Chemical Properties of Toluene (CAS 108-88-3)

InChI

InChI=1S/C7H8/c1-7-5-3-2-4-6-7/h2-6H,1H3

InChI Key

YXFVVABEGXRONW-UHFFFAOYSA-N

Formula

C7H8

SMILES

Cc1ccccc1

Molecular Weight¹

92.14

CAS

108-88-3

Other Names

• Antisal 1a
• Benzene, methyl
• CP 25
• Dracyl
• Methacide
• Methane, phenyl-
• Methylbenzol
• Monomethyl benzene
• NCI-C07272
• NSC 406333
• Phenylmethane
• Rcra waste number U220
• Tolu-sol
• Tolueen
• Toluen
• Toluol
• Toluolo
• UN 1294
• methylbenzene
• methylbenzene (toluene)

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• C_sat : Molar heat capacity at saturation pressure (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• ε_r : Dielectric Constant (Relative permittivity).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_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 standard conditions (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.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• D^*_i : Self diffusion coefficient (m²/s).
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boil(P) : Boiling point at given pressure (K).
• T_boilr : Boiling point at reduced pressure (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• α_diff : Thermal diffusivity (m²/s).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• V_COSTALD : COSTALD Characteristic Volume (m³/kmol).
• ω_SRK : SRK acentric factor.
• 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. Pressure Dependent Properties
4. Datasets
5. Correlations
6. Similar Compounds
7. Mixtures
8. Sources

