		Relay (1.0) Calculated Property
Cp,liquid	215.00	J/mol×K	Partial Molar Heat Capacities and Partial Molar Volumes of All of the Isomeric (C3 to C5) Alkanols at Infinite Dilution in Water at 298.15 K
ΔfG°	-148.04	kJ/mol	Joback Calculated Property
ΔfH°gas	-305.56	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	9.27	kJ/mol	Joback Calculated Property
ΔvapH°	52.39	kJ/mol	Relay (1.0) Calculated Property
IE	9.91	eV	Relay (1.0) Calculated Property
log10WS	-0.47		Aq. Solubility Prediction
logPoct/wat	1.025		Crippen Calculated Property
McVol	87.180	ml/mol	McGowan Calculated Property
Pc	3916.03	kPa	Joback Calculated Property
Tboil	[401.27; 402.45]	K
Tboil	402.45	K	Vapor-Liquid Equilibrium of the Ethanol + 2-Methyl-1-butanol System
Tboil	401.93	K	Vapor-Liquid Equilibrium of Binary Mixtures Containing Ethyl Acetate + 2-Methyl-1-propanol and Ethyl Acetate + 2-Methyl-1-butanol at 101.3 kPa
Tboil	401.93	K	Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures Containing 2-Methyl-1-propanol + 2-Methyl-1-butanol, 2-Methyl-1-propanol + 3-Methyl-1-butanol, and 2-Methyl-1-propanol + 1-Pentanol
Tboil	401.27	K	Isobaric Vapor Liquid Equilibria for the Binary and Ternary Systems of 2-Methyl-1-butanol, 2-Methyl-butanol Acetate, and Dimethylformamide (DMF) at 101.3 kPa
Tc	571.66	K	Relay (1.0) Calculated Property
Tfus	157.75	K	Relay (1.0) Calculated Property
Ttriple	118.00	K	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Vc	0.300	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[169.82; 216.94]	J/mol×K	[405.54; 570.76]
Cp,gas	169.82	J/mol×K	405.54	Joback Calculated Property
Cp,gas	178.43	J/mol×K	433.08	Joback Calculated Property
Cp,gas	186.73	J/mol×K	460.61	Joback Calculated Property
Cp,gas	194.72	J/mol×K	488.15	Joback Calculated Property
Cp,gas	202.42	J/mol×K	515.68	Joback Calculated Property
Cp,gas	209.82	J/mol×K	543.22	Joback Calculated Property
Cp,gas	216.94	J/mol×K	570.76	Joback Calculated Property
η	[0.0002833; 0.3005917]	Pa×s	[191.93; 405.54]
η	0.3005917	Pa×s	191.93	Joback Calculated Property
η	0.0379452	Pa×s	227.53	Joback Calculated Property
η	0.0083860	Pa×s	263.13	Joback Calculated Property
η	0.0026559	Pa×s	298.74	Joback Calculated Property
η	0.0010745	Pa×s	334.34	Joback Calculated Property
η	0.0005174	Pa×s	369.94	Joback Calculated Property
η	0.0002833	Pa×s	405.54	Joback Calculated Property
ν	[0.0000027; 0.0000061]	m2/s	[293.15; 323.15]
ν	0.0000061	m2/s	293.15	Density, Viscosity, Excess Molar Volume, and Viscosity Deviation of Three Amyl Alcohols + Ethanol Binary Mixtures from 293.15 to 323.15 K
ν	0.0000053	m2/s	298.15	Density, Viscosity, Excess Molar Volume, and Viscosity Deviation of Three Amyl Alcohols + Ethanol Binary Mixtures from 293.15 to 323.15 K
ν	0.0000047	m2/s	303.15	Density, Viscosity, Excess Molar Volume, and Viscosity Deviation of Three Amyl Alcohols + Ethanol Binary Mixtures from 293.15 to 323.15 K
ν	0.0000041	m2/s	308.15	Density, Viscosity, Excess Molar Volume, and Viscosity Deviation of Three Amyl Alcohols + Ethanol Binary Mixtures from 293.15 to 323.15 K
ν	0.0000035	m2/s	313.15	Density, Viscosity, Excess Molar Volume, and Viscosity Deviation of Three Amyl Alcohols + Ethanol Binary Mixtures from 293.15 to 323.15 K
ν	0.0000031	m2/s	318.15	Density, Viscosity, Excess Molar Volume, and Viscosity Deviation of Three Amyl Alcohols + Ethanol Binary Mixtures from 293.15 to 323.15 K
