Chemical Properties of 2-Propanol, 2-methyl- (CAS 75-65-0)

InChI

InChI=1S/C4H10O/c1-4(2,3)5/h5H,1-3H3

InChI Key

DKGAVHZHDRPRBM-UHFFFAOYSA-N

Formula

C4H10O

SMILES

CC(C)(C)O

Molecular Weight¹

74.12

CAS

75-65-0

Other Names

• 1,1-Dimethylethanol
• 2-Methyl n-propan-2-ol
• 2-Methylpropanol-2
• 2-methyl-2-propanol
• 2-methylpropan-2-ol
• Alcool butylique tertiaire
• Butanol tertiaire
• Ethanol, 1,1-Dimethyl-
• Methanol, trimethyl-
• Methyl-2 propanol-2
• NCI-C55367
• Tert.-butyl alcohol
• Trimethylcarbinol
• Trimethylmethanol
• t-Butanol
• t-Butyl hydroxide
• tert-Butyl hydroxide
• tert-C4H9OH
• tert-butanol
• tert-butyl alcohol

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• Δ_cH°_solid : Standard solid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• C_p,solid : Solid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• ε_r : Dielectric Constant (Relative permittivity).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• 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).
• 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).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• 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).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• S°_{solid,1 bar} : Solid phase molar entropy at standard conditions (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.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Datasets
4. Correlations
5. Similar Compounds
6. Mixtures
7. Sources