Physical Properties

Property	Value	Unit	Source
ω	[0.2570; 0.2640]
ω	0.2570		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2640		ChemSep v8.3 pure component data Compiled value
ω	0.2630		KDB
PAff	[782.40; 784.00]	kJ/mol
PAff	784.00	kJ/mol	NIST
PAff	782.40	kJ/mol	NIST
Tig	[753.15; 809.26]	K
Tig	809.26	K	KDB
Tig	753.15	K	NCMS SOLV-DB
BasG	[753.50; 756.30]	kJ/mol
BasG	756.30	kJ/mol	NIST
BasG	753.50	kJ/mol	NIST
ΔcH°liquid	[-3938.00; -3909.90]	kJ/mol
ΔcH°liquid	-3910.90 ± 0.46	kJ/mol	NIST
ΔcH°liquid	-3909.90 ± 0.50	kJ/mol	NIST
ΔcH°liquid	-3938.00	kJ/mol	NIST
ΔcH°liquid	-3913.00	kJ/mol	NIST
ΔcH°liquid	-3920.70	kJ/mol	NIST
ΔcH°liquid	-3927.00	kJ/mol	NIST
μ	[0.36; 0.40]	debye
μ	0.36	debye	ChemSep v8.3 pure component data Compiled value
μ	0.40	debye	KDB
η	[0.0005540; 0.0005641]	Pa×s
η	0.0005540	Pa×s	Liquid-Liquid Equilibrium Data, Density, Viscosity, and Interfacial Tension of Ternary System (Toluene-Acetic Acid-Water) at 298.15 K: Experiment and Correlation
η	0.0005641	Pa×s	Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
η	0.0005560	Pa×s	Densities and Viscosities for the Ternary Systems of Methyl tert-Butyl Ether + Methanol + Benzene and Methyl tert-Butyl Ether + Methanol + Toluene and Their Sub-binary Systems at 298.15 K
εr	2.38		NCMS SOLV-DB
LFL	1.27	% in Air	KDB
UFL	7.00	% in Air	KDB
Tflash,cc	[277.15; 285.93]	K
Tflash,cc	285.93	K	KDB
Tflash,cc	277.15	K	NCMS SOLV-DB
Tflash,oc	277.59	K	KDB
ΔfG°	[122.10; 122.20]	kJ/mol
ΔfG°	122.20	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	122.10	kJ/mol	KDB
Rg	3.4430		KDB
Δc,grossH	3909.95	kJ/mol	KDB
Δc,netH	3733.885	kJ/mol	KDB
ΔfH°gas	[48.00; 50.41]	kJ/mol
ΔfH°gas	50.41 ± 0.37	kJ/mol	Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas	50.17	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	50.03	kJ/mol	KDB
ΔfH°gas	50.10 ± 1.10	kJ/mol	NIST
ΔfH°gas	50.00 ± 0.63	kJ/mol	NIST
ΔfH°gas	Outlier 48.00	kJ/mol	NIST
ΔfH°liquid	[12.00; 12.00]	kJ/mol
ΔfH°liquid	12.00 ± 1.10	kJ/mol	NIST
ΔfH°liquid	12.00 ± 0.63	kJ/mol	NIST
ΔfusH°	7.93	kJ/mol	Joback Calculated Property
ΔsubH°	43.10	kJ/mol	NIST
ΔvapH°	[33.30; 38.14]	kJ/mol
ΔvapH°	37.99	kJ/mol	NCMS SOLV-DB
ΔvapH°	38.06	kJ/mol	NIST
ΔvapH°	38.10 ± 0.10	kJ/mol	NIST
ΔvapH°	37.79 ± 0.13	kJ/mol	NIST
ΔvapH°	38.00	kJ/mol	NIST
ΔvapH°	38.14	kJ/mol	NIST
ΔvapH°	38.00	kJ/mol	NIST
ΔvapH°	37.99	kJ/mol	NIST
ΔvapH°	38.00	kJ/mol	NIST
ΔvapH°	Outlier 33.30 ± 0.04	kJ/mol	NIST
IE	[8.67; 9.00]	eV
IE	8.83 ± 0.00	eV	NIST
IE	8.83 ± 0.00	eV	NIST
IE	8.79	eV	NIST
IE	8.80 ± 0.07	eV	NIST
IE	8.83	eV	NIST
IE	8.82	eV	NIST
IE	8.82	eV	NIST
IE	8.82	eV	NIST
IE	8.82 ± 0.01	eV	NIST
IE	8.84	eV	NIST
IE	8.82	eV	NIST
IE	8.81	eV	NIST
IE	8.80	eV	NIST
IE	8.78 ± 0.02	eV	NIST
IE	8.91	eV	NIST
IE	8.80 ± 0.10	eV	NIST
IE	8.72	eV	NIST
IE	Outlier 8.67	eV	NIST
IE	8.82	eV	NIST
IE	8.89 ± 0.03	eV	NIST
IE	8.71	eV	NIST
IE	8.82	eV	NIST
IE	8.80 ± 0.04	eV	NIST
IE	8.82 ± 0.02	eV	NIST
IE	8.82	eV	NIST
IE	8.82 ± 0.01	eV	NIST
IE	8.82 ± 0.05	eV	NIST
IE	8.82	eV	NIST
IE	8.85	eV	NIST
IE	Outlier 9.00	eV	NIST
IE	8.90 ± 0.03	eV	NIST
IE	8.82	eV	NIST
IE	8.85 ± 0.01	eV	NIST
IE	Outlier 9.00 ± 0.03	eV	NIST
log10WS	[-2.21; -2.21]
log10WS	-2.21		Aq. Solubility Prediction
log10WS	-2.21		Estimated Solubility
logPoct/wat	2.730		NCMS SOLV-DB
McVol	85.730	ml/mol	McGowan Calculated Property
NFPA Fire	[%!d(float64=3); %!d(float64=3)]
NFPA Fire	3		KDB
NFPA Fire	3		NCMS SOLV-DB
NFPA Health	[%!d(float64=2); %!d(float64=2)]
NFPA Health	2		KDB
NFPA Health	2		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	[4080.00; 4236.50]	kPa
Pc	4108.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value
Pc	4113.80	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4108.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	4108.00	kPa	KDB
Pc	4108.00 ± 10.00	kPa	NIST
Pc	4162.00 ± 50.00	kPa	NIST
Pc	4107.00 ± 20.00	kPa	NIST
Pc	Outlier 4236.50 ± 120.00	kPa	NIST
Pc	4109.00 ± 20.00	kPa	NIST
Pc	4106.60 ± 4.00	kPa	NIST
Pc	4108.70 ± 4.00	kPa	NIST
Pc	4235.80 ± 140.00	kPa	NIST
Pc	4109.00 ± 5.00	kPa	NIST
Pc	4220.00 ± 101.32	kPa	NIST
Pc	4080.00 ± 4.90	kPa	NIST
Ptriple	4.75e-05	kPa	ChemSep v8.3 pure component data Compiled value
ρc	[290.24; 292.08]	kg/m3
ρc	292.08 ± 0.92	kg/m3	NIST
ρc	291.16 ± 3.69	kg/m3	NIST
ρc	290.24 ± 4.61	kg/m3	NIST
ρc	291.16 ± 4.61	kg/m3	NIST
ρc	291.34 ± 4.61	kg/m3	NIST
Inp	[106.10; 796.80]
Inp	785.29		NIST
Inp	792.81		NIST
Inp	774.14		NIST
Inp	778.14		NIST
Inp	759.70		NIST
Inp	754.80		NIST
Inp	760.90		NIST
Inp	755.20		NIST
Inp	752.60		NIST
Inp	751.60		NIST
Inp	755.30		NIST
Inp	786.00		NIST
Inp	782.20		NIST
Inp	787.70		NIST
Inp	751.72		NIST
Inp	753.79		NIST
Inp	756.18		NIST
Inp	758.31		NIST
Inp	760.55		NIST
Inp	763.41		NIST
Inp	765.53		NIST
Inp	767.08		NIST
Inp	769.68		NIST
Inp	773.08		NIST
Inp	774.96		NIST
Inp	777.86		NIST
Inp	767.72		NIST
Inp	770.81		NIST
Inp	772.35		NIST
Inp	774.88		NIST
Inp	776.58		NIST
Inp	779.16		NIST
Inp	781.85		NIST
Inp	784.33		NIST
Inp	787.46		NIST
Inp	773.24		NIST
Inp	743.70		NIST
Inp	746.20		NIST
Inp	748.70		NIST
Inp	751.20		NIST
Inp	753.50		NIST
Inp	756.20		NIST
Inp	758.80		NIST
Inp	750.10		NIST
Inp	754.90		NIST
Inp	786.91		NIST
Inp	784.00		NIST
Inp	756.97		NIST
Inp	756.97		NIST
Inp	766.30		NIST
Inp	767.00		NIST
Inp	754.00		NIST
Inp	758.00		NIST
Inp	746.00		NIST
Inp	780.00		NIST
Inp	779.00		NIST
Inp	765.50		NIST
Inp	768.40		NIST
Inp	761.80		NIST
Inp	763.00		NIST
Inp	757.50		NIST
Inp	764.50		NIST
Inp	777.10		NIST
Inp	786.90		NIST
Inp	756.20		NIST
Inp	756.50		NIST
Inp	756.60		NIST
Inp	756.70		NIST
Inp	756.50		NIST
Inp	771.60		NIST
Inp	757.00		NIST
Inp	784.00		NIST
Inp	749.00		NIST
Inp	756.00		NIST
Inp	756.00		NIST
Inp	766.00		NIST
Inp	766.00		NIST
Inp	757.00		NIST
Inp	786.00		NIST
Inp	766.00		NIST
Inp	771.40		NIST
Inp	766.00		NIST
Inp	753.60		NIST
Inp	756.60		NIST
Inp	758.40		NIST
Inp	759.90		NIST
Inp	771.90		NIST
Inp	775.40		NIST
Inp	766.00		NIST
Inp	752.00		NIST
Inp	759.00		NIST
Inp	760.00		NIST
Inp	753.00		NIST
Inp	757.00		NIST
Inp	762.00		NIST
Inp	744.10		NIST
Inp	749.00		NIST
Inp	767.00		NIST
Inp	753.00		NIST
Inp	758.00		NIST
Inp	744.00		NIST
Inp	746.00		NIST
Inp	748.00		NIST
Inp	754.00		NIST
Inp	756.10		NIST
Inp	758.00		NIST
Inp	759.80		NIST
Inp	788.00		NIST
Inp	753.00		NIST
Inp	788.00		NIST
Inp	780.00		NIST
Inp	771.00		NIST
Inp	764.00		NIST
Inp	766.00		NIST
Inp	764.00		NIST
Inp	766.00		NIST
Inp	762.00		NIST
Inp	751.00		NIST
Inp	753.00		NIST
Inp	755.00		NIST
Inp	757.00		NIST
Inp	759.00		NIST
Inp	761.00		NIST
Inp	772.30		NIST
Inp	774.40		NIST
Inp	776.70		NIST
Inp	779.00		NIST
Inp	781.50		NIST
Inp	784.20		NIST
Inp	757.00		NIST
Inp	755.00		NIST
Inp	756.20		NIST
Inp	756.70		NIST
Inp	759.90		NIST
Inp	767.00		NIST
Inp	754.00		NIST
Inp	774.00		NIST
Inp	761.00		NIST
Inp	766.00		NIST
Inp	772.00		NIST
Inp	782.00		NIST
Inp	756.00		NIST
Inp	756.00		NIST
Inp	755.00		NIST
Inp	757.10		NIST
Inp	766.40		NIST
Inp	771.50		NIST
Inp	781.50		NIST
Inp	758.00		NIST
Inp	761.40		NIST
Inp	750.00		NIST
Inp	791.00		NIST
Inp	757.00		NIST
Inp	745.20		NIST
Inp	750.00		NIST
Inp	744.20		NIST
Inp	749.30		NIST
Inp	754.70		NIST
Inp	755.00		NIST
Inp	755.30		NIST
Inp	755.50		NIST
Inp	749.80		NIST
Inp	751.20		NIST
Inp	754.00		NIST
Inp	755.00		NIST
Inp	749.20		NIST
Inp	749.40		NIST
Inp	755.00		NIST
Inp	757.10		NIST
Inp	760.00		NIST
Inp	746.00		NIST
Inp	731.40		NIST
Inp	731.40		NIST
Inp	766.80		NIST
Inp	747.00		NIST
Inp	750.00		NIST
Inp	751.68		NIST
Inp	756.00		NIST
Inp	770.00		NIST
Inp	773.00		NIST
Inp	776.00		NIST
Inp	778.00		NIST
Inp	772.00		NIST
Inp	776.00		NIST
Inp	778.00		NIST
Inp	781.00		NIST
Inp	785.00		NIST
Inp	763.00		NIST
Inp	745.00		NIST
Inp	750.00		NIST
Inp	757.70		NIST
Inp	757.70		NIST
Inp	757.70		NIST
Inp	757.70		NIST
Inp	757.70		NIST
Inp	757.60		NIST
Inp	758.00		NIST
Inp	755.00		NIST
Inp	756.00		NIST
Inp	757.00		NIST
Inp	753.00		NIST
Inp	760.00		NIST
Inp	763.00		NIST
Inp	764.00		NIST
Inp	767.00		NIST
Inp	773.00		NIST
Inp	747.00		NIST
Inp	746.80		NIST
Inp	759.00		NIST
Inp	758.00		NIST
Inp	763.00		NIST
Inp	754.70		NIST
Inp	758.00		NIST
Inp	761.10		NIST
Inp	760.70		NIST
Inp	754.20		NIST
Inp	788.00		NIST
Inp	740.60		NIST
Inp	747.00		NIST
Inp	751.00		NIST
Inp	756.00		NIST
Inp	789.00		NIST
Inp	796.00		NIST
Inp	783.00		NIST
Inp	756.00		NIST
Inp	763.00		NIST
Inp	769.00		NIST
Inp	753.00		NIST
Inp	756.40		NIST
Inp	756.00		NIST
Inp	738.00		NIST
Inp	739.00		NIST
Inp	742.00		NIST
Inp	750.00		NIST
Inp	752.00		NIST
Inp	767.00		NIST
Inp	757.00		NIST
Inp	787.00		NIST
Inp	759.00		NIST
Inp	750.00		NIST
Inp	753.00		NIST
Inp	756.00		NIST
Inp	747.00		NIST
Inp	751.00		NIST
Inp	757.00		NIST
Inp	748.00		NIST
Inp	752.00		NIST
Inp	756.00		NIST
Inp	748.00		NIST
Inp	751.00		NIST
Inp	761.00		NIST
Inp	751.00		NIST
Inp	755.00		NIST
Inp	776.00		NIST
Inp	768.00		NIST
Inp	772.00		NIST
Inp	756.00		NIST
Inp	748.00		NIST
Inp	752.00		NIST
Inp	761.00		NIST
Inp	751.00		NIST
Inp	755.00		NIST
Inp	752.00		NIST
Inp	744.00		NIST
Inp	749.00		NIST
Inp	758.00		NIST
Inp	749.00		NIST
Inp	753.00		NIST
Inp	758.00		NIST
Inp	769.00		NIST
Inp	748.00		NIST
Inp	755.00		NIST
Inp	763.00		NIST
Inp	746.00		NIST
Inp	758.00		NIST
Inp	748.00		NIST
Inp	764.00		NIST
Inp	765.00		NIST
Inp	776.00		NIST
Inp	776.00		NIST
Inp	759.00		NIST
Inp	752.00		NIST
Inp	755.00		NIST
Inp	788.20		NIST
Inp	760.00		NIST
Inp	771.00		NIST
Inp	771.00		NIST
Inp	769.00		NIST
Inp	779.20		NIST
Inp	796.80		NIST
Inp	765.00		NIST
Inp	784.00		NIST
Inp	779.00		NIST
Inp	773.00		NIST
Inp	784.00		NIST
Inp	769.00		NIST
Inp	775.00		NIST
Inp	776.00		NIST
Inp	755.40		NIST
Inp	750.00		NIST
Inp	760.00		NIST
Inp	747.02		NIST
Inp	747.41		NIST
Inp	744.00		NIST
Inp	758.90		NIST
Inp	761.30		NIST
Inp	761.70		NIST
Inp	770.80		NIST
Inp	773.00		NIST
Inp	766.00		NIST
Inp	776.00		NIST
Inp	760.00		NIST
Inp	752.00		NIST
Inp	756.50		NIST
Inp	761.00		NIST
Inp	751.50		NIST
Inp	771.00		NIST
Inp	760.00		NIST
Inp	757.00		NIST
Inp	777.00		NIST
Inp	742.00		NIST
Inp	768.00		NIST
Inp	756.00		NIST
Inp	756.00		NIST
Inp	762.90		NIST
Inp	746.50		NIST
Inp	747.10		NIST
Inp	750.10		NIST
Inp	753.20		NIST
Inp	767.60		NIST
Inp	758.90		NIST
Inp	761.30		NIST
Inp	761.70		NIST
Inp	751.00		NIST
Inp	748.39		NIST
Inp	749.03		NIST
Inp	762.00		NIST
Inp	751.00		NIST
Inp	754.00		NIST
Inp	748.65		NIST
Inp	749.00		NIST
Inp	749.00		NIST
Inp	775.00		NIST
Inp	759.00		NIST
Inp	756.80		NIST
Inp	753.40		NIST
Inp	752.80		NIST
Inp	763.00		NIST
Inp	763.00		NIST
Inp	746.99		NIST
Inp	749.29		NIST
Inp	750.81		NIST
Inp	761.89		NIST
Inp	764.46		NIST
Inp	766.26		NIST
Inp	764.00		NIST
Inp	755.27		NIST
Inp	754.08		NIST
Inp	752.00		NIST
Inp	751.88		NIST
Inp	748.00		NIST
Inp	730.00		NIST
Inp	754.00		NIST
Inp	781.00		NIST
Inp	762.00		NIST
Inp	762.00		NIST
Inp	762.00		NIST
Inp	768.00		NIST
Inp	771.00		NIST
Inp	778.00		NIST
Inp	754.00		NIST
Inp	756.00		NIST
Inp	770.00		NIST
Inp	765.30		NIST
Inp	771.00		NIST
Inp	760.00		NIST
Inp	751.00		NIST
Inp	761.00		NIST
Inp	744.00		NIST
Inp	764.00		NIST
Inp	766.00		NIST
Inp	760.00		NIST
Inp	763.00		NIST
Inp	766.00		NIST
Inp	771.00		NIST
Inp	776.00		NIST
Inp	761.00		NIST
Inp	772.00		NIST
Inp	757.00		NIST
Inp	754.00		NIST
Inp	764.00		NIST
Inp	766.00		NIST
Inp	766.00		NIST
Inp	766.00		NIST
Inp	767.00		NIST
Inp	757.00		NIST
Inp	763.00		NIST
Inp	766.00		NIST
Inp	766.00		NIST
Inp	770.00		NIST
Inp	772.00		NIST
Inp	760.00		NIST
Inp	760.00		NIST
Inp	762.00		NIST
Inp	763.00		NIST
Inp	758.00		NIST
Inp	758.00		NIST
Inp	759.00		NIST
Inp	769.00		NIST
Inp	771.00		NIST
Inp	771.00		NIST
Inp	772.00		NIST
Inp	773.00		NIST
Inp	774.00		NIST
Inp	776.00		NIST
Inp	745.00		NIST
Inp	754.00		NIST
Inp	758.00		NIST
Inp	770.00		NIST
Inp	760.00		NIST
Inp	746.00		NIST
Inp	759.00		NIST
Inp	792.00		NIST
Inp	743.00		NIST
Inp	769.00		NIST
Inp	768.00		NIST
Inp	756.00		NIST
Inp	759.00		NIST
Inp	757.00		NIST
Inp	751.00		NIST
Inp	762.00		NIST
Inp	763.00		NIST
Inp	769.00		NIST
Inp	765.00		NIST
Inp	766.00		NIST
Inp	766.00		NIST
Inp	759.00		NIST
Inp	771.00		NIST
Inp	757.00		NIST
Inp	773.00		NIST
Inp	758.00		NIST
Inp	770.00		NIST
Inp	770.00		NIST
Inp	753.00		NIST
Inp	746.00		NIST
Inp	746.00		NIST
Inp	750.00		NIST
Inp	750.00		NIST
Inp	750.00		NIST
Inp	756.00		NIST
Inp	756.00		NIST
Inp	766.10		NIST
Inp	766.00		NIST
Inp	773.00		NIST
Inp	753.00		NIST
Inp	776.00		NIST
Inp	745.00		NIST
Inp	748.00		NIST
Inp	772.00		NIST
Inp	771.00		NIST
Inp	764.00		NIST
Inp	773.00		NIST
Inp	773.00		NIST
Inp	768.00		NIST
Inp	741.00		NIST
Inp	742.00		NIST
Inp	766.00		NIST
Inp	761.00		NIST
Inp	776.00		NIST
Inp	769.00		NIST
Inp	770.00		NIST
Inp	761.00		NIST
Inp	753.20		NIST
Inp	751.13		NIST
Inp	770.00		NIST
Inp	769.00		NIST
Inp	753.00		NIST
Inp	754.00		NIST
Inp	756.00		NIST
Inp	779.00		NIST
Inp	752.00		NIST
Inp	771.20		NIST
Inp	744.00		NIST
Inp	750.00		NIST
Inp	765.00		NIST
Inp	765.00		NIST
Inp	748.00		NIST
Inp	752.00		NIST
Inp	756.00		NIST
Inp	743.00		NIST
Inp	746.00		NIST
Inp	746.00		NIST
Inp	771.00		NIST
Inp	774.00		NIST
Inp	774.00		NIST
Inp	752.00		NIST
Inp	752.00		NIST
Inp	756.00		NIST
Inp	756.00		NIST
Inp	764.00		NIST
Inp	748.00		NIST
Inp	748.00		NIST
Inp	749.00		NIST
Inp	753.00		NIST
Inp	760.00		NIST
Inp	765.00		NIST
Inp	748.70		NIST
Inp	752.00		NIST
Inp	750.00		NIST
Inp	748.00		NIST
Inp	748.00		NIST
Inp	748.00		NIST
Inp	734.00		NIST
Inp	753.00		NIST
Inp	761.00		NIST
Inp	760.00		NIST
Inp	771.00		NIST
Inp	776.00		NIST
Inp	764.00		NIST
Inp	759.00		NIST
Inp	756.00		NIST
Inp	772.00		NIST
Inp	761.00		NIST
Inp	746.00		NIST
Inp	750.00		NIST
Inp	769.00		NIST
Inp	764.00		NIST
Inp	763.00		NIST
Inp	770.00		NIST
Inp	746.00		NIST
Inp	765.00		NIST
Inp	776.00		NIST
Inp	756.00		NIST
Inp	767.00		NIST
Inp	772.00		NIST
Inp	780.00		NIST
Inp	773.00		NIST
Inp	780.00		NIST
Inp	780.00		NIST
Inp	766.00		NIST
Inp	759.00		NIST
Inp	746.00		NIST
Inp	776.00		NIST
Inp	774.00		NIST
Inp	769.00		NIST
Inp	753.00		NIST
Inp	752.00		NIST
Inp	772.00		NIST
Inp	772.00		NIST
Inp	766.00		NIST
Inp	760.00		NIST
Inp	767.00		NIST
Inp	772.00		NIST
Inp	770.00		NIST
Inp	769.00		NIST
Inp	744.20		NIST
Inp	766.00		NIST
Inp	780.00		NIST
Inp	766.00		NIST
Inp	756.00		NIST
Inp	769.00		NIST
Inp	751.00		NIST
Inp	755.00		NIST
Inp	756.00		NIST
Inp	771.00		NIST
Inp	773.00		NIST
Inp	756.00		NIST
Inp	760.00		NIST
Inp	751.00		NIST
Inp	778.00		NIST
Inp	763.00		NIST
Inp	760.00		NIST
Inp	770.00		NIST
Inp	768.00		NIST
Inp	764.00		NIST
Inp	760.00		NIST
Inp	766.00		NIST
Inp	760.00		NIST
Inp	760.00		NIST
Inp	765.00		NIST
Inp	752.00		NIST
Inp	760.00		NIST
Inp	749.00		NIST
Inp	758.00		NIST
Inp	749.00		NIST
Inp	763.00		NIST
Inp	768.00		NIST
Inp	763.00		NIST
Inp	760.70		NIST
Inp	768.50		NIST
Inp	769.00		NIST
Inp	768.00		NIST
Inp	757.60		NIST
Inp	771.00		NIST
Inp	766.00		NIST
Inp	751.00		NIST
Inp	755.00		NIST
Inp	739.00		NIST
Inp	748.00		NIST
Inp	763.00		NIST
Inp	771.00		NIST
Inp	764.00		NIST
Inp	734.00		NIST
Inp	745.00		NIST
Inp	748.00		NIST
Inp	751.00		NIST
Inp	752.00		NIST
Inp	753.00		NIST
Inp	761.00		NIST
Inp	764.00		NIST
Inp	767.00		NIST
Inp	756.00		NIST
Inp	749.00		NIST
Inp	770.00		NIST
Inp	755.00		NIST
Inp	770.00		NIST
Inp	755.00		NIST
Inp	Outlier 106.10		NIST
Inp	Outlier 106.10		NIST
Inp	Outlier 112.43		NIST
Inp	Outlier 112.62		NIST
Inp	Outlier 111.93		NIST
Inp	760.00		NIST
Inp	756.00		NIST
Inp	769.00		NIST
Inp	765.00		NIST
Inp	780.00		NIST
Inp	759.00		NIST
Inp	753.00		NIST
Inp	744.20		NIST
Inp	773.00		NIST
Inp	763.00		NIST
Inp	752.00		NIST
Inp	751.00		NIST
Inp	771.00		NIST
Inp	767.00		NIST
Inp	770.00		NIST
Inp	766.00		NIST
Inp	776.00		NIST
Inp	764.00		NIST
Inp	757.00		NIST
Inp	772.00		NIST
Inp	758.00		NIST
Inp	745.00		NIST
Inp	746.00		NIST
Inp	768.00		NIST
Inp	785.29		NIST
Inp	754.80		NIST
Inp	755.30		NIST
Inp	753.79		NIST
Inp	765.53		NIST
Inp	777.86		NIST
Inp	776.58		NIST
Inp	773.24		NIST
Inp	753.50		NIST
Inp	786.91		NIST
Inp	779.00		NIST
Inp	757.50		NIST
Inp	756.50		NIST
Inp	771.40		NIST
Inp	759.90		NIST
Inp	744.10		NIST
Inp	744.00		NIST
Inp	776.70		NIST
Inp	755.00		NIST
Inp	754.00		NIST
Inp	782.00		NIST
Inp	766.40		NIST
Inp	750.00		NIST
Inp	755.50		NIST
Inp	749.20		NIST
Inp	781.00		NIST
Inp	757.70		NIST
Inp	757.60		NIST
Inp	754.20		NIST
Inp	738.00		NIST
Inp	748.00		NIST
Inp	761.00		NIST
Inp	762.00		NIST
Inp	778.00		NIST
Inp	766.10		NIST
Inp	771.20		NIST
Inp	748.70		NIST
Inp	Outlier 106.10		NIST
Ip	[1011.00; 1093.00]
Ip	1077.50		NIST
Ip	Outlier 1088.30		NIST
Ip	1043.09		NIST
Ip	1049.50		NIST
Ip	1057.61		NIST
Ip	1068.53		NIST
Ip	1076.25		NIST
Ip	Outlier 1084.20		NIST
Ip	1026.00		NIST
Ip	1030.00		NIST
Ip	1039.50		NIST
Ip	1052.30		NIST
Ip	1054.20		NIST
Ip	1057.00		NIST
Ip	1067.04		NIST
Ip	1071.62		NIST
Ip	1076.10		NIST
Ip	1053.89		NIST
Ip	1057.98		NIST
Ip	1062.76		NIST
Ip	1049.50		NIST
Ip	1068.20		NIST
Ip	1073.30		NIST
Ip	1078.40		NIST
Ip	Outlier 1083.40		NIST
Ip	Outlier 1088.50		NIST
Ip	1054.00		NIST
Ip	1054.00		NIST
Ip	1069.70		NIST
Ip	1072.90		NIST
Ip	1073.40		NIST
Ip	1069.70		NIST
Ip	Outlier 1090.90		NIST
Ip	1043.20		NIST
Ip	1027.10		NIST
Ip	1077.00		NIST
Ip	1077.00		NIST
Ip	Outlier 1093.00		NIST
Ip	1071.00		NIST
Ip	1078.00		NIST
Ip	Outlier 1085.00		NIST
Ip	1064.00		NIST
Ip	1066.00		NIST
Ip	1042.00		NIST
Ip	1037.00		NIST
Ip	1042.00		NIST
Ip	1042.00		NIST
Ip	1040.00		NIST
Ip	1041.00		NIST
Ip	1037.00		NIST
Ip	1041.00		NIST
Ip	1019.00		NIST
Ip	1038.00		NIST
Ip	1066.00		NIST
Ip	1055.00		NIST
Ip	1036.00		NIST
Ip	1027.00		NIST
Ip	1034.00		NIST
Ip	1017.00		NIST
Ip	1029.00		NIST
Ip	1046.00		NIST
Ip	1075.00		NIST
Ip	1073.00		NIST
Ip	1033.00		NIST
Ip	1014.00		NIST
Ip	1056.00		NIST
Ip	1029.00		NIST
Ip	1028.00		NIST
Ip	1041.00		NIST
Ip	1041.00		NIST
Ip	1033.00		NIST
Ip	1040.00		NIST
Ip	1039.00		NIST
Ip	1033.00		NIST
Ip	1040.00		NIST
Ip	1043.00		NIST
Ip	1049.00		NIST
Ip	1031.00		NIST
Ip	1024.00		NIST
Ip	1041.00		NIST
Ip	1033.00		NIST
Ip	1044.00		NIST
Ip	1058.00		NIST
Ip	1042.00		NIST
Ip	1040.00		NIST
Ip	1028.00		NIST
Ip	1039.00		NIST
Ip	1036.00		NIST
Ip	1049.00		NIST
Ip	1040.00		NIST
Ip	1037.00		NIST
Ip	1042.00		NIST
Ip	1070.00		NIST
Ip	1035.00		NIST
Ip	1051.00		NIST
Ip	1019.00		NIST
Ip	1015.00		NIST
Ip	1025.00		NIST
Ip	1042.00		NIST
Ip	1040.00		NIST
Ip	1043.00		NIST
Ip	1022.00		NIST
Ip	1027.00		NIST
Ip	1061.00		NIST
Ip	1035.00		NIST
Ip	1040.00		NIST
Ip	1043.00		NIST
Ip	1035.00		NIST
Ip	1035.00		NIST
Ip	1035.00		NIST
Ip	1058.00		NIST
Ip	1047.00		NIST
Ip	1038.00		NIST
Ip	1034.00		NIST
Ip	1033.00		NIST
Ip	1050.00		NIST
Ip	1073.00		NIST
Ip	Outlier 1083.00		NIST
Ip	1052.00		NIST
Ip	1062.00		NIST
Ip	1065.00		NIST
Ip	1056.00		NIST
Ip	1058.00		NIST
Ip	1068.00		NIST
Ip	1077.00		NIST
Ip	1041.00		NIST
Ip	1048.00		NIST
Ip	1027.00		NIST
Ip	1038.00		NIST
Ip	1070.00		NIST
Ip	Outlier 1093.00		NIST
Ip	1028.00		NIST
Ip	1022.00		NIST
Ip	1059.00		NIST
Ip	1040.00		NIST
Ip	1061.00		NIST
Ip	1029.00		NIST
Ip	1047.00		NIST
Ip	1051.00		NIST
Ip	1043.00		NIST
Ip	1051.00		NIST
Ip	1051.00		NIST
Ip	1027.00		NIST
Ip	1026.00		NIST
Ip	1065.00		NIST
Ip	1041.00		NIST
Ip	1020.00		NIST
Ip	1029.00		NIST
Ip	1059.00		NIST
Ip	1034.00		NIST
Ip	1037.00		NIST
Ip	1030.00		NIST
Ip	1026.00		NIST
Ip	1059.00		NIST
Ip	1017.00		NIST
Ip	1019.00		NIST
Ip	1040.00		NIST
Ip	1031.00		NIST
Ip	1040.00		NIST
Ip	1055.00		NIST
Ip	1041.00		NIST
Ip	1037.00		NIST
Ip	1031.00		NIST
Ip	1036.00		NIST
Ip	1011.00		NIST
Ip	1029.00		NIST
Ip	1043.00		NIST
Ip	1038.00		NIST
Ip	1060.00		NIST
Ip	1038.00		NIST
Ip	1047.00		NIST
Ip	1017.00		NIST
Ip	1035.00		NIST
Ip	1024.00		NIST
Ip	1017.00		NIST
Ip	1035.00		NIST
Ip	1035.00		NIST
Ip	1055.00		NIST
Ip	1039.00		NIST
Ip	1040.00		NIST
Ip	1042.00		NIST
Ip	1040.00		NIST
Ip	1069.00		NIST
Ip	1043.00		NIST
Ip	1026.00		NIST
Ip	1030.00		NIST
Ip	Outlier 1081.00		NIST
Ip	1061.00		NIST
Ip	1040.00		NIST
Ip	1043.00		NIST
Ip	1043.00		NIST
Ip	1042.00		NIST
Ip	1026.00		NIST
Ip	1023.00		NIST
Ip	1023.00		NIST
Ip	1043.00		NIST
Ip	1033.00		NIST
Ip	1036.00		NIST
Ip	1023.00		NIST
Ip	1050.00		NIST
Ip	1027.00		NIST
Ip	1043.00		NIST
Ip	1012.00		NIST
Ip	1034.00		NIST
Ip	1047.00		NIST
Ip	1058.00		NIST
Ip	1051.00		NIST
Ip	1050.00		NIST
Ip	1031.00		NIST
Ip	1032.00		NIST
Ip	1043.00		NIST
Ip	1051.00		NIST
Ip	1032.00		NIST
Ip	1027.00		NIST
Ip	1027.00		NIST
Ip	1037.00		NIST
Ip	1054.00		NIST
Ip	1035.00		NIST
Ip	1028.00		NIST
Ip	1029.00		NIST
Ip	1051.00		NIST
Ip	1020.00		NIST
Ip	1030.00		NIST
Ip	1040.00		NIST
Ip	1037.00		NIST
Ip	1043.00		NIST
Ip	1017.00		NIST
Ip	1035.00		NIST
S°liquid	[219.20; 220.96]	J/mol×K
S°liquid	220.96	J/mol×K	NIST
S°liquid	219.20	J/mol×K	NIST
Tboil	[373.00; 386.15]	K
Tboil	383.76	K	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Tboil	383.77	K	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Tboil	383.40	K	Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
Tboil	383.80	K	Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
Tboil	383.69	K	Isobaric vapor-liquid equilibrium for four binary systems of 3-methylthiophene
Tboil	383.40	K	Isobaric vapor-liquid equilibrium for binary systemsof toluene + o-xylene, benzene + o-xylene, nonane + benzene and nonane + heptane at 101.3 kPa
Tboil	383.81	K	Isobaric vapor-liquid equilibrium for binary system of cinnamaldehyde + benzaldehyde at 10, 20 and 30 kPa
Tboil	383.39	K	Isobaric vapour + liquid equilibria for three binary systems (toluene + anisole, nbutylbenzene + anisole, and guaiacol + anisole) at 101.33 kPa
Tboil	383.73	K	Isobaric vapor-liquid equilibrium for binary and ternary systems with toluene, 2-methoxyethanol and dimethyl sulfoxide at 101.3 kPa
Tboil	383.95	K	Isobaric (vapour + liquid) equilibria for sulfolane with toluene, ethylbenzene, and isopropylbenzene at 101.33 kPa
Tboil	383.60	K	A new analysis method for improving collection of vapor-liquid equilibrium (VLE) data of binary mixtures using differential scanning calorimetry (DSC)
Tboil	383.82	K	Isobaric Vapor Liquid Equilibrium for Binary and Ternary Systems of Isoamyl Alcohol + Isoamyl Acetate + Dimethyl Sulfoxide at 101.33 kPa
Tboil	383.75	K	Vapor-Liquid Equilibrium of Ferrocene in Some Organic Solvents Using Spectroscopic Methods
Tboil	383.55	K	Isobaric Vapor-Liquid Equilibrium for Binary Systems of Toluene + Ethanol, Toluene + Isopropanol at (101.3, 121.3, 161.3 and 201.3) kPa
Tboil	383.79	K	ChemSep v8.3 pure component data Compiled value
Tboil	383.78	K	KDB
Tboil	383.78	K	NCMS SOLV-DB
Tboil	383.80 ± 0.30	K	NIST
Tboil	383.60 ± 0.40	K	NIST
Tboil	383.77 ± 0.20	K	NIST
Tboil	383.79 ± 0.15	K	NIST
Tboil	383.75 ± 0.20	K	NIST
Tboil	383.73 ± 0.10	K	NIST
Tboil	383.65 ± 0.30	K	NIST
Tboil	383.70 ± 0.30	K	NIST
Tboil	383.80	K	NIST
Tboil	383.85 ± 0.15	K	NIST
Tboil	383.73 ± 0.08	K	NIST
Tboil	383.85 ± 0.20	K	NIST
Tboil	383.84 ± 0.10	K	NIST
Tboil	383.80	K	NIST
Tboil	383.75 ± 0.30	K	NIST
Tboil	383.75 ± 0.30	K	NIST
Tboil	383.83 ± 0.10	K	NIST
Tboil	383.80 ± 0.30	K	NIST
Tboil	383.80 ± 0.40	K	NIST
Tboil	383.00 ± 1.00	K	NIST
Tboil	383.80 ± 0.15	K	NIST
Tboil	383.75 ± 0.50	K	NIST
Tboil	383.15 ± 0.20	K	NIST
Tboil	383.75 ± 0.30	K	NIST
Tboil	383.50 ± 0.60	K	NIST
Tboil	383.80 ± 0.40	K	NIST
Tboil	383.80 ± 0.40	K	NIST
Tboil	383.73 ± 0.20	K	NIST
Tboil	383.93 ± 0.15	K	NIST
Tboil	383.60 ± 0.50	K	NIST
Tboil	383.71 ± 0.15	K	NIST
Tboil	383.77 ± 0.15	K	NIST
Tboil	383.95 ± 0.20	K	NIST
Tboil	383.45 ± 0.30	K	NIST
Tboil	383.80 ± 0.30	K	NIST
Tboil	383.90 ± 0.50	K	NIST
Tboil	383.85 ± 0.30	K	NIST
Tboil	383.90 ± 0.20	K	NIST
Tboil	383.80 ± 0.50	K	NIST
Tboil	385.00 ± 4.00	K	NIST
Tboil	383.75 ± 0.30	K	NIST
Tboil	383.75 ± 0.20	K	NIST
Tboil	383.78 ± 0.15	K	NIST
Tboil	383.50 ± 0.30	K	NIST
Tboil	383.80 ± 0.50	K	NIST
Tboil	383.80 ± 0.10	K	NIST
Tboil	383.77 ± 0.12	K	NIST
Tboil	383.75 ± 0.20	K	NIST
Tboil	383.75 ± 0.50	K	NIST
Tboil	383.90 ± 0.30	K	NIST
Tboil	384.70 ± 2.00	K	NIST
Tboil	383.78 ± 0.30	K	NIST
Tboil	383.40 ± 2.00	K	NIST
Tboil	Outlier 375.00 ± 10.00	K	NIST
Tboil	383.80 ± 0.60	K	NIST
Tboil	Outlier 373.00 ± 10.00	K	NIST
Tboil	383.80 ± 0.40	K	NIST
Tboil	384.00 ± 0.50	K	NIST
Tboil	383.85 ± 0.30	K	NIST
Tboil	383.75 ± 0.50	K	NIST
Tboil	383.70 ± 0.40	K	NIST
Tboil	383.74 ± 0.08	K	NIST
Tboil	383.80 ± 0.60	K	NIST
Tboil	383.80 ± 0.20	K	NIST
Tboil	383.95 ± 0.30	K	NIST
Tboil	384.02 ± 0.30	K	NIST
Tboil	383.45 ± 0.50	K	NIST
Tboil	383.00 ± 2.00	K	NIST
Tboil	385.15 ± 5.00	K	NIST
Tboil	383.80 ± 0.40	K	NIST
Tboil	383.65 ± 2.00	K	NIST
Tboil	384.00 ± 0.15	K	NIST
Tboil	383.80 ± 0.30	K	NIST
Tboil	383.77 ± 0.02	K	NIST
Tboil	383.77 ± 0.27	K	NIST
Tboil	383.79 ± 0.20	K	NIST
Tboil	383.80 ± 0.50	K	NIST
Tboil	383.95 ± 0.50	K	NIST
Tboil	383.65 ± 0.50	K	NIST
Tboil	383.20 ± 0.50	K	NIST
Tboil	384.00 ± 0.50	K	NIST
Tboil	383.80 ± 0.00	K	NIST
Tboil	383.90 ± 0.40	K	NIST
Tboil	383.90 ± 0.30	K	NIST
Tboil	383.77 ± 0.05	K	NIST
Tboil	383.73 ± 0.20	K	NIST
Tboil	383.85 ± 0.30	K	NIST
Tboil	384.00 ± 0.30	K	NIST
Tboil	383.15 ± 0.50	K	NIST
Tboil	383.77 ± 0.05	K	NIST
Tboil	384.00 ± 0.15	K	NIST
Tboil	383.85 ± 0.25	K	NIST
Tboil	Outlier 380.65 ± 2.00	K	NIST
Tboil	Outlier 380.15 ± 2.00	K	NIST
Tboil	384.00 ± 0.60	K	NIST
Tboil	383.77 ± 0.10	K	NIST
Tboil	383.95 ± 0.30	K	NIST
Tboil	383.80 ± 0.20	K	NIST
Tboil	383.95 ± 0.20	K	NIST
Tboil	386.15 ± 1.50	K	NIST
Tboil	383.70 ± 0.20	K	NIST
Tboil	383.65 ± 3.00	K	NIST
Tboil	383.65 ± 0.40	K	NIST
Tboil	381.00 ± 6.00	K	NIST
Tboil	383.95 ± 0.20	K	NIST
Tboil	383.55 ± 0.50	K	NIST
Tboil	383.89 ± 0.06	K	NIST
Tboil	384.00 ± 2.00	K	NIST
Tboil	383.70 ± 0.30	K	NIST
Tboil	383.65 ± 1.00	K	NIST
Tboil	383.90 ± 0.30	K	NIST
Tboil	383.82 ± 0.20	K	NIST
Tboil	383.95 ± 0.20	K	NIST
Tboil	383.65 ± 2.00	K	NIST
Tboil	383.70 ± 0.20	K	NIST
Tboil	383.70 ± 0.25	K	NIST
Tboil	383.85 ± 0.20	K	NIST
Tboil	383.85 ± 0.20	K	NIST
Tboil	383.71 ± 0.30	K	NIST
Tboil	Outlier 376.65 ± 0.20	K	NIST
Tboil	382.65 ± 2.00	K	NIST
Tboil	384.00 ± 1.00	K	NIST
Tboil	383.00 ± 2.00	K	NIST
Tboil	383.71 ± 0.15	K	NIST
Tboil	382.65 ± 0.30	K	NIST
Tboil	383.85 ± 0.30	K	NIST
Tboil	383.85 ± 0.20	K	NIST
Tboil	382.70 ± 0.30	K	NIST
Tboil	383.01 ± 0.30	K	NIST
Tboil	383.75 ± 0.50	K	NIST
Tboil	383.00 ± 2.00	K	NIST
Tboil	384.15 ± 1.00	K	NIST
Tc	[591.50; 594.00]	K
Tc	591.89	K	Measurements of the isochoric heat capacity, the critical point (TC, nC) and vapor liquid coexistence curve (TS, nS) of high-purity toluene near the critical point*
Tc	591.75	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value
Tc	591.70	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	591.75	K	ChemSep v8.3 pure component data Compiled value
Tc	591.75	K	KDB
Tc	591.75 ± 0.15	K	NIST
Tc	592.50 ± 1.00	K	NIST
Tc	591.55 ± 0.20	K	NIST
Tc	591.50 ± 0.60	K	NIST
Tc	593.91 ± 2.00	K	NIST
Tc	593.00 ± 1.00	K	NIST
Tc	591.79 ± 0.07	K	NIST
Tc	591.80 ± 0.07	K	NIST
Tc	591.70	K	NIST
Tc	592.40 ± 0.60	K	NIST
Tc	592.00 ± 0.59	K	NIST
Tc	594.00 ± 2.00	K	NIST
Tc	591.72 ± 0.20	K	NIST
Tc	591.95 ± 0.10	K	NIST
Tc	591.80 ± 0.15	K	NIST
Tc	593.10 ± 1.50	K	NIST
Tc	594.00 ± 3.00	K	NIST
Tc	594.00 ± 3.00	K	NIST
Tc	593.80 ± 2.00	K	NIST
Tc	594.00 ± 2.00	K	NIST
Tfus	[176.60; 179.20]	K
Tfus	178.10	K	Phase equilibria of didecyldimethylammonium nitrate ionic liquid with water and organic solvents
Tfus	Outlier 179.20	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	178.18	K	ChemSep v8.3 pure component data Compiled value
Tfus	178.16	K	KDB
Tfus	Outlier 179.18	K	Aq. Solubility Prediction
Tfus	178.16	K	NCMS SOLV-DB
Tfus	178.17	K	NIST
Tfus	178.16	K	NIST
Tfus	178.15 ± 0.20	K	NIST
Tfus	178.15 ± 0.20	K	NIST
Tfus	178.15 ± 0.20	K	NIST
Tfus	178.16 ± 0.05	K	NIST
Tfus	178.15 ± 5.00	K	NIST
Tfus	178.13 ± 0.15	K	NIST
Tfus	Outlier 177.15 ± 10.00	K	NIST
Tfus	177.70 ± 0.50	K	NIST
Tfus	178.11 ± 0.01	K	NIST
Tfus	178.14 ± 0.15	K	NIST
Tfus	177.92 ± 0.20	K	NIST
Tfus	177.55 ± 0.20	K	NIST
Tfus	178.15 ± 2.00	K	NIST
Tfus	177.90 ± 0.20	K	NIST
Tfus	178.00 ± 2.00	K	NIST
Tfus	178.15 ± 0.40	K	NIST
Tfus	178.10 ± 0.40	K	NIST
Tfus	178.00 ± 0.15	K	NIST
Tfus	178.15 ± 0.15	K	NIST
Tfus	178.20 ± 0.50	K	NIST
Tfus	Outlier 176.60 ± 1.00	K	NIST
Tfus	178.65 ± 0.30	K	NIST
Tfus	179.00 ± 0.50	K	NIST
Ttriple	[177.90; 178.18]	K
Ttriple	178.18	K	ChemSep v8.3 pure component data Compiled value
Ttriple	178.15 ± 0.05	K	NIST
Ttriple	178.00 ± 0.20	K	NIST
Ttriple	177.90 ± 0.20	K	NIST
Ttriple	177.95 ± 0.02	K	NIST
Ttriple	178.15 ± 0.05	K	NIST
Ttriple	177.95 ± 0.02	K	NIST
UQi	2.97		ChemSep v8.3 pure component data Compiled value
URi	3.92		ChemSep v8.3 pure component data Compiled value
Vc	[0.316; 0.316]	m3/kmol
Vc	0.316	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value
Vc	0.316	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.316	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.316	m3/kmol	KDB
Vc	0.316	m3/kmol	NIST
VCOSTALD	0.31	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.27		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2638410; 0.2640000]
Zc	0.2640000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value
Zc	0.2640000		ChemSep v8.3 pure component data Compiled value
Zc	0.2638410		KDB
Zra	[0.26; 0.26]
Zra	0.26		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.26		ChemSep v8.3 pure component data Compiled value
Zra	0.26		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[130.08; 171.46]	J/mol×K	[371.20; 500.20]
Cp,gas	130.08 ± 0.26	J/mol×K	371.20	NIST
Cp,gas	140.20	J/mol×K	390.00	NIST
Cp,gas	137.20 ± 1.30	J/mol×K	393.00	NIST
Cp,gas	138.87 ± 0.27	J/mol×K	396.20	NIST
Cp,gas	146.40	J/mol×K	410.00	NIST
Cp,gas	149.16 ± 0.30	J/mol×K	427.20	NIST
Cp,gas	149.40 ± 1.70	J/mol×K	428.00	NIST
Cp,gas	160.33 ± 0.32	J/mol×K	462.20	NIST
Cp,gas	159.00 ± 1.70	J/mol×K	463.00	NIST
Cp,gas	171.46 ± 0.34	J/mol×K	500.20	NIST
Cp,liquid	[138.39; 175.10]	J/mol×K	[28.44; 353.20]
Cp,liquid	153.09	J/mol×K	28.44	NIST
Cp,liquid	142.70	J/mol×K	227.80	NIST
Cp,liquid	138.39	J/mol×K	228.15	Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
Cp,liquid	139.13	J/mol×K	228.15	Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
Cp,liquid	140.97	J/mol×K	238.15	Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
Cp,liquid	140.79	J/mol×K	238.15	Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
Cp,liquid	158.60	J/mol×K	293.00	NIST
Cp,liquid	156.00	J/mol×K	293.15	NIST
Cp,liquid	151.00	J/mol×K	293.20	NIST
Cp,liquid	157.00	J/mol×K	294.71	NIST
Cp,liquid	140.00	J/mol×K	295.00	NIST
Cp,liquid	158.60	J/mol×K	298.00	NIST
Cp,liquid	156.50	J/mol×K	298.00	NIST
Cp,liquid	156.50	J/mol×K	298.00	NIST
Cp,liquid	158.20	J/mol×K	298.00	NIST
Cp,liquid	156.90	J/mol×K	298.10	NIST
Cp,liquid	156.50	J/mol×K	298.10	NIST
Cp,liquid	157.00	J/mol×K	298.15	NIST
Cp,liquid	158.40	J/mol×K	298.15	NIST
Cp,liquid	157.09	J/mol×K	298.15	NIST
Cp,liquid	155.96	J/mol×K	298.15	NIST
Cp,liquid	161.90	J/mol×K	298.15	NIST
Cp,liquid	157.08	J/mol×K	298.15	NIST
Cp,liquid	158.70	J/mol×K	298.15	NIST
Cp,liquid	158.70	J/mol×K	298.15	NIST
Cp,liquid	157.23	J/mol×K	298.15	NIST
Cp,liquid	157.15	J/mol×K	298.15	NIST
Cp,liquid	156.80	J/mol×K	298.15	NIST
Cp,liquid	156.99	J/mol×K	298.15	NIST
Cp,liquid	157.06	J/mol×K	298.15	NIST
Cp,liquid	157.08	J/mol×K	298.15	NIST
Cp,liquid	156.94	J/mol×K	298.15	NIST
Cp,liquid	157.03	J/mol×K	298.15	NIST
Cp,liquid	157.07	J/mol×K	298.20	NIST
Cp,liquid	157.33	J/mol×K	298.71	NIST
Cp,liquid	153.60	J/mol×K	303.00	NIST
Cp,liquid	159.90	J/mol×K	303.15	NIST
Cp,liquid	157.65	J/mol×K	303.15	Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
Cp,liquid	159.03	J/mol×K	303.15	Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
Cp,liquid	159.10	J/mol×K	303.20	Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
Cp,liquid	160.40	J/mol×K	308.20	Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
Cp,liquid	161.98	J/mol×K	313.15	Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
Cp,liquid	162.35	J/mol×K	313.15	Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
Cp,liquid	161.60	J/mol×K	313.20	Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
Cp,liquid	163.00	J/mol×K	318.20	Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
Cp,liquid	164.10	J/mol×K	323.20	Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
Cp,liquid	166.90	J/mol×K	324.00	NIST
Cp,liquid	165.50	J/mol×K	328.20	Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
Cp,liquid	167.00	J/mol×K	333.20	Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
Cp,liquid	168.60	J/mol×K	338.20	Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
Cp,liquid	170.40	J/mol×K	343.20	Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
Cp,liquid	172.80	J/mol×K	348.20	Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
Cp,liquid	175.10	J/mol×K	353.20	Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
Csat	[152.85; 170.85]	J/mol×K	[283.15; 343.15]
Csat	152.85	J/mol×K	283.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	155.56	J/mol×K	293.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	158.38	J/mol×K	303.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	161.47	J/mol×K	313.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	164.51	J/mol×K	323.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	167.63	J/mol×K	333.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	170.85	J/mol×K	343.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
η	[0.0002860; 0.0006657]	Pa×s	[283.15; 363.15]
η	0.0006657	Pa×s	283.15	Density and Viscosity of Decalin, Cyclohexane, and Toluene Binary Mixtures at (283.15, 293.15, 303.15, 313.15, and 323.15) K
η	0.0006300	Pa×s	288.15	Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
η	0.0005880	Pa×s	293.15	Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
η	0.0005958	Pa×s	293.15	Density and Viscosity of Decalin, Cyclohexane, and Toluene Binary Mixtures at (283.15, 293.15, 303.15, 313.15, and 323.15) K
η	0.0005525	Pa×s	298.15	NCMS SOLV-DB
η	0.0005531	Pa×s	298.15	Ultrasonic and viscometric study of molecular interactions in binary mixtures of aniline with 1-propanol, 2-propanol, 2-methyl-1-propanol, and 2-methyl-2-propanol at different temperatures
η	0.0005560	Pa×s	298.15	Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
η	0.0005530	Pa×s	298.15	Densities and Viscosities of N-Formylmorpholine + Benzene, + Toluene at Different Temperatures and Atmospheric Pressures
η	0.0005635	Pa×s	298.15	Excess parameter studies on the binary mixtures of toluene with ketones at different temperatures
η	0.0005540	Pa×s	298.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0005580	Pa×s	298.15	Density and Viscosity Studies of Binary Mixtures of N,N-Dimethylformamide with Toluene and Methyl Benzoate at (298.15, 303.15, 308.15, and 313.15) K
η	0.0005635	Pa×s	298.15	Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
η	0.0005530	Pa×s	298.15	Densities, viscosities, and excess properties of (N-methylmorpholine + cyclohexane, + benzene, and + toluene) at T = (298.15, 303.15, 313.15, 323.15) K
η	0.0005540	Pa×s	298.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Sulfolane with Benzene, Toluene, Ethylbenzene, p-Xylene, o-Xylene, and m-Xylene at 303.15 and 323.15 K and Atmospheric Pressure
η	0.0005500	Pa×s	298.15	Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for CmH2m+1(OCH2CH2)nOH (m ) 1 or 2 or 4 andn ) 1) + Benzene, + Toluene, + (o-, m-, and p-) Xylenes, + Ethylbenzene, and + Cyclohexane
η	0.0005635	Pa×s	298.15	Molecular interaction studies and theoretical estimation of ultrasonic speeds using scaled particle theory in binary mixtures of toluene with homologous nitriles at different temperatures
η	0.0005251	Pa×s	303.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Sulfolane with Benzene, Toluene, Ethylbenzene, p-Xylene, o-Xylene, and m-Xylene at 303.15 and 323.15 K and Atmospheric Pressure
η	0.0005344	Pa×s	303.15	Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
η	0.0005368	Pa×s	303.15	Density and Viscosity of Decalin, Cyclohexane, and Toluene Binary Mixtures at (283.15, 293.15, 303.15, 313.15, and 323.15) K
η	0.0005230	Pa×s	303.15	Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
η	0.0005344	Pa×s	303.15	Molecular interaction studies and theoretical estimation of ultrasonic speeds using scaled particle theory in binary mixtures of toluene with homologous nitriles at different temperatures
η	0.0005344	Pa×s	303.15	Excess parameter studies on the binary mixtures of toluene with ketones at different temperatures
η	0.0005220	Pa×s	303.15	Densities and Viscosities of N-Formylmorpholine + Benzene, + Toluene at Different Temperatures and Atmospheric Pressures
η	0.0005250	Pa×s	303.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0005230	Pa×s	303.15	Densities, viscosities, and excess properties of (N-methylmorpholine + cyclohexane, + benzene, and + toluene) at T = (298.15, 303.15, 313.15, 323.15) K
η	0.0005253	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
η	0.0005250	Pa×s	303.15	Densities, Viscosities, and Speed of Sound Studies of Binary Mixtures of Methylbenzene with Heptan-1-ol, Octan-1-ol, and Decan-1-ol at (303.15 and 313.15) K
η	0.0005250	Pa×s	303.15	Thermodynamic properties of binary mixtures of N-methyl-2-pyrrolidinone with cyclohexane, benzene, toluene at (303.15 to 353.15) K and atmospheric pressure
η	0.0005260	Pa×s	303.15	Density and Viscosity Studies of Binary Mixtures of N,N-Dimethylformamide with Toluene and Methyl Benzoate at (298.15, 303.15, 308.15, and 313.15) K
η	0.0004960	Pa×s	308.15	Density and Viscosity Studies of Binary Mixtures of N,N-Dimethylformamide with Toluene and Methyl Benzoate at (298.15, 303.15, 308.15, and 313.15) K
η	0.0004990	Pa×s	308.15	Densities and Viscosities of Binary Mixtures of Methyl 4-Chlorobutyrate with Aromatic Hydrocarbons at T ) (298.15 to 318.15) K
η	0.0005091	Pa×s	308.15	Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
η	0.0004980	Pa×s	308.15	Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for CmH2m+1(OCH2CH2)nOH (m ) 1 or 2 or 4 andn ) 1) + Benzene, + Toluene, + (o-, m-, and p-) Xylenes, + Ethylbenzene, and + Cyclohexane
η	0.0005091	Pa×s	308.15	Molecular interaction studies and theoretical estimation of ultrasonic speeds using scaled particle theory in binary mixtures of toluene with homologous nitriles at different temperatures
η	0.0004940	Pa×s	308.15	Viscometric and Volumetric Properties of 10 Regular Binary Systems at 308.15 K and 313.15 K
η	0.0004933	Pa×s	308.15	Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
η	0.0005091	Pa×s	308.15	Excess parameter studies on the binary mixtures of toluene with ketones at different temperatures
η	0.0005020	Pa×s	308.15	Ultrasonic and viscometric study of molecular interactions in binary mixtures of aniline with 1-propanol, 2-propanol, 2-methyl-1-propanol, and 2-methyl-2-propanol at different temperatures
η	0.0004700	Pa×s	313.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0004700	Pa×s	313.15	Thermodynamic properties of binary mixtures of N-methyl-2-pyrrolidinone with cyclohexane, benzene, toluene at (303.15 to 353.15) K and atmospheric pressure
η	0.0004755	Pa×s	313.15	Viscometric and Volumetric Properties of 10 Regular Binary Systems at 308.15 K and 313.15 K
η	0.0004859	Pa×s	313.15	Density and Viscosity of Decalin, Cyclohexane, and Toluene Binary Mixtures at (283.15, 293.15, 303.15, 313.15, and 323.15) K
η	0.0004700	Pa×s	313.15	Density and Viscosity Studies of Binary Mixtures of N,N-Dimethylformamide with Toluene and Methyl Benzoate at (298.15, 303.15, 308.15, and 313.15) K
η	0.0004710	Pa×s	313.15	Densities, Viscosities, and Speed of Sound Studies of Binary Mixtures of Methylbenzene with Heptan-1-ol, Octan-1-ol, and Decan-1-ol at (303.15 and 313.15) K
η	0.0004676	Pa×s	313.15	Viscometric and Volumetric Properties of 10 Regular Binary Systems at 308.15 K and 313.15 K
η	0.0004710	Pa×s	313.15	Densities, viscosities, and excess properties of (N-methylmorpholine + cyclohexane, + benzene, and + toluene) at T = (298.15, 303.15, 313.15, 323.15) K
η	0.0004670	Pa×s	313.15	Densities and Viscosities of N-Formylmorpholine + Benzene, + Toluene at Different Temperatures and Atmospheric Pressures
η	0.0004717	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
η	0.0004379	Pa×s	318.15	Ultrasonic and viscometric study of molecular interactions in binary mixtures of aniline with 1-propanol, 2-propanol, 2-methyl-1-propanol, and 2-methyl-2-propanol at different temperatures
η	0.0004491	Pa×s	318.15	Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
η	0.0004460	Pa×s	318.15	Densities and Viscosities of Binary Mixtures of Methyl 4-Chlorobutyrate with Aromatic Hydrocarbons at T ) (298.15 to 318.15) K
η	0.0004230	Pa×s	323.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0004229	Pa×s	323.15	Excess Molar Volumes and Viscosities of Binary Mixtures of Sulfolane with Benzene, Toluene, Ethylbenzene, p-Xylene, o-Xylene, and m-Xylene at 303.15 and 323.15 K and Atmospheric Pressure
η	0.0004230	Pa×s	323.15	Thermodynamic properties of binary mixtures of N-methyl-2-pyrrolidinone with cyclohexane, benzene, toluene at (303.15 to 353.15) K and atmospheric pressure
η	0.0004220	Pa×s	323.15	Densities, viscosities, and excess properties of (N-methylmorpholine + cyclohexane, + benzene, and + toluene) at T = (298.15, 303.15, 313.15, 323.15) K
η	0.0004210	Pa×s	323.15	Densities and Viscosities of N-Formylmorpholine + Benzene, + Toluene at Different Temperatures and Atmospheric Pressures
η	0.0004244	Pa×s	323.15	Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
η	0.0004408	Pa×s	323.15	Density and Viscosity of Decalin, Cyclohexane, and Toluene Binary Mixtures at (283.15, 293.15, 303.15, 313.15, and 323.15) K
η	0.0004082	Pa×s	328.15	Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
η	0.0003835	Pa×s	333.15	Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
η	0.0003850	Pa×s	333.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0003810	Pa×s	333.15	Densities and Viscosities of N-Formylmorpholine + Benzene, + Toluene at Different Temperatures and Atmospheric Pressures
η	0.0003850	Pa×s	333.15	Thermodynamic properties of binary mixtures of N-methyl-2-pyrrolidinone with cyclohexane, benzene, toluene at (303.15 to 353.15) K and atmospheric pressure
η	0.0003500	Pa×s	343.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0003500	Pa×s	343.15	Thermodynamic properties of binary mixtures of N-methyl-2-pyrrolidinone with cyclohexane, benzene, toluene at (303.15 to 353.15) K and atmospheric pressure
η	0.0003490	Pa×s	343.15	Densities and Viscosities of N-Formylmorpholine + Benzene, + Toluene at Different Temperatures and Atmospheric Pressures
η	0.0003100	Pa×s	353.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0003210	Pa×s	353.15	Densities and Viscosities of N-Formylmorpholine + Benzene, + Toluene at Different Temperatures and Atmospheric Pressures
η	0.0003230	Pa×s	353.15	Thermodynamic properties of binary mixtures of N-methyl-2-pyrrolidinone with cyclohexane, benzene, toluene at (303.15 to 353.15) K and atmospheric pressure
η	0.0002860	Pa×s	363.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
ΔfusH	[6.55; 6.64]	kJ/mol	[177.95; 178.15]
ΔfusH	6.62	kJ/mol	177.95	NIST
ΔfusH	6.62	kJ/mol	177.95	NIST
ΔfusH	6.55	kJ/mol	178.00	NIST
ΔfusH	6.61	kJ/mol	178.00	NIST
ΔfusH	6.62	kJ/mol	178.00	NIST
ΔfusH	6.64	kJ/mol	178.15	NIST
ΔfusH	6.64	kJ/mol	178.15	NIST
ΔvapH	[24.00; 40.60]	kJ/mol	[244.50; 561.00]
ΔvapH	40.60	kJ/mol	244.50	NIST
ΔvapH	37.80	kJ/mol	251.50	NIST
ΔvapH	38.90	kJ/mol	284.00	NIST
ΔvapH	38.02	kJ/mol	298.00	Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
ΔvapH	38.80	kJ/mol	298.00	NIST
ΔvapH	36.90	kJ/mol	318.00	NIST
ΔvapH	37.30	kJ/mol	323.00	NIST
ΔvapH	37.80	kJ/mol	324.00	NIST
ΔvapH	35.40	kJ/mol	333.00	NIST
ΔvapH	35.65	kJ/mol	341.27	NIST
ΔvapH	37.00	kJ/mol	346.00	NIST
ΔvapH	37.00	kJ/mol	347.00	NIST
ΔvapH	35.40	kJ/mol	363.00	NIST
ΔvapH	33.40	kJ/mol	373.00	NIST
ΔvapH	33.50 ± 0.10	kJ/mol	380.00	NIST
ΔvapH	33.18	kJ/mol	383.70	KDB
ΔvapH	33.18	kJ/mol	383.80	NIST
ΔvapH	32.10 ± 0.10	kJ/mol	403.00	NIST
ΔvapH	31.40	kJ/mol	413.00	NIST
ΔvapH	35.70	kJ/mol	413.50	NIST
ΔvapH	34.40	kJ/mol	414.00	NIST
ΔvapH	29.40 ± 0.10	kJ/mol	441.00	NIST
ΔvapH	28.40	kJ/mol	453.00	NIST
ΔvapH	27.10 ± 0.10	kJ/mol	470.00	NIST
ΔvapH	33.20	kJ/mol	485.50	NIST
ΔvapH	24.00	kJ/mol	493.00	NIST
ΔvapH	24.00 ± 0.10	kJ/mol	505.00	NIST
ΔvapH	33.30	kJ/mol	561.00	NIST
Pvap	[0.24; 3280.00]	kPa	[253.83; 573.20]
Pvap	0.24	kPa	253.83	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	0.47	kPa	263.15	Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
Pvap	0.48	kPa	263.64	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	0.48	kPa	263.64	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	0.43	kPa	263.75	Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
Pvap	0.91	kPa	273.15	Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
Pvap	0.91	kPa	273.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	0.84	kPa	273.47	Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
Pvap	0.93	kPa	273.47	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	0.93	kPa	273.47	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	1.26	kPa	278.70	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	1.67	kPa	283.15	Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
Pvap	1.67	kPa	283.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	1.68	kPa	283.32	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	1.68	kPa	283.32	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	1.57	kPa	283.35	Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
Pvap	1.70	kPa	283.60	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	2.42	kPa	288.15	Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
Pvap	2.35	kPa	288.15	Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
Pvap	2.26	kPa	288.50	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	3.18	kPa	293.15	Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
Pvap	2.91	kPa	293.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	2.91	kPa	293.15	Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
Pvap	3.05	kPa	293.15	Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
Pvap	2.93	kPa	293.24	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	2.93	kPa	293.24	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	2.93	kPa	293.26	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	2.82	kPa	293.29	Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
Pvap	2.97	kPa	293.40	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	3.78	kPa	298.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	3.80	kPa	298.15	(Vapour + liquid) equilibria of (1-butanol + benzene, or toluene, or o-, or m-, or p-xylene) at T = 308.15 K
Pvap	3.84	kPa	298.15	Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
Pvap	3.79	kPa	298.15	NCMS SOLV-DB
Pvap	3.80	kPa	298.25	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	3.80	kPa	298.25	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	3.89	kPa	298.30	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	4.47	kPa	300.89	Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
Pvap	4.87	kPa	303.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap	4.73	kPa	303.15	Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
Pvap	4.87	kPa	303.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	4.90	kPa	303.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap	4.87	kPa	303.15	Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
Pvap	5.00	kPa	303.20	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	4.90	kPa	303.21	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	4.90	kPa	303.23	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	4.89	kPa	303.23	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	4.89	kPa	303.23	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	4.79	kPa	303.28	Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
Pvap	5.17	kPa	305.64	Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
Pvap	5.23	kPa	305.68	Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
Pvap	6.27	kPa	308.10	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	6.32	kPa	308.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap	6.26	kPa	308.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap	7.99	kPa	313.10	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	7.88	kPa	313.15	Vapor Liquid Equilibria of Binary Mixtures Containing 2-Butanol and Hydrocarbons at 313.15 K
Pvap	7.96	kPa	313.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap	7.78	kPa	313.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap	7.88	kPa	313.15	Isothermal vapor liquid equilibrium and molar excess Gibbs energies of two ternary systems containing either 1-butanol or 2-butanol + 1- hexene + methylbenzene at 313.15 K
Pvap	7.89	kPa	313.15	Phase equilibrium properties of the ternary mixture dibutyl ether + toluene + heptane at 313.15 K
Pvap	7.85	kPa	313.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	7.85	kPa	313.15	Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
Pvap	7.88	kPa	313.15	Vapor-Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K
Pvap	7.87	kPa	313.19	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	7.87	kPa	313.19	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	8.10	kPa	313.20	Isothermal vapor-liquid equilibrium of binary and ternary systems of anisole, hexane, and toluene and ternary system of methyl tert-butyl ether, hexane, and toluene
Pvap	7.87	kPa	313.22	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	7.87	kPa	313.22	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	7.79	kPa	313.27	Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
Pvap	8.62	kPa	315.15	Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap	9.95	kPa	318.00	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	9.89	kPa	318.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap	9.96	kPa	318.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap	10.77	kPa	320.15	Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap	12.26	kPa	323.00	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	12.22	kPa	323.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	12.23	kPa	323.15	Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
Pvap	12.27	kPa	323.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap	12.31	kPa	323.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap	12.22	kPa	323.15	Isothermal Phase Equilibria and Excess Molar Enthalpies for Binary Systems with Dimethyl Ether at 323.15 K
Pvap	12.29	kPa	323.16	Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
Pvap	12.25	kPa	323.22	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	12.24	kPa	323.22	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	12.30	kPa	323.25	Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
Pvap	13.40	kPa	324.21	Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
Pvap	13.34	kPa	325.15	Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap	13.37	kPa	325.16	Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
Pvap	14.53	kPa	327.15	Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
Pvap	14.90	kPa	327.60	Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
Pvap	15.00	kPa	327.90	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	15.14	kPa	328.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap	14.96	kPa	328.15	Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap	15.77	kPa	329.15	Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
Pvap	16.40	kPa	330.15	Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap	17.80	kPa	332.15	Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
Pvap	18.26	kPa	332.80	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	18.46	kPa	333.15	Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
Pvap	18.56	kPa	333.15	An equipment for dynamic measurements of vapour liquid equilibria and results in binary systems containing cyclohexylamine
Pvap	18.56	kPa	333.15	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
Pvap	18.62	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	18.86	kPa	333.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap	18.45	kPa	333.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	18.57	kPa	333.20	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	18.57	kPa	333.20	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	18.93	kPa	333.22	Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
Pvap	19.35	kPa	334.25	Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
Pvap	20.02	kPa	335.15	Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap	20.00	kPa	335.25	Isobaric Vapor Liquid Equilibrium for Binary Systems of Toluene + Acrylic Acid, Toluene + Acetic Acid, and Cyclohexane + Acrylic Acid at 20 kPa
Pvap	22.08	kPa	337.65	Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
Pvap	22.04	kPa	337.80	A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap	22.61	kPa	338.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap	23.83	kPa	339.65	Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
Pvap	26.32	kPa	342.30	Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
Pvap	26.47	kPa	342.45	Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
Pvap	26.66	kPa	342.65	Isobaric Vapor-Liquid Equilibria of the Ternary System Toluene + Ethylbenzene + Amyl Acetate
Pvap	27.10	kPa	343.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	27.24	kPa	343.15	An equipment for dynamic measurements of vapour liquid equilibria and results in binary systems containing cyclohexylamine
Pvap	27.12	kPa	343.15	Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
Pvap	27.31	kPa	343.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap	27.20	kPa	343.16	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	27.20	kPa	343.16	Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
Pvap	27.76	kPa	343.18	Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
Pvap	29.21	kPa	345.25	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	32.72	kPa	348.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap	32.41	kPa	348.15	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	37.22	kPa	352.05	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	37.61	kPa	352.25	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	38.84	kPa	353.13	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	38.84	kPa	353.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	38.40	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	38.92	kPa	353.15	Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
Pvap	38.82	kPa	353.15	An equipment for dynamic measurements of vapour liquid equilibria and results in binary systems containing cyclohexylamine
Pvap	38.87	kPa	353.15	Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
Pvap	43.67	kPa	356.65	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	45.96	kPa	357.90	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	46.17	kPa	358.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap	49.60	kPa	360.70	Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
Pvap	51.35	kPa	361.30	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	53.33	kPa	362.63	Isobaric Vapor-Liquid Equilibria of the Ternary System Toluene + Ethylbenzene + Amyl Acetate
Pvap	53.30	kPa	362.64	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	54.13	kPa	363.08	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	54.22	kPa	363.15	An equipment for dynamic measurements of vapour liquid equilibria and results in binary systems containing cyclohexylamine
Pvap	54.42	kPa	363.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
Pvap	54.49	kPa	363.15	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
Pvap	55.59	kPa	363.75	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	63.84	kPa	368.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap	63.48	kPa	368.25	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	70.12	kPa	371.40	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	80.00	kPa	375.66	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	79.99	kPa	375.66	Isobaric Vapor-Liquid Equilibria of the Ternary System Toluene + Ethylbenzene + Amyl Acetate
Pvap	79.30	kPa	375.80	Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
Pvap	82.48	kPa	376.65	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	86.25	kPa	378.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap	95.30	kPa	381.65	Vapor-liquid equilibrium for the binary mixtures of dimethylsulfoxide with substituted benzenes
Pvap	99.89	kPa	383.25	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	101.30	kPa	383.40	Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
Pvap	100.66	kPa	383.50	Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
Pvap	101.30	kPa	383.55	Isobaric Vapor-Liquid Equilibrium for Binary Systems of Toluene + Ethanol, Toluene + Isopropanol at (101.3, 121.3, 161.3 and 201.3) kPa
Pvap	101.30	kPa	383.60	A new analysis method for improving collection of vapor-liquid equilibrium (VLE) data of binary mixtures using differential scanning calorimetry (DSC)
Pvap	101.33	kPa	383.75	Vapor-Liquid Equilibrium of Ferrocene in Some Organic Solvents Using Spectroscopic Methods
Pvap	101.30	kPa	383.76	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	101.33	kPa	383.77	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	101.30	kPa	383.80	Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
Pvap	101.33	kPa	383.81	Isobaric vapor-liquid equilibrium for binary system of cinnamaldehyde + benzaldehyde at 10, 20 and 30 kPa
Pvap	101.33	kPa	383.82	Isobaric Vapor Liquid Equilibrium for Binary and Ternary Systems of Isoamyl Alcohol + Isoamyl Acetate + Dimethyl Sulfoxide at 101.33 kPa
Pvap	102.00	kPa	384.10	Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
Pvap	102.73	kPa	384.30	Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
