Chemical Properties of Benzene (CAS 71-43-2)

InChI

InChI=1S/C6H6/c1-2-4-6-5-3-1/h1-6H

InChI Key

UHOVQNZJYSORNB-UHFFFAOYSA-N

Formula

C6H6

SMILES

c1ccccc1

Molecular Weight¹

78.11

CAS

71-43-2

Other Names

• 1,3,5-Cyclohexatriene
• Benzeen
• Benzen
• Benzin
• Benzine
• Benzol
• Benzole
• Benzolene
• Benzolo
• Bicarburet of hydrogen
• Carbon oil
• Coal naphtha
• Cyclohexatriene
• Fenzen
• Mineral naphtha
• Motor benzol
• NCI-C55276
• NSC 67315
• Phene
• Phenyl hydride
• Pyrobenzol
• Pyrobenzole
• Rcra waste number U019
• UN 1114
• [6]Annulene

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• C_p,solid : Solid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• 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_subH : Enthalpy of sublimation at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_sub : Sublimation 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 : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• S°_{solid,1 bar} : Solid phase molar entropy at standard conditions (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_boil : Boiling point at given pressure (K).
• T_c : Critical Temperature (K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_fus : Melting point (K).
• V_c : Critical Volume (m³/kmol).
• v_spec : Specific Volume (m³/kg).
• 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	0.2120		KDB
PAff	[746.40; 750.40]	kJ/mol
PAff	750.40	kJ/mol	NIST
PAff	746.40	kJ/mol	NIST
Tig	864.82	K	KDB
BasG	[721.70; 725.40]	kJ/mol
BasG	725.40	kJ/mol	NIST
BasG	721.70	kJ/mol	NIST
μ	0.00	debye	KDB
η	[0.0006040; 0.0006080]	Pa×s
η	0.0006080	Pa×s	Densiti...
η	0.0006040	Pa×s	Densiti...
LFL	1.30	% in Air	KDB
UFL	7.90	% in Air	KDB
Tflash,oc	262.04	K	KDB
ΔfG°	129.70	kJ/mol	KDB
Rg	3.0040		KDB
Δc,grossH	3267.62	kJ/mol	KDB
Δc,netH	3135.573	kJ/mol	KDB
ΔfH°gas	[79.90; 82.98]	kJ/mol
ΔfH°gas	82.98	kJ/mol	KDB
ΔfH°gas	82.90 ± 0.90	kJ/mol	NIST
ΔfH°gas	82.80	kJ/mol	NIST
ΔfH°gas	82.93 ± 0.50	kJ/mol	NIST
ΔfH°gas	79.90	kJ/mol	NIST
ΔfH°liquid	[46.00; 49.04]	kJ/mol
ΔfH°liquid	49.00 ± 0.90	kJ/mol	NIST
ΔfH°liquid	48.95 ± 0.54	kJ/mol	NIST
ΔfH°liquid	49.04 ± 0.50	kJ/mol	NIST
ΔfH°liquid	46.00	kJ/mol	NIST
ΔfusH°	5.73	kJ/mol	Joback Calculated Property
ΔsubH°	44.40	kJ/mol	NIST
ΔvapH°	30.56	kJ/mol	Joback Calculated Property
IE	[9.20; 9.80]	eV
IE	9.24 ± 0.00	eV	NIST
IE	9.24 ± 0.00	eV	NIST
IE	9.24 ± 0.00	eV	NIST
IE	9.20	eV	NIST
IE	9.25 ± 0.00	eV	NIST
IE	9.23 ± 0.03	eV	NIST
IE	9.25	eV	NIST
IE	9.23	eV	NIST
IE	9.25	eV	NIST
IE	9.24 ± 0.00	eV	NIST
IE	9.44	eV	NIST
IE	9.25	eV	NIST
IE	9.22	eV	NIST
IE	9.24	eV	NIST
IE	9.25 ± 0.02	eV	NIST
IE	9.25 ± 0.07	eV	NIST
IE	9.24	eV	NIST
IE	Outlier 9.70	eV	NIST
IE	9.25	eV	NIST
IE	9.20 ± 0.10	eV	NIST
IE	9.26 ± 0.06	eV	NIST
IE	9.27	eV	NIST
IE	9.24 ± 0.01	eV	NIST
IE	9.25 ± 0.01	eV	NIST
IE	9.36 ± 0.05	eV	NIST
IE	9.24 ± 0.00	eV	NIST
IE	9.24	eV	NIST
IE	9.24 ± 0.01	eV	NIST
IE	9.25 ± 0.01	eV	NIST
IE	9.20 ± 0.04	eV	NIST
IE	9.24	eV	NIST
IE	9.25	eV	NIST
IE	9.25 ± 0.02	eV	NIST
IE	9.26 ± 0.02	eV	NIST
IE	9.25 ± 0.01	eV	NIST
IE	9.24 ± 0.01	eV	NIST
IE	9.24 ± 0.01	eV	NIST
IE	9.25	eV	NIST
IE	9.20	eV	NIST
IE	9.25	eV	NIST
IE	9.25 ± 0.00	eV	NIST
IE	9.25 ± 0.01	eV	NIST
IE	Outlier 9.80 ± 0.10	eV	NIST
IE	9.24 ± 0.01	eV	NIST
IE	9.23	eV	NIST
IE	9.25	eV	NIST
IE	9.25	eV	NIST
IE	9.22	eV	NIST
IE	9.23	eV	NIST
IE	9.30	eV	NIST
IE	9.24 ± 0.02	eV	NIST
IE	9.25 ± 0.05	eV	NIST
IE	9.24	eV	NIST
IE	9.24	eV	NIST
IE	9.23	eV	NIST
IE	9.24	eV	NIST
IE	9.24	eV	NIST
IE	9.25 ± 0.03	eV	NIST
IE	9.24	eV	NIST
IE	9.20	eV	NIST
IE	9.24	eV	NIST
IE	9.24	eV	NIST
log10WS	[-1.64; -1.64]
log10WS	-1.64		Aq. Sol...
log10WS	-1.64		Estimat...
logPoct/wat	1.687		Crippen Calculated Property
McVol	71.640	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	2		KDB
Pc	[4852.27; 6120.00]	kPa
Pc	4895.00	kPa	KDB
Pc	4895.00 ± 6.00	kPa	NIST
Pc	4884.00 ± 20.00	kPa	NIST
Pc	4900.00 ± 10.00	kPa	NIST
Pc	4894.00 ± 10.00	kPa	NIST
Pc	4875.75 ± 30.00	kPa	NIST
Pc	4898.00 ± 2.00	kPa	NIST
Pc	4897.00 ± 10.00	kPa	NIST
Pc	4887.00 ± 3.00	kPa	NIST
Pc	4889.00 ± 3.00	kPa	NIST
Pc	4900.00 ± 50.66	kPa	NIST
Pc	4885.89 ± 5.06	kPa	NIST
Pc	4885.89 ± 4.05	kPa	NIST
Pc	4898.00 ± 5.00	kPa	NIST
Pc	4896.00 ± 10.34	kPa	NIST
Pc	4900.00 ± 10.13	kPa	NIST
Pc	4892.00 ± 8.10	kPa	NIST
Pc	4936.65 ± 55.15	kPa	NIST
Pc	4853.47 ± 50.66	kPa	NIST
Pc	4898.00 ± 10.13	kPa	NIST
Pc	4875.00 ± 27.58	kPa	NIST
Pc	4930.90 ± 40.00	kPa	NIST
Pc	4852.30 ± 53.33	kPa	NIST
Pc	5020.00 ± 101.33	kPa	NIST
Pc	4910.00 ± 4.90	kPa	NIST
Pc	4852.27 ± 39.99	kPa	NIST
Pc	Outlier 6120.00 ± 709.28	kPa	NIST
ρc	[274.95; 316.35]	kg/m3
ρc	304.64 ± 0.47	kg/m3	NIST
ρc	303.78 ± 3.91	kg/m3	NIST
ρc	302.29 ± 6.25	kg/m3	NIST
ρc	300.73 ± 6.25	kg/m3	NIST
ρc	300.73 ± 6.25	kg/m3	NIST
ρc	316.35 ± 4.69	kg/m3	NIST
ρc	306.20 ± 2.34	kg/m3	NIST
ρc	Outlier 274.95 ± 1.48	kg/m3	NIST
ρc	303.85 ± 4.69	kg/m3	NIST
ρc	304.40 ± 3.91	kg/m3	NIST
ρc	296.98 ± 7.81	kg/m3	NIST
ρc	304.48 ± 3.91	kg/m3	NIST
Inp	[629.00; 694.74]
Inp	Outlier 685.00		NIST
Inp	Outlier 694.74		NIST
Inp	672.74		NIST
Inp	674.03		NIST
Inp	651.10		NIST
Inp	648.90		NIST
Inp	657.60		NIST
Inp	650.20		NIST
Inp	646.80		NIST
Inp	645.00		NIST
Inp	652.60		NIST
Inp	638.00		NIST
Inp	678.80		NIST
Inp	Outlier 683.30		NIST
Inp	641.51		NIST
Inp	641.45		NIST
Inp	641.96		NIST
Inp	649.89		NIST
Inp	651.77		NIST
Inp	653.93		NIST
Inp	656.09		NIST
Inp	658.35		NIST
Inp	660.36		NIST
Inp	663.60		NIST
Inp	664.40		NIST
Inp	666.96		NIST
Inp	670.44		NIST
Inp	672.02		NIST
Inp	674.86		NIST
Inp	666.03		NIST
Inp	667.42		NIST
Inp	669.56		NIST
Inp	671.74		NIST
Inp	673.50		NIST
Inp	675.70		NIST
Inp	677.75		NIST
Inp	680.27		NIST
Inp	681.27		NIST
Inp	Outlier 683.59		NIST
Inp	Outlier 685.29		NIST
Inp	Outlier 687.79		NIST
Inp	672.00		NIST
Inp	Outlier 684.60		NIST
Inp	682.50		NIST
Inp	676.00		NIST
Inp	Outlier 686.40		NIST
Inp	670.45		NIST
Inp	636.60		NIST
Inp	639.10		NIST
Inp	641.70		NIST
Inp	644.50		NIST
Inp	646.60		NIST
Inp	650.00		NIST
Inp	652.50		NIST
Inp	677.20		NIST
Inp	654.52		NIST
Inp	662.00		NIST
Inp	675.00		NIST
Inp	663.00		NIST
Inp	663.00		NIST
Inp	668.00		NIST
Inp	654.00		NIST
Inp	644.00		NIST
Inp	677.00		NIST
Inp	663.20		NIST
Inp	667.40		NIST
Inp	654.70		NIST
Inp	660.20		NIST
Inp	649.40		NIST
Inp	656.30		NIST
Inp	643.00		NIST
Inp	678.10		NIST
Inp	Outlier 688.00		NIST
Inp	653.80		NIST
Inp	654.20		NIST
Inp	654.20		NIST
Inp	654.40		NIST
Inp	653.50		NIST
Inp	647.20		NIST
Inp	669.90		NIST
Inp	649.00		NIST
Inp	666.00		NIST
Inp	675.00		NIST
Inp	655.00		NIST
Inp	655.00		NIST
Inp	664.00		NIST
Inp	664.00		NIST
Inp	663.10		NIST
Inp	670.70		NIST
Inp	663.00		NIST
Inp	651.30		NIST
Inp	655.40		NIST
Inp	651.40		NIST
Inp	655.80		NIST
Inp	637.20		NIST
Inp	641.80		NIST
Inp	666.50		NIST
Inp	667.40		NIST
Inp	645.00		NIST
Inp	654.00		NIST
Inp	655.00		NIST
Inp	649.00		NIST
Inp	653.00		NIST
Inp	658.00		NIST
Inp	637.00		NIST
Inp	641.40		NIST
Inp	662.00		NIST
Inp	661.00		NIST
Inp	630.00		NIST
Inp	650.00		NIST
Inp	664.00		NIST
Inp	Outlier 687.00		NIST
Inp	672.00		NIST
Inp	646.00		NIST
Inp	642.00		NIST
Inp	651.00		NIST
Inp	652.10		NIST
Inp	654.10		NIST
Inp	656.00		NIST
Inp	658.30		NIST
Inp	Outlier 687.00		NIST
Inp	681.00		NIST
Inp	655.00		NIST
Inp	681.00		NIST
Inp	668.00		NIST
Inp	675.00		NIST
Inp	669.00		NIST
Inp	662.00		NIST
Inp	664.00		NIST
Inp	662.00		NIST
Inp	664.00		NIST
Inp	670.00		NIST
Inp	647.00		NIST
Inp	653.00		NIST
Inp	652.00		NIST
Inp	675.00		NIST
Inp	647.00		NIST
Inp	649.00		NIST
Inp	651.00		NIST
Inp	653.00		NIST
Inp	656.00		NIST
Inp	658.00		NIST
Inp	671.10		NIST
Inp	673.00		NIST
Inp	675.10		NIST
Inp	677.20		NIST
Inp	679.50		NIST
Inp	681.90		NIST
Inp	650.00		NIST
Inp	647.00		NIST
Inp	653.80		NIST
Inp	654.40		NIST
Inp	657.10		NIST
Inp	Outlier 685.20		NIST
Inp	Outlier 685.60		NIST
Inp	Outlier 686.80		NIST
Inp	Outlier 687.40		NIST
Inp	664.00		NIST
Inp	652.00		NIST
Inp	670.00		NIST
Inp	659.00		NIST
Inp	664.00		NIST
Inp	671.00		NIST
Inp	678.00		NIST
Inp	667.00		NIST
Inp	680.00		NIST
Inp	654.00		NIST
Inp	651.00		NIST
Inp	653.00		NIST
Inp	650.00		NIST
Inp	648.00		NIST
Inp	650.22		NIST
Inp	648.40		NIST
Inp	650.50		NIST
Inp	652.60		NIST
Inp	654.90		NIST
Inp	657.20		NIST
Inp	659.70		NIST
Inp	645.70		NIST
Inp	648.00		NIST
Inp	650.30		NIST
Inp	652.70		NIST
Inp	655.20		NIST
Inp	658.20		NIST
Inp	663.60		NIST
Inp	670.70		NIST
Inp	677.80		NIST
Inp	638.00		NIST
Inp	638.00		NIST
Inp	646.00		NIST
Inp	659.10		NIST
Inp	642.90		NIST
Inp	Outlier 683.00		NIST
Inp	650.00		NIST
Inp	637.40		NIST
Inp	642.20		NIST
Inp	637.20		NIST
Inp	642.50		NIST
Inp	651.00		NIST
Inp	652.00		NIST
Inp	648.00		NIST
Inp	647.80		NIST
Inp	648.00		NIST
Inp	648.70		NIST
Inp	649.00		NIST
Inp	642.50		NIST
Inp	642.90		NIST
Inp	641.10		NIST
Inp	641.40		NIST
Inp	648.00		NIST
Inp	650.20		NIST
Inp	636.80		NIST
Inp	Outlier 684.00		NIST
Inp	650.00		NIST
Inp	645.50		NIST
Inp	646.00		NIST
Inp	659.20		NIST
Inp	639.00		NIST
Inp	642.00		NIST
Inp	644.42		NIST
Inp	648.00		NIST
Inp	647.00		NIST
Inp	650.00		NIST
Inp	674.00		NIST
Inp	636.00		NIST
Inp	644.00		NIST
Inp	637.00		NIST
Inp	642.00		NIST
Inp	654.80		NIST
Inp	654.80		NIST
Inp	654.80		NIST
Inp	654.70		NIST
Inp	654.70		NIST
Inp	654.80		NIST
Inp	650.40		NIST
Inp	638.00		NIST
Inp	652.00		NIST
Inp	654.00		NIST
Inp	654.00		NIST
Inp	656.00		NIST
Inp	660.70		NIST
Inp	649.00		NIST
Inp	644.00		NIST
Inp	652.00		NIST
Inp	655.00		NIST
Inp	657.00		NIST
Inp	660.00		NIST
Inp	662.00		NIST
Inp	640.00		NIST
Inp	639.70		NIST
Inp	656.00		NIST
Inp	648.00		NIST
Inp	637.00		NIST
Inp	Outlier 685.00		NIST
Inp	648.50		NIST
Inp	653.60		NIST
Inp	646.60		NIST
Inp	681.00		NIST
Inp	634.00		NIST
Inp	640.00		NIST
Inp	645.00		NIST
Inp	649.00		NIST
Inp	680.00		NIST
Inp	Outlier 686.00		NIST
Inp	Outlier 694.00		NIST
Inp	681.00		NIST
Inp	650.00		NIST
Inp	655.00		NIST
Inp	660.00		NIST
Inp	645.00		NIST
Inp	631.00		NIST
Inp	632.00		NIST
Inp	634.00		NIST
Inp	643.00		NIST
Inp	645.00		NIST
Inp	Outlier 691.00		NIST
Inp	662.00		NIST
Inp	650.00		NIST
Inp	642.00		NIST
Inp	665.00		NIST
Inp	647.00		NIST
Inp	667.00		NIST
Inp	664.00		NIST
Inp	Outlier 629.00		NIST
Inp	649.70		NIST
Inp	649.00		NIST
Inp	681.30		NIST
Inp	661.60		NIST
Inp	652.00		NIST
Inp	650.00		NIST
Inp	663.00		NIST
Inp	654.00		NIST
Inp	662.00		NIST
Inp	663.00		NIST
Inp	647.50		NIST
Inp	648.00		NIST
Inp	638.32		NIST
Inp	638.98		NIST
Inp	654.80		NIST
Inp	653.80		NIST
Inp	654.20		NIST
