Chemical Properties of Ethylbenzene (CAS 100-41-4)

InChI

InChI=1S/C8H10/c1-2-8-6-4-3-5-7-8/h3-7H,2H2,1H3

InChI Key

YNQLUTRBYVCPMQ-UHFFFAOYSA-N

Formula

C8H10

SMILES

CCc1ccccc1

Molecular Weight¹

106.17

CAS

100-41-4

Other Names

• .alpha.-methyltoluene
• Aethylbenzol
• Benzene, ethyl-
• EB
• Ethylbenzeen
• Ethylbenzol
• Etilbenzene
• Etylobenzen
• NCI-C56393
• NSC 406903
• Phenylethane
• UN 1175
• «alpha»-Methyltoluene
• «alpha»-Methyltoluene

• 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).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_c,grossH : Heat of Combustion, Gross form (kJ/mol).
• Δ_c,netH : Heat of Combustion, Net Form (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_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_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°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• Δ_vapS : Entropy of vaporization at a given temperature (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_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

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

Physical Properties

Property	Value	Unit	Source
ω	0.3020		KDB
PAff	[788.00; 789.90]	kJ/mol
PAff	788.00	kJ/mol	NIST
PAff	789.90	kJ/mol	NIST
Tig	733.15	K	KDB
BasG	[760.20; 760.30]	kJ/mol
BasG	760.30	kJ/mol	NIST
BasG	760.20	kJ/mol	NIST
Cp,liquid	185.44	J/mol×K	Thermod...
μ	0.40	debye	KDB
LFL	1.00	% in Air	KDB
UFL	6.70	% in Air	KDB
Tflash,cc	299.82	K	KDB
Tflash,oc	288.15	K	KDB
ΔfG°	130.70	kJ/mol	KDB
Rg	3.8210		KDB
Δc,grossH	4564.87	kJ/mol	KDB
Δc,netH	4344.792	kJ/mol	KDB
ΔfH°gas	[29.80; 69.30]	kJ/mol
ΔfH°gas	29.81	kJ/mol	KDB
ΔfH°gas	29.80 ± 0.84	kJ/mol	NIST
ΔfH°gas	49.00 ± 4.00	kJ/mol	NIST
ΔfH°gas	69.30	kJ/mol	NIST
ΔfH°liquid	[-12.50; 27.00]	kJ/mol
ΔfH°liquid	-12.50 ± 0.84	kJ/mol	NIST
ΔfH°liquid	6.80 ± 4.00	kJ/mol	NIST
ΔfH°liquid	27.00	kJ/mol	NIST
ΔfusH°	10.52	kJ/mol	Joback Calculated Property
ΔvapH°	35.68	kJ/mol	Joback Calculated Property
IE	[8.61; 9.38]	eV
IE	8.77 ± 0.01	eV	NIST
IE	8.77	eV	NIST
IE	8.61	eV	NIST
IE	8.65 ± 0.10	eV	NIST
IE	8.76	eV	NIST
IE	8.77 ± 0.01	eV	NIST
IE	8.75 ± 0.05	eV	NIST
IE	8.76 ± 0.01	eV	NIST
IE	8.77 ± 0.01	eV	NIST
IE	8.77	eV	NIST
IE	8.73	eV	NIST
IE	Outlier 9.38	eV	NIST
log10WS	[-2.77; -2.77]
log10WS	-2.77		Aq. Sol...
log10WS	-2.77		Estimat...
logPoct/wat	2.249		Crippen Calculated Property
McVol	99.820	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	2		KDB
Pc	3609.00	kPa	KDB
ρc	[283.46; 284.52]	kg/m3
ρc	284.52 ± 1.06	kg/m3	NIST
ρc	283.46 ± 4.25	kg/m3	NIST
Inp	[118.30; 893.00]
Inp	850.60		NIST
Inp	844.50		NIST
Inp	846.80		NIST
Inp	843.40		NIST
Inp	841.80		NIST