Pvap	121.30	kPa	390.25	Isobaric Vapor-Liquid Equilibrium for Binary Systems of Toluene + Ethanol, Toluene + Isopropanol at (101.3, 121.3, 161.3 and 201.3) kPa
Pvap	121.30	kPa	390.26	Isobaric Vapor-Liquid Equilibrium for Binary Systems of Toluene + Ethanol, Toluene + Isopropanol at (101.3, 121.3, 161.3 and 201.3) kPa
Pvap	161.30	kPa	400.75	Isobaric Vapor-Liquid Equilibrium for Binary Systems of Toluene + Ethanol, Toluene + Isopropanol at (101.3, 121.3, 161.3 and 201.3) kPa
Pvap	201.30	kPa	409.65	Isobaric Vapor-Liquid Equilibrium for Binary Systems of Toluene + Ethanol, Toluene + Isopropanol at (101.3, 121.3, 161.3 and 201.3) kPa
Pvap	498.30	kPa	451.00	Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
Pvap	499.90	kPa	451.50	Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
Pvap	760.00	kPa	473.30	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	760.00	kPa	473.30	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	760.00	kPa	473.30	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	1009.33	kPa	490.40	Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
Pvap	1140.00	kPa	498.30	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	1120.00	kPa	498.30	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	1150.00	kPa	498.30	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	1660.00	kPa	523.40	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	1660.00	kPa	523.40	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	1670.00	kPa	523.40	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	2350.00	kPa	548.30	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	2340.00	kPa	548.40	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	2340.00	kPa	548.40	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	3280.00	kPa	573.20	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	3250.00	kPa	573.20	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
Pvap	3230.00	kPa	573.20	A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
n0	[1.48260; 1.50278]		[283.15; 318.15]
n0	1.50278		283.15	Density, Speed of Sound, and Refractive Index of the Binary Systems Cyclohexane (1) or Methylcyclohexane (1) or Cyclo-octane (1) with Benzene (2), Toluene (2), and Ethylbenzene (2) at Two Temperatures
n0	1.49980		288.15	Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
n0	1.49960		288.15	Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
n0	1.49980		288.15	Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n0	1.49600		293.00	Quaternary Liquid-Liquid Equilibrium of Water + Acetic Acid + Propionic Acid + Solvent (Amyl Alcohol, Cyclohexyl Acetate, or Toluene) Systems
n0	1.48730		293.10	(Liquid + liquid) equilibria of three ternary systems: (heptane + benzene + N-formylmorpholine), (heptane + toluene + N-formylmorpholine), (heptane + xylene + N-formylmorpholine) from T = (298.15 to 353.15) K
n0	1.49650		293.10	A study on densities and excess volumes in the (c-butyrolactone + aromatic hydrocarbon) system at various temperatures
n0	1.49650		293.10	Densities and volumetric properties of N-methyl-2-pyrrolidone with aromatic hydrocarbon at different temperature
n0	1.48730		293.10	Measurement and Correlation of Liquid-Liquid Equilibria of Methylcyclohexane + Toluene + N-Formylmorpholine at (293, 303, 313, and 323) K
n0	1.49610		293.10	Vapor-Liquid Equilibria of Binary Systems Comprising 1-Chloro-2-ethylhexane and 2-Ethyl-1-hexanol
n0	1.49690		293.15	Liquid-liquid equilibria of water + solutes (acetic acid/ acetol/furfural/guaiacol/methanol/phenol/propanal) + solvents (isopropyl acetate/toluene) ternary systems for pyrolysis oil fractionation
n0	1.49600		293.15	Distribution of Butyric Acid between Water and Several Solvents
n0	1.49650		293.15	Experimental densities and excess volumes for binary mixtures of (dimethyl sulfoxide + an aromatic hydrocarbon) at temperatures from (293.15 to 353.15) K at atmospheric pressure
n0	1.49650		293.15	Effect of temperature on the volumetric properties of (cyclohexanone + an aromatic hydrocarbon)
n0	1.49687		293.15	Solubility, Thermodynamic Properties, and Derived Excess Properties of Benzoic Acid in (Acetic Acid + Water) and (Acetic Acid + Toluene) Binary Mixtures
n0	1.49700		293.15	Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n0	1.49300		293.15	Volumetric properties of binary mixtures of tributylamine with benzene derivatives and comparison with ERAS model results at temperatures from (293.15 to 333.15) K
n0	1.49700		293.15	Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
n0	1.49670		293.15	Solubilities of Phosphorus-Containing Compounds in Selected Solvents
n0	1.49620		293.15	Infinite Dilution Activity Coefficients of Hydrocarbons in Triethylene Glycol and Tetraethylene Glycol
n0	1.49700		293.15	Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
n0	1.49650		293.15	A study of densities and volumetric properties of binary mixtures containing nitrobenzene at T = (293.15 to 353.15) K
n0	1.49600		293.15	Ternary Liquid-Liquid(-Liquid) Equilibria of Aniline + Cyclohexylamine + Water, Aniline + Cyclohexylamine + Octane, Aniline + Water + Toluene, and Aniline + Water + Octane
n0	1.49670		293.15	Solubilities of Triphenylphosphine Oxide in Selected Solvents
n0	1.49600		293.15	Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Water + Cyclohexylamine + Aromatic Hydrocarbon (Toluene or Propylbenzene) or Aliphatic Hydrocarbon (Heptane or Octane)
n0	1.49620		293.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Anisole with Benzene, Methylbenzene, Ethylbenzene, Propylbenzene, and Butylbenzene at (293.15 and 303.15) K
n0	1.49650		293.15	Vapor-Liquid Equilibrium Measurements of MTBE and TAME with Toluene
n0	1.49600		293.15	Vapor liquid equilibria in ternary systems of associating components (water, aniline, cyclohexylamine) and hydrocarbons (octane or toluene)
n0	1.49530		293.15	Isobaric (vapour + liquid) equilibria data for the binary systems {1,2-dichloroethane (1) + toluene (2)} and {1,2-dichloroethane (1) + acetic acid (2)} at atmospheric pressure
n0	1.49670		293.15	Solubilities of Methyldiphenylphosphine Oxide in Selected Solvents
n0	1.49670		293.15	Solubilities of (2,5-Dihydroxyphenyl)diphenyl Phosphine Oxide in Selected Solvents
n0	1.49670		293.20	Liquid phase equilibria for mixtures of (an aliphatic hydrocarbon + toluene + gamma-butyrolactone)
n0	1.49393		298.10	Liquid-Liquid Equilibria for [C8mim][NTf2] + Thiophene + 2,2,4-Trimethylpentane or + Toluene
n0	1.49400		298.15	Liquid-liquid equilibria for mixtures of (Furfural + an Aromatic hydrocarbon + an alkane) at T=298.15 K
n0	1.49410		298.15	Excess molar volumes of (propiophenone + toluene) and estimated density of liquid propiophenone below its melting temperature
n0	1.49400		298.15	NCMS SOLV-DB
n0	1.49398		298.15	Application of [HMim][NTf2], [HMim][TfO] and [BMim][TfO] ionic liquids on the extraction of toluene from alkanes: Effect of the anion and the alkyl chain length of the cation on the LLE
n0	1.49413		298.15	KDB
n0	1.49393		298.15	Volumetric behaviour of the (2,2,4-trimethylpentane + methylbenzene + butan-1-ol) ternary system and its binary sub-systems within the temperature range (298.15-328.15) K
n0	1.49393		298.15	Volumetric behavior of the ternary system (methyl tert-butyl ether + methylbenzene + butan-1-ol) and its binary sub-system (methyl tert-butyl ether + butan-1-ol) within the temperature range (298.15 to 328.15) K
n0	1.49399		298.15	Extraction of toluene from aliphatic compounds using an ionic liquid as solvent: Influence of the alkane on the (liquid + liquid) equilibrium
n0	1.49406		298.15	Solubility, Thermodynamic Properties, and Derived Excess Properties of Benzoic Acid in (Acetic Acid + Water) and (Acetic Acid + Toluene) Binary Mixtures
n0	1.49399		298.15	Effect of the Chain Length on the Aromatic Ring in the Separation of Aromatic Compounds from Methylcyclohexane Using the Ionic Liquid 1-Ethyl-3-methylpyridinium Ethylsulfate
n0	1.49399		298.15	Effect of Temperature on the Change of Refractive Index on Mixing for Butyl Acetate + Aromatic Hydrocarbons
n0	1.49410		298.15	Volumetric behaviour of binary liquid systems composed of toluene, isooctane, and methyl tert-butyl ether at temperatures from (298.15 to 328.15) K
n0	1.49410		298.15	Solubility of -Carotene in Binary Solvents Formed by Some Hydrocarbons with Dibutyl Ether and 1,2-Dimethoxyethane
n0	1.49410		298.15	Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with tert-Butyl Methyl Ether and with tert-Amyl Methyl Ether
n0	1.49410		298.15	Excess molar volumes of (octane + benzene, or toluene, or 1,3-xylene, or 1,3,5-trimethylbenzene) at temperatures between (298.15 and 328.15) K
n0	1.49410		298.15	Physical properties of (propyl propanoate + hexane + toluene) at 298.15 K
n0	1.49419		298.15	Vapor-Liquid Equilibrium and Density of the Binary System 1-Phenylethylamine + Toluene
n0	1.49650		298.15	Densities and excess volumes of binary mixtures of N,N-dimethylformamide with aromatic hydrocarbon at different temperature
n0	1.49399		298.15	Liquid-Liquid Equilibrium for Ternary Mixtures of Hexane + Aromatic Compounds + [EMpy][ESO4] at T = 298.15 K
n0	1.49390		298.15	Densities, speeds of sound, and refractive indices of the ternary mixtures (toluene + methyl acetate + butyl acetate) and (toluene + methyl acetate + methyl heptanoate) at 298.15 K
n0	1.49399		298.15	Density, Speed of Sound, and Refractive Index of the Binary Systems Cyclohexane (1) or Methylcyclohexane (1) or Cyclo-octane (1) with Benzene (2), Toluene (2), and Ethylbenzene (2) at Two Temperatures
n0	1.49440		298.15	Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
n0	1.49390		298.15	Vapor-Liquid Equilibrium for Binary System of 1-Propanethiol, Thiophene, and Diethyl Sulfide with Toluene at 90.03 kPa
n0	1.49390		298.15	Vapor-Liquid Equilibrium for Binary System of Thiophene + n-Hexane at (338.15 and 323.15) K and Thiophene + 1-Hexene at (333.15 and 323.15) K
n0	1.49390		298.15	Vapor-Liquid Equilibrium for Binary System of Diethyl Sulfide + n-Heptane and Diethyl Sulfide + 2,2,4-Trimethylpentane at (363.15 and 353.15) K
n0	1.49420		298.15	Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
n0	1.49390		298.15	Vapor-Liquid Equilibrium for Binary System of Diethyl Sulfide + n-Hexane at (338.15 and 323.15) K and Diethyl Sulfide + 1-Hexene at (333.15 and 323.15) K
n0	1.49399		298.15	Separation of toluene from cyclic hydrocarbons using 1-butyl-3-methylimidazolium methylsulfate ionic liquid at T = 298.15 K and atmospheric pressure
n0	1.49360		298.15	Experimental Isobaric Vapor-Liquid Equilibria of Binary Mixtures of 2,2,2-Trifluoroethanol with Benzene or Toluene
n0	1.49390		298.15	Vapor liquid equilibrium for binary system of diethyl sulfide + cyclohexane at 353.15 and 343.15 K and diethyl sulfide + 2-ethoxy-2-methylpropane at 343.15 and 333.15 K
n0	1.49400		298.15	Vapor liquid equilibrium for binary system of thiophene + 2,2,4-trimethylpentane at 343.15 and 353.15K and thiophene + 2-ethoxy-2-methylpropane at 333.15 and 343.15K
n0	1.49310		298.15	Excess and deviation properties for the binary mixtures of methylcyclohexane with benzene, toluene, p-xylene, mesitylene, and anisole at T = (298.15, 303.15, and 308.15) K
n0	1.49420		298.15	Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n0	1.49397		298.15	Isothermal vapor liquid equilibrium at 333.15K and excess volumes and molar refractivity deviation at 298.15K for the ternary system di-butyl ether (1) + ethanol (2) + toluene (3) and its binary subsystems
n0	1.49420		298.15	Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
n0	1.49397		298.15	Isothermal vapor-liquid equilibrium at T = 333.15 K and excess volumes and molar refractivity deviation at T = 298.15 K for the ternary mixtures {di-methyl carbonate (DMC) + ethanol + benzene} and {DMC+ ethanol + toluene}
n0	1.49410		298.15	Excess Molar Volumes of (propiophenone + benzene, or toluene, or ethylbenzene, or butylbenzene) at temperatures 298.15 K and 328.15 K
n0	1.49380		298.15	Experimental and predicted volumetric and refractive index properties of ternary mixtures of iodoethane with toluene and alcohols at temperature 298.15 K and pressure 101 kPa
n0	1.49650		298.15	The volumetric properties of (1,2-propanediol carbonate + benzene, or toluene, or styrene) binary mixtures at temperatures from T = 293.15 K to T = 353.15 K
n0	1.49380		298.20	(Liquid + liquid) equilibrium data of (water + phosphoric acid + solvents) systems at T = (308.2 and 318.2) K
n0	1.49400		298.20	(Liquid + liquid) equilibria of aqueous solutions of butyric acid with n-heptane and toluene at T = (298.2, 308.2, and 318.2) K
n0	1.49020		303.15	Excess and deviation properties for the binary mixtures of methylcyclohexane with benzene, toluene, p-xylene, mesitylene, and anisole at T = (298.15, 303.15, and 308.15) K
n0	1.49130		303.15	Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
n0	1.49124		303.15	Solubility, Thermodynamic Properties, and Derived Excess Properties of Benzoic Acid in (Acetic Acid + Water) and (Acetic Acid + Toluene) Binary Mixtures
n0	1.49140		303.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Anisole with Benzene, Methylbenzene, Ethylbenzene, Propylbenzene, and Butylbenzene at (293.15 and 303.15) K
n0	1.49180		303.15	Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
n0	1.49130		303.15	Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n0	1.48840		308.15	Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
n0	1.48740		308.15	Excess and deviation properties for the binary mixtures of methylcyclohexane with benzene, toluene, p-xylene, mesitylene, and anisole at T = (298.15, 303.15, and 308.15) K
n0	1.48850		308.15	Topological and thermodynamic investigations of molecular interactions in binary mixtures: Molar excess volumes and molar excess enthalpies
n0	1.48840		308.15	Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n0	1.48550		313.15	Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
n0	1.48550		313.15	Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n0	1.48260		318.15	Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
n0	1.48260		318.15	Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
ρl	[781.97; 885.28]	kg/m3	[273.15; 373.20]
ρl	885.28	kg/m3	273.15	Isobaric Thermal Expansivities of Toluene Measured by Scanning Transitiometry at Temperatures from (243 to 423) K and Pressures up to 200 MPa
ρl	880.70	kg/m3	278.15	Isobaric Thermal Expansivities of Toluene Measured by Scanning Transitiometry at Temperatures from (243 to 423) K and Pressures up to 200 MPa
ρl	876.19	kg/m3	283.15	Volumetric and acoustic properties of binary systems (furfural or furfuryl alcohol + toluene) and (furfuryl alcohol + ethanol) at different temperatures
ρl	876.11	kg/m3	283.15	Isobaric Thermal Expansivities of Toluene Measured by Scanning Transitiometry at Temperatures from (243 to 423) K and Pressures up to 200 MPa
ρl	871.79	kg/m3	288.15	Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
ρl	871.00	kg/m3	288.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	871.50	kg/m3	288.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρl	871.50	kg/m3	288.15	Isobaric Thermal Expansivities of Toluene Measured by Scanning Transitiometry at Temperatures from (243 to 423) K and Pressures up to 200 MPa
ρl	871.44	kg/m3	288.15	Volumetric properties of binary liquid mixtures: Application of the Prigogine Flory Patterson theory to excess molar volumes of dichloromethane with benzene or toluene
ρl	871.92	kg/m3	288.20	The impact of uni-univalent electrolytes on (water + acetic acid + toluene) equilibria: Representation with electrolyte-NRTL model
ρl	867.00	kg/m3	293.00	KDB
ρl	866.84	kg/m3	293.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
ρl	866.68	kg/m3	293.15	Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
ρl	866.78	kg/m3	293.15	Liquid-Liquid Equilibria in Ternary Systems of Aromatic Hydrocarbons (Toluene or Ethylbenzene) + Phenols + Water
ρl	866.92	kg/m3	293.15	Volumetric properties of binary liquid mixtures: Application of the Prigogine Flory Patterson theory to excess molar volumes of dichloromethane with benzene or toluene
ρl	866.80	kg/m3	293.15	Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
ρl	867.08	kg/m3	293.15	Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
ρl	866.84	kg/m3	293.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl	866.70	kg/m3	293.15	Densities and Kinematic Viscosities of One Quinary Regular Liquid System and Its Five Quaternary Sub-Systems at Temperatures (293.15 and 298.15) K
ρl	866.82	kg/m3	293.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene and Trans-decahydronaphthalene
ρl	866.82	kg/m3	293.15	Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
ρl	866.93	kg/m3	293.15	Partial molar volume of paracetamol in water, 0.1 M HCl and 0.154 M NaCl at T = (298.15, 303.15, 308.15 and 310.65) K and at 101.325 kPa
ρl	868.00	kg/m3	293.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	867.00	kg/m3	293.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	866.70	kg/m3	293.15	Densities and Kinematic Viscosities of a Quinary Regular Liquid System and Its Five Quaternary Subsystems at 293.15A K and 298.15A K
ρl	866.91	kg/m3	293.15	Volumetric and acoustic properties of binary systems (furfural or furfuryl alcohol + toluene) and (furfuryl alcohol + ethanol) at different temperatures
ρl	866.87	kg/m3	293.15	Isobaric Thermal Expansivities of Toluene Measured by Scanning Transitiometry at Temperatures from (243 to 423) K and Pressures up to 200 MPa
ρl	866.98	kg/m3	293.15	Thermodynamics of Mixtures Containing Amines. XII. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for N-Methylaniline + Hydrocarbon Systems
ρl	866.84	kg/m3	293.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρl	867.30	kg/m3	293.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	867.61	kg/m3	293.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	867.80	kg/m3	293.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	866.51	kg/m3	293.20	Isothermal Vapor-Liquid Equilibrium Data for Binary Systems of CHF3 or C2F6 with Methylcyclohexane or Toluene
ρl	866.81	kg/m3	293.20	Isobaric Vapor-Liquid Equilibria for Binary Mixtures of 1,2-Dibromoethane with Benzene, Toluene, Fluorobenzene, and Bromobenzene at Atmospheric Pressure
ρl	864.69	kg/m3	295.20	Isothermal Vapor-Liquid Equilibrium Data for Binary Systems of CHF3 or C2F6 with Methylcyclohexane or Toluene
ρl	862.86	kg/m3	297.20	Isothermal Vapor-Liquid Equilibrium Data for Binary Systems of CHF3 or C2F6 with Methylcyclohexane or Toluene
ρl	857.61	kg/m3	298.00	Removal of aromatic hydrocarbons from hydrocarbon mixture using glycols at 303.15 K and 333.15 K and atmospheric pressure: Experimental and calculated data by NRTL and UNIQUAC models
ρl	862.19	kg/m3	298.15	Viscosities and Excess Molar Volumes of the Ternary System Toluene (1) + Cyclohexane (2) + Pentane (3) at 298.15 K
ρl	862.22	kg/m3	298.15	Excess Enthalpy and Excess Volume for Pyridine + Methyldiethanolamine and Pyridine + Ethanolamine Mixtures
ρl	862.36	kg/m3	298.15	Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
ρl	862.27	kg/m3	298.15	Mutual Solubility of Pyridinium-Based Tetrafluoroborates and Toluene
ρl	857.58	kg/m3	298.15	Experimental and theoretical study of surface tension of binary mixtures of (n-alkyl acetates + heptane, benzene, and toluene)
ρl	862.17	kg/m3	298.15	Molar Excess Volumes and Excess Isentropic Compressibilities of {2-Methylaniline (i) + Benzene (j) + Methylbenzene}, {2-Methylaniline (i) + Benzene (j) + 1,2-Dimethylbenzene (k)}, and {2-Methylaniline (i) + Benzene (j) + 1,4-Dimethylbenzene (k)} at T = 308.15 K
ρl	862.23	kg/m3	298.15	Binary and Ternary Vapor-Liquid Equilibrium at 323.15 K and Excess Molar Volumes at 298.15 K for the Mixtures of Propyl Vinyl Ether + 1-Propanol + Toluene
ρl	861.81	kg/m3	298.15	Volumetric properties of binary liquid mixtures: Application of the Prigogine Flory Patterson theory to excess molar volumes of dichloromethane with benzene or toluene
ρl	862.10	kg/m3	298.15	Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes and Aromatic Compounds at T = 313.15 K
ρl	862.35	kg/m3	298.15	Thermodynamics of mixtures containing amines. XI. Liquid + liquid equilibria and molar excess enthalpies at 298.15 K for N-methylaniline + hydrocarbon systems. Characterization in terms of DISQUAC and ERAS models
ρl	862.17	kg/m3	298.15	Evaluation of ionic liquids as solvent for aromatic extraction: Experimental, correlation and COSMO-RS predictions
ρl	862.17	kg/m3	298.15	Phase behavior of ternary mixtures {aliphatic hydrocarbon + aromatic hydrocarbon + ionic liquid}: Experimental LLE data and their modeling by COSMO-RS
ρl	862.17	kg/m3	298.15	(Liquid + liquid) equilibrium at T = 298.15 K for ternary mixtures of alkane + aromatic compounds + imidazolium-based ionic liquids
ρl	862.11	kg/m3	298.15	Densities and volumes of mixing of the ternary system toluene + butyl acrylate + methyl methacrylate and its binaries at 298.15 K
ρl	862.18	kg/m3	298.15	Hexyl dimethylpyridinium ionic liquids for desulfurization of fuels. Effect of the position of the alkyl side chains
ρl	862.40	kg/m3	298.15	Thermo Physical Properties of 4-Hydroxy 4-Methyl Pentanone with Nitrobenzene or Ethyl Benzene at Temperatures of (303.15, 313.15, and 323.15) K and a Pressure of 0.1 MPa
ρl	862.23	kg/m3	298.15	Quaternary (liquid + liquid) equilibrium data for the extraction of toluene from alkanes using the ionic liquid [EMim][MSO4]
ρl	862.22	kg/m3	298.15	Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
ρl	862.23	kg/m3	298.15	(Liquid + liquid) equilibrium of ternary and quaternary systems containing heptane, cyclohexane, toluene and the ionic liquid [EMim][N(CN)2]. Experimental data and correlation
ρl	862.20	kg/m3	298.15	Fully automatized apparatus for determining speed of sound for liquids in the temperature and pressure interval (283.15-343.15) K and (0.1-95) MPa
ρl	862.21	kg/m3	298.15	Conformational analysis of branched alkanes using limiting partial molar volumes
ρl	862.19	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	866.90	kg/m3	298.15	Liquid-liquid equilibria for ternary mixtures of 2,2-dimethyl-1,3-dioxolane-4-methanol with n-heptane, toluene, ethanol and water
ρl	862.00	kg/m3	298.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	862.21	kg/m3	298.15	Molar Excess Volumes and Excess Isentropic Compressibilities of Ternary Mixtures of o-Toluidine
ρl	862.19	kg/m3	298.15	Excess Enthalpies of Chloroalkylbenzene + Alkylbenzene Mixtures
ρl	862.18	kg/m3	298.15	Thermodynamic Properties of Ternary Liquid Mixtures Containing o-Chlorotoluene: Excess Molar Volumes and Excess Isentropic Compressibilities
ρl	863.67	kg/m3	298.15	Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
ρl	862.29	kg/m3	298.15	Thermodynamics of Mixtures Containing Amines. XII. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for N-Methylaniline + Hydrocarbon Systems
ρl	862.34	kg/m3	298.15	Evaluation of the Performance of Four Solvents for the Liquid Liquid Extraction of Acrylic Acid from Water
ρl	862.21	kg/m3	298.15	Experimental measurements and modelling of volumetric properties, refractive index and viscosity of binary systems of ethyl lactate with methyl ethyl ketone, toluene and n-methyl-2-pirrolidone at 288.15 323.15 K and atmospheric pressure. New UNIFAC VISCO and ASOG VISCO interaction parameters
ρl	862.34	kg/m3	298.15	Liquid liquid equilibria in the ternary systems {hexadecane + BTX aromatics + 2-methoxyethanol or acetonitrile} at 298.15 K
ρl	862.18	kg/m3	298.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρl	862.23	kg/m3	298.15	Excess Molar Volumes of 2,4,6,8-Tetramethylcyclotetrasiloxane with Benzene, Toluene, and Xylene at T = (288.15, 298.15, and 308.15) K
ρl	862.27	kg/m3	298.15	Liquid-Liquid Equilibrium in Ternary Systems Containing Ethylene Glycol, Monofunctional Benzene Derivative, and Ethyl Acetate
ρl	862.22	kg/m3	298.15	Isobaric Thermal Expansivities of Toluene Measured by Scanning Transitiometry at Temperatures from (243 to 423) K and Pressures up to 200 MPa
ρl	862.23	kg/m3	298.15	Topological Investigations of Excess Molar Volumes and Excess Isentropic Compressibilities of Ternary Mixtures Containing Pyrrolidin-2-one at 308.15 K
ρl	862.00	kg/m3	298.15	Densities and Kinematic Viscosities of One Quinary Regular Liquid System and Its Five Quaternary Sub-Systems at Temperatures (293.15 and 298.15) K
ρl	862.00	kg/m3	298.15	Densities and Kinematic Viscosities of a Quinary Regular Liquid System and Its Five Quaternary Subsystems at 293.15A K and 298.15A K
ρl	862.27	kg/m3	298.15	Binary liquid liquid equilibrium in the systems containing monofunctional benzene derivates and 1,2-ethanediol
ρl	863.67	kg/m3	298.15	Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
ρl	866.90	kg/m3	298.15	Liquid-liquid equilibria for multicomponent mixtures of 2,2-dimethyl-1,3-dioxolane with n-heptane, toluene, ethanol and water
ρl	862.35	kg/m3	298.15	Mutual Solubilities of Terpene in Methanol and Water and Their Multicomponent Liquid-Liquid Equilibria
ρl	862.19	kg/m3	298.15	Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
ρl	862.21	kg/m3	298.15	Thermodynamic Properties of Ternary Liquid Mixtures of 2-Pyrrolidinone with Aromatic Hydrocarbons
ρl	861.74	kg/m3	298.15	Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
ρl	862.20	kg/m3	298.15	Thermodynamics of Ternary Liquid Mixtures Containing Toluene, Ethylbenzene, and Chlorobenzene
ρl	862.18	kg/m3	298.15	Desulfurization of fuels by liquid-liquid extraction with1-ethyl-3-methylimidazolium ionic liquids
ρl	862.18	kg/m3	298.15	Heat capacities of binary and ternary mixtures containing o-chlorotoluene, cyclic ether and aromatic hydrocarbons
ρl	862.18	kg/m3	298.15	Densities, viscosities and ultrasonic velocities of binary mixtures of methylbenzene with hexan-2-ol, heptan-2-ol and octan-2-ol at T = 298.15 and 308.15K
ρl	864.99	kg/m3	298.15	Liquid liquid equilibrium of ternary systems 1-butyl-3-methylimidazolium hexafluorophosphate + aromatic + aliphatic
ρl	862.10	kg/m3	298.15	Determination and Correlation of Liquid-Liquid Equilibria Data for Water + Cyclohexanol + (Mesityl Oxide, Toluene, and p-Xylene) Ternary Systems at Different Temperatures
ρl	862.23	kg/m3	298.15	Isothermal vapor liquid equilibrium at 333.15K and excess molar volumes at 298.15K for the ternary system di-isopropyl ether + n-propyl alcohol + toluene and its binary subsystems
ρl	861.94	kg/m3	298.20	Isothermal Vapor-Liquid Equilibrium Data for Binary Systems of CHF3 or C2F6 with Methylcyclohexane or Toluene
ρl	862.49	kg/m3	298.20	The impact of uni-univalent electrolytes on (water + acetic acid + toluene) equilibria: Representation with electrolyte-NRTL model
ρl	861.45	kg/m3	298.70	Isothermal Vapor-Liquid Equilibrium Data for Binary Systems of CHF3 or C2F6 with Methylcyclohexane or Toluene
ρl	857.50	kg/m3	303.15	Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
ρl	857.47	kg/m3	303.15	Vapor-Liquid Equilibria in Ternary Systems of Toluene or Octane + Phenols + Water
ρl	857.50	kg/m3	303.15	Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
ρl	857.50	kg/m3	303.15	Volumetric properties of binary liquid mixtures: Application of the Prigogine Flory Patterson theory to excess molar volumes of dichloromethane with benzene or toluene
ρl	858.00	kg/m3	303.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	857.53	kg/m3	303.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl	857.64	kg/m3	303.15	Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
ρl	857.50	kg/m3	303.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene and Trans-decahydronaphthalene
ρl	857.51	kg/m3	303.15	Thermodynamic Properties of Ternary Liquid Mixtures Containing o-Chlorotoluene: Excess Molar Volumes and Excess Isentropic Compressibilities
ρl	857.73	kg/m3	303.15	Thermodynamics of Mixtures Containing Amines. XII. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for N-Methylaniline + Hydrocarbon Systems
ρl	857.51	kg/m3	303.15	Heat capacities of binary and ternary mixtures containing o-chlorotoluene, cyclic ether and aromatic hydrocarbons
ρl	857.61	kg/m3	303.15	Measurement of phase equilibria data for the extraction of toluene from alkane using different solvents
ρl	857.51	kg/m3	303.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρl	857.52	kg/m3	303.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
ρl	857.50	kg/m3	303.15	Densities and Dynamic Viscosities of Alicyclic Cyclohexane with Toluene, o-Xylene, and Mesitylene at T = (303.15 to 323.15) K and Atmospheric Pressure
ρl	857.39	kg/m3	303.15	Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
ρl	857.58	kg/m3	303.15	Volumetric and acoustic properties of binary systems (furfural or furfuryl alcohol + toluene) and (furfuryl alcohol + ethanol) at different temperatures
ρl	857.55	kg/m3	303.15	Isobaric Thermal Expansivities of Toluene Measured by Scanning Transitiometry at Temperatures from (243 to 423) K and Pressures up to 200 MPa
ρl	855.63	kg/m3	303.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	855.94	kg/m3	303.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	856.12	kg/m3	303.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	852.86	kg/m3	308.15	Isobaric Thermal Expansivities of Toluene Measured by Scanning Transitiometry at Temperatures from (243 to 423) K and Pressures up to 200 MPa
ρl	852.82	kg/m3	308.15	Heat capacities of binary and ternary mixtures containing o-chlorotoluene, cyclic ether and aromatic hydrocarbons
ρl	851.69	kg/m3	308.15	Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
ρl	852.79	kg/m3	308.15	Densities, viscosities and ultrasonic velocities of binary mixtures of methylbenzene with hexan-2-ol, heptan-2-ol and octan-2-ol at T = 298.15 and 308.15K
ρl	852.80	kg/m3	308.15	Densities and Dynamic Viscosities of Alicyclic Cyclohexane with Toluene, o-Xylene, and Mesitylene at T = (303.15 to 323.15) K and Atmospheric Pressure
ρl	852.83	kg/m3	308.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρl	852.93	kg/m3	308.15	Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
ρl	852.82	kg/m3	308.15	Thermodynamic Properties of Ternary Liquid Mixtures Containing o-Chlorotoluene: Excess Molar Volumes and Excess Isentropic Compressibilities
ρl	848.07	kg/m3	313.15	Vapor-Liquid Equilibria in Ternary Systems of Toluene or Octane + Phenols + Water
ρl	848.11	kg/m3	313.15	Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
ρl	848.11	kg/m3	313.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene and Trans-decahydronaphthalene
ρl	848.80	kg/m3	313.15	Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
ρl	847.82	kg/m3	313.15	Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
ρl	848.00	kg/m3	313.15	Densities and Dynamic Viscosities of Alicyclic Cyclohexane with Toluene, o-Xylene, and Mesitylene at T = (303.15 to 323.15) K and Atmospheric Pressure
ρl	848.15	kg/m3	313.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρl	848.14	kg/m3	313.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
ρl	848.21	kg/m3	313.15	Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
ρl	848.00	kg/m3	313.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	848.14	kg/m3	313.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl	848.20	kg/m3	313.15	Volumetric and acoustic properties of binary systems (furfural or furfuryl alcohol + toluene) and (furfuryl alcohol + ethanol) at different temperatures
ρl	848.15	kg/m3	313.15	Isobaric Thermal Expansivities of Toluene Measured by Scanning Transitiometry at Temperatures from (243 to 423) K and Pressures up to 200 MPa
ρl	844.75	kg/m3	313.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	848.23	kg/m3	313.20	The impact of uni-univalent electrolytes on (water + acetic acid + toluene) equilibria: Representation with electrolyte-NRTL model
ρl	844.57	kg/m3	313.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	844.27	kg/m3	313.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	843.42	kg/m3	318.15	Isobaric Thermal Expansivities of Toluene Measured by Scanning Transitiometry at Temperatures from (243 to 423) K and Pressures up to 200 MPa
ρl	843.49	kg/m3	318.15	Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
ρl	843.44	kg/m3	318.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρl	842.88	kg/m3	318.15	Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
ρl	843.30	kg/m3	318.15	Densities and Dynamic Viscosities of Alicyclic Cyclohexane with Toluene, o-Xylene, and Mesitylene at T = (303.15 to 323.15) K and Atmospheric Pressure
ρl	838.42	kg/m3	323.15	Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
ρl	838.66	kg/m3	323.15	Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
ρl	838.70	kg/m3	323.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl	838.67	kg/m3	323.15	Isobaric Thermal Expansivities of Toluene Measured by Scanning Transitiometry at Temperatures from (243 to 423) K and Pressures up to 200 MPa
ρl	838.66	kg/m3	323.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene and Trans-decahydronaphthalene
ρl	838.68	kg/m3	323.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
ρl	838.90	kg/m3	323.15	Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
ρl	838.73	kg/m3	323.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρl	838.50	kg/m3	323.15	Densities and Dynamic Viscosities of Alicyclic Cyclohexane with Toluene, o-Xylene, and Mesitylene at T = (303.15 to 323.15) K and Atmospheric Pressure
ρl	840.00	kg/m3	323.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	833.51	kg/m3	323.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	833.68	kg/m3	323.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	833.21	kg/m3	323.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	833.90	kg/m3	328.15	Isobaric Thermal Expansivities of Toluene Measured by Scanning Transitiometry at Temperatures from (243 to 423) K and Pressures up to 200 MPa
ρl	834.00	kg/m3	328.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρl	829.11	kg/m3	333.15	Isobaric Thermal Expansivities of Toluene Measured by Scanning Transitiometry at Temperatures from (243 to 423) K and Pressures up to 200 MPa
ρl	831.00	kg/m3	333.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	829.25	kg/m3	333.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρl	829.12	kg/m3	333.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene and Trans-decahydronaphthalene
ρl	829.15	kg/m3	333.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
ρl	829.16	kg/m3	333.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl	829.60	kg/m3	333.15	Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
ρl	828.94	kg/m3	333.15	Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
ρl	829.13	kg/m3	333.15	Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
ρl	822.73	kg/m3	333.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	822.90	kg/m3	333.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	822.43	kg/m3	333.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	824.30	kg/m3	338.15	Isobaric Thermal Expansivities of Toluene Measured by Scanning Transitiometry at Temperatures from (243 to 423) K and Pressures up to 200 MPa
ρl	819.51	kg/m3	343.15	Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
ρl	819.60	kg/m3	343.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
ρl	819.60	kg/m3	343.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl	821.00	kg/m3	343.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	819.47	kg/m3	343.15	Isobaric Thermal Expansivities of Toluene Measured by Scanning Transitiometry at Temperatures from (243 to 423) K and Pressures up to 200 MPa
ρl	820.20	kg/m3	343.15	Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
ρl	812.22	kg/m3	343.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	812.39	kg/m3	343.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	811.93	kg/m3	343.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	814.62	kg/m3	348.15	Isobaric Thermal Expansivities of Toluene Measured by Scanning Transitiometry at Temperatures from (243 to 423) K and Pressures up to 200 MPa
ρl	809.75	kg/m3	353.15	Isobaric Thermal Expansivities of Toluene Measured by Scanning Transitiometry at Temperatures from (243 to 423) K and Pressures up to 200 MPa
ρl	809.80	kg/m3	353.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
ρl	809.70	kg/m3	353.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl	801.98	kg/m3	353.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	801.69	kg/m3	353.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	802.15	kg/m3	353.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	804.86	kg/m3	358.15	Isobaric Thermal Expansivities of Toluene Measured by Scanning Transitiometry at Temperatures from (243 to 423) K and Pressures up to 200 MPa
ρl	799.96	kg/m3	363.15	Isobaric Thermal Expansivities of Toluene Measured by Scanning Transitiometry at Temperatures from (243 to 423) K and Pressures up to 200 MPa
ρl	799.70	kg/m3	363.15	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl	791.71	kg/m3	363.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	792.00	kg/m3	363.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	792.16	kg/m3	363.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	781.97	kg/m3	373.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	782.42	kg/m3	373.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
ρl	782.26	kg/m3	373.20	Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
D*i	[0.00; 0.00]	m2/s	[239.09; 343.45]
D*i	0.00	m2/s	239.09	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	240.94	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	248.57	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	251.71	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	253.27	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	253.28	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	258.16	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	258.23	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	263.51	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	268.32	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	273.43	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	273.54	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	278.07	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	278.15	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	288.05	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	293.08	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	298.00	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	298.18	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	298.20	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	298.21	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	298.21	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	298.21	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	308.07	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	322.69	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	323.16	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	323.18	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	332.93	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	333.16	Viscous Calibration Liquids for Self-diffusion Measurements
D*i	0.00	m2/s	343.45	Viscous Calibration Liquids for Self-diffusion Measurements
ΔfusS	[36.79; 37.25]	J/mol×K	[177.95; 178.15]
ΔfusS	37.20	J/mol×K	177.95	NIST
ΔfusS	37.20	J/mol×K	177.95	NIST
ΔfusS	36.79	J/mol×K	178.00	NIST
ΔfusS	37.25	J/mol×K	178.15	NIST
ΔfusS	37.25	J/mol×K	178.15	NIST
csound,fluid	[425.50; 1394.10]	m/s	[278.15; 523.15]
csound,fluid	1394.10	m/s	278.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
csound,fluid	1371.50	m/s	283.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
csound,fluid	1347.50	m/s	288.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1349.10	m/s	288.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
csound,fluid	1347.50	m/s	288.15	Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
csound,fluid	1336.32	m/s	290.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1325.34	m/s	293.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1326.90	m/s	293.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
csound,fluid	1328.60	m/s	293.15	Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
csound,fluid	1314.33	m/s	295.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1307.30	m/s	298.15	Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
csound,fluid	1303.00	m/s	298.15	Thermodynamic and topological investigations of molecular interactions in binary and ternary mixtures containing 1-methyl pyrrolidin-2-one at T = 308.15 K
csound,fluid	1303.44	m/s	298.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1305.10	m/s	298.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
csound,fluid	1303.00	m/s	298.15	Isentropic Compressibilities Changes of Mixing of Tetrahydropyran and Aromatic Hydrocarbons Ternary Mixtures at 308.15 K
csound,fluid	1304.00	m/s	298.15	Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
csound,fluid	1304.00	m/s	298.15	Densities, Excess Molar Volumes at T = (298.15 to 313.15) K, Speeds of Sound, Excess Isentropic Compressibilities, Relative Permittivities and Deviations in Molar Polarizations at T = (298.15 and 308.15) K for Methyl Methacrylate + 2-Butoxyethanol or + Dibutyl Ether + Benzene, + Toluene and + p-Xylene
csound,fluid	1303.44	m/s	298.15	Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
csound,fluid	1292.64	m/s	300.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1283.60	m/s	303.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
csound,fluid	1281.88	m/s	303.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1285.50	m/s	303.15	Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
csound,fluid	1271.16	m/s	305.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1262.00	m/s	308.15	Densities, Excess Molar Volumes at T = (298.15 to 313.15) K, Speeds of Sound, Excess Isentropic Compressibilities, Relative Permittivities and Deviations in Molar Polarizations at T = (298.15 and 308.15) K for Methyl Methacrylate + 2-Butoxyethanol or + Dibutyl Ether + Benzene, + Toluene and + p-Xylene
csound,fluid	1262.20	m/s	308.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
csound,fluid	1262.00	m/s	308.15	Thermodynamic and topological investigations of molecular interactions in binary and ternary mixtures containing 1-methyl pyrrolidin-2-one at T = 308.15 K
csound,fluid	1262.00	m/s	308.15	Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
csound,fluid	1260.49	m/s	308.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1264.20	m/s	308.15	Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
csound,fluid	1249.83	m/s	310.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1240.90	m/s	313.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
csound,fluid	1242.40	m/s	313.15	Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
csound,fluid	1239.22	m/s	313.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1228.62	m/s	315.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1220.70	m/s	318.15	Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
csound,fluid	1219.90	m/s	318.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
csound,fluid	1218.01	m/s	318.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1207.31	m/s	320.65	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1198.90	m/s	323.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
csound,fluid	1196.60	m/s	323.15	Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
csound,fluid	1200.80	m/s	323.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	1196.60	m/s	323.15	Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid	1200.80	m/s	323.15	Speed of sound measurement in ethyl tert-butyl ether and tert-amyl methyl ether by Brillouin light scattering
csound,fluid	1178.20	m/s	328.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
csound,fluid	1157.70	m/s	333.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
csound,fluid	1137.20	m/s	338.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
csound,fluid	1117.00	m/s	343.15	Advanced calibration, adjustment, and operation of a density and sound speed analyzer
csound,fluid	1000.00	m/s	373.15	Speed of sound measurement in ethyl tert-butyl ether and tert-amyl methyl ether by Brillouin light scattering
csound,fluid	806.00	m/s	423.15	Speed of sound measurement in ethyl tert-butyl ether and tert-amyl methyl ether by Brillouin light scattering
csound,fluid	806.00	m/s	423.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
csound,fluid	616.20	m/s	473.15	Speed of sound measurement in ethyl tert-butyl ether and tert-amyl methyl ether by Brillouin light scattering
csound,fluid	425.50	m/s	523.15	Speed of sound measurement in ethyl tert-butyl ether and tert-amyl methyl ether by Brillouin light scattering
csound,fluid	425.50	m/s	523.15	Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
γ	[0.02; 0.03]	N/m	[277.85; 368.14]
γ	0.03	N/m	277.85	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.03	N/m	278.15	Thermodynamic investigation of N,N-dimethylformamide/toluene binary mixtures in the temperature range from 278.15 to 293.15 K
γ	0.03	N/m	283.15	Thermodynamic investigation of N,N-dimethylformamide/toluene binary mixtures in the temperature range from 278.15 to 293.15 K
γ	0.03	N/m	287.81	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.03	N/m	288.15	Surface Tension of the Ternary System Water + Acetone + Toluene
γ	0.03	N/m	293.00	Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
γ	0.03	N/m	293.15	Thermodynamic investigation of N,N-dimethylformamide/toluene binary mixtures in the temperature range from 278.15 to 293.15 K
γ	0.03	N/m	293.20	KDB
γ	0.03	N/m	297.82	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.03	N/m	298.15	Surface Tension of the Ternary System Water + Acetone + Toluene
γ	0.03	N/m	298.15	NCMS SOLV-DB
γ	0.03	N/m	302.83	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.03	N/m	303.16	Surface tension of four oxygenated fuels: experiment and correlation
γ	0.03	N/m	307.86	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.03	N/m	308.15	Surface tension of four oxygenated fuels: experiment and correlation
γ	0.03	N/m	308.15	Surface Tension of the Ternary System Water + Acetone + Toluene
γ	0.03	N/m	312.87	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.03	N/m	313.15	Surface tension of four oxygenated fuels: experiment and correlation
γ	0.03	N/m	317.86	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.03	N/m	318.13	Surface tension of four oxygenated fuels: experiment and correlation
γ	0.03	N/m	318.15	Surface Tension of the Ternary System Water + Acetone + Toluene
γ	0.02	N/m	323.15	Surface tension of four oxygenated fuels: experiment and correlation
γ	0.02	N/m	327.88	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.02	N/m	328.15	Surface Tension of the Ternary System Water + Acetone + Toluene
γ	0.02	N/m	328.16	Surface tension of four oxygenated fuels: experiment and correlation
γ	0.02	N/m	333.14	Surface tension of four oxygenated fuels: experiment and correlation
γ	0.02	N/m	337.88	Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ	0.02	N/m	338.16	Surface tension of four oxygenated fuels: experiment and correlation
γ	0.02	N/m	343.16	Surface tension of four oxygenated fuels: experiment and correlation
γ	0.02	N/m	348.16	Surface tension of four oxygenated fuels: experiment and correlation
γ	0.02	N/m	353.15	Surface tension of four oxygenated fuels: experiment and correlation
γ	0.02	N/m	358.15	Surface tension of four oxygenated fuels: experiment and correlation
γ	0.02	N/m	363.16	Surface tension of four oxygenated fuels: experiment and correlation
γ	0.02	N/m	368.14	Surface tension of four oxygenated fuels: experiment and correlation
λliquid	[0.11; 0.15]	W/m×K	[234.60; 375.71]
λliquid	0.15	W/m×K	234.60	Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
λliquid	0.14	W/m×K	254.58	Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
λliquid	0.14	W/m×K	272.64	Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
λliquid	0.14	W/m×K	273.17	Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
λliquid	0.14	W/m×K	273.45	Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
λliquid	0.14	W/m×K	274.65	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.14	W/m×K	275.40	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.14	W/m×K	275.95	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.14	W/m×K	276.19	Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
λliquid	0.14	W/m×K	276.31	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.13	W/m×K	278.42	Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
λliquid	0.13	W/m×K	281.25	Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
λliquid	0.13	W/m×K	281.25	Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
λliquid	0.13	W/m×K	287.33	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.13	W/m×K	288.72	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.13	W/m×K	289.65	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.13	W/m×K	293.23	Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
λliquid	0.13	W/m×K	294.45	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.13	W/m×K	294.69	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.13	W/m×K	295.01	Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
λliquid	0.13	W/m×K	295.07	Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
λliquid	0.13	W/m×K	295.08	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.13	W/m×K	295.47	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.13	W/m×K	295.79	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.13	W/m×K	297.45	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.13	W/m×K	298.60	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.13	W/m×K	300.43	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.13	W/m×K	302.05	Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
λliquid	0.13	W/m×K	304.59	Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
λliquid	0.13	W/m×K	307.66	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.13	W/m×K	308.62	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.13	W/m×K	310.22	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.13	W/m×K	314.68	Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
λliquid	0.13	W/m×K	314.69	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.13	W/m×K	314.74	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.13	W/m×K	315.55	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.13	W/m×K	315.85	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.13	W/m×K	316.70	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.13	W/m×K	316.82	Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
λliquid	0.13	W/m×K	317.94	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.12	W/m×K	318.80	Thermal conductivity of ethyl fluoride (HFC161)
λliquid	0.12	W/m×K	318.84	Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
λliquid	0.12	W/m×K	319.32	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.12	W/m×K	319.96	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.12	W/m×K	321.21	Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
λliquid	0.12	W/m×K	327.65	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.12	W/m×K	328.48	Thermal conductivity of ethyl fluoride (HFC161)
λliquid	0.12	W/m×K	329.50	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.12	W/m×K	329.65	Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
λliquid	0.12	W/m×K	330.77	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.12	W/m×K	331.24	Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
λliquid	0.12	W/m×K	333.34	Thermal conductivity of ethyl fluoride (HFC161)
λliquid	0.12	W/m×K	334.99	Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
λliquid	0.12	W/m×K	335.27	Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
λliquid	0.12	W/m×K	337.36	Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
λliquid	0.12	W/m×K	337.63	Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
λliquid	0.12	W/m×K	338.23	Thermal conductivity of ethyl fluoride (HFC161)
λliquid	0.12	W/m×K	338.39	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.12	W/m×K	339.65	Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
λliquid	0.12	W/m×K	339.77	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.12	W/m×K	339.85	Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
λliquid	0.12	W/m×K	340.17	Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
λliquid	0.12	W/m×K	340.62	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.12	W/m×K	341.16	Thermal conductivity of ethyl fluoride (HFC161)
λliquid	0.12	W/m×K	343.09	Thermal conductivity of ethyl fluoride (HFC161)
λliquid	0.12	W/m×K	346.01	Thermal conductivity of ethyl fluoride (HFC161)
λliquid	0.12	W/m×K	347.00	Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
λliquid	0.11	W/m×K	350.87	Thermal conductivity of ethyl fluoride (HFC161)
λliquid	0.12	W/m×K	351.33	Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
λliquid	0.12	W/m×K	351.55	Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
λliquid	0.12	W/m×K	352.25	Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
λliquid	0.11	W/m×K	354.89	Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
λliquid	0.11	W/m×K	355.63	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.12	W/m×K	355.71	Thermal conductivity of ethyl fluoride (HFC161)
λliquid	0.11	W/m×K	355.95	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.11	W/m×K	357.02	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.11	W/m×K	365.42	Thermal conductivity of ethyl fluoride (HFC161)
λliquid	0.11	W/m×K	370.29	Thermal conductivity of ethyl fluoride (HFC161)
λliquid	0.11	W/m×K	373.92	Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
λliquid	0.11	W/m×K	375.26	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.11	W/m×K	375.26	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
λliquid	0.11	W/m×K	375.71	Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
αdiff	[4.66e-08; 8.63e-08]	m2/s	[302.90; 523.38]
αdiff	8.63e-08	m2/s	302.90	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	8.33e-08	m2/s	312.45	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	8.03e-08	m2/s	323.07	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	7.77e-08	m2/s	333.27	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	7.52e-08	m2/s	343.52	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	7.30e-08	m2/s	353.73	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	7.09e-08	m2/s	363.73	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	6.90e-08	m2/s	373.04	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	6.71e-08	m2/s	382.94	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	6.52e-08	m2/s	392.88	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	6.33e-08	m2/s	402.93	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	6.15e-08	m2/s	413.06	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	5.98e-08	m2/s	422.73	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	5.81e-08	m2/s	432.67	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	5.64e-08	m2/s	442.68	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	5.48e-08	m2/s	452.96	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	5.33e-08	m2/s	462.99	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	5.19e-08	m2/s	473.20	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	5.06e-08	m2/s	482.98	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	4.94e-08	m2/s	493.05	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	4.84e-08	m2/s	503.17	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	4.74e-08	m2/s	513.41	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
αdiff	4.66e-08	m2/s	523.38	Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil(P)	[345.50; 418.60]	K	[29.65; 247.50]
Tboil(P)	345.50	K	29.65	Application of a DSC based vapor pressure method for examining the extent of ideality in associating binary mixtures with narrow boiling range oil cuts as a mixture component
Tboil(P)	360.60	K	49.44	Application of a DSC based vapor pressure method for examining the extent of ideality in associating binary mixtures with narrow boiling range oil cuts as a mixture component
Tboil(P)	371.10	K	69.20	Application of a DSC based vapor pressure method for examining the extent of ideality in associating binary mixtures with narrow boiling range oil cuts as a mixture component
Tboil(P)	383.05	K	95.30	Excess enthalpies of dimethylsulfoxide with substituted benzenes at 298.15K
Tboil(P)	384.95	K	96.60	Low cost apparatus for rapid boiling point determination of small air sensitive samples under inert atmosphere
Tboil(P)	384.30	K	101.60	Application of a DSC based vapor pressure method for examining the extent of ideality in associating binary mixtures with narrow boiling range oil cuts as a mixture component
Tboil(P)	418.60	K	247.50	Application of a DSC based vapor pressure method for examining the extent of ideality in associating binary mixtures with narrow boiling range oil cuts as a mixture component
Tboilr	287.70	K	2.00	NIST