Inp	654.80		NIST
Inp	656.10		NIST
Inp	660.60		NIST
Inp	648.00		NIST
Inp	645.00		NIST
Inp	658.00		NIST
Inp	639.00		NIST
Inp	664.00		NIST
Inp	654.10		NIST
Inp	638.60		NIST
Inp	640.70		NIST
Inp	645.00		NIST
Inp	645.00		NIST
Inp	646.00		NIST
Inp	643.10		NIST
Inp	640.50		NIST
Inp	660.10		NIST
Inp	654.20		NIST
Inp	654.80		NIST
Inp	656.10		NIST
Inp	654.80		NIST
Inp	653.80		NIST
Inp	641.77		NIST
Inp	641.83		NIST
Inp	630.00		NIST
Inp	644.00		NIST
Inp	654.00		NIST
Inp	641.72		NIST
Inp	642.00		NIST
Inp	642.00		NIST
Inp	654.00		NIST
Inp	651.40		NIST
Inp	648.90		NIST
Inp	648.00		NIST
Inp	640.61		NIST
Inp	643.07		NIST
Inp	644.46		NIST
Inp	655.57		NIST
Inp	658.13		NIST
Inp	659.63		NIST
Inp	654.00		NIST
Inp	645.26		NIST
Inp	642.70		NIST
Inp	646.00		NIST
Inp	647.11		NIST
Inp	642.00		NIST
Inp	650.00		NIST
Inp	648.00		NIST
Inp	659.00		NIST
Inp	630.00		NIST
Inp	640.20		NIST
Inp	654.00		NIST
Inp	654.00		NIST
Inp	663.00		NIST
Inp	657.00		NIST
Inp	660.00		NIST
Inp	667.00		NIST
Inp	668.00		NIST
Inp	668.00		NIST
Inp	662.00		NIST
Inp	668.00		NIST
Inp	672.00		NIST
Inp	658.00		NIST
Inp	668.00		NIST
Inp	668.00		NIST
Inp	668.00		NIST
Inp	678.00		NIST
Inp	654.00		NIST
Inp	663.00		NIST
Inp	664.00		NIST
Inp	670.00		NIST
Inp	670.00		NIST
Inp	656.00		NIST
Inp	657.00		NIST
Inp	658.00		NIST
Inp	659.00		NIST
Inp	654.00		NIST
Inp	655.00		NIST
Inp	655.00		NIST
Inp	638.00		NIST
Inp	651.00		NIST
Inp	655.00		NIST
Inp	670.00		NIST
Inp	652.00		NIST
Inp	638.00		NIST
Inp	650.00		NIST
Inp	682.00		NIST
Inp	635.00		NIST
Inp	658.00		NIST
Inp	655.00		NIST
Inp	654.00		NIST
Inp	660.00		NIST
Inp	648.00		NIST
Inp	653.00		NIST
Inp	643.00		NIST
Inp	653.00		NIST
Inp	657.00		NIST
Inp	637.00		NIST
Inp	661.00		NIST
Inp	657.00		NIST
Inp	646.00		NIST
Inp	656.00		NIST
Inp	653.00		NIST
Inp	661.00		NIST
Inp	652.00		NIST
Inp	645.30		NIST
Inp	638.83		NIST
Inp	667.00		NIST
Inp	649.00		NIST
Inp	648.00		NIST
Inp	661.00		NIST
Inp	671.30		NIST
Inp	649.00		NIST
Inp	638.00		NIST
Inp	640.00		NIST
Inp	640.00		NIST
Inp	653.00		NIST
Inp	644.00		NIST
Inp	647.00		NIST
Inp	640.00		NIST
Inp	642.00		NIST
Inp	643.00		NIST
Inp	640.50		NIST
Inp	644.00		NIST
Inp	641.00		NIST
Inp	642.00		NIST
Inp	641.00		NIST
Inp	663.00		NIST
Inp	648.00		NIST
Inp	652.00		NIST
Inp	657.00		NIST
Inp	642.00		NIST
Inp	642.00		NIST
Inp	655.00		NIST
Inp	661.00		NIST
Inp	670.00		NIST
Inp	651.00		NIST
Inp	Outlier 686.00		NIST
Inp	662.00		NIST
Inp	639.25		NIST
Inp	663.00		NIST
Inp	671.00		NIST
Inp	664.00		NIST
Inp	654.00		NIST
Inp	649.00		NIST
Inp	657.00		NIST
Inp	655.00		NIST
Inp	654.00		NIST
Inp	657.00		NIST
Inp	664.00		NIST
Inp	657.00		NIST
Inp	674.00		NIST
Inp	643.00		NIST
Inp	640.00		NIST
Inp	651.00		NIST
Inp	640.00		NIST
Inp	658.00		NIST
Inp	665.00		NIST
Inp	660.00		NIST
Inp	648.60		NIST
Inp	658.00		NIST
Inp	663.50		NIST
Inp	664.60		NIST
Inp	644.00		NIST
Inp	644.00		NIST
Inp	650.40		NIST
Inp	663.00		NIST
Inp	634.00		NIST
Inp	644.00		NIST
Inp	665.00		NIST
Inp	666.00		NIST
Inp	669.00		NIST
Inp	653.00		NIST
Inp	673.00		NIST
Inp	660.00		NIST
Inp	644.00		NIST
Inp	665.00		NIST
Inp	645.00		NIST
Inp	665.00		NIST
Inp	645.00		NIST
Inp	663.00		NIST
Inp	668.00		NIST
Inp	657.00		NIST
Inp	655.00		NIST
Inp	652.00		NIST
Inp	658.00		NIST
Inp	670.00		NIST
Inp	640.00		NIST
Inp	650.40		NIST
Inp	666.00		NIST
Inp	644.00		NIST
Inp	Outlier 685.00		NIST
Inp	648.90		NIST
Inp	652.60		NIST
Inp	641.45		NIST
Inp	656.09		NIST
Inp	666.96		NIST
Inp	667.42		NIST
Inp	677.75		NIST
Inp	Outlier 687.79		NIST
Inp	Outlier 686.40		NIST
Inp	644.50		NIST
Inp	654.52		NIST
Inp	667.40		NIST
Inp	643.00		NIST
Inp	654.20		NIST
Inp	649.00		NIST
Inp	664.00		NIST
Inp	651.30		NIST
Inp	641.80		NIST
Inp	641.40		NIST
Inp	651.00		NIST
Inp	Outlier 687.00		NIST
Inp	675.00		NIST
Inp	656.00		NIST
Inp	677.20		NIST
Inp	653.80		NIST
Inp	Outlier 686.80		NIST
Inp	659.00		NIST
Inp	680.00		NIST
Inp	648.00		NIST
Inp	654.90		NIST
Inp	650.30		NIST
Inp	670.70		NIST
Inp	659.10		NIST
Inp	642.20		NIST
Inp	642.50		NIST
Inp	650.20		NIST
Inp	646.00		NIST
Inp	654.80		NIST
Inp	638.00		NIST
Inp	660.70		NIST
Inp	653.60		NIST
Inp	645.00		NIST
Inp	681.00		NIST
Inp	631.00		NIST
Inp	Outlier 691.00		NIST
I	[924.00; 1007.64]
I	979.00		NIST
I	979.40		NIST
I	988.60		NIST
I	Outlier 999.50		NIST
I	947.77		NIST
I	953.66		NIST
I	963.67		NIST
I	971.57		NIST
I	980.53		NIST
I	989.54		NIST
I	998.62		NIST
I	Outlier 1007.64		NIST
I	970.00		NIST
I	971.00		NIST
I	925.00		NIST
I	955.50		NIST
I	945.20		NIST
I	958.20		NIST
I	959.50		NIST
I	964.00		NIST
I	992.00		NIST
I	952.00		NIST
I	971.00		NIST
I	968.66		NIST
I	972.80		NIST
I	976.91		NIST
I	957.21		NIST
I	960.69		NIST
I	964.88		NIST
I	979.00		NIST
I	954.50		NIST
I	965.70		NIST
I	973.30		NIST
I	979.30		NIST
I	982.60		NIST
I	969.70		NIST
I	974.20		NIST
I	978.80		NIST
I	983.40		NIST
I	992.60		NIST
I	959.00		NIST
I	955.00		NIST
I	967.00		NIST
I	972.60		NIST
I	973.40		NIST
I	985.70		NIST
I	947.20		NIST
I	933.40		NIST
I	987.00		NIST
I	978.00		NIST
I	Outlier 1005.00		NIST
I	991.00		NIST
I	Outlier 1000.00		NIST
I	970.00		NIST
I	985.00		NIST
I	974.00		NIST
I	981.00		NIST
I	987.00		NIST
I	967.00		NIST
I	924.00		NIST
I	947.00		NIST
I	953.00		NIST
I	967.70		NIST
I	936.00		NIST
I	940.00		NIST
I	954.00		NIST
I	942.00		NIST
I	943.00		NIST
I	947.00		NIST
I	939.00		NIST
I	938.00		NIST
I	940.00		NIST
I	947.00		NIST
I	938.00		NIST
I	926.00		NIST
I	965.00		NIST
I	936.00		NIST
I	938.00		NIST
I	938.00		NIST
I	938.00		NIST
I	930.00		NIST
I	975.00		NIST
I	982.00		NIST
I	994.00		NIST
I	956.00		NIST
I	965.00		NIST
I	959.00		NIST
I	960.00		NIST
I	965.00		NIST
I	947.00		NIST
I	952.00		NIST
I	933.00		NIST
I	957.00		NIST
I	937.00		NIST
I	955.00		NIST
I	957.00		NIST
I	983.00		NIST
I	934.00		NIST
I	932.00		NIST
I	938.00		NIST
I	930.00		NIST
I	937.00		NIST
I	937.00		NIST
I	938.00		NIST
I	937.00		NIST
I	938.00		NIST
I	936.00		NIST
I	951.00		NIST
I	936.00		NIST
I	938.00		NIST
I	924.00		NIST
I	979.00		NIST
I	947.00		NIST
I	954.00		NIST
I	947.00		NIST
I	950.00		NIST
I	937.00		NIST
I	937.00		NIST
I	935.00		NIST
I	959.00		NIST
I	965.00		NIST
I	948.00		NIST
I	936.00		NIST
I	957.00		NIST
I	934.00		NIST
I	937.00		NIST
S°liquid	[173.26; 175.30]	J/mol×K
S°liquid	173.26	J/mol×K	NIST
S°liquid	175.30	J/mol×K	NIST
S°solid,1 bar	45.56	J/mol×K	NIST
Tboil	[353.00; 353.30]	K
Tboil	353.24	K	KDB
Tboil	353.16	K	Isobari...
Tboil	353.30	K	Isobari...
Tboil	353.30	K	Isobari...
Tboil	353.26	K	Isobari...
Tboil	353.15	K	Phase e...
Tboil	Outlier 353.00	K	Phase d...
Tboil	353.15	K	Excess ...
Tboil	353.25	K	Vapor L...
Tboil	353.27	K	Isobari...
Tboil	353.25	K	Vapor-L...
Tboil	353.16	K	Vapor-L...
Tc	[561.20; 569.60]	K
Tc	562.05	K	KDB
Tc	562.20	K	The Cri...
Tc	562.05 ± 0.07	K	NIST
Tc	561.80 ± 0.40	K	NIST
Tc	562.20 ± 0.20	K	NIST
Tc	562.36 ± 0.40	K	NIST
Tc	561.71 ± 0.40	K	NIST
Tc	562.16 ± 0.05	K	NIST
Tc	562.10	K	NIST
Tc	562.17 ± 0.20	K	NIST
Tc	562.00 ± 0.05	K	NIST
Tc	562.05 ± 0.02	K	NIST
Tc	562.60 ± 0.60	K	NIST
Tc	563.30 ± 0.50	K	NIST
Tc	561.80 ± 0.40	K	NIST
Tc	561.20 ± 0.80	K	NIST
Tc	562.20 ± 0.60	K	NIST
Tc	562.10 ± 0.20	K	NIST
Tc	562.10 ± 0.30	K	NIST
Tc	562.00 ± 1.00	K	NIST
Tc	562.15 ± 0.20	K	NIST
Tc	561.70 ± 0.50	K	NIST
Tc	561.99 ± 0.10	K	NIST
Tc	562.09 ± 0.15	K	NIST
Tc	562.59 ± 2.22	K	NIST
Tc	561.85 ± 0.10	K	NIST
Tc	562.00 ± 0.20	K	NIST
Tc	563.20 ± 1.50	K	NIST
Tc	561.70 ± 0.50	K	NIST
Tc	561.65 ± 0.30	K	NIST
Tc	562.09 ± 0.20	K	NIST
Tc	561.86 ± 0.20	K	NIST
Tc	562.70 ± 0.60	K	NIST
Tc	564.40 ± 2.00	K	NIST
Tc	564.00 ± 2.00	K	NIST
Tc	561.70 ± 0.60	K	NIST
Tc	561.55 ± 4.00	K	NIST
Tc	561.83 ± 0.40	K	NIST
Tc	561.30 ± 1.00	K	NIST
Tc	563.70 ± 1.50	K	NIST
Tc	Outlier 569.60 ± 8.00	K	NIST
Tc	561.65 ± 0.40	K	NIST
Tc	564.90 ± 4.00	K	NIST
Tfus	[5.45; 551.90]	K
Tfus	278.66	K	Aq. Sol...
Tfus	278.68	K	KDB
Tfus	279.05	K	Influen...
Tfus	278.95	K	Solid-L...
Tfus	278.29	K	Phase E...
Tfus	278.67 ± 0.01	K	NIST
Tfus	278.64 ± 0.02	K	NIST
Tfus	278.63 ± 0.08	K	NIST
Tfus	278.70 ± 0.15	K	NIST
Tfus	278.70 ± 0.15	K	NIST
Tfus	278.65 ± 0.30	K	NIST
Tfus	Outlier 551.90 ± 0.20	K	NIST
Tfus	279.10 ± 1.00	K	NIST
Tfus	278.66 ± 0.04	K	NIST
Tfus	278.66 ± 0.05	K	NIST
Tfus	278.64 ± 0.05	K	NIST
Tfus	278.66 ± 0.06	K	NIST
Tfus	278.67 ± 0.10	K	NIST
Tfus	279.00 ± 0.20	K	NIST
Tfus	278.66 ± 0.01	K	NIST
Tfus	278.68 ± 0.10	K	NIST
Tfus	278.80 ± 0.20	K	NIST
Tfus	278.71 ± 0.05	K	NIST
Tfus	278.75 ± 0.40	K	NIST
Tfus	278.66 ± 0.10	K	NIST
Tfus	278.66 ± 0.05	K	NIST
Tfus	Outlier 5.45 ± 0.10	K	NIST
Tfus	278.65 ± 0.30	K	NIST
Tfus	278.65 ± 0.30	K	NIST
Tfus	278.62 ± 0.10	K	NIST
Tfus	278.40 ± 0.60	K	NIST
Tfus	278.68 ± 0.05	K	NIST
Tfus	278.61 ± 0.10	K	NIST
Tfus	278.58 ± 0.20	K	NIST
Tfus	278.63 ± 0.10	K	NIST
Tfus	278.49 ± 0.20	K	NIST
Tfus	278.70 ± 0.20	K	NIST
Tfus	278.65 ± 0.30	K	NIST
Tfus	278.70 ± 0.20	K	NIST
Tfus	278.66 ± 0.10	K	NIST
Tfus	280.00 ± 0.10	K	NIST
Tfus	278.64 ± 0.10	K	NIST
Tfus	278.65 ± 0.30	K	NIST
Tfus	278.65 ± 0.01	K	NIST
Tfus	278.65 ± 0.10	K	NIST
Tfus	278.59 ± 0.08	K	NIST
Tfus	278.64 ± 0.10	K	NIST
Tfus	278.65 ± 0.20	K	NIST
Tfus	278.65 ± 0.20	K	NIST
Tfus	267.65 ± 1.50	K	NIST
Tfus	278.45 ± 0.40	K	NIST
Tfus	278.60 ± 0.03	K	NIST
Tfus	278.66 ± 0.02	K	NIST
Tfus	278.70 ± 0.60	K	NIST
Tfus	278.70 ± 1.00	K	NIST
Tfus	278.63 ± 0.05	K	NIST
Tfus	278.63 ± 0.05	K	NIST
Tfus	278.55 ± 0.20	K	NIST
Tfus	278.70 ± 0.40	K	NIST
Tfus	278.60 ± 0.25	K	NIST
Tfus	278.55 ± 0.20	K	NIST
Tfus	278.55 ± 0.20	K	NIST
Tfus	278.64 ± 0.07	K	NIST
Tfus	278.63 ± 0.06	K	NIST
Tfus	278.63 ± 0.05	K	NIST
Tfus	278.58 ± 0.25	K	NIST
Tfus	278.60 ± 0.80	K	NIST
Tfus	278.25 ± 0.30	K	NIST
Tfus	278.63 ± 0.10	K	NIST
Tfus	278.63 ± 0.30	K	NIST
Tfus	278.63 ± 0.07	K	NIST
Tfus	278.55 ± 0.10	K	NIST
Tfus	278.58 ± 0.05	K	NIST
Tfus	277.00 ± 2.00	K	NIST
Vc	0.256	m3/kmol	KDB
vspec	0.00	m3/kg	PVT Rel...
Zc	0.2681520		KDB
Zra	0.27		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[93.32; 145.59]	J/mol×K	[333.15; 527.15]
Cp,gas	93.32 ± 0.06	J/mol×K	333.15	NIST
Cp,gas	95.81	J/mol×K	341.60	NIST
Cp,gas	97.99 ± 0.06	J/mol×K	348.15	NIST
Cp,gas	103.98 ± 0.06	J/mol×K	368.15	NIST
Cp,gas	105.02	J/mol×K	370.00	NIST
Cp,gas	104.77	J/mol×K	371.20	NIST
Cp,gas	108.80 ± 1.30	J/mol×K	388.00	NIST
Cp,gas	110.88	J/mol×K	390.00	NIST
Cp,gas	110.50 ± 1.30	J/mol×K	393.00	NIST
Cp,gas	113.93	J/mol×K	402.30	NIST
Cp,gas	114.29 ± 0.07	J/mol×K	403.15	NIST
Cp,gas	115.48	J/mol×K	410.00	NIST
Cp,gas	117.60 ± 1.30	J/mol×K	417.00	NIST