ν	0.0000027	m2/s	323.15	Density, Viscosity, Excess Molar Volume, and Viscosity Deviation of Three Amyl Alcohols + Ethanol Binary Mixtures from 293.15 to 323.15 K
Pvap	[9.33; 101.30]	kPa	[345.51; 402.45]
Pvap	9.33	kPa	345.51	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	12.00	kPa	350.44	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	14.66	kPa	354.51	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	16.70	kPa	357.85	Vapor-Liquid Equilibrium of the Ethanol + 2-Methyl-1-butanol System
Pvap	17.33	kPa	358.02	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	20.66	kPa	361.80	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	23.30	kPa	364.85	Effect of addition of calcium chloride on vapor pressure of 2-methyl-1-butanol
Pvap	23.30	kPa	364.85	Vapor-Liquid Equilibrium of the Ethanol + 2-Methyl-1-butanol System
Pvap	24.00	kPa	365.12	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	28.00	kPa	368.62	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	30.00	kPa	370.45	Vapor-Liquid Equilibrium of the Ethanol + 2-Methyl-1-butanol System
Pvap	30.00	kPa	370.45	Effect of addition of calcium chloride on vapor pressure of 2-methyl-1-butanol
Pvap	32.00	kPa	371.74	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	33.30	kPa	372.95	Vapor-Liquid Equilibrium of the Ethanol + 2-Methyl-1-butanol System
Pvap	33.30	kPa	373.05	Effect of addition of calcium chloride on vapor pressure of 2-methyl-1-butanol
Pvap	36.00	kPa	374.56	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	36.70	kPa	375.15	Effect of addition of calcium chloride on vapor pressure of 2-methyl-1-butanol
Pvap	36.70	kPa	375.15	Vapor-Liquid Equilibrium of the Ethanol + 2-Methyl-1-butanol System
Pvap	40.00	kPa	377.13	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	43.30	kPa	379.05	Effect of addition of calcium chloride on vapor pressure of 2-methyl-1-butanol
Pvap	43.30	kPa	379.05	Vapor-Liquid Equilibrium of the Ethanol + 2-Methyl-1-butanol System
Pvap	44.00	kPa	379.50	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	48.66	kPa	382.05	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	50.00	kPa	382.75	Vapor-Liquid Equilibrium of the Ethanol + 2-Methyl-1-butanol System
Pvap	50.00	kPa	382.75	Effect of addition of calcium chloride on vapor pressure of 2-methyl-1-butanol
Pvap	53.33	kPa	384.41	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	56.60	kPa	385.65	Vapor-Liquid Equilibrium of the Ethanol + 2-Methyl-1-butanol System
Pvap	56.60	kPa	385.65	Effect of addition of calcium chloride on vapor pressure of 2-methyl-1-butanol
Pvap	58.66	kPa	386.92	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	63.30	kPa	388.95	Vapor-Liquid Equilibrium of the Ethanol + 2-Methyl-1-butanol System
Pvap	63.30	kPa	388.95	Effect of addition of calcium chloride on vapor pressure of 2-methyl-1-butanol
Pvap	63.99	kPa	389.23	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	66.60	kPa	390.35	Vapor-Liquid Equilibrium of the Ethanol + 2-Methyl-1-butanol System
Pvap	69.33	kPa	391.40	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	70.00	kPa	391.65	Effect of addition of calcium chloride on vapor pressure of 2-methyl-1-butanol
Pvap	70.00	kPa	391.65	Vapor-Liquid Equilibrium of the Ethanol + 2-Methyl-1-butanol System
Pvap	74.66	kPa	393.43	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	76.60	kPa	394.15	Vapor-Liquid Equilibrium of the Ethanol + 2-Methyl-1-butanol System
Pvap	76.60	kPa	394.15	Effect of addition of calcium chloride on vapor pressure of 2-methyl-1-butanol