Datasets

1. Viscosity, Pa*s (11)
2. Relative permittivity at zero frequency (1)
3. Refractive index (Na D-line) (1)
4. Mass density, kg/m3 (14)
5. Speed of sound, m/s (4)
6. Thermal conductivity, W/m/K (2)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
273.13	1000.00	0.0008
273.13	5000.00	0.0008
273.13	10000.00	0.0008
273.13	20000.00	0.0009
273.13	30000.00	0.0010
298.15	1000.00	0.0006
298.15	5000.00	0.0006
298.15	10000.00	0.0006
298.15	20000.00	0.0006
298.15	30000.00	0.0007
323.16	1000.00	0.0004
323.16	5000.00	0.0004
323.16	10000.00	0.0005
323.16	20000.00	0.0005
323.16	30000.00	0.0005
343.16	1000.00	0.0003
343.16	5000.00	0.0004
343.16	10000.00	0.0004
343.16	20000.00	0.0004
343.16	30000.00	0.0004
363.16	1000.00	0.0003
363.16	5000.00	0.0003
363.16	10000.00	0.0003
363.16	20000.00	0.0003
363.16	30000.00	0.0004
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
293.15	100.00	0.0006
293.15	1000.00	0.0006
293.15	5000.00	0.0006
293.15	10000.00	0.0006
293.15	20000.00	0.0007
293.15	30000.00	0.0007
293.15	40000.00	0.0008
293.15	50000.00	0.0009
293.15	60000.00	0.0009
293.15	70000.00	0.0010
293.15	80000.00	0.0010
293.15	100000.00	0.0011
293.15	120000.00	0.0013
293.15	140000.00	0.0015
298.15	100.00	0.0006
298.15	1000.00	0.0006
298.15	5000.00	0.0006
298.15	10000.00	0.0006
298.15	20000.00	0.0006
298.15	30000.00	0.0007
298.15	40000.00	0.0007
298.15	50000.00	0.0008
298.15	60000.00	0.0008
298.15	70000.00	0.0009
298.15	80000.00	0.0010
298.15	100000.00	0.0011
298.15	120000.00	0.0012
298.15	140000.00	0.0013
313.15	100.00	0.0005
313.15	1000.00	0.0005
313.15	5000.00	0.0005
313.15	10000.00	0.0005
313.15	20000.00	0.0005
313.15	30000.00	0.0006
313.15	40000.00	0.0006
313.15	50000.00	0.0007
313.15	60000.00	0.0007
313.15	70000.00	0.0008
313.15	80000.00	0.0008
313.15	100000.00	0.0009
313.15	120000.00	0.0010
313.15	140000.00	0.0011
323.15	100.00	0.0004
323.15	1000.00	0.0004
323.15	5000.00	0.0004
323.15	10000.00	0.0005
323.15	20000.00	0.0005
323.15	30000.00	0.0005
323.15	40000.00	0.0006
323.15	50000.00	0.0006
323.15	60000.00	0.0006
323.15	70000.00	0.0007
323.15	80000.00	0.0007
323.15	100000.00	0.0008
323.15	120000.00	0.0009
323.15	140000.00	0.0010
333.15	100.00	0.0004
333.15	1000.00	0.0004
333.15	5000.00	0.0004
333.15	10000.00	0.0004
333.15	20000.00	0.0004
333.15	30000.00	0.0005
333.15	40000.00	0.0005
333.15	50000.00	0.0005
333.15	60000.00	0.0006
333.15	70000.00	0.0006
333.15	80000.00	0.0007
333.15	100000.00	0.0007
333.15	120000.00	0.0008
333.15	140000.00	0.0009
348.15	100.00	0.0003
348.15	1000.00	0.0003
348.15	5000.00	0.0003
348.15	10000.00	0.0004
348.15	20000.00	0.0004
348.15	30000.00	0.0004
348.15	40000.00	0.0004
348.15	50000.00	0.0005
348.15	60000.00	0.0005
348.15	70000.00	0.0005
348.15	80000.00	0.0006
348.15	100000.00	0.0006
348.15	120000.00	0.0007
348.15	140000.00	0.0008
353.15	100.00	0.0003
353.15	1000.00	0.0003
353.15	5000.00	0.0003
353.15	10000.00	0.0003
353.15	20000.00	0.0004
353.15	30000.00	0.0004
353.15	40000.00	0.0004
353.15	50000.00	0.0005
353.15	60000.00	0.0005
353.15	70000.00	0.0005
353.15	80000.00	0.0005
353.15	100000.00	0.0006
353.15	120000.00	0.0007
353.15	140000.00	0.0008
373.15	100.00	0.0003
373.15	1000.00	0.0003
373.15	5000.00	0.0003
373.15	10000.00	0.0003
373.15	20000.00	0.0003
373.15	30000.00	0.0003
373.15	40000.00	0.0004
373.15	50000.00	0.0004
373.15	60000.00	0.0004
373.15	70000.00	0.0004
373.15	80000.00	0.0005
373.15	100000.00	0.0005
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.15	101.30	0.0005
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.15	100.00	0.0006
298.15	2110.00	0.0006
298.15	4100.00	0.0006
298.15	6100.00	0.0006
298.15	8110.00	0.0006
298.15	10110.00	0.0006
323.15	100.00	0.0004
323.15	2080.00	0.0004
323.15	4110.00	0.0004
323.15	6000.00	0.0004
323.15	8120.00	0.0004
323.15	10050.00	0.0005
323.15	12210.00	0.0005
323.15	15000.00	0.0005
348.15	100.00	0.0003
348.15	2120.00	0.0003
348.15	12110.00	0.0004
348.15	15210.00	0.0004
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.15	100.00	0.0005
303.15	1000.00	0.0005
303.15	5000.00	0.0005
303.15	10000.00	0.0006
303.15	15000.00	0.0006
303.15	20000.00	0.0006
303.15	25000.00	0.0006
303.15	30000.00	0.0007
303.15	35000.00	0.0007
303.15	40000.00	0.0007
303.15	45000.00	0.0007
303.15	50000.00	0.0008
303.15	55000.00	0.0008
303.15	60000.00	0.0008
313.15	100.00	0.0005
313.15	1000.00	0.0005
313.15	5000.00	0.0005
313.15	10000.00	0.0005
313.15	15000.00	0.0005
313.15	20000.00	0.0006
313.15	25000.00	0.0006
313.15	30000.00	0.0006
313.15	35000.00	0.0006
313.15	40000.00	0.0006
313.15	45000.00	0.0007
313.15	50000.00	0.0007
313.15	55000.00	0.0007
313.15	60000.00	0.0007
323.15	100.00	0.0004
323.15	1000.00	0.0004
323.15	5000.00	0.0004
323.15	10000.00	0.0005
323.15	15000.00	0.0005
323.15	20000.00	0.0005
323.15	25000.00	0.0005
323.15	30000.00	0.0005
323.15	35000.00	0.0006
323.15	40000.00	0.0006
323.15	45000.00	0.0006
323.15	50000.00	0.0006
323.15	55000.00	0.0006
323.15	60000.00	0.0007
333.15	100.00	0.0004
333.15	1000.00	0.0004
333.15	5000.00	0.0004
333.15	10000.00	0.0004
333.15	15000.00	0.0004
333.15	20000.00	0.0004
333.15	25000.00	0.0005
333.15	30000.00	0.0005
333.15	35000.00	0.0005
333.15	40000.00	0.0005
333.15	45000.00	0.0005
333.15	50000.00	0.0006
333.15	55000.00	0.0006
333.15	60000.00	0.0006
343.15	100.00	0.0003
343.15	1000.00	0.0004
343.15	5000.00	0.0004
343.15	10000.00	0.0004
343.15	15000.00	0.0004
343.15	20000.00	0.0004
343.15	25000.00	0.0004
343.15	30000.00	0.0004
343.15	35000.00	0.0005
343.15	40000.00	0.0005
343.15	45000.00	0.0005
343.15	50000.00	0.0005
343.15	55000.00	0.0005
343.15	60000.00	0.0005
353.15	100.00	0.0003
353.15	1000.00	0.0003
353.15	5000.00	0.0003
353.15	10000.00	0.0003
353.15	15000.00	0.0004
353.15	20000.00	0.0004
353.15	25000.00	0.0004
353.15	30000.00	0.0004
353.15	35000.00	0.0004
353.15	40000.00	0.0004
353.15	45000.00	0.0004
353.15	50000.00	0.0005
353.15	55000.00	0.0005
353.15	60000.00	0.0005
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
323.15	100.00	0.0004
323.15	13940.00	0.0005
323.15	27338.00	0.0005
323.15	41055.00	0.0006
323.15	54593.00	0.0006
323.15	68135.00	0.0007
373.11	13270.00	0.0003
373.11	26975.00	0.0003
373.11	40789.00	0.0004
373.11	54631.00	0.0004
373.11	68196.00	0.0004
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
248.16	1000.00	0.0012
248.16	10000.00	0.0013
248.16	20000.00	0.0014
248.16	30000.00	0.0015
273.15	1000.00	0.0008
273.15	10000.00	0.0008
273.15	20000.00	0.0009
273.15	30000.00	0.0010
273.15	40000.00	0.0010
298.14	1000.00	0.0006
298.14	10000.00	0.0006
298.14	20000.00	0.0006
298.14	30000.00	0.0007
298.14	40000.00	0.0007
323.13	1000.00	0.0004
323.13	10000.00	0.0005
323.13	20000.00	0.0005
323.13	30000.00	0.0005
323.13	40000.00	0.0006
348.13	1000.00	0.0003
348.13	10000.00	0.0004
348.13	20000.00	0.0004
348.13	30000.00	0.0004
348.13	40000.00	0.0004
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
101.00	293.31	0.0006
101.00	303.04	0.0005
101.00	312.90	0.0005
101.00	322.79	0.0004
101.00	332.41	0.0004
2230.00	332.42	0.0004
4430.00	332.36	0.0004
6420.00	332.32	0.0004
8310.00	332.30	0.0004
10060.00	332.32	0.0004
11850.00	332.34	0.0004
14200.00	332.58	0.0004
15730.00	332.37	0.0004
17830.00	332.67	0.0004
1240.00	303.02	0.0005
2110.00	302.82	0.0005
3960.00	302.73	0.0005
5660.00	302.76	0.0006
7840.00	302.77	0.0006
9860.00	302.68	0.0006
12320.00	302.92	0.0006
14080.00	302.92	0.0006
15900.00	302.94	0.0006
17780.00	302.97	0.0006
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.15	100.00	0.0006
298.15	2300.00	0.0006
298.15	4400.00	0.0006
298.15	7430.00	0.0006
298.15	10400.00	0.0006
298.15	12470.00	0.0006
298.15	14490.00	0.0006
323.15	120.00	0.0004
323.15	3340.00	0.0004
323.15	6340.00	0.0004
323.15	9600.00	0.0005
323.15	12750.00	0.0005
323.15	14770.00	0.0005
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
313.15	100.00	0.0005
323.15	100.00	0.0004
333.15	100.00	0.0004
333.15	800.00	0.0004
333.15	1600.00	0.0004
333.15	2400.00	0.0004
333.15	3200.00	0.0004
343.15	100.00	0.0003
353.15	100.00	0.0003
363.15	100.00	0.0003
373.15	100.00	0.0003
373.15	800.00	0.0003
373.15	1600.00	0.0003
373.15	2400.00	0.0003
373.15	3200.00	0.0003
393.15	1600.00	0.0002
413.15	1600.00	0.0002
433.15	1600.00	0.0002
453.15	1600.00	0.0002
473.15	1600.00	0.0001
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
100.00	293.15	0.0006
100.00	313.15	0.0005
100.00	333.15	0.0004
100.00	353.15	0.0003
20000.00	293.15	0.0007
20000.00	313.15	0.0005
20000.00	333.15	0.0004
20000.00	353.15	0.0004
40000.00	293.15	0.0008
40000.00	313.15	0.0006
40000.00	333.15	0.0005
40000.00	353.15	0.0004
60000.00	293.15	0.0009
60000.00	313.15	0.0007
60000.00	333.15	0.0006
60000.00	353.15	0.0005
80000.00	293.15	0.0010
80000.00	313.15	0.0008
80000.00	333.15	0.0007
80000.00	353.15	0.0005
100000.00	293.15	0.0012
100000.00	313.15	0.0009
100000.00	333.15	0.0007
100000.00	353.15	0.0006
Reference

Relative permittivity at zero frequency

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Relative permittivity at zero frequency - Liquid
290.63	100.00	2.4045
290.65	100.00	2.4045
290.69	2170.00	2.4127
290.77	4240.00	2.4141
290.81	6310.00	2.4172
290.83	8370.00	2.4202
290.87	12510.00	2.4263
290.88	16100.00	2.4314
290.90	16650.00	2.4322
291.15	100.00	2.3983
292.65	100.00	2.4035
294.80	100.00	2.3909
310.68	100.00	2.3567
310.79	100.00	2.3565
311.94	100.00	2.3536
314.47	100.00	2.3479
315.68	100.00	2.3403
315.77	100.00	2.34
315.78	1140.00	2.3418
315.78	8370.00	2.3543
315.79	2170.00	2.3437
315.79	3200.00	2.3455
315.79	4240.00	2.3473
315.79	6310.00	2.3508
315.79	12510.00	2.3609
315.79	16650.00	2.3674
315.79	19410.00	2.3715
320.64	100.00	2.3293
320.66	1140.00	2.3311
324.52	100.00	2.3205
324.53	1140.00	2.3224
324.54	2170.00	2.3243
324.54	3200.00	2.3262
324.54	4240.00	2.3281
324.54	6310.00	2.3318
324.58	8370.00	2.3353
324.61	12510.00	2.3422
324.62	16650.00	2.349
339.31	100.00	2.2878
339.35	2170.00	2.2919
339.38	4240.00	2.296
339.38	6310.00	2.2999
339.39	8370.00	2.3038
339.41	12510.00	2.3113
339.41	16650.00	2.3184
357.44	6310.00	2.2616
357.45	2170.00	2.2526
357.45	4240.00	2.2572
357.46	100.00	2.2479
357.52	8370.00	2.2658
357.54	12510.00	2.274
357.55	16650.00	2.2818
390.53	170.00	2.1778
390.53	2170.00	2.1834
390.59	100.00	2.177
390.59	4240.00	2.189
390.61	6310.00	2.1943
390.63	8370.00	2.1997
390.65	12510.00	2.2097
390.68	16650.00	2.2193
405.84	2170.00	2.1495
406.30	6310.00	2.1608
406.32	4240.00	2.1547
406.37	8370.00	2.1665
406.54	12510.00	2.1772
406.64	16650.00	2.1873
Reference

Refractive index (Na D-line)