Cp,gas	118.80 ± 1.30	J/mol×K	428.00	NIST
Cp,gas	123.39	J/mol×K	436.15	NIST
Cp,gas	123.93 ± 0.07	J/mol×K	438.15	NIST
Cp,gas	126.80 ± 1.30	J/mol×K	463.00	NIST
Cp,gas	132.42	J/mol×K	471.10	NIST
Cp,gas	132.94 ± 0.08	J/mol×K	473.15	NIST
Cp,gas	131.40 ± 1.30	J/mol×K	481.00	NIST
Cp,gas	139.47 ± 0.08	J/mol×K	500.15	NIST
Cp,gas	145.59 ± 0.09	J/mol×K	527.15	NIST
Cp,liquid	[31.80; 151.20]	J/mol×K	[287.80; 350.15]
Cp,liquid	131.40	J/mol×K	287.80	NIST
Cp,liquid	131.40	J/mol×K	287.80	NIST
Cp,liquid	31.80	J/mol×K	293.00	NIST
Cp,liquid	134.60	J/mol×K	293.00	NIST
Cp,liquid	133.60	J/mol×K	293.15	NIST
Cp,liquid	134.61	J/mol×K	293.15	NIST
Cp,liquid	133.63	J/mol×K	293.15	Excess ...
Cp,liquid	133.10	J/mol×K	293.20	NIST
Cp,liquid	119.00	J/mol×K	295.00	NIST
Cp,liquid	134.80	J/mol×K	295.15	Measure...
Cp,liquid	135.23	J/mol×K	298.00	NIST
Cp,liquid	133.50	J/mol×K	298.00	NIST
Cp,liquid	134.98	J/mol×K	298.00	NIST
Cp,liquid	134.30	J/mol×K	298.00	NIST
Cp,liquid	135.40	J/mol×K	298.00	NIST
Cp,liquid	133.50	J/mol×K	298.00	NIST
Cp,liquid	132.20	J/mol×K	298.00	NIST
Cp,liquid	137.20	J/mol×K	298.00	NIST
Cp,liquid	135.90	J/mol×K	298.00	NIST
Cp,liquid	130.00	J/mol×K	298.00	NIST
Cp,liquid	136.00	J/mol×K	298.10	NIST
Cp,liquid	135.10	J/mol×K	298.10	NIST
Cp,liquid	135.71	J/mol×K	298.15	NIST
Cp,liquid	135.75	J/mol×K	298.15	NIST
Cp,liquid	136.06	J/mol×K	298.15	NIST
Cp,liquid	134.63	J/mol×K	298.15	NIST
Cp,liquid	136.24	J/mol×K	298.15	NIST
Cp,liquid	135.62	J/mol×K	298.15	NIST
Cp,liquid	135.70	J/mol×K	298.15	NIST
Cp,liquid	135.74	J/mol×K	298.15	NIST
Cp,liquid	135.60	J/mol×K	298.15	NIST
Cp,liquid	131.40	J/mol×K	298.15	NIST
Cp,liquid	135.90	J/mol×K	298.15	NIST
Cp,liquid	135.69	J/mol×K	298.15	NIST
Cp,liquid	135.90	J/mol×K	298.15	NIST
Cp,liquid	135.60	J/mol×K	298.15	NIST
Cp,liquid	135.76	J/mol×K	298.15	NIST
Cp,liquid	136.06	J/mol×K	298.15	NIST
Cp,liquid	135.70	J/mol×K	298.15	NIST
Cp,liquid	135.32	J/mol×K	298.15	Excess ...
Cp,liquid	135.90	J/mol×K	298.15	NIST
Cp,liquid	135.61	J/mol×K	298.15	NIST
Cp,liquid	135.76	J/mol×K	298.15	NIST
Cp,liquid	135.72	J/mol×K	298.15	NIST
Cp,liquid	135.44	J/mol×K	298.20	NIST
Cp,liquid	135.90	J/mol×K	298.50	NIST
Cp,liquid	135.30	J/mol×K	300.00	NIST
Cp,liquid	135.10	J/mol×K	300.00	NIST
Cp,liquid	136.50	J/mol×K	300.00	NIST
Cp,liquid	135.40	J/mol×K	300.15	Measure...
Cp,liquid	136.40	J/mol×K	303.00	NIST
Cp,liquid	133.90	J/mol×K	303.00	NIST
Cp,liquid	136.62	J/mol×K	303.15	Excess ...
Cp,liquid	137.40	J/mol×K	303.15	NIST
Cp,liquid	136.50	J/mol×K	305.15	Measure...
Cp,liquid	137.90	J/mol×K	310.15	Measure...
Cp,liquid	139.20	J/mol×K	315.15	Measure...
Cp,liquid	135.10	J/mol×K	316.00	NIST
Cp,liquid	140.85	J/mol×K	320.15	Measure...
Cp,liquid	139.90	J/mol×K	322.05	NIST
Cp,liquid	143.57	J/mol×K	323.15	NIST
Cp,liquid	142.50	J/mol×K	325.15	Measure...
Cp,liquid	144.15	J/mol×K	330.15	Measure...
Cp,liquid	145.80	J/mol×K	335.15	Measure...
Cp,liquid	147.55	J/mol×K	340.15	Measure...
Cp,liquid	149.30	J/mol×K	345.15	Measure...
Cp,liquid	151.20	J/mol×K	350.15	Measure...
Cp,solid	[47.86; 118.40]	J/mol×K	[90.00; 273.00]
Cp,solid	47.86	J/mol×K	90.00	NIST
Cp,solid	97.90	J/mol×K	223.90	NIST
Cp,solid	118.40	J/mol×K	273.00	NIST
η	[0.0003450; 0.0007090]	Pa×s	[288.15; 343.15]
η	0.0007090	Pa×s	288.15	Viscosi...
η	0.0006480	Pa×s	293.15	Viscosi...
η	0.0006010	Pa×s	298.15	Densiti...
η	0.0006030	Pa×s	298.15	Densiti...
η	0.0006020	Pa×s	298.15	Densiti...
η	0.0006030	Pa×s	298.15	Densiti...
η	0.0006010	Pa×s	298.15	Densiti...
η	0.0006040	Pa×s	298.15	Viscosi...
η	0.0006025	Pa×s	298.15	Ultraso...
η	0.0006038	Pa×s	298.15	Excess ...
η	0.0005612	Pa×s	303.15	Excess ...
η	0.0005630	Pa×s	303.15	Densiti...
η	0.0005620	Pa×s	303.15	Densiti...
η	0.0005690	Pa×s	303.15	Density...
η	0.0005610	Pa×s	303.15	Thermod...
η	0.0005680	Pa×s	303.15	Densiti...
η	0.0005640	Pa×s	303.15	Densiti...
η	0.0005690	Pa×s	303.15	Physica...
η	0.0005710	Pa×s	303.15	Viscosi...
η	0.0005310	Pa×s	308.15	Densiti...
η	0.0005340	Pa×s	308.15	Physica...
η	0.0005330	Pa×s	308.15	Densiti...
η	0.0005272	Pa×s	308.15	Viscome...
η	0.0005340	Pa×s	308.15	Density...
η	0.0005395	Pa×s	308.15	Ultraso...
η	0.0005260	Pa×s	308.15	Densiti...
η	0.0005232	Pa×s	308.15	Densiti...
η	0.0004970	Pa×s	313.15	Density...
η	0.0004940	Pa×s	313.15	Densiti...
η	0.0004930	Pa×s	313.15	Densiti...
η	0.0004970	Pa×s	313.15	Physica...
η	0.0004942	Pa×s	313.15	Viscome...
η	0.0005001	Pa×s	313.15	Densiti...
η	0.0005000	Pa×s	313.15	Densiti...
η	0.0004930	Pa×s	313.15	Thermod...
η	0.0004660	Pa×s	318.15	Densiti...
η	0.0004714	Pa×s	318.15	Densiti...
η	0.0004670	Pa×s	318.15	Ultraso...
η	0.0004397	Pa×s	323.15	Densiti...
η	0.0004360	Pa×s	323.15	Thermod...
η	0.0004360	Pa×s	323.15	Densiti...
η	0.0004360	Pa×s	323.15	Densiti...
η	0.0004362	Pa×s	323.15	Excess ...
η	0.0004145	Pa×s	328.15	Densiti...
η	0.0003890	Pa×s	333.15	Densiti...
η	0.0003880	Pa×s	333.15	Thermod...
η	0.0003932	Pa×s	333.15	Densiti...
η	0.0003450	Pa×s	343.15	Thermod...
η	0.0003540	Pa×s	343.15	Densiti...
ΔfusH	[8.95; 10.00]	kJ/mol	[278.55; 279.10]
ΔfusH	9.88	kJ/mol	278.55	NIST
ΔfusH	9.80	kJ/mol	278.60	NIST
ΔfusH	9.94	kJ/mol	278.60	NIST
ΔfusH	10.00	kJ/mol	278.64	NIST
ΔfusH	9.92	kJ/mol	278.65	NIST
ΔfusH	9.87	kJ/mol	278.69	NIST
ΔfusH	9.87	kJ/mol	278.70	NIST
ΔfusH	8.95	kJ/mol	278.80	NIST
ΔfusH	9.30	kJ/mol	279.10	NIST
ΔsubH	[38.00; 53.90]	kJ/mol	[193.00; 303.00]
ΔsubH	53.90 ± 0.80	kJ/mol	193.00	NIST
ΔsubH	49.40 ± 0.40	kJ/mol	193.00	NIST
ΔsubH	43.30	kJ/mol	226.00	NIST
ΔsubH	43.10	kJ/mol	229.00	NIST
ΔsubH	45.60	kJ/mol	244.50	NIST
ΔsubH	45.20	kJ/mol	251.00	NIST
ΔsubH	44.10	kJ/mol	261.00	NIST
ΔsubH	41.70	kJ/mol	265.50	NIST
ΔsubH	46.60	kJ/mol	266.50	NIST
ΔsubH	44.60	kJ/mol	273.00	NIST
ΔsubH	45.10	kJ/mol	278.00	NIST
ΔsubH	44.60	kJ/mol	279.00	NIST
ΔsubH	38.00	kJ/mol	303.00	NIST
ΔvapH	[30.20; 35.60]	kJ/mol	[285.50; 531.50]
ΔvapH	35.60	kJ/mol	285.50	NIST
ΔvapH	34.10	kJ/mol	293.00	NIST
ΔvapH	31.20	kJ/mol	294.00	NIST
ΔvapH	33.25	kJ/mol	298.00	Enthalp...
ΔvapH	33.40	kJ/mol	307.00	NIST
ΔvapH	34.50	kJ/mol	310.50	NIST
ΔvapH	32.60 ± 0.40	kJ/mol	313.00	NIST
ΔvapH	33.00 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	33.10	kJ/mol	314.00	NIST
ΔvapH	34.10	kJ/mol	318.00	NIST
ΔvapH	34.10	kJ/mol	319.00	NIST
ΔvapH	34.10	kJ/mol	321.00	NIST
ΔvapH	32.40	kJ/mol	324.00	NIST
ΔvapH	33.20	kJ/mol	325.00	NIST
ΔvapH	32.20 ± 0.10	kJ/mol	328.00	NIST
ΔvapH	34.40	kJ/mol	328.00	NIST
ΔvapH	32.50 ± 0.50	kJ/mol	328.00	NIST
ΔvapH	31.90	kJ/mol	332.00	NIST
ΔvapH	31.80 ± 0.10	kJ/mol	333.00	NIST
ΔvapH	33.40	kJ/mol	335.50	NIST
ΔvapH	33.50	kJ/mol	336.50	NIST
ΔvapH	35.30	kJ/mol	343.00	NIST
ΔvapH	31.40 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	31.40	kJ/mol	344.00	NIST
ΔvapH	31.60 ± 0.40	kJ/mol	345.00	NIST
ΔvapH	31.00	kJ/mol	350.00	NIST
ΔvapH	30.80	kJ/mol	352.00	NIST
ΔvapH	30.90 ± 0.10	kJ/mol	353.00	NIST
ΔvapH	30.60	kJ/mol	353.00	NIST
ΔvapH	30.72	kJ/mol	353.30	NIST
ΔvapH	30.76	kJ/mol	353.30	KDB
ΔvapH	30.50	kJ/mol	361.00	NIST
ΔvapH	30.20	kJ/mol	366.00	NIST
ΔvapH	31.50	kJ/mol	387.50	NIST
ΔvapH	30.20	kJ/mol	461.00	NIST
ΔvapH	30.30	kJ/mol	531.50	NIST
Psub	[0.10; 1.23]	kPa	[233.20; 260.68]
Psub	0.10	kPa	233.20	Recomme...
Psub	0.10	kPa	233.20	Recomme...
Psub	0.10	kPa	233.20	Recomme...
Psub	0.13	kPa	235.70	Recomme...
Psub	0.13	kPa	235.70	Recomme...
Psub	0.13	kPa	235.70	Recomme...
Psub	0.16	kPa	238.21	Recomme...
Psub	0.16	kPa	238.21	Recomme...
Psub	0.16	kPa	238.21	Recomme...
Psub	0.21	kPa	240.70	Recomme...
Psub	0.21	kPa	240.70	Recomme...
Psub	0.21	kPa	240.70	Recomme...
Psub	0.27	kPa	243.20	Recomme...
Psub	0.27	kPa	243.20	Recomme...
Psub	0.27	kPa	243.20	Recomme...
Psub	0.34	kPa	245.68	Recomme...
Psub	0.34	kPa	245.68	Recomme...
Psub	0.34	kPa	245.68	Recomme...
Psub	0.42	kPa	248.18	Recomme...
Psub	0.42	kPa	248.18	Recomme...
Psub	0.42	kPa	248.18	Recomme...
Psub	0.53	kPa	250.68	Recomme...
Psub	0.53	kPa	250.68	Recomme...
Psub	0.53	kPa	250.68	Recomme...
Psub	0.65	kPa	253.17	Recomme...
Psub	0.65	kPa	253.17	Recomme...
Psub	0.65	kPa	253.17	Recomme...
Psub	0.81	kPa	255.67	Recomme...
Psub	0.81	kPa	255.67	Recomme...
Psub	0.81	kPa	255.67	Recomme...
Psub	1.00	kPa	258.16	Recomme...
Psub	1.00	kPa	258.16	Recomme...
Psub	1.00	kPa	258.16	Recomme...
Psub	1.23	kPa	260.68	Recomme...
Psub	1.23	kPa	260.68	Recomme...
Psub	1.23	kPa	260.68	Recomme...
Pvap	[6.08; 2877.00]	kPa	[283.15; 520.05]
Pvap	6.08	kPa	283.15	Total v...
Pvap	7.85	kPa	288.15	Total v...
Pvap	10.03	kPa	293.15	Total v...
Pvap	9.98	kPa	293.15	Vapor-l...
Pvap	12.69	kPa	298.15	Total v...
Pvap	12.70	kPa	298.15	Thermod...
Pvap	12.71	kPa	298.15	(Vapour...
Pvap	12.64	kPa	298.15	Vapor-l...
Pvap	15.63	kPa	303.15	Vapor P...
Pvap	15.93	kPa	303.15	Total v...
Pvap	15.92	kPa	303.15	Thermod...
Pvap	15.85	kPa	303.15	Vapor-l...
Pvap	19.66	kPa	308.15	Thermod...
Pvap	19.81	kPa	308.15	Total v...
Pvap	19.71	kPa	308.15	Vapor-l...
Pvap	24.35	kPa	313.14	Vapor-L...
Pvap	24.40	kPa	313.15	Total v...
Pvap	24.33	kPa	313.15	Thermod...
Pvap	24.45	kPa	313.15	Vapor P...
Pvap	24.30	kPa	313.15	Vapor-l...
Pvap	29.73	kPa	318.15	Vapor-l...
Pvap	29.85	kPa	318.15	Total v...
Pvap	36.15	kPa	323.14	Vapor-L...
Pvap	36.60	kPa	323.15	Vapor P...
Pvap	35.47	kPa	323.15	Isother...
Pvap	36.09	kPa	323.15	Vapor-l...
Pvap	36.24	kPa	323.15	Total v...
Pvap	40.00	kPa	325.60	Determi...
Pvap	39.52	kPa	325.60	Extensi...
Pvap	43.51	kPa	328.15	Vapor-l...
Pvap	43.65	kPa	328.15	Vapor L...
Pvap	49.45	kPa	331.70	Extensi...
Pvap	52.17	kPa	333.13	Vapor-L...
Pvap	52.11	kPa	333.15	Vapor-l...
Pvap	52.45	kPa	333.15	Vapor l...
Pvap	53.12	kPa	333.15	Vapor P...
Pvap	53.33	kPa	333.56	Determi...
Pvap	62.01	kPa	338.15	Vapor-l...
Pvap	62.10	kPa	338.15	Phase e...
Pvap	66.66	kPa	340.06	Determi...
Pvap	69.20	kPa	341.70	Extensi...
Pvap	74.82	kPa	343.15	Vapor P...
Pvap	73.35	kPa	343.15	Vapor-l...
Pvap	79.99	kPa	345.61	Determi...
Pvap	86.40	kPa	348.15	Phase e...
Pvap	86.27	kPa	348.15	Vapor-l...
Pvap	93.32	kPa	350.50	Determi...
Pvap	100.00	kPa	353.15	Vapor l...
Pvap	100.91	kPa	353.15	Vapor-l...
Pvap	101.33	kPa	353.15	Phase e...
Pvap	101.33	kPa	353.25	Vapor L...
Pvap	101.30	kPa	353.25	Vapor-L...
Pvap	101.33	kPa	353.26	Isobari...
Pvap	101.33	kPa	353.27	Isobari...
Pvap	101.30	kPa	353.30	Isobari...
Pvap	101.60	kPa	353.60	Extensi...
Pvap	137.28	kPa	363.15	Vapor-L...
Pvap	205.00	kPa	378.35	Quantit...
Pvap	247.52	kPa	385.30	Extensi...
Pvap	366.00	kPa	401.25	Quantit...
Pvap	379.30	kPa	403.15	Isother...