Physical Properties

Property	Value	Unit	Source
ω	[0.6120; 0.6180]
ω	0.6180		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.6130		ChemSep v8.3 pure component data Compiled value
ω	0.6120		KDB
PAff	802.60	kJ/mol	NIST
Tig	753.15	K	KDB
BasG	772.20	kJ/mol	NIST
ΔcH°liquid	-2644.00 ± 0.79	kJ/mol	NIST
ΔcH°solid	-2633.00	kJ/mol	NIST
μ	[1.67; 1.70]	debye
μ	1.67	debye	ChemSep v8.3 pure component data Compiled value
μ	1.70	debye	KDB
LFL	2.35	% in Air	KDB
UFL	8.00	% in Air	KDB
Tflash,cc	289.26	K	KDB
Tflash,oc	284.26	K	KDB
ΔfG°	[-178.80; -177.60]	kJ/mol
ΔfG°	-177.60	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	-178.80	kJ/mol	KDB
Rg	3.0190		KDB
ΔfH°gas	[-313.00; -309.70]	kJ/mol
ΔfH°gas	-312.40	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-312.80	kJ/mol	KDB
ΔfH°gas	-312.60 ± 0.88	kJ/mol	NIST
ΔfH°gas	-313.00 ± 1.50	kJ/mol	NIST
ΔfH°gas	-309.70	kJ/mol	NIST
ΔfH°liquid	[-359.30; -356.00]	kJ/mol
ΔfH°liquid	-359.20 ± 0.84	kJ/mol	NIST
ΔfH°liquid	-359.30 ± 0.79	kJ/mol	NIST
ΔfH°liquid	-356.00	kJ/mol	NIST
ΔfusH°	2.79	kJ/mol	Joback Calculated Property
ΔsubH°	41.00	kJ/mol	NIST
ΔvapH°	[44.90; 47.40]	kJ/mol
ΔvapH°	46.74	kJ/mol	NIST
ΔvapH°	47.40	kJ/mol	NIST
ΔvapH°	45.40	kJ/mol	NIST
ΔvapH°	46.60	kJ/mol	NIST
ΔvapH°	46.94 ± 0.02	kJ/mol	NIST
ΔvapH°	46.94 ± 0.02	kJ/mol	NIST
ΔvapH°	46.60 ± 0.10	kJ/mol	NIST
ΔvapH°	46.61 ± 0.08	kJ/mol	NIST
ΔvapH°	Outlier 44.90	kJ/mol	NIST
ΔvapH°	46.02	kJ/mol	NIST
ΔvapH°	46.30	kJ/mol	NIST
IE	[9.90; 10.26]	eV
IE	9.90 ± 0.03	eV	NIST
IE	9.90 ± 0.03	eV	NIST
IE	9.97 ± 0.02	eV	NIST
IE	10.23	eV	NIST
IE	10.23	eV	NIST
IE	10.26	eV	NIST
IE	10.25 ± 0.03	eV	NIST
IE	10.25	eV	NIST
log10WS	0.34		Relay (1.0) Calculated Property
logPoct/wat	0.777		Crippen Calculated Property
McVol	73.090	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	[3970.00; 4232.00]	kPa
Pc	3972.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Pc	3971.94	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3973.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3972.00	kPa	KDB
Pc	3970.00 ± 20.00	kPa	NIST
Pc	3972.00	kPa	NIST
Pc	Outlier 4232.00	kPa	NIST
Ptriple	5.88	kPa	ChemSep v8.3 pure component data Compiled value
ρc	[257.94; 270.02]	kg/m3
ρc	269.80 ± 1.48	kg/m3	NIST
ρc	270.02	kg/m3	NIST
ρc	257.94	kg/m3	NIST
Inp	[471.00; 543.00]
Inp	472.10		NIST
Inp	471.00		NIST
Inp	500.00		NIST
Inp	500.00		NIST
Inp	500.00		NIST
Inp	515.00		NIST
Inp	493.00		NIST
Inp	521.00		NIST
Inp	491.00		NIST
Inp	487.00		NIST
Inp	488.00		NIST
Inp	472.00		NIST
Inp	488.00		NIST
Inp	478.10		NIST
Inp	493.00		NIST
Inp	524.00		NIST
Inp	527.00		NIST
Inp	514.00		NIST
Inp	471.00		NIST
Inp	493.00		NIST
Inp	472.00		NIST
Inp	488.00		NIST
Inp	523.50		NIST
Inp	526.30		NIST
Inp	518.00		NIST
Inp	531.00		NIST
Inp	534.00		NIST
Inp	519.00		NIST
Inp	507.30		NIST
Inp	500.00		NIST
Inp	530.00		NIST
Inp	500.00		NIST
Inp	512.00		NIST
Inp	514.00		NIST
Inp	509.00		NIST
Inp	512.00		NIST
Inp	512.00		NIST
Inp	509.00		NIST
Inp	512.00		NIST
Inp	518.00		NIST
Inp	543.00		NIST
Inp	512.00		NIST
Inp	472.10		NIST
Inp	515.00		NIST
Inp	488.00		NIST
Inp	524.00		NIST
Inp	472.00		NIST
Inp	530.00		NIST
Inp	512.00		NIST
Inp	543.00		NIST
Inp	526.30		NIST
Inp	519.00		NIST
Ip	[863.00; 942.00]
Ip	930.00		NIST
Ip	942.00		NIST
Ip	930.00		NIST
Ip	942.00		NIST
Ip	934.00		NIST
Ip	897.00		NIST
Ip	867.00		NIST
Ip	906.00		NIST
Ip	881.00		NIST
Ip	863.00		NIST
Ip	882.00		NIST
Ip	902.00		NIST
Ip	891.00		NIST
Ip	879.00		NIST
Ip	914.00		NIST
Ip	875.00		NIST
Ip	900.00		NIST
Ip	880.00		NIST
Ip	871.00		NIST
Ip	897.00		NIST
Ip	920.00		NIST
Ip	871.00		NIST
Ip	916.00		NIST
Ip	934.00		NIST
Ip	875.00		NIST
Ip	897.00		NIST
Ip	875.00		NIST
Ip	900.00		NIST
S°liquid	[189.50; 197.50]	J/mol×K
S°liquid	189.50	J/mol×K	NIST
S°liquid	197.50	J/mol×K	NIST
S°solid,1 bar	170.87	J/mol×K	NIST
Tboil	[325.70; 375.50]	K
Tboil	355.33	K	Isobaric vapor liquid equilibrium for ternary mixtures of ethanol and methylcyclohexane with 3-methylpentane and tert-butyl alcohol at 101.3 kPa
Tboil	355.55	K	Measurement and correlation of binary vapor liquid equilibria of isomeric butanols with 1,4-dioxane
Tboil	355.80	K	Isobaric vapour-liquid equilibrium of (tert-butanol + water) system with biological buffer TRIS at 101.3 kPa
Tboil	355.51	K	Isobaric Vapor Liquid Equilibrium for the Binary Systems of sec-Butyl Acetate + n-Butyl Alcohol, Isobutyl Alcohol, or tert-Butyl Alcohol at 101.3 kPa
Tboil	355.59	K	Isobaric Vapor-Liquid Equilibrium for Binary and Ternary Systems of tert-Butanol + tert-Butyl Acetate + Chlorobenzene at 101.33 kPa
Tboil	355.58	K	Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
Tboil	355.56	K	Isobaric Vapor Liquid Equilibrium of tert-Butyl Alcohol + Water + Triethanolamine-Based Ionic Liquid Ternary Systems at 101.3 kPa
Tboil	355.49	K	ChemSep v8.3 pure component data Compiled value
Tboil	355.50	K	KDB
Tboil	355.60 ± 0.30	K	NIST
Tboil	355.60 ± 0.30	K	NIST
Tboil	355.30 ± 0.40	K	NIST
Tboil	355.60 ± 0.30	K	NIST
Tboil	355.55 ± 0.30	K	NIST
Tboil	355.50	K	NIST
Tboil	355.00	K	NIST
Tboil	355.55 ± 0.25	K	NIST
Tboil	355.65 ± 0.25	K	NIST
Tboil	355.55 ± 0.30	K	NIST
Tboil	355.50	K	NIST
Tboil	355.35 ± 0.30	K	NIST
Tboil	355.70 ± 0.40	K	NIST
Tboil	355.45 ± 0.40	K	NIST
Tboil	355.40 ± 0.50	K	NIST
Tboil	355.70 ± 0.30	K	NIST
Tboil	355.70 ± 0.30	K	NIST
Tboil	355.60 ± 0.50	K	NIST
Tboil	355.65 ± 0.20	K	NIST
Tboil	355.47 ± 0.12	K	NIST
Tboil	355.47 ± 0.10	K	NIST
Tboil	354.61 ± 0.10	K	NIST
Tboil	355.95 ± 0.50	K	NIST
Tboil	355.70 ± 1.00	K	NIST
Tboil	355.55 ± 0.50	K	NIST
Tboil	355.50 ± 0.50	K	NIST
Tboil	355.40 ± 0.25	K	NIST
Tboil	353.65 ± 2.00	K	NIST
Tboil	355.65 ± 1.00	K	NIST
Tboil	355.65 ± 2.00	K	NIST
Tboil	354.65 ± 2.00	K	NIST
Tboil	355.95 ± 0.50	K	NIST
Tboil	355.15 ± 1.00	K	NIST
Tboil	355.95 ± 0.30	K	NIST
Tboil	355.75 ± 0.30	K	NIST
Tboil	354.65 ± 1.00	K	NIST
Tboil	355.15 ± 1.00	K	NIST
Tboil	355.25 ± 1.00	K	NIST
Tboil	355.15 ± 1.00	K	NIST
Tboil	355.75 ± 0.50	K	NIST
Tboil	355.56 ± 0.10	K	NIST
Tboil	355.60 ± 0.10	K	NIST
Tboil	355.60 ± 0.40	K	NIST
Tboil	Outlier 375.50 ± 0.30	K	NIST
Tboil	355.60 ± 0.10	K	NIST
Tboil	355.85 ± 0.50	K	NIST
Tboil	355.65 ± 1.00	K	NIST
Tboil	357.65 ± 2.00	K	NIST
Tboil	356.00 ± 1.00	K	NIST
Tboil	354.15 ± 3.00	K	NIST
Tboil	354.65 ± 1.00	K	NIST
Tboil	355.65 ± 2.00	K	NIST
Tboil	356.15 ± 1.00	K	NIST
Tboil	355.65 ± 0.10	K	NIST
Tboil	355.75 ± 0.50	K	NIST
Tboil	355.85 ± 0.50	K	NIST
Tboil	355.37 ± 0.20	K	NIST
Tboil	355.75 ± 0.30	K	NIST
Tboil	Outlier 325.70 ± 0.25	K	NIST
Tboil	355.70 ± 0.20	K	NIST
Tboil	355.75 ± 0.50	K	NIST
Tboil	356.01 ± 0.20	K	NIST
Tboil	355.15 ± 0.50	K	NIST
Tboil	355.40 ± 0.30	K	NIST
Tboil	355.10 ± 0.50	K	NIST
Tboil	355.72 ± 0.30	K	NIST
Tboil	356.20 ± 1.00	K	NIST
Tboil	356.09 ± 0.50	K	NIST
Tboil	354.90 ± 1.00	K	NIST
Tboil	355.55 ± 0.50	K	NIST
Tc	[506.20; 508.90]	K
Tc	506.35	K	Experimental study of the isochoric heat capacity of tert-butanol in the critical and supercritical regions
Tc	506.20	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Tc	506.20	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	506.21	K	ChemSep v8.3 pure component data Compiled value
Tc	506.20	K	KDB
Tc	506.20 ± 0.30	K	NIST
Tc	506.20	K	NIST
Tc	506.20	K	NIST
Tc	Outlier 508.90	K	NIST
Tc	508.10	K	NIST
Tfus	[296.15; 302.15]	K
Tfus	298.70	K	Solid liquid equilibria of mixtures containing tert-butanol, m-chlorophenol, and p-chlorophenol and development of adductive crystallization processes
Tfus	297.99	K	Solubility of Benzimidazoles in Alcohols
Tfus	298.35	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	298.97	K	ChemSep v8.3 pure component data Compiled value
Tfus	298.50	K	KDB
Tfus	298.87 ± 0.05	K	NIST
Tfus	298.55 ± 0.20	K	NIST
Tfus	298.75 ± 0.20	K	NIST
Tfus	298.65 ± 0.30	K	NIST
Tfus	298.20 ± 0.60	K	NIST
Tfus	298.55 ± 0.30	K	NIST
Tfus	298.15 ± 0.50	K	NIST
Tfus	298.55 ± 0.40	K	NIST
Tfus	298.07 ± 0.20	K	NIST
Tfus	298.30 ± 0.30	K	NIST
Tfus	Outlier 296.15 ± 2.00	K	NIST
Tfus	298.00 ± 1.50	K	NIST
Tfus	298.25 ± 0.50	K	NIST
Tfus	297.70 ± 0.30	K	NIST
Tfus	298.15 ± 1.50	K	NIST
Tfus	297.45 ± 0.50	K	NIST
Tfus	Outlier 302.15 ± 2.00	K	NIST
Ttriple	[298.50; 298.97]	K
Ttriple	298.97	K	ChemSep v8.3 pure component data Compiled value
Ttriple	298.96 ± 0.06	K	NIST
Ttriple	298.97 ± 0.06	K	NIST
Ttriple	298.50 ± 0.20	K	NIST
Ttriple	298.50 ± 0.20	K	NIST
UQi	3.13		ChemSep v8.3 pure component data Compiled value
URi	3.45		ChemSep v8.3 pure component data Compiled value
Vc	[0.275; 0.275]	m3/kmol
Vc	0.275	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Vc	0.275	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.275	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.275	m3/kmol	KDB
Vc	0.275	m3/kmol	NIST
Zc	[0.2590000; 0.2600000]
Zc	0.2590000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Zc	0.2600000		ChemSep v8.3 pure component data Compiled value
Zc	0.2595270		KDB
Zra	0.26		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[132.63; 187.30]	J/mol×K	[360.55; 591.55]
Cp,gas	133.40 ± 1.10	J/mol×K	360.55	NIST
Cp,gas	132.63	J/mol×K	365.15	NIST
Cp,gas	136.20 ± 1.10	J/mol×K	372.85	NIST
Cp,gas	137.95	J/mol×K	383.15	NIST
Cp,gas	139.20 ± 1.10	J/mol×K	385.65	NIST
Cp,gas	142.88	J/mol×K	401.15	NIST
Cp,gas	145.10 ± 1.10	J/mol×K	410.85	NIST
Cp,gas	148.07	J/mol×K	419.15	NIST
Cp,gas	153.55	J/mol×K	437.15	NIST
Cp,gas	151.90 ± 1.10	J/mol×K	439.85	NIST
Cp,gas	152.20 ± 1.10	J/mol×K	441.45	NIST
Cp,gas	159.10 ± 1.10	J/mol×K	470.75	NIST
Cp,gas	165.70 ± 1.10	J/mol×K	499.25	NIST
Cp,gas	172.60 ± 1.10	J/mol×K	528.75	NIST
Cp,gas	183.40 ± 1.10	J/mol×K	575.05	NIST
Cp,gas	187.30 ± 1.10	J/mol×K	591.55	NIST
Cp,liquid	[210.00; 224.90]	J/mol×K	[298.00; 300.00]
Cp,liquid	210.00	J/mol×K	298.00	NIST
Cp,liquid	215.37	J/mol×K	298.15	NIST
Cp,liquid	210.00	J/mol×K	298.15	NIST
Cp,liquid	224.90	J/mol×K	298.15	NIST
Cp,liquid	218.60	J/mol×K	298.15	NIST
Cp,liquid	221.88	J/mol×K	299.15	NIST
Cp,liquid	224.70	J/mol×K	300.00	NIST
Cp,solid	146.11	J/mol×K	298.15	NIST
η	[0.0007603; 0.0054860]	Pa×s	[293.15; 343.15]
η	0.0054860	Pa×s	293.15	Densities, Viscosities, and Excess Molar Enthalpies of 2-Pyrrolidone + Butanol Isomers at T ) (293.15, 298.15, and 303.15) K
η	0.0044330	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of 1-Bromobutane with Butanol Isomers at Several Temperatures
η	0.0044360	Pa×s	298.15	Densities, Viscosities, and Excess Molar Enthalpies of 2-Pyrrolidone + Butanol Isomers at T ) (293.15, 298.15, and 303.15) K
η	0.0044330	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
η	0.0033550	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
η	0.0033780	Pa×s	303.15	Densities, Viscosities, and Excess Molar Enthalpies of 2-Pyrrolidone + Butanol Isomers at T ) (293.15, 298.15, and 303.15) K
η	0.0033550	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of 1-Bromobutane with Butanol Isomers at Several Temperatures
η	0.0026110	Pa×s	308.15	Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
η	0.0026905	Pa×s	308.15	Densities and Viscosities of Binary Mixtures of n-Butanol with 2-Butanol, Isobutanol, and tert-Butanol from (303.15 to 343.15) K
η	0.0026110	Pa×s	308.15	Densities and Viscosities of Binary Mixtures of 1-Bromobutane with Butanol Isomers at Several Temperatures
η	0.0021423	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of n-Butanol with 2-Butanol, Isobutanol, and tert-Butanol from (303.15 to 343.15) K
η	0.0020740	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
η	0.0020740	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of 1-Bromobutane with Butanol Isomers at Several Temperatures
η	0.0016850	Pa×s	318.15	Densities and Viscosities of Binary Mixtures of 1-Bromobutane with Butanol Isomers at Several Temperatures
η	0.0016850	Pa×s	318.15	Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
η	0.0017369	Pa×s	318.15	Densities and Viscosities of Binary Mixtures of n-Butanol with 2-Butanol, Isobutanol, and tert-Butanol from (303.15 to 343.15) K
η	0.0014284	Pa×s	323.15	Densities and Viscosities of Binary Mixtures of n-Butanol with 2-Butanol, Isobutanol, and tert-Butanol from (303.15 to 343.15) K
η	0.0011964	Pa×s	328.15	Densities and Viscosities of Binary Mixtures of n-Butanol with 2-Butanol, Isobutanol, and tert-Butanol from (303.15 to 343.15) K
