Chemical Properties of Nonane (CAS 111-84-2)

InChI

InChI=1S/C9H20/c1-3-5-7-9-8-6-4-2/h3-9H2,1-2H3

InChI Key

BKIMMITUMNQMOS-UHFFFAOYSA-N

Formula

C9H20

SMILES

CCCCCCCCC

Molecular Weight¹

128.26

CAS

111-84-2

Other Names

• Shellsol 140
• UN 1920
• n-C9H20
• n-nonane

• ω : Acentric Factor.
• T_ig : Autoignition Temperature (K).
• α_p : Isobaric thermal expansion coefficient (1/K).
• AP : Aniline Point (K).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• 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,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_c,grossH : Heat of Combustion, Gross form (kJ/mol).
• Δ_c,netH : Heat of Combustion, Net Form (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_subH : Enthalpy of sublimation at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• P_c : Critical Pressure (kPa).
• P_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.
• S°_gas : Molar entropy at standard conditions (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).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• 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	0.4450		KDB
Tig	478.15	K	KDB
AP	346.850	K	KDB
ΔcH°liquid	[-6125.21; -6119.80]	kJ/mol
ΔcH°liquid	-6125.21 ± 0.54	kJ/mol	NIST
ΔcH°liquid	-6124.90 ± 1.10	kJ/mol	NIST
ΔcH°liquid	-6119.80	kJ/mol	NIST
LFL	0.87	% in Air	KDB
UFL	2.90	% in Air	KDB
Tflash,oc	304.26	K	KDB
ΔfG°	24.83	kJ/mol	KDB
Δc,grossH	6125.17	kJ/mol	KDB
Δc,netH	5685.052	kJ/mol	KDB
ΔfH°gas	[-229.20; -228.30]	kJ/mol
ΔfH°gas	-229.20	kJ/mol	KDB
ΔfH°gas	-228.30	kJ/mol	NIST
ΔfH°liquid	-274.70 ± 1.00	kJ/mol	NIST
ΔfusH°	19.07	kJ/mol	Joback Calculated Property
ΔvapH°	[46.40; 46.60]	kJ/mol
ΔvapH°	46.43	kJ/mol	NIST
ΔvapH°	46.50 ± 0.20	kJ/mol	NIST
ΔvapH°	46.60 ± 0.20	kJ/mol	NIST
ΔvapH°	46.60	kJ/mol	NIST
ΔvapH°	46.40	kJ/mol	NIST
ΔvapH°	46.40	kJ/mol	NIST
ΔvapH°	46.43	kJ/mol	NIST
IE	[9.63; 10.19]	eV
IE	9.71 ± 0.10	eV	NIST
IE	9.87	eV	NIST
IE	9.71 ± 0.10	eV	NIST
IE	9.63 ± 0.15	eV	NIST
IE	10.19	eV	NIST
log10WS	[-5.88; -5.88]
log10WS	-5.88		Aq. Solubility Prediction
log10WS	-5.88		Estimated Solubility
logPoct/wat	3.757		Crippen Calculated Property
McVol	137.670	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
Pc	[2270.00; 2357.30]	kPa
Pc	2290.00	kPa	KDB
Pc	2290.00 ± 50.00	kPa	NIST
Pc	2280.00 ± 20.00	kPa	NIST
Pc	2299.00 ± 5.00	kPa	NIST
Pc	2270.00 ± 30.00	kPa	NIST
Pc	2291.10 ± 0.22	kPa	NIST
Pc	2290.40 ± 0.22	kPa	NIST
Pc	2305.60 ± 0.23	kPa	NIST
Pc	Outlier 2357.30 ± 0.23	kPa	NIST
Pc	2294.00 ± 6.89	kPa	NIST
Pc	2288.00 ± 10.00	kPa	NIST
ρc	[230.86; 235.99]	kg/m3
ρc	230.86 ± 6.41	kg/m3	NIST
ρc	235.99 ± 10.00	kg/m3	NIST
ρc	230.86 ± 6.41	kg/m3	NIST
Inp	[138.27; 144.03]
Inp	138.27		NIST
Inp	144.03		NIST
Inp	138.27		NIST
S°gas	506.50 ± 1.00	J/mol×K	NIST
S°liquid	[392.90; 393.67]	J/mol×K
S°liquid	393.67	J/mol×K	NIST
S°liquid	392.90	J/mol×K	NIST
Tboil	[421.15; 424.15]	K
Tboil	423.80	K	Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
Tboil	423.80	K	Isobaric vapor-liquid equilibrium for binary systemsof toluene + o-xylene, benzene + o-xylene, nonane + benzene and nonane + heptane at 101.3 kPa
Tboil	423.94	K	Solutions of alkyl methanoates and alkanes: Simultaneous modeling of phase equilibria and mixing properties. Estimation of behavior by UNIFAC with recalculation of parameters
Tboil	423.66	K	Densities and Excess Molar Properties of Dimethyl Carbonate with Alkanes (C6 to C10) and VLE of Dimethyl Carbonate with Alkanes (C9 to C10) at 101.3 kPa
Tboil	423.97	K	Isobaric Vapor-Liquid Equilibria of the Ternary System Methylbutyl Ketone + Nonane + Cyclohexanol
Tboil	423.94	K	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Tboil	423.97	K	KDB
Tboil	424.00	K	NIST
Tboil	424.00	K	NIST
Tboil	423.82 ± 0.25	K	NIST
Tboil	423.88 ± 0.50	K	NIST
Tboil	424.15 ± 0.20	K	NIST
Tboil	423.90 ± 0.50	K	NIST
Tboil	423.54 ± 0.50	K	NIST
Tboil	423.20 ± 2.00	K	NIST
Tboil	423.75 ± 0.30	K	NIST
Tboil	423.91 ± 0.15	K	NIST
Tboil	423.45 ± 0.40	K	NIST
Tboil	423.45 ± 0.17	K	NIST
Tboil	423.85 ± 0.20	K	NIST
Tboil	423.45 ± 0.25	K	NIST
Tboil	423.95 ± 0.15	K	NIST
Tboil	423.65 ± 0.25	K	NIST
Tboil	423.95 ± 0.30	K	NIST
Tboil	Outlier 421.65 ± 1.50	K	NIST
Tboil	423.75 ± 0.50	K	NIST
Tboil	423.80 ± 0.60	K	NIST
Tboil	423.80 ± 0.20	K	NIST
Tboil	423.80 ± 0.20	K	NIST
Tboil	422.95 ± 0.50	K	NIST
Tboil	423.92 ± 0.15	K	NIST
Tboil	423.86 ± 0.50	K	NIST
Tboil	423.90 ± 0.30	K	NIST
Tboil	423.94 ± 0.03	K	NIST
Tboil	423.05 ± 1.00	K	NIST
Tboil	423.96 ± 0.30	K	NIST
Tboil	423.95 ± 0.30	K	NIST
Tboil	423.94 ± 0.01	K	NIST
Tboil	424.00 ± 0.15	K	NIST
Tboil	424.00 ± 2.00	K	NIST
Tboil	423.65 ± 2.00	K	NIST
Tboil	424.00 ± 0.20	K	NIST
Tboil	423.95 ± 0.10	K	NIST
Tboil	423.85 ± 0.60	K	NIST
Tboil	423.85 ± 0.30	K	NIST
Tboil	423.96 ± 0.20	K	NIST
Tboil	423.40 ± 0.70	K	NIST
Tboil	423.85 ± 0.30	K	NIST
Tboil	423.70 ± 0.50	K	NIST
Tboil	423.87 ± 0.10	K	NIST
Tboil	423.86 ± 0.15	K	NIST
Tboil	423.88 ± 0.10	K	NIST
Tboil	423.86 ± 0.15	K	NIST
Tboil	423.87 ± 0.10	K	NIST
Tboil	Outlier 421.15 ± 3.00	K	NIST
Tboil	423.90 ± 2.00	K	NIST
Tboil	422.65 ± 0.70	K	NIST
Tboil	422.65 ± 1.00	K	NIST
Tc	[593.61; 595.85]	K
Tc	594.52	K	Experimental determination of critical data of multi-component mixtures containing potential gasoline additives 2-butanol by a flow-type apparatus
Tc	594.50	K	Measurement of Critical Properties for Binary and Ternary Mixtures Containing n-Butanol and n-Alkane
Tc	594.52	K	Determination of the Critical Properties of C6 C10 n-Alkanes and Their Binary Systems Using a Flow Apparatus
Tc	594.60	K	KDB
Tc	594.60 ± 0.60	K	NIST
Tc	594.60 ± 1.00	K	NIST
Tc	594.50 ± 0.30	K	NIST
Tc	594.70 ± 0.60	K	NIST
Tc	594.60	K	NIST
Tc	593.81 ± 0.10	K	NIST
Tc	594.60 ± 0.40	K	NIST
Tc	594.60	K	NIST
Tc	594.60 ± 0.70	K	NIST
Tc	593.61 ± 0.20	K	NIST
Tc	595.85 ± 0.05	K	NIST
Tc	595.85 ± 0.05	K	NIST
Tc	595.65 ± 0.05	K	NIST
Tc	595.75 ± 0.05	K	NIST
Tc	593.80 ± 0.30	K	NIST
Tc	594.56 ± 0.10	K	NIST
Tfus	[218.95; 220.15]	K
Tfus	219.60	K	KDB
Tfus	219.77	K	Aq. Solubility Prediction
Tfus	219.56 ± 0.02	K	NIST
Tfus	219.85 ± 0.15	K	NIST
Tfus	219.64 ± 0.20	K	NIST
Tfus	219.60 ± 0.20	K	NIST
Tfus	219.61 ± 0.08	K	NIST
Tfus	219.45 ± 0.20	K	NIST
Tfus	219.62 ± 0.08	K	NIST
Tfus	Outlier 218.95 ± 0.50	K	NIST
Tfus	Outlier 218.95 ± 0.60	K	NIST
Tfus	219.61 ± 0.02	K	NIST
Tfus	219.54 ± 0.01	K	NIST
Tfus	219.19 ± 0.20	K	NIST
Tfus	219.35 ± 0.40	K	NIST
Tfus	219.45 ± 0.40	K	NIST
Tfus	219.35 ± 0.20	K	NIST
Tfus	219.45 ± 0.20	K	NIST
Tfus	Outlier 220.15 ± 2.00	K	NIST
Tfus	219.45 ± 0.10	K	NIST
Tfus	219.20 ± 0.30	K	NIST
Tfus	219.25 ± 0.40	K	NIST
Tfus	219.47 ± 0.08	K	NIST
Tfus	219.50 ± 0.12	K	NIST
Tfus	219.39 ± 0.15	K	NIST
Tfus	219.45 ± 0.10	K	NIST
Ttriple	[219.20; 219.65]	K
Ttriple	219.65	K	KDB
Ttriple	219.65 ± 0.01	K	NIST
Ttriple	219.65 ± 0.03	K	NIST
Ttriple	219.65 ± 0.20	K	NIST
Ttriple	219.62 ± 0.20	K	NIST
Ttriple	219.62 ± 0.06	K	NIST
Ttriple	219.62 ± 0.03	K	NIST
Ttriple	Outlier 219.20 ± 0.20	K	NIST
Vc	[0.555; 0.555]	m3/kmol
Vc	0.555	m3/kmol	KDB
Vc	0.555	m3/kmol	NIST
Zc	0.2570790		KDB
Zra	0.25		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[264.50; 323.20]	J/mol×K	[230.00; 370.00]
Cp,liquid	264.50	J/mol×K	230.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	265.10	J/mol×K	240.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	266.90	J/mol×K	250.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	269.50	J/mol×K	260.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	272.90	J/mol×K	270.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	274.00	J/mol×K	273.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	276.70	J/mol×K	280.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	280.13	J/mol×K	288.15	Thermodynamic behaviour of the binary systems dimethyl carbonate + n-octane or n-nonane
Cp,liquid	280.90	J/mol×K	290.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	280.70	J/mol×K	297.90	NIST
Cp,liquid	284.34	J/mol×K	298.15	NIST
Cp,liquid	284.76	J/mol×K	298.15	NIST
Cp,liquid	284.00	J/mol×K	298.15	NIST
Cp,liquid	283.80	J/mol×K	298.15	NIST
Cp,liquid	284.40	J/mol×K	298.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	284.23	J/mol×K	298.15	Thermodynamic behaviour of the binary systems dimethyl carbonate + n-octane or n-nonane
Cp,liquid	284.01	J/mol×K	298.15	NIST
Cp,liquid	284.39	J/mol×K	298.15	NIST
Cp,liquid	281.20	J/mol×K	299.10	NIST
Cp,liquid	285.20	J/mol×K	300.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	288.80	J/mol×K	308.15	Thermodynamic behaviour of the binary systems dimethyl carbonate + n-octane or n-nonane
Cp,liquid	289.50	J/mol×K	310.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	292.18	J/mol×K	318.15	NIST
Cp,liquid	293.90	J/mol×K	320.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	293.20	J/mol×K	323.00	NIST
Cp,liquid	298.50	J/mol×K	330.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	303.60	J/mol×K	340.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	322.20	J/mol×K	350.00	NIST
Cp,liquid	309.30	J/mol×K	350.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	315.80	J/mol×K	360.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	323.20	J/mol×K	370.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
η	[0.0003460; 0.0009720]	Pa×s	[273.15; 358.15]
η	0.0009720	Pa×s	273.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η	0.0008960	Pa×s	278.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η	0.0008280	Pa×s	283.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η	0.0007680	Pa×s	288.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η	0.0007091	Pa×s	293.15	Densities and Viscosities of Ternary Mixtures of Heptane, Octane, Nonane, and Hexyl Benzene from 293.15 K to 313.15 K
η	0.0007160	Pa×s	293.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η	0.0006690	Pa×s	298.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η	0.0006640	Pa×s	298.15	Densities and Viscosities of Ternary Mixtures of Heptane, Octane, Nonane, and Hexyl Benzene from 293.15 K to 313.15 K
η	0.0006217	Pa×s	303.15	Densities and Viscosities of Ternary Mixtures of Heptane, Octane, Nonane, and Hexyl Benzene from 293.15 K to 313.15 K
η	0.0006280	Pa×s	303.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η	0.0005849	Pa×s	308.15	Densities and Viscosities of Ternary Mixtures of Heptane, Octane, Nonane, and Hexyl Benzene from 293.15 K to 313.15 K
η	0.0005900	Pa×s	308.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η	0.0005500	Pa×s	313.15	Densities and Viscosities of Ternary Mixtures of Heptane, Octane, Nonane, and Hexyl Benzene from 293.15 K to 313.15 K
η	0.0005550	Pa×s	313.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η	0.0005220	Pa×s	318.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η	0.0004930	Pa×s	323.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η	0.0004660	Pa×s	328.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η	0.0004420	Pa×s	333.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η	0.0004200	Pa×s	338.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η	0.0003990	Pa×s	343.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η	0.0003800	Pa×s	348.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η	0.0003620	Pa×s	353.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η	0.0003460	Pa×s	358.15	Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
εr	[1.93; 1.99]		[288.15; 338.15]
εr	1.99		288.15	Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures
εr	1.98		298.15	Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures
εr	1.97		308.15	Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures
εr	1.95		318.15	Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures
εr	1.94		328.15	Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures
εr	1.93		338.15	Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures
ΔfusH	[15.00; 15.48]	kJ/mol	[219.50; 219.70]
ΔfusH	15.00	kJ/mol	219.50	NIST
ΔfusH	15.48	kJ/mol	219.70	NIST
ΔsubH	74.60	kJ/mol	219.00	NIST
ΔvapH	[36.91; 48.30]	kJ/mol	[263.50; 424.00]
ΔvapH	48.30	kJ/mol	263.50	NIST
ΔvapH	46.70	kJ/mol	299.00	NIST
ΔvapH	46.00	kJ/mol	314.00	NIST
ΔvapH	44.30	kJ/mol	328.00	NIST
ΔvapH	43.20	kJ/mol	343.00	NIST
ΔvapH	42.10	kJ/mol	358.00	NIST
ΔvapH	43.90	kJ/mol	367.50	NIST
ΔvapH	42.70	kJ/mol	385.00	NIST
ΔvapH	36.91	kJ/mol	423.80	KDB
ΔvapH	36.91	kJ/mol	424.00	NIST
Pvap	[2.34; 195.54]	kPa	[322.59; 450.56]
Pvap	2.34	kPa	322.59	Vapor-Liquid Equilibrium Studies for Systems Containing n-Butylisocyanate at Temperatures between 323.15 K and 371.15 K
Pvap	3.97	kPa	333.15	Vapor liquid equilibria and density measurement for binary mixtures of toluene, benzene, o-xylene, m-xylene, sulfolane and nonane at 333.15K and 353.15K
Pvap	4.99	kPa	338.33	Vapor-Liquid Equilibrium Studies for Systems Containing n-Butylisocyanate at Temperatures between 323.15 K and 371.15 K
Pvap	9.00	kPa	351.53	Vapor-Liquid Equilibrium Studies for Systems Containing n-Butylisocyanate at Temperatures between 323.15 K and 371.15 K
Pvap	9.65	kPa	353.15	Measurement of vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide and prediction of these properties and A using modified UNIFAC (Dortmund)
Pvap	10.28	kPa	353.15	Vapor liquid equilibria and density measurement for binary mixtures of toluene, benzene, o-xylene, m-xylene, sulfolane and nonane at 333.15K and 353.15K
Pvap	15.58	kPa	365.30	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	18.07	kPa	369.25	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	19.81	kPa	371.37	Vapor-Liquid Equilibrium Studies for Systems Containing n-Butylisocyanate at Temperatures between 323.15 K and 371.15 K
Pvap	20.58	kPa	372.81	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	23.49	kPa	376.46	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	26.35	kPa	379.71	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	28.78	kPa	382.25	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	31.22	kPa	384.65	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	33.80	kPa	387.02	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	36.62	kPa	389.45	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	40.00	kPa	391.78	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	39.52	kPa	391.80	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	40.00	kPa	391.87	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	40.00	kPa	391.90	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	40.00	kPa	392.17	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	39.96	kPa	392.77	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	41.74	kPa	393.48	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	44.15	kPa	395.26	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	46.56	kPa	396.96	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	49.15	kPa	398.71	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	49.24	kPa	399.76	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	52.12	kPa	400.61	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	54.42	kPa	402.01	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	56.55	kPa	403.31	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	58.04	kPa	404.65	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	59.01	kPa	404.73	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	61.77	kPa	406.27	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	64.58	kPa	407.78	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	66.76	kPa	408.93	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	66.68	kPa	409.14	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	69.09	kPa	410.11	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	71.53	kPa	411.32	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	74.01	kPa	412.52	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	75.48	kPa	413.23	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	76.48	kPa	413.68	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	79.03	kPa	414.83	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	81.41	kPa	415.90	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	84.18	kPa	417.05	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	84.44	kPa	417.22	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	86.85	kPa	418.24	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	89.41	kPa	419.28	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	92.43	kPa	420.50	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	93.72	kPa	420.83	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	95.25	kPa	421.62	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	98.40	kPa	422.83	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	99.35	kPa	423.20	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	100.44	kPa	423.61	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	101.30	kPa	423.80	Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
Pvap	101.70	kPa	423.88	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	101.32	kPa	423.94	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	104.00	kPa	424.92	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	106.50	kPa	425.83	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	108.99	kPa	426.71	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	111.54	kPa	427.60	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	113.88	kPa	428.40	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	116.44	kPa	429.26	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	119.35	kPa	430.22	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	122.04	kPa	431.09	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	124.99	kPa	432.04	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	127.82	kPa	432.94	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	130.52	kPa	433.74	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	133.60	kPa	434.68	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	136.62	kPa	435.58	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	139.12	kPa	436.31	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	141.90	kPa	437.11	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	144.81	kPa	437.95	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	147.42	kPa	438.67	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	150.23	kPa	439.45	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	152.67	kPa	440.11	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	155.08	kPa	440.76	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	157.53	kPa	441.41	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	159.98	kPa	442.05	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	162.80	kPa	442.77	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	165.61	kPa	443.49	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	168.53	kPa	444.23	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	171.39	kPa	444.93	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	173.63	kPa	445.49	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	176.52	kPa	446.19	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	178.85	kPa	446.75	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	181.82	kPa	447.44	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	184.55	kPa	448.07	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	186.86	kPa	448.61	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	189.75	kPa	449.27	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	192.00	kPa	449.81	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap	195.54	kPa	450.56	Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
n0	[1.39380; 1.40740]		[293.13; 318.15]
n0	1.40550		293.13	Isobaric Vapor-Liquid Equilibria of the Ternary System Pentan-1-ol + Pentyl Acetate + Nonane
n0	1.40580		293.15	Activity Coefficients at Infinite Dilution and Excess Molar Volumes in Binary Mixtures Containing Normal Alkanes (Nonane, Decane, Undecane, or Dodecane) and Cresols (2-Methylphenol or 3-Methylphenol)
n0	1.40400		293.15	Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
n0	1.40550		293.15	Isobaric Vapor Liquid Equilibria of the Ternary System 1-Pentanol + Nonane Anisole
n0	1.40680		293.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene with Some n-Alkanes at T = (293.15 to 313.15) K
n0	1.40550		293.15	Isobaric Vapor-Liquid Equilibria of the Ternary System Dibutyl Ether + 1-Pentanol + Nonane
n0	1.40550		293.15	Activity Coefficients at Infinite Dilution of Cylcohexylamine + Octane, Toluene, Ethylbenzene, or Aniline and Excess Molar Volumes in Binary Mixtures of Cyclohexylamine + Heptane, Octane, Nonane, Decane, Undecane, Aniline, or Water
n0	1.40550		293.15	Isobaric Vapor-Liquid Equilibria of the Ternary System Methylbutyl Ketone + 1-Pentanol + Nonane
n0	1.40740		293.15	Vapor-Liquid Equilibrium Measurements of Ethanol and n-Nonane or n-Decane Binary Mixtures with Large Relative Volatility
n0	1.40560		293.15	P-rho-T Data and Modeling for Propan-1-ol + n-Octane or n-Nonane or n-Decane from 313.15 K to 363.15 K and 1 MPa to 20 MPa
n0	1.40570		293.15	Infinite Dilution Activity Coefficients of Hydrocarbons in Triethylene Glycol and Tetraethylene Glycol
n0	1.40320		298.15	Measurements and Correlations of the Isobaric Vapor Liquid Equilibria of Binary Mixtures and Excess Properties for Mixtures Containing an Alkyl (Methyl, Ethyl) Butanoate with an Alkane (Heptane, Nonane) at 101.3 kPa
n0	1.40310		298.15	Multiproperty Correlation of Experimental Data of the Binaries Propyl Ethanoate + Alkanes (Pentane to Decane). New Experimental Information for Vapor Liquid Equilibrium and Mixing Properties
n0	1.40311		298.15	KDB
n0	1.40270		298.15	Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
n0	1.40326		298.15	Separation of Benzene from Linear Alkanes (C6-C9) Using 1-Ethyl-3-Methylimidazolium Ethylsulfate at T = 298.15 K
n0	1.40326		298.15	Liquid-Liquid Equilibria of the Ternary Systems of Alkane + Aromatic + 1-Ethylpyridinium Ethylsulfate Ionic Liquid at T = (283.15 and 298.15) K
n0	1.40210		298.15	Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
n0	1.40320		298.15	Improvements in the Experimentation and the Representation of Thermodynamic Properties (iso-p VLE and yE) of Alkyl Propanoate + Alkane Binaries
n0	1.40326		298.15	Extraction of toluene from aliphatic compounds using an ionic liquid as solvent: Influence of the alkane on the (liquid + liquid) equilibrium
n0	1.40220		303.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene with Some n-Alkanes at T = (293.15 to 313.15) K
n0	1.40020		303.15	Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
n0	1.39980		303.15	Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
n0	1.39730		308.15	Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
n0	1.39380		318.15	Multiproperty Correlation of Experimental Data of the Binaries Propyl Ethanoate + Alkanes (Pentane to Decane). New Experimental Information for Vapor Liquid Equilibrium and Mixing Properties
n0	1.39390		318.15	Thermodynamic properties of (an ester + an alkane). XVI. Experimental HEm and V Em values and a new correlation method for (an alkyl ethanoate + an n-alkane) at 318.15 K