Pvap	499.10	kPa	415.80	Extensi...
Pvap	572.00	kPa	421.85	Quantit...
Pvap	750.14	kPa	435.40	Extensi...
Pvap	778.00	kPa	437.45	Quantit...
Pvap	1173.00	kPa	460.35	Quantit...
Pvap	1622.00	kPa	480.45	Quantit...
Pvap	2183.00	kPa	500.15	Quantit...
Pvap	2877.00	kPa	520.05	Quantit...
n0	[1.38820; 1.50765]		[283.15; 318.15]
n0	1.50765		283.15	Density...
n0	1.50420		288.15	Refract...
n0	1.50420		288.15	Densiti...
n0	1.50500		288.15	Excess ...
n0	1.50090		293.10	Densiti...
n0	1.38820		293.10	Liquid ...
n0	1.50240		293.10	(Liquid...
n0	1.50090		293.10	A study...
n0	1.50110		293.15	Solubil...
n0	1.50090		293.15	A study...
n0	1.50150		293.15	Infinit...
n0	1.50110		293.15	Solubil...
n0	1.50110		293.15	Solubil...
n0	1.50110		293.15	Refract...
n0	1.50110		293.15	Excess ...
n0	1.50110		293.15	Densiti...
n0	1.50090		293.15	Effect ...
n0	1.50090		293.15	Experim...
n0	1.50110		293.15	Solubil...
n0	1.50110		293.15	Densiti...
n0	1.49774		298.15	Liquid ...
n0	1.49692		298.15	Azeotro...
n0	1.49710		298.15	Excess ...
n0	1.50090		298.15	The vol...
n0	1.49790		298.15	Excess ...
n0	1.49774		298.15	Experim...
n0	1.49764		298.15	Isother...
n0	1.49790		298.15	Excess ...
n0	1.49785		298.15	Isother...
n0	1.49810		298.15	Separat...
n0	1.49800		298.15	Densiti...
n0	1.50090		298.15	Densiti...
n0	1.49774		298.15	Effect ...
n0	1.49765		298.15	Isobari...
n0	1.50090		298.15	Effects...
n0	1.49790		298.15	Excess ...
n0	1.49790		298.15	p, Vm, ...
n0	1.49774		298.15	Thermop...
n0	1.49900		298.15	Liquid-...
n0	1.49790		298.15	Volumet...
n0	1.49774		298.15	Density...
n0	1.49740		298.15	Experim...
n0	1.49764		298.15	Isother...
n0	1.49774		298.15	Separat...
n0	1.49790		298.15	Densiti...
n0	1.49774		298.15	Liquid ...
n0	1.49774		298.15	Liquid-...
n0	1.49774		298.15	Extract...
n0	1.49792		298.15	KDB
n0	1.49800		298.15	Refract...
n0	1.49720		298.20	Liquid-...
n0	1.49360		303.15	Excess ...
n0	1.48490		303.15	Excess ...
n0	1.49620		303.15	Densiti...
n0	1.49490		303.15	Refract...
n0	1.49620		303.15	Volumet...
n0	1.49490		303.15	Densiti...
n0	1.49470		303.15	Densiti...
n0	1.49540		303.15	Study o...
n0	1.49440		308.15	Volumet...
n0	1.49180		308.15	Densiti...
n0	1.49440		308.15	Densiti...
n0	1.49210		308.15	Topolog...
n0	1.49180		308.15	Refract...
n0	1.49030		308.15	Excess ...
n0	1.49290		313.15	Volumet...
n0	1.48870		313.15	Densiti...
n0	1.49290		313.15	Densiti...
n0	1.48870		313.15	Refract...
n0	1.49110		318.15	Densiti...
n0	1.48560		318.15	Refract...
n0	1.48560		318.15	Densiti...
ρl	[824.70; 885.00]	kg/m3	[288.15; 343.15]
ρl	884.25	kg/m3	288.15	Densiti...
ρl	884.25	kg/m3	288.15	Tempera...
ρl	884.25	kg/m3	288.15	Volumet...
ρl	884.25	kg/m3	288.15	Effect ...
ρl	883.90	kg/m3	288.15	Volumet...
ρl	884.30	kg/m3	288.15	Densiti...
ρl	885.00	kg/m3	289.00	KDB
ρl	878.98	kg/m3	293.00	Volumet...
ρl	878.92	kg/m3	293.15	Effect ...
ρl	878.90	kg/m3	293.15	Densiti...
ρl	878.92	kg/m3	293.15	Densiti...
ρl	878.95	kg/m3	293.15	Densiti...
ρl	878.87	kg/m3	293.15	Theoret...
ρl	878.93	kg/m3	293.15	Density...
ρl	878.89	kg/m3	293.15	Excess ...
ρl	876.85	kg/m3	293.15	Volumet...
ρl	878.23	kg/m3	293.15	Densiti...
ρl	878.92	kg/m3	293.15	Volumet...
ρl	878.92	kg/m3	293.15	Tempera...
ρl	876.53	kg/m3	293.20	Isobari...
ρl	873.45	kg/m3	298.10	Excess ...
ρl	873.67	kg/m3	298.10	Excess ...
ρl	873.58	kg/m3	298.15	Volumet...
ρl	873.54	kg/m3	298.15	Thermod...
ρl	873.57	kg/m3	298.15	Excess ...
ρl	873.58	kg/m3	298.15	Volumet...
ρl	873.58	kg/m3	298.15	Effect ...
ρl	873.58	kg/m3	298.15	Thermod...
ρl	873.62	kg/m3	298.15	Topolog...
ρl	873.55	kg/m3	298.15	Experim...
ρl	873.60	kg/m3	298.15	Fluid P...
ρl	873.58	kg/m3	298.15	Excess ...
ρl	873.64	kg/m3	298.15	Vapor-L...
ρl	873.66	kg/m3	298.15	Densiti...
ρl	873.95	kg/m3	298.15	Liquid ...
ρl	873.45	kg/m3	298.15	Experim...
ρl	874.00	kg/m3	298.15	Liquid ...
ρl	873.62	kg/m3	298.15	Density...
ρl	873.11	kg/m3	298.15	Densiti...
ρl	873.53	kg/m3	298.15	Phase b...
ρl	873.79	kg/m3	298.15	Liquid-...
ρl	873.54	kg/m3	298.15	Heat ca...
ρl	873.64	kg/m3	298.15	Excess ...
ρl	873.40	kg/m3	298.15	Mutual ...
ρl	873.53	kg/m3	298.15	Phase b...
ρl	873.73	kg/m3	298.15	Liquid ...
ρl	873.71	kg/m3	298.15	Study o...
ρl	873.71	kg/m3	298.15	Applica...
ρl	873.20	kg/m3	298.15	Ternary...
ρl	873.61	kg/m3	298.15	Densiti...
ρl	873.71	kg/m3	298.15	Determi...
ρl	873.57	kg/m3	298.15	Measure...
ρl	873.54	kg/m3	298.15	Excess ...
ρl	873.58	kg/m3	298.15	Densiti...
ρl	873.57	kg/m3	298.15	(Liquid...
ρl	874.16	kg/m3	298.15	Experim...
ρl	873.50	kg/m3	298.15	Density...
ρl	873.64	kg/m3	298.15	Molar E...
ρl	873.36	kg/m3	298.15	Volumet...
ρl	873.58	kg/m3	298.15	Tempera...
ρl	873.57	kg/m3	298.15	Evaluat...
ρl	875.47	kg/m3	298.15	Calorim...
ρl	868.30	kg/m3	303.00	Volumet...
ρl	868.20	kg/m3	303.15	Thermod...
ρl	868.23	kg/m3	303.15	Volumet...
ρl	868.20	kg/m3	303.15	Excess ...
ρl	868.10	kg/m3	303.15	Volumet...
ρl	868.20	kg/m3	303.15	Densiti...
ρl	868.23	kg/m3	303.15	Effect ...
ρl	868.20	kg/m3	303.15	Theoret...
ρl	868.71	kg/m3	303.15	Volumet...
ρl	868.23	kg/m3	303.15	Densiti...
ρl	868.26	kg/m3	303.15	Densiti...
ρl	868.30	kg/m3	303.15	Studies...
ρl	868.23	kg/m3	303.15	Tempera...
ρl	868.42	kg/m3	303.15	Volumet...
ρl	868.10	kg/m3	303.15	Viscome...
ρl	867.59	kg/m3	303.15	Densiti...
ρl	868.29	kg/m3	303.15	Densiti...
ρl	868.29	kg/m3	303.15	Density...
ρl	868.20	kg/m3	303.15	Heat ca...
ρl	862.84	kg/m3	308.15	Thermod...
ρl	862.94	kg/m3	308.15	Density...
ρl	862.21	kg/m3	308.15	Densiti...
ρl	862.90	kg/m3	308.15	Densiti...
ρl	862.84	kg/m3	308.15	Heat ca...
ρl	862.87	kg/m3	308.15	Volumet...
ρl	862.87	kg/m3	308.15	Tempera...
ρl	862.87	kg/m3	308.15	Effect ...
ρl	862.92	kg/m3	308.15	Densiti...
ρl	862.87	kg/m3	308.15	Densiti...
ρl	857.57	kg/m3	313.00	Volumet...
ρl	857.56	kg/m3	313.15	Densiti...
ρl	857.50	kg/m3	313.15	Effect ...
ρl	857.50	kg/m3	313.15	Volumet...
ρl	857.50	kg/m3	313.15	Tempera...
ρl	857.58	kg/m3	313.15	Density...
ρl	857.40	kg/m3	313.15	Volumet...
ρl	857.44	kg/m3	313.15	Theoret...
ρl	857.59	kg/m3	313.15	Studies...
ρl	857.40	kg/m3	313.15	Viscome...
ρl	857.40	kg/m3	313.15	Densiti...
ρl	856.82	kg/m3	313.15	Densiti...
ρl	857.50	kg/m3	313.15	Densiti...
ρl	852.23	kg/m3	318.15	Densiti...
ρl	852.19	kg/m3	318.15	Density...
ρl	846.76	kg/m3	323.00	Volumet...
ρl	846.60	kg/m3	323.15	Volumet...
ρl	846.77	kg/m3	323.15	Density...
ρl	846.62	kg/m3	323.15	Theoret...
ρl	846.60	kg/m3	323.15	Viscome...
ρl	846.50	kg/m3	323.15	Densiti...
ρl	846.05	kg/m3	323.15	Densiti...
ρl	835.71	kg/m3	333.15	Theoret...
ρl	835.70	kg/m3	333.15	Densiti...
ρl	835.76	kg/m3	333.15	Densiti...
ρl	824.89	kg/m3	343.15	Densiti...
ρl	824.70	kg/m3	343.15	Densiti...
ΔfusS	[32.10; 35.90]	J/mol×K	[278.55; 279.10]
ΔfusS	35.50	J/mol×K	278.55	NIST
ΔfusS	35.19	J/mol×K	278.60	NIST
ΔfusS	35.90	J/mol×K	278.64	NIST
ΔfusS	35.59	J/mol×K	278.65	NIST
ΔfusS	35.40	J/mol×K	278.69	NIST
ΔfusS	32.10	J/mol×K	278.80	NIST
ΔfusS	33.30	J/mol×K	279.10	NIST
csound,fluid	[1184.47; 1368.70]	m/s	[283.15; 323.15]
csound,fluid	1368.70	m/s	283.15	Speeds ...
csound,fluid	1345.47	m/s	288.15	Tempera...
csound,fluid	1345.47	m/s	288.15	Influen...
csound,fluid	1333.44	m/s	290.65	Influen...
csound,fluid	1316.50	m/s	293.00	Ultraso...
csound,fluid	1322.70	m/s	293.15	Tempera...
csound,fluid	1321.59	m/s	293.15	Influen...
csound,fluid	1322.72	m/s	293.15	Volumet...
csound,fluid	1324.40	m/s	293.15	Physico...
csound,fluid	1309.88	m/s	295.65	Influen...
csound,fluid	1294.00	m/s	298.00	Ultraso...
csound,fluid	1299.50	m/s	298.15	Physico...
csound,fluid	1298.27	m/s	298.15	Tempera...
csound,fluid	1299.00	m/s	298.15	Densiti...
csound,fluid	1298.27	m/s	298.15	Influen...
csound,fluid	1298.20	m/s	298.15	Sound s...
csound,fluid	1300.00	m/s	298.15	Densiti...
csound,fluid	1298.30	m/s	298.15	Speeds ...
csound,fluid	1298.00	m/s	298.15	Isentro...
csound,fluid	1298.00	m/s	298.15	Thermod...
csound,fluid	1299.30	m/s	298.15	Tempera...
csound,fluid	1299.33	m/s	298.15	Volumet...
csound,fluid	1286.68	m/s	300.65	Influen...
csound,fluid	1272.80	m/s	303.00	Ultraso...
csound,fluid	1276.00	m/s	303.15	Tempera...
csound,fluid	1275.70	m/s	303.15	Physico...
csound,fluid	1275.96	m/s	303.15	Volumet...
csound,fluid	1275.13	m/s	303.15	Influen...
csound,fluid	1263.59	m/s	305.65	Influen...
csound,fluid	1252.08	m/s	308.15	Influen...
csound,fluid	1252.80	m/s	308.15	Tempera...
csound,fluid	1260.00	m/s	308.15	Densiti...
csound,fluid	1260.00	m/s	308.15	Densiti...
csound,fluid	1252.76	m/s	308.15	Volumet...
csound,fluid	1259.00	m/s	308.15	Thermod...
csound,fluid	1252.40	m/s	308.15	Physico...
csound,fluid	1240.69	m/s	310.65	Influen...
csound,fluid	1226.50	m/s	313.00	Ultraso...
csound,fluid	1229.30	m/s	313.15	Physico...
csound,fluid	1229.50	m/s	313.15	Speeds ...
csound,fluid	1229.76	m/s	313.15	Volumet...
csound,fluid	1229.29	m/s	313.15	Influen...
csound,fluid	1229.80	m/s	313.15	Tempera...
csound,fluid	1217.94	m/s	315.65	Influen...
csound,fluid	1207.00	m/s	318.15	Tempera...
csound,fluid	1206.70	m/s	318.15	Influen...
csound,fluid	1207.04	m/s	318.15	Volumet...
csound,fluid	1207.80	m/s	318.15	Physico...
csound,fluid	1195.55	m/s	320.65	Influen...
csound,fluid	1184.50	m/s	323.15	Tempera...
csound,fluid	1184.63	m/s	323.15	Influen...
csound,fluid	1184.47	m/s	323.15	Volumet...
csound,fluid	1184.63	m/s	323.15	Tempera...
γ	[0.03; 0.03]	N/m	[280.25; 313.44]
γ	0.03	N/m	280.25	Standar...
γ	0.03	N/m	283.13	Standar...
γ	0.03	N/m	285.64	Standar...
γ	0.03	N/m	288.11	Standar...
γ	0.03	N/m	290.58	Standar...
γ	0.03	N/m	293.08	Standar...
γ	0.03	N/m	293.15	Investi...
γ	0.03	N/m	293.20	KDB
γ	0.03	N/m	295.46	Standar...
γ	0.03	N/m	298.09	Standar...
γ	0.03	N/m	300.41	Standar...
γ	0.03	N/m	303.24	Standar...
γ	0.03	N/m	306.00	Standar...
γ	0.03	N/m	308.05	Standar...
γ	0.03	N/m	310.32	Standar...
γ	0.03	N/m	313.44	Standar...
λ	[0.11; 0.15]	W/m×K	[281.18; 392.16]
λ	0.15	W/m×K	281.18	Thermal...
λ	0.15	W/m×K	281.49	Thermal...
λ	0.15	W/m×K	281.76	Thermal...
λ	0.14	W/m×K	295.92	Thermal...
λ	0.14	W/m×K	296.25	Thermal...
λ	0.14	W/m×K	296.53	Thermal...
λ	0.14	W/m×K	301.25	Thermal...
λ	0.14	W/m×K	301.59	Thermal...
λ	0.14	W/m×K	301.87	Thermal...
λ	0.14	W/m×K	302.75	Thermal...
λ	0.13	W/m×K	319.14	Thermal...
λ	0.13	W/m×K	319.49	Thermal...
λ	0.13	W/m×K	319.79	Thermal...
λ	0.13	W/m×K	332.54	Thermal...
λ	0.12	W/m×K	362.39	Thermal...
λ	0.11	W/m×K	392.16	Thermal...