η	0.0010160	Pa×s	333.15	Densities and Viscosities of Binary Mixtures of n-Butanol with 2-Butanol, Isobutanol, and tert-Butanol from (303.15 to 343.15) K
η	0.0008734	Pa×s	338.15	Densities and Viscosities of Binary Mixtures of n-Butanol with 2-Butanol, Isobutanol, and tert-Butanol from (303.15 to 343.15) K
η	0.0007603	Pa×s	343.15	Densities and Viscosities of Binary Mixtures of n-Butanol with 2-Butanol, Isobutanol, and tert-Butanol from (303.15 to 343.15) K
εr	[10.40; 14.49]		[288.15; 308.15]
εr	14.49		288.15	Static Permittivities of Isomeric Butanol Mixtures at Temperatures from (288.15 to 308.15) K
εr	13.38		293.15	Static Permittivities of Isomeric Butanol Mixtures at Temperatures from (288.15 to 308.15) K
εr	12.49		298.15	Static Permittivities of Isomeric Butanol Mixtures at Temperatures from (288.15 to 308.15) K
εr	11.34		303.15	Static Permittivities of Isomeric Butanol Mixtures at Temperatures from (288.15 to 308.15) K
εr	10.40		308.15	Static Permittivities of Isomeric Butanol Mixtures at Temperatures from (288.15 to 308.15) K
ΔfusH	[0.49; 6.78]	kJ/mol	[286.10; 299.00]
ΔfusH	0.83	kJ/mol	286.10	NIST
ΔfusH	0.49	kJ/mol	294.50	NIST
ΔfusH	6.78	kJ/mol	298.50	NIST
ΔfusH	6.78	kJ/mol	298.50	NIST
ΔfusH	6.70	kJ/mol	299.00	NIST
ΔfusH	6.70	kJ/mol	299.00	NIST
ΔsubH	51.30	kJ/mol	275.50	NIST
ΔvapH	[33.60; 46.50]	kJ/mol	[303.00; 479.50]
ΔvapH	46.20 ± 0.10	kJ/mol	303.00	NIST
ΔvapH	46.12 ± 0.05	kJ/mol	303.20	NIST
ΔvapH	44.90 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	44.70	kJ/mol	328.00	NIST
ΔvapH	43.00 ± 0.10	kJ/mol	328.00	NIST
ΔvapH	42.50 ± 0.10	kJ/mol	330.00	NIST
ΔvapH	44.70	kJ/mol	331.50	NIST
ΔvapH	44.20	kJ/mol	334.00	NIST
ΔvapH	46.50	kJ/mol	334.50	NIST
ΔvapH	46.20	kJ/mol	337.00	NIST
ΔvapH	41.30 ± 0.10	kJ/mol	340.00	NIST
ΔvapH	43.40	kJ/mol	340.00	NIST
ΔvapH	41.00 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	42.70	kJ/mol	345.50	NIST
ΔvapH	42.60	kJ/mol	346.00	NIST
ΔvapH	40.40 ± 0.10	kJ/mol	346.00	NIST
ΔvapH	42.10	kJ/mol	348.00	NIST
ΔvapH	40.00 ± 0.10	kJ/mol	349.00	NIST
ΔvapH	41.40	kJ/mol	355.00	NIST
ΔvapH	41.40	kJ/mol	355.00	NIST
ΔvapH	39.07	kJ/mol	355.50	NIST
ΔvapH	39.04	kJ/mol	355.90	KDB
ΔvapH	39.00 ± 0.10	kJ/mol	356.00	NIST
ΔvapH	37.20 ± 0.10	kJ/mol	368.00	NIST
ΔvapH	39.80	kJ/mol	409.00	NIST
ΔvapH	43.20	kJ/mol	418.00	NIST
ΔvapH	38.70	kJ/mol	439.50	NIST
ΔvapH	33.60	kJ/mol	479.50	NIST
ν	[0.0000027; 0.0000056]	m2/s	[298.15; 313.15]
ν	0.0000056	m2/s	298.15	Viscosities of Binary Mixtures of Isomeric Butanols or Isomeric Chlorobutanes with 2-Methyltetrahydrofuran
ν	0.0000027	m2/s	313.15	Viscosities of Binary Mixtures of Isomeric Butanols or Isomeric Chlorobutanes with 2-Methyltetrahydrofuran
Pvap	[8.96; 818.16]	kPa	[305.87; 423.15]
Pvap	8.96	kPa	305.87	Vapor-Liquid Equilibrium for Benzaldehyde with 1-Methylethylbenzene and for 2-Methyl-propan-2-ol with 2,4,4-Trimethyl-1-pentene
Pvap	11.51	kPa	310.08	Vapor-Liquid Equilibrium for Benzaldehyde with 1-Methylethylbenzene and for 2-Methyl-propan-2-ol with 2,4,4-Trimethyl-1-pentene
Pvap	13.77	kPa	313.08	Vapour liquid equilibrium for the 2-methylpropane + methanol, +ethanol, +2-propanol, +2-butanol and +2-methyl-2-propanol systems at 313.15K
Pvap	13.72	kPa	313.14	Vapor-Liquid Equilibrium for Benzaldehyde with 1-Methylethylbenzene and for 2-Methyl-propan-2-ol with 2,4,4-Trimethyl-1-pentene
Pvap	16.11	kPa	316.04	Vapor-Liquid Equilibrium for Benzaldehyde with 1-Methylethylbenzene and for 2-Methyl-propan-2-ol with 2,4,4-Trimethyl-1-pentene
Pvap	19.43	kPa	319.50	Vapor-Liquid Equilibrium for Benzaldehyde with 1-Methylethylbenzene and for 2-Methyl-propan-2-ol with 2,4,4-Trimethyl-1-pentene
Pvap	23.07	kPa	322.78	Isothermal Vapor Liquid Equilibrium for Binary 2-Methylpropene - C1-C4 Alcohol-Systems
Pvap	23.28	kPa	322.94	Vapor-Liquid Equilibrium for Benzaldehyde with 1-Methylethylbenzene and for 2-Methyl-propan-2-ol with 2,4,4-Trimethyl-1-pentene
Pvap	23.80	kPa	323.20	Vapor Liquid Equilibrium for Butane + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-Propanol (TBA) at 323 K
Pvap	27.62	kPa	326.30	Vapor-Liquid Equilibrium for Benzaldehyde with 1-Methylethylbenzene and for 2-Methyl-propan-2-ol with 2,4,4-Trimethyl-1-pentene
Pvap	32.74	kPa	329.74	Vapor-Liquid Equilibrium for Benzaldehyde with 1-Methylethylbenzene and for 2-Methyl-propan-2-ol with 2,4,4-Trimethyl-1-pentene
Pvap	36.97	kPa	332.06	Vapor Liquid Equilibrium for the Trans-2-Butene + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol and + 2-Methyl-2-Propanol Systems at 332 K
Pvap	38.57	kPa	333.15	Vapor-Liquid Equilibrium for Benzaldehyde with 1-Methylethylbenzene and for 2-Methyl-propan-2-ol with 2,4,4-Trimethyl-1-pentene
Pvap	38.60	kPa	333.15	Isothermal Vapor-Liquid Equilibria for Binary Mixtures Composed of the Closely Boiling Compounds 1,2-Dimethoxybenzene and 2-Methoxyphenol with an Adducted Agent: tert-Butanol or Morpholine
Pvap	40.00	kPa	333.90	Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
Pvap	44.94	kPa	336.41	Vapor-Liquid Equilibrium for Benzaldehyde with 1-Methylethylbenzene and for 2-Methyl-propan-2-ol with 2,4,4-Trimethyl-1-pentene
Pvap	52.29	kPa	339.74	Vapor-Liquid Equilibrium for Benzaldehyde with 1-Methylethylbenzene and for 2-Methyl-propan-2-ol with 2,4,4-Trimethyl-1-pentene
Pvap	53.33	kPa	340.13	Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
Pvap	60.80	kPa	343.15	Isothermal Vapor-Liquid Equilibria for Binary Mixtures Composed of the Closely Boiling Compounds 1,2-Dimethoxybenzene and 2-Methoxyphenol with an Adducted Agent: tert-Butanol or Morpholine
Pvap	61.09	kPa	343.25	Vapor-Liquid Equilibrium for Benzaldehyde with 1-Methylethylbenzene and for 2-Methyl-propan-2-ol with 2,4,4-Trimethyl-1-pentene
Pvap	66.66	kPa	344.84	Isobaric Phase Equilibrium of tert-Butyl Alcohol + Glycerol at Local and Subatmospheric Pressures, Volumetric Properties, and Molar Refractivity from 303.15 to 333.15 K of tert-Butyl Alcohol + Glycerol, tert-Butyl Alcohol + Water, and Water + Glycerol Binary Systems
Pvap	66.66	kPa	345.21	Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
Pvap	70.27	kPa	346.50	Vapor-Liquid Equilibrium for Benzaldehyde with 1-Methylethylbenzene and for 2-Methyl-propan-2-ol with 2,4,4-Trimethyl-1-pentene
Pvap	79.99	kPa	349.23	Isobaric Phase Equilibrium of tert-Butyl Alcohol + Glycerol at Local and Subatmospheric Pressures, Volumetric Properties, and Molar Refractivity from 303.15 to 333.15 K of tert-Butyl Alcohol + Glycerol, tert-Butyl Alcohol + Water, and Water + Glycerol Binary Systems
Pvap	79.99	kPa	349.53	Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
Pvap	80.85	kPa	349.84	Vapor-Liquid Equilibrium for Benzaldehyde with 1-Methylethylbenzene and for 2-Methyl-propan-2-ol with 2,4,4-Trimethyl-1-pentene
Pvap	92.40	kPa	353.15	Isothermal Vapor-Liquid Equilibria for Binary Mixtures Composed of the Closely Boiling Compounds 1,2-Dimethoxybenzene and 2-Methoxyphenol with an Adducted Agent: tert-Butanol or Morpholine
Pvap	92.53	kPa	353.15	Vapor-Liquid Equilibrium for Benzaldehyde with 1-Methylethylbenzene and for 2-Methyl-propan-2-ol with 2,4,4-Trimethyl-1-pentene
Pvap	93.32	kPa	353.32	Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
Pvap	95.99	kPa	353.80	Isobaric Phase Equilibrium of tert-Butyl Alcohol + Glycerol at Local and Subatmospheric Pressures, Volumetric Properties, and Molar Refractivity from 303.15 to 333.15 K of tert-Butyl Alcohol + Glycerol, tert-Butyl Alcohol + Water, and Water + Glycerol Binary Systems
Pvap	98.66	kPa	354.61	Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
Pvap	100.00	kPa	355.20	Isobaric vapor-liquid equilibria for the extractive distillation of tert-butyl alcohol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
Pvap	100.91	kPa	355.31	Vapor-Liquid Equilibrium for Benzaldehyde with 1-Methylethylbenzene and for 2-Methyl-propan-2-ol with 2,4,4-Trimethyl-1-pentene
Pvap	101.00	kPa	355.56	Isobaric Vapor Liquid Equilibrium of tert-Butyl Alcohol + Water + Triethanolamine-Based Ionic Liquid Ternary Systems at 101.3 kPa
Pvap	101.33	kPa	355.59	Isobaric Vapor-Liquid Equilibrium for Binary and Ternary Systems of tert-Butanol + tert-Butyl Acetate + Chlorobenzene at 101.33 kPa
Pvap	101.30	kPa	355.80	Isobaric vapour-liquid equilibrium of (tert-butanol + water) system with biological buffer TRIS at 101.3 kPa
Pvap	142.60	kPa	364.50	Vapour liquid equilibrium for the systems butane + methanol, +2-propanol, +1-butanol, +2-butanol, +2-methyl-2-propanol at 364.5K
Pvap	142.60	kPa	364.50	Vapor Liquid Equilibrium for the Systems 2-Methylpropane + Methanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol at 364.5 K
Pvap	143.30	kPa	364.52	Vapor Liquid Equilibrium for the Systems trans-2-Butene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol at 364.5 K
Pvap	143.00	kPa	364.52	Vapor-Liquid Equilibrium for the cis-2-Butene + Methanol, + 2-Propanol, + 2-Butanol, + 2-Methyl-2-propanol Systems at 364.5 K
Pvap	142.70	kPa	364.52	Isothermal Vapor Liquid Equilibrium for 2-Methylpropene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol Binary Systems at 364.5 K
Pvap	191.18	kPa	373.15	Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap	192.46	kPa	373.15	Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap	816.37	kPa	423.15	Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap	818.16	kPa	423.15	Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
n0	[1.37097; 1.38870]		[293.15; 323.15]
n0	1.38810		293.15	Liquid-liquid equilibrium for the ternary system water + 2-methyl-1-propanol + butyl acetate and water + 2-methyl-2-propanol + butyl acetate at (298.15 and 323.15) K
n0	1.38770		293.15	Isobaric Vapor Liquid Equilibrium Data for the Binary Mixtures 2-Methyl Propan-2-ol with Tetraethoxysilane and 1-Phenyl Ethanone at 95.5 kPa
n0	1.38780		293.15	Isobaric Vapor Liquid Equilibrium Data of 2-Methyl-propan-2-ol (1) + Heptan-1-ol (2), Methanol (1) + Heptan-1-ol (2), Ethanol (1) + Heptan-1-ol (2), and Propan-1-ol (1) + Heptan-1-ol (2) at 96.5 kPa
n0	1.38510		298.15	Volumetric behavior of carbon dioxide + 2-methyl-1-propanol and carbondioxide + 2-methyl-2-propanol mixtures at 313.15 K
n0	1.38510		298.15	Isobaric (vapour + liquid) equilibrium for N-methyl-2-pyrrolidone with branched alcohols
n0	1.38510		298.15	Excess volumes and excess enthalpies of N-methyl-2-pyrrolidone with branched alcohols
n0	1.38510		298.15	Isobaric vapor-liquid equilibria for the binary systems isobutyl alcohol + isobutyl acetate and tert-butyl alcohol + tert-butyl acetate at 20 and 101.3 kPa
n0	1.38520		298.15	(Vapor + liquid) equilibria of binary mixtures formed by iso-octane with a variety of compounds at 95.8 kPa
n0	1.38520		298.15	(Vapor + liquid) equilibria of the binary mixtures of m-cresol with C1 C4 aliphatic alcohols at 95.5 kPa
n0	1.38520		298.15	Excess Gibbs free energies of the binary mixtures of acetonitrile with butanols at 94.83 kPa
n0	1.38870		298.15	Bubble Temperatures of the Binary Mixtures of Dimethylcarbonate with Some Alcohols at 95.8 kPa
n0	1.38520		298.15	Vapor-Liquid Equilibrium and Excess Gibbs Energies of Hexane + N,N-Dimethyl Formamide, 2-Methylpropan-2-ol + 2-Aminophenol, N,N-Dimethyl Formamide, and 2-Propanol + Diisopropyl Amine at 94.4 kPa
n0	1.38520		298.15	Excess Gibbs energies of selected binary mixtures formed by N,N-dimethyl formamide at 95.5 kPa
n0	1.38520		298.15	Activity coefficients of the binary mixtures of a-cresol or p-cresol with C l-C4 aliphatic alcohols near ambient pressure
n0	1.38481		298.15	Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Ethanol, 2-Methylpropan-2-ol, and 2,2,4-Trimethylpentane
n0	1.38500		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	1.38640		298.20	Dielectric study of molecular association in the binary mixtures (2-ethyl-1-hexanol + alcohol) and (cyclohexane + alcohol) at 298.2 K
n0	1.38200		303.15	Isobaric Vapor-Liquid Equilibria and Excess Quantities for Binary Mixtures of an Ethyl Ester + tert-Butanol and a New Approach to VLE Data Processing
n0	1.38220		303.15	Correlation and Prediction of Excess Quantities and Vapor-Liquid Equilibria of Alkyl Esters + tert-Butyl Alcohol: Experimental Data for Propyl Esters + tert-Butyl Alcohol