ρl	[661.14; 732.83]	kg/m3	[273.15; 363.15]
ρl	732.83	kg/m3	273.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	729.01	kg/m3	278.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	725.58	kg/m3	283.15	Density, viscosity and excess molar volume of binary mixtures of tri-n-octylamine + diluents (n-heptane, n-octane, n-nonane, and n-decane) at various temperatures
ρl	725.16	kg/m3	283.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	724.54	kg/m3	285.15	Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl	721.32	kg/m3	288.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	722.22	kg/m3	288.15	Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl	721.64	kg/m3	288.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	721.77	kg/m3	288.15	On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl	718.00	kg/m3	293.00	KDB
ρl	717.86	kg/m3	293.15	Density, viscosity and excess molar volume of binary mixtures of tri-n-octylamine + diluents (n-heptane, n-octane, n-nonane, and n-decane) at various temperatures
ρl	718.00	kg/m3	293.15	Volume expansion prediction of supercritical CO 2 + crude oil
ρl	718.42	kg/m3	293.15	Liquid liquid equilibrium of ternary systems 1-butyl-3-methylimidazolium hexafluorophosphate + aromatic + aliphatic
ρl	718.35	kg/m3	293.15	Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl	717.88	kg/m3	293.15	An Isothermal vapour-liquid equilibrium data for the binary systems of CHF3 with (n-nonane, n-decane, or n-undecane) and C2F6 with (n-nonane or n-decane)
ρl	717.88	kg/m3	293.15	Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
ρl	717.45	kg/m3	293.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	717.94	kg/m3	293.15	Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
ρl	717.76	kg/m3	293.15	On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl	717.78	kg/m3	293.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	716.60	kg/m3	294.15	An Isothermal vapour-liquid equilibrium data for the binary systems of CHF3 with (n-nonane, n-decane, or n-undecane) and C2F6 with (n-nonane or n-decane)
ρl	715.82	kg/m3	295.15	An Isothermal vapour-liquid equilibrium data for the binary systems of CHF3 with (n-nonane, n-decane, or n-undecane) and C2F6 with (n-nonane or n-decane)
ρl	715.04	kg/m3	296.15	An Isothermal vapour-liquid equilibrium data for the binary systems of CHF3 with (n-nonane, n-decane, or n-undecane) and C2F6 with (n-nonane or n-decane)
ρl	714.27	kg/m3	297.15	An Isothermal vapour-liquid equilibrium data for the binary systems of CHF3 with (n-nonane, n-decane, or n-undecane) and C2F6 with (n-nonane or n-decane)
ρl	713.69	kg/m3	298.15	An Isothermal vapour-liquid equilibrium data for the binary systems of CHF3 with (n-nonane, n-decane, or n-undecane) and C2F6 with (n-nonane or n-decane)
ρl	714.00	kg/m3	298.15	Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
ρl	714.06	kg/m3	298.15	Thermodynamics of mixtures containing amines VI. Liquid liquid equilibria for mixtures of o-toluidine + selected alkanes
ρl	713.91	kg/m3	298.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	713.77	kg/m3	298.15	On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl	713.99	kg/m3	298.15	Evaluation of ionic liquids as solvent for aromatic extraction: Experimental, correlation and COSMO-RS predictions
ρl	713.58	kg/m3	298.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	714.01	kg/m3	298.15	Excess molar volumes and dynamic viscosities for binary mixtures of toluene + n-alkanes (C5 C10) at T = 298.15 K Comparison with Prigogine Flory Patterson theory
ρl	714.46	kg/m3	298.15	Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl	714.11	kg/m3	298.15	Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
ρl	714.05	kg/m3	298.15	Liquid-liquid equilibria for (2-hydroxy benzaldehyde + n-alkane) mixtures. Intermolecular and proximity effects in systems containing hydroxyl and aldehyde groups
ρl	714.00	kg/m3	298.15	Excess molar enthalpies for binary mixtures of cyclopentanone, cyclohexanone, or cycloheptanone with n-nonane at T = 298.15 K and atmospheric pressure
ρl	714.06	kg/m3	298.15	Thermodynamics of Mixtures Containing a Strongly Polar Compound. 9. Liquid-Liquid Equilibria for epsilon-Caprolactam + Selected Alkanes
ρl	714.06	kg/m3	298.15	Thermodynamics of Mixtures Containing a Strongly Polar Compound. 8. Liquid-Liquid Equilibria for N,N-Dialkylamide + Selected N-Alkanes
ρl	713.90	kg/m3	298.15	(Liquid + liquid) equilibrium at T = 298.15 K for ternary mixtures of alkane + aromatic compounds + imidazolium-based ionic liquids
ρl	713.95	kg/m3	298.15	Density, viscosity and excess molar volume of binary mixtures of tri-n-octylamine + diluents (n-heptane, n-octane, n-nonane, and n-decane) at various temperatures
ρl	713.94	kg/m3	298.20	Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
ρl	710.03	kg/m3	303.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	709.89	kg/m3	303.15	On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl	710.10	kg/m3	303.15	Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
ρl	710.55	kg/m3	303.15	Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl	710.20	kg/m3	303.15	Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
ρl	710.06	kg/m3	303.15	Density, viscosity and excess molar volume of binary mixtures of tri-n-octylamine + diluents (n-heptane, n-octane, n-nonane, and n-decane) at various temperatures
ρl	709.69	kg/m3	303.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	706.12	kg/m3	308.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	706.63	kg/m3	308.15	Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl	706.20	kg/m3	308.15	On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl	706.19	kg/m3	308.15	Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
ρl	706.29	kg/m3	308.15	Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
ρl	705.78	kg/m3	308.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	702.35	kg/m3	313.15	Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
ρl	701.86	kg/m3	313.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	702.70	kg/m3	313.15	Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl	702.26	kg/m3	313.15	Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
ρl	702.20	kg/m3	313.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	698.14	kg/m3	318.15	On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl	698.26	kg/m3	318.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	697.91	kg/m3	318.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	698.40	kg/m3	318.15	Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
ρl	693.95	kg/m3	323.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	694.43	kg/m3	323.15	Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
ρl	694.30	kg/m3	323.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	690.14	kg/m3	328.15	On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl	690.33	kg/m3	328.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	689.97	kg/m3	328.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	685.97	kg/m3	333.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	686.34	kg/m3	333.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	681.94	kg/m3	338.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	682.31	kg/m3	338.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	677.88	kg/m3	343.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	678.26	kg/m3	343.15	Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl	673.91	kg/m3	348.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	669.71	kg/m3	353.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	665.58	kg/m3	358.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl	661.14	kg/m3	363.15	Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
csound,fluid	[738.00; 1227.30]	m/s	[293.15; 423.15]
csound,fluid	1227.30	m/s	293.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	1207.20	m/s	298.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	1187.20	m/s	303.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	1167.30	m/s	308.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	1147.50	m/s	313.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	1127.80	m/s	318.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	1108.20	m/s	323.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	1088.70	m/s	328.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	1069.30	m/s	333.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	1050.00	m/s	338.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	1030.80	m/s	343.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	1011.80	m/s	348.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	992.80	m/s	353.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	973.90	m/s	358.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	955.20	m/s	363.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	936.50	m/s	368.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	917.90	m/s	373.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	899.50	m/s	378.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	881.10	m/s	383.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	862.90	m/s	388.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	844.70	m/s	393.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	826.70	m/s	398.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	808.80	m/s	403.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	790.90	m/s	408.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	773.20	m/s	413.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	755.60	m/s	418.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid	738.00	m/s	423.15	Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
γ	[0.02; 0.02]	N/m	[288.15; 323.15]
γ	0.02	N/m	288.15	Density and surface tension variation with temperature for n-nonane + 1-hexanol
γ	0.02	N/m	293.15	Density, Refractive Index, Viscosity, and Surface Tension of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with Some n-Alkanes from (293.15 to 313.15) K
γ	0.02	N/m	293.15	Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ	0.02	N/m	293.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.02	N/m	293.20	KDB
γ	0.02	N/m	298.15	Density and surface tension variation with temperature for n-nonane + 1-hexanol
γ	0.02	N/m	298.15	Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ	0.02	N/m	298.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.02	N/m	303.15	Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ	0.02	N/m	303.15	Density, Refractive Index, Viscosity, and Surface Tension of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with Some n-Alkanes from (293.15 to 313.15) K
γ	0.02	N/m	303.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.02	N/m	308.15	Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ	0.02	N/m	308.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.02	N/m	308.15	Density and surface tension variation with temperature for n-nonane + 1-hexanol
γ	0.02	N/m	313.15	Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ	0.02	N/m	313.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.02	N/m	318.15	Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ	0.02	N/m	318.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.02	N/m	323.15	Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ	0.02	N/m	323.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures

Datasets

1. Isobaric coefficient of expansion, 1/K (1)
2. Viscosity, Pa*s (1)
3. Mass density, kg/m3 (5)
4. Speed of sound, m/s (1)

Isobaric coefficient of expansion, 1/K

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Isobaric coefficient of expansion, 1/K - Liquid
278.15	5000.00	0.0010
278.15	10000.00	0.0010
278.15	15000.00	0.0010
278.15	20000.00	0.0009
278.15	25000.00	0.0009
278.15	30000.00	0.0009
278.15	35000.00	0.0009
278.15	40000.00	0.0008
278.15	45000.00	0.0008
278.15	50000.00	0.0008
278.15	55000.00	0.0008
288.15	5000.00	0.0010
288.15	10000.00	0.0010
288.15	15000.00	0.0010
288.15	20000.00	0.0009
288.15	25000.00	0.0009
288.15	30000.00	0.0009
288.15	35000.00	0.0009
288.15	40000.00	0.0009
288.15	45000.00	0.0008
288.15	50000.00	0.0008
288.15	55000.00	0.0008
298.15	5000.00	0.0010
298.15	10000.00	0.0010
298.15	15000.00	0.0010
298.15	20000.00	0.0010
298.15	25000.00	0.0009
298.15	30000.00	0.0009
298.15	35000.00	0.0009
298.15	40000.00	0.0009
298.15	45000.00	0.0008
298.15	50000.00	0.0008
298.15	55000.00	0.0008
308.15	5000.00	0.0011
308.15	10000.00	0.0010
308.15	15000.00	0.0010
308.15	20000.00	0.0010
308.15	25000.00	0.0009
308.15	30000.00	0.0009
308.15	35000.00	0.0009
308.15	40000.00	0.0009
308.15	45000.00	0.0008
308.15	50000.00	0.0008
308.15	55000.00	0.0008
318.15	5000.00	0.0011
318.15	10000.00	0.0010
318.15	15000.00	0.0010
318.15	20000.00	0.0010
318.15	25000.00	0.0009
318.15	30000.00	0.0009
318.15	35000.00	0.0009
318.15	40000.00	0.0009
318.15	45000.00	0.0008
318.15	50000.00	0.0008
318.15	55000.00	0.0008
328.15	5000.00	0.0011
328.15	10000.00	0.0011
328.15	15000.00	0.0010
328.15	20000.00	0.0010
328.15	25000.00	0.0009
328.15	30000.00	0.0009
328.15	35000.00	0.0009
328.15	40000.00	0.0009
328.15	45000.00	0.0008
328.15	50000.00	0.0008
328.15	55000.00	0.0008
338.15	5000.00	0.0011
338.15	10000.00	0.0011
338.15	15000.00	0.0010
338.15	20000.00	0.0010
338.15	25000.00	0.0010
338.15	30000.00	0.0009
338.15	35000.00	0.0009
338.15	40000.00	0.0009
338.15	45000.00	0.0008
338.15	50000.00	0.0008
338.15	55000.00	0.0008
348.15	5000.00	0.0011
348.15	10000.00	0.0011
348.15	15000.00	0.0010
348.15	20000.00	0.0010
348.15	25000.00	0.0010
348.15	30000.00	0.0009
348.15	35000.00	0.0009
348.15	40000.00	0.0009
348.15	45000.00	0.0008
348.15	50000.00	0.0008
348.15	55000.00	0.0008
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.15	101.33	0.0006
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
233.15	101.46	763.962
233.15	1176.07	764.563
233.15	2178.21	765.126
233.15	4167.03	766.231
233.15	5936.52	767.203
233.15	8144.53	768.395
233.15	10065.60	769.42
233.15	12147.70	770.516
233.15	14076.40	771.516
233.15	16087.10	772.548
233.15	18066.90	773.551
233.15	19984.50	774.511
233.15	21989.60	775.502
233.15	24043.80	776.506
233.15	25990.20	777.446
233.15	27926.70	778.373
233.15	29906.00	779.308
253.15	101.82	748.678
253.15	1135.27	749.335
253.15	2178.61	749.992
253.15	3967.76	751.107
253.15	6147.47	752.446
253.15	8137.98	753.648
253.15	10112.30	754.82
253.15	12111.20	755.991
253.15	14130.20	757.156
253.15	16140.10	758.299
253.15	18106.10	759.398
253.15	20064.20	760.484
253.15	22026.10	761.552
253.15	23955.00	762.59
253.15	25972.30	763.661
253.15	27912.60	764.677
253.15	29966.80	765.739
273.15	102.52	733.389
273.15	1156.84	734.143
273.15	2137.97	734.842
273.15	4026.01	736.166
273.15	6169.44	737.644
273.15	8161.45	738.99
273.15	10122.00	740.29
273.15	12106.50	741.586
273.15	14100.70	742.864
273.15	16067.00	744.108
273.15	18074.30	745.354
273.15	20036.30	746.555
273.15	21999.70	747.737
273.15	23995.50	748.923
273.15	25993.50	750.093
273.15	27981.50	751.238
273.15	29875.50	752.316
293.15	101.69	717.968
293.15	1184.28	718.847
293.15	2129.17	719.604
293.15	3960.49	721.055
293.15	6115.45	722.729
293.15	7981.56	724.145
293.15	10014.70	725.663
293.15	12148.60	727.214
293.15	13981.10	728.526
293.15	16170.10	730.062
293.15	17942.90	731.285
293.15	20200.00	732.813
293.15	22156.50	734.115
293.15	24157.90	735.421
293.15	26136.50	736.696
293.15	28126.30	737.958
293.15	29978.50	739.115
313.15	98.73	702.339
313.15	1168.73	703.323
313.15	2131.95	704.205
313.15	3967.37	705.852
313.15	6162.29	707.777
313.15	8113.86	709.449
313.15	10023.50	711.038
313.15	12172.80	712.791
313.15	14170.00	714.384
313.15	16194.40	715.964
313.15	17956.10	717.315
313.15	20057.40	718.889
313.15	22190.80	720.459
313.15	24136.30	721.862
313.15	26139.10	723.282
313.15	28073.10	724.629
313.15	29972.40	725.932
333.15	102.84	686.431
333.15	1137.45	687.521
333.15	2113.93	688.539
333.15	4162.71	690.632
333.15	6145.33	692.599
333.15	8151.89	694.535
333.15	10023.60	696.296
333.15	12113.90	698.208
333.15	14126.60	700.005
333.15	15989.20	701.627
333.15	18027.40	703.362
333.15	19954.20	704.977
333.15	22112.40	706.723
333.15	24079.90	708.292
333.15	26037.60	709.821
333.15	28054.20	711.366
333.15	29912.30	712.772
353.15	97.13	671.217
353.15	2136.70	672.617
353.15	6141.90	677.222
353.15	8110.87	679.378
353.15	10054.10	681.439
353.15	12124.00	683.57
353.15	14143.80	685.589
353.15	15989.00	687.385
353.15	18010.60	689.305
353.15	20035.80	691.174
353.15	21991.10	692.938
353.15	23964.80	694.678
353.15	25968.30	696.403
353.15	27955.30	698.078
353.15	29938.70	699.718
373.15	102.37	653.427
373.15	1227.94	655.018
373.15	2148.86	656.298
373.15	4131.53	658.968
373.15	6127.03	661.551
373.15	8138.76	664.058
373.15	10022.20	666.323
373.15	12111.60	668.749
373.15	14118.80	671.003
373.15	16133.90	673.197
373.15	18104.00	675.276
373.15	20078.30	677.302
373.15	22063.50	679.286
373.15	23987.70	681.158
373.15	26124.00	683.184
373.15	28010.20	684.93
373.15	29904.70	686.647
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	298.15	713.93
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	1010.00	726.22
283.15	5040.00	729.17
283.15	10020.00	732.75
283.15	15020.00	736.14
283.15	20040.00	739.41
283.15	25020.00	742.54
283.15	30040.00	745.52
283.15	35050.00	748.45
283.15	40010.00	751.23
283.15	45050.00	753.99
283.15	50010.00	756.62