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil	353.35	K	96.60	Low cos...
Tfus	[278.94; 663.67]	K	[100.00; 3000000.00]
Tfus	278.94	K	100.00	Activit...
Tfus	293.15	K	53620.00	Influen...
Tfus	303.15	K	92220.00	Influen...
Tfus	306.44	K	100000.00	Fusion ...
Tfus	313.15	K	133290.00	Influen...
Tfus	323.15	K	176820.00	Influen...
Tfus	329.93	K	200000.00	Fusion ...
Tfus	333.15	K	222810.00	Influen...
Tfus	343.15	K	271270.00	Influen...
Tfus	351.25	K	300000.00	Fusion ...
Tfus	353.15	K	322200.00	Influen...
Tfus	370.85	K	400000.00	Fusion ...
Tfus	389.07	K	500000.00	Fusion ...
Tfus	406.15	K	600000.00	Fusion ...
Tfus	422.25	K	700000.00	Fusion ...
Tfus	437.52	K	800000.00	Fusion ...
Tfus	452.06	K	900000.00	Fusion ...
Tfus	465.96	K	1000000.00	Fusion ...
Tfus	538.73	K	1500000.00	Fusion ...
Tfus	584.85	K	2000000.00	Fusion ...
Tfus	625.73	K	2500000.00	Fusion ...
Tfus	663.67	K	3000000.00	Fusion ...