Inp	843.50		NIST
Inp	848.10		NIST
Inp	866.85		NIST
Inp	879.95		NIST
Inp	847.30		NIST
Inp	875.40		NIST
Inp	848.34		NIST
Inp	848.34		NIST
Inp	859.20		NIST
Inp	861.00		NIST
Inp	847.00		NIST
Inp	850.00		NIST
Inp	848.00		NIST
Inp	854.80		NIST
Inp	871.10		NIST
Inp	880.00		NIST
Inp	847.80		NIST
Inp	848.10		NIST
Inp	848.10		NIST
Inp	848.20		NIST
Inp	847.60		NIST
Inp	849.00		NIST
Inp	874.00		NIST
Inp	848.00		NIST
Inp	848.00		NIST
Inp	859.00		NIST
Inp	859.00		NIST
Inp	848.00		NIST
Inp	875.00		NIST
Inp	858.40		NIST
Inp	863.30		NIST
Inp	857.30		NIST
Inp	857.00		NIST
Inp	844.60		NIST
Inp	849.70		NIST
Inp	834.60		NIST
Inp	839.80		NIST
Inp	858.00		NIST
Inp	840.00		NIST
Inp	859.00		NIST
Inp	860.00		NIST
Inp	832.80		NIST
Inp	838.50		NIST
Inp	857.00		NIST
Inp	858.00		NIST
Inp	859.00		NIST
Inp	849.00		NIST
Inp	833.30		NIST
Inp	870.00		NIST
Inp	857.00		NIST
Inp	859.00		NIST
Inp	857.00		NIST
Inp	860.00		NIST
Inp	854.00		NIST
Inp	848.00		NIST
Inp	845.00		NIST
Inp	847.80		NIST
Inp	848.20		NIST
Inp	851.40		NIST
Inp	859.00		NIST
Inp	867.00		NIST
Inp	854.00		NIST
Inp	859.00		NIST
Inp	864.00		NIST
Inp	870.00		NIST
Inp	821.00		NIST
Inp	845.30		NIST
Inp	847.70		NIST
Inp	858.90		NIST
Inp	864.20		NIST
Inp	870.10		NIST
Inp	846.00		NIST
Inp	834.10		NIST
Inp	839.50		NIST
Inp	844.60		NIST
Inp	844.60		NIST
Inp	844.80		NIST
Inp	845.30		NIST
Inp	839.40		NIST
Inp	840.60		NIST
Inp	839.00		NIST
Inp	839.20		NIST
Inp	845.30		NIST
Inp	847.70		NIST
Inp	850.00		NIST
Inp	844.00		NIST
Inp	844.00		NIST
Inp	855.20		NIST
Inp	837.00		NIST
Inp	839.00		NIST
Inp	841.56		NIST
Inp	864.00		NIST
Inp	866.00		NIST
Inp	870.00		NIST
Inp	873.00		NIST
Inp	868.00		NIST
Inp	872.00		NIST
Inp	875.00		NIST
Inp	877.00		NIST
Inp	880.00		NIST
Inp	850.00		NIST
Inp	835.00		NIST
Inp	840.00		NIST
Inp	849.10		NIST
Inp	849.10		NIST
Inp	849.10		NIST
Inp	849.10		NIST
Inp	849.10		NIST
Inp	849.10		NIST
Inp	847.70		NIST
Inp	848.00		NIST
Inp	843.00		NIST
Inp	846.00		NIST
Inp	850.00		NIST
Inp	852.00		NIST
Inp	855.00		NIST
Inp	859.00		NIST
Inp	834.00		NIST
Inp	848.00		NIST
Inp	844.20		NIST
Inp	851.30		NIST
Inp	844.30		NIST
Inp	879.00		NIST
Inp	830.00		NIST
Inp	836.00		NIST
Inp	841.00		NIST
Inp	846.00		NIST
Inp	876.00		NIST
Inp	884.00		NIST
Inp	892.00		NIST
Inp	868.00		NIST
Inp	847.00		NIST
Inp	853.00		NIST
Inp	859.00		NIST
Inp	843.00		NIST
Inp	840.00		NIST
Inp	844.00		NIST
Inp	848.00		NIST
Inp	864.10		NIST
Inp	844.00		NIST
Inp	853.00		NIST
Inp	858.00		NIST
Inp	843.00		NIST
Inp	850.00		NIST
Inp	851.00		NIST
Inp	855.00		NIST
Inp	857.00		NIST
Inp	868.00		NIST
Inp	855.60		NIST
Inp	850.00		NIST
Inp	850.00		NIST
Inp	866.00		NIST
Inp	862.00		NIST
Inp	879.00		NIST