283.15	55020.00	759.19
283.15	60030.00	761.66
283.15	65010.00	764.08
283.15	5020.00	729.22
298.15	1020.00	714.83
298.15	5010.00	718.08
298.15	10030.00	721.94
298.15	15060.00	725.7
298.15	20040.00	729.17
298.15	25040.00	732.54
298.15	30010.00	735.76
298.15	35050.00	738.87
298.15	40010.00	741.88
298.15	45060.00	744.79
298.15	50010.00	747.56
298.15	55040.00	750.31
298.15	60020.00	752.92
298.15	65010.00	755.48
298.15	5040.00	718.12
323.15	1030.00	695.27
323.15	5030.00	699.04
323.15	10050.00	703.57
323.15	15020.00	707.81
323.15	20050.00	711.84
323.15	25020.00	715.63
323.15	30020.00	719.22
323.15	35080.00	722.75
323.15	40050.00	726.09
323.15	45060.00	729.27
323.15	50030.00	732.36
323.15	55050.00	735.35
323.15	60010.00	738.19
323.15	65010.00	741.02
323.15	5060.00	699.09
348.15	1010.00	675.18
348.15	5040.00	679.76
348.15	10030.00	685.0
348.15	15020.00	689.84
348.15	20040.00	694.44
348.15	25050.00	698.79
348.15	30030.00	702.84
348.15	35050.00	706.74
348.15	40020.00	710.4
348.15	45070.00	714.01
348.15	50040.00	717.37
348.15	55050.00	720.67
348.15	60000.00	723.79
348.15	65040.00	726.84
348.15	5030.00	679.76
373.15	1010.00	654.52
373.15	5050.00	659.99
373.15	10030.00	666.13
373.15	15070.00	671.78
373.15	20030.00	677.04
373.15	25060.00	681.94
373.15	30040.00	686.51
373.15	35060.00	690.83
373.15	40020.00	694.95
373.15	45070.00	698.87
373.15	50070.00	702.65
373.15	55060.00	706.23
373.15	60040.00	709.66
373.15	65030.00	712.95
373.15	5050.00	659.99
398.15	1020.00	633.06
398.15	5020.00	639.53
398.15	10050.00	646.89
398.15	15070.00	653.53
398.15	20020.00	659.49
398.15	25030.00	665.05
398.15	30050.00	670.22
398.15	35050.00	675.1
398.15	40020.00	679.63
398.15	45070.00	683.97
398.15	50020.00	688.07
398.15	55040.00	692.01
398.15	60030.00	695.72
398.15	65040.00	699.37
398.15	5030.00	639.58
423.15	1020.00	610.45
423.15	5030.00	618.42
423.15	10030.00	627.15
423.15	15030.00	634.86
423.15	20040.00	641.8
423.15	25040.00	648.1
423.15	30020.00	653.92
423.15	35050.00	659.35
423.15	40020.00	664.4
423.15	45020.00	669.15
423.15	50040.00	673.7
423.15	55020.00	677.97
423.15	60030.00	682.03
423.15	65040.00	685.95
423.15	5030.00	618.47
448.15	1000.00	586.37
448.15	5020.00	596.41
448.15	10040.00	607.05
448.15	15010.00	616.06
448.15	20010.00	624.0
448.15	25040.00	631.27
448.15	30030.00	637.78
448.15	35030.00	643.8
448.15	40010.00	649.38
448.15	45050.00	654.67
448.15	50020.00	659.58
448.15	55040.00	664.24
448.15	60030.00	668.62
448.15	65020.00	672.85
448.15	5020.00	596.46
473.15	5010.00	573.14
473.15	10040.00	586.15
473.15	15040.00	596.86
473.15	20020.00	606.05
473.15	25050.00	614.28
473.15	30020.00	621.6
473.15	35030.00	628.3
473.15	40050.00	634.51
473.15	45050.00	640.25
473.15	50040.00	645.6
473.15	55020.00	650.62
473.15	60010.00	655.39
473.15	65010.00	659.92
473.15	5010.00	573.14
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.21	1993.00	719.36
293.21	3991.00	721.16
293.21	5993.00	722.88
293.21	7996.00	724.42
293.21	10001.00	725.92
293.21	13001.00	728.0
293.22	16000.00	730.02
293.21	19004.00	732.11
293.21	22005.00	734.14
293.21	24997.00	736.13
293.21	27997.00	738.31
293.21	29995.00	739.58
313.11	2000.00	704.08
313.11	4007.00	705.88
313.11	6006.00	707.62
313.11	8004.00	709.24
313.11	10007.00	710.92
313.11	13003.00	713.28
313.11	16007.00	715.76
313.10	19007.00	718.18
313.10	22007.00	720.52
313.10	25009.00	722.7
313.10	28007.00	724.82
313.10	30010.00	726.21
333.00	2014.00	688.53
333.00	3990.00	690.6
333.00	5995.00	692.58
333.01	8001.00	694.51
333.01	10007.00	696.11
333.01	13004.00	698.84
333.01	16002.00	701.48
333.01	19006.00	704.03
333.01	22003.00	706.5
333.01	25006.00	708.9
333.01	28003.00	711.23
333.01	30012.00	712.74
353.12	2004.00	672.27
353.12	3995.00	674.59
353.12	6000.00	676.83
353.12	8005.00	679.1
353.12	10010.00	681.31
353.12	13002.00	684.37
353.12	16003.00	687.3
353.12	18999.00	689.99
353.12	22002.00	692.72
353.12	25004.00	695.35
353.12	28007.00	697.9
353.12	30003.00	699.56
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	283.15	725.6
100.00	288.15	721.6
100.00	293.15	717.8
100.00	298.15	713.7
100.00	303.15	709.9
100.00	308.15	706.0
100.00	313.15	701.9
100.00	318.15	698.1
100.00	323.15	694.1
3000.00	283.15	727.7
3000.00	288.15	723.8
3000.00	293.15	720.0
3000.00	298.15	716.1
3000.00	303.15	712.3
3000.00	308.15	708.5
3000.00	313.15	704.5
3000.00	318.15	700.7
3000.00	323.15	696.9
5000.00	283.15	729.1
5000.00	288.15	725.3
5000.00	293.15	721.5
5000.00	298.15	717.7
5000.00	303.15	713.9
5000.00	308.15	710.1
5000.00	313.15	706.3
5000.00	318.15	702.4
5000.00	323.15	698.6
7500.00	283.15	730.8
7500.00	288.15	727.0
7500.00	293.15	723.4
7500.00	298.15	719.5
7500.00	303.15	715.8
7500.00	308.15	712.1
7500.00	313.15	708.3
7500.00	318.15	704.6
7500.00	323.15	700.8
10000.00	283.15	732.6
10000.00	288.15	728.9
10000.00	293.15	725.2
10000.00	298.15	721.5
10000.00	303.15	717.8
10000.00	308.15	714.2
10000.00	313.15	710.4
10000.00	318.15	706.8
10000.00	323.15	703.0
20000.00	283.15	739.2
20000.00	288.15	735.7
20000.00	293.15	732.2
20000.00	298.15	728.7
20000.00	303.15	725.2
20000.00	308.15	721.7
20000.00	313.15	718.2
20000.00	318.15	714.7
20000.00	323.15	711.2
30000.00	283.15	745.3
30000.00	288.15	742.0
30000.00	293.15	738.7
30000.00	298.15	735.2
30000.00	303.15	731.9
30000.00	308.15	728.5
30000.00	313.15	725.3
30000.00	318.15	721.9
30000.00	323.15	718.6
40000.00	283.15	751.1
40000.00	288.15	747.9
40000.00	293.15	744.6
40000.00	298.15	741.4
40000.00	303.15	738.2
40000.00	308.15	735.0
40000.00	313.15	731.8
40000.00	318.15	728.6
40000.00	323.15	725.4
50000.00	283.15	756.4
50000.00	288.15	753.4
50000.00	293.15	750.3
50000.00	298.15	747.1
50000.00	303.15	744.1
50000.00	308.15	740.9
50000.00	313.15	737.8
50000.00	318.15	734.8
50000.00	323.15	731.6
60000.00	283.15	761.6
60000.00	288.15	758.5
60000.00	293.15	755.5
60000.00	298.15	752.5
60000.00	303.15	749.5
60000.00	308.15	746.6
60000.00	313.15	743.5
60000.00	318.15	740.5
60000.00	323.15	737.5
Reference