Datasets

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

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
313.20	690.00	0.0005
313.20	5000.00	0.0005
313.20	10000.00	0.0005
313.20	20000.00	0.0006
313.20	30000.00	0.0006
313.20	40000.00	0.0007
313.20	50000.00	0.0007
313.20	60000.00	0.0008
333.20	690.00	0.0004
333.20	5000.00	0.0004
333.20	10000.00	0.0004
333.20	20000.00	0.0005
333.20	30000.00	0.0005
333.20	40000.00	0.0006
333.20	50000.00	0.0006
333.20	60000.00	0.0006
353.20	690.00	0.0003
353.20	5000.00	0.0003
353.20	10000.00	0.0003
353.20	20000.00	0.0004
353.20	30000.00	0.0004
353.20	40000.00	0.0005
353.20	50000.00	0.0005
353.20	60000.00	0.0005
373.20	690.00	0.0003
373.20	5000.00	0.0003
373.20	10000.00	0.0003
373.20	20000.00	0.0003
373.20	30000.00	0.0003
373.20	40000.00	0.0004
373.20	50000.00	0.0004
373.20	60000.00	0.0004
393.20	690.00	0.0002
393.20	5000.00	0.0002
393.20	10000.00	0.0003
393.20	20000.00	0.0003
393.20	30000.00	0.0003
393.20	40000.00	0.0003
393.20	50000.00	0.0003
393.20	60000.00	0.0004
Reference

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

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.00	2100.00	877.4
293.00	3100.00	878.1
293.00	4100.00	878.8
293.00	5000.00	879.6
293.00	10100.00	883.4
293.00	20000.00	890.4
293.00	30000.00	896.9
293.00	40000.00	902.9
293.00	50000.00	908.6
293.00	60000.00	914.0
293.00	70000.00	919.6
313.00	2100.00	857.0
313.00	3100.00	857.8
313.00	4100.00	858.7
313.00	5000.00	859.6
313.00	10100.00	863.9
313.00	20000.00	871.5
313.00	30000.00	878.7
313.00	40000.00	885.2
313.00	50000.00	891.6
313.00	60000.00	897.5
313.00	70000.00	902.9
333.00	2100.00	835.1
333.00	3100.00	836.0
333.00	4100.00	837.0
333.00	5000.00	838.0
333.00	10100.00	842.7
333.00	20000.00	851.8
333.00	30000.00	859.4
333.00	40000.00	867.0
333.00	50000.00	874.2
333.00	60000.00	880.8
333.00	70000.00	886.7
353.00	2100.00	813.1
353.00	3100.00	814.2
353.00	4100.00	815.4
353.00	5000.00	816.5
353.00	10100.00	822.3
353.00	20000.00	832.3
353.00	30000.00	841.2
353.00	40000.00	849.5
353.00	50000.00	857.0
353.00	60000.00	864.3
353.00	70000.00	871.2
373.00	2100.00	790.7
373.00	3100.00	792.1
373.00	4100.00	793.4
373.00	5000.00	794.7
373.00	10100.00	801.4
373.00	20000.00	812.9
373.00	30000.00	823.1
373.00	40000.00	832.3
373.00	50000.00	840.7
373.00	60000.00	848.2
373.00	70000.00	855.7
393.00	2100.00	767.6
393.00	3100.00	769.4
393.00	4100.00	770.9
393.00	5000.00	772.5
393.00	10100.00	780.0
393.00	20000.00	793.0
393.00	30000.00	804.5
393.00	40000.00	814.6
393.00	50000.00	824.0
393.00	60000.00	832.6
393.00	70000.00	841.0
413.00	2100.00	743.0
413.00	3100.00	745.1
413.00	4100.00	747.0
413.00	5000.00	748.8
413.00	10100.00	758.0
413.00	20000.00	773.2
413.00	30000.00	786.2
413.00	40000.00	797.5
413.00	50000.00	807.8
413.00	60000.00	817.2
413.00	70000.00	825.8
433.00	2100.00	716.7
433.00	3100.00	719.4
433.00	4100.00	721.8
433.00	5000.00	724.0
433.00	10100.00	735.4
433.00	20000.00	753.0
433.00	30000.00	767.8
433.00	40000.00	780.3
433.00	50000.00	791.6
433.00	60000.00	801.7
433.00	70000.00	811.0
448.00	2100.00	696.0
448.00	3100.00	699.2
448.00	4100.00	702.1
448.00	5000.00	704.8
448.00	10100.00	717.8
448.00	20000.00	738.0
448.00	30000.00	754.2
448.00	40000.00	767.8
448.00	50000.00	779.8
448.00	60000.00	790.6
448.00	70000.00	800.3
468.00	2100.00	666.9
468.00	3100.00	670.7
468.00	4100.00	674.3
468.00	5000.00	677.8
468.00	10100.00	693.2
468.00	20000.00	717.0
468.00	30000.00	735.1
468.00	40000.00	750.3
468.00	50000.00	763.6
468.00	60000.00	775.5
468.00	70000.00	786.1
Reference