n0	1.38222		303.15	Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
n0	1.38222		303.15	Experimental Determination of Densities and Refractive Indices of the Ternary Mixture 2-Methyl-2-propanol + Cyclohexylamine + n-Heptane at T = (303.15 to 323.15) K
n0	1.37960		308.15	Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Ethanol, 2-Methylpropan-2-ol, and 2,2,4-Trimethylpentane
n0	1.37947		308.15	Experimental Determination of Densities and Refractive Indices of the Ternary Mixture 2-Methyl-2-propanol + Cyclohexylamine + n-Heptane at T = (303.15 to 323.15) K
n0	1.37947		308.15	Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
n0	1.37667		313.15	Experimental Determination of Densities and Refractive Indices of the Ternary Mixture 2-Methyl-2-propanol + Cyclohexylamine + n-Heptane at T = (303.15 to 323.15) K
n0	1.37667		313.15	Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
n0	1.37416		318.15	Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Ethanol, 2-Methylpropan-2-ol, and 2,2,4-Trimethylpentane
n0	1.37384		318.15	Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
n0	1.37384		318.15	Experimental Determination of Densities and Refractive Indices of the Ternary Mixture 2-Methyl-2-propanol + Cyclohexylamine + n-Heptane at T = (303.15 to 323.15) K
n0	1.37410		318.15	Excess Properties and Isobaric Vapor-Liquid Equilibria for Binary Mixtures of Methyl Esters + tert-Butanol
n0	1.37097		323.15	Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
n0	1.37097		323.15	Experimental Determination of Densities and Refractive Indices of the Ternary Mixture 2-Methyl-2-propanol + Cyclohexylamine + n-Heptane at T = (303.15 to 323.15) K
ρl	[725.06; 787.00]	kg/m3	[293.00; 348.15]
ρl	787.00	kg/m3	293.00	KDB
ρl	785.75	kg/m3	293.15	Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
ρl	780.85	kg/m3	298.15	Excess Molar Volumes and Surface Tensions of 1,2,4-Trimethylbenzene and 1,3,5-Trimethylbenzene with 1-Butanol, 2-Methyl-1-propanol, 2-Butanol, and 2-Methyl-2-propanol at 298.15 K
ρl	780.27	kg/m3	298.15	Excess Molar Volumes and Surface Tensions of Xylene with 2-propanol or 2-methyl-2-propanol at 298.15 K
ρl	781.04	kg/m3	298.15	Vapor-liquid equilibria of binary systems composed of polyoxyethylene 4-octylphenyl ether and alcohols: Experimental measurements and correlation
ρl	780.44	kg/m3	298.15	Isothermal Vapor-Liquid Equilibria in the Two Binary and the Ternary Systems Composed of tert-Amyl Methyl Ether, tert-Butanol, and Isooctane
ρl	780.78	kg/m3	298.15	Densities and Viscosities of the Ternary Mixtures 2-Methyl-1-propanol (or 2-Methyl-2-propanol) + N-Hexane + 1-Chlorobutane at 298.15 K
ρl	780.78	kg/m3	298.15	Surface Tensions of the Ternary Mixtures Containing an Isomeric Butanol + n-Hexane + 1-Chlorobutane at 298.15 K
ρl	781.00	kg/m3	298.15	(Vapour + liquid) equilibrium of binary mixtures (1,3-dioxolane or 1,4-dioxane + 2-methyl-1-propanol or 2-methyl-2-propanol) at isobaric conditions
ρl	780.57	kg/m3	298.15	Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
ρl	780.86	kg/m3	298.15	Liquid Liquid Equilibria, Equilibrium Phase Densities, and Refractive Indices for the Quaternary Mixtures Containing 2-Propanol or 2-Methyl-2-Propanol of Fuel Oxygenate at T = 298.15 and 318.15 K
ρl	780.72	kg/m3	298.15	Experimental and theoretical excess molar properties of imidazolium based ionic liquids with isomers of butanol
ρl	780.61	kg/m3	298.15	Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρl	780.63	kg/m3	298.15	Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
ρl	781.20	kg/m3	298.15	Bubble point temperatures of the binary mixtures of nitrobenzene with C1 C4 aliphatic alcohols at 94.95 kPa
ρl	779.48	kg/m3	299.15	Densities and volume properties of (water + tert-butanol) over the temperature range of (274.15 to 348.15) K at pressure of 0.1 MPa
ρl	779.48	kg/m3	299.15	Excess specific volume of water + tert-butyl alcohol solvent mixtures: Experimental data, modeling and derived excess partial specific thermodynamic quantities.
ρl	775.39	kg/m3	303.15	Densities and volume properties of (water + tert-butanol) over the temperature range of (274.15 to 348.15) K at pressure of 0.1 MPa
ρl	775.46	kg/m3	303.15	Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
ρl	775.51	kg/m3	303.15	Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
ρl	775.38	kg/m3	303.15	Excess specific volume of water + tert-butyl alcohol solvent mixtures: Experimental data, modeling and derived excess partial specific thermodynamic quantities.
ρl	775.42	kg/m3	303.15	Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρl	775.10	kg/m3	303.15	Viscous synergy and antagonism and isentropic compressibility of ternary mixtures containing 1,3-dioxolane, water and monoalkanols at 303.15K
ρl	775.41	kg/m3	303.15	Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl	770.36	kg/m3	308.15	Densities and Viscosities of Binary Mixtures of 2-Butanol + Isobutanol, 2-Butanol + tert-Butanol, and Isobutanol + tert-Butanol from (308.15 to 343.15) K
ρl	770.25	kg/m3	308.15	Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
ρl	770.39	kg/m3	308.15	Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
ρl	770.19	kg/m3	308.15	Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl	770.21	kg/m3	308.15	Experimental and theoretical excess molar properties of imidazolium based ionic liquids with isomers of butanol
ρl	770.15	kg/m3	308.15	Densities and volume properties of (water + tert-butanol) over the temperature range of (274.15 to 348.15) K at pressure of 0.1 MPa
ρl	770.21	kg/m3	308.15	Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρl	770.17	kg/m3	308.15	Excess specific volume of water + tert-butyl alcohol solvent mixtures: Experimental data, modeling and derived excess partial specific thermodynamic quantities.
ρl	764.95	kg/m3	313.15	Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
ρl	764.88	kg/m3	313.15	Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl	764.86	kg/m3	313.15	Excess specific volume of water + tert-butyl alcohol solvent mixtures: Experimental data, modeling and derived excess partial specific thermodynamic quantities.
ρl	765.07	kg/m3	313.15	Densities and Viscosities of Binary Mixtures of 2-Butanol + Isobutanol, 2-Butanol + tert-Butanol, and Isobutanol + tert-Butanol from (308.15 to 343.15) K
ρl	765.26	kg/m3	313.15	Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
ρl	764.84	kg/m3	313.15	Densities and volume properties of (water + tert-butanol) over the temperature range of (274.15 to 348.15) K at pressure of 0.1 MPa
ρl	764.92	kg/m3	313.15	Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρl	760.13	kg/m3	318.15	Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
ρl	759.56	kg/m3	318.15	Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
ρl	759.42	kg/m3	318.15	Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρl	759.47	kg/m3	318.15	Excess specific volume of water + tert-butyl alcohol solvent mixtures: Experimental data, modeling and derived excess partial specific thermodynamic quantities.
ρl	759.50	kg/m3	318.15	Experimental and theoretical excess molar properties of imidazolium based ionic liquids with isomers of butanol
ρl	759.46	kg/m3	318.15	Densities and volume properties of (water + tert-butanol) over the temperature range of (274.15 to 348.15) K at pressure of 0.1 MPa
ρl	759.67	kg/m3	318.15	Densities and Viscosities of Binary Mixtures of 2-Butanol + Isobutanol, 2-Butanol + tert-Butanol, and Isobutanol + tert-Butanol from (308.15 to 343.15) K
ρl	759.49	kg/m3	318.15	Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl	754.01	kg/m3	323.15	Excess specific volume of water + tert-butyl alcohol solvent mixtures: Experimental data, modeling and derived excess partial specific thermodynamic quantities.
ρl	753.95	kg/m3	323.15	Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρl	753.94	kg/m3	323.15	Densities and volume properties of (water + tert-butanol) over the temperature range of (274.15 to 348.15) K at pressure of 0.1 MPa
ρl	754.19	kg/m3	323.15	Densities and Viscosities of Binary Mixtures of 2-Butanol + Isobutanol, 2-Butanol + tert-Butanol, and Isobutanol + tert-Butanol from (308.15 to 343.15) K
ρl	754.10	kg/m3	323.15	Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
ρl	754.01	kg/m3	323.15	Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl	748.62	kg/m3	328.15	Densities and Viscosities of Binary Mixtures of 2-Butanol + Isobutanol, 2-Butanol + tert-Butanol, and Isobutanol + tert-Butanol from (308.15 to 343.15) K
ρl	742.70	kg/m3	333.15	Densities and volume properties of (water + tert-butanol) over the temperature range of (274.15 to 348.15) K at pressure of 0.1 MPa
ρl	742.95	kg/m3	333.15	Densities and Viscosities of Binary Mixtures of 2-Butanol + Isobutanol, 2-Butanol + tert-Butanol, and Isobutanol + tert-Butanol from (308.15 to 343.15) K
ρl	737.19	kg/m3	338.15	Densities and Viscosities of Binary Mixtures of 2-Butanol + Isobutanol, 2-Butanol + tert-Butanol, and Isobutanol + tert-Butanol from (308.15 to 343.15) K
ρl	731.31	kg/m3	343.15	Densities and Viscosities of Binary Mixtures of 2-Butanol + Isobutanol, 2-Butanol + tert-Butanol, and Isobutanol + tert-Butanol from (308.15 to 343.15) K
ρl	725.06	kg/m3	348.15	Densities and volume properties of (water + tert-butanol) over the temperature range of (274.15 to 348.15) K at pressure of 0.1 MPa
ΔfusS	[1.66; 22.72]	J/mol×K	[286.10; 299.00]
ΔfusS	2.90	J/mol×K	286.10	NIST
ΔfusS	1.66	J/mol×K	294.50	NIST
ΔfusS	22.72	J/mol×K	298.50	NIST
ΔfusS	22.72	J/mol×K	298.50	NIST
ΔfusS	22.42	J/mol×K	299.00	NIST
csound,fluid	[1013.01; 1122.80]	m/s	[298.15; 323.15]
csound,fluid	1122.80	m/s	298.15	Densities and speeds of sound for binary mixtures of (1,3-dioxolane or 1,4-dioxane) with (2-methyl-1-propanol or 2-methyl-2-propanol) at the temperatures 298.15 K and 313.15 K
csound,fluid	1108.98	m/s	301.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1099.02	m/s	303.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1101.90	m/s	303.15	Excess Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 2-Methyl-1-propanol or 2-Methyl-2-propanol at Several Temperatures
csound,fluid	1098.21	m/s	303.15	Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
csound,fluid	1088.33	m/s	305.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1077.71	m/s	308.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1067.22	m/s	310.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1057.40	m/s	313.15	Densities and speeds of sound for binary mixtures of (1,3-dioxolane or 1,4-dioxane) with (2-methyl-1-propanol or 2-methyl-2-propanol) at the temperatures 298.15 K and 313.15 K
csound,fluid	1055.36	m/s	313.15	Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
csound,fluid	1056.73	m/s	313.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1056.40	m/s	313.15	Excess Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 2-Methyl-1-propanol or 2-Methyl-2-propanol at Several Temperatures
csound,fluid	1046.12	m/s	315.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1035.66	m/s	318.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1025.17	m/s	320.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1014.76	m/s	323.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1013.01	m/s	323.15	Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
csound,fluid	1015.90	m/s	323.15	Excess Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 2-Methyl-1-propanol or 2-Methyl-2-propanol at Several Temperatures
γ	[0.02; 0.02]	N/m	[298.15; 328.15]
γ	0.02	N/m	298.15	Equilibrium surface tension and the interaction energy of DMSO with tert-butyl alcohol or iso-amyl alcohol at various temperatures
γ	0.02	N/m	308.15	Equilibrium surface tension and the interaction energy of DMSO with tert-butyl alcohol or iso-amyl alcohol at various temperatures
γ	0.02	N/m	318.15	Equilibrium surface tension and the interaction energy of DMSO with tert-butyl alcohol or iso-amyl alcohol at various temperatures
γ	0.02	N/m	318.20	KDB
γ	0.02	N/m	328.15	Equilibrium surface tension and the interaction energy of DMSO with tert-butyl alcohol or iso-amyl alcohol at various temperatures