Pvap	79.99	kPa	395.35	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	83.30	kPa	396.65	Vapor-Liquid Equilibrium of the Ethanol + 2-Methyl-1-butanol System
Pvap	83.30	kPa	396.65	Effect of addition of calcium chloride on vapor pressure of 2-methyl-1-butanol
Pvap	85.33	kPa	397.17	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	90.00	kPa	398.85	Vapor-Liquid Equilibrium of the Ethanol + 2-Methyl-1-butanol System
Pvap	90.00	kPa	398.85	Effect of addition of calcium chloride on vapor pressure of 2-methyl-1-butanol
Pvap	90.66	kPa	398.90	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	97.33	kPa	400.96	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	96.60	kPa	401.05	Vapor-Liquid Equilibrium of the Ethanol + 2-Methyl-1-butanol System
Pvap	96.60	kPa	401.05	Effect of addition of calcium chloride on vapor pressure of 2-methyl-1-butanol
Pvap	101.30	kPa	402.45	Vapor-Liquid Equilibrium of the Ethanol + 2-Methyl-1-butanol System
n0	[1.40840; 1.40950]		[293.15; 298.15]
n0	1.40950		293.15	Isobaric Vapor - Liquid Equilibria for the Ternary System of 2-Methyl-1-butanol, 3-Methyl-1-butanol, and Ethylene Glycol at 101.3 kPa
n0	1.40860		298.15	Study of the Effects of Temperature and Pressure on the Thermodynamic and Acoustic Properties of 2-Methyl-1-butanol at Temperatures from 293K to 318K and Pressures up to 100MPa
n0	1.40840		298.15	Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
n0	1.40872		298.15	Density, Refractive Index, Speed of Sound at 298.15 K, and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Methanol + 2-Methyl-1-butanol and Ethanol + 2-Methyl-1-butanol
n0	1.40872		298.15	Density, Refractive Index, Speed of Sound at 298.15 K, and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Propanol + 2-Methyl-1-butanol and Propanol + 3-Methyl-1-butanol
ρl	[783.84; 823.35]	kg/m3	[288.15; 338.15]
ρl	823.35	kg/m3	288.15	Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl	823.02	kg/m3	288.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl	819.56	kg/m3	293.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl	819.64	kg/m3	293.15	Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl	814.83	kg/m3	298.15	Vapor Liquid Equilibrium for 2-Methyl-1-butanol + Ethylbenzene + Xylene Isomers at 101.33 kPa
ρl	815.82	kg/m3	298.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl	814.98	kg/m3	298.15	Excess molar enthalpies of the binary systems: (Dibutyl ether + isomers of pentanol) at T = (298.15 and 308.15) K
ρl	815.85	kg/m3	298.15	Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl	812.03	kg/m3	303.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl	812.12	kg/m3	303.15	Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl	808.20	kg/m3	308.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl	807.63	kg/m3	308.15	Excess molar enthalpies of the binary systems: (Dibutyl ether + isomers of pentanol) at T = (298.15 and 308.15) K
ρl	808.29	kg/m3	308.15	Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl	804.41	kg/m3	313.15	Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl	804.33	kg/m3	313.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl	800.39	kg/m3	318.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl	800.47	kg/m3	318.15	Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl	796.39	kg/m3	323.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl	796.47	kg/m3	323.15	Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl	792.41	kg/m3	328.15	Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl	792.34	kg/m3	328.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl	788.20	kg/m3	333.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl	783.84	kg/m3	338.15	Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