Speed of sound, m/s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
283.15	101.00	1371.6
283.15	1112.00	1376.8
283.15	2281.00	1382.4
283.15	4616.00	1393.2
283.15	6766.00	1403.3
283.15	9100.00	1413.6
283.15	11628.00	1424.5
283.15	14278.00	1436.0
283.15	15957.00	1443.4
283.15	18556.00	1454.0
283.15	20823.00	1463.0
283.15	23405.00	1473.4
298.15	101.00	1299.9
298.15	888.00	1305.0
298.15	1246.00	1305.8
298.15	2254.00	1311.8
298.15	2506.00	1312.2
298.15	4580.00	1322.5
298.15	4719.00	1323.9
298.15	6991.00	1334.4
298.15	7131.00	1335.5
298.15	9327.00	1346.2
298.15	9335.00	1346.2
298.15	9408.00	1346.0
298.15	11563.00	1355.8
298.15	11640.00	1357.0
298.15	14137.00	1368.5
298.15	14317.00	1368.6
298.15	15927.00	1375.9
298.15	16524.00	1379.1
298.15	18655.00	1388.6
298.15	18844.00	1389.0
298.15	20826.00	1398.1
298.15	21001.00	1398.6
298.15	23151.00	1407.9
298.15	23834.00	1410.7
298.15	25699.00	1418.5
298.15	26172.00	1420.5
298.15	28369.00	1428.5
298.15	101.00	1300.2
313.15	101.00	1230.8
313.15	2047.00	1241.3
313.15	3268.00	1247.8
313.15	5111.00	1257.8
313.15	7199.00	1268.7
313.15	9383.00	1280.0
313.15	11613.00	1291.3
313.15	14139.00	1303.7
313.15	16386.00	1314.6
313.15	18686.00	1325.5
313.15	21242.00	1337.2
313.15	23254.00	1346.4
313.15	24384.00	1351.3
313.15	25607.00	1357.2
313.15	25608.00	1357.3
313.15	28210.00	1368.6
333.15	101.00	1142.4
333.15	1260.00	1148.0
333.15	2426.00	1155.0
333.15	5026.00	1170.5
333.15	7135.00	1182.9
333.15	9195.00	1194.5
333.15	11729.00	1208.4
333.15	14011.00	1220.6
333.15	16310.00	1232.7
333.15	18687.00	1244.8
333.15	20059.00	1251.8
333.15	21112.00	1257.2
333.15	23196.00	1267.4
333.15	25517.00	1278.7
333.15	28165.00	1287.7
Reference

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Frequency, MHz - Liquid	Speed of sound, m/s - Liquid
303.15	101.33	2.0	1257.0
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
29815.10	283.21	1498.11
24857.00	283.20	1479.03
20203.80	283.20	1460.21
15331.80	283.20	1439.87
10233.80	283.20	1418.25
5280.10	283.20	1395.99
102.10	283.20	1372.03
30106.10	298.20	1436.88
25017.80	298.20	1415.76
20104.10	298.20	1394.27
14866.50	298.20	1371.03
10068.60	298.20	1349.48
5421.70	298.20	1326.99
84.20	298.20	1299.74
29980.00	313.20	1375.67
25204.40	313.20	1354.82
20194.50	313.20	1332.15
15331.60	313.20	1309.02
10140.00	313.20	1283.5
5536.50	313.20	1259.76
61.20	313.20	1230.41
30145.60	333.21	1299.17
24756.40	333.21	1273.95
19600.70	333.21	1248.51
15038.40	333.21	1225.05
10149.20	333.21	1198.3
5378.80	333.21	1171.44
153.70	333.21	1139.68
30063.00	353.21	1225.96
24679.70	353.21	1198.74
19917.50	353.20	1173.19
15092.20	353.20	1146.64
10006.90	353.21	1116.2
5094.90	353.21	1084.94
172.30	353.21	1052.25
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[263.55; 376.19]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.36756e+01
Coefficient B			-2.51081e+03
Coefficient C			-7.60040e+01
Temperature range, min.			263.55
Temperature range, max.			376.19
Pvap	1.33	kPa	263.55	Calculated Property
Pvap	3.08	kPa	276.07	Calculated Property
Pvap	6.45	kPa	288.58	Calculated Property
Pvap	12.44	kPa	301.10	Calculated Property
Pvap	22.39	kPa	313.61	Calculated Property
Pvap	37.99	kPa	326.13	Calculated Property
Pvap	61.29	kPa	338.64	Calculated Property
Pvap	94.68	kPa	351.16	Calculated Property
Pvap	140.82	kPa	363.67	Calculated Property
Pvap	202.63	kPa	376.19	Calculated Property
Pvap	[4.80; 4881.18]	kPa	[278.68; 562.16]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			7.11072e+01
Coefficient B			-6.28104e+03
Coefficient C			-8.43361e+00
Coefficient D			6.19841e-06
Temperature range, min.			278.68
Temperature range, max.			562.16
Pvap	4.80	kPa	278.68	Calculated Property
Pvap	21.52	kPa	310.18	Calculated Property
Pvap	69.91	kPa	341.68	Calculated Property
Pvap	180.32	kPa	373.17	Calculated Property
Pvap	392.79	kPa	404.67	Calculated Property
Pvap	754.58	kPa	436.17	Calculated Property
Pvap	1318.78	kPa	467.67	Calculated Property
Pvap	2145.24	kPa	499.16	Calculated Property
Pvap	3304.00	kPa	530.66	Calculated Property
Pvap	4881.18	kPa	562.16	Calculated Property

Similar Compounds

Find more compounds similar to Benzene.

Mixtures

• 1,3-Dioxolane + Benzene
• Benzene + 1,4-Dioxane
• Benzene + Tributylamine
• Benzene + Triethylamine
• Benzene + Propane, 2-methoxy-2-methyl-
• Benzene + 1-Butanol
• Benzene + Trichloromethane + 1-Butanol
• 2-Propenoic acid, ethyl ester + Benzene
• Benzene + 2-Propenoic acid, butyl ester
• Benzene + 2-Propenoic acid, methyl ester
• Benzene + Styrene
• Benzene + Toluene
• Benzene + Ethylbenzene
• Benzene + Heptane
• Benzene + Cyclooctane
• Benzene + 1-Propanol
• Benzene + 1-Propanol + 2-Pyrrolidinone
• Benzene + Toluene + Tetrahydropyran
• Benzene + Tetrahydropyran + o-Xylene
• Benzene + p-Xylene + Tetrahydropyran