Datasets

1. Viscosity, Pa*s (1)
2. Mass density, kg/m3 (3)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.15	101.33	0.0034
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
308.15	101.30	770.14
323.15	101.30	753.94
323.15	10000.00	764.58
323.15	25000.00	778.73
323.15	50000.00	798.2
323.15	75000.00	813.79
323.15	100000.00	827.34
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
308.15	97.00	770.2
348.15	98.00	725.1
303.15	99.00	775.3
313.15	99.00	764.8
323.15	99.00	753.9
343.15	99.00	731.0
353.15	99.00	719.0
318.15	100.00	759.4
338.15	100.00	737.1
328.15	101.00	748.4
333.15	103.00	742.8
358.15	103.00	712.8
358.15	293.00	713.1
348.15	295.00	725.3
313.15	298.00	765.0
318.15	298.00	759.6
323.15	298.00	754.1
328.15	298.00	748.7
303.15	298.00	775.5
308.15	298.00	770.4
363.15	299.00	706.4
353.15	300.00	719.3
343.15	305.00	731.3
333.15	307.00	743.1
338.15	309.00	737.3
318.15	498.00	759.8
348.15	498.00	725.7
358.15	498.00	713.4
328.15	499.00	748.9
303.15	499.00	775.7
308.15	500.00	770.6
353.15	501.00	719.6
313.15	502.00	765.2
323.15	502.00	754.4
333.15	502.00	743.3
363.15	502.00	706.8
343.15	503.00	731.6
338.15	505.00	737.6
308.15	897.00	771.0
353.15	897.00	720.2
328.15	898.00	749.4
338.15	898.00	738.1
348.15	898.00	726.2
303.15	898.00	776.1
358.15	899.00	714.0
318.15	901.00	760.3
323.15	901.00	754.9
343.15	901.00	732.1
363.15	901.00	707.4
313.15	904.00	765.7
333.15	915.00	743.8
353.15	1000.00	720.3
303.15	1002.00	776.2
308.15	1002.00	771.1
343.15	1002.00	732.2
363.15	1002.00	707.6
338.15	1003.00	738.2
358.15	1003.00	714.2
323.15	1004.00	755.0
348.15	1004.00	726.4
328.15	1005.00	749.5
318.15	1006.00	760.4
333.15	1007.00	744.0
313.15	1009.00	765.8
343.15	2000.00	733.6
353.15	2000.00	721.8
328.15	2001.00	750.7
338.15	2001.00	739.5
318.15	2001.00	761.5
363.15	2001.00	709.2
323.15	2003.00	756.1
348.15	2006.00	727.8
303.15	2007.00	777.1
358.15	2008.00	715.7
308.15	2009.00	772.1
333.15	2013.00	745.2
313.15	2016.00	766.8
353.15	2999.00	723.2
308.15	3000.00	773.1
328.15	3001.00	751.9
343.15	3001.00	734.9
348.15	3001.00	729.2
323.15	3002.00	757.2
318.15	3003.00	762.6
358.15	3003.00	717.3
338.15	3005.00	740.8
363.15	3005.00	710.8
333.15	3006.00	746.4
313.15	3006.00	767.8
303.15	3007.00	778.1
303.15	4999.00	780.0
353.15	4999.00	726.1
328.15	5001.00	754.1
318.15	5002.00	764.7
333.15	5002.00	748.8
363.15	5002.00	713.9
338.15	5003.00	743.2
358.15	5003.00	720.2
323.15	5004.00	759.4
343.15	5005.00	737.5
348.15	5005.00	731.9
308.15	5006.00	775.1
313.15	5010.00	769.9
348.15	6999.00	734.5
353.15	6999.00	728.8
328.15	7001.00	756.3
323.15	7002.00	761.5
303.15	7003.00	781.9
358.15	7003.00	723.0
343.15	7004.00	740.0
333.15	7005.00	751.1
318.15	7005.00	766.7
308.16	7005.00	777.0
313.15	7006.00	771.8
338.15	7014.00	745.6
363.15	7023.00	716.9
303.15	8992.00	783.7
353.15	8998.00	731.4
318.15	8999.00	768.7
333.15	9001.00	753.3
358.15	9001.00	725.8
363.15	9001.00	719.7
323.15	9002.00	763.5
328.15	9004.00	758.5
338.15	9004.00	747.9
313.15	9005.00	773.7
308.15	9006.00	778.8
348.15	9012.00	737.0
343.15	9033.00	742.4
358.15	9998.00	727.1
328.15	9999.00	759.5
333.15	9999.00	754.3
338.15	10002.00	749.0
323.15	10002.00	764.5
318.15	10002.00	769.7
353.15	10003.00	732.6
303.15	10005.00	784.6
313.15	10007.00	774.7
308.15	10007.00	779.7
363.15	10009.00	721.1
348.15	10014.00	738.2
343.15	10020.00	743.6
353.15	11997.00	735.1
338.15	11998.00	751.2
328.15	11999.00	761.6
318.15	11999.00	771.6
303.15	11999.00	786.3
323.15	12000.00	766.5
343.15	12001.00	745.8
333.15	12003.00	756.5
348.15	12003.00	740.6
308.15	12005.00	781.5
313.15	12005.00	776.5
358.15	12010.00	729.7
363.15	12038.00	723.8
363.15	14998.00	727.6
338.15	14999.00	754.4
348.15	14999.00	744.0
323.15	14999.00	769.3
358.15	14999.00	733.3
333.15	15000.00	759.6
353.15	15001.00	738.7
343.15	15002.00	749.1
328.15	15004.00	764.5
313.15	15005.00	779.2
318.15	15010.00	774.4
308.15	15021.00	784.1
333.15	17995.00	762.5
338.15	17997.00	757.5
318.15	17998.00	777.0
323.15	17998.00	772.1
348.15	17999.00	747.3
353.15	17999.00	742.1
363.15	18000.00	731.3
343.15	18001.00	752.3
313.15	18003.00	781.8
328.15	18006.00	767.4
308.16	18006.00	786.6
358.15	18040.00	736.9
328.15	19995.00	769.2
333.15	19997.00	764.4
358.15	19997.00	739.1
308.15	19998.00	788.2
323.15	20000.00	773.9
348.15	20000.00	749.4
353.15	20000.00	744.2
318.15	20006.00	778.8
338.15	20007.00	759.4
313.15	20015.00	783.5
343.15	20018.00	754.4
363.15	20033.00	733.7
343.15	21994.00	756.4
358.15	21995.00	741.3
333.15	21996.00	766.2
348.15	21998.00	751.5
338.15	21999.00	761.4
318.15	21999.00	780.5
353.15	21999.00	746.4
328.15	22000.00	771.0
323.15	22000.00	775.7
313.15	22002.00	785.1
308.15	22003.00	789.8
363.15	22005.00	735.9
308.15	24990.00	792.2
318.15	24994.00	782.9
333.15	24994.00	768.9
328.15	24996.00	773.6
348.15	24996.00	754.4
353.15	24997.00	749.4
338.15	25000.00	764.2
323.15	25000.00	778.2
363.15	25000.00	739.2
313.15	25007.00	787.5
358.15	25017.00	744.5
343.15	25026.00	759.3
343.15	27993.00	762.1
333.15	27993.00	771.6
338.15	27994.00	766.9
358.15	27994.00	747.6
323.15	27995.00	780.7
348.15	27995.00	757.3
328.15	27998.00	776.2
353.15	27999.00	752.5
313.15	28002.00	789.9
318.15	28005.00	785.4
308.15	28006.00	794.5
363.15	28009.00	742.4
358.15	29991.00	749.6
313.15	30000.00	791.4
318.15	30001.00	787.0
323.15	30002.00	782.4
333.15	30003.00	773.3
343.15	30004.00	763.9
353.15	30004.00	754.4
328.15	30005.00	777.9
308.15	30005.00	796.0
338.15	30011.00	768.6
363.15	30011.00	744.4
348.15	30045.00	759.3
343.15	32000.00	765.7
348.15	32000.00	761.0
323.15	32000.00	784.0
318.15	32001.00	788.5
313.16	32001.00	792.9
358.15	32001.00	751.5
353.15	32003.00	756.3
333.15	32004.00	775.0
328.15	32005.00	779.5
338.15	32005.00	770.4
363.15	32033.00	746.5
333.15	32850.00	775.7
333.15	32871.00	775.7
348.15	32878.00	761.8
343.15	32963.00	766.6
363.15	32982.00	747.4
353.15	32985.00	757.1
318.15	32993.00	789.3
358.15	32997.00	752.5
338.15	32998.00	771.2
323.15	33000.00	784.7
343.15	33001.00	766.6
313.15	33001.00	793.7
323.15	33001.00	784.7
353.15	33002.00	757.2
318.15	33002.00	789.3
348.15	33012.00	761.9
313.15	33012.00	793.6
363.15	33012.00	747.4
358.15	33015.00	752.5
328.15	33023.00	780.3
338.15	33033.00	771.2
328.15	33038.00	780.4
333.15	34000.00	776.6
348.15	34000.00	762.8
353.15	34000.00	758.1
323.15	34000.00	785.5
343.15	34002.00	767.5
313.15	34006.00	794.4
338.15	34007.00	772.0
318.15	34010.00	790.0
328.15	34013.00	781.1
363.15	34035.00	748.4
358.15	34056.00	753.5
333.15	34990.00	777.4
363.15	34999.00	749.3
338.15	35000.00	772.9
348.15	35001.00	763.7
318.15	35001.00	790.8
343.15	35003.00	768.3
353.15	35004.00	759.0
328.15	35004.00	781.9
323.15	35004.00	786.2
313.15	35008.00	795.1
358.15	35075.00	754.4
358.15	37998.00	757.0
363.15	37998.00	752.1
318.15	38000.00	793.0
323.15	38000.00	788.5
348.15	38001.00	766.3
328.15	38002.00	784.3
333.15	38004.00	779.8
313.15	38012.00	797.2
343.15	38027.00	770.8
338.15	38031.00	775.3
363.16	38458.00	752.5
353.15	38477.00	762.2
363.15	39147.00	753.2
333.15	39997.00	781.4
343.15	39998.00	772.5
323.15	39998.00	790.0
348.15	39999.00	768.0
358.15	40001.00	758.8
313.15	40002.00	798.6
353.15	40002.00	763.4
363.15	40009.00	753.9
318.15	40010.00	794.4
338.15	40024.00	776.9
328.15	40024.00	785.8
348.15	41997.00	769.6
323.15	41998.00	791.5
338.15	41998.00	778.5
333.15	41998.00	782.9
363.15	41998.00	755.7
328.15	41999.00	787.2
343.15	42000.00	774.1
358.15	42007.00	760.6
313.15	42007.00	800.0
318.15	42021.00	795.9
353.15	42035.00	765.1
338.15	43195.00	779.4
338.15	44574.00	780.4
333.15	44909.00	785.1
313.15	44997.00	802.0
348.15	44999.00	772.0
363.15	44999.00	758.4
323.15	45000.00	793.6
358.15	45002.00	763.1
328.15	45002.00	789.4
318.15	45005.00	797.9
353.15	45022.00	767.6
338.15	46152.00	781.6
358.15	47995.00	765.5
323.15	47996.00	795.7
363.15	47996.00	760.9
328.15	47997.00	791.6
318.15	47997.00	799.9
353.15	48092.00	770.1
333.15	48119.00	787.4
338.15	48333.00	783.3
353.15	49989.00	771.5
328.15	49992.00	793.0
318.15	49998.00	801.3
363.15	49998.00	762.5
333.15	50000.00	788.7
323.15	50000.00	797.1
358.15	50001.00	767.0
338.15	50050.00	784.5
328.16	51996.00	794.3
323.15	51998.00	798.4
363.15	52002.00	764.2
318.15	52004.00	802.6
333.15	52050.00	790.2
338.15	52462.00	786.3
328.15	55000.00	796.4
318.15	55002.00	804.6
363.15	55003.00	766.6
323.15	55006.00	800.5
333.15	55010.00	792.3
338.15	56690.00	789.2
318.15	57994.00	806.5
323.15	57995.00	802.4
328.15	57995.00	798.3
333.15	57996.00	794.3
363.15	57998.00	768.9
363.15	59999.00	770.4
323.15	60000.00	803.7
318.15	60002.00	807.7
328.15	60003.00	799.6
333.15	60003.00	795.6
338.15	60003.00	791.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	5.61	780.885
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[85.11; 285.28]	J/mol×K	[200.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			6.55600e+01
Coefficient B			-5.40880e+02
Coefficient C			5.65024e+00
Coefficient D			1.46950e-04
Coefficient E			-5.23240e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	85.11	J/mol×K	200.00	Calculated Property
Cp,gas	127.39	J/mol×K	344.44	Calculated Property
Cp,gas	165.37	J/mol×K	488.89	Calculated Property
Cp,gas	195.66	J/mol×K	633.33	Calculated Property
Cp,gas	219.64	J/mol×K	777.78	Calculated Property
Cp,gas	238.82	J/mol×K	922.22	Calculated Property
Cp,gas	254.30	J/mol×K	1066.67	Calculated Property
Cp,gas	266.88	J/mol×K	1211.11	Calculated Property
Cp,gas	277.07	J/mol×K	1355.56	Calculated Property
Cp,gas	285.28	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[221.83; 296.27]	J/mol×K	[298.15; 460.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			-1.58220e+02
Coefficient B			-1.66800e+02
Coefficient C			6.26024e+00
Coefficient D			1.39590e-03
Coefficient E			-1.98760e-06
Temperature range, min.			298.15
Temperature range, max.			460.00
Cp,liquid	221.83	J/mol×K	298.15	Calculated Property
Cp,liquid	235.35	J/mol×K	316.13	Calculated Property
Cp,liquid	247.45	J/mol×K	334.12	Calculated Property
Cp,liquid	258.16	J/mol×K	352.10	Calculated Property
Cp,liquid	267.55	J/mol×K	370.08	Calculated Property
Cp,liquid	275.67	J/mol×K	388.07	Calculated Property
Cp,liquid	282.56	J/mol×K	406.05	Calculated Property
Cp,liquid	288.27	J/mol×K	424.03	Calculated Property
Cp,liquid	292.82	J/mol×K	442.02	Calculated Property
Cp,liquid	296.27	J/mol×K	460.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0060901; 0.0001006]	Pa×s	[293.15; 451.21]	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			-9.33240e+02