γ	[0.02; 0.02]	N/m	[293.15; 323.15]
γ	0.02	N/m	293.15	Surface Tensions of Three Amyl Alcohol + Ethanol Binary Mixtures from (293.15 to 323.15) K
γ	0.02	N/m	298.15	Surface Tensions of Three Amyl Alcohol + Ethanol Binary Mixtures from (293.15 to 323.15) K
γ	0.02	N/m	303.15	Surface Tensions of Three Amyl Alcohol + Ethanol Binary Mixtures from (293.15 to 323.15) K
γ	0.02	N/m	308.15	Surface Tensions of Three Amyl Alcohol + Ethanol Binary Mixtures from (293.15 to 323.15) K
γ	0.02	N/m	313.15	Surface Tensions of Three Amyl Alcohol + Ethanol Binary Mixtures from (293.15 to 323.15) K
γ	0.02	N/m	318.15	Surface Tensions of Three Amyl Alcohol + Ethanol Binary Mixtures from (293.15 to 323.15) K
γ	0.02	N/m	323.15	Surface Tensions of Three Amyl Alcohol + Ethanol Binary Mixtures from (293.15 to 323.15) K

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[313.37; 424.10]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.43135e+01
Coefficient B			-2.78286e+03
Coefficient C			-1.14962e+02
Temperature range, min.			313.37
Temperature range, max.			424.10
Pvap	1.33	kPa	313.37	Calculated Property
Pvap	3.02	kPa	325.67	Calculated Property
Pvap	6.27	kPa	337.98	Calculated Property
Pvap	12.03	kPa	350.28	Calculated Property
Pvap	21.65	kPa	362.58	Calculated Property
Pvap	36.86	kPa	374.89	Calculated Property
Pvap	59.79	kPa	387.19	Calculated Property
Pvap	93.03	kPa	399.49	Calculated Property
Pvap	139.54	kPa	411.80	Calculated Property
Pvap	202.64	kPa	424.10	Calculated Property
Pvap	[3.89e-07; 3977.66]	kPa	[203.00; 565.00]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			2.88019e+02
Coefficient B			-1.78736e+04
Coefficient C			-4.06446e+01
Coefficient D			2.96397e-05
Temperature range, min.			203.00
Temperature range, max.			565.00
Pvap	3.89e-07	kPa	203.00	Calculated Property
Pvap	8.99e-04	kPa	243.22	Calculated Property
Pvap	0.11	kPa	283.44	Calculated Property
Pvap	2.69	kPa	323.67	Calculated Property
Pvap	23.35	kPa	363.89	Calculated Property
Pvap	109.26	kPa	404.11	Calculated Property
Pvap	348.09	kPa	444.33	Calculated Property
Pvap	877.25	kPa	484.56	Calculated Property
Pvap	1931.78	kPa	524.78	Calculated Property
Pvap	3977.66	kPa	565.00	Calculated Property

Similar Compounds

Find more compounds similar to 2-Methyl-1-butanol.

Mixtures

• 2-Methyl-1-butanol + Water
• Sodium nitrate + 2-Methyl-1-butanol + Water
• Potassium nitrate + 2-Methyl-1-butanol + Water
• 2-Methyl-1-butanol + Heptane
• 2-Methyl-1-butanol + Ethyl Acetate
• Ethanol + 2-Methyl-1-butanol
• 2-Butene, (Z)- + 2-Methyl-1-butanol
• 2-Methyl-1-butanol + Dimethyl ether
• Ethyl Chloride + 2-Methyl-1-butanol
• 2-Methyl-1-butanol + Ethane, 1,1-difluoro-
• n-Butyl ether + 2-Methyl-1-butanol
• 1,2-Ethanediol + 1-Butanol, 3-methyl- + 2-Methyl-1-butanol
• Propane + 2-Methyl-1-butanol
• Propene + 2-Methyl-1-butanol
• Butane + 2-Methyl-1-butanol
• 2-Methyl-1-butanol + Isobutane
• 1-Butene + 2-Methyl-1-butanol
• 1-Propene, 2-methyl- + 2-Methyl-1-butanol
• 2-Methyl-1-butanol + 2-Butene, (E)-
• 1,3-Butadiene + 2-Methyl-1-butanol

Find more mixtures with 2-Methyl-1-butanol.