Speed of sound, m/s

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
100.00	293.15	1226.379
100.00	313.15	1146.226
100.00	333.15	1068.198
100.00	353.15	992.6189
100.00	373.15	922.1599
100.00	393.15	867.4314
10000.00	293.15	1288.02
10000.00	313.15	1212.824
10000.00	333.15	1140.94
10000.00	353.15	1072.568
10000.00	373.15	1004.987
10000.00	393.15	946.865
20000.00	293.15	1344.821
20000.00	313.15	1274.241
20000.00	333.15	1206.915
20000.00	353.15	1142.609
20000.00	373.15	1081.282
20000.00	393.15	1022.924
30000.00	293.15	1396.854
30000.00	313.15	1329.834
30000.00	333.15	1266.203
30000.00	353.15	1205.597
30000.00	373.15	1148.091
30000.00	393.15	1093.674
40000.00	293.15	1445.084
40000.00	313.15	1380.943
40000.00	353.15	1262.461
40000.00	373.15	1207.979
40000.00	393.15	1156.595
50000.00	293.15	1490.057
50000.00	313.15	1428.288
50000.00	333.15	1369.835
50000.00	353.15	1314.591
50000.00	373.15	1262.528
50000.00	393.15	1213.59
60000.00	293.15	1532.464
60000.00	313.15	1472.742
60000.00	333.15	1416.313
60000.00	353.15	1363.169
60000.00	373.15	1313.133
60000.00	393.15	1266.136
70000.00	293.15	1572.512
70000.00	313.15	1514.719
70000.00	333.15	1460.059
70000.00	353.15	1408.501
70000.00	373.15	1360.053
70000.00	393.15	1314.71
80000.00	293.15	1610.591
80000.00	313.15	1554.351
80000.00	333.15	1501.308
80000.00	353.15	1451.316
80000.00	373.15	1404.349
80000.00	393.15	1360.387
90000.00	293.15	1646.928
90000.00	313.15	1592.049
90000.00	333.15	1540.349
90000.00	353.15	1491.697
90000.00	373.15	1446.071
90000.00	393.15	1403.307
100000.00	293.15	1681.563
100000.00	313.15	1628.026
100000.00	333.15	1577.369
100000.00	353.15	1529.841
100000.00	373.15	1485.463
100000.00	393.15	1443.653
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[196.41; 483.65]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			-5.29300e+00
Coefficient B			8.58840e-01
Coefficient C			-4.65800e-04
Coefficient D			9.59000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	196.41	J/mol×K	273.00	Calculated Property
Cp,gas	244.49	J/mol×K	353.78	Calculated Property
Cp,gas	287.83	J/mol×K	434.56	Calculated Property
Cp,gas	326.72	J/mol×K	515.33	Calculated Property
Cp,gas	361.46	J/mol×K	596.11	Calculated Property
Cp,gas	392.37	J/mol×K	676.89	Calculated Property
Cp,gas	419.74	J/mol×K	757.67	Calculated Property
Cp,gas	443.87	J/mol×K	838.44	Calculated Property
Cp,gas	465.07	J/mol×K	919.22	Calculated Property
Cp,gas	483.65	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[310.51; 451.94]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.45385e+01
Coefficient B			-3.70195e+03
Coefficient C			-5.07360e+01
Temperature range, min.			310.51
Temperature range, max.			451.94
Pvap	1.33	kPa	310.51	Calculated Property
Pvap	3.01	kPa	326.22	Calculated Property
Pvap	6.21	kPa	341.94	Calculated Property
Pvap	11.90	kPa	357.65	Calculated Property
Pvap	21.42	kPa	373.37	Calculated Property
Pvap	36.50	kPa	389.08	Calculated Property
Pvap	59.31	kPa	404.80	Calculated Property
Pvap	92.49	kPa	420.51	Calculated Property
Pvap	139.11	kPa	436.23	Calculated Property
Pvap	202.64	kPa	451.94	Calculated Property
Pvap	[6.08e-04; 2266.69]	kPa	[219.63; 595.65]	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			7.25466e+01
Coefficient B			-7.73941e+03
Coefficient C			-8.32740e+00
Coefficient D			3.89483e-06
Coefficient E			0.00000e+00
Temperature range, min.			219.63
Temperature range, max.			595.65
Pvap	6.08e-04	kPa	219.63	Calculated Property
Pvap	0.04	kPa	261.41	Calculated Property
Pvap	0.81	kPa	303.19	Calculated Property
Pvap	6.78	kPa	344.97	Calculated Property
Pvap	33.28	kPa	386.75	Calculated Property
Pvap	113.80	kPa	428.53	Calculated Property
Pvap	301.98	kPa	470.31	Calculated Property
Pvap	667.88	kPa	512.09	Calculated Property
Pvap	1292.71	kPa	553.87	Calculated Property
Pvap	2266.69	kPa	595.65	Calculated Property
Pvap	[5.14e-04; 0.79]	kPa	[219.70; 307.73]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.34123e+01
Coefficient B			-3.43759e+03
Coefficient C			-5.58950e+01
Reference			Carruth and Kobayashi, 1973
Temperature range, min.			219.70
Temperature range, max.			307.73
Pvap	5.14e-04	kPa	219.70	Calculated Property
Pvap	1.68e-03	kPa	229.48	Calculated Property
Pvap	4.82e-03	kPa	239.26	Calculated Property
Pvap	0.01	kPa	249.04	Calculated Property
Pvap	0.03	kPa	258.82	Calculated Property
Pvap	0.06	kPa	268.61	Calculated Property
Pvap	0.13	kPa	278.39	Calculated Property
Pvap	0.25	kPa	288.17	Calculated Property
Pvap	0.45	kPa	297.95	Calculated Property
Pvap	0.79	kPa	307.73	Calculated Property
Pvap	[6.40; 104.01]	kPa	[343.49; 424.94]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39593e+01
Coefficient B			-3.29356e+03
Coefficient C			-7.13550e+01
Reference			Forziati, Norris, et al., 1949, 2
Temperature range, min.			343.49
Temperature range, max.			424.94
Pvap	6.40	kPa	343.49	Calculated Property
Pvap	9.45	kPa	352.54	Calculated Property
Pvap	13.62	kPa	361.59	Calculated Property
Pvap	19.19	kPa	370.64	Calculated Property
Pvap	26.51	kPa	379.69	Calculated Property
Pvap	35.95	kPa	388.74	Calculated Property
Pvap	47.93	kPa	397.79	Calculated Property
Pvap	62.93	kPa	406.84	Calculated Property
Pvap	81.44	kPa	415.89	Calculated Property
Pvap	104.01	kPa	424.94	Calculated Property
Pvap	[6.40; 104.01]	kPa	[343.49; 424.94]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39593e+01
Coefficient B			-3.29356e+03
Coefficient C			-7.13550e+01
Reference			Forziati, Norris, et al., 1949
Temperature range, min.			343.49
Temperature range, max.			424.94
Pvap	6.40	kPa	343.49	Calculated Property
Pvap	9.45	kPa	352.54	Calculated Property
Pvap	13.62	kPa	361.59	Calculated Property
Pvap	19.19	kPa	370.64	Calculated Property
Pvap	26.51	kPa	379.69	Calculated Property
Pvap	35.95	kPa	388.74	Calculated Property
Pvap	47.93	kPa	397.79	Calculated Property
Pvap	62.93	kPa	406.84	Calculated Property
Pvap	81.44	kPa	415.89	Calculated Property
Pvap	104.01	kPa	424.94	Calculated Property

Similar Compounds

Find more compounds similar to Nonane.