Coefficient B			3.91840e+04
Coefficient C			1.42250e+02
Coefficient D			-1.58300e-04
Coefficient E			2.00000e+00
Temperature range, min.			293.15
Temperature range, max.			451.21
η	0.0060901	Pa×s	293.15	Calculated Property
η	0.0023379	Pa×s	310.71	Calculated Property
η	0.0011588	Pa×s	328.27	Calculated Property
η	0.0006876	Pa×s	345.84	Calculated Property
η	0.0004604	Pa×s	363.40	Calculated Property
η	0.0003321	Pa×s	380.96	Calculated Property
η	0.0002489	Pa×s	398.52	Calculated Property
η	0.0001880	Pa×s	416.09	Calculated Property
η	0.0001399	Pa×s	433.65	Calculated Property
η	0.0001006	Pa×s	451.21	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[46.99; 0.14]	kJ/mol	[298.00; 506.20]	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			9.49928e+01
Coefficient B			1.07739e+00
Coefficient C			-1.85452e-01
Coefficient D			-8.22732e-01
Coefficient E			5.35399e-01
Critical temperature, Tc (K)			5.06210e+02
Temperature range, min.			298.00
Temperature range, max.			506.20
ΔvapH	46.99	kJ/mol	298.00	Calculated Property
ΔvapH	43.98	kJ/mol	321.13	Calculated Property
ΔvapH	40.91	kJ/mol	344.27	Calculated Property
ΔvapH	37.71	kJ/mol	367.40	Calculated Property
ΔvapH	34.28	kJ/mol	390.53	Calculated Property
ΔvapH	30.50	kJ/mol	413.67	Calculated Property
ΔvapH	26.17	kJ/mol	436.80	Calculated Property
ΔvapH	20.98	kJ/mol	459.93	Calculated Property
ΔvapH	14.18	kJ/mol	483.07	Calculated Property
ΔvapH	0.14	kJ/mol	506.20	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[278.50; 374.62]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.44210e+01
Coefficient B			-2.46322e+03
Coefficient C			-1.04219e+02
Temperature range, min.			278.50
Temperature range, max.			374.62
Pvap	1.33	kPa	278.50	Calculated Property
Pvap	3.01	kPa	289.18	Calculated Property
Pvap	6.24	kPa	299.86	Calculated Property
Pvap	11.97	kPa	310.54	Calculated Property
Pvap	21.54	kPa	321.22	Calculated Property
Pvap	36.68	kPa	331.90	Calculated Property
Pvap	59.56	kPa	342.58	Calculated Property
Pvap	92.77	kPa	353.26	Calculated Property
Pvap	139.33	kPa	363.94	Calculated Property
Pvap	202.65	kPa	374.62	Calculated Property
Pvap	[0.14; 3973.00]	kPa	[252.75; 498.94]	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			1.89990e+02
Coefficient B			-1.24398e+04
Coefficient C			-2.60311e+01
Coefficient D			1.98743e-05
Coefficient E			2.00000e+00
Comment			Range stopped where the equation exceeds Pc; ChemSep gives it to 506.2 K.
Temperature range, min.			252.75
Temperature range, max.			498.94
Pvap	0.14	kPa	252.75	Calculated Property
Pvap	1.57	kPa	280.10	Calculated Property
Pvap	9.91	kPa	307.46	Calculated Property
Pvap	41.67	kPa	334.81	Calculated Property
Pvap	130.41	kPa	362.17	Calculated Property
Pvap	328.99	kPa	389.52	Calculated Property
Pvap	708.59	kPa	416.88	Calculated Property
Pvap	1359.01	kPa	444.23	Calculated Property
Pvap	2395.17	kPa	471.58	Calculated Property
Pvap	3973.00	kPa	498.94	Calculated Property
Pvap	[4.06; 4016.87]	kPa	[293.00; 506.20]	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			9.13446e+01
Coefficient B			-8.70216e+03
Coefficient C			-1.06233e+01
Coefficient D			1.15210e-06
Coefficient E			0.00000e+00
Temperature range, min.			293.00
Temperature range, max.			506.20
Pvap	4.06	kPa	293.00	Calculated Property
Pvap	16.67	kPa	316.69	Calculated Property
Pvap	53.39	kPa	340.38	Calculated Property
Pvap	140.56	kPa	364.07	Calculated Property
Pvap	316.31	kPa	387.76	Calculated Property
Pvap	626.86	kPa	411.44	Calculated Property
Pvap	1119.44	kPa	435.13	Calculated Property
Pvap	1834.21	kPa	458.82	Calculated Property
Pvap	2797.34	kPa	482.51	Calculated Property
Pvap	4016.87	kPa	506.20	Calculated Property
Pvap	[13.39; 101.70]	kPa	[312.66; 355.56]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.49616e+01
Coefficient B			-2.70524e+03
Coefficient C			-9.39200e+01
Reference			Brown, Fock, et al., 1969
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			312.66
Temperature range, max.			355.56
Pvap	13.39	kPa	312.66	Calculated Property
Pvap	17.43	kPa	317.43	Calculated Property
Pvap	22.44	kPa	322.19	Calculated Property
Pvap	28.59	kPa	326.96	Calculated Property
Pvap	36.08	kPa	331.73	Calculated Property
Pvap	45.12	kPa	336.49	Calculated Property
Pvap	55.94	kPa	341.26	Calculated Property
Pvap	68.79	kPa	346.03	Calculated Property
Pvap	83.95	kPa	350.79	Calculated Property
Pvap	101.70	kPa	355.56	Calculated Property
Pvap	[216.75; 3959.38]	kPa	[376.42; 506.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.44230e+01
Coefficient B			-2.47661e+03
Coefficient C			-1.02588e+02
Reference			Ambrose and Townsend, 1963, 3
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			376.42
Temperature range, max.			506.00
Pvap	216.75	kPa	376.42	Calculated Property
Pvap	340.53	kPa	390.82	Calculated Property
Pvap	512.51	kPa	405.22	Calculated Property
Pvap	743.21	kPa	419.61	Calculated Property
Pvap	1043.51	kPa	434.01	Calculated Property
Pvap	1424.34	kPa	448.41	Calculated Property
Pvap	1896.39	kPa	462.81	Calculated Property
Pvap	2469.93	kPa	477.20	Calculated Property
Pvap	3154.63	kPa	491.60	Calculated Property
Pvap	3959.38	kPa	506.00	Calculated Property
Pvap	[34.24; 135.27]	kPa	[330.60; 363.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.51815e+01
Coefficient B			-2.82216e+03
Coefficient C			-8.83160e+01
Reference			Beynon and McKetta, 1963
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			330.60
Temperature range, max.			363.00
Pvap	34.24	kPa	330.60	Calculated Property
Pvap	40.60	kPa	334.20	Calculated Property
Pvap	47.92	kPa	337.80	Calculated Property
Pvap	56.28	kPa	341.40	Calculated Property
Pvap	65.81	kPa	345.00	Calculated Property
Pvap	76.62	kPa	348.60	Calculated Property
Pvap	88.83	kPa	352.20	Calculated Property
Pvap	102.59	kPa	355.80	Calculated Property
Pvap	118.02	kPa	359.40	Calculated Property
Pvap	135.27	kPa	363.00	Calculated Property
Pvap	[40.05; 133.53]	kPa	[333.93; 362.71]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.45813e+01
Coefficient B			-2.52152e+03
Coefficient C			-1.02409e+02
Reference			Biddiscombe, Collerson, et al., 1963
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			333.93
Temperature range, max.			362.71
Pvap	40.05	kPa	333.93	Calculated Property
Pvap	46.46	kPa	337.13	Calculated Property
Pvap	53.68	kPa	340.33	Calculated Property
Pvap	61.78	kPa	343.52	Calculated Property
Pvap	70.84	kPa	346.72	Calculated Property
Pvap	80.94	kPa	349.92	Calculated Property
Pvap	92.17	kPa	353.12	Calculated Property
Pvap	104.62	kPa	356.31	Calculated Property
Pvap	118.38	kPa	359.51	Calculated Property
Pvap	133.53	kPa	362.71	Calculated Property
Pvap	[216.75; 3959.38]	kPa	[376.42; 506.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.44230e+01
Coefficient B			-2.47661e+03
Coefficient C			-1.02588e+02
Reference			Ambrose and Townsend, 1963
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			376.42
Temperature range, max.			506.00
Pvap	216.75	kPa	376.42	Calculated Property
Pvap	340.53	kPa	390.82	Calculated Property
Pvap	512.51	kPa	405.22	Calculated Property
Pvap	743.21	kPa	419.61	Calculated Property
Pvap	1043.51	kPa	434.01	Calculated Property
Pvap	1424.34	kPa	448.41	Calculated Property
Pvap	1896.39	kPa	462.81	Calculated Property
Pvap	2469.93	kPa	477.20	Calculated Property
Pvap	3154.63	kPa	491.60	Calculated Property
Pvap	3959.38	kPa	506.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[791.75; 332.95]	kg/m3	[293.15; 506.21]	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			3.02698e+01
Coefficient B			1.70340e-01
Coefficient C			5.08880e+02
Coefficient D			1.97400e-01
Comment			Range stopped at Tc; ChemSep gives it to 508.87 K.
Temperature range, min.			293.15
Temperature range, max.			506.21
ρl	791.75	kg/m3	293.15	Calculated Property
ρl	765.37	kg/m3	316.82	Calculated Property
ρl	737.25	kg/m3	340.50	Calculated Property
ρl	706.98	kg/m3	364.17	Calculated Property
ρl	673.95	kg/m3	387.84	Calculated Property
ρl	637.21	kg/m3	411.52	Calculated Property
ρl	595.12	kg/m3	435.19	Calculated Property
ρl	544.44	kg/m3	458.86	Calculated Property
ρl	476.59	kg/m3	482.54	Calculated Property
ρl	332.95	kg/m3	506.21	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.02; 0.01]	N/m	[288.15; 355.57]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			2.55890e-03
Coefficient B			-1.09820e+03
Coefficient C			4.09530e+00
Coefficient D			-1.40960e-02
Coefficient E			-3.15610e-06
Temperature range, min.			288.15
Temperature range, max.			355.57
γ	0.02	N/m	288.15	Calculated Property
γ	0.02	N/m	295.64	Calculated Property
γ	0.02	N/m	303.13	Calculated Property
γ	0.02	N/m	310.62	Calculated Property
γ	0.02	N/m	318.11	Calculated Property
γ	0.02	N/m	325.61	Calculated Property
γ	0.02	N/m	333.10	Calculated Property
γ	0.02	N/m	340.59	Calculated Property
γ	0.02	N/m	348.08	Calculated Property
γ	0.01	N/m	355.57	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.07]	W/m×K	[255.93; 766.87]	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			4.23650e-07
Coefficient B			1.79290e+00
Coefficient C			-1.30930e+02
Coefficient D			1.79890e+04
Temperature range, min.			255.93
Temperature range, max.			766.87
λgas	0.01	W/m×K	255.93	Calculated Property
λgas	0.02	W/m×K	312.70	Calculated Property
λgas	0.02	W/m×K	369.47	Calculated Property
λgas	0.03	W/m×K	426.24	Calculated Property
λgas	0.03	W/m×K	483.01	Calculated Property
λgas	0.04	W/m×K	539.78	Calculated Property
λgas	0.05	W/m×K	596.56	Calculated Property
λgas	0.06	W/m×K	653.33	Calculated Property
λgas	0.06	W/m×K	710.10	Calculated Property
λgas	0.07	W/m×K	766.87	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.12; 0.09]	W/m×K	[298.97; 404.96]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			5.69470e-03
Coefficient B			3.58710e+02
Coefficient C			-5.57740e+00
Coefficient D			1.29130e-02
Coefficient E			-1.82730e-05
Temperature range, min.			298.97
Temperature range, max.			404.96
λliquid	0.12	W/m×K	298.97	Calculated Property
λliquid	0.12	W/m×K	310.75	Calculated Property
λliquid	0.12	W/m×K	322.52	Calculated Property
λliquid	0.11	W/m×K	334.30	Calculated Property
λliquid	0.11	W/m×K	346.08	Calculated Property
λliquid	0.11	W/m×K	357.85	Calculated Property
λliquid	0.10	W/m×K	369.63	Calculated Property
λliquid	0.10	W/m×K	381.41	Calculated Property
λliquid	0.10	W/m×K	393.18	Calculated Property
λliquid	0.09	W/m×K	404.96	Calculated Property