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Refractive index (Na D-line) - Liquid
100.00	293.15	1.4966
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
323.20	5240.00	843.3
323.20	10200.00	847.8
333.10	2090.00	830.7
333.10	4220.00	832.7
333.10	6360.00	834.8
333.10	10200.00	838.2
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	876.1
283.15	5000.00	879.5
283.15	10000.00	882.9
283.15	15000.00	886.1
283.15	20000.00	889.3
283.15	25000.00	892.4
283.15	30000.00	895.3
283.15	35000.00	898.2
283.15	40000.00	901.0
283.15	45000.00	903.7
293.15	100.00	866.8
293.15	5000.00	870.5
293.15	10000.00	874.1
293.15	15000.00	877.5
293.15	20000.00	880.8
293.15	25000.00	884.0
293.15	30000.00	887.1
293.15	35000.00	890.1
293.15	40000.00	893.0
293.15	45000.00	895.9
303.15	100.00	857.5
303.15	5000.00	861.4
303.15	10000.00	865.2
303.15	15000.00	868.8
303.15	20000.00	872.3
303.15	25000.00	875.7
303.15	30000.00	879.0
303.15	35000.00	882.1
303.15	40000.00	885.2
303.15	45000.00	888.1
313.15	100.00	848.1
313.15	5000.00	852.2
313.15	10000.00	856.2
313.15	15000.00	860.0
313.15	20000.00	863.7
313.15	25000.00	867.3
313.15	30000.00	870.7
313.15	35000.00	874.0
313.15	40000.00	877.2
313.15	45000.00	880.3
323.15	100.00	838.6
323.15	5000.00	843.0
323.15	10000.00	847.2
323.15	15000.00	851.3
323.15	20000.00	855.2
323.15	25000.00	858.9
323.15	30000.00	862.5
323.15	35000.00	866.0
323.15	40000.00	869.4
323.15	45000.00	872.6
333.15	100.00	828.8
333.15	5000.00	833.5
333.15	10000.00	838.0
333.15	15000.00	842.3
333.15	20000.00	846.4
333.15	25000.00	850.4
333.15	30000.00	854.2
333.15	35000.00	857.9
333.15	40000.00	861.4
333.15	45000.00	864.8
343.15	100.00	819.2
343.15	5000.00	824.1
343.15	10000.00	829.0
343.15	15000.00	833.5
343.15	20000.00	837.9
343.15	25000.00	842.1
343.15	30000.00	846.0
343.15	35000.00	849.9
343.15	40000.00	853.5
343.15	45000.00	857.0
353.15	100.00	809.4
353.15	5000.00	814.7
353.15	10000.00	819.9
353.15	15000.00	824.7
353.15	20000.00	829.3
353.15	25000.00	833.7
353.15	30000.00	837.9
353.15	35000.00	841.9
353.15	40000.00	845.7
353.15	45000.00	849.4
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	293.15	867.1
100.00	303.15	857.5
100.00	313.15	847.8
100.00	323.15	838.4
100.00	333.15	828.8
100.00	343.15	819.4
100.00	353.15	809.7
5000.00	293.15	870.6
5000.00	303.15	861.4
5000.00	313.15	852.0
5000.00	323.15	842.7
5000.00	333.15	833.5
5000.00	343.15	824.5
5000.00	353.15	815.1
10000.00	293.15	874.2
10000.00	303.15	865.1
10000.00	313.15	856.1
10000.00	323.15	847.0
10000.00	333.15	838.2
10000.00	343.15	829.3
10000.00	353.15	820.3
15000.00	293.15	877.6
15000.00	303.15	869.0
15000.00	313.15	859.9
15000.00	323.15	851.1
15000.00	333.15	842.6
15000.00	343.15	833.9
15000.00	353.15	825.3
20000.00	293.15	881.1
20000.00	303.15	872.4
20000.00	313.15	863.5
20000.00	323.15	855.0
20000.00	333.15	846.6
20000.00	343.15	838.1
20000.00	353.15	829.9
25000.00	293.15	884.2
25000.00	303.15	875.8
25000.00	313.15	867.1
25000.00	323.15	858.9
25000.00	333.15	850.5
25000.00	343.15	842.3
25000.00	353.15	834.0
30000.00	293.15	887.3
30000.00	303.15	879.0
30000.00	313.15	870.5
30000.00	323.15	862.5
30000.00	333.15	854.3
30000.00	343.15	846.2
30000.00	353.15	838.2
35000.00	293.15	890.3
35000.00	303.15	882.1
35000.00	313.15	873.8
35000.00	323.15	866.0
35000.00	333.15	857.9
35000.00	343.15	850.1
35000.00	353.15	842.2
40000.00	293.15	893.3
40000.00	303.15	885.2
40000.00	313.15	877.0
40000.00	323.15	869.4
40000.00	333.15	861.4
40000.00	343.15	853.7
40000.00	353.15	846.1
45000.00	293.15	896.1
45000.00	303.15	888.2
45000.00	313.15	880.2
45000.00	323.15	872.5
45000.00	333.15	864.8
45000.00	343.15	857.4
45000.00	353.15	849.8
50000.00	293.15	898.9
50000.00	303.15	891.1
50000.00	313.15	883.3
50000.00	323.15	875.7
50000.00	333.15	868.1
50000.00	343.15	860.8
50000.00	353.15	853.3
55000.00	293.15	901.6
55000.00	303.15	894.0
55000.00	313.15	886.2
55000.00	323.15	878.7
55000.00	333.15	871.4
55000.00	343.15	864.2
55000.00	353.15	856.7
60000.00	293.15	904.2
60000.00	303.15	896.7
60000.00	313.15	889.0
60000.00	323.15	881.7
60000.00	333.15	874.5
60000.00	343.15	867.4
60000.00	353.15	860.1
65000.00	293.15	906.7
65000.00	303.15	899.2
65000.00	313.15	891.8
65000.00	323.15	884.6
65000.00	333.15	877.5
65000.00	343.15	870.3
65000.00	353.15	863.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.00	2000.00	871.2
293.00	3000.00	871.9
293.00	4000.00	872.6
293.00	5000.00	873.2
293.00	10000.00	876.8
293.00	20000.00	883.4
293.00	30000.00	889.3
293.00	40000.00	895.1
293.00	50000.00	900.5
293.00	60000.00	905.8
293.00	70000.00	910.8
293.00	80000.00	915.8
293.00	90000.00	920.4
293.00	100000.00	924.8
293.00	110000.00	929.4
293.00	120000.00	933.6
293.00	130000.00	938.0
293.00	135000.00	939.9
293.00	137500.00	940.9
313.00	2000.00	852.2
313.00	3000.00	853.0
313.00	4000.00	853.9
313.00	5000.00	854.6
313.00	10000.00	858.6
313.00	20000.00	866.1
313.00	30000.00	872.9
313.00	40000.00	879.0
313.00	50000.00	884.8
313.00	60000.00	890.4
313.00	70000.00	896.0
313.00	80000.00	901.2
313.00	90000.00	906.3
313.00	100000.00	911.0
313.00	110000.00	915.7
313.00	120000.00	920.3
313.00	130000.00	924.8
313.00	135000.00	927.0
313.00	137500.00	927.9
333.00	2000.00	833.0
333.00	3000.00	834.0
333.00	4000.00	834.9
333.00	5000.00	835.8
333.00	10000.00	840.2
333.00	20000.00	848.2
333.00	30000.00	855.9
333.00	40000.00	863.0
333.00	50000.00	869.2
333.00	60000.00	875.6
333.00	70000.00	881.5
333.00	80000.00	887.1
333.00	90000.00	892.3
333.00	100000.00	897.6
333.00	110000.00	902.5
333.00	120000.00	907.3
333.00	130000.00	912.0
333.00	135000.00	914.2
333.00	137500.00	915.4
353.00	2000.00	814.2
353.00	3000.00	815.2
353.00	4000.00	816.3
353.00	5000.00	817.3
353.00	10000.00	822.4
353.00	20000.00	831.5
353.00	30000.00	840.1
353.00	40000.00	847.6
353.00	50000.00	854.7
353.00	60000.00	861.5
353.00	70000.00	867.7
353.00	80000.00	873.8
353.00	90000.00	879.6
353.00	100000.00	884.9
353.00	110000.00	890.3
353.00	120000.00	895.4
353.00	130000.00	900.3
353.00	135000.00	902.6
353.00	137500.00	903.7
373.00	2000.00	794.2
373.00	3000.00	795.4
373.00	4000.00	796.6
373.00	5000.00	797.8
373.00	10000.00	803.8
373.00	20000.00	814.0
373.00	30000.00	823.5
373.00	40000.00	832.0
373.00	50000.00	840.2
373.00	60000.00	847.2
373.00	70000.00	853.9
373.00	80000.00	860.3
373.00	90000.00	866.6
373.00	100000.00	872.2
373.00	110000.00	877.8
373.00	120000.00	883.3
373.00	130000.00	888.5
373.00	135000.00	890.8
373.00	137500.00	892.0
393.00	2000.00	774.2
393.00	3000.00	775.7
393.00	4000.00	777.2
393.00	5000.00	778.5
393.00	10000.00	785.1
393.00	20000.00	797.0
393.00	30000.00	807.5
393.00	40000.00	816.9
393.00	50000.00	825.2
393.00	60000.00	833.3
393.00	70000.00	840.6
393.00	80000.00	847.3
393.00	90000.00	854.0
393.00	100000.00	860.1
393.00	110000.00	866.0
393.00	120000.00	871.6
393.00	130000.00	877.2
393.00	135000.00	879.8
393.00	137500.00	881.0
413.00	2000.00	753.1
413.00	3000.00	754.9
413.00	4000.00	756.5
413.00	5000.00	758.3
413.00	10000.00	766.1
413.00	20000.00	779.5
413.00	30000.00	791.3
413.00	40000.00	801.6
413.00	50000.00	810.8
413.00	60000.00	819.2
413.00	70000.00	827.3
413.00	80000.00	834.6
413.00	90000.00	841.3
413.00	100000.00	848.0
413.00	110000.00	854.2
413.00	120000.00	860.2
413.00	130000.00	865.8
413.00	135000.00	868.5
413.00	137500.00	869.7
433.00	2000.00	731.6
433.00	3000.00	733.6
433.00	4000.00	735.6
433.00	5000.00	737.5
433.00	10000.00	746.9
433.00	20000.00	762.1
433.00	30000.00	774.9
433.00	40000.00	786.5
433.00	50000.00	796.7
433.00	60000.00	805.8
433.00	70000.00	814.3
433.00	80000.00	822.0
433.00	90000.00	829.2
433.00	100000.00	836.0
433.00	110000.00	842.6
433.00	120000.00	848.7
433.00	130000.00	854.9
433.00	135000.00	857.7
433.00	137500.00	859.0
448.00	2000.00	714.3
448.00	3000.00	716.6
448.00	4000.00	718.9
448.00	5000.00	721.1
448.00	10000.00	731.4
448.00	20000.00	748.5
448.00	30000.00	762.6
448.00	40000.00	774.7
448.00	50000.00	785.5
448.00	60000.00	795.1
448.00	70000.00	804.1
448.00	80000.00	812.3
448.00	90000.00	820.0
448.00	100000.00	827.2
448.00	110000.00	833.9
448.00	120000.00	840.2
448.00	130000.00	846.6
448.00	135000.00	849.6
448.00	137500.00	850.9
468.00	2000.00	689.9
468.00	3000.00	692.7
468.00	4000.00	695.5
468.00	5000.00	698.2
468.00	10000.00	710.6
468.00	20000.00	730.4
468.00	30000.00	745.9
468.00	40000.00	759.3
468.00	50000.00	771.1
468.00	60000.00	781.7
468.00	70000.00	790.9
468.00	80000.00	799.8
468.00	90000.00	808.0
468.00	100000.00	815.5
468.00	110000.00	822.8
468.00	120000.00	829.5
468.00	130000.00	836.0
468.00	135000.00	838.9
468.00	137500.00	840.4
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	862.1
298.15	2130.00	863.6
298.15	4150.00	865.2
298.15	6180.00	866.7
298.15	8210.00	868.2
298.15	10230.00	869.6
298.15	11250.00	870.4
298.15	12260.00	871.1
298.15	14290.00	872.5
298.15	16310.00	873.9
298.15	18340.00	875.3
298.15	20370.00	876.7
298.15	22390.00	878.0
298.15	24420.00	879.3
298.15	26450.00	880.6
298.15	28470.00	881.9
298.15	29490.00	882.5
298.15	30500.00	883.2
298.15	32530.00	884.4
298.15	34550.00	885.6
298.15	36580.00	886.8
298.15	38600.00	888.0
298.15	39620.00	888.6
308.15	100.00	853.0
308.15	2130.00	854.5
308.15	4150.00	856.2
308.15	6180.00	857.8
308.15	8210.00	859.3
308.15	10230.00	860.9
308.15	11250.00	861.7
308.15	12260.00	862.4
308.15	14290.00	863.9
308.15	16310.00	865.4
308.15	18340.00	866.8
308.15	20370.00	868.2
308.15	22390.00	869.6
308.15	24420.00	871.0
308.15	26450.00	872.4
308.15	28470.00	873.8
308.15	29490.00	874.4
308.15	30500.00	875.0
308.15	32530.00	876.3
308.15	34550.00	877.6
308.15	36580.00	878.9
308.15	38600.00	880.1
308.15	39620.00	880.7
318.15	100.00	843.8
318.15	2130.00	845.6
318.15	4150.00	847.3
318.15	6180.00	849.0
318.15	8210.00	850.6
318.15	10230.00	852.3
318.15	11250.00	853.1
318.15	12260.00	853.9
318.15	14290.00	855.4
318.15	16310.00	857.0
318.15	18340.00	858.5
318.15	20370.00	860.0
318.15	22390.00	861.5
318.15	24420.00	862.9
318.15	26450.00	864.4
318.15	28470.00	865.8
318.15	29490.00	866.5
318.15	30500.00	867.2
318.15	32530.00	868.5
318.15	34550.00	869.9
318.15	36580.00	871.2
318.15	38600.00	872.5
318.15	39620.00	873.2
328.15	100.00	834.5
328.15	2130.00	836.5
328.15	4150.00	838.3
328.15	6180.00	840.1
328.15	8210.00	841.8
328.15	10230.00	843.5
328.15	11250.00	844.4
328.15	12260.00	845.2
328.15	14290.00	846.9
328.15	16310.00	848.6
328.15	18340.00	850.1
328.15	20370.00	851.7
328.15	22390.00	853.3
328.15	24420.00	854.8
328.15	26450.00	856.3
328.15	28470.00	857.8
328.15	29490.00	858.5
328.15	30500.00	859.3
328.15	32530.00	860.7
328.15	34550.00	862.1
328.15	36580.00	863.5
328.15	38600.00	864.9
328.15	39620.00	865.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	876.0
283.15	1000.00	876.6
283.15	5000.00	879.5
283.15	10000.00	882.9
283.15	30000.00	895.3
283.15	50000.00	906.4
283.15	70000.00	916.4
298.15	100.00	862.5
298.15	1000.00	863.0
298.15	5000.00	866.1
298.15	10000.00	869.7
298.15	30000.00	883.1
298.15	50000.00	894.9
298.15	70000.00	905.5
323.15	100.00	839.1
323.15	1000.00	839.7
323.15	5000.00	843.2
323.15	10000.00	847.5
323.15	30000.00	862.8
323.15	50000.00	876.0
323.15	70000.00	887.6
333.15	100.00	829.6
333.15	1000.00	830.2
333.15	5000.00	834.0
333.15	10000.00	838.5
333.15	30000.00	854.6
333.15	50000.00	868.4
333.15	70000.00	880.6
348.15	100.00	815.1
348.15	1000.00	815.8
348.15	5000.00	820.0
348.15	10000.00	825.0
348.15	30000.00	842.4
348.15	50000.00	857.2
348.15	70000.00	870.1
373.15	100.00	789.5
373.15	1000.00	791.4
373.15	5000.00	796.4
373.15	10000.00	802.3
373.15	30000.00	822.4
373.15	50000.00	838.9
373.15	70000.00	853.1
398.15	1000.00	765.1
398.15	5000.00	771.0
398.15	10000.00	777.9
398.15	30000.00	801.1
398.15	50000.00	819.6
398.15	70000.00	835.1
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	298.15	862.0
1000.00	298.15	862.7
5000.00	298.15	865.7
10000.00	298.15	869.4
15000.00	298.15	873.0
20000.00	298.15	876.4
30000.00	298.15	882.9
40000.00	298.15	889.0
45000.00	298.15	891.9
50000.00	298.15	894.7
60000.00	298.15	900.2
100.00	323.15	838.7
1000.00	323.15	839.5
5000.00	323.15	843.1
10000.00	323.15	847.4
15000.00	323.15	851.5
20000.00	323.15	855.4
30000.00	323.15	862.7
40000.00	323.15	869.5
45000.00	323.15	872.7
50000.00	323.15	875.9
60000.00	323.15	881.9
100.00	348.15	814.6
1000.00	348.15	815.6
5000.00	348.15	819.8
10000.00	348.15	824.7
15000.00	348.15	829.5
20000.00	348.15	834.0
30000.00	348.15	842.4
40000.00	348.15	850.0
45000.00	348.15	853.6
50000.00	348.15	857.1
60000.00	348.15	863.8
1000.00	373.15	791.1
5000.00	373.15	796.0
10000.00	373.15	801.8
15000.00	373.15	807.3
20000.00	373.15	812.5
30000.00	373.15	822.0
40000.00	373.15	830.6
45000.00	373.15	834.6
50000.00	373.15	838.4
60000.00	373.15	845.8
1000.00	398.15	765.3
5000.00	398.15	771.3
10000.00	398.15	778.3
15000.00	398.15	784.7
20000.00	398.15	790.8
30000.00	398.15	801.6
40000.00	398.15	811.2
45000.00	398.15	815.7
50000.00	398.15	819.9
60000.00	398.15	828.0
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
233.15	101.25	922.207
233.15	1055.60	922.722
233.15	1861.30	923.156
233.15	3871.07	924.223
233.15	5873.94	925.287
233.15	8031.15	926.415
233.15	9906.49	927.392
233.15	11972.80	928.445
233.15	13947.10	929.451
233.15	15970.80	930.461
233.15	18028.60	931.487
233.15	19921.10	932.422
233.15	22000.00	933.432
233.15	24028.70	934.411
233.15	25833.40	935.279
233.15	27875.90	936.25
233.15	29775.60	937.146
253.15	102.01	903.705
253.15	1102.59	904.316
253.15	1837.13	904.762
253.15	3915.79	906.0
253.15	6024.32	907.237
253.15	7905.75	908.333
253.15	9884.50	909.467
253.15	11994.60	910.665
253.15	13974.90	911.777
253.15	15950.90	912.877
253.15	17977.80	913.989
253.15	20022.00	915.098
253.15	21921.00	916.119
253.15	24088.40	917.274
253.15	25989.80	918.275
253.15	27826.70	919.23
253.15	29745.90	920.223
273.15	97.87	885.25
273.15	1027.82	885.881
273.15	1996.92	886.534
273.15	4081.70	887.926
273.15	5913.44	889.129
273.15	8004.24	890.482
273.15	9932.36	891.714
273.15	11879.80	892.948
273.15	13887.70	894.195
273.15	16098.50	895.56
273.15	18098.90	896.771
273.15	19969.20	897.897
273.15	21859.80	899.011
273.15	23914.00	900.215
273.15	25979.60	901.41
273.15	28069.50	902.607
273.15	30122.70	903.766
293.15	99.87	866.733
293.15	1127.75	867.518
293.15	2021.41	868.196
293.15	3955.95	869.643
293.15	6107.05	871.23
293.15	8032.84	872.623
293.15	9984.75	874.014
293.15	12114.30	875.512
293.15	13946.90	876.779
293.15	15848.70	878.081
293.15	17969.10	879.506
293.15	19990.50	880.848
293.15	22236.40	882.319
293.15	23980.90	883.441
293.15	25908.50	884.671
293.15	27990.50	885.976
293.15	30011.00	887.242
313.15	100.25	848.035
313.15	1103.10	848.903
313.15	2030.62	849.693
313.15	3897.28	851.277
313.15	6141.83	853.137
313.15	7925.24	854.59
313.15	9859.02	856.142
313.15	11934.70	857.774
313.15	13950.30	859.327
313.15	16069.10	860.941
313.15	17874.10	862.289
313.15	19838.40	863.738
313.15	22114.30	865.383
313.15	24096.90	866.799
313.15	25913.10	868.068
313.15	28004.70	869.523
313.15	29965.50	870.863
333.15	98.96	829.055
333.15	1101.01	830.042
333.15	2134.31	831.05
333.15	4003.84	832.841
333.15	6105.69	834.814
333.15	8004.97	836.556
333.15	9960.27	838.314
333.15	12120.50	840.218
333.15	14111.20	841.938
333.15	15856.90	843.417
333.15	18129.10	845.312
333.15	19859.70	846.724
333.15	22144.00	848.558
333.15	24050.50	850.059
333.15	25886.50	851.479
333.15	28037.10	853.128
333.15	29895.00	854.529
353.15	100.22	809.674
353.15	1169.90	810.881
353.15	2003.60	811.814
353.15	4142.50	814.153
353.15	6005.54	816.142
353.15	8141.30	818.365
353.15	10003.50	820.255
353.15	12008.20	822.24
353.15	14198.40	824.368
353.15	16142.20	826.212
353.15	18101.40	828.027
353.15	19916.80	829.683
353.15	22137.50	831.662
353.15	24034.00	833.323
353.15	26059.00	835.06
353.15	28105.10	836.785
353.15	29954.10	838.316
373.15	1259.86	791.299
373.15	2065.80	792.34
373.15	3870.71	794.611
373.15	6198.30	797.456
373.15	8095.93	799.709
373.15	9917.32	801.809
373.15	12114.50	804.274
373.15	13933.50	806.263
373.15	16020.00	808.493
373.15	18023.10	810.573
373.15	19927.20	812.508
373.15	22108.00	814.677
373.15	23970.20	816.486
373.15	25950.10	818.372
373.15	27873.70	820.167
373.15	29906.80	822.029
393.15	1097.43	770.672
393.15	1998.69	772.03
393.15	4084.58	775.078
393.15	6214.76	778.084
393.15	8059.27	780.589
393.15	9988.38	783.137
393.15	12133.60	785.871
393.15	14051.30	788.257
393.15	16078.00	790.683
393.15	18011.70	792.945
393.15	19811.10	794.994
393.15	22109.50	797.55
393.15	23923.10	799.514
393.15	25870.20	801.576
393.15	27974.20	803.747
393.15	29891.10	805.692
413.15	1099.07	749.389
413.15	1960.79	750.924
413.15	4038.31	754.503
413.15	6026.64	757.773
413.15	8189.08	761.18
413.15	9852.03	763.702
413.15	12116.70	767.016
413.15	14167.50	769.904
413.15	16108.40	772.544
413.15	18095.40	775.165
413.15	20103.80	777.733
413.15	22151.60	780.275
413.15	24008.60	782.518
413.15	25995.60	784.857
413.15	27793.40	786.922
413.15	29814.70	789.193
433.15	1101.78	726.984
433.15	1976.67	728.858
433.15	4084.44	733.177
433.15	6154.50	737.18
433.15	8078.74	740.731
433.15	9952.57	744.032
433.15	11979.80	747.451
433.15	13969.10	750.677
433.15	16091.10	753.964
433.15	17960.70	756.765
433.15	19890.30	759.561
433.15	22082.30	762.624
433.15	24002.20	765.215
433.15	26048.90	767.899
433.15	27835.50	770.185
433.15	29992.70	772.844
453.15	1107.48	703.102
453.15	2037.85	705.548
453.15	4185.27	710.874
453.15	6060.45	715.218
453.15	8005.22	719.474
453.15	9870.31	723.328
453.15	12115.30	727.721
453.15	14139.10	731.482
453.15	16026.60	734.835
453.15	17927.80	738.09
453.15	20153.00	741.727
453.15	22071.10	744.756
453.15	24056.90	747.767
453.15	26028.80	750.661
453.15	27966.30	753.404
453.15	29817.00	755.955
473.15	1104.44	677.2
473.15	2031.33	680.289
473.15	4033.85	686.456
473.15	6024.42	692.111
473.15	7930.82	697.122
473.15	10106.60	702.459
473.15	11931.20	706.639
473.15	13958.70	711.045
473.15	16004.30	715.254
473.15	17878.30	718.918
473.15	19844.40	722.599
473.15	22087.70	726.587
473.15	24074.30	729.989
473.15	26037.60	733.203
473.15	27839.80	736.071
473.15	29805.80	739.091
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
295.90	15300.00	873.9
295.90	15300.00	873.9
295.90	36900.00	888.3
295.90	37000.00	888.3
295.90	56300.00	899.5
295.90	56300.00	899.5
295.90	77100.00	910.8
295.90	77100.00	910.8
295.90	92300.00	918.5
295.90	92300.00	918.5
295.90	112400.00	927.8
295.90	112500.00	927.9
295.90	113100.00	928.0
295.90	113100.00	927.9
295.90	132800.00	936.5
295.90	132800.00	936.5
295.90	154900.00	945.5
295.90	155000.00	945.5
305.10	8800.00	860.1
305.10	8800.00	860.1
305.10	71100.00	900.3
305.10	71100.00	900.3
305.10	71100.00	900.3
305.10	71100.00	900.3
305.10	125700.00	926.6
305.10	125700.00	926.6
305.10	174300.00	946.6
305.10	174500.00	946.6
323.40	21600.00	852.5
323.40	21700.00	852.5
323.40	31600.00	860.3
323.40	56700.00	877.1
323.40	56700.00	877.1
323.40	56700.00	877.1
323.40	77500.00	889.3
323.40	77600.00	889.4
323.40	110300.00	906.5
323.40	110400.00	906.5
323.40	133100.00	919.1
323.40	133100.00	919.2
323.40	149000.00	926.0
323.40	149100.00	926.0
323.40	153800.00	926.0
323.40	153900.00	926.0
323.40	153900.00	926.0
323.40	154000.00	926.0
323.40	182500.00	939.6
323.40	182500.00	939.5
323.40	202800.00	947.3
323.40	202900.00	947.4
323.40	219900.00	953.2
323.40	220100.00	953.3
323.40	223000.00	952.9
323.40	223300.00	952.9
347.30	9200.00	821.2
347.30	9200.00	821.3
347.30	35500.00	845.5
347.30	35600.00	845.6
347.30	82100.00	877.4
347.30	82200.00	877.4
347.30	106400.00	891.1
347.30	106500.00	891.1
347.30	140400.00	907.9
347.30	140400.00	907.9
347.30	140600.00	907.9
347.30	140700.00	907.9
347.30	160800.00	917.1
347.30	160800.00	917.1
347.30	182500.00	926.1
347.30	182500.00	926.1
347.30	182500.00	926.2
347.30	182600.00	926.2
347.30	204500.00	934.8
347.30	204800.00	934.8
392.50	16800.00	789.6
392.50	16800.00	789.7
392.50	35200.00	810.6
392.50	35200.00	810.6
392.50	35200.00	810.6
392.50	35300.00	810.6
392.50	48400.00	822.9
392.50	48500.00	822.9
392.50	64700.00	831.8
392.50	64800.00	832.6
392.50	78400.00	846.1
392.50	78500.00	846.2
392.50	90500.00	849.8
392.50	90600.00	850.6
392.50	113000.00	865.4
392.50	113100.00	866.2
392.50	133600.00	875.1
392.50	133700.00	875.9
392.50	154300.00	886.5
392.50	154400.00	886.6
392.50	174900.00	895.6
392.50	195100.00	904.6
392.50	195200.00	904.6
392.50	195200.00	905.4
392.50	216900.00	913.6
392.50	217100.00	914.4
392.50	238700.00	923.8
392.50	238900.00	924.7
392.50	258600.00	929.8
392.50	258900.00	930.7
392.50	279100.00	938.4
392.50	279700.00	939.3
421.50	10200.00	755.6
421.50	10300.00	755.7
421.50	21700.00	771.9
421.50	21900.00	772.0
421.50	36200.00	788.7
421.50	36200.00	788.8
421.50	49700.00	802.4
421.50	49800.00	802.5
421.50	70900.00	818.3
421.50	70900.00	818.7
421.50	87800.00	832.8
421.50	87800.00	832.4
421.50	106200.00	841.8
421.50	106200.00	842.1
421.50	121800.00	852.0
421.50	121800.00	851.6
421.50	133100.00	862.0
421.50	133200.00	862.1
421.50	139800.00	862.1
421.50	139900.00	865.9
421.50	160700.00	873.2
421.50	160700.00	873.3
421.50	175700.00	881.8
421.50	177600.00	881.7
421.50	188500.00	890.6
421.50	188700.00	890.5
421.50	196400.00	890.5
421.50	196500.00	890.4
421.50	216100.00	899.2
421.50	216200.00	899.2
421.50	237800.00	912.0
421.50	237900.00	911.7
421.50	258000.00	916.4
421.50	258400.00	916.5
421.50	274100.00	925.5
421.50	274400.00	925.6
421.50	296000.00	932.5
421.50	297900.00	932.7
451.80	18700.00	738.4
451.80	18800.00	738.7
451.80	43000.00	772.1
451.80	43100.00	772.1
451.80	43200.00	772.4
451.80	70500.00	799.4
451.80	70600.00	799.6
451.80	85500.00	812.0
451.80	85500.00	812.2
451.80	99500.00	822.4
451.80	99600.00	822.4
451.80	99600.00	822.7
451.80	112800.00	827.6
451.80	113000.00	827.0
451.80	116500.00	833.9
451.80	116600.00	834.2
451.80	133600.00	842.0
451.80	133600.00	842.0
451.80	133700.00	841.4
451.80	174900.00	865.2
451.80	175000.00	864.5
451.80	216400.00	885.3
451.80	216600.00	884.6
451.80	238400.00	896.6
451.80	259000.00	906.0
451.80	259300.00	905.4
451.80	279400.00	912.7
451.80	280100.00	913.6
451.80	280100.00	912.9
500.30	23600.00	700.8
500.30	23700.00	700.7
500.30	56400.00	751.7
500.30	56600.00	751.6
500.30	84300.00	780.6
500.30	84400.00	780.4
500.30	105100.00	797.7
500.30	105200.00	797.6
500.30	129700.00	810.6
500.30	129800.00	810.7
500.30	168300.00	836.2
500.30	168500.00	836.3
500.30	188400.00	847.4
500.30	188500.00	847.5
500.30	215100.00	860.8
500.30	215300.00	860.9
500.30	235700.00	871.9
500.30	235900.00	872.0
500.30	238600.00	871.9
500.30	238800.00	872.0
500.30	258100.00	881.8
500.30	258300.00	881.9
500.30	279600.00	890.2
500.30	280200.00	890.3
534.90	38300.00	697.6
534.90	38300.00	696.9
534.90	52600.00	721.7
534.90	52800.00	721.0
534.90	69500.00	743.2
534.90	69600.00	742.5
534.90	89900.00	764.7
534.90	89900.00	764.7
534.90	90000.00	764.0
534.90	90000.00	764.0
534.90	105800.00	778.7
534.90	105900.00	778.0
534.90	125700.00	794.4
534.90	125800.00	793.6
534.90	171000.00	819.0
534.90	171100.00	819.0
534.90	171300.00	820.8
534.90	211800.00	843.1
534.90	212000.00	844.9
534.90	237300.00	859.2
534.90	257400.00	865.2
534.90	257700.00	867.1
534.90	279600.00	876.8
534.90	280800.00	878.1
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.16	1020.00	876.55
283.16	5010.00	879.36
283.16	10030.00	882.78
283.16	15050.00	886.11
283.16	20080.00	889.23
283.16	25060.00	892.35
283.16	30040.00	895.27
283.16	35080.00	898.24
283.16	40060.00	901.05
283.16	45050.00	903.77
283.16	50010.00	906.43
283.16	55060.00	909.09
283.16	60030.00	911.65
283.16	65050.00	914.15
298.15	1040.00	862.88
298.15	5040.00	865.93
298.15	10030.00	869.6
298.15	15050.00	873.21
298.15	20040.00	876.63
298.15	25050.00	879.93
298.15	30060.00	883.14
298.15	35020.00	886.25
298.15	40040.00	889.26
298.15	45070.00	892.2
298.15	50040.00	895.06
298.15	55040.00	897.86
298.15	60030.00	900.56
298.15	65020.00	903.2
323.15	1050.00	839.46
323.15	5050.00	843.04
323.15	10030.00	847.29
323.15	15010.00	851.38
323.15	20010.00	855.27
323.15	25060.00	859.05
323.15	30080.00	862.69
323.15	35020.00	866.13
323.15	40010.00	869.52
323.15	45060.00	872.84
323.15	50010.00	875.93
323.15	55010.00	879.01
323.15	60050.00	882.04
323.15	65030.00	884.91
348.15	1060.00	815.55
348.15	5070.00	819.75
348.15	10010.00	824.67
348.15	15030.00	829.43
348.15	20030.00	833.88
348.15	25020.00	838.2
348.15	30080.00	842.3
348.15	35050.00	846.21
348.15	40050.00	849.97
348.15	45070.00	853.63
348.15	50020.00	857.09
348.15	55060.00	860.49
348.15	60040.00	863.8
348.15	65070.00	867.0
373.15	1050.00	790.86
373.15	5020.00	795.87
373.15	10040.00	801.74
373.15	15040.00	807.26
373.15	20030.00	812.38
373.15	25080.00	817.35
373.15	30070.00	821.93
373.15	35040.00	826.36
373.15	40040.00	830.59
373.15	45030.00	834.57
373.15	50040.00	838.5
373.15	55040.00	842.23
373.15	60010.00	845.81
398.15	1070.00	765.25
398.15	5030.00	771.26
398.15	10040.00	778.22
398.15	15080.00	784.74
398.15	20010.00	790.62
398.15	25050.00	796.25
398.15	30040.00	801.49
398.15	35040.00	806.48
398.15	40020.00	811.17
398.15	45040.00	815.71
398.15	50020.00	819.96
398.15	55040.00	824.15
398.15	60020.00	828.11
398.15	65080.00	831.99
423.15	1050.00	738.06
423.15	5030.00	745.45
423.15	10060.00	753.93
423.15	15030.00	761.54
423.15	20000.00	768.41
423.15	25020.00	774.89
423.15	30020.00	780.87
423.15	35060.00	786.56
423.15	40020.00	791.82
423.15	45040.00	796.87
423.15	50040.00	801.63
423.15	55060.00	806.24
423.15	60040.00	810.55
423.15	65050.00	814.77
448.15	1040.00	708.96
448.15	5070.00	718.48
448.15	10040.00	728.71
448.15	15070.00	737.86
448.15	20050.00	745.94
448.15	25050.00	753.39
448.15	30040.00	760.21
448.15	35040.00	766.59
448.15	40020.00	772.48
448.15	45030.00	778.13
448.15	50030.00	783.39
448.15	55060.00	788.44
448.15	60010.00	793.17
448.15	65060.00	797.83
473.15	1030.00	676.8
473.15	5050.00	689.34
473.15	10050.00	702.19
473.15	15060.00	713.2
473.15	20020.00	722.73
473.15	25040.00	731.39
473.15	30010.00	739.18
473.15	35040.00	746.42
473.15	40050.00	753.09
473.15	45060.00	759.38
473.15	50050.00	765.18
473.15	55020.00	770.69
473.15	60030.00	775.95
473.15	65020.00	780.92
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
101.30	293.15	867.1
2000.00	293.15	868.3
4000.00	293.15	869.8
6000.00	293.15	871.2
10000.00	293.15	874.1
20000.00	293.15	880.9
30000.00	293.15	887.2
40000.00	293.15	893.2
50000.00	293.15	898.8
60000.00	293.15	904.1
70000.00	293.15	909.2
80000.00	293.15	914.1
90000.00	293.15	918.7
94000.00	293.15	920.5
96000.00	293.15	921.4
98000.00	293.15	922.3
100000.00	293.15	923.2
101.30	323.15	838.8
2000.00	323.15	840.3
4000.00	323.15	842.1
6000.00	323.15	843.8
10000.00	323.15	847.3
20000.00	323.15	855.2
30000.00	323.15	862.6
40000.00	323.15	869.4
50000.00	323.15	875.8
60000.00	323.15	881.8
70000.00	323.15	887.5
80000.00	323.15	893.0
90000.00	323.15	898.1
94000.00	323.15	900.1
96000.00	323.15	901.0
98000.00	323.15	902.0
100000.00	323.15	902.9
101.30	303.15	857.7
2000.00	303.15	858.8
4000.00	303.15	860.4
6000.00	303.15	861.9
10000.00	303.15	865.1
20000.00	303.15	872.3
30000.00	303.15	879.0
40000.00	303.15	885.2
50000.00	303.15	891.0
60000.00	303.15	896.7
70000.00	303.15	901.9
80000.00	303.15	907.0
90000.00	303.15	911.8
94000.00	303.15	913.6
96000.00	303.15	914.4
98000.00	303.15	915.3
100000.00	303.15	916.5
101.30	333.15	829.0
2000.00	333.15	830.9
4000.00	333.15	832.8
6000.00	333.15	834.7
10000.00	333.15	838.3
20000.00	333.15	846.8
30000.00	333.15	854.4
40000.00	333.15	861.6
50000.00	333.15	868.2
60000.00	333.15	874.5
70000.00	333.15	880.4
80000.00	333.15	885.9
90000.00	333.15	891.3
94000.00	333.15	893.3
96000.00	333.15	894.4
98000.00	333.15	895.4
100000.00	333.15	896.3
101.30	313.15	848.1
2000.00	313.15	849.4
4000.00	313.15	851.1
6000.00	313.15	852.8
10000.00	313.15	856.3
20000.00	313.15	863.8
30000.00	313.15	870.8
40000.00	313.15	877.5
50000.00	313.15	883.4
60000.00	313.15	889.2
70000.00	313.15	894.7
80000.00	313.15	899.9
90000.00	313.15	904.9
94000.00	313.15	906.6
96000.00	313.15	907.5
98000.00	313.15	908.5
100000.00	313.15	909.7
101.30	343.15	819.4
2000.00	343.15	821.4
4000.00	343.15	823.4
6000.00	343.15	825.4
10000.00	343.15	829.2
20000.00	343.15	838.2
30000.00	343.15	846.3
40000.00	343.15	853.8
50000.00	343.15	860.7
60000.00	343.15	867.2
70000.00	343.15	873.4
80000.00	343.15	879.2
90000.00	343.15	884.7
94000.00	343.15	886.7
96000.00	343.15	887.8
98000.00	343.15	888.8
100000.00	343.15	889.8
8000.00	298.15	872.6
12000.00	298.15	875.5
14000.00	298.15	876.9
16000.00	298.15	878.2
18000.00	298.15	879.6
22000.00	298.15	882.2
24000.00	298.15	883.5
26000.00	298.15	884.7
28000.00	298.15	886.0
32000.00	298.15	888.5
34000.00	298.15	889.6
36000.00	298.15	890.8
38000.00	298.15	892.0
42000.00	298.15	894.3
44000.00	298.15	895.4
46000.00	298.15	896.5
48000.00	298.15	897.7
52000.00	298.15	899.8
54000.00	298.15	900.9
56000.00	298.15	902.0
58000.00	298.15	903.1
62000.00	298.15	905.2
64000.00	298.15	906.2
66000.00	298.15	907.2
68000.00	298.15	908.2
72000.00	298.15	910.2
74000.00	298.15	911.2
76000.00	298.15	912.2
78000.00	298.15	913.1
82000.00	298.15	915.0
84000.00	298.15	915.9
86000.00	298.15	916.9
88000.00	298.15	917.8
92000.00	298.15	919.6
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
303.15	100.00	857.4
303.15	5000.00	861.3
303.15	10000.00	865.1
303.15	15000.00	868.7
303.15	20000.00	872.3
303.15	25000.00	875.6
303.15	30000.00	878.9
313.15	100.00	848.1
313.15	5000.00	852.1
313.15	10000.00	856.2
313.15	15000.00	860.0
313.15	20000.00	863.7
313.15	25000.00	867.2
313.15	30000.00	870.7
323.15	100.00	838.6
323.15	5000.00	842.9
323.15	10000.00	847.2
323.15	15000.00	851.2
323.15	20000.00	855.1
323.15	25000.00	858.9
323.15	30000.00	862.5
333.15	100.00	829.2
333.15	5000.00	833.7
333.15	10000.00	838.2
333.15	15000.00	842.5
333.15	20000.00	846.6
333.15	25000.00	850.5
333.15	30000.00	854.3
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	283.15	875.7
100.00	288.15	871.3
100.00	293.15	866.7
100.00	298.15	862.3
100.00	303.15	857.4
100.00	308.15	852.8
100.00	313.15	848.2
100.00	318.15	843.4
100.00	323.15	838.7
5000.00	283.15	879.4
5000.00	288.15	874.9
5000.00	293.15	870.4
5000.00	298.15	865.8
5000.00	303.15	861.3
5000.00	308.15	856.8
5000.00	313.15	852.2
5000.00	318.15	847.7
5000.00	323.15	843.0
10000.00	283.15	882.8
10000.00	288.15	878.4
10000.00	293.15	874.0
10000.00	298.15	869.5
10000.00	303.15	865.1
10000.00	308.15	860.7
10000.00	313.15	856.3
10000.00	318.15	851.8
10000.00	323.15	847.3
20000.00	283.15	889.3
20000.00	288.15	885.0
20000.00	293.15	880.8
20000.00	298.15	876.5
20000.00	303.15	872.3
20000.00	308.15	868.1
20000.00	313.15	863.8
20000.00	318.15	859.5
20000.00	323.15	855.2
30000.00	283.15	895.4
30000.00	288.15	891.3
30000.00	293.15	887.2
30000.00	298.15	883.0
30000.00	303.15	879.0
30000.00	308.15	875.0
30000.00	313.15	870.8
30000.00	318.15	866.8
30000.00	323.15	862.6
40000.00	283.15	901.1
40000.00	288.15	897.1
40000.00	293.15	893.2
40000.00	298.15	889.2
40000.00	303.15	885.2
40000.00	308.15	881.4
40000.00	313.15	877.4
40000.00	318.15	873.5
40000.00	323.15	869.5
50000.00	283.15	906.6
50000.00	288.15	902.7
50000.00	293.15	898.9
50000.00	298.15	895.0
50000.00	303.15	891.2
50000.00	308.15	887.4
50000.00	313.15	883.5
50000.00	318.15	879.7
50000.00	323.15	875.9
60000.00	283.15	911.7
60000.00	288.15	908.0
60000.00	293.15	904.3
60000.00	298.15	900.5
60000.00	303.15	896.8
60000.00	308.15	893.1
60000.00	313.15	889.4
60000.00	318.15	885.7
60000.00	323.15	881.9
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.14	580.00	867.3
293.14	2080.00	868.44
293.14	2100.00	868.49
293.14	4080.00	869.92
293.14	6080.00	871.41
293.14	8080.00	872.84
293.14	10080.00	874.27
293.14	10110.00	874.35
293.14	15090.00	877.74
293.14	15110.00	877.83
293.14	20090.00	881.09
293.14	20110.00	881.18
293.14	25090.00	884.33
293.14	25120.00	884.42
293.14	30090.00	887.47
293.14	30120.00	887.56
293.15	2080.00	868.48
293.15	4080.00	869.98
293.15	6080.00	871.45
293.15	8080.00	872.9
293.15	10080.00	874.33
293.15	15080.00	877.8
293.15	20080.00	881.15
293.15	25080.00	884.39
313.14	590.00	848.73
313.14	2090.00	850.02
313.14	4090.00	851.7
313.14	6090.00	853.35
313.14	8090.00	854.98
313.14	10090.00	856.57
313.14	15090.00	860.44
313.14	20090.00	864.16
313.14	25090.00	867.74
333.14	590.00	829.86
333.14	2090.00	831.32
333.14	4090.00	833.23
333.14	6090.00	835.1
333.14	8090.00	836.93
333.14	10090.00	838.73
333.14	15090.00	843.06
333.14	20090.00	847.2
333.14	25090.00	851.15
333.14	30090.00	854.96
353.14	2090.00	812.26
353.14	4090.00	814.44
353.14	6090.00	816.57
353.14	8090.00	818.63
353.14	10090.00	820.66
353.14	15090.00	825.54
353.14	20090.00	830.16
353.14	25090.00	834.54
353.14	30090.00	838.72
373.15	590.00	790.76
373.15	2090.00	792.7
373.15	4090.00	795.21
373.15	6090.00	797.64
373.15	8090.00	800.0
373.15	10090.00	802.3
373.15	15080.00	807.86
373.15	15090.00	807.78
373.15	20080.00	813.03
373.15	25080.00	817.91
373.15	30080.00	822.54
373.15	2090.00	792.76
373.15	4090.00	795.27
373.15	6090.00	797.7
373.15	8090.00	800.07
373.15	10090.00	802.37
373.49	2100.00	792.38
373.49	10110.00	802.04
373.49	15110.00	807.56
373.49	20120.00	812.74
373.49	25120.00	817.63
373.49	30120.00	822.28
Reference

Speed of sound, m/s

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Frequency, MHz - Liquid	Speed of sound, m/s - Liquid
303.15	101.33	2.0	1271.9
Reference

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Frequency, MHz - Liquid	Speed of sound, m/s - Liquid
303.15	100.00	2.0	1282.6
Reference