Mixtures

• Carbon dioxide + Nonane
• 2,5,8,11,14-Pentaoxapentadecane + Nonane
• 1-Octanamine, N,N-dioctyl- + Nonane
• Benzyl nitrile + Nonane
• Benzene + Nonane
• Heptane + Nonane
• Anisole + Nonane
• Acetic acid, methyl ester + Nonane
• Ethyl Acetate + Nonane
• Acetic acid, propyl ester + Nonane
• Acetic acid, butyl ester + Nonane
• Acetic acid, pentyl ester + Nonane
• Toluene + Nonane
• Octadecafluorooctane + Nonane
• 2,5,8,11-Tetraoxadodecane + Nonane
• Nonane + Cyclohexane
• Benzene, 1,3-dimethyl- + Nonane
• p-Xylene + Nonane
• Carbon dioxide + Ethanol + Nonane
• Nonane + N-Formylmorpholine

Find more mixtures with Nonane.

Sources

• KDB Vapor Pressure Data
• Crippen Method
• Speed-of-Sound Measurements in n-Nonane at Temperatures between 293.15 and 393.15 K and at Pressures up to 100 MPa
• Determination of excess molar enthalpies of the ternary system methyl tert-butyl ether + 1-pentanol + nonane at 298.15K Analysis and comparison with predicted values of the UNIFAC model and some empirical methods
• Solubility of 9-fluorenone, thianthrene and xanthene in organic solvents
• High pressure vapor liquid equilibria for the systems thiophene + nonane +CO2, and thiophene + decane +CO2
• Density and surface tension variation with temperature for n-nonane + 1-hexanol
• Liquid liquid equilibrium of (perfluoroalkane + alkane) binary mixtures
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• Measurement of infinite dilution activity coefficients of n-alkanes in 4-methyl-n-butylpyridinium tetrafluoroborate using gas liquid chromatography
• Thermodynamics of mixtures containing amines VI. Liquid liquid equilibria for mixtures of o-toluidine + selected alkanes
• New isothermal vapor liquid equilibria for the CO2 + n-nonane, and CO2 + n-undecane systems
• Measurement of vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide and prediction of these properties and A using modified UNIFAC (Dortmund)
• Liquid liquid equilibrium of ternary systems 1-butyl-3-methylimidazolium hexafluorophosphate + aromatic + aliphatic
• Measurement and prediction of activity coefficients at infinite dilution ( ), vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1,1-dialkyl-pyrrolidinium bis(trifluoromethylsulfonyl)imide using mod. UNIFAC (Dortmund)
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
• (Solid + liquid) and (liquid + liquid) phase equilibria measurements and correlation of the binary systems {tri-iso-butyl(methyl)phosphonium tosylate + alcohol, or +hydrocarbon}
• Activity coefficients at infinite dilution of alkanes and alkenes in 1-alkyl-3-methylimidazolium tetrafluoroborate
• Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
• Vapor liquid equilibria and density measurement for binary mixtures of toluene, benzene, o-xylene, m-xylene, sulfolane and nonane at 333.15K and 353.15K
• Liquid liquid equilibrium of ternary systems 1-octyl-3-methylimidazolium hexafluorophosphate + aromatic + aliphatic hydrocarbons
• Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
• 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
• Determination and correlation of liquid-liquid equilibria for nine binary acetonitrile + n-alkane systems
• Introduction of the amine group at cycloaliphatic hydrocarbon (c-CHNH2) for the modified UNIFAC (Dortmund) model and validation in multicomponent systems containing cyclohexylamine
• Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
• Liquid-liquid equilibria of mixtures with ethyl lactate and various hydrocarbons
• Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
• Distribution of MEG and methanol in well-defined hydrocarbon and water systems: Experimental measurement and modeling using the CPA EoS
• Vapor liquid equilibrium for the ternary carbon dioxide ethanol nonane and decane systems
• Liquid-liquid equilibria containing fluorous solvents as environmentally benign solvent
• Isobaric vapor-liquid equilibrium for binary systemsof toluene + o-xylene, benzene + o-xylene, nonane + benzene and nonane + heptane at 101.3 kPa
• Enthalpies and Gibbs free energies of solvation in ethylene glycol at298 K: Influence of the solvophobic effect
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• Solutions of alkyl methanoates and alkanes: Simultaneous modeling of phase equilibria and mixing properties. Estimation of behavior by UNIFAC with recalculation of parameters
• 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
• Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 K
• Volume expansion prediction of supercritical CO 2 + crude oil
• Measurement and correlation of the interfacial tension for paraffin + CO2 and (CO2+N2) mixture gas at elevated temperatures and pressures
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• An Isothermal vapour-liquid equilibrium data for the binary systems of CHF3 with (n-nonane, n-decane, or n-undecane) and C2F6 with (n-nonane or n-decane)
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
• 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
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• Thermodynamic properties of (an ester + an alkane). XVI. Experimental HEm and V Em values and a new correlation method for (an alkyl ethanoate + an n-alkane) at 318.15 K
• On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
• Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
• Thermodynamic properties of (an ester + and alkane). XVII. Experimental He and Ve values for (an alkyl propanoate + an alkane) at 318.15K
• Coexistence curves of critical nonaqueous microemulsions of (AOT + DMA + nonane) and (AOT + DMA + octane)
• Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
• On the permittivity and density of the systems {tetraglyme + (n-nonane or n-dodecane)} at various temperatures
• Excess molar volumes and dynamic viscosities for binary mixtures of toluene + n-alkanes (C5 C10) at T = 298.15 K Comparison with Prigogine Flory Patterson theory
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• (p,Vm,T) measurements of (cyclohexane + nonane) at temperatures from 298.15 K to 328.15 K and at pressures up to 40 MPa
• Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
• Measurement and correlation of the (p, ?, T) relation of liquid n-heptane, n-nonane, 2,4-dichlorotoluene, and bromobenzene in the temperature range from (233.15 to 473.15) K at pressures up to 30 MPa for use as density reference liquids
• Activity coefficients at infinite dilution of hydrocarbons, alkylbenzenes, and alcohols in the paramagnetic ionic liquid 1-butyl-3-methyl-imidazolium tetrachloridoferrate(III) using gas liquid chromatography
• Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
• Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
• Experimental densities, refractive indices, and speeds of sound of 12 binary mixtures containing alkanes and aromatic compounds at T = 313.15 K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
• Separation of benzene from alkanes using 1-ethyl-3-methylpyridinium ethylsulfate ionic liquid at several temperatures and atmospheric pressure: Effect of the size of the aliphatic hydrocarbons
• Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
• LLE data for the ionic liquid 3-methyl-N-butyl pyridinium dicyanamide with several aromatic and aliphatic hydrocarbons
• Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
• Separation of toluene from alkanes using 1-ethyl-3-methylpyridinium ethylsulfate ionic liquid at T = 298.15 K and atmospheric pressure
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate [EMIM][TCB] using gas liquid chromatography
• Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
• Activity coefficients at infinite dilution of organic solutes in N-alkylpyridinium bis(trifluoromethylsulfonyl)imide ([CnPY][NTf2], n = 2, 4, 5) using gas liquid chromatography
• Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
• Extraction of toluene from aliphatic compounds using an ionic liquid as solvent: Influence of the alkane on the (liquid + liquid) equilibrium
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyl(tetradecyl)phosphonium tetrafluoroborate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 373.15) K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium hexafluoroantimonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid, methyl(trioctyl)ammonium thiosalicylate, [N1888][TS] by gas liquid chromatography at T = (303.15, 313.15, and 323.15) K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
• Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
• (Liquid + liquid) equilibrium for binary systems of N-formylmorpholine with alkanes
• 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 of organic solutes in the ionic liquid trihexyltetradecylphosphonium hexafluorophosphate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 363.15) K
• 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
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• 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
• 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
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
• 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
• Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
• Activity coefficients at infinite dilution of organic solutes in N-formylmorpholine and N-methylpyrrolidone from gas-liquid chromatography
• 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
• Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography at T = (313.15, 333.15, 353.15 and 373.15) K
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Evaluation of ionic liquids as solvent for aromatic extraction: Experimental, correlation and COSMO-RS predictions
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
• The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
• Density, viscosity and excess molar volume of binary mixtures of tri-n-octylamine + diluents (n-heptane, n-octane, n-nonane, and n-decane) at various temperatures
• Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium 2-(2-methoxyethoxy) ethylsulfate at T = (308.15, 313.15, 323.15 and 333.15) K using gas + liquid chromatography
• 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
• Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
• (Liquid + liquid) equilibrium at T = 298.15 K for ternary mixtures of alkane + aromatic compounds + imidazolium-based ionic liquids
• Excess molar enthalpies for binary mixtures of cyclopentanone, cyclohexanone, or cycloheptanone with n-nonane at T = 298.15 K and atmospheric pressure
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium methyl sulfate
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Thermodynamics of solvation in propylene glycol and methyl cellosolve
• Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
• Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
• 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 for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
• 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
• Activity coefficients at infinite dilution of alkanes, alkenes, alkyl benzenes in dimethylphosphate based ionic liquids using gas liquid chromatography