Similar Compounds

Find more compounds similar to 2-Propanol, 2-methyl-.

Mixtures

• 2-Propanol, 2-methyl- + Butane
• 2-Propanol, 2-methyl- + Ethanol + Cyclohexane, methyl-
• 2-Propanol, 2-methyl- + Pentane, 2,2,4-trimethyl-
• 2-Propanol, 2-methyl- + Benzene, nitro-
• 2-Propanol, 2-methyl- + 1,3-Dioxolane
• 2-Propanol, 2-methyl- + 1,4-Dioxane
• 2-Propanol, 2-methyl- + Water
• 2-Propanol, 2-methyl- + 1,3-Dioxolane + Water
• 2-Propanol, 2-methyl- + Dimethyl Sulfoxide
• 2-Propanol, 2-methyl- + Glycerin
• 2-Propanol, 2-methyl- + Dimethyl Sulfoxide + Water
• 2-Propanol, 2-methyl- + Acetonitrile
• 2-Propanol, 2-methyl- + Phenol, 3-methyl-
• 2-Propanol, 2-methyl- + 2-Butene, (Z)-
• 2-Propanol, 2-methyl- + Dimethyl ether
• 2-Propanol, 2-methyl- + Ethyl Chloride
• 2-Propanol, 2-methyl- + Ethane, 1,1-difluoro-
• 2-Propanol, 2-methyl- + Diosgenin
• 2-Propanol, 2-methyl- + Tromethamine + Water
• 2-Propanol, 2-methyl- + Phenol, 3-chloro-

Find more mixtures with 2-Propanol, 2-methyl-.