Operational condition: Frequency, MHz = 5 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
323.29	10200.00	1253.17
323.32	20600.00	1305.92
323.32	20480.00	1305.37
323.34	31540.00	1356.69
323.37	44870.00	1413.48
323.39	60820.00	1475.53
323.38	60790.00	1475.45
373.85	35520.00	1209.33
373.83	21270.00	1132.5
373.82	7570.00	1046.51
373.83	2170.00	1007.88
373.90	50350.00	1279.95
373.87	64470.00	1340.7
422.93	6580.00	863.73
422.98	20740.00	974.49
423.01	36450.00	1073.37
423.04	56200.00	1176.92
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
240.00	103.32	1571.05
240.00	1104.21	1574.99
240.00	2104.94	1578.9
240.00	3105.74	1582.79
240.00	4106.28	1586.66
240.00	5107.43	1590.51
240.00	6107.67	1594.31
240.00	7108.38	1598.11
240.00	8109.15	1601.89
240.00	9109.83	1605.65
240.00	10110.50	1609.38
240.00	12612.20	1618.62
240.00	15113.80	1627.73
240.00	17615.50	1636.72
240.00	20117.10	1645.58
240.00	25120.60	1662.98
240.00	30124.00	1679.95
240.00	35127.40	1696.5
240.00	40130.80	1712.69
240.00	45134.20	1728.51
240.00	50137.60	1743.99
240.00	60144.40	1774.01
240.00	70151.40	1802.89
240.00	80158.20	1830.74
240.00	90165.20	1857.63
240.00	100172.00	1883.64
260.00	102.53	1476.76
260.00	1103.38	1481.1
260.00	2103.99	1485.39
260.00	3104.83	1489.66
260.00	4105.61	1493.9
260.00	5106.49	1498.11
260.00	6106.82	1502.29
260.00	7107.53	1506.45
260.00	8108.28	1510.58
260.00	9109.01	1514.67
260.00	10109.80	1518.75
260.00	12611.80	1528.82
260.00	17615.40	1548.49
260.00	20117.20	1558.1
260.00	25120.70	1576.92
260.00	30124.10	1595.21
260.00	35127.60	1613.03
260.00	40131.00	1630.39
260.00	45134.50	1647.33
260.00	50138.20	1663.87
260.00	60145.40	1695.85
260.00	70152.50	1726.52
260.00	80159.50	1755.96
260.00	90166.50	1784.35
260.00	15113.60	1538.73
260.00	100174.00	1811.73
280.00	103.62	1385.49
280.00	1104.53	1390.25
280.00	2105.31	1394.98
280.00	3106.24	1399.66
280.00	4107.05	1404.31
280.00	5107.65	1408.92
280.00	6108.14	1413.5
280.00	7108.79	1418.04
280.00	8109.45	1422.55
280.00	9110.12	1427.02
280.00	10110.80	1431.46
280.00	12612.50	1442.42
280.00	15114.20	1453.19
280.00	17616.00	1463.78
280.00	20118.00	1474.18
280.00	25121.50	1494.49
280.00	30125.00	1514.18
280.00	35128.50	1533.29
280.00	40132.00	1551.88
280.00	45135.00	1569.95
280.00	50138.50	1587.57
280.00	60145.30	1621.55
280.00	70152.30	1653.99
280.00	80159.10	1685.08
280.00	90165.80	1714.93
280.00	100173.00	1743.69
300.00	102.33	1297.15
300.00	1103.24	1302.4
300.00	2104.05	1307.6
300.00	3104.69	1312.74
300.00	103.33	1297.13
300.01	1104.24	1302.37
300.01	2104.88	1307.56
300.01	3105.58	1312.7
300.01	4106.36	1317.8
300.01	5107.04	1322.86
300.01	6107.45	1327.87
300.01	7108.08	1332.83
300.01	8108.73	1337.75
300.01	9109.36	1342.63
300.01	10110.00	1347.47
300.01	12611.70	1359.39
300.01	15113.40	1371.09
300.01	17615.20	1382.55
300.01	20116.90	1393.79
300.01	25120.30	1415.68
300.01	30123.60	1436.82
300.01	35126.90	1457.3
300.01	40130.10	1477.14
300.01	45133.30	1496.4
300.01	50136.50	1515.12
300.01	60143.10	1551.11
300.01	70150.40	1585.36
300.01	80158.50	1618.06
300.01	90165.60	1649.39
300.01	100172.00	1679.48
320.00	102.82	1211.56
320.00	102.83	1211.57
320.00	1103.61	1217.34
320.00	2104.26	1223.07
320.00	3105.03	1228.73
320.00	4105.82	1234.33
320.00	5106.65	1239.88
320.00	6107.07	1245.37
320.00	7107.78	1250.8
320.00	8108.51	1256.17
320.00	9109.16	1261.5
320.00	10109.80	1266.77
320.00	12611.50	1279.74
320.00	15113.20	1292.43
320.00	17614.90	1304.82
320.00	20116.60	1316.97
320.00	25120.10	1340.53
320.00	30123.50	1363.2
320.00	35127.10	1385.08
320.00	40130.90	1406.22
320.00	50137.90	1446.53
320.00	45134.40	1426.68
320.00	60144.90	1484.55
320.00	70152.00	1520.59
320.00	80158.90	1554.89
320.00	90165.90	1587.66
320.00	100173.00	1619.07
340.00	102.94	1128.51
340.00	1103.68	1134.9
340.00	2104.32	1141.21
340.00	3105.04	1147.45
340.00	4105.83	1153.61
340.00	103.20	1128.51
340.00	1104.11	1134.9
340.00	2104.92	1141.22
340.00	3105.78	1147.45
340.00	4106.59	1153.62
340.00	5107.25	1159.71
340.00	6107.67	1165.72
340.00	7108.35	1171.67
340.00	8109.05	1177.55
340.00	9109.73	1183.36
340.00	10110.30	1189.11
340.00	12612.00	1203.23
340.00	15113.70	1216.98
340.00	17615.40	1230.4
340.00	20117.10	1243.5
340.00	25120.50	1268.83
340.00	30124.00	1293.1
340.00	35127.60	1316.43
340.00	40131.20	1338.91
340.00	45134.90	1360.61
340.00	50138.80	1381.6
340.00	60145.70	1421.66
340.00	70152.60	1459.49
340.00	80159.50	1495.39
340.00	90166.50	1529.58
340.00	100174.00	1562.28
360.00	103.40	1047.63
360.00	1104.11	1054.73
360.00	2104.83	1061.73
360.00	3105.45	1068.62
360.00	4106.44	1075.42
360.00	5107.02	1082.11
360.00	6107.39	1088.72
360.00	7108.04	1095.24
360.00	8108.72	1101.68
360.00	9109.46	1108.04
360.00	10110.10	1114.32
359.99	10111.10	1114.35
360.00	12611.90	1129.68
359.99	12612.60	1129.71
359.99	15114.00	1144.62
359.99	17615.60	1159.13
359.99	20117.30	1173.26
359.99	25120.80	1200.47
359.99	30124.20	1226.42
359.99	35127.60	1251.26
359.99	40131.10	1275.12
359.99	45134.50	1298.07
359.99	50137.90	1320.21
359.99	60144.90	1362.33
359.99	70152.00	1401.95
359.99	80159.00	1439.41
359.99	90166.00	1474.99
359.99	100173.00	1508.93
380.00	101.06	968.429
380.00	1102.50	976.366
380.00	2103.36	984.155
380.00	3104.10	991.809
380.00	4104.99	999.336
380.00	5105.71	1006.74
380.00	6106.12	1014.03
380.00	7106.84	1021.2
380.00	8107.59	1028.27
380.00	9108.31	1035.23
380.00	10109.00	1042.09
380.00	12610.80	1058.83
380.00	15113.40	1075.03
380.00	17615.20	1090.72
380.00	20116.90	1105.95
380.00	25120.40	1135.15
380.00	30123.90	1162.87
380.00	35127.30	1189.28
380.00	40130.80	1214.55
380.00	45134.00	1238.78
380.00	50137.50	1262.09
380.00	60144.50	1306.28
380.00	70151.60	1347.66
380.00	80158.60	1386.66
380.00	90165.60	1423.62
380.00	100173.00	1458.77
400.00	603.01	894.984
400.00	1104.15	899.421
400.00	2104.60	908.149
400.00	3105.31	916.697
400.00	4106.00	925.074
400.00	5106.69	933.288
400.00	6107.36	941.35
400.00	7108.01	949.265
400.00	8108.66	957.044
400.00	9109.32	964.687
400.00	10109.90	972.207
400.00	12611.60	990.479
400.00	15113.30	1008.07
400.00	17615.10	1025.05
400.00	20116.80	1041.47
400.00	25120.20	1072.79
400.00	608.94	895.044
400.00	4105.08	925.079
400.00	15112.70	1008.09
400.00	30123.20	1102.36
400.00	35126.70	1130.4
400.00	40130.40	1157.11
400.00	45134.00	1182.65
400.00	50137.50	1207.15
400.00	60144.50	1253.4
400.00	70151.50	1296.54
400.00	80158.50	1337.05
400.00	90165.60	1375.32
400.00	100173.00	1411.65
420.00	1102.46	823.404
420.00	2103.16	833.269
420.00	3103.88	842.891
420.00	4104.56	852.281
420.00	5105.25	861.453
420.00	6105.94	870.42
420.00	7106.62	879.196
420.00	8107.32	887.789
420.00	9108.03	896.213
420.00	10108.70	904.476
420.00	12610.50	924.47
420.00	15112.30	943.614
420.00	17614.10	961.991
420.00	20115.90	979.684
420.00	25119.40	1013.26
420.00	30122.80	1044.75
420.00	35126.30	1074.47
420.00	40129.80	1102.67
420.00	45133.20	1129.52
420.00	50136.70	1155.2
420.00	60143.90	1203.5
420.00	70151.00	1248.37
420.00	80158.00	1290.36
420.00	90165.10	1329.92
420.00	100172.00	1367.39
Reference

Thermal conductivity, W/m/K

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Thermal conductivity, W/m/K - Liquid
294.20	100.00	0.1320
294.20	10000.00	0.1360
294.20	20000.00	0.1390
314.10	100.00	0.1270
314.10	10000.00	0.1310
314.10	20000.00	0.1350
334.40	100.00	0.1220
334.40	10000.00	0.1260
334.40	20000.00	0.1290
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Thermal conductivity, W/m/K - Liquid
317.52	20330.00	0.1330
317.46	15330.00	0.1292
317.42	10550.00	0.1277
317.39	5130.00	0.1266
317.42	1050.00	0.1251
336.30	20300.00	0.1267
336.34	15140.00	0.1245
336.32	10150.00	0.1229
336.39	5020.00	0.1205
336.42	1030.00	0.1194
356.27	20040.00	0.1218
356.27	15170.00	0.1205
356.36	10440.00	0.1184
356.43	5170.00	0.1166
356.41	1160.00	0.1131
376.88	20030.00	0.1185
376.95	15270.00	0.1147
376.95	10160.00	0.1124
376.95	5200.00	0.1108
377.07	1080.00	0.1096
396.26	20010.00	0.1141
395.96	15140.00	0.1121
396.23	10180.00	0.1091
396.28	5150.00	0.1072
396.32	1030.00	0.1059
416.29	20250.00	0.1104
416.33	15150.00	0.1066
416.72	10280.00	0.1054
416.68	5290.00	0.1033
416.75	1040.00	0.1013
436.23	20100.00	0.1051
436.34	15130.00	0.1036
436.48	10230.00	0.1026
436.52	5170.00	0.0992
436.37	1020.00	0.0972
456.02	20030.00	0.1029
456.22	15290.00	0.1003
456.24	10330.00	0.0990
456.04	5400.00	0.0956
456.26	1140.00	0.0928
476.38	20260.00	0.0994
476.75	15330.00	0.0965
476.35	10170.00	0.0941
476.73	5010.00	0.0914
476.61	1110.00	0.0901
496.03	20300.00	0.0962
496.27	15290.00	0.0945
496.31	10420.00	0.0928
496.49	5210.00	0.0870
496.15	2850.00	0.0875
516.06	20190.00	0.0940
516.20	15360.00	0.0916
516.21	10220.00	0.0906
516.40	5090.00	0.0862
536.56	20330.00	0.0921
536.39	15400.00	0.0897
536.30	10150.00	0.0873
556.59	20100.00	0.0927
556.53	15430.00	0.0908
556.68	10050.00	0.0869
576.72	20150.00	0.0885
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[56.04; 300.47]	J/mol×K	[150.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			4.72250e+01
Coefficient B			-5.65850e+02
Coefficient C			5.94824e+00
Coefficient D			5.53500e-06
Coefficient E			-1.99800e-08
Temperature range, min.			150.00
Temperature range, max.			1500.00
Cp,gas	56.04	J/mol×K	150.00	Calculated Property
Cp,gas	105.31	J/mol×K	300.00	Calculated Property
Cp,gas	156.00	J/mol×K	450.00	Calculated Property
Cp,gas	195.83	J/mol×K	600.00	Calculated Property
Cp,gas	226.10	J/mol×K	750.00	Calculated Property
Cp,gas	249.24	J/mol×K	900.00	Calculated Property
Cp,gas	267.11	J/mol×K	1050.00	Calculated Property
Cp,gas	281.05	J/mol×K	1200.00	Calculated Property
Cp,gas	291.95	J/mol×K	1350.00	Calculated Property
Cp,gas	300.47	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[134.82; 238.35]	J/mol×K	[178.10; 500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			2.82910e+01
Coefficient B			4.81710e+01
Coefficient C			4.00424e+00
Coefficient D			2.05420e-03
Coefficient E			8.78750e-07
Temperature range, min.			178.10
Temperature range, max.			500.00
Cp,liquid	134.82	J/mol×K	178.10	Calculated Property
Cp,liquid	139.23	J/mol×K	213.87	Calculated Property
Cp,liquid	145.60	J/mol×K	249.63	Calculated Property
Cp,liquid	153.61	J/mol×K	285.40	Calculated Property
Cp,liquid	163.20	J/mol×K	321.17	Calculated Property
Cp,liquid	174.40	J/mol×K	356.93	Calculated Property
Cp,liquid	187.32	J/mol×K	392.70	Calculated Property
Cp,liquid	202.13	J/mol×K	428.47	Calculated Property
Cp,liquid	219.05	J/mol×K	464.23	Calculated Property
Cp,liquid	238.35	J/mol×K	500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0156138; 0.0000752]	Pa×s	[178.18; 473.40]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.52840e+02
Coefficient B			5.64460e+03
Coefficient C			2.28260e+01
Coefficient D			-4.09870e-05
Coefficient E			2.00000e+00
Temperature range, min.			178.18
Temperature range, max.			473.40
η	0.0156138	Pa×s	178.18	Calculated Property
η	0.0031797	Pa×s	210.98	Calculated Property
η	0.0012765	Pa×s	243.78	Calculated Property
η	0.0007262	Pa×s	276.59	Calculated Property
η	0.0004900	Pa×s	309.39	Calculated Property
η	0.0003542	Pa×s	342.19	Calculated Property
η	0.0002578	Pa×s	374.99	Calculated Property
η	0.0001818	Pa×s	407.80	Calculated Property
η	0.0001212	Pa×s	440.60	Calculated Property
η	0.0000752	Pa×s	473.40	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[44.58; 14.19]	kJ/mol	[178.18; 569.98]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			5.37520e+01
Coefficient B			5.03410e-01
Coefficient C			2.47550e-01
Coefficient D			-7.28980e-01
Coefficient E			3.77940e-01
Critical temperature, Tc (K)			5.91750e+02
Temperature range, min.			178.18
Temperature range, max.			569.98
ΔvapH	44.58	kJ/mol	178.18	Calculated Property
ΔvapH	42.23	kJ/mol	221.71	Calculated Property
ΔvapH	39.88	kJ/mol	265.25	Calculated Property
ΔvapH	37.51	kJ/mol	308.78	Calculated Property
ΔvapH	35.06	kJ/mol	352.31	Calculated Property
ΔvapH	32.47	kJ/mol	395.85	Calculated Property
ΔvapH	29.59	kJ/mol	439.38	Calculated Property
ΔvapH	26.16	kJ/mol	482.91	Calculated Property
ΔvapH	21.64	kJ/mol	526.45	Calculated Property
ΔvapH	14.19	kJ/mol	569.98	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[278.80; 409.82]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.44176e+01
Coefficient B			-3.35553e+03
Coefficient C			-4.13230e+01
Temperature range, min.			278.80
Temperature range, max.			409.82
Pvap	1.33	kPa	278.80	Calculated Property
Pvap	3.02	kPa	293.36	Calculated Property
Pvap	6.24	kPa	307.92	Calculated Property
Pvap	11.97	kPa	322.47	Calculated Property
Pvap	21.54	kPa	337.03	Calculated Property
Pvap	36.69	kPa	351.59	Calculated Property
Pvap	59.58	kPa	366.15	Calculated Property
Pvap	92.79	kPa	380.70	Calculated Property
Pvap	139.36	kPa	395.26	Calculated Property
Pvap	202.67	kPa	409.82	Calculated Property
Pvap	[1.01e-04; 3840.11]	kPa	[178.18; 591.75]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			2.59912e+01
Coefficient B			-5.01381e+03
Coefficient C			-1.34892e+00
Coefficient D			-1.86993e-06
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 592.15 K.
Temperature range, min.			178.18
Temperature range, max.			591.75
Pvap	1.01e-04	kPa	178.18	Calculated Property
Pvap	0.02	kPa	224.13	Calculated Property
Pvap	0.77	kPa	270.08	Calculated Property
Pvap	8.81	kPa	316.04	Calculated Property
Pvap	51.84	kPa	361.99	Calculated Property
Pvap	196.55	kPa	407.94	Calculated Property
Pvap	548.50	kPa	453.89	Calculated Property
Pvap	1224.96	kPa	499.85	Calculated Property
Pvap	2313.90	kPa	545.80	Calculated Property
Pvap	3840.11	kPa	591.75	Calculated Property
Pvap	[4.12e-05; 4093.14]	kPa	[178.18; 591.79]	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			7.41358e+01
Coefficient B			-6.91880e+03
Coefficient C			-8.79548e+00
Coefficient D			5.75491e-06
Coefficient E			0.00000e+00
Temperature range, min.			178.18
Temperature range, max.			591.79
Pvap	4.12e-05	kPa	178.18	Calculated Property
Pvap	0.02	kPa	224.14	Calculated Property
Pvap	0.74	kPa	270.09	Calculated Property
Pvap	8.96	kPa	316.05	Calculated Property
Pvap	52.33	kPa	362.01	Calculated Property
Pvap	193.07	kPa	407.96	Calculated Property
Pvap	528.04	kPa	453.92	Calculated Property
Pvap	1181.47	kPa	499.88	Calculated Property
Pvap	2305.03	kPa	545.83	Calculated Property
Pvap	4093.14	kPa	591.79	Calculated Property
Pvap	[0.91; 3.76]	kPa	[273.13; 297.89]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.43607e+01
Coefficient B			-3.28452e+03
Coefficient C			-4.59570e+01
Reference			Besley and Bottomley, 1974
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			273.13
Temperature range, max.			297.89
Pvap	0.91	kPa	273.13	Calculated Property
Pvap	1.08	kPa	275.88	Calculated Property
Pvap	1.28	kPa	278.63	Calculated Property
Pvap	1.51	kPa	281.38	Calculated Property
Pvap	1.77	kPa	284.13	Calculated Property
Pvap	2.07	kPa	286.89	Calculated Property
Pvap	2.42	kPa	289.64	Calculated Property
Pvap	2.81	kPa	292.39	Calculated Property
Pvap	3.25	kPa	295.14	Calculated Property
Pvap	3.76	kPa	297.89	Calculated Property
Pvap	[4.85; 27.02]	kPa	[303.00; 343.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40054e+01
Coefficient B			-3.10016e+03
Coefficient C			-5.35080e+01
Reference			Gaw and Swinton, 1968, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			303.00
Temperature range, max.			343.00
Pvap	4.85	kPa	303.00	Calculated Property
Pvap	6.03	kPa	307.44	Calculated Property
Pvap	7.44	kPa	311.89	Calculated Property
Pvap	9.11	kPa	316.33	Calculated Property
Pvap	11.09	kPa	320.78	Calculated Property
Pvap	13.41	kPa	325.22	Calculated Property
Pvap	16.11	kPa	329.67	Calculated Property
Pvap	19.24	kPa	334.11	Calculated Property
Pvap	22.86	kPa	338.56	Calculated Property
Pvap	27.02	kPa	343.00	Calculated Property
Pvap	[256.95; 3545.12]	kPa	[420.00; 580.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.50689e+01
Coefficient B			-4.00218e+03
Coefficient C			3.94000e-01
Reference			Ambrose, Broderick, et al., 1967
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			420.00
Temperature range, max.			580.00
Pvap	256.95	kPa	420.00	Calculated Property
Pvap	378.09	kPa	437.78	Calculated Property
Pvap	539.84	kPa	455.56	Calculated Property
Pvap	750.45	kPa	473.33	Calculated Property
Pvap	1018.67	kPa	491.11	Calculated Property
Pvap	1353.56	kPa	508.89	Calculated Property
Pvap	1764.39	kPa	526.67	Calculated Property
Pvap	2260.47	kPa	544.44	Calculated Property
Pvap	2851.03	kPa	562.22	Calculated Property
Pvap	3545.12	kPa	580.00	Calculated Property
Pvap	[6.35; 103.90]	kPa	[308.52; 384.66]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39957e+01
Coefficient B			-3.09454e+03
Coefficient C			-5.37730e+01
Reference			Williamham, Taylor, et al., 1945
Temperature range, min.			308.52
Temperature range, max.			384.66
Pvap	6.35	kPa	308.52	Calculated Property
Pvap	9.38	kPa	316.98	Calculated Property
Pvap	13.53	kPa	325.44	Calculated Property
Pvap	19.08	kPa	333.90	Calculated Property
Pvap	26.38	kPa	342.36	Calculated Property
Pvap	35.80	kPa	350.82	Calculated Property
Pvap	47.78	kPa	359.28	Calculated Property
Pvap	62.77	kPa	367.74	Calculated Property
Pvap	81.29	kPa	376.20	Calculated Property
Pvap	103.90	kPa	384.66	Calculated Property
Pvap	[0.89; 12.19]	kPa	[273.00; 323.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.41415e+01
Coefficient B			-3.17199e+03
Coefficient C			-5.05070e+01
Reference			Pitzer and Scott, 1943
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			273.00
Temperature range, max.			323.00
Pvap	0.89	kPa	273.00	Calculated Property
Pvap	1.26	kPa	278.56	Calculated Property
Pvap	1.76	kPa	284.11	Calculated Property
Pvap	2.41	kPa	289.67	Calculated Property
Pvap	3.25	kPa	295.22	Calculated Property
Pvap	4.34	kPa	300.78	Calculated Property
Pvap	5.71	kPa	306.33	Calculated Property
Pvap	7.43	kPa	311.89	Calculated Property
Pvap	9.57	kPa	317.44	Calculated Property
Pvap	12.19	kPa	323.00	Calculated Property
Pvap	[4.85; 27.02]	kPa	[303.00; 343.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40054e+01
Coefficient B			-3.10016e+03
Coefficient C			-5.35080e+01
Reference			Gaw and Swinton, 1968
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			303.00
Temperature range, max.			343.00
Pvap	4.85	kPa	303.00	Calculated Property
Pvap	6.03	kPa	307.44	Calculated Property
Pvap	7.44	kPa	311.89	Calculated Property
Pvap	9.11	kPa	316.33	Calculated Property
Pvap	11.09	kPa	320.78	Calculated Property
Pvap	13.41	kPa	325.22	Calculated Property
Pvap	16.11	kPa	329.67	Calculated Property
Pvap	19.24	kPa	334.11	Calculated Property
Pvap	22.86	kPa	338.56	Calculated Property
Pvap	27.02	kPa	343.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[980.85; 381.88]	kg/m3	[163.10; 589.80]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			8.27394e+01
Coefficient B			2.73590e-01
Coefficient C			5.91750e+02
Coefficient D			3.00060e-01
Temperature range, min.			163.10
Temperature range, max.			589.80
ρl	980.85	kg/m3	163.10	Calculated Property
ρl	941.76	kg/m3	210.51	Calculated Property
ρl	900.89	kg/m3	257.92	Calculated Property
ρl	857.78	kg/m3	305.33	Calculated Property
ρl	811.79	kg/m3	352.74	Calculated Property
ρl	761.93	kg/m3	400.16	Calculated Property
ρl	706.49	kg/m3	447.57	Calculated Property
ρl	642.02	kg/m3	494.98	Calculated Property
ρl	559.44	kg/m3	542.39	Calculated Property
ρl	381.88	kg/m3	589.80	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.02]	N/m	[178.25; 383.75]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			6.33775e-02
Coefficient B			-1.18900e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			178.25
Temperature range, max.			383.75
γ	0.04	N/m	178.25	Calculated Property
γ	0.04	N/m	201.08	Calculated Property
γ	0.04	N/m	223.92	Calculated Property
γ	0.03	N/m	246.75	Calculated Property
γ	0.03	N/m	269.58	Calculated Property
γ	0.03	N/m	292.42	Calculated Property
γ	0.03	N/m	315.25	Calculated Property
γ	0.02	N/m	338.08	Calculated Property
γ	0.02	N/m	360.92	Calculated Property
γ	0.02	N/m	383.75	Calculated Property
γ	[0.04; 0.00]	N/m	[178.18; 569.98]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-1.42610e-02
Coefficient B			1.96660e+01
Coefficient C			-2.79220e+00
Coefficient D			-3.51880e-04
Coefficient E			-3.76370e-06
Temperature range, min.			178.18
Temperature range, max.			569.98
γ	0.04	N/m	178.18	Calculated Property
γ	0.04	N/m	221.71	Calculated Property
γ	0.03	N/m	265.25	Calculated Property
γ	0.03	N/m	308.78	Calculated Property
γ	0.02	N/m	352.31	Calculated Property
γ	0.02	N/m	395.85	Calculated Property
γ	0.01	N/m	439.38	Calculated Property
γ	0.01	N/m	482.91	Calculated Property
γ	0.00	N/m	526.45	Calculated Property
γ	0.00	N/m	569.98	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.10]	W/m×K	[178.18; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			6.77841e-06
Coefficient B			1.42825e+00
Coefficient C			3.53347e+02
Coefficient D			-5.22208e+04
Temperature range, min.			178.18
Temperature range, max.			1000.00
λgas	0.01	W/m×K	178.18	Calculated Property
λgas	0.01	W/m×K	269.49	Calculated Property
λgas	0.02	W/m×K	360.81	Calculated Property
λgas	0.03	W/m×K	452.12	Calculated Property
λgas	0.04	W/m×K	543.43	Calculated Property
λgas	0.05	W/m×K	634.75	Calculated Property
λgas	0.06	W/m×K	726.06	Calculated Property
λgas	0.07	W/m×K	817.37	Calculated Property
λgas	0.09	W/m×K	908.69	Calculated Property
λgas	0.10	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.16; 0.09]	W/m×K	[178.18; 474.85]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			-7.29220e-02
Coefficient B			-2.31530e+01
Coefficient C			-1.02770e+00
Coefficient D			-1.70740e-03
Coefficient E			3.67870e-07
Temperature range, min.			178.18
Temperature range, max.			474.85
λliquid	0.16	W/m×K	178.18	Calculated Property
λliquid	0.15	W/m×K	211.14	Calculated Property
λliquid	0.15	W/m×K	244.11	Calculated Property
λliquid	0.14	W/m×K	277.07	Calculated Property
λliquid	0.13	W/m×K	310.03	Calculated Property
λliquid	0.12	W/m×K	343.00	Calculated Property
λliquid	0.11	W/m×K	375.96	Calculated Property
λliquid	0.11	W/m×K	408.92	Calculated Property
λliquid	0.10	W/m×K	441.89	Calculated Property
λliquid	0.09	W/m×K	474.85	Calculated Property

Similar Compounds

Find more compounds similar to Toluene.

Mixtures

• Toluene + Acetonitrile + Water
• Toluene + Acetone + Water
• Toluene + Acetone
• Toluene + Acetonitrile
• Toluene + Octacosanol
• Toluene + Ethane, iodo-
• Toluene + Methyl Alcohol
• Toluene + Ethanol
• 1-Propanol + Toluene
• Toluene + Ethane, iodo- + Methyl Alcohol
• Toluene + Ethane, iodo- + Ethanol
• 1-Propanol + Toluene + Ethane, iodo-
• Toluene + Water
• Benzene, nitro- + Toluene
• Benzene + Toluene
• Toluene + Benzene, 1,3-dimethyl-
• Toluene + Formamide, N-methyl-
• Toluene + 1-Octanol
• Toluene + Pentane, 2,2,4-trimethyl-
• Toluene + Propane, 2-methoxy-2-methyl-

Find more mixtures with Toluene.