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Study of the Effects of Temperature and Pressure on the Thermodynamic and Acoustic Properties of 2-Methyl-1-butanol at Temperatures from 293K to 318K and Pressures up to 100MPa
• Isothermal vapor liquid equilibria for different binary mixtures involved in the alcoholic distillation
• Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
• The influence of cation, anion and temperature on the liquid-liquid equilibrium of some pentanols-water system
• Henry's law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-pentanol, 3-pentanol, 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
• Excess molar enthalpies of the binary systems: (Dibutyl ether + isomers of pentanol) at T = (298.15 and 308.15) K
• Mutual diffusion coefficients of 3-methyl-1-butanol + n-heptane and 2-methyl-1-butanol + n-heptane from 288.15 K to 318.15 K
• Solution enthalpies of 1-bromoadamantane in monoalcohols at 298.15K
• Liquid Liquid Equilibria for the Ternary Systems of Water + Butane-2,3-diol + 2-Methylbutan-1-ol, 2-Ethylbutan-1-ol, and 4-Methylpentan-2-ol at 298.15 and 308.15 K
• Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
• Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
• Vapor-Liquid Equilibrium of the Ethanol + 2-Methyl-1-butanol System
• Solubility of Anthracene in Binary Alcohol + Acetonitrile Solvent Mixtures at 298.2 K
• Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
• Solubility in Binary Solvent Mixtures: Anthracene Dissolved in Alcohol + 2-Methyl-1-butanol Mixtures at 298.2 K
• Isobaric Vapor - Liquid Equilibria for the Ternary System of 2-Methyl-1-butanol, 3-Methyl-1-butanol, and Ethylene Glycol at 101.3 kPa
• Effect of addition of calcium chloride on vapor pressure of 2-methyl-1-butanol
• Henry's law constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
• Partial Molar Heat Capacities and Partial Molar Volumes of All of the Isomeric (C3 to C5) Alkanols at Infinite Dilution in Water at 298.15 K
• Density, Refractive Index, Speed of Sound at 298.15 K, and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Methanol + 2-Methyl-1-butanol and Ethanol + 2-Methyl-1-butanol
• Density, Refractive Index, Speed of Sound at 298.15 K, and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Propanol + 2-Methyl-1-butanol and Propanol + 3-Methyl-1-butanol
• Density, Viscosity, Excess Molar Volume, and Viscosity Deviation of Three Amyl Alcohols + Ethanol Binary Mixtures from 293.15 to 323.15 K
• Vapor-Liquid Equilibrium of Binary Mixtures Containing Ethyl Acetate + 2-Methyl-1-propanol and Ethyl Acetate + 2-Methyl-1-butanol at 101.3 kPa
• Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures Containing 2-Methyl-1-propanol + 2-Methyl-1-butanol, 2-Methyl-1-propanol + 3-Methyl-1-butanol, and 2-Methyl-1-propanol + 1-Pentanol
• Ethanol + 2-Methyl-1-butanol + Calcium Chloride System: Vapor-Liquid Equilibrium Data and Correlation Using the NRTL Electrolyte Model
• Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
• Surface Tensions of Three Amyl Alcohol + Ethanol Binary Mixtures from (293.15 to 323.15) K
• Vapor Liquid Equilibrium for 2-Methyl-1-butanol + Ethylbenzene + Xylene Isomers at 101.33 kPa
• Isobaric Vapor Liquid Equilibria for the Binary and Ternary Systems of 2-Methyl-1-butanol, 2-Methyl-butanol Acetate, and Dimethylformamide (DMF) at 101.3 kPa
• Isobaric Vapor Liquid Equilibria of Binary Systems (Propyl Acetate + 2-Methylbutan-1-ol), (Propyl Acetate + Hexan-1-ol), and (Propyl Acetate + Heptan-1-ol) at 101.3 kPa
• Isobaric Vapor-Liquid Equilibria for 2-Methyl-butan-1-ol + 3-Methyl-butan-1-ol + CuCl2, ZnCl2, and FeCl3 Systems at 101.3 kPa
• Temperature Dependence of Limiting Activity Coefficients, Henry s Law Constants, and Related Infinite Dilution Properties of Branched Pentanols in Water. Measurement, Critical Compilation, Correlation, and Recommended Data
• Joback Method
• Aqueous Solubility Prediction Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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