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.
• 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
• Crippen Method
• Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
• Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
• Isobaric vapor-liquid equilibria for the binary systems isobutyl alcohol + isobutyl acetate and tert-butyl alcohol + tert-butyl acetate at 20 and 101.3 kPa
• Vapour liquid equilibrium for the 2-methylpropane + methanol, +ethanol, +2-propanol, +2-butanol and +2-methyl-2-propanol systems at 313.15K
• Isobaric vapor liquid phase equilibria for the binary systems of tert-butanol + 2-ethyl-1-hexanol and n-butanol + 2-ethyl-1-hexanol
• Solid liquid equilibria of mixtures containing tert-butanol, m-chlorophenol, and p-chlorophenol and development of adductive crystallization processes
• Viscous synergy and antagonism and isentropic compressibility of ternary mixtures containing 1,3-dioxolane, water and monoalkanols at 303.15K
• Activity coefficients of the binary mixtures of a-cresol or p-cresol with C l-C4 aliphatic alcohols near ambient pressure
• Experimental and statistical mechanical studies of heats of dilution of alkanols in pyridine derivatives based on ab initio calculations of hydrogen bonding energies
• Excess Gibbs energies of selected binary mixtures formed by N,N-dimethyl formamide at 95.5 kPa
• Excess volumes and excess enthalpies of N-methyl-2-pyrrolidone with branched alcohols
• Vapour liquid equilibrium for the systems butane + methanol, +2-propanol, +1-butanol, +2-butanol, +2-methyl-2-propanol at 364.5K
• Isobaric vapor liquid equilibrium for ternary mixtures of ethanol and methylcyclohexane with 3-methylpentane and tert-butyl alcohol at 101.3 kPa
• Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
• Measurement and correlation of binary vapor liquid equilibria of isomeric butanols with 1,4-dioxane
• Solubilities of cinnamic acid esters in binary mixtures of ionic liquids and organic solvents
• Viscosity of the binary systems 2-methyl-2-propanol with n-alkanes at T = (303.15, 308.15, 313.15, 318.15 and 323.15) K: Prediction and correlation - New UNIFAC-VISCO interaction parameters
• Experimental study of the isochoric heat capacity of tert-butanol in the critical and supercritical regions
• Thermodynamic study of aqueous two phase systems for some aliphatic alcohols + sodium thiosulfate + water
• Liquid liquid equilibrium of 1-propanol, 2-propanol, 2-methyl-2-propanol or 2-butanol + sodium sulfite + water aqueous two phase systems
• Solubility of chlocyphos in different solvents
• The study of phase behavior of aqueous 1-propanol/2-propanol/2-butanol/2-methyl-2-propanol systems in the presence of disodium tartrate or disodium succinate at T = 298.15 K
• Volumetric behavior of carbon dioxide + 2-methyl-1-propanol and carbondioxide + 2-methyl-2-propanol mixtures at 313.15 K
• The effect of temperature on the liquid-liquid equilibria of somealiphatic alcohols + di-sodium hydrogen citrate + water systems: Experimental and correlation
• Vapor-liquid equilibria of binary systems composed of polyoxyethylene 4-octylphenyl ether and alcohols: Experimental measurements and correlation
• Liquid-liquid equilibria of 1-octyl-3-methylimidazolium hexafluorophosphate with 1-propanol or tert-butanol in the critical region
• Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
• Liquid-liquid equilibrium for the ternary system water + 2-methyl-1-propanol + butyl acetate and water + 2-methyl-2-propanol + butyl acetate at (298.15 and 323.15) K
• Mesoscale solubilization and critical phenomena in binary and quasi-binary solutions of hydrotropes
• Solubility of diazepam in water + tert-butyl alcohol solvent mixtures: Part 1. Experimental data and thermodynamic analysis
• Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
• Excess specific volume of water + tert-butyl alcohol solvent mixtures: Experimental data, modeling and derived excess partial specific thermodynamic quantities.
• Evaluation of the solvent structural effect upon the vapor-liquid equilibrium of [C4C1im][Cl] + Alcohols
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Solubility and dissolution characteristics of capecitabine in pure lower alcohols and water with methanol mixture solvents at atmospheric pressure and different temperatures
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• Measurement and correlation of aqueous biphasic systems composed of alcohol (1-propanol/ 2-propanol/tert-butanol) + (NH4)2SO4 + H2O at 298 K and a textile dye partition.
• New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Isobaric vapor-liquid equilibria for tert-butanol + water with single and mixed ionic liquids as solvents at 101.3 kPa
• (Vapour + liquid) equilibrium of binary mixtures (1,3-dioxolane or 1,4-dioxane + 2-methyl-1-propanol or 2-methyl-2-propanol) at isobaric conditions
• (Liquid + liquid) phase behavior for systems containing (aromatic + TBA + methylcyclohexane)
• Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in isobutanol and tert-butanol
• Densities and speeds of sound for binary mixtures of (1,3-dioxolane or 1,4-dioxane) with (2-methyl-1-propanol or 2-methyl-2-propanol) at the temperatures 298.15 K and 313.15 K
• Dielectric study of molecular association in the binary mixtures (2-ethyl-1-hexanol + alcohol) and (cyclohexane + alcohol) at 298.2 K
• Salt effect on (liquid + liquid) equilibrium of (water + tertbutanol + 1-butanol) system: Experimental data and correlation
• (Vapor + liquid) equilibria of binary mixtures formed by iso-octane with a variety of compounds at 95.8 kPa
• Partial molar volumes of organic solutes in water. XIII. Butanols (aq) at temperatures T = 298 K to 573 K and at pressures up to 30 MPa
• Excess molar enthalpies of dimethyl carbonate and (butanol isomers and 1-pentanol) at T = (298.15, 313.15, and 328.15) K and p = (0.1, 1.0, and 10.0) MPa
• 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
• Bubble point temperatures of the binary mixtures of nitrobenzene with C1 C4 aliphatic alcohols at 94.95 kPa
• Adiabatic compressibility of pseudo-binary aqueous solutions of tert-butyl alcohol and dimethylsulfoxide as a result of ultrasonic investigations
• (Vapor + liquid) equilibria of the binary mixtures of m-cresol with C1 C4 aliphatic alcohols at 95.5 kPa
• Excess Gibbs free energies of the binary mixtures of acetonitrile with butanols at 94.83 kPa
• Enthalpies of solution of 1,1,3,3-tetramethylurea in normal and branched alkanols (C2 C4) at 298.15 K
• Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
• Solubility and Stability of Nesquehonite (MgCO3 *3H2O) in NaCl, KCl, MgCl2, and NH4Cl Solutions
• Isobaric (vapour + liquid) equilibrium for N-methyl-2-pyrrolidone with branched alcohols
• (Liquid + liquid) equilibrium of {water + phenol + (1-butanol, or 2-butanol, or tert-butanol)} systems
• Densities and volume properties of (water + tert-butanol) over the temperature range of (274.15 to 348.15) K at pressure of 0.1 MPa
• Experimental and predicted refractive index properties in ternary mixtures of associated liquids
• The buffering-out effect and phase separation in aqueous solutions of EPPS buffer with 1-propanol, 2-propanol, or 2-methyl-2-propanol at T = 298.15 K
• Solubilities of some organic solutes in 1-ethyl-3-methylimidazolium acetate. Chromatographic measurements and predictions from COSMO-RS
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
• Determination and correlation of the solubility for diosgenin in alcohols solvents
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
• Thermodynamic investigation of the ATPSs composed of some (aliphatic alcohol + sodium carbonate + water) ternary systems
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
• Liquid phase PVTx properties of (water + tert-butanol) binary mixtures at temperatures from 278.15 to 323.15 K and pressures from 0.1 to 100 MPa. I. Experimental results, excess and partial molar volumes
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
• Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Equilibrium surface tension and the interaction energy of DMSO with tert-butyl alcohol or iso-amyl alcohol at various temperatures
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Isobaric vapour-liquid equilibrium of (tert-butanol + water) system with biological buffer TRIS at 101.3 kPa
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• Experimental and modeling vapor-liquid equilibrium for the binary systems {ethanol(1) + glycerol(2)} and {tert-butanol(1) + glycerol(2)} at high pressures
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
• Isobaric vapor-liquid equilibria for the extractive distillation of tert-butyl alcohol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
• Solution enthalpies of 1-bromoadamantane in monoalcohols at 298.15K
• Effect of intramolecular cyclization on the enthalpies of solvation of tetramethylurea in water and alkanols at 298.15K
• Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
• Solvation of benzene and its simple mono derivatives in water-tertiary butanol mixtures
• Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
• Experimental and theoretical excess molar properties of imidazolium based ionic liquids with isomers of butanol
• Measurement and Correlation of the Solubility of Antioxidant 626 in Alcohols
• Measurements of Infinite Dilution Activity Coefficients of Alkanols in the Ionic Liquid Tributylmethylammonium Methyl Sulfate Using HS-SPME/GC/FID
• P-rho-T Data for 2-Butanol and tert-Butanol from (283.15 to 363.15) K and (303.15 to 363.15) at pressures up to 66 MPa
• Isobaric Phase Equilibrium of tert-Butyl Alcohol + Glycerol at Local and Subatmospheric Pressures, Volumetric Properties, and Molar Refractivity from 303.15 to 333.15 K of tert-Butyl Alcohol + Glycerol, tert-Butyl Alcohol + Water, and Water + Glycerol Binary Systems
• Liquid Liquid Equilibria, Equilibrium Phase Densities, and Refractive Indices for the Quaternary Mixtures Containing 2-Propanol or 2-Methyl-2-Propanol of Fuel Oxygenate at T = 298.15 and 318.15 K
• Isobaric Vapor Liquid Equilibrium for the Binary Systems of sec-Butyl Acetate + n-Butyl Alcohol, Isobutyl Alcohol, or tert-Butyl Alcohol at 101.3 kPa
• Determination of Ternary Liquid Liquid Equilibria for Dimethyl Carbonate + 2-Methyl-1-propanol or 2-Methyl-2-propanol + Water Systems at T = 303.15 and 313.15 K
• Phase Separation of Alcohol (1-Propanol, 2-Propanol, or tert-Butanol) from Its Aqueous Solution in the Presence of Biological Buffer MOPS
• Isobaric Vapor-Liquid Equilibrium for Binary and Ternary Systems of tert-Butanol + tert-Butyl Acetate + Chlorobenzene at 101.33 kPa
• Equilibrium Diagrams of Water + NaCl or KCl + 2-Methyl 2-Propanol at the Boiling Temperature and 101.3 kPa
• Isobaric Vapor-Liquid Equilibria and Excess Quantities for Binary Mixtures of an Ethyl Ester + tert-Butanol and a New Approach to VLE Data Processing
• High-Pressure Vapor-Liquid Equilibria for CO2 + 2-Butanol, CO2 + iso-Butanol and CO2 + tert-Butanol Systems
• Solubility of Benzimidazoles in Alcohols
• Excess Molar Volumes and Surface Tensions of Xylene with 2-propanol or 2-methyl-2-propanol at 298.15 K
• Bubble Temperatures of the Binary Mixtures of Dimethylcarbonate with Some Alcohols at 95.8 kPa
• 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
• Viscosities of Binary Mixtures of Isomeric Butanols or Isomeric Chlorobutanes with 2-Methyltetrahydrofuran
• Isothermal Vapor-Liquid Equilibria for Binary Mixtures Composed of the Closely Boiling Compounds 1,2-Dimethoxybenzene and 2-Methoxyphenol with an Adducted Agent: tert-Butanol or Morpholine
• Thermodynamic Functions for Transfer of Anthracene from Water to (Water + Alcohol) Mixtures at 298.15K
• Vapor Liquid Equilibrium for the Trans-2-Butene + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol and + 2-Methyl-2-Propanol Systems at 332 K
• Isothermal Vapor Liquid Equilibrium for Binary 2-Methylpropene - C1-C4 Alcohol-Systems
• Excess Properties and Isobaric Vapor-Liquid Equilibria for Binary Mixtures of Methyl Esters + tert-Butanol
• Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
• Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
• 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
• Excess Molar Volumes and Surface Tensions of 1,2,4-Trimethylbenzene and 1,3,5-Trimethylbenzene with 1-Butanol, 2-Methyl-1-propanol, 2-Butanol, and 2-Methyl-2-propanol at 298.15 K
• Solubility of Cesium Nitrate in Alcohol Aqueous Solutions at (25, 35 and 45 ) C
• Phase Diagrams of Some Aliphatic Alcohols + Potassium or Sodium Citrate + Water at 25 deg C
• Densities and Viscosities of Binary Mixtures of 1-Bromobutane with Butanol Isomers at Several Temperatures
• Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Ethanol, 2-Methylpropan-2-ol, and 2,2,4-Trimethylpentane
• Experimental and Predicted Results of Anomeric Equilibrium of Glucose in Alcohols
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
• Isothermal Vapor Liquid Equilibrium for 2-Methylpropene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol Binary Systems at 364.5 K
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
• Temperature Effect on the Liquid-Liquid Equilibria for Some Aliphatic Alcohols + Water + K2CO3 Systems
• Correlation and Prediction of Excess Quantities and Vapor-Liquid Equilibria of Alkyl Esters + tert-Butyl Alcohol: Experimental Data for Propyl Esters + tert-Butyl Alcohol
• Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
• Vapor-Liquid Equilibrium for Benzaldehyde with 1-Methylethylbenzene and for 2-Methyl-propan-2-ol with 2,4,4-Trimethyl-1-pentene
• Surface Tensions of the Ternary Mixtures Containing an Isomeric Butanol + n-Hexane + 1-Chlorobutane at 298.15 K
• Experimental Determination of Densities and Refractive Indices of the Ternary Mixture 2-Methyl-2-propanol + Cyclohexylamine + n-Heptane at T = (303.15 to 323.15) K
• Isobaric Vapor Liquid Equilibrium Data for the Binary Mixtures 2-Methyl Propan-2-ol with Tetraethoxysilane and 1-Phenyl Ethanone at 95.5 kPa
• Binodal Curves and Tie-Lines of Aliphatic Alcohols + Diammonium Hydrogen Citrate + Water Ternary Systems: Measurement and Modeling
• Liquid Liquid Equilibrium of Some Aliphatic Alcohols + Disodium Tartrate + Water Aqueous Two-Phase Systems at 298.15 K
• Isobaric Vapor Liquid Equilibrium Data of 2-Methyl-propan-2-ol (1) + Heptan-1-ol (2), Methanol (1) + Heptan-1-ol (2), Ethanol (1) + Heptan-1-ol (2), and Propan-1-ol (1) + Heptan-1-ol (2) at 96.5 kPa
• Static Permittivities of Isomeric Butanol Mixtures at Temperatures from (288.15 to 308.15) K
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Liquid Liquid Equilibrium for the Ternary System 2-Methyl-2-propanol + 1-Pentanol + Water at T = (303.15, 328.15, and 353.15) K
• Experimental Vapor Liquid Equilibria for the Systems {2-Ethyl-1-hexanol + Glycerol + CO2} and {2-Methyl-2-propanol + Glycerol + CO2}
• Densities and Viscosities of Binary Mixtures of 2-Butanol + Isobutanol, 2-Butanol + tert-Butanol, and Isobutanol + tert-Butanol from (308.15 to 343.15) K
• Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
• Isobaric Vapor Liquid Equilibrium of tert-Butyl Alcohol + Water + Triethanolamine-Based Ionic Liquid Ternary Systems at 101.3 kPa
• Temperature Dependence of Limiting Activity Coefficients, Henry s Law Constants, and Related Infinite Dilution Properties of Branched (C3 and C4) Alkanols in Water. Measurement, Critical Compilation, Correlation, and Recommended Data
• Vapor-Liquid Equilibrium and Excess Gibbs Energies of Hexane + N,N-Dimethyl Formamide, 2-Methylpropan-2-ol + 2-Aminophenol, N,N-Dimethyl Formamide, and 2-Propanol + Diisopropyl Amine at 94.4 kPa
• Excess Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 2-Methyl-1-propanol or 2-Methyl-2-propanol at Several Temperatures
• Vapor Liquid Equilibrium for Butane + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-Propanol (TBA) at 323 K
• Liquid Liquid Equilibria for the Ternary System Water + Methyl Isobutyl Ketone + tert-Butyl Alcohol at Several Temperatures
• Vapor Liquid Equilibrium for the Systems trans-2-Butene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol at 364.5 K
• Vapor Liquid Equilibrium for the Systems 2-Methylpropane + Methanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol at 364.5 K
• Densities and Viscosities of the Ternary Mixtures 2-Methyl-1-propanol (or 2-Methyl-2-propanol) + N-Hexane + 1-Chlorobutane at 298.15 K
• Vapor-Liquid Equilibrium for the cis-2-Butene + Methanol, + 2-Propanol, + 2-Butanol, + 2-Methyl-2-propanol Systems at 364.5 K
• Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
• Vapor-Liquid Equilibrium for 1-Butene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and 2-Methyl-2-propanol (TBA) at 364.5 K
• Activity Coefficients at Infinite Dilution of Alkanols in the Ionic Liquids 1-Butyl-3-methylimidazolium Hexafluorophosphate, 1-Butyl-3-methylimidazolium Methyl Sulfate, and 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Amide Using the Dilutor Technique
• Liquid-Liquid Equilibria in Ternary Systems 2-Methylbutane + 2-Methyl-2-propanol + Water and Pentane + 2-Methyl-2-propanol + Water at 293.15 K
• Viscosity of Water + tert-Butyl Alcohol (2-Methyl-2-propanol) Mixtures at Low Temperatures and High Pressure
• Unusual S-Shaped Binodal Curves of the System Water + Lithium Chloride + 2-Methyl-2-propanol
• Dielectric Properties of Methanol Mixtures with Ethanol, Isomers of Propanol, and Butanol
• Densities, Viscosities, and Excess Molar Enthalpies of 2-Pyrrolidone + Butanol Isomers at T ) (293.15, 298.15, and 303.15) K
• Isothermal Vapor-Liquid Equilibrium of Ternary Mixtures Containing 2-Methyl-1-propanol or 2-Methyl-2-propanol, n-Hexane, and 1-Chlorobutane at 298.15 K
• Solubilities of Cinnamic Acid Esters in Organic Solvents
• Densities and Viscosities of Binary Mixtures of n-Butanol with 2-Butanol, Isobutanol, and tert-Butanol from (303.15 to 343.15) K
• Liquid-Liquid Equilibria for Aliphatic Alcohols + Dipotassium Oxalate + Water
• Isothermal Vapor-Liquid Equilibria in the Two Binary and the Ternary Systems Composed of tert-Amyl Methyl Ether, tert-Butanol, and Isooctane
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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