Inp	871.00		NIST
Inp	868.00		NIST
Inp	869.00		NIST
Inp	854.00		NIST
Inp	864.00		NIST
Inp	864.00		NIST
Inp	893.00		NIST
Inp	850.80		NIST
Inp	876.00		NIST
Inp	856.30		NIST
Inp	855.50		NIST
Inp	853.20		NIST
Inp	856.30		NIST
Inp	857.20		NIST
Inp	839.80		NIST
Inp	868.30		NIST
Inp	872.00		NIST
Inp	860.00		NIST
Inp	857.00		NIST
Inp	865.00		NIST
Inp	866.00		NIST
Inp	865.00		NIST
Inp	866.00		NIST
Inp	856.00		NIST
Inp	847.00		NIST
Inp	855.00		NIST
Inp	849.00		NIST
Inp	834.00		NIST
Inp	860.90		NIST
Inp	836.10		NIST
Inp	841.70		NIST
Inp	846.10		NIST
Inp	846.40		NIST
Inp	861.50		NIST
Inp	853.20		NIST
Inp	856.30		NIST
Inp	857.20		NIST
Inp	856.30		NIST
Inp	855.50		NIST
Inp	844.19		NIST
Inp	844.47		NIST
Inp	858.00		NIST
Inp	845.00		NIST
Inp	858.00		NIST
Inp	844.50		NIST
Inp	844.74		NIST
Inp	845.00		NIST
Inp	864.00		NIST
Inp	855.00		NIST
Inp	848.30		NIST
Inp	856.20		NIST
Inp	848.30		NIST
Inp	848.30		NIST
Inp	856.20		NIST
Inp	845.17		NIST
Inp	845.49		NIST
Inp	848.70		NIST
Inp	844.80		NIST
Inp	844.60		NIST
Inp	841.26		NIST
Inp	844.05		NIST
Inp	845.90		NIST
Inp	857.33		NIST
Inp	860.40		NIST
Inp	862.45		NIST
Inp	843.00		NIST
Inp	877.00		NIST
Inp	858.00		NIST
Inp	863.00		NIST
Inp	865.00		NIST
Inp	846.00		NIST
Inp	870.79		NIST
Inp	845.00		NIST
Inp	858.00		NIST
Inp	859.00		NIST
Inp	852.00		NIST
Inp	855.00		NIST
Inp	858.00		NIST
Inp	864.00		NIST
Inp	869.00		NIST
Inp	853.00		NIST
Inp	859.00		NIST
Inp	847.00		NIST
Inp	857.00		NIST
Inp	858.00		NIST
Inp	858.00		NIST
Inp	859.00		NIST
Inp	859.00		NIST
Inp	847.00		NIST
Inp	850.00		NIST
Inp	858.00		NIST
Inp	859.00		NIST
Inp	863.00		NIST
Inp	864.00		NIST
Inp	843.00		NIST
Inp	843.00		NIST
Inp	844.00		NIST
Inp	844.00		NIST
Inp	842.00		NIST
Inp	842.00		NIST
Inp	842.00		NIST
Inp	852.00		NIST
Inp	852.00		NIST
Inp	852.00		NIST
Inp	852.00		NIST
Inp	852.00		NIST
Inp	852.00		NIST
Inp	853.00		NIST
Inp	835.00		NIST
Inp	847.00		NIST
Inp	831.00		NIST
Inp	838.00		NIST
Inp	845.00		NIST
Inp	849.00		NIST
Inp	842.00		NIST
Inp	856.00		NIST
Inp	836.00		NIST
Inp	850.00		NIST
Inp	859.00		NIST
Inp	852.00		NIST
Inp	857.00		NIST
Inp	849.00		NIST
Inp	858.00		NIST
Inp	864.00		NIST
Inp	845.00		NIST
Inp	863.00		NIST
Inp	851.00		NIST
Inp	851.00		NIST
Inp	866.00		NIST
Inp	845.00		NIST
Inp	861.00		NIST
Inp	846.00		NIST
Inp	863.30		NIST
Inp	868.00		NIST
Inp	829.00		NIST
Inp	846.00		NIST
Inp	886.00		NIST
Inp	859.00		NIST
Inp	866.00		NIST
Inp	860.00		NIST
Inp	865.00		NIST
Inp	878.00		NIST
Inp	855.00		NIST
Inp	849.00		NIST
Inp	847.66		NIST
Inp	851.00		NIST
Inp	847.00		NIST
Inp	868.10		NIST
Inp	843.00		NIST
Inp	846.00		NIST
Inp	850.00		NIST
Inp	852.00		NIST
Inp	838.00		NIST
Inp	841.00		NIST