Sources

• KDB Vapor Pressure Data
• Active Thermochemical Tables 1.112, gas-phase enthalpies of formation ChEDL chemicals 1.5.2, from Active Thermochemical Tables (ATcT), version 1.112, Argonne National Laboratory; Ruscic, B. et al. Active Thermochemical Tables: Thermochemistry for the 21st Century. J. Phys.: Conf. Ser. 2005, 16, 561.
• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• Hankinson and Thomson (1979), COSTALD parameters ChEDL chemicals 1.5.2, from Hankinson, R. W.; Thomson, G. H. A New Correlation for Saturated Densities of Liquids and Their Mixtures. AIChE J. 1979, 25, 653-663.
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 ChEDL chemicals 1.5.2, from Tsonopoulos, C.; Ambrose, D. Vapor-Liquid Critical Properties of Elements and Compounds. 3. Aromatic Hydrocarbons. J. Chem. Eng. Data 1995, 40, 547-558.
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• High-Pressure Viscosity Measurements for the Ethanol + Toluene Binary System
• Effect of Temperature on the Change of Refractive Index on Mixing for Butyl Acetate + Aromatic Hydrocarbons
• Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
• Thermal Conductivities of [bmim][PF6], [hmim][PF6], and [omim][PF6] from 294 to 335 K at Pressures up to 20 MPa.
• A Digital Variable-Angle Rolling-Ball Viscometer for Measurement of Viscosity, Density, and Bubble-Point Pressure of CO2 and Organic Liquid Mixtures
• Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
• Viscometric and Volumetric Properties of 10 Regular Binary Systems at 308.15 K and 313.15 K
• Thermodynamic Properties of Ternary Liquid Mixtures of 2-Pyrrolidinone with Aromatic Hydrocarbons
• Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
• Topological Investigations of Excess Molar Volumes and Excess Isentropic Compressibilities of Ternary Mixtures Containing Pyrrolidin-2-one at 308.15 K
• Isentropic Compressibilities Changes of Mixing of Tetrahydropyran and Aromatic Hydrocarbons Ternary Mixtures at 308.15 K
• Densities and Kinematic Viscosities of One Quinary Regular Liquid System and Its Five Quaternary Sub-Systems at Temperatures (293.15 and 298.15) K
• Study of Acoustic Parameters in Binary Mixture at Variable Frequencies
• Densities and Kinematic Viscosities of a Quinary Regular Liquid System and Its Five Quaternary Subsystems at 293.15A K and 298.15A K
• Thermal Conductivity of n-Pentadecane (C15H32)
• Hydrogen solubility in a chemical hydrogen storage medium, aromatic hydrocarbon, cyclic hydrocarbon, and their mixture for fuel cell systems
• Experimental solubility data of various n-alkane waxes: effects of alkane chain length, alkane odd versus even carbon number structures, and solvent chemistry on solubility
• The experiments and correlations of the solubility of ethylene in toluene solvent
• An equipment for dynamic measurements of vapour liquid equilibria and results in binary systems containing cyclohexylamine
• Volumetric properties under pressure for the binary system ethanol + toluene
• Topological and thermodynamic investigations of molecular interactions in binary mixtures: Molar excess volumes and molar excess enthalpies
• Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
• Experimental investigation of the vapour-liquid equilibrium of binary and ternary mixtures containing dibutyl ether (DBE), cyclohexane and toluene at 313.15 K
• Vapor liquid liquid equilibria of perfluorohexane +CO2 + methanol, +toluene, and +acetone at 313K
• Solubility of hydrogen in toluene for the ternary system H2 +CO2 + toluene from 305 to 343K and 1.2 to 10.5MPa
• Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
• Infinite dilution activity coefficient measurements by inert gas stripping method
• Volumetric and derivative properties under pressure for the system 1-propanol + toluene: A discussion of PC-SAFT and SAFT-VR
• Ternary liquid liquid equilibria for mixtures of toluene + n-heptane + an ionic liquid
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• Binary liquid liquid equilibrium in the systems containing monofunctional benzene derivates and 1,2-ethanediol
• Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
• Vapor liquid equilibrium for binary system of diethyl sulfide + cyclohexane at 353.15 and 343.15 K and diethyl sulfide + 2-ethoxy-2-methylpropane at 343.15 and 333.15 K
• Densities, viscosities and ultrasonic velocities of binary mixtures of methylbenzene with hexan-2-ol, heptan-2-ol and octan-2-ol at T = 298.15 and 308.15K
• Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
• A simple apparatus for data solubility determination
• 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)
• Vapor liquid equilibrium for binary system of thiophene + 2,2,4-trimethylpentane at 343.15 and 353.15K and thiophene + 2-ethoxy-2-methylpropane at 333.15 and 343.15K
• Ultrasonic and viscometric study of molecular interactions in binary mixtures of aniline with 1-propanol, 2-propanol, 2-methyl-1-propanol, and 2-methyl-2-propanol at different temperatures
• Vapor liquid equilibria in ternary systems of associating components (water, aniline, cyclohexylamine) and hydrocarbons (octane or toluene)
• Hydrogen solubility of mixed naphthenes and aromatics for a new hydrogen storage medium in fuel cell system
• Vapor-liquid equilibrium for the binary mixtures of dimethylsulfoxide with substituted benzenes
• Isothermal vapor liquid equilibrium at 333.15K and excess volumes and molar refractivity deviation at 298.15K for the ternary system di-butyl ether (1) + ethanol (2) + toluene (3) and its binary subsystems
• Measurements of the isochoric heat capacity, the critical point (TC, nC) and vapor liquid coexistence curve (TS, nS) of high-purity toluene near the critical point*
• Excess enthalpies of dimethylsulfoxide with substituted benzenes at 298.15K
• Liquid liquid equilibrium of ternary systems 1-butyl-3-methylimidazolium hexafluorophosphate + aromatic + aliphatic
• Homogeneity of the water + ethanol + toluene azeotrope at 101.3 kPa
• Experimental and predicted phase equilibria and excess properties for systems with ionic liquids
• A new high-pressure vapour liquid equilibrium apparatus
• Isothermal vapor liquid equilibrium at 333.15K and excess molar volumes at 298.15K for the ternary system di-isopropyl ether + n-propyl alcohol + toluene and its binary subsystems
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
• Isothermal vapor liquid equilibria for binary mixtures of benzene, toluene, m-xylene, and N-methylformamide at 333.15K and 353.15K
• 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
• Liquid phase equilibria for mixtures of (an aliphatic hydrocarbon + toluene + gamma-butyrolactone)
• 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
• Vapor liquid equilibrium for the binary systems tetrahydrothiophene + toluene and tetrahydrothiophene + o-xylene at 368.15 K and 383.15 K
• Measurement and correlation of liquid liquid equilibria for ternary systems {cyclooctane + aromatic hydrocarbon + 1-ethyl-3-methylpyridinium ethylsulfate} at T = 298.15 K and atmospheric pressure
• (Solid + liquid) and (liquid + liquid) phase equilibria study and correlation of the binary systems {N-butyl-3-methylpyridinium tosylate + water, or + an alcohol, or + a hydrocarbon}
• Liquid liquid equilibrium of ternary systems 1-octyl-3-methylimidazolium hexafluorophosphate + aromatic + aliphatic hydrocarbons
• Phase equilibria on five binary systems containing 1-butanethiol and 3-methylthiophene in hydrocarbons
• Phase equilibria for systems containing dimethyl disulfide and diethyl disulfide with hydrocarbons at 368.15 K
• Liquid-liquid equilibria for ternary systems of {cyclohexane + aromatic compounds + 1-ethyl-3-methylpyridinium ethylsulfate}
• Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
• Prediction of phase equilibria and excess properties for systems with ionic liquids using modified UNIFAC: Typical results and present status of the modified UNIFAC matrix for ionic liquids
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• N-butylpyridinium bis-(trifluoromethylsulfonyl)imide ionic liquids as solvents for the liquid-liquid extraction of aromatics from their mixtures with alkanes: isomeric effect of the cation
• Isothermal vapor-liquid equilibrium at T = 333.15 K and excess volumes and molar refractivity deviation at T = 298.15 K for the ternary mixtures {di-methyl carbonate (DMC) + ethanol + benzene} and {DMC+ ethanol + toluene}
• Application of [EMim][ESO4] ionic liquid as solvent in the extraction of toluene from cycloalkanes: Study of liquid-liquid equilibria at T = 298.15 K
• Influence of anion structure on the liquid-liquid equilibria of 1-(3-hydroxypropyl)pyridinium cation based ionic liquid-hydrocarbon binary systems
• Physical properties of 3-methyl-N-butylpyridinium tricyanomethanide and ternary LLE data with an aromatic and an aliphatic hydrocarbon at T = (303.2 and 328.2) K and p = 0.1 MPa
• Liquid-liquid equilibria of {n-heptane + toluene + aniline} ternary system: Experimental data and correlation
• Vapor liquid liquid equilibrium and vapor liquid equilibrium for the quaternary system water ethanol cyclohexane toluene and the ternary system water cyclohexane toluene. Isobaric experimental determination at 101.3 kPa
• Solubility of elemental sulfur in pure organic solvents and organic solvent-ionic liquid mixtures from 293.15 to 353.15 K
• Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
• Hexyl dimethylpyridinium ionic liquids for desulfurization of fuels. Effect of the position of the alkyl side chains
• Ether + alcohol + hydrocarbon mixtures in fuels and bio-fuels: Excess enthalpies of binary mixtures containing dibutyl ether (DBE) or 1-butanol and 1-hexene or methylcyclohexane or toluene or cyclohexane or 2,2,4-trimethylpentane at 298.15K and 313.15K
• Capacity of ionic liquids [EMim][NTf2] and [EMpy][NTf2] for extraction of toluene from mixtures with alkanes: Comparative study of the effect of the cation
• Effect of temperature on the solubility of 3-aminopyridine in binary ethanol + toluene solvent mixtures
• Thermodynamic characterization of second generation biofuels: Vapour-liquid equilibria and excess enthalpies of the binary mixtures 1-pentanol and cyclohexane or toluene
• Phase equilibrium properties of the ternary mixture dibutyl ether + toluene + heptane at 313.15 K
• Determination of the solubility, dissolution enthalpy and entropy of pyrene in different solvents
• Isobaric vapor-liquid equilibrium for four binary systems of 3-methylthiophene
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid ethyl(2-hydroxyethyl)dimethyl-ammonium diethylphosphate using gas liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
• Effect of 1-methyl 3-octylimidazolium thiocyanate on vapor-liquid equilibria of binary mixtures of hydrocarbons
• Vapour-liquid equilibrium (VLE) for the systems furan + n-hexane and furan + toluene. Measurements, data treatment and modeling using molecular models
• Solubility of hydrofluorocarbons in aromatic solvents and alcohols: Experimental data and modeling with CPA EoS
• Isobaric vapor-liquid equilibrium of binary systems of decane with p-, o-, m-xylene at 20 kPa
• Liquid-liquid equilibria of imidazolium ionic liquids having bistriflamide or triflate anions with aromatic non-polar and polar compounds
• Separation of toluene from n-heptane using monocationic and dicationic ionic liquids
• Solubility of ethylene in toluene, norbornene, and toluene + norbornene mixture
• Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
• Isobaric vapor-liquid equilibrium for binary systemsof toluene + o-xylene, benzene + o-xylene, nonane + benzene and nonane + heptane at 101.3 kPa
• Using binary mixtures of dicationic ionic liquids for determination ofactivity coefficients at infinite dilution by gas-liquid chromatography
• Enthalpies and Gibbs free energies of solvation in ethylene glycol at298 K: Influence of the solvophobic effect
• A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
• Desulfurization of fuels by liquid-liquid extraction with1-ethyl-3-methylimidazolium ionic liquids
• Solubility of 1, 3, 2-dioxaphosphorinane-5,5-dimethyl -2- (2,4,6-tribromophenoxy)-2-oxide in selected solvents
• Phase equilibria of binary mixtures (ionic liquid + aromatic hydrocarbon): Effect of the structure of the components on the solubility
• Measurements of activity coefficients at infinite dilution in vegetable oils and capric acid using the dilutor technique
• Towards automated characterisation of liquid-liquid equilibria
• Extraction of toluene from alkane using [Bmim][NO3] or [Omim][NO3] ionic liquid at 298.15 K and atmospheric pressure
• Prediction and measurement of phase equilibria for the extraction of BTX from naphtha reformate using BMIMPF6 ionic liquid
• Isobaric vapor-liquid equilibrium for binary system of cinnamaldehyde + benzaldehyde at 10, 20 and 30 kPa
• Liquid-liquid extraction of toluene from n-heptane by {[emim][TCM] + [emim][DCA]} binary ionic liquid mixtures
• Isobaric vapour + liquid equilibria for three binary systems (toluene + anisole, nbutylbenzene + anisole, and guaiacol + anisole) at 101.33 kPa
• Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
• Isobaric vapor-liquid equilibrium for binary and ternary systems with toluene, 2-methoxyethanol and dimethyl sulfoxide at 101.3 kPa
• Thermodynamics of risperidone and solubility in pure organic solvents
• Thermal conductivity of ethyl fluoride (HFC161)
• Study of critical and maximum temperatures of coexistence of liquid and gas phase in hydrocarbons binary mixtures of aromatic hydrocarbons with alkanes and cycloalkanes
• Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
• Heat capacities of binary and ternary mixtures containing o-chlorotoluene, cyclic ether and aromatic hydrocarbons
• Liquid-liquid equilibria for multicomponent mixtures of 2,2-dimethyl-1,3-dioxolane with n-heptane, toluene, ethanol and water
• A modified continuous flow apparatus for gas solubility measurements at high pressure and temperature with camera system
• Measurement and correlation of the solubility of N-(phosphonomethyl)iminodiacetic acid in different organic solvents
• Liquid-liquid equilibria for ternary system water + toluene+ benzaldehyde at (303.2 to 343.2) K
• Phase equilibria of the water + 1-butanol + toluene ternary system at 101.3 kPa
• Isothermal vapor liquid equilibrium and molar excess Gibbs energies of two ternary systems containing either 1-butanol or 2-butanol + 1- hexene + methylbenzene at 313.15 K
• Liquid-liquid equilibrium data for binary systems containing o-dichlorobenzene and nitrobenzene
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
• Vapor liquid equilibria of {n-heptane + toluene + [emim][DCA]} system by headspace gas chromatography
• Removal of aromatic hydrocarbons from hydrocarbon mixture using glycols at 303.15 K and 333.15 K and atmospheric pressure: Experimental and calculated data by NRTL and UNIQUAC models
• Solubilities of phosphoric acid, P,P0-1,4-phenylene P,P,P0,P0-tetraphenyl ester in the organic solvents
• Liquid liquid equilibria in the ternary systems {hexadecane + BTX aromatics + 2-methoxyethanol or acetonitrile} at 298.15 K
• Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
• Solid-liquid equilibrium of diphenyl anilinophosphonate in the different organic solvents
• Experimental measurements and modelling of volumetric properties, refractive index and viscosity of binary systems of ethyl lactate with methyl ethyl ketone, toluene and n-methyl-2-pirrolidone at 288.15 323.15 K and atmospheric pressure. New UNIFAC VISCO and ASOG VISCO interaction parameters
• Measurement of phase equilibria data for the extraction of toluene from alkane using different solvents
• The ionic liquid 1-ethyl-3-methylimidazolium tris(pentafluoroethyl) trifluorophosphate as alternative extractant for BTEX separation
• Liquid-liquid equilibria for ternary mixtures of 2,2-dimethyl-1,3-dioxolane-4-methanol with n-heptane, toluene, ethanol and water
• Liquid-liquid phase diagrams of poly(ethylene glycol) and aromatic hydrocarbons
• Solubility correlation and thermodynamic analysis of two forms of Metaxalone in different pure solvents
• Non-random two-liquid modelling of switchable-hydrophilicity solvent systems: N,N-Dimethylcyclohexanamine, water, and toluene
• Thermodynamics properties, VLE and HE, of the systems 2-pentanol and cyclohexane or methylbenzene for contributing to the knowledge of new biofuels
• Speed of sound measurement in ethyl tert-butyl ether and tert-amyl methyl ether by Brillouin light scattering
• Measurement of infinite dilution partition coefficients of isomeric benzene derivatives in [bmim][Tf2N]-CO2 biphasic system and correlation with the ePC-SAFT equation of state
• Liquid-liquid equilibria in the ternary and multicomponent systems involving hydrocarbons, thiophene or pyridine and ionic liquid (1-benzyl-3-metylimidazolium bis(trifluorometylsulfonyl)imide)
• 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
• Vapor-liquid equilibria for n-heptane + (benzene, toluene, pxylene, or ethylbenzene) + {[4empy][Tf2N] (0.3) + [emim][DCA] (0.7)} binary ionic liquid mixture
• Solubility of D-phenylglycine methyl ester hydrochloride in water and in organic individual or mixed solvents: Experimental data and results of thermodynamic modeling
• Phase-equilibrium measurements with a novel multi-purpose high-pressure view cell: CO2 + n-decane and CO2 + toluene
• Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
• Liquid-liquid equilibria for the extraction of furfural from aqueous solution using different solvents
• Phase equilibria of phenol + toluene + quaternary ammonium salts for the separation of phenols from oil with forming deep eutectic solvents
• Determination of solubility parameters from density measurements for non-polar hydrocarbons at temperatures from (298 to 433) K and pressures up to 137 MPa
• Measurement and prediction of liquid-liquid equilibria in ternary systems containing water, an organic component, and cyclohexanol
• Measurement of the solubility of the salt of 2- mercaptobenzothiazole with cyclohexylamine and tert-butylamine in various solvents at low temperatures: Models and thermodynamic parameters
• In situ measurement of liquid-liquid equilibria by medium field nuclear magnetic resonance
• Separation of the mixture pyridine + methylbenzene via several acidic ionic liquids: Phase equilibrium measurement and correlation
• A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
• Ternary phase behavior of phenol + toluene + zwitterionic alkaloids for separating phenols from oil mixtures via forming deep eutectic solvents
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Phase behavior and densities of propylene + toluene and ethylene + toluene systems to 580 K and 70 MPa
• The solubility of maleic acid in various inorganic salts and organic solvents: Thermodynamics model and parameters
• Surface tension of four oxygenated fuels: experiment and correlation
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
• Plotting of phase (vapor-liquid) transition surface near the critical point out of data from isochoric experiment. Experimental procedure
• Determination and correlation of solubility of 2,2',4,4',6,6 '-hexanitro-1,1'-biphenyl and 2,2',2" ,4,4',4" ,6,6',6" -Nonanitro-1,1 ':3',1"-terphenyl in six pure solvents
• Liquid-liquid equilibria of water + solutes (acetic acid/ acetol/furfural/guaiacol/methanol/phenol/propanal) + solvents (isopropyl acetate/toluene) ternary systems for pyrolysis oil fractionation
• Solubility of 1-methyl-4-nitropyrazole in seventeen pure solvents at temperatures from 283.15 K to 323.15 K
• Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
• 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
• High temperature and pressure water/oil interfacial tension benchmark data for the Ninth Industrial Fluid Properties Simulation Challenge
• Solubility of citalopram hydrobromide in(ethanol + toluene) and (ethanol + ethyl acetate) at 283.15-318.15 K and its correlation with the Jouyban-Acree and CNIBS/R-K models
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Phase equilibria of 1-hexyl-3-methylimidazolium acetate with water and oil
• Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
• Dissolution behavior and thermodynamic properties of lapatinib ditosylate in pure and mixed organic solvents from T = (283.15-323.15) K
• Measurement and modeling of infinite dilution activity coefficients of organic compounds in an equimolar ionic liquid mixture of [Bmim]Cl and [Bmim][Tf2N]
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• Solubility measurements and thermodynamic modeling of pyrazinamide in five different solvent-antisolvent mixtures
• Mixture densities and viscosities of toluene with ethylene or propylene at temperatures to 530 K and pressures to 70 MPa
• (Liquid + liquid) phase behavior for systems containing (aromatic + TBA + methylcyclohexane)
• (Vapour + liquid) equilibria of (1-butanol + benzene, or toluene, or o-, or m-, or p-xylene) at T = 308.15 K
• Effect of temperature on the volumetric properties of (cyclohexanone + an aromatic hydrocarbon)
• Experimental densities and excess volumes for binary mixtures of (dimethyl sulfoxide + an aromatic hydrocarbon) at temperatures from (293.15 to 353.15) K at atmospheric pressure
• (P, Vm, T) Measurements of (toluene + propiophenone) at temperatures from 298.15 K to 328.15 K and at pressures up to 40 MPa
• Excess molar volumes of (acetophenone + benzene, or toluene, or 1,3-xylene, or 1,3,5-trimethylbenzene) at temperatures (298.15 and 328.15) K
• Studies on thermo-acoustic parameters in binary liquid mixtures of phosphinic acid (Cyanex 272) with different diluents at temperature 303.15 K: an ultrasonic study
• A study of densities and volumetric properties of binary mixtures containing nitrobenzene at T = (293.15 to 353.15) K
• Excess Molar Volumes of (propiophenone + benzene, or toluene, or ethylbenzene, or butylbenzene) at temperatures 298.15 K and 328.15 K
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid 1-butyl-3-methyl-imidazolium 2-(2-methoxyethoxy) ethyl sulfate using g.l.c. at T = (298.15, 303.15, and 308.15) K
• Liquid + liquid equilibria for ternary mixtures of (solvent + aromatic hydrocarbon + alkane)
• Liquid phase behaviour of 1-hexyloxymethyl-3-methyl-imidazolium-based ionic liquids with hydrocarbons: The influence of anion
• Partial molar volume of paracetamol in water, 0.1 M HCl and 0.154 M NaCl at T = (298.15, 303.15, 308.15 and 310.65) K and at 101.325 kPa
• The volumetric properties of (1,2-propanediol carbonate + benzene, or toluene, or styrene) binary mixtures at temperatures from T = 293.15 K to T = 353.15 K
• (Liquid + liquid) equilibria for ternary mixtures of (methanol or ethanol + toluene or m-xylene + n-dodecane)
• Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
• Tailor-made ionic liquids
• Experimental and predicted volumetric and refractive index properties of ternary mixtures of iodoethane with toluene and alcohols at temperature 298.15 K and pressure 101 kPa
• Thermodynamic investigation of N,N-dimethylformamide/toluene binary mixtures in the temperature range from 278.15 to 293.15 K
• 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
• Excess and deviation properties for the binary mixtures of methylcyclohexane with benzene, toluene, p-xylene, mesitylene, and anisole at T = (298.15, 303.15, and 308.15) K
• Excess molar volumes of (propiophenone + toluene) and estimated density of liquid propiophenone below its melting temperature
• Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
• Densities and volumetric properties of N-methyl-2-pyrrolidone with aromatic hydrocarbon at different temperature
• Densities and volumes of mixing of the ternary system toluene + butyl acrylate + methyl methacrylate and its binaries at 298.15 K
• Thermodynamic properties of binary mixtures of N-methyl-2-pyrrolidinone with cyclohexane, benzene, toluene at (303.15 to 353.15) K and atmospheric pressure
• Densities, speeds of sound, and refractive indices of the ternary mixtures (toluene + methyl acetate + butyl acetate) and (toluene + methyl acetate + methyl heptanoate) at 298.15 K
• Densities and excess volumes of binary mixtures of N,N-dimethylformamide with aromatic hydrocarbon at different temperature
• Solubility data for toluene in various aqueous alkanolamine solutions
• Physical properties of (propyl propanoate + hexane + toluene) at 298.15 K
• A study on densities and excess volumes in the (c-butyrolactone + aromatic hydrocarbon) system at various temperatures
• Phase equilibria of didecyldimethylammonium nitrate ionic liquid with water and organic solvents
• Determination of solvation and specific interaction enthalpies of adamantane derivatives in aprotic solvents
• Isobaric (vapour + liquid) equilibria data for the binary systems {1,2-dichloroethane (1) + toluene (2)} and {1,2-dichloroethane (1) + acetic acid (2)} at atmospheric pressure
• (Liquid + liquid) equilibria of three ternary systems: (heptane + benzene + N-formylmorpholine), (heptane + toluene + N-formylmorpholine), (heptane + xylene + N-formylmorpholine) from T = (298.15 to 353.15) K
• (Liquid + liquid) equilibria of ternary and quaternary systems containing n-hexane, toluene, m-xylene, propanol, sulfolane, and water at T = 303.15 K
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
• Excess molar volumes of (octane + benzene, or toluene, or 1,3-xylene, or 1,3,5-trimethylbenzene) at temperatures between (298.15 and 328.15) K
• Densities, viscosities, and excess properties of (N-methylmorpholine + cyclohexane, + benzene, and + toluene) at T = (298.15, 303.15, 313.15, 323.15) K
• Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
• Development of a Henry s constant correlation and solubility measurements of n-pentane, i-pentane, cyclopentane, n-hexane, and toluene in water
• (Liquid + liquid) equilibria for ternary mixtures of (ethylene glycol + toluene + n-octane)
• Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
• 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
• Thermodynamics of fuels with a bio-synthetic component (IV): (Vapor + liquid) equilibrium data for the ternary mixture (ethyl 1,1-dimethylethyl ether + 1-hexene + toluene) at T = 313.15 K
• Experimental and theoretical study of surface tension of binary mixtures of (n-alkyl acetates + heptane, benzene, and toluene)
• Thermodynamics of biofuels: Excess enthalpies for binary mixtures involving ethyl 1,1-dimethylethyl ether and hydrocarbons at different temperatures using a new flow calorimeter
• 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
• Automated densimetric system: Measurements and uncertainties for compressed fluids
• Volumetric behaviour of binary liquid systems composed of toluene, isooctane, and methyl tert-butyl ether at temperatures from (298.15 to 328.15) K
• Experimental densities, refractive indices, and speeds of sound of 12 binary mixtures containing alkanes and aromatic compounds at T = 313.15 K
• Volumetric properties of binary liquid mixtures: Application of the Prigogine Flory Patterson theory to excess molar volumes of dichloromethane with benzene or toluene
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
• Effect of temperature on the physical properties of two ionic liquids
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium trifluoromethanesulfonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Temperature and pressure dependences of volumetric properties of two poly(propylene glycol) dimethyl ether lubricants
• (Liquid + liquid) equilibria in the binary systems (aliphatic, or aromatic hydrocarbons + 1-ethyl-3-methylimidazolium ethylsulfate, or 1-butyl-3-methylimidazolium methylsulfate ionic liquids)
• Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
• (Liquid + liquid) equilibria for ternary mixtures of (water + propionic acid + organic solvent) at T = 303.2 K
• (Liquid + liquid) equilibria of (heptane, or hexane, or cyclohexane + toluene + 1,3- dimethyl-2-imidazolidinone) ternary systems at T = 298.15 K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-octyl-3-methylimidazolium hexafluorophosphate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Excess parameter studies on the binary mixtures of toluene with ketones at different temperatures
• Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
• Evaluation of the polysubstituted pyridinium ionic liquid [hmmpy][Ntf2] as a suitable solvent for desulfurization: Phase equilibria
• Thermochemistry of ionic liquid-catalysed reactions. Isomerisation and transalkylation of tert-alkyl-benzenes. Are these systems ideal?
• 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
• Volumetric behaviour of the ternary liquid system composed of methyl tert-butyl ether, toluene, and isooctane at temperatures from (298.15 to 328.15) K: Experimental data and correlation
• Separation of toluene and heptane by liquid liquid extraction using z-methyl-N-butylpyridinium tetrafluoroborate isomers (z = 2, 3, or 4) at T = 313.2 K
• Separation of aromatic hydrocarbons (toluene or benzene) from aliphatic hydrocarbon (n-heptane) by extraction with ethylene carbonate
• 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
• Excess molar volumes, excess molar enthalpies, and excess isentropic compressibilities of tetrahydropyran with aromatic hydrocarbons
• Measurement and correlation of the (p, rho, T) relation of liquid cyclohexane, toluene, and ethanol in the temperature range from 233.15 K to 473.15 K at pressures up to 30 MPa for use as density reference liquids
• 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
• Separation of toluene from cyclic hydrocarbons using 1-butyl-3-methylimidazolium methylsulfate ionic liquid at T = 298.15 K and atmospheric pressure
• Thermodynamic and topological investigations of molecular interactions in binary and ternary mixtures containing 1-methyl pyrrolidin-2-one at T = 308.15 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
• Thermophysical properties and phase equilibria study of the binary systems {N-hexylquinolinium bis(trifluoromethylsulfonyl)imide + aromatic hydrocarbons, or an alcohol}
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Densities, viscosities, speed of sound, and IR spectroscopic studies of binary mixtures of tert-butyl acetate with benzene, methylbenzene, and ethylbenzene at T = (298.15 and 308.15) K
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
• (Liquid + liquid) equilibrium for ternary mixtures of {heptane + aromatic compounds + [EMpy][ESO4]} at T = 298.15 K
• Physical properties of 3-methyl-N-butylpyridinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium tetracyanoborate and ternary LLE data of [3-mebupy]B(CN)4 with an aromatic and an aliphatic hydrocarbon at T = 303.2 K and 328.2 K and p = 0.1 MPa
• (Liquid + liquid) equilibrium for the ternary systems {heptane + toluene + 1-allyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide} and {heptane + toluene + 1-methyl-3-propylimidazolium bis(trifluoromethylsulfonyl)imide} ionic liquids
• Binary and ternary (liquid + liquid) equilibrium for {methylcyclohexane (1) + toluene (2) + 1-hexyl-3-methylimidazolium tetracyanoborate (3)/1-butyl-3-methylimidazolium tetracyanoborate (3)}
• Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
• Isobaric (vapour + liquid) equilibria for sulfolane with toluene, ethylbenzene, and isopropylbenzene at 101.33 kPa
• Thermodynamic properties of biofuels: Heat capacities of binary mixtures containing ethanol and hydrocarbons up to 20 MPa and the pure compounds using a new flow calorimeter
• Volumetric behaviour of binary and ternary liquid systems composed of ethanol, isooctane, and toluene at temperatures from (298.15 to 328.15) K. Experimental data and correlation
• Alkylsulfate-based ionic liquids in the liquid-liquid extraction of aromatic hydrocarbons
• Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Volumetric properties of binary mixtures of tributylamine with benzene derivatives and comparison with ERAS model results at temperatures from (293.15 to 333.15) K
• Solubilities of some organic solutes in 1-ethyl-3-methylimidazolium acetate. Chromatographic measurements and predictions from COSMO-RS
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
• (Liquid + liquid) equilibria for the ternary mixtures (alkane + toluene + ionic liquid) at T = 298.15 K: Influence of the anion on the phase equilibria
• Tar removal from biosyngas in the biomass gasification process. (Liquid + liquid) equilibrium {water + solvent (paraxylene and methyl hexadecanoate) + model molecules of tar (benzene, toluene, phenol)}
• 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
• Determination of infinite dilution activity coefficients using HS-SPME/GC/FID for hydrocarbons in furfural at temperatures of (298.15, 308.15, and 318.15) 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
• The potential of head-space gas chromatography for VLE measurements
• 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
• (Liquid + liquid) equilibrium data of (water + phosphoric acid + solvents) systems at T = (308.2 and 318.2) K
• Application of [HMim][NTf2], [HMim][TfO] and [BMim][TfO] ionic liquids on the extraction of toluene from alkanes: Effect of the anion and the alkyl chain length of the cation on the LLE
• 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
• Measurement and correlation of the solubility of 2,3,4,5-tetrabromothiophene in different solvents
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
• Thermodynamics of mixtures containing amines. XI. Liquid + liquid equilibria and molar excess enthalpies at 298.15 K for N-methylaniline + hydrocarbon systems. Characterization in terms of DISQUAC and ERAS models
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
• (Liquid + liquid) equilibria for the ternary (water + acetic acid + toluene) system at different temperatures: Experimental data and correlation
• Henry s constants and activity coefficients of some organic solutes in 1-butyl,3-methylimidazolium hydrogen sulfate and in 1-methyl,3-trimethylsilylmethylimidazolium chloride
• (Liquid + liquid) equilibria of aqueous solutions of butyric acid with n-heptane and toluene at T = (298.2, 308.2, and 318.2) K
• Desulfurization of fuel-oils with [C2mim][NTf2]: A comparative study
• Advanced calibration, adjustment, and operation of a density and sound speed analyzer
• Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
• Liquid liquid equilibria for ternary systems of (ethylene glycol + toluene + heptane) at temperatures (303.15, 308.15, and 313.15) K and atmospheric pressure: Experimental results and correlation with UNIQUAC and NRTL models
• 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
• Interface adsorption and micelle formation of ionic liquid 1-hexyl-3-methylimidazolium chloride in the toluene + water system
• Viscosity measurements for 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) and trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
• Phase equilibria study of the (N-octylisoquinolinium thiocyanate ionic liquid + aliphatic and aromatic hydrocarbon, or thiophene) binary systems
• Thermodynamics of solvation and solvophobic effect in formamide
• 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
• Volumetric behaviour of the (2,2,4-trimethylpentane + methylbenzene + butan-1-ol) ternary system and its binary sub-systems within the temperature range (298.15-328.15) K
• 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
• Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
• Thermodynamics of fenoxycarb in solution
• 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
• 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
• Selective extraction of toluene from n-heptane using [emim][SCN] and [bmim][SCN] ionic liquids as solvents
• Phase behavior of ternary mixtures {aliphatic hydrocarbon + aromatic hydrocarbon + ionic liquid}: Experimental LLE data and their modeling by COSMO-RS
• (Liquid + liquid) equilibrium at T = 298.15 K for ternary mixtures of alkane + aromatic compounds + imidazolium-based ionic liquids
• The impact of uni-univalent electrolytes on (water + acetic acid + toluene) equilibria: Representation with electrolyte-NRTL model
• Quaternary (liquid + liquid) equilibrium data for the extraction of toluene from alkanes using the ionic liquid [EMim][MSO4]
• Application of 1-pentyl-3-methylimidazolium bis(trifluoromethylsulfonyl) imide for desulfurization, denitrification and dearomatization of FCC gasoline
• 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
• Measurement and correlation of solubility of 4-chloro-2,5-dimethoxynitrobenzene and 4-chloro-2,5- dimethoxyaniline in methanol, ethanol, xylene and toluene
• Phase equilibria study of binary systems comprising an (ionic liquid + hydrocarbon)
• Solvation parameter model and thermodynamic parameters in a dicationic ionic liquid based on pyrrolidinium
• Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
• Phase equilibrium measurements of (methane + benzene) and (methane + methylbenzene) at temperatures from (188 to 348) K and pressures to 13 MPa
• Excess enthalpies of ternary mixtures of (oxygenated additives + aromatic hydrocarbon) mixtures in fuels and bio-fuels: (Dibutyl-ether + 1-propanol + benzene), or toluene, at T = (298.15 and 313.15) K
• 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
• Measurement and correlation of the solubility of 3,4-bis(3-nitrofurazan-4-yl)furoxan (DNTF) in different solvents
• Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
• Volumetric behavior of the ternary system (methyl tert-butyl ether + methylbenzene + butan-1-ol) and its binary sub-system (methyl tert-butyl ether + butan-1-ol) within the temperature range (298.15 to 328.15) K
• (Vapour + liquid) equilibria, (VLE) excess molar enthalpies and infinite dilution activity coefficients of selected binary systems involving n-hexyl pyridinium bis(trifluoromethylsulphonyl)imide ionic liquid: Experimental and predictions using modified UNIFAC (Dortmund)
• Solubility measurement and modelling of 1,8-dinitronaphthalene in nine organic solvents from T = (273.15 to 308.15) K and mixing properties of solutions
• Use of selective ionic liquids and ionic liquid/salt mixtures as entrainer in a (vapor + liquid) system to separate n-heptane from toluene
• 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
• Ultrasonic and 31P NMR investigations of an acidic nuclear extractant with some monosubstituted benzenes
• Solubility determination and correlation for 1,8-dinitronaphthalene in (acetone + methanol), (toluene + methanol) and (acetonitrile + methanol) mixed solvents
• (Liquid + liquid) equilibrium of ternary and quaternary systems containing heptane, cyclohexane, toluene and the ionic liquid [EMim][N(CN)2]. Experimental data and correlation
• Solubility modelling and thermodynamic dissolution functions of phthalimide in ten organic solvents
• Solubility and solution thermodynamics of ethyl 5-amino-4-cyano-3-(2-ethoxy-2-oxoethyl)-2-thiophenecarboxylate in nine organic solvents at evaluated temperatures
• Contributing to accurate high pressure viscosity measurements: Vibrating wire viscometer and falling body viscometer techniques
• Selective recovery of aliphatics from aromatics in the presence of the {[4empy][Tf2N] + [emim][DCA]} ionic liquid mixture
• Solvation of hydrocarbons in aqueous-organic mixtures
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Determination and thermodynamic modeling of solid-liquid phase equilibrium for 3,5-dichloroaniline in pure solvents and ternary 3,5-dichloroaniline + 1,3,5-trichlorobenzene + toluene system
• Solubility determination and thermodynamic dissolution functions of 1,3-diphenylguanidine in nine organic solvents at evaluated temperatures
• Measurement and correlation of solubility of pronamide in five organic solvents at (278.15-323.15) K
• Solubility determination and thermodynamic modeling of 5-nitro-8- hydroxyquinoline in ten organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Solubility and solution thermodynamics of 2-methyl-6-nitroaniline in ten organic solvents at elevated temperatures
• Solubility determination and thermodynamic models for dehydroepiandrosterone acetate in mixed solvents of (ethyl acetate + methanol), (ethyl acetate + ethanol) and (ethyl acetate + isopropanol)
• 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
• Solubility determination and thermodynamic modeling of 2,4-dinitroaniline in nine organic solvents from T = (278.15 to 318.15) K and mixing properties of solutions
• 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
• Solubility determination and thermodynamic modeling of 3-methyl-4- nitrobenzoic acid in twelve organic solvents from T = (283.15-318.15) K and mixing properties of solutions
• Liquid-liquid extraction of toluene from alkane with pyridinium based ionic liquid ([BPy][NO3] and [HPy][NO3]) at 298.15 K and atmospheric pressure
• Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
• Solubility determination and thermodynamic modelling of 2,4-dihydro-5-methyl-2-(4-methylphenyl)-3H-pyrazol-3-one in twelve organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Solubility of N-phenylanthranilic acid in nine organic solvents from T = (283.15 to 318.15) K: Determination and modelling
• Thermodynamic modelling for solubility of 4-nitrobenzaldehyde in different solvents at temperature range from (273.15 to 313.15) K and mixing properties of solutions
• Fully automatized apparatus for determining speed of sound for liquids in the temperature and pressure interval (283.15-343.15) K and (0.1-95) MPa
• Solubility determination and thermodynamic modeling of paclobutrazol in nine organic solvents from T = (278.15 to 318.15) K and mixing properties of solutions
• Thermodynamic modelling for solubility of 5-chloro-1-methyl-4-nitroimidazole in eleven organic solvents from T = (283.15 to 318.15) K
• Measurement and correlation of solubility of ciclesonide in seven pure organic solvents
• Thermodynamic study of solubility for 2-amino-4-chloro-6-methoxypyrimidine in twelve organic solvents at temperatures from 273.15 K to 323.15 K
• Solubility and solution thermodynamics of 2-methyl-4-nitroaniline in eleven organic solvents at elevated temperatures
• Solubility measurement and thermodynamic functions of 3-nitrobenzaldehyde in different solvents at elevated temperatures
• Solubility determination and modelling of 4-nitro-1,2-phenylenediamine in eleven organic solvents from T = (283.15 to 318.15) K and thermodynamic properties of solutions
• Solubility determination and thermodynamic modelling for 2-amino-4-chlorobenzoic acid in eleven organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Solubility and thermodynamic functions of tebuconazole in nine organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Solubility of 2-isopropylimidazole in nine pure organic solvents and liquid mixture of (methanol + ethyl acetate) from T = (278.15 to 313.15) K: Experimental measurement and thermodynamic modelling
• Solubility of 2-nitro-p-phenylenediamine in nine pure solvents and mixture of (methanol + N-methyl-2-pyrrolidone) from T = (283.15 to 318.15) K: Determination and modelling
• Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
• Solubility of 4-methyl-2-nitroaniline in fourteen organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Solubility determination and thermodynamic modelling of 3,5-dimethylpyrazole in nine organic solvents from T = (283.15 to 313.15) K and mixing properties of solutions
• Solubility of commercial octacosanol in organic solvents and their correlation by thermodynamic models at different temperatures
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Solubility modelling and dissolution properties of 5-phenyltetrazole in thirteen mono-solvents and liquid mixtures of (methanol + ethyl acetate) at elevated temperatures
• Thermodynamic functions for solubility of 2-mercaptobenzothiazole in eleven pure organic solvents at temperatures from 273.15 K to 318.15 K and mixing properties of solutions
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• High-temperature, high-pressure viscosities and densities of toluene
• Conformational analysis of branched alkanes using limiting partial molar volumes
• Liquid-liquid equilibria for toluene/heptane + phenol/cresols + ethylene glycol system
• Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
• 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
• Solvent screening and liquid-liquid measurement for extraction of phenols from aromatic hydrocarbon mixtures
• Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
• Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
• Ternary phase diagram of phenanthrene and carbazole in different solvents and its application in the separation of them
• Solubility parameter of lenalidomide for predicting the type of solubility profile and application of thermodynamic model
• Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
• Speed of sound and derived thermodynamic properties of para-xylene at temperatures between (306 and 448) K and at pressures up to 66 MPa
• Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
• The dissolution behaviour and apparent thermodynamic analysis of diprophylline in pure and mixed solvents
• Co-solvence phenomenon and thermodynamic properties of edaravone in pure and mixed solvents
• Volumetric and viscometric studies of molecular interaction of the ternary system toluene (1) + cyclohexane (2) + n-hexane (3) at 298.15K
• Molecular interactions in binary mixtures containing o-toluidine
• Excess molar volumes and excess isentropic compressibilities of 2-pyrrolidinone at 308.15K
• Molecular interaction studies and theoretical estimation of ultrasonic speeds using scaled particle theory in binary mixtures of toluene with homologous nitriles at different temperatures
• Excess Molar Enthalpies for Binary and Ternary Mixtures containing Cyclic Ether, 2-Methylaniline and Aromatic Hydrocarbons
• Excess molar enthalpies of ternary mixtures containing o-toluidine + tetrahydropyran with pyridine or isomeric picolines or benzene or toluene at 308.15K