• Screening of environmental friendly ionic liquid as a solvent for the different types of separations problem: Insight from activity coefficients at infinite dilution measurement using (gas + liquid) chromatography technique
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Experimental determination of critical data of multi-component mixtures containing potential gasoline additives 2-butanol by a flow-type apparatus
• 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
• Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-hexyl-2,3-dimethylimidazolium bis(trifluoromethylsulfonyl)imide
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Activity coefficients at infinite dilution of hydrocarbons in glycols: Experimental data and thermodynamic modeling with the GCA-EoS
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Pressure dependence of the solubility of light fullerenes in n-nonane
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• Experiment and correlation of the equilibrium interfacial tension for paraffin + CO2 modified with ethanol
• Thermodynamics of mixtures containing aromatic nitriles
• 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
• Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
• 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
• Density, sound speed and derived thermophysical properties of n-nonane at temperatures between (283.15 and 473.15)K and at pressures up to 390MPa
• Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
• Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
• Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
• Liquid-liquid equilibria for (2-hydroxy benzaldehyde + n-alkane) mixtures. Intermolecular and proximity effects in systems containing hydroxyl and aldehyde groups
• Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
• Thermodynamic behaviour of the binary systems dimethyl carbonate + n-octane or n-nonane
• Calorimetric study of solvation of low polar solutes in propylene glycol and methyl cellosolve at 298 K
• Effect of halogen substitution on the enthalpies of solvation and hydrogen bonding of organic solutes in chlorobenzene and 1,2-dichlorobenzene derived using multi-parameter correlations
• Standard molar Gibbs free energy and enthalpy of solvation of lowpolar solutes in formamide derivatives at 298 K
• Thermodynamics of hydrogen bonding and van der Waals interactions of organic solutes in solutions of imidazolium based ionic liquids: "structure-property" relationships
• Bubble Point Measurements of n-Butane + n-Octane and n-Butane + n-Nonane Binary Mixtures
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
• Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
• Measurement and Correlation of High Pressure Phase Equilibria for CO2 + Alkanes and CO2 + Crude Oil Systems
• Simultaneous Measurement of Dynamic Viscosity and Density of n-Alkanes at High Pressures
• Vapor-Liquid Equilibrium Measurements of Ethanol and n-Nonane or n-Decane Binary Mixtures with Large Relative Volatility
• Determination of Activity Coefficients at Infinite Dilution of Organic Solutes in the Ionic Liquid 1-(2-Hydroxyethyl)-3-methylimidazolium Nonafluoro-1-butanesulfonate Using Gas-Liquid Chromatography
• P-rho-T Data and Modeling for Propan-1-ol + n-Octane or n-Nonane or n-Decane from 313.15 K to 363.15 K and 1 MPa to 20 MPa
• Measurement of Critical Properties for Binary and Ternary Mixtures Containing n-Butanol and n-Alkane
• Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
• Liquid Extraction of Toluene from Heptane, Octane, or Nonane Using Mixed Ionic Solvents of 1-Ethyl-3-methylimidazolium Methylsulfate and 1-Hexyl-3-methylimidazolium Hexafluorophosphate
• Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
• Measuring Activity Coefficient at Infinite Dilution of Hydrocarbons in Ionic Liquids and Evaluation of Other Thermodynamic Properties using Gas Chromatography
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• Infinite Dilution Activity Coefficients of Hydrocarbons in Triethylene Glycol and Tetraethylene Glycol
• Densities and Excess Molar Properties of Dimethyl Carbonate with Alkanes (C6 to C10) and VLE of Dimethyl Carbonate with Alkanes (C9 to C10) at 101.3 kPa
• Vapor-Liquid Equilibrium Studies for Systems Containing n-Butylisocyanate at Temperatures between 323.15 K and 371.15 K
• Solubility of Benzophenone in Binary Alkane + Carbon Tetrachloride Solvent Mixtures
• Liquid-Liquid Equilibria of Methyl Acetate + Methanol + Octane or Nonane
• Liquid-Liquid Equilibria for Monoethylene Glycol + Water + Alkane Systems in the Range (273 to 313) K and Atmospheric Pressure
• Isobaric Vapor-Liquid Equilibria of the Ternary System Methylbutyl Ketone + Nonane + Cyclohexanol
• Activity Coefficients at Infinite Dilution and Excess Molar Volumes in Binary Mixtures Containing Normal Alkanes (Nonane, Decane, Undecane, or Dodecane) and Cresols (2-Methylphenol or 3-Methylphenol)
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 5. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-butyl-imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 6. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-octyl-imidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
• Isobaric Vapor-Liquid Equilibria of the Ternary System Methylbutyl Ketone + 1-Pentanol + Nonane
• Activity Coefficients at Infinite Dilution of Cylcohexylamine + Octane, Toluene, Ethylbenzene, or Aniline and Excess Molar Volumes in Binary Mixtures of Cyclohexylamine + Heptane, Octane, Nonane, Decane, Undecane, Aniline, or Water
• 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
• Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
• Thermodynamics of Mixtures Containing a Strongly Polar Compound. 8. Liquid-Liquid Equilibria for N,N-Dialkylamide + Selected N-Alkanes
• 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
• Thermodynamic Properties of Mixtures Containing Ionic Liquids: Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Propyl Boronic Acid-3-Alkylimidazolium Bromide and 1-Propenyl-3-alkylimidazolium Bromide Using Inverse Gas Chromatography
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Isobaric Vapor-Liquid Equilibria of the Ternary System Dibutyl Ether + 1-Pentanol + Nonane
• Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
• Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
• Separation of Benzene from Linear Alkanes (C6-C9) Using 1-Ethyl-3-Methylimidazolium Ethylsulfate at T = 298.15 K
• Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
• Vapor-Liquid Equilibria and Density Measurement for Binary Mixtures of Benzene + Nonane, Methylbenzene + 1,2-Dimethylbenzene, 1,3-Dimethylbenzene + 2,3,4,5-Tetrahydrothiophene-1,1-dioxide (Sulfolane), 1,2-Dimethylbenzene + Sulfolane, 1,2-Dimethylbenzene + N-Methylformamide (NMF), 1,3-Dimethylbenzene + NMF, and 1,4-Dimethylbenzene + NMF from (333.15 to 353.15) K at Vacuum Conditions
• Liquid-Liquid Equilibria of the Ternary Systems of Alkane + Aromatic + 1-Ethylpyridinium Ethylsulfate Ionic Liquid at T = (283.15 and 298.15) K
• Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
• Isobaric Vapor-Liquid Equilibria of the Ternary System Pentan-1-ol + Pentyl Acetate + Nonane
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Butyl-3-methylimidazolium Nitrate Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Ethyl-3-methylimidazolium Diethylphosphate Using Gas Liquid Chromatography
• Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
• Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
• Vapor Liquid Equilibria of Binary and Ternary Systems Containing Carbon Dioxide, Alkane, and Benzothiophene
• Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
• Density, Refractive Index, Viscosity, and Surface Tension of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with Some n-Alkanes from (293.15 to 313.15) K
• Excess Molar Enthalpies of Ternary and Binary Mixtures Containing 2-Methoxy-2-Methylpropane, Ethanol, and Nonane
• Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Dibutylphosphate Using Gas Liquid Chromatography
• Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
• Measurements and Correlations of the Isobaric Vapor Liquid Equilibria of Binary Mixtures and Excess Properties for Mixtures Containing an Alkyl (Methyl, Ethyl) Butanoate with an Alkane (Heptane, Nonane) at 101.3 kPa
• Densities, Viscosities, and Refractive Indices of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene with Some n-Alkanes at T = (293.15 to 313.15) K
• Multiproperty Correlation of Experimental Data of the Binaries Propyl Ethanoate + Alkanes (Pentane to Decane). New Experimental Information for Vapor Liquid Equilibrium and Mixing Properties
• Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
• Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
• Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
• Improvements in the Experimentation and the Representation of Thermodynamic Properties (iso-p VLE and yE) of Alkyl Propanoate + Alkane Binaries
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Liquid Liquid Extraction of Toluene from n-Alkanes using {[4empy][Tf2N] + [emim][DCA]} Ionic Liquid Mixtures
• Comparison Study on Temperature Dependence of the Interfacial Tension of n-Alkane Water and n-Alcohol Water Two Binary Systems
• Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
• Determination of the Critical Properties of C6 C10 n-Alkanes and Their Binary Systems Using a Flow Apparatus
• Measurement of the Critical Properties of the Ternary Systems Hexane + Heptane + Octane and Octane + Nonane + Decane Using a Flow Apparatus
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
• Measurement of Activity Coefficient at Infinite Dilution of Hydrocarbons in Sulfolane Using Gas-Liquid Chromatography
• Densities and Viscosities of Ternary Mixtures of Heptane, Octane, Nonane, and Hexyl Benzene from 293.15 K to 313.15 K
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• Thermodynamics of Mixing Tetrahydrofuran with 1-Alkanols and Excess Enthalpies of Homomorphy-Related Systems
• Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
• Isobaric Vapor Liquid Equilibria of the Ternary System 1-Pentanol + Nonane Anisole
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Hexyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
• Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
• Thermophysical Characterization of Liquids Using Precise Density and Isobaric Heat Capacity Measurements As a Function of Pressure
• Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
• Excess Molar Enthalpies of Ternary and Binary Mixtures Containing 2-Methoxy-2-methylpropane, 1-Propanol, and Nonane
• Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Phase Equilibria of (1-Hexyl-3-methylimidazolium Thiocyanate + Water, Alcohol, or Hydrocarbon) Binary Systems
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
• Isobaric Thermal Expansivity for Nonpolar Compounds
• Thermodynamics of Mixtures Containing a Strongly Polar Compound. 9. Liquid-Liquid Equilibria for epsilon-Caprolactam + Selected Alkanes
• Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tris(pentafluoroethyl)trifluorophosphate [EMIM][FAP] Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure
• Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD

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