Find more mixtures with Benzene.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
• Densities and Refractive Indices of Binary Mixtures of Benzene with Triethylamine and Tributylamine at Different Temperatures
• Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
• Temperature Dependence of Densities and Excess Molar Volumes of the Ternary Mixture (1-Butanol + Chloroform + Benzene) and its Binary Constituents (1-Butanol + Chloroform and 1-Butanol + Benzene)
• Volumetric, Viscometric, Ultrasonic, and Refractive Index Properties of Liquid Mixtures of Benzene with Industrially Important Monomers at Different Temperatures
• PVT Relationships of Binary Mixtures of Indole with 2-Methylnaphthalene and Biphenyl at 333.15 K and Pressures up to 270 MPa
• Viscometric and Volumetric Properties of 10 Regular Binary Systems at 308.15 K and 313.15 K
• 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, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Ethyl-1-hexanol with Benzene and Halobenzenes
• Fluid Phase Topology of Benzene + Cyclohexane + 1-Propanol at 101.3 kPa
• Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachlorethane or tetrachloroethene with benzene at nine temperatures
• Hydrogen solubility in a chemical hydrogen storage medium, aromatic hydrocarbon, cyclic hydrocarbon, and their mixture for fuel cell systems
• Liquid liquid equilibria for pseudoternary systems: isooctane benzene (methanol +water)
• Activity coefficient at infinite dilution, azeotropic data, excess enthalpies and solid liquid-equilibria for binary systems of alkanes and aromatics with esters
• Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, trihexyl(tetradecyl)-phosphonium tris(pentafluoroethyl) trifluorophosphate, by gas liquid chromatography
• Topological and thermodynamic investigations of molecular interactions in binary mixtures: Molar excess volumes and molar excess enthalpies
• Thermodynamic properties of mixtures containing ionic liquids Vapor pressures and activity coefficients of n-alcohols and benzene in binary mixtures with 1-methyl-3-butyl-imidazolium bis(trifluoromethyl-sulfonyl) imide
• Ultrasonic velocity, viscosity and excess properties of binary mixture of tetrahydrofuran with 1-propanol and 2-propanol
• Experimental and predicted vapour liquid equilibrium of 1,4-dioxane with cycloalkanes and benzene
• Effect of temperature on the excess molar volumes of some alcohol + aromatic mixtures and modelling by cubic EOS mixing rules
• Total pressure and excess Gibbs energy for the ternary mixture di-isopropyl ether + 1-propanol + benzene and its corresponding binary systems at 313.15K
• Phase equilibria properties of binary and ternary systems containing di-isopropyl ether + isobutanol + benzene at 313.15K
• Isobaric vapor liquid equilibrium for methyltrichlorosilane dimethyldichlorosilane benzene system
• Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, tributylmethylphosphonium methylsulphate by gas liquid chromatography
• Measurement of heat capacities of ionic liquids by differential scanning calorimetry
• Excess enthalpies of binary mixtures of 2-ethoxyethanol with four hydrocarbons at 298.15, 308.15, and 318.15K An experimental and theoretical study
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
• Volumetric properties of the ternary system ethanol + chloroform + benzene at temperature range (288.15 313.15) K: Experimental data, correlation and prediction by cubic EOS
• Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
• Liquid liquid equilibria of methylcyclohexane benzene N-formylmorpholine at several temperatures
• 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)
• Separation of aromatic hydrocarbons from alkanes using ammonium ionic liquid C2NTf2 at T = 298.15K
• 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
• Hydrogen solubility of mixed naphthenes and aromatics for a new hydrogen storage medium in fuel cell system
• Liquid viscosities of benzene, n-tetradecane, and benzene + n-tetradecane from 313 to 393K and pressures up to 60MPa: Experiment and modeling
• Liquid liquid equilibrium of ternary systems 1-butyl-3-methylimidazolium hexafluorophosphate + aromatic + aliphatic
• Isothermal vapor liquid equilibrium at 323.15K and excess molar volumes and refractive indices at 298.15K for the ternary system propyl vinyl ether + 1-propanol + benzene and its binary sub-systems
• Measurement and correlation of vapor pressure of benzene and thiophene with BMIM][PF6] and [BMIM][BF4] ionic liquids
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid N-butyl-4-methylpyridinium tosylate using GLC at T = (328.15, 333.15, 338.15, and 343.15)K
• 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
• Solubility of pyrene in simple and mixed solvent systems
• Liquid liquid equilibria for {hexane + benzene + 1-ethyl-3-methylimidazolium ethylsulfate} at (298.2, 313.2 and 328.2)K
• Excess enthalpies of ether + alcohol + hydrocarbon mixtures: Binary and ternary mixtures containing dibutyl ether (DBE), 1-butanol and benzene at 298.15K and 313.15K
• 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
• 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
• 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 for benzene-cyclohexene and activity coefficients at infinite dilution for the ternary systems with ionic liquids
• 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
• Experimental and predicted excess molar enthalpies of binary mixtures containing 2,2'-oxybis[propane], benzene, butan-1-ol, 2-methylpropan-1-ol, 2-methyl-2-ene-1-propanol at 303.15 K
• 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
• 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}
• Volumetric behavior of the binary systems benzene + cyclohexane and benzene + 2,2,4-trimethyl-pentane at temperatures 293.15-323.15K
• Influence of anion structure on the liquid-liquid equilibria of 1-(3-hydroxypropyl)pyridinium cation based ionic liquid-hydrocarbon binary systems
• Influence of temperature on the (liquid + liquid) equilibria of {methanol + benzene + hexane} ternary system
• 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
• Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid ethyl(2-hydroxyethyl)dimethyl-ammonium diethylphosphate using gas liquid chromatography
• Solid-liquid phase equilibrium of glyphosate in selected solvents
• 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
• Volumetric behavior of the ternary system benzene-2-methoxy-2-methylbutane-2,2,4-trimethylpentane and all binary sub-systems at temperature range (298.15 - 318.15) K
• 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
• Ternary (liquid liquid) equilibria of nitrate based ionic liquid + alkane + benzene at 298.15 K: Experiments and correlation
• Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
• (Liquid-liquid) equilibria for ternary and quaternary systems of representative compounds of gasoline + methanol at 293.15 K: Experimental data and correlation
• 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
• Standard reference data for the air-liquid and vapor-liquid surface tension of benzene
• Phase equilibria of binary mixtures (ionic liquid + aromatic hydrocarbon): Effect of the structure of the components on the solubility
• Liquid-liquid equilibria of binary systems {benzene + [x-Mim][NTf2]ionic liquid}: Experimental data and thermodynamic modeling usinga group contribution equation of state
• Phase equilibria and excess molar enthalpies study of the binary systems (pyrrole + hydrocarbon, or an alcohol) and modeling
• Experimental data, correlation and prediction of the extraction of benzene from cyclic hydrocarbons using [Epy][ESO4] ionic liquid
• 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 equilibrium data for ternary mixtures composed of n-hexane, benzene and acetonitrile at (298.15, 308.15, and 318.15) K
• Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
• Present status of the modified UNIFAC Model for the prediction of phase equilibria and excess enthalpies for systems with ionic liquids
• 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
• Extraction of benzene, ethylbenzene, and xylenes from n-heptane using binary mixtures of [4empy][Tf2N] and [emim][DCA] ionic liquids
• 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
• Liquid liquid equilibria in the ternary systems {hexadecane + BTX aromatics + 2-methoxyethanol or acetonitrile} at 298.15 K
• Separation of benzene and thiophene with a mixture of N-methyl-2- pyrrolidinone (NMP) and ionic liquid as the entrainer
• The ionic liquid 1-ethyl-3-methylimidazolium tris(pentafluoroethyl) trifluorophosphate as alternative extractant for BTEX separation
• Liquid-liquid phase diagrams of poly(ethylene glycol) and aromatic hydrocarbons
• Phase equilibria of three binary systems containing 2,5-dimethylthiophene and 2-ethylthiophene in hydrocarbons
• Extraction of benzene from heptane with pyridinium based ionic liquid at (298.15, 308.15 and 318.15) K
• 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
• Study of the suitability of two ammonium-based ionic liquids for the extraction of benzene from its mixtures with aliphatic hydrocarbons.
• Vapor-liquid equilibria for n-heptane + (benzene, toluene, pxylene, or ethylbenzene) + {[4empy][Tf2N] (0.3) + [emim][DCA] (0.7)} binary ionic liquid mixture
• Application of the ionic liquid tributylmethylammonium bis(trifluoromethylsulfonyl)imide as solvent for the extraction of benzene from octane and decane at T = 298.15 K and atmospheric pressure
• Quantitative comparison between predicted and experimental binary n-alkane p benzene phase behaviors using cubic and PC-SAFT EOS
• Determination of solubility parameters from density measurements for non-polar hydrocarbons at temperatures from (298 to 433) K and pressures up to 137 MPa
• Determination and correlation of solubility of N-methyl-3,4,5- trinitropyrazole (MTNP) in ten pure solvents from 283.15 K to 323.15 K
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• 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
• 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
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
• Effective extraction of benzene and thiophene by novel deep eutectic solvents from hexane / aromatic mixture at different temperatures
• Measurement and modeling of infinite dilution activity coefficients of organic compounds in an equimolar ionic liquid mixture of [Bmim]Cl and [Bmim][Tf2N]
• Gas solubilities of nitrogen or oxygen in benzene, divinylbenzene, styrene and of an equimolar (N2:O2) mixture in styrene at (293-313) K
• Separation abilities of three acetate-based ionic liquids for benzene-methanol mixture through vapor-liquid equilibrium experiment at 101.3 kPa
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• The determination of activity coefficients at infinite dilution using g.l.c. for hydrocarbons in furfural at T = 278:15 K and T = 298:15 K
• (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
• Activity coefficients at infinite dilution for hydrocarbons in furfuryl alcohol at T=(278.15 and 298.15) K, determined by g.l.c.
• Speed of sound in liquid tetrachloromethane and benzene at temperatures from 283.15 K to 333.15 K and pressures up to 30 MPa
• Ternary (liquid + liquid) equilibria for mixtures of 1-hexyl-3-methylimidazolium (tetrafluoroborate or hexafluorophosphate) + benzene + an alkane at T = 298.2 K and p = 0.1 MPa
• 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
• 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 phase behaviour of 1-hexyloxymethyl-3-methyl-imidazolium-based ionic liquids with hydrocarbons: The influence of anion
• The (p,q,T) of (methanol + benzene) and (methanol + ethylbenzene)
• Influence of size and shape effects on the high-pressure solubility of n-alkanes: Experimental data, correlation and prediction
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid hexyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)-imide using g.l.c. at T = (298.15, 313.15, and 333.15) K
• 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
• 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)
• Measurement of activity coefficients at infinite dilution using polar and non-polar solutes in the ionic liquid 1-methyl-3-octyl-imidazolium diethyleneglycolmonomethylethersulfate at T = (288.15, 298.15, and 313.15) K
• Phase equilibrium properties of binary and ternary systems containing di-isopropyl ether + 1-butanol + benzene at 313.15 K
• Sound speed and density measurements for tetra-n-butylammonium bromide in benzene and carbon tetrachloride solutions at T = 298.15 K
• Azeotropic behaviour of (benzene + cyclohexane + chlorobenzene) ternary mixture using chlorobenzene as entrainer at 101.3 kPa
• 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 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
• Study of activity coefficients for sodium iodide in (methanol + benzene) system by (vapour + liquid) equilibrium measurements
• 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 and excess volumes of binary mixtures of N,N-dimethylformamide with aromatic hydrocarbon at different temperature
• A study on densities and excess volumes in the (c-butyrolactone + aromatic hydrocarbon) system at various temperatures
• (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
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• Effects of the presence of ethylacetate or benzene on the densities and volumetric properties of mixture (styrene + N,N-dimethylformamide)
• Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
• Phase diagrams of (vapour + liquid) equilibrium for binary mixtures of a,a,a-trifluorotoluene with ethanol, or benzene, or chloroform at pressure 101.4 kPa
• 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
• p, Vm, T) measurements of (octane + benzene) at temperatures from (298.15 to 328.15) K and at pressures up to 40 MPa
• Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid trihexyltetradecylphosphonium-bis-(2,4,4-trimethylpentyl)- phosphinate using g.l.c. at T = (303.15, 308.15, 313.15, and 318.15) K
• 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
• Experimental and theoretical study of surface tension of binary mixtures of (n-alkyl acetates + heptane, benzene, and toluene)
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
• Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
• Experimental densities, refractive indices, and speeds of sound of 12 binary mixtures containing alkanes and aromatic compounds at T = 313.15 K
• Volumetric properties of binary liquid mixtures: Application of the Prigogine Flory Patterson theory to excess molar volumes of dichloromethane with benzene or toluene
• (Liquid + liquid) equilibria for ternary mixtures of (alkane + benzene + [EMpy] [ESO4]) at several temperatures and atmospheric pressure
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
• 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
• Separation of benzene from alkanes using 1-ethyl-3-methylpyridinium ethylsulfate ionic liquid at several temperatures and atmospheric pressure: Effect of the size of the aliphatic hydrocarbons
• (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 of (sulfolane + benzene + n-hexane), (N-formylmorpholine + benzene + n-hexane), and (sulfolane + N-formylmorpholine + benzene + n-hexane) at temperatures ranging from (298.15 to 318.15) K: Experimental results and correlation
• LLE data for the ionic liquid 3-methyl-N-butyl pyridinium dicyanamide with several aromatic and aliphatic hydrocarbons
• 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
• Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
• Thermochemistry of ionic liquid-catalysed reactions. Isomerisation and transalkylation of tert-alkyl-benzenes. Are these systems ideal?
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate [EMIM][TCB] using gas liquid chromatography
• (Vapour + liquid) equilibria of ternary systems with ionic liquids using headspace gas chromatography
• Separation of benzene from alkanes by solvent extraction with 1-ethylpyridinium ethylsulfate ionic liquid
• 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
• (Liquid + liquid) equilibria for mixtures of (ethylene glycol + benzene + cyclohexane) at temperatures (298.15, 308.15, and 318.15) K
• Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
• Thermodynamic properties of chiral fenchones in some solutions at T = 298.15 K
• 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
• 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}
• Measurement of (liquid + liquid) equilibria for ternary systems of (N-formylmorpholine + benzene + cyclohexane) at temperatures (303.15, 308.15, and 313.15) K
• 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
• Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
• Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• 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
• Evaluation of the ionic liquids 1-alkyl-3-methylimidazolium hexafluorophosphate as a solvent for the extraction of benzene from cyclohexane: (Liquid + liquid) 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
• (Liquid + liquid) equilibria of {benzene + cyclohexane + two ionic liquids} at different temperature and atmospheric pressure
• 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
• Experimental study on vapor-liquid equilibria of ternary systems of hydrocarbons/ionic liquid using headspace gas chromatography
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
• Henry s constants and activity coefficients of some organic solutes in 1-butyl,3-methylimidazolium hydrogen sulfate and in 1-methyl,3-trimethylsilylmethylimidazolium chloride
• 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
• 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
• Phase equilibria study of the (N-octylisoquinolinium thiocyanate ionic liquid + aliphatic and aromatic hydrocarbon, or thiophene) binary systems
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography at T = (313.15, 333.15, 353.15 and 373.15) K
• Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
• 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
• Recommended sublimation pressure and enthalpy of benzene
• 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
• Experimental and predicted data of excess molar enthalpies and excess molar volumes for the ternary system (1,3-dichlorobenzene + benzene + 1-chlorohexane) at T = 298.15 K
• (Liquid + liquid) equilibrium at T = 298.15 K for ternary mixtures of alkane + aromatic compounds + imidazolium-based ionic liquids
• 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
• Excess enthalpy for the (benzene + cyclohexane) mixture over a wide range of temperature and pressure
• Thermodynamics of solvation in propylene glycol and methyl cellosolve
• Pressure dependence of excess enthalpy for (benzene + cyclohexane) mixture near the critical locus at T = (558.2, 563.2 and 573.2) K and p = (3 to 15) MPa
• Phase equilibria study of binary systems comprising an (ionic liquid + hydrocarbon)
• (Liquid + liquid) equilibria for (benzene + cyclohexane + dimethyl sulfoxide) system at T = (298.15 or 303.15) K: Experimental data and correlation
• Excess heat capacities of mixtures containing 1-methylpyrrolidin-2-one, chlorotoluenes and benzene
• 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
• (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)
• 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
• Determination and correlation of (liquid + liquid) equilibria of ternary and quaternary systems with octane, decane, benzene and [BMpyr][DCA] at T = 298.15 K and atmospheric pressure
• Theoretical and experimental study on volumetric and electromagnetic properties of binary systems consisting of 1,2-dichloroethane with benzene and its derivatives at T = (293.15 to 333.15) K
• Selective recovery of aliphatics from aromatics in the presence of the {[4empy][Tf2N] + [emim][DCA]} ionic liquid mixture
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Comparative study of the LLE of the quaternary and ternary systems involving benzene, n-octane, n-decane and the ionic liquid [BMpyr] [NTf2]
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
• Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-hexyl-2,3-dimethylimidazolium bis(trifluoromethylsulfonyl)imide
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Experimental determination of the LLE data of systems consisting of {hexane + benzene + deep eutectic solvent} and prediction using the Conductor-like Screening Model for Real Solvents
• Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• 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
• The contour of excess molar enthalpy at a mole fraction of benzene x = 0.548 on the p-T plane in liquid state and near the critical points for the (benzene + cyclohexane) mixture
• 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
• Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
• Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
• Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
• Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
• Studies of partial molar volumes of alkylamine in non-electrolyte solvents I. Alkylamines in hydrocarbons at 303.15 and 313.15K
• Thermophysical properties of the binary mixtures of 2-methyl-tetrahydrofuran with benzene and halobenzenes
• Excess volumes, densities, speeds of sound and viscosities for the binary systems of diisopropyl ether with hydrocarbons at 303.15K
• Solubility data for benzene in aqueous solutions of methyldiethanolamine (MDEA) and of diglycolamine (DGA)
• Liquid liquid equilibria for mixtures of (ethylene carbonate + aromatic hydrocarbon + cyclohexane)
• Thermophysical properties and thermodynamic phase behavior of ionic liquids
• Molecular interactions in binary mixtures containing o-toluidine
• Volumetric and transport properties of ternary mixtures containing 1-propanol + ethyl ethanoate + cyclohexane or benzene at 303.15 K: Experimental data, correlation and prediction by ERAS model
• Excess molar volumes and excess isentropic compressibilities of 2-pyrrolidinone at 308.15K
• Excess molar volumes and isentropic compressibilities changes of mixing of tetrahydropyran + benzene + cyclo or n-alkanes ternary mixtures at 308.15 K
• 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
• Volumetric and Acoustic Properties of Binary Mixtures of Cyclohexane + Benzene and + Benzaldehyde at (293.15 to 323.15) K
• Temperature dependence of densities, speeds of sound, and derived properties of cyclohexylamine + cyclohexane or benzene in the range (293.15 to 323.15) K
• 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
• Extension of the DSC method to measuring vapor pressures of narrow boiling range oil cuts
• 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
• Low cost apparatus for rapid boiling point determination of small air sensitive samples under inert atmosphere
• Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
• Vapor Liquid Equilibrium Data for Binary Systems of N,N-Dimethylacetamide with Cyclohexene, Cyclohexane, and Benzene Separately at Atmospheric Pressure
• Investigation of Surface and Solubility Properties of N-Vinylimidazolium Tetrahalogenidoferrate(III) Magnetic Ionic Liquids Using Density Functional Theory
• Liquid Liquid Equilibrium data for the ternary systems of Water, Isopropyl alcohol, and selected entrainers
• Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
• Isothermal Vapor Liquid Equilibrium Data for the Methanol + Benzene + Tetraphenylphosphonium Chloride System
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Equilibrium Study on the Extraction of Levulinic Acid from Aqueous Solution with Aliquat 336 Dissolved in Different Diluents: Solvent s Polarity Effect and Column Design
• Determination and Correlation of Solubility of 3,4-Dinitro-1H-pyrazole in Different Pure Solvents from 298.15 K to 338.15 K
• Mutual solubility of aromatic hydrocarbons in pyrrolidinium and ammonium-based ionic liquids and its modeling using the Cubic-Plus-Association (CPA) Equation of State
• Isobaric Vapor Liquid Equilibrium for Binary and Ternary Systems of Isoamyl Alcohol + Isoamyl Acetate + Dimethyl Sulfoxide at 101.33 kPa
• Isobaric Vapor Liquid Equilibrium for Binary Systems of Cyclohexanone + Benzene, Cyclohexanone + Toluene, and Cyclohexanone + p-Xylene at 101.3 kPa
• Vapor-Liquid Equilibrium for Binary Systems of Allyl Alcohol + Water and Allyl Alcohol + Benzene at 101.3 kPa
• Solvent Polarity Effect when Amberlite-LA2 Is Used in the Extraction of Picric Acid
• Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
• The Critical Temperatures of a Number of (i) (Chloroalkane (C3 C4) + Hydrocarbon (C6 C7)) Binary Mixtures and (ii) (Aromatic Halocarbon (Chlorobenzene, Fluorobenzene, 1,2-Dichlorobenzene, or 1,3-Dichlorobenzene) + Alkane (C8)) Binary Mixtures
• Solid Liquid Phase Equilibrium of N,N'-Piperazinebis(neopentylglycol)phosphoramidate in Selected Solvents from T = (293.15 to 333.15) K
• Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
• Liquid-Liquid Equilibrium in the Ternary Systems Water + Cyclohexanone + Benzene or Methyl Isobutyl Carbinol at 303.15 and 323.15 K: Experimental Data and Correlation
• Solubility in Different Solvents, Crystal Polymorph and Morphology, and Optimization of Crystallization Process of AIBN
• Synthesis and Solubility of 5,5-Dimethyl-2-(phenyl(phenylamino)methyl)-1,3,2-dioxaphosphinane 2-oxide in Selected Solvents between 278.15 K and 347.15 K
• Measurement and Correlation of the Solubilities of Sulfur S8 in 10 Solvents
• Measurement and Correlation of the Dissolution Equilibria of o-Iodoaniline and p-Iodoaniline in Pure Solvents
• 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
• Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
• 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)]
• Effect of Diluents on Extraction Equilibrium of trans-Aconitic Acid
• Thermodynamic Studies of Solubility for Naphthalene in 12 Solvents from 279 to 330 K
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• Solubility and Thermodynamic Modeling of Sulfanilamide in 12 Mono Solvents and 4 Binary Solvent Mixtures from 278.15 to 318.15 K
• 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
• Thermodynamic Properties of Mixtures Containing Precursors of Vitamin B5
• Vapor-Liquid Equilibria for Four Binary Systems at 363.15 K: N-Methylformamide + Hexane, + Benzene, + Chlorobenzene, and + Acetonitrile
• Excess Molar Enthalpies of Propyl Propanoate + 1-Hexanol + Benzene at the Temperatures of 25 :C and 35 :C
• Solubility of 1-Alkyl-3-methylimidazolium Hexafluorophosphate in Hydrocarbons
• Excess Molar Enthalpies for the Binary Systems of Benzene or Cyclohexane with 1,1-Diethoxyethane at 323.15 K or with 2,2-Dimethoxybutane at 303.15 K and Infinite Dilution Activity Coefficients in 1,1-Diethoxyethane
• Infinite Dilution Activity Coefficients of Hydrocarbons in Triethylene Glycol and Tetraethylene Glycol
• An apparatus for the on-line GC determination of hydrocarbon solubility in water: benzene and cyclohexane from 70 C to 150 C
• Excess Molar Enthalpies and Excess Molar Volumes of the Ternary System 1,2-Dichlorobenzene + Benzene +1-Chlorohexane at 298.15 K
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Hexyl-3-methylimidazolium Hexafluorophosphate from Gas-Liquid Chromatography
• Measurement of Activity Coefficients of Solutes at Infinite Dilution in (Dimethyl Sulfoxide + Acetamide, or Formamide, or Urea) Using Gas Liquid Chromatography at the Temperature 298.15 K
• Densities, Viscosities, and Thermodynamic Properties of (N,N-Dimethylformamide + Benzene + Chlorobenzene) Ternary Mixtures at (298.15, 303.15, 308.15, and 313.15) K
• Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid 1-Hexyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography at the Temperatures 298.15 K and 323.15 K
• 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
• Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
• Vapor-Liquid Equilibria of the Binary System 1-Pentanol + Anisole and the Quaternary System Benzene+Cyclohexane+1-Pentanol+Anisole at 101.32 kPa
• 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
• Solubility of Alkylbenzenes and a Model for Predicting the Solubility of Liquid Organics in High-Temperature Water
• Measurement and Prediction of Excess Molar Enthalpies and Excess Molar Volumes of the Ternary System 1,3-dichlorobenzene + Benzene + Hexane at 298.15 K.
• Measurement and Prediction of Solubility of Four Arylamine Molecules in Benzene, Hexane, and Methanol
• Phase Separation in Binary Mixtures Containing Linear Perfluoroalkanes
• Vapor-Liquid Equilibria and Excess Enthalpies for Binary Systems of Dimethoxymethane with Hydrocarbons
• Determination of Activity Coefficients at Infinite Dilution of Polar and Nonpolar Solutes in the Ionic Liquid 1-Ethyl-3-methyl- imidazolium Bis(trifluoromethylsulfonyl) Imidate Using Gas-Liquid Chromatography at the Temperature 303.15 K or 318.15 K
• 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 for Benzene + 2-Methylpentane and Allyl Alcohol + 1-Propanol
• 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
• Influence of High Pressure on the Liquidus Curve Shape in Binary Hydrocarbon Mixtures: Experimental Data, Correlation, and Prediction
• Isothermal Vapor-Liquid Equilibrium Data for the System Methanol + Benzene + Sodium Tetraphenylborate
• Isobaric Vapor-Liquid Equilibria for Binary Mixtures of 1,2-Dibromoethane with Benzene, Toluene, Fluorobenzene, and Bromobenzene at Atmospheric Pressure
• Densities, Viscosities, and Refractive Indices of Binary Mixtures of Anisole with Benzene, Methylbenzene, Ethylbenzene, Propylbenzene, and Butylbenzene at (293.15 and 303.15) K
• Vapor-Liquid Equilibrium of Binary and Ternary Mixtures Containing Isopropyl Ether, 2-Butanol, and Benzene at T ) 313.15 K
• 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
• Vapor Pressures and Activity Coefficients of n-Alcohols and Benzene in Binary Mixtures with 1-Methyl-3-Butyl-Imidazolium Octylsulfate and 1-Methyl-3-Octyl-Imidazolium Tetrafluoroborate
• 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
• Liquid-Liquid Equilibria for Ternary Mixtures (an Ionic Liquid + Benzene +Heptane or Hexadecane) at T ) 298.2 K and Atmospheric Pressure
• Determination and Study of the Solubility of Methane in Mixtures of Methanol plus Various Hydrocarbons at High Pressures
• Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• 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
• 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
• Ternary Liquid-Liquid Equilibria for Mixtures of an Aromatic + an Aliphatic Hydrocarbon + 4-Methyl-N-butylpyridinium Tetrafluoroborate
• 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
• Solid-Liquid Equilibria for Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-Butoxy Ethanol
• 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
• Infinite Dilution Activity Coefficients for Trihexyltetradecyl Phosphonium Ionic Liquids: Measurements and COSMO-RS Prediction
• Measurement and Correlation of CO2 Solubility in the Systems of CO2 + Toluene, CO2 + Benzene, and CO2 + n-Hexane at Near-Critical and Supercritical Conditions
• Solubilities of Triphenylphosphine in Ethanol, 2-Propanol, Acetone, Benzene, and Toluene
• 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
• Volumetric Properties of the Binary Methanol + Chloroform and Ternary Methanol + Chloroform + Benzene Mixtures at (288.15, 293.15, 298.15, 303.15, 308.15, and 313.15) 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 Equilibrium of Ternary and Quaternary Systems Including Methyl Acetate, Benzene, Toluene, and Water at 283.2 K under Atmosphere
• Cosolvent Selection for Benzene-Cyclohexane Separation in Extractive Distillation
• Isobaric Vapor-Liquid Equilibria for Binary Systems of Acetic Acid + Benzene, Chloroacetic Acid + Benzene, and Dichloroacetic Acid + Benzene at 101.33 kPa
• Separation of Benzene from Linear Alkanes (C6-C9) Using 1-Ethyl-3-Methylimidazolium Ethylsulfate at T = 298.15 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
• Calorimetric Study of Nitrile Group-Solvent Interactions and Comparison with Dispersive Quasi-Chemical (DISQUAC) Predictions
• Liquid Extraction of Benzene from Its Mixtures Using 1-Ethyl-3-methylimidazolium Ethylsulfate as a Solvent
• 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
• 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
• Measuring the Aqueous Henry's Law Constant at Elevated Temperatures Using an Extended EPICS Technique
• Liquid-Liquid Equilibria of the Ternary Systems of Alkane + Aromatic + 1-Ethylpyridinium Ethylsulfate Ionic Liquid at T = (283.15 and 298.15) K
• Liquid-Liquid Equilibria Measurement of Systems Involving Alkanes (Heptane and Dodecane), Aromatics (Benzene or Toluene), and Furfural
• 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
• Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
• 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
• Viscometric Behavior of Binary Mixtures of Butan-2-one with Benzene at T = (303.15, 313.15, and 323.15) K
• Densities and Viscosities of [Bmim][PF6] and Binary Systems [Bmim][PF6] + Ethanol, [Bmim][PF6] + Benzene at Several Temperatures and Pressures: Determined by the Falling-Ball Method
• Isothermal Vapor-Liquid Equilibrium for Methanol and 2,3-Dimethyl-1-butene at 343.06 K, 353.27 K, 363.19 K, and 372.90 K
• 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
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Ethyl-3-methylimidazolium Diethylphosphate Using Gas Liquid Chromatography
• Extraction of Benzene from Aliphatic Compounds Using Commercial Ionic Liquids as Solvents: Study of the Liquid Liquid Equilibrium at T = 298.15 K
• 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
• Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
• 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
• 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
• 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
• Liquid Liquid Extraction of Aromatic Compounds from Cycloalkanes Using 1-Butyl-3-methylimidazolium Methylsulfate Ionic Liquid
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• 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
• 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
• Solubilities of Phosphonic Acid, P,P'-(1,4-Piperazinediyl)bis-,P,P,P',P'-tetraphenyl Ester in Selected Solvents
• Liquid Liquid Equilibria for the Ternary Systems of Perfluamine + Hydrofluoroether + Benzene, Toluene, or Xylene at 298.15 K or 313.15 K
• Liquid Liquid Equilibria of Benzene + n-Heptane + N,N-Dimethylformamide and Benzene + n-Heptane + N,N-Dimethylformamide + Ammonium Thiocyanate
• Solid Liquid Phase Equilibria of N,N'-[1,3-Phenylenebis(methylene)]bis(phosphoramidic acid) P,P,P',P'-Tetraphenyl Ester in 10 Pure Solvents
• Excess Heat Capacities of Binary and Ternary Mixtures Containing 1-Ethyl-3-methylimidazolium Tetrafluoroborate and Anilines
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Investigation of Surface Properties and Solubility of 1-Vinyl-3-alkyl/Esterimidazolium Halide Ionic Liquids by Density Functional Methods
• Liquid Liquid Equilibria for the Systems: Heptane + Benzene + Solvent (Propylene carbonate, N,N-Dimethylformamide, or Mixtures) at Temperatures from (303.2 to 323.2) K
• Comparison Study on Temperature Dependence of the Interfacial Tension of n-Alkane Water and n-Alcohol Water Two Binary Systems
• Thermodynamic Properties of Ternary Liquid Mixtures Containing o-Chlorotoluene: Excess Molar Volumes and Excess Isentropic Compressibilities
• Liquid Liquid Equilibria of Three Ternary Systems: {Glycerol + Benzene + Methanol}, {Glycerol + Benzene + Ethanol}, and {Glycerol + Benzene + 1-Propanol}
• Thermal Stability and Vapor Liquid Equilibrium for Imidazolium Ionic Liquids as Alternative Reaction Media
• Solution Thermodynamics of Imidazolium-Based Ionic Liquids and Volatile Organic Compounds: Benzene and Acetone
• Selective Separation of Aromatics from Paraffins and Cycloalkanes Using Morpholinium-Based Ionic Liquid
• Solid Liquid Phase Equilibrium of Phosphoramidic acid, N,N'-1,2-Ethanediylbis-P,P,P',P'-tetraphenyl Ester in Selected Solvents
• Speed of Sound Measurements in Ethanol and Benzene over the Temperature Range from (253.2 to 353.2) K at Pressures up to 30 MPa
• Measurement and Correlation of the Solubility for 4,4'-Diaminodiphenylmethane in Different Solvents
• 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
• Isothermal Vapor-Liquid Equilibrium at 333.15 K, Density, and Refractive Index at 298.15 K for the Ternary Mixture of Dibutyl Ether + Ethanol + Benzene and Binary Subsystems
• Experimental Isobaric Vapor-Liquid Equilibria of Binary Mixtures of 2,2,2-Trifluoroethanol with Benzene or Toluene
• Measurement of Activity Coefficient at Infinite Dilution of Hydrocarbons in Sulfolane Using Gas-Liquid Chromatography
• Solubility of Chlorpheniramine Maleate in Ethanol, 1-Propanol, 1-Butanol, Benzene, Ethyl Acetate, Ethyl Formate, and Butyl Acetate between 283 K and 333 K
• Isothermal Phase Equilibria and Excess Molar Enthalpies for Binary Systems with Dimethyl Ether at 323.15 K
• Solubility of Phenacetinum in Methanol, Ethanol, 1-Propanol, 1-Butanol, 1-Pentanol, Tetrahydrofuran, Ethyl Acetate, and Benzene between 282.65 K and 333.70 K
• Excess Enthalpies of Chloroalkylbenzene + Alkylbenzene Mixtures
• Densities and Excess Molar Volumes of the Binary 1-Propanol + Chloroform and 1-Propanol + Benzene and Ternary 1-Propanol + Chloroform + Benzene Mixtures at (288.15, 293.15, 298.15, 303.15, 308.15, and 313.15) K
• Densities of Ionic Liquids, 1-Butyl-3-methylimidazolium Hexafluorophosphate and 1-Butyl-3-methylimidazolium Tetrafluoroborate, with Benzene, Acetonitrile, and 1-Propanol at T = (293.15 to 343.15) K
• Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• 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
• 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
• Solubility of 2-(4-Ethylbenzoyl)benzoic Acid in Eleven Organic Solvents between 279.55 K and 343.15 K
• Mutual Solubility Measurements of Hydrocarbon-Water Systems Containing Benzene, Toluene, and 3-Methylpentane
• Diffusion Coefficients of Organic Compounds at Infinite Dilution in Mixtures Involving Associating Compounds. Experimental Determination and Modeling by Group Contribution Methods
• 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
• 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
• 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
• Liquid-Liquid Equilibria for Benzene + Cyclohexane + 1-Methyl-3-methylimidazolium Dimethylphosphate or + 1-Ethyl-3-methylimidazolium Diethylphosphate
• 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
• Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
• Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid, Trihexyltetradecylphosphonium Bis(trifluoromethylsulfonyl) Imide, Using Gas-Liquid Chromatography at T ) (303.15, 308.15, 313.15, and 318.15) K
• Densities and Excess Molar Volumes of the Ternary Mixture 2-Butanol + Chloroform + Benzene and Binary Mixtures 2-Butanol + Chloroform, or + Benzene over the Temperature Range (288.15 to 313.15) K
• 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
• Ternary Liquid-Liquid Equilibria Measurement for Benzene + Cyclohexane + N-Methylimidazole, or N-Ethylimidazole, or N-Methylimidazolium Dibutylphosphate at 298.2 K and Atmospheric Pressure
• 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
• Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water)
• Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
• Solubility of Fluorene in Benzene, Chloroform, Acetone, 1-Propanol, Isobutanol, and Methylbenzene from (283 to 323) K
• Solubility of Acenaphthene in Different Solvents from (283.00 to 323.00) K
• Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
• 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
• Liquid Viscosities of Cyclohexane, Cyclohexane + Tetradecane, and Cyclohexane + Benzene from (313 to 393) K and Pressures Up to 60 MPa
• Volumetric Behavior of the Binary Mixtures of Methyl Ethyl Ketone with n-Hexane, Cyclohexane, and Benzene at T ) (303.15, 313.15, and 323.15) K
• Liquid Viscosities of the Ternary System Benzene + Cyclohexane + n-Tetradecane from (313 to 393) K and Pressures up to 60 MPa
• Isobaric Vapor-Liquid Equilibria for the Binary Systems Benzene + Methyl Ethanoate, Benzene + Butyl Ethanoate, and Benzene + Methyl Heptanoate at 101.31kPa
• Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes and Aromatic Compounds at T = 313.15 K
• Densities of Ionic Liquid [BMIM][BF4] + Ethanol, + Benzene, and + Acetonitrile at Different Temperature and Pressure
• Densities and Viscosities of Binary Mixtures of Methyl 4-Chlorobutyrate with Aromatic Hydrocarbons at T ) (298.15 to 318.15) K
• 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
• 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
• Ternary Liquid-Liquid Equilibria Measurement for Hexane and Benzene with the Ionic Liquid 1-Butyl-3-methylimidazolium Methylsulfate at T = (298.2, 313.2, and 328.2) K
• Liquid-Liquid Equilibria for Benzene + Cyclohexane + 1-Butyl-3-methylimidazolium Hexafluorophosphate
• Solubilities of 3,9-Dimethyl-3,9-dioxide-2,4,8,10-tetraoxa-3,9-diphosphaspiro[5.5]undecane in Selected 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
• Excess Molar Enthalpies of Dibromomethane with Benzene, Methanol, Dimethylsulfoxide, and Pyrrolidin-2-one at 303.15 K
• 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
• Thermal Conductivity Measurement of Polyglycol Alkyl Ethers at Temperatures from (303.15 to 393.15) K
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
• Physical Properties of Binary Mixtures of Ethyl Formate with Benzene, Isopropyl Benzene, Isobutyl Benzene, and Butylbenzene at (303.15, 308.15, and 313.15) K
• Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
• 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
• Thermodynamic Properties of Binary and Ternary Mixtures Containing Di-isopropyl Ether, 2-Propanol, and Benzene at T = 313.15 K
• Mutual Solubility of Pyridinium-Based Tetrafluoroborates and Toluene
• Density and Viscosity of Propyl Formate + Aromatic Hydrocarbons at T = (303.15, 308.15, and 313.15) K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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