• Determination of the solubility, dissolution enthalpy and entropy of 3-pentadecylphenyl acrylate in different organic solvents
• Solubility in binary solvent mixtures: pyrene dissolved in alcohol + toluene mixtures
• Correlation and prediction of the phase behavior and thermal properties of binary and ternary systems of 2,2 -oxybis[propane] + benzene, toluene, cyclohexane or n-heptane
• Dielectric and excess dielectric constants in non polar + polar binary liquidmixtures of toluene with alcohols at 303, 313 and 323 K
• Calorimetric study of solvation of low polar solutes in propylene glycol and methyl cellosolve at 298 K
• Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
• Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
• Volumetric and acoustic properties of binary systems (furfural or furfuryl alcohol + toluene) and (furfuryl alcohol + ethanol) at different temperatures
• New method for determination of vaporization and sublimation enthalpy of aromatic compounds at 298.15 K using solution calorimetry technique and group-additivity scheme
• 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
• Application of a DSC based vapor pressure method for examining the extent of ideality in associating binary mixtures with narrow boiling range oil cuts as a mixture component
• Experimental measurement and phase equilibria calculation for ternary systems of carbon dioxide+ toluene + naphthalene and carbon dioxide+ ethanol + acridine, applicable for fine particle production in GAS process
• Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
• Low cost apparatus for rapid boiling point determination of small air sensitive samples under inert atmosphere
• A new analysis method for improving collection of vapor-liquid equilibrium (VLE) data of binary mixtures using differential scanning calorimetry (DSC)
• Isothermal vapor-liquid equilibrium of binary and ternary systems of anisole, hexane, and toluene and ternary system of methyl tert-butyl ether, hexane, and toluene
• Solubilities of Phosphoramidic Acid, N-(phenylmethyl)-, Diphenyl Ester in Selected Solvents
• Solid Forms, Crystal Habits, and Solubility of Danthron
• Solubility, Thermodynamic Properties, and Derived Excess Properties of Benzoic Acid in (Acetic Acid + Water) and (Acetic Acid + Toluene) Binary Mixtures
• Viscous Calibration Liquids for Self-diffusion Measurements
• Solubility and Dissolution Thermodynamics for 1,3,5- Trichlorobenzene in Organic Solvents
• Mass Diffusion Coefficient and Soret Coefficient of o-Dichlorobenzene Solutions of PCBM and [60]Fullerene by the Soret Forced Rayleigh Scattering Method
• Experimental and Computational Study on Liquid Liquid Equilibrium in Ternary Systems of -Valerolactone, Toluene, and Hydrocarbons
• Vapor Liquid Equilibria of n-Heptane + Toluene +1-Ethyl-4-methylpyridinium Bis(trifluoromethylsulfonyl)imide Ionic Liquid
• Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
• Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
• Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
• Solubility Measurement and Correlation of (+)-Biotin Intermediate Lactone in Different Organic Solvents from (287.15 to 323.75) K
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Solubility Modeling of 4-(Methylsulfonyl)benzaldehyde in Nine Organic Solvents at Elevated Temperatures
• Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene and Trans-decahydronaphthalene
• Solubilities of Dihydroxylammonium 5,5'-Bistetrazole-1,1'-diolate in Various Pure Solvents at Temperatures Between 293.15 and 323.15 K
• Vapor Liquid Equilibria for (n-Hexane, n-Octane, Cyclohexane, or 2,3-Dimethylpentane) + Toluene + {[4empy][Tf2N] (0.3) + [emim][DCA] (0.7)} Mixed Ionic Liquids
• Solubility of Mercury in Liquid Hydrocarbons and Hydrocarbon Mixtures
• Determination and Correlation of Solubility of 3,4-Dinitro-1H-pyrazole in Different Pure Solvents from 298.15 K to 338.15 K
• Solubility Measurement and Thermodynamic Modeling of 4-Nitrophthalimide in Twelve Pure Solvents at Elevated Temperatures Ranging from (273.15 to 323.15) K
• Isothermal Vapor Liquid Equilibrium Data for the Toluene + Methanol + N-Butylpyridinium Bromide System
• Solubility of 3,7,9,11-Tetraoxo-2,4,6,8,10-pentaaza[3.3.3] Propellane (TOPAP) in Different Pure Solvents at Temperatures between 273.15 and 318.15 K
• Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
• Vapor Liquid Equilibrium Data for the Furan-Toluene Binary System between 313.02 and 352.99 K
• Liquid Liquid Equilibria for the Ternary Systems Dodecane + Toluene or Thiophene or Pyridine + 1-Ethyl-3-methylimidazolium Methyl Sulfate
• Measurement and Modeling of Solid Liquid Equilibrium of para-tert-Butylbenzoic Acid in Acetic Acid/Methanol + Water and Acetic Acid + para-tert-Butyltoluene Binary Systems at Various Temperatures
• Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
• Liquid-Liquid Equilibrium Measurements for Model Systems Related to Catalytic Fast Pyrolysis of Biomass
• Mutual solubility of aromatic hydrocarbons in pyrrolidinium and ammonium-based ionic liquids and its modeling using the Cubic-Plus-Association (CPA) Equation of State
• Diffusion Coefficients of Carbon Dioxide in Eight Hydrocarbon Liquids at Temperatures between (298.15 and 423.15) K at Pressures up to 69 MPa
• Isobaric Vapor Liquid Equilibrium for Binary and Ternary Systems of Isoamyl Alcohol + Isoamyl Acetate + Dimethyl Sulfoxide at 101.33 kPa
• Measurement and Correlation of the Solubility of e-CL-20 in 12 Organic Solvents at Temperatures Ranging from 278.15 to 318.15 K
• Solubility Measurement and the Correlation of 1-Naphthaleneacetic Acid in Pure and Methanol + Water Binary Solvents from T = (278.25 to 323.55) K
• Isobaric Vapor Liquid Equilibrium for Binary Systems of Cyclohexanone + Benzene, Cyclohexanone + Toluene, and Cyclohexanone + p-Xylene at 101.3 kPa
• Measurement and Modeling of Solubility of para-tert-Butylbenzoic Acid in Pure and Mixed Organic Solvents at Different Temperatures
• Solvent Polarity Effect when Amberlite-LA2 Is Used in the Extraction of Picric Acid
• Liquid Liquid Equilibria of Binary, Ternary, and Quaternary Systems Involving Monoethylene Glycol, Water, Toluene, p-Xylene, Hexane, and Octane
• Measurement and Prediction of Vapor Liquid(-Liquid) Equilibria in Ternary Systems Containing Water, an Organic Component, and Cyclohexanol
• Dilute Vapor Absorption: A New Accurate Technique for Measurement of the Limiting Activity Coefficient of Water in Hydrophobic Solvents of Lower Volatility
• Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
• Phase Behavior Data of (CO2 + Toluene + Phenanthrene) and (CO2 + (Methanol + Phenanthrene) Systems at High Pressure
• Phase Behavior of the System (Carbon Dioxide + n-Heptane + Methylbenzene): A Comparison between Experimental Data and SAFT-gamma-Mie Predictions
• Solid Liquid Phase Equilibrium of N,N'-Piperazinebis(neopentylglycol)phosphoramidate in Selected Solvents from T = (293.15 to 333.15) K
• Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
• Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
• Experimental Determination and Correlation of Liquid Liquid Equilibria for Water + Cyclohexanone + Solvents (Toluene or p-Xylene) Ternary Systems at 303.15 and 323.15 K under 101.3 kPa
• Experimental and Modeling Studies on the Solubility of 2-Chloro-N-(4-methylphenyl)propanamide (S1) in Binary Ethyl Acetate + Hexane, Toluene + Hexane, Acetone + Hexane, and Butanone + Hexane Solvent Mixtures Using Polythermal Method
• Thermodynamic Functions for Solubility of 1-Hydroxybenzotriazole in Sixteen Solvents at Temperatures from (278.15 to 313.15) K and Mixing Property of Mixtures
• Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
• Liquid-Liquid Equilibrium Data, Density, Viscosity, and Interfacial Tension of Ternary System (Toluene-Acetic Acid-Water) at 298.15 K: Experiment and Correlation
• Solubility Modeling and Mixing Thermodynamics of Thiamphenicol in Water and Twelve Neat Organic Solvents from T = (278.15 to 318.15) K
• Liquid-Liquid Equilibrium Data and Correlation for the Quaternary Systems Water + Polyphenol (Hydroquinone, Catechol, and Resorcinol) + Methyl Isobutyl Ketone + Methylbenzene
• Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
• Thermodynamic Functions for the Solubility of 3-Nitrobenzonitrile in 12 Organic Solvents from T/K = (278.15 to 318.15)
• Determination and Correlation of Liquid-Liquid Equilibria Data for Water + Cyclohexanol + (Mesityl Oxide, Toluene, and p-Xylene) Ternary Systems at Different Temperatures
• Measurement and Correlation of Solubility of Resorcinol Bis(cyclic 2,2-dimethyl-1,3-propanediol phosphate) in Selected Solvents from T = 293.15 to 333.15 K
• Measurement and Correlation of the Solubilities of Sulfur S8 in 10 Solvents
• Measurement and Prediction of Vapor-Liquid Equilibria in Ternary Systems Containing an Organic Component, Cyclohexylamine, and Cyclohexanol
• Solubility Modeling and Mixing Properties for Benzoin in Different Monosolvents and Solvent Mixtures at the Temperature Range from 273.15 to 313.15 K
• Separation of Protocatechuic Acid Using Di-(2-ethylhexyl)phosphoric Acid in Isobutyl Acetate, Toluene, and Petroleum Ether
• Densities and Dynamic Viscosities of Alicyclic Cyclohexane with Toluene, o-Xylene, and Mesitylene at T = (303.15 to 323.15) K and Atmospheric Pressure
• Solubility Measurement and Thermodynamic Modeling of N-(4-Methylphenyl-Z-3-chloro-2-(phenylthio)propenamide in 12 Pure Solvents at Temperatures Ranging from 278.15 to 318.15 K
• Aniracetam Solubility in Pure and Binary Solvents: Effect of Molecular Interaction and Analysis of Crystallized Products
• 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
• Isothermal Vapor-Liquid Equilibrium Data for Binary Systems of CHF3 or C2F6 with Methylcyclohexane or Toluene
• Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
• Solubility of 2-Chlorophenylacetic Acid in 12 Pure Solvents from T = (273.15/283.15 to 318.15) K: Determination and Modeling
• Computation of Liquid Isothermal Compressibility from Density Measurements: An Application to Toluene
• Solid-Liquid Phase Equilibria of the Ternary System (2-Naphthaldehyde + 4-Methylphthalic Anhydride + Ethyl Acetate) at (288.15, 298.15, and 308.15) K
• Solubility Measurement and Modeling of 1-(3-nitrophenyl)Ethanone and 1-(4-nitrophenyl)Ethenone in Nine Pure Organic Solvents from T = (278.15 to 318.15) K and Mixing Properties of Solutions
• Solubility and Molecular Interactions of Trimetazidine Hydrochloride in 12 Monosolvents and Solvent Mixtures of Methanol + (Ethanol, N,N-Dimethylformamide or Ethyl Acetate)
• Solubility Measurement, Modeling, and Thermodynamic Functions for para-Methoxyphenylacetic Acid in Pure and Mixed Organic and Aqueous Systems
• Solubility Measurement and Modeling of 2-Amino-4,6-dichoropyrimidine in Ten Pure Solvents and (Ethyl Acetate + Ethanol) Solvent Mixtures
• Experiment and Computation of Solubility and Dissolution Properties for Enalapril Maleate and Its Intermediate in Pure Solvents
• Solubility Measurement and Correlation for epsilon-2,4,6,8,10,12-Hexanitro-2,4,6,8,10,12-hexaazaisowurtzitane in Different Alkanes/Aromatic Hydrocarbon + Ethyl Acetate Binary Solvents at Temperatures of between 283.15 and 323.15 K
• Influence of Different Solvent Properties and Composition for the Solubility of Iopromide
• Solubilities of Organic Semiconductors and Nonsteroidal Anti-inflammatory Drugs in Pure and Mixed Organic Solvents: Measurement and Modeling with Hansen Solubility Parameter
• Solubility of Toltrazuril and the Effect of a Cosolvent
• Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
• Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
• Solubility of Diflufenican in Pure and Binary Solvent Systems
• Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
• Experimental Measurements and Modeling Study of Liquid-Liquid Equilibrium [(Water + Methyl Oleate + Model Molecules of Tar Issued from the Biomass Gasification Process (Benzene, Toluene, Phenol, Thiophene, and Pyridine)]
• 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
• Solubility Measurement and Thermodynamic Properties of Levetiracetam in Pure and Mixed Solvents
• Measurement and Correlation of Solubility of Gatifloxacin in 12 Pure Solvents from 273.15 K to 318.15 K
• Solubility Measurement and Thermodynamic Model Correlation and Evaluation of 2-Chloro-5-nitroaniline in 12 Pure Solvents
• Experiment and Application of the Solid-Liquid Phase Equilibrium for Ternary 2-Nitro-p-phenylenediamine + Ethyl Acetate + Isopropanol and 2-Nitro-p-phenylenediamine + 4-Nitro-o-phenylenediamine + N-Methyl-2-pyrrolidone systems
• Solubility of N-tert-Butylbenzothiazole-2-sulfenamide in Several Pure and Binary Solvents
• Effect of Solvent Properties and Composition on the Solubility of Ganciclovir Form I
• Solubility Determination and Thermodynamic Modeling of Buprofezin in Different Solvents and Mixing Properties of Solutions
• Solubility in Different Solvents, Correlation, and Solvent Effect in the Solvent Crystallization Process of Iohexol
• Binary Solid-Liquid Solubility Determination and Model Correlation of Quizalofop-p-ethyl in Different Pure Solvents
• Solid-Liquid Equilibrium of Azacyclotridecan-2-one in 15 Pure Solvents from T = 273.15 to 323.15 K: Experimental Determination and Thermodynamic Modeling
• Solubility Determination of 1,5-Naphthalenediamine and 1,8-Naphthalenediamine in Different Solvents and Mixing Properties of Solutions
• Solubility, Model Correlation, and Solvent Effect of 2-Amino-3-methylbenzoic Acid in 12 Pure Solvents
• Solubility and Solution Thermodynamics of 3-Nitrophthalonitrile in 12 Neat Solvents at Temperatures from 278.15 to 323.15 K
• Experimental Determination and Modeling of Liquid-Liquid Equilibrium for Ternary Mixtures of Ethylene Glycol + 1,2-Butanediol + 3-Heptanone or Anisole
• Solid-Liquid Equilibrium of 5-Chloro-8-hydroxyquinoline and 5,7-Dichloro-8-hydroxyquinoline in Different Solvents and Mixing Properties of Solutions
• Parametric Analysis of Mandelic Acid Separation from Aqueous Solutions by Using Secondary Amine Mixture (Amberlite LA-2) in Various Diluents
• Measuring Activity Coefficient at Infinite Dilution of Hydrocarbons in Ionic Liquids and Evaluation of Other Thermodynamic Properties using Gas Chromatography
• Solubility Determination and Thermodynamic Modeling of 2-Mercaptobenzimidazole in 12 Solvents from T = 278.15 K to T = 318.15 K
• Reactive Extraction of Gallic Acid Using Tributyl Phosphate in Different Classes of Diluents
• Solubility Measurement and Thermodynamic Model Correlation of 5-Nitrosalicylaldehyde in Different Solvents
• o-Nitrophenylacetonitrile Solubility in Several Pure Solvents: Measurement, Correlation, and Solvent Effect Analysis
• Solubility of Gastrodin in Pure and Mixed Solvents at 273.15-313.15 K and Its Correlation with Different Thermodynamic Models
• Solubility Measurement and Correlation of 2-Oxindole in 12 Pure Organic Solvents
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• Measurement of the Solubility of Diclazuril and Discussion of the Effect of the Cosolvent
• Ternary Liquid-Liquid Equilibrium of Toluene + Dimethyl Carbonate + ILs at 298.15 K and Atmospheric Pressure
• Determination and Correlation of Solubilities of 1,3,5-Trifluoro-2,4,6-triiodobenzene in Different Solvents from 289.25 to 332.15 K
• Solubility Determination, Correlation, and Solute-Solvent Molecular Interactions of 5-Aminotetrazole in Various Pure Solvents
• Solubility Determination and Thermodynamic Mixing Properties of 5-Methyl-2-pyrazinecarboxylic Acid in Different Solvents
• Solubility and Thermodynamic Modeling of Sulfanilamide in 12 Mono Solvents and 4 Binary Solvent Mixtures from 278.15 to 318.15 K
• Solid-Liquid Phase Equilibrium for Ternary Systems of p-Nitroacetophenone plus m-Nitroacetophenone plus Methanol/Toluene/Ethyl Acetate
• Solubility, Solubility Modeling, and Antisolvent Precipitation of 1,3-Bis(9-carbazolyl)benzene in Organic Solvents
• Binary Equilibrium Solubility of Amidinothiourea in Monosolvents: Experimental Determination, Model Correlation, and Solvent Effect Analysis
• Measurement and Correlation of Solubility of Marbofloxacin in 12 Pure Solvents from 283.15 to 328.15 K
• Solubility Study and Mixing Property of 3,5-Dinitro-2-methylbenzoic Acid in 13 Pure Solvents from 288.15 to 333.15 K
• Experimental and Correlated Liquid-Liquid Equilibrium Data for Ternary Systems (Water + Poly(oxymethylene) Dimethyl Ethers + Toluene) at T = 293.15 and 303.15 K and p = 101.3 kPa
• Solubility Increment and Thermodynamic Analysis of Bioactive Antofloxacin Hydrochloride in Aqueous ChCl/PTS Deep Eutectic Solvent and Cosolvent Mixtures
• Infinite Dilution Activity Coefficients in Ethylene Glycol and Ethylene Carbonate
• Liquid-liquid equilibria for mixtures of (Furfural + an Aromatic hydrocarbon + an alkane) at T=298.15 K
• Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
• Thermodynamic Properties of Mixtures Containing Precursors of Vitamin B5
• Surface Tension of Pure Liquids and Binary Liquid Mixtures
• Solubility of 1-Alkyl-3-methylimidazolium Hexafluorophosphate in Hydrocarbons
• Thermodynamics of Ternary Liquid Mixtures Containing Toluene, Ethylbenzene, and Chlorobenzene
• Infinite Dilution Activity Coefficients of Hydrocarbons in Triethylene Glycol and Tetraethylene Glycol
• Determination of Isobaric Thermal Expansivity of Organic Compounds from 0.1 to 30 MPa at 30 C with an Isothermal Pressure Scanning Microcalorimeter
• Solubility of -Carotene in Binary Solvents Formed by Some Hydrocarbons with Dibutyl Ether and 1,2-Dimethoxyethane
• Isobaric Vapor-Liquid Equilibria of the Ternary System Toluene + Ethylbenzene + Amyl Acetate
• Partition Coefficients of Organic Solutes between Supercritical Carbon Dioxide and Water: Experimental Measurements and Empirical Correlations
• Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for CmH2m+1(OCH2CH2)nOH (m ) 1 or 2 or 4 andn ) 1) + Benzene, + Toluene, + (o-, m-, and p-) Xylenes, + Ethylbenzene, and + Cyclohexane
• Densities, Excess Molar Volumes at T = (298.15 to 313.15) K, Speeds of Sound, Excess Isentropic Compressibilities, Relative Permittivities and Deviations in Molar Polarizations at T = (298.15 and 308.15) K for Methyl Methacrylate + 2-Butoxyethanol or + Dibutyl Ether + Benzene, + Toluene and + p-Xylene
• Liquid-Liquid Equilibria for Binary Mixtures of Water + Benzene, + Toluene, and + p-Xylene from 273 K to 458 K
• Surface Tension and Interfacial Tension of Binary Organic Liquid Mixtures
• Excess Molar Volumes and Viscosities of Binary Mixtures of Sulfolane with Benzene, Toluene, Ethylbenzene, p-Xylene, o-Xylene, and m-Xylene at 303.15 and 323.15 K and Atmospheric Pressure
• Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
• Density, Viscosity, and Excess Properties of Binary Liquid Mixtures of Propylene Carbonate with Polar and Nonpolar Solvents
• Pressure-Density-Temperature Behavior of CO2/Acetone, CO2/Toluene, and CO2/Monochlorobenzene Mixtures in the Near-Critical Region
• Density and Viscosity Studies of Binary Mixtures of N,N-Dimethylformamide with Toluene and Methyl Benzoate at (298.15, 303.15, 308.15, and 313.15) K
• Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with tert-Butyl Methyl Ether and with tert-Amyl Methyl Ether
• Vibrating Wire Viscometer with Wire Diameters of (0.05 and 0.15) mm: Results for Methylbenzene and Two Fluids with Nominal Viscosities at T = 298 K and p = 0.01 MPa of (14 and 232) mPa*s at Temperatures between (298 and 373) K and Pressures below 40 MPa
• Liquid-Liquid Equilibrium for the Quaternary System Toluene + Water + Propionic Acid + Ethyl Acetate at 25 deg C and Atmospheric Pressure
• Experimental Dynamic Viscosities of 2,3-Dimethylpentane up to 60 MPa and from (303.15 to 353.15) K Using a Rolling-Ball Viscometer
• Density Measurements under Pressure for the Binary System 1-Propanol + Toluene
• Measurement of Diffusion Coefficients in Thermodynamically Nonideal Systems
• Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
• Quaternary Liquid-Liquid Equilibrium of Water + Acetic Acid + Propionic Acid + Solvent (Amyl Alcohol, Cyclohexyl Acetate, or Toluene) Systems
• High-Pressure Vapor-Liquid Equilbria of Some Carbon Dioxide + Organic Binary Systems
• Vapor-Liquid Equilibrium Measurements of MTBE and TAME with Toluene
• Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
• Vapor-Liquid Equilibrium and Density of the Binary System 1-Phenylethylamine + Toluene
• Solubility of Imidazoles, Benzimidazoles, and Phenylimidazoles in Dichloromethane, 1-Chlorobutane, Toluene, and 2-Nitrotoluene
• Surface and interfacial tension of the ternary system heptane + toluene + N,N-dimethylformamide
• Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid 1-Butyl-3-methylimidazolium Octyl Sulfate Using Gas-Liquid Chromatography at a Temperature of 298.15 K, 313.15 K, or 328.15 K
• Viscosities and Excess Molar Volumes of the Ternary System Toluene (1) + Cyclohexane (2) + Pentane (3) at 298.15 K
• Apparatus for the Determination of Water Solubility in Hydrocarbon: Toluene and Alkylcyclohexanes (C6 to C8) from 30 C to 180 C
• Isobaric Vapor-Liquid Equilibria for Binary Mixtures of 1,2-Dibromoethane with Benzene, Toluene, Fluorobenzene, and Bromobenzene at Atmospheric Pressure
• Mutual Solubilities of Terpene in Methanol and Water and Their Multicomponent Liquid-Liquid Equilibria
• Densities, Viscosities, and Refractive Indices of Binary Mixtures of Anisole with Benzene, Methylbenzene, Ethylbenzene, Propylbenzene, and Butylbenzene at (293.15 and 303.15) K
• 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
• A Vibrating Edge Supported Plate, Fabricated by the Methods of Micro Electro Mechanical System for the Simultaneous Measurement of Density and Viscosity: Results for Methylbenzene and Octane at Temperatures between (323 and 423) K and Pressures in the Range (0.1 to 68) MPa
• 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
• Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
• Liquid-Liquid Equilibria for Binary and Ternary Systems Containing Glycols, Aromatic Hydrocarbons, and Water: Experimental Measurements and Modeling with the CPA EoS
• Solubilities of 2-(6-Oxido-6H-dibenz[c,e][1,2]oxaphosphorin-6-yl)-methanol in the Selected Solvents
• Determination and Study of the Solubility of Methane in Mixtures of Methanol plus Various Hydrocarbons at High Pressures
• Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Water + Cyclohexylamine + Aromatic Hydrocarbon (Toluene or Propylbenzene) or Aliphatic Hydrocarbon (Heptane or Octane)
• Solubilities at High Dilution of Toluene, Ethylbenzene, 1,2,4-Trimethylbenzene, and Hexane in Di-2-ethylhexyl, Diisoheptyl, and Diisononyl Phthalates
• Ternary Liquid-Liquid(-Liquid) Equilibria of Aniline + Cyclohexylamine + Water, Aniline + Cyclohexylamine + Octane, Aniline + Water + Toluene, and Aniline + Water + Octane
• Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Vapor-Liquid Equilibrium of Ferrocene in Some Organic Solvents Using Spectroscopic Methods
• Distribution of Butyric Acid between Water and Several Solvents
• Azeotropic and Heats of Mixing Data for Several Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-Butoxy Ethanol
• 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
• Solubilities of Benzene, Toluene, and Xylene Isomers in 1-Butyl-3-methylimidazolium Tetrafluoroborate
• Densities and Viscosities for the Ternary Systems of Methyl tert-Butyl Ether + Methanol + Benzene and Methyl tert-Butyl Ether + Methanol + Toluene and Their Sub-binary Systems at 298.15 K
• Vapor-Liquid Equilibrium for Binary System of 1-Propanethiol, Thiophene, and Diethyl Sulfide with Toluene at 90.03 kPa
• Phase Boundaries of CO2 + Toluene, CO2 + Acetone, and CO2 + Ethanol at High Temperatures and High Pressures
• Ternary Liquid-Liquid Equilibria for Systems of (Sulfolane + Toluene or Chloronaphthalene + Octane)
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Liquid-Liquid Equilibria of Ternary and Six-Component Systems Including Cyclohexane, Benzene, Toluene, Ethylbenzene, Cumene, and Sulfolane at 303.15 K
• Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
• Interfacial Tension of Toluene + Water + Sodium Dodecyl Sulfate from (20 to 50) degC and pH between 4 and 9
• Thermodynamics of Fuels with a Biosynthetic Component: Vapor-Liquid Equilibrium Data for Binary and Ternary Mixtures Containing Ethyl 1,1-Dimethylethyl Ether, n-Heptane, and Toluene at T ) 313.15 K
• Excess Molar Volumes at 298.15 K and Isothermal Vapor-Liquid Equilibria at 333.15 K for the Binary Mixtures of Dimethyl Carbonate with Benzene, Toluene, n-Heptane, and Isooctane
• Densities, Viscosities, and Speed of Sound Studies of Binary Mixtures of Methylbenzene with Heptan-1-ol, Octan-1-ol, and Decan-1-ol at (303.15 and 313.15) K
• Solubility of Ethylene in 2,2,4-Trimethylpentane at Various Temperatures and Pressures
• Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
• Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Binary Mixtures at 298.15 K
• Measurement and Correlation of CO2 Solubility in the Systems of CO2 + Toluene, CO2 + Benzene, and CO2 + n-Hexane at Near-Critical and Supercritical Conditions
• Solubility of D-p-Hydroxyphenylglycine in Water, Methanol, Ethanol, Carbon Tetrachloride, Toluene, and N,N-Dimethylformamide between 278 K and 323 K
• Vapor-Liquid Equilibrium for Binary System of Thiophene + n-Hexane at (338.15 and 323.15) K and Thiophene + 1-Hexene at (333.15 and 323.15) K
• Vapor-Liquid Equilibrium for Carbon Dioxide + Isopropyl, Isobutyl, and Isoamyl Acetates
• Solubility of 4-(3,4-Dichlorophenyl)-1-tetralone in Some Organic Solvents
• Ternary and Quaternary Liquid + Liquid Equilibria for Systems of (Water + Toluene + m-Xylene + Phenol)
• Solubility of Xylitol in Ethanol, Acetone, N,N-Dimethylformamide, 1-Butanol, 1-Pentanol, Toluene, 2-Propanol, and Water
• Solubilities of Triphenylphosphine in Ethanol, 2-Propanol, Acetone, Benzene, and Toluene
• Vapor-Liquid Equilibrium for Binary System of Diethyl Sulfide + n-Heptane and Diethyl Sulfide + 2,2,4-Trimethylpentane at (363.15 and 353.15) K
• Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
• Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Styrene
• Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Vapor-Liquid Equilibrium for Binary System of Diethyl Sulfide + n-Hexane at (338.15 and 323.15) K and Diethyl Sulfide + 1-Hexene at (333.15 and 323.15) K
• Densities and Viscosities of N-Formylmorpholine + Benzene, + Toluene at Different Temperatures and Atmospheric Pressures
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
• Liquid-Liquid Equilibria in Ternary Systems of Aromatic Hydrocarbons (Toluene or Ethylbenzene) + Phenols + Water
• Liquid-Liquid Equilibrium of Ternary and Quaternary Systems Including Methyl Acetate, Benzene, Toluene, and Water at 283.2 K under Atmosphere
• Solubility of Artemisinin in Different Single and Binary Solvent Mixtures Between (284.15 and 323.15) K and NRTL Interaction Parameters
• Solubility of Decabromodiphenyl Ether in Different Solvents at (283.0 to 323.0) K
• Solubilities of Phosphorus-Containing Compounds in Selected Solvents
• Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
• Solvent Extraction of Toluene from Heptane with the Ionic Liquids N-Ethylpyridinium Bis(trifluoromethylsulfonyl)imide and z-Methyl-N-ethylpyridinium Bis(trifluoromethylsulfonyl)imide (z = 2, 3, or 4) at T = 313.2 K
• 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
• Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
• Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
• Isobaric Thermal Expansivities of Toluene Measured by Scanning Transitiometry at Temperatures from (243 to 423) K and Pressures up to 200 MPa
• Solubility of Benzoic Acid in Pure Solvents and Binary Mixtures
• Measuring the Aqueous Henry's Law Constant at Elevated Temperatures Using an Extended EPICS Technique
• Vapor-Liquid Equilibria in Ternary Systems of Toluene or Octane + Phenols + Water
• Liquid-Liquid Equilibria Measurement of Systems Involving Alkanes (Heptane and Dodecane), Aromatics (Benzene or Toluene), and Furfural
• Liquid-Liquid Equilibrium in Ternary Systems Containing Ethylene Glycol, Monofunctional Benzene Derivative, and Ethyl Acetate
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Solubilities of Phenylphosphinic Acid, Methylphenylphosphinic Acid, Hexachlorocyclotriphosphazene, and Hexaphenoxycyclotriphosphazene in Selected Solvents
• Liquid-Liquid Extraction of Toluene from Heptane Using 1-Alkyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide Ionic Liquids
• Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
• Solubilities of N-[(4-Bromo-3,5-difluorine)-phenyl]maleimide in Different Organic Solvents
• Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
• Influence of Anion Structure on the Liquid-Liquid Equilibria of 1-Ethyl-3-methyl-imidazolium Cation Based Ionic Liquid-Hydrocarbon Binary Systems
• Ternary Liquid-Liquid Equilibria for the (Methanol + Methylbenzene + Decane) System at Different Temperatures
• Solubilities of 3-Carboxy-3-hydroxypentanedioic Acid in Ethanol, Butan-1-ol, Water, Acetone, and Methylbenzene
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Butyl-3-methylimidazolium Nitrate Using Gas-Liquid Chromatography
• Solubilities of 1-Hexyl-3-methylimidazole Nitrate and 1-Octyl-3-methylimidazole Nitrate in Selected Solvents
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Experimental Determination of Quaternary and Ternary Isobaric Vapor Liquid Liquid Equilibrium and Vapor Liquid Equilibrium for the Systems Water Ethanol Hexane Toluene and Water Hexane Toluene at 101.3 kPa
• Solubilities of Tris(o-phenylenedioxy)cyclotriphosphazene in Selected Solvents
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Ethyl-3-methylimidazolium Diethylphosphate Using Gas Liquid Chromatography
• Sulfonate-Based Ionic Liquids in the Liquid Liquid Extraction of Aromatic Hydrocarbons
• 1-Alkyl-2,3-dimethylimidazolium Bis(trifluoromethylsulfonyl)imide Ionic Liquids for the Liquid Liquid Extraction of Toluene from Heptane
• Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
• Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
• Isobaric Vapor Liquid Equilibrium for Binary Systems of Toluene + Acrylic Acid, Toluene + Acetic Acid, and Cyclohexane + Acrylic Acid at 20 kPa
• Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
• Vapor-Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K
• Compressed Liquid Viscosity of 1,1,1,3,3-Pentafluoropropane (R245fa) and 1,1,1,3,3,3-Hexafluoropropane (R236fa)
• Isobaric Vapor-Liquid Equilibrium for Binary Systems of Toluene + Ethanol, Toluene + Isopropanol at (101.3, 121.3, 161.3 and 201.3) kPa
• Excess Molar Volumes of 2,4,6,8-Tetramethylcyclotetrasiloxane with Benzene, Toluene, and Xylene at T = (288.15, 298.15, and 308.15) K
• Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
• Evaluation of the Performance of Four Solvents for the Liquid Liquid Extraction of Acrylic Acid from Water
• Solid Liquid Phase Equilibrium and Solubility of Dibenzo[b,d]furan and 9H-Fluoren-9-one in Organic Solvents
• Vapor Liquid Equilibria of Binary Mixtures Containing 2-Butanol and Hydrocarbons at 313.15 K
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Dibutylphosphate Using Gas Liquid Chromatography
• Determination of Gas Concentrations in Liquids by Nuclear Magnetic Resonance: Hydrogen in Organic Solvents
• Solubility of 6-Chloropyridazin-3-amine in Different Solvents
• Crystal Structures, Reaction Rates, and Selected Physical Properties of Halo-Boronsubphthalocyanines (Halo = Fluoride, Chloride, and Bromide)
• Biomass-Derived Platform Chemicals: Thermodynamic Studies on the Extraction of 5-Hydroxymethylfurfural from Ionic Liquids
• Ternary and Quaternary Liquid Liquid Equilibria for Systems of Water + Methanol + Methylanthranilate + Toluene at Different Temperatures
• Measurements and Correlations of Liquid.Liquid Equilibria for Water + Ethanol + 1,1'-Oxybis(butane) + Methylbenzene or Heptane Mixtures at 298.15 K
• 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
• Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
• Determination and Correlation of Solubility Data and Dissolution Thermodynamic Data of l-Lactide in Different Pure Solvents
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Liquid - Liquid Equilibria for the Ternary Systems of Per fl uorohexane + Methyl Nona fl uorobutyl Ether + Toluene, + 1,4-Dioxane, or + Dimethylformamide at 298.15 K
• Solubilities of 4,4'-Dichlorodiphenyl Disulfide in Six Organic Solvents between (303.15 and 333.15) K
• A Novel Vibrating-Wire Viscometer for High-Viscosity Liquids at Moderate Pressures
• Liquid Liquid Equilibrium Data for {Heptane + Aromatic + 1-(2-Hydroxyethyl)-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide ([hemim][NTf2])} Ternary Systems
• A Promising Ionic Liquid [BMIM][FeCl4] for the Extractive Separation of Aromatic and Aliphatic Hydrocarbons
• Solubilities of 4-Amino-4?-nitrodiphenyl Sulfide in Six Organic Solvents from 287.45 K to 365.55 K
• Determination of the relative permittivity, a, and Conductance, G, of methylbenzene at temperatures between (303 and 393) K and pressures below 60 MPa with a concentric cylinder capacitor at a frequency of 1 kHz
• Thermodynamics of Mixtures Containing Amines. XII. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for N-Methylaniline + Hydrocarbon Systems
• Measurements of the Speed of Sound in Liquid Toluene
• Excess Enthalpy and Excess Volume for Pyridine + Methyldiethanolamine and Pyridine + Ethanolamine Mixtures
• 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
• Solubility Measurement and Modeling for 2-Benzoyl-3-chlorobenzoic Acid and 1-Chloroanthraquinone in Organic Solvents
• Solubility of Benzyl Disulfide in Five Organic Solvents between (283.45 and 333.15) K
• Solubilities of Phosphonic Acid, P,P'-(1,4-Piperazinediyl)bis-,P,P,P',P'-tetraphenyl Ester in Selected Solvents
• Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
• Liquid Liquid Equilibria for the Ternary Systems of Perfluamine + Hydrofluoroether + Benzene, Toluene, or Xylene at 298.15 K or 313.15 K
• Measurement and Correlation of Solubilities of Indole-2-carboxylic Acid in Ten Different Pure Solvents from (278.15 to 360.15) K
• Solubility of 1-Fluoro-4-(methylsulfonyl)benzene in Five Pure Organic Solvents at Temperatures from (288.40 to 331.50) K
• Solid Liquid Phase Equilibria of N,N'-[1,3-Phenylenebis(methylene)]bis(phosphoramidic acid) P,P,P',P'-Tetraphenyl Ester in 10 Pure Solvents
• Experimental Measurements and Modeling of the Solubility of Aceclofenac in Six Pure Solvents from (293.35 to 338.25) K
• 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
• Liquid Liquid Equilibria for the Ternary System Water + Benzyl Alcohol + Methylbenzene at (303.2 to 343.2) K
• Experimental and Modeling of the Propene Solubility in the Heptane and Methylbenzene Solvents
• Solubility and Thermodynamic Functions of Isatin in Pure Solvents
• Thermodynamic Properties of Ternary Liquid Mixtures Containing o-Chlorotoluene: Excess Molar Volumes and Excess Isentropic Compressibilities
• Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
• Liquid Liquid Equilibria for Quaternary Systems of Water + Ethanol + Diethyl Carbonate + Methylbenzene or Heptane
• Solubilities of Benzoic Acid in Binary Methylbenzene + Benzyl Alcohol and Methylbenzene + Benzaldehyde Solvent Mixtures
• Experimental Study: The Impact of Dissolved Water on the Viscosity of Reservoir Fluids at HPHT Conditions
• Measuring and Modeling the Solubility and Density for CO2 Toluene and C2H6 Toluene Systems
• Selective Separation of Aromatics from Paraffins and Cycloalkanes Using Morpholinium-Based Ionic Liquid
• Determination and Correlation of Solubilities of 2-Isopropylthioxanthone (ITX) in Seven Different Solvents from (299.15 to 329.85) K
• Solid Liquid Phase Equilibrium of Phosphoramidic acid, N,N'-1,2-Ethanediylbis-P,P,P',P'-tetraphenyl Ester in Selected Solvents
• Experimental Study of Solubility of Water in Liquid Organic Hydrogen Carriers
• Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
• Measurement and Correlation of the Solubility for 4,4'-Diaminodiphenylmethane in Different Solvents
• Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
• Dialkylphosphate-Based Ionic Liquids as Solvents to Extract Toluene from Heptane
• Measurement and Correlation of Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Alkane and Cycloalkane Solvents
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Surface Tension of the Ternary System Water + Acetone + Toluene
• Experimental Isobaric Vapor-Liquid Equilibria of Binary Mixtures of 2,2,2-Trifluoroethanol with Benzene or Toluene
• Measurement and Correlation of Liquid-Liquid Equilibria of Methylcyclohexane + Toluene + N-Formylmorpholine at (293, 303, 313, and 323) K
• Measurement of Activity Coefficient at Infinite Dilution of Hydrocarbons in Sulfolane Using Gas-Liquid Chromatography
• Isothermal Phase Equilibria and Excess Molar Enthalpies for Binary Systems with Dimethyl Ether at 323.15 K
• Solubility of Fluorene in Different Solvents from 278.98 K to 338.35 K
• Isothermal Vapor-Liquid Equilibrium Data for the System Methanol + Toluene + Triphenylbenzylphosphonium Chloride
• Solubility of 2,6-Diaminopyridine in Toluene, o-Xylene, Ethylbenzene, Methanol, Ethanol, 2-Propanol, and Sodium Hydroxide Solutions
• Excess Enthalpies of Chloroalkylbenzene + Alkylbenzene Mixtures
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• Liquid-Liquid Equilibrium for the Quaternary System Water + Tetrahydrofuran + Toluene + 1-Butanol Mixture at 25 deg C and Atmospheric Pressure
• Molar Excess Volume of sec- and tert-Butyl Chloride with Aromatic Hydrocarbons at T = 298.15 K
• Solubilities of the Gaseous and Liquid Solutes and Their Thermodynamics of Solubilization in the Novel Room-Temperature Ionic Liquids at Infinite Dilution by Gas Chromatography
• Measurement and Prediction of Oxygen Solubility in Toluene at Temperatures from 298.45 K to 393.15 K and Pressures up to 1.0 MPa
• Solubility of Acenaphthylene in Different Solvents between (278 and 323) K
• Solubilities of Vitamin K3 in Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene between (299.44 and 344.24) K
• Excess Enthalpies of (N-Methylformamide or N-Methylacetamide) + Aromatic Compounds at 303.15 K
• Henry s Law Constants for Fragrance and Organic Solvent Compounds in Aqueous Industrial Surfactants
• Mutual Solubility Measurements of Hydrocarbon-Water Systems Containing Benzene, Toluene, and 3-Methylpentane
• Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
• Vapor Liquid Equilibrium of N-Formylmorpholine with Toluene and Xylene at 101.33 kPa
• Measuring Surface Tension of Liquids at High Temperature and Elevated Pressure
• Phase Equilibria of (1-Ethyl-3-methylimidazolium Ethylsulfate + Hydrocarbon, + Ketone, and + Ether) Binary Systems
• Influence of the Temperature on the Liquid Liquid Equilibria of Heptane + Toluene + Sulfolane and Heptane + m-Xylene + Sulfolane
• Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
• Determination of the Relative Permittivity, E , of Methylbenzene at Temperatures between (290 and 406) K and Pressures below 20 MPa with a Radio Frequency Re-Entrant Cavity and Evaluation of a MEMS Capacitor for the Measurement of E
• Liquid-Liquid Equilibrium of Ternary Systems of Cyclohexane + (Benzene, + Toluene, + Ethylbenzene, or + o-Xylene) + 4-Methyl-N-butyl Pyridinium Tetrafluoroborate Ionic Liquid at 303.15 K
• Density and Viscosity Measurements of Diethyl Adipate from (303 to 373) K and up to 20 MPa
• Measurements and Correlation of Liquid Liquid Equilibria of (Water + Ethanol + Dimethyl Carbonate + 2,2,4-Trimethylpentane or n-Heptane) and (Water + Dimethyl Carbonate + n-Heptane + Toluene)
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Hexyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• Solubilities of Diphenylphosphinic Acid in Selected Solvents
• Liquid-Liquid Equilibria for [C8mim][NTf2] + Thiophene + 2,2,4-Trimethylpentane or + Toluene
• Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
• Molar Excess Volumes and Excess Isentropic Compressibilities of Ternary Mixtures of o-Toluidine
• Vapor-Liquid Equilibrium Data for the System Methanol + Toluene + Tetrabutylammonium Tetraphenylborate
• Vapor-Liquid Equilibria of Binary Systems Comprising 1-Chloro-2-ethylhexane and 2-Ethyl-1-hexanol
• Diffusion of Benzonitrile in CO2-Expanded Ethanol
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Measurement of Infinite Dilution Activity Coefficients of Alcohols, Ketones, and Aromatic Hydrocarbons in 4-Methyl-N-butylpyridinium Tetrafluoroborate and 1-Butyl-3-methylimidazolium Hexafluorophosphate by Gas-Liquid Chromatography
• Thermo Physical Properties of 4-Hydroxy 4-Methyl Pentanone with Nitrobenzene or Ethyl Benzene at Temperatures of (303.15, 313.15, and 323.15) K and a Pressure of 0.1 MPa
• Solubility of Diamantane, Trimantane, Tetramantane, and Their Derivatives in Organic Solvents
• Solubilities of 1,4-Naphthoquinone in Acetone, Toluene, Xylene, Ethanol, and n-Butyl Alcohol
• Solubility of Artemisinin in Seven Different Pure Solvents from (283.15 to 323.15) K
• Solubility of Bis(benzoxazolyl-2-methyl) Sulfide in Different Pure Solvents and Ethanol + Water Binary Mixtures between (273.25 and 325.25) K
• Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
• Measurement and Correlation for Solubilities of Naphthalene in Acetone, Toluene, Xylene, Ethanol, Heptane, and 1-Butanol
• Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water)
• Viscosities of p-Xylene, Acetic Acid, and p-Xylene + Acetic Acid at (313.15 to 473.15) K and (0.10 to 3.20) MPa: Determined by the Rolling-Ball Method
• Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
• Vapor-Liquid Equilibria of Water + Triethylene Glycol (TEG) and Water + TEG + Toluene at 85 kPa
• Solubility of Fluorene in Benzene, Chloroform, Acetone, 1-Propanol, Isobutanol, and Methylbenzene from (283 to 323) K
• Thermophysical Characterization of Liquids Using Precise Density and Isobaric Heat Capacity Measurements As a Function of Pressure
• Solubility of Adipic Acid in Acetone, Chloroform, and Toluene
• Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
• Solubility of Canthaxanthin in Pure Solvents from (293.15 to 343.15) K
• Solubilities of Triphenylphosphine Oxide in Selected Solvents
• Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
• Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
• Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes and Aromatic Compounds at T = 313.15 K
• Density and Viscosity of Decalin, Cyclohexane, and Toluene Binary Mixtures at (283.15, 293.15, 303.15, 313.15, and 323.15) K
• Binary and Ternary Vapor-Liquid Equilibrium at 323.15 K and Excess Molar Volumes at 298.15 K for the Mixtures of Propyl Vinyl Ether + 1-Propanol + Toluene
• Determination of the Density of Toluene in the Range from (293 to 373) K and from (0.1 to 30) MPa
• Densities and Viscosities of Binary Mixtures of Methyl 4-Chlorobutyrate with Aromatic Hydrocarbons at T ) (298.15 to 318.15) K
• Solubility of Elemental Sulfur in Toluene between (267.15 and 313.15) K under Atmospheric Pressure
• Molar Excess Volumes and Excess Isentropic Compressibilities of {2-Methylaniline (i) + Benzene (j) + Methylbenzene}, {2-Methylaniline (i) + Benzene (j) + 1,2-Dimethylbenzene (k)}, and {2-Methylaniline (i) + Benzene (j) + 1,4-Dimethylbenzene (k)} at T = 308.15 K
• Dynamic Viscosity of the Binary System 1-Propanol + Toluene as a Function of Temperature and Pressure
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Solubilities of Methyldiphenylphosphine Oxide in Selected Solvents
• Measurement and Correlation of Bubble Point Pressure in (CO2 + C6H6), (CO2 + CH3C6H5), (CO2 + C6H14), and (CO2 + C7H16) at Temperatures from (293.15 to 313.15) K
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Solubility of Penicillin Sulfoxide in Different Solvents
• Solubilities of 3-Pentadecylphenol in Ethanol, 1-Butanol, Toluene, Acetone, Tetrachloromethane, and Ethyl Acetate
• Pure Component and Binary Vapor-Liquid Equilibrium + Modeling for Hexafluoropropylene and Hexafluoropropylene Oxide with Toluene and Hexafluoroethane
• Liquid-Liquid Equilibria for the Three Ternary Systems (3-Methyl-N-butylpyridinium Dicyanamide + Toluene + Heptane), (1-Butyl-3-methylimidazolium Dicyanamide + Toluene + Heptane) and (1-Butyl-3-methylimidazolium Thiocyanate + Toluene + Heptane) at T = (313.15 and 348.15) K and p = 0.1 MPa
• Comparison of the Efficiencies of Amine Extractants on Lactic Acid with Different Organic Solvents
• Phase Equilibria of (1-Hexyl-3-methylimidazolium Thiocyanate + Water, Alcohol, or Hydrocarbon) Binary Systems
• Density, Speed of Sound, and Refractive Index of the Binary Systems Cyclohexane (1) or Methylcyclohexane (1) or Cyclo-octane (1) with Benzene (2), Toluene (2), and Ethylbenzene (2) at Two Temperatures
• Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
• Liquid-Liquid Equilibrium for Ternary Mixtures of Hexane + Aromatic Compounds + [EMpy][ESO4] at T = 298.15 K
• Phase Equilibria for Liquid Mixtures of (an Alkane + Toluene + Dimethyl Phthalate)
• Solubilities of N-[(4-Bromo-3,5-difluorine)phenyl]acrylamide in Benzene, Methanol, Pyridine, Ethanol, Acetonitrile, and Toluene at Temperatures between (284.65 and 348.95) K
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
• Solubilities of (2,5-Dihydroxyphenyl)diphenyl Phosphine Oxide in Selected Solvents
• Effect of the Chain Length on the Aromatic Ring in the Separation of Aromatic Compounds from Methylcyclohexane Using the Ionic Liquid 1-Ethyl-3-methylpyridinium Ethylsulfate
• 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
• Solubility of Triadimefon in Organic Solvents at Temperatures between (288.15 and 333.15) K
• Liquid-Liquid Equilibria for the Ternary Systems {Heptane + Toluene + N-Butylpyridinium Tetrafluoroborate or N-Hexylpyridinium Tetrafluoroborate} at T = 313.2 K
• Mutual Solubility of Pyridinium-Based Tetrafluoroborates and Toluene
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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