Inp	842.00		NIST
Inp	856.00		NIST
Inp	869.00		NIST
Inp	843.00		NIST
Inp	850.00		NIST
Inp	848.00		NIST
Inp	844.00		NIST
Inp	844.00		NIST
Inp	844.00		NIST
Inp	868.00		NIST
Inp	846.00		NIST
Inp	850.00		NIST
Inp	835.30		NIST
Inp	837.60		NIST
Inp	840.80		NIST
Inp	843.30		NIST
Inp	845.30		NIST
Inp	847.00		NIST
Inp	835.00		NIST
Inp	837.00		NIST
Inp	840.00		NIST
Inp	843.00		NIST
Inp	845.00		NIST
Inp	846.00		NIST
Inp	842.00		NIST
Inp	841.00		NIST
Inp	845.00		NIST
Inp	842.00		NIST
Inp	860.00		NIST
Inp	850.00		NIST
Inp	864.00		NIST
Inp	866.00		NIST
Inp	852.00		NIST
Inp	840.00		NIST
Inp	867.00		NIST
Inp	857.00		NIST
Inp	868.00		NIST
Inp	851.00		NIST
Inp	870.00		NIST
Inp	869.00		NIST
Inp	850.00		NIST
Inp	871.00		NIST
Inp	855.00		NIST
Inp	893.00		NIST
Inp	855.00		NIST
Inp	868.00		NIST
Inp	868.00		NIST
Inp	851.00		NIST
Inp	859.00		NIST
Inp	866.00		NIST
Inp	851.00		NIST
Inp	839.30		NIST
Inp	869.00		NIST
Inp	879.00		NIST
Inp	858.00		NIST
Inp	848.00		NIST
Inp	868.00		NIST
Inp	853.00		NIST
Inp	846.00		NIST
Inp	848.00		NIST
Inp	854.00		NIST
Inp	861.00		NIST
Inp	854.00		NIST
Inp	872.00		NIST
Inp	858.00		NIST
Inp	851.00		NIST
Inp	858.00		NIST
Inp	854.00		NIST
Inp	854.00		NIST
Inp	863.00		NIST
Inp	846.00		NIST
Inp	854.00		NIST
Inp	846.00		NIST
Inp	847.00		NIST
Inp	861.00		NIST
Inp	860.00		NIST
Inp	859.10		NIST
Inp	863.30		NIST
Inp	862.80		NIST
Inp	862.60		NIST
Inp	847.50		NIST
Inp	867.00		NIST
Inp	844.00		NIST
Inp	870.00		NIST
Inp	846.00		NIST
Inp	830.00		NIST
Inp	840.00		NIST
Inp	846.00		NIST
Inp	846.00		NIST
Inp	848.00		NIST
Inp	849.00		NIST
Inp	864.00		NIST
Inp	843.00		NIST
Inp	Outlier 118.80		NIST
Inp	Outlier 118.30		NIST
Inp	Outlier 134.54		NIST
Inp	Outlier 118.90		NIST
Inp	Outlier 129.41		NIST
Inp	858.00		NIST
Inp	845.00		NIST
I	[1098.00; 1180.00]
I	1100.00		NIST
I	1105.00		NIST
I	1138.00		NIST
I	1131.90		NIST
I	1158.90		NIST
I	1164.30		NIST
I	Outlier 1169.80		NIST
I	Outlier 1175.20		NIST
I	1136.00		NIST
I	1160.90		NIST
I	1158.40		NIST
I	1159.40		NIST
I	1127.10		NIST
I	1111.10		NIST
I	Outlier 1178.00		NIST
I	1154.00		NIST
I	1162.00		NIST
I	Outlier 1169.00		NIST
I	1147.00		NIST
I	1126.00		NIST
I	1128.00		NIST
I	1098.00		NIST
I	1122.00		NIST
I	1116.00		NIST
I	1120.00		NIST
I	1134.00		NIST
I	1146.10		NIST
I	1123.00		NIST
I	1129.00		NIST
I	1129.00		NIST
I	1131.00		NIST
I	1127.00		NIST
I	1138.00		NIST
I	1115.00		NIST
I	1115.00		NIST
I	1130.00		NIST
I	1118.00		NIST
I	1133.00		NIST
I	Outlier 1168.00		NIST
I	1138.00		NIST
I	1125.00		NIST
I	1125.00		NIST
I	1124.00		NIST
I	1138.00		NIST
I	1125.00		NIST
I	1123.00		NIST
I	1125.00		NIST
I	1129.00		NIST
I	1122.00		NIST
I	1130.00		NIST
I	1116.00		NIST
I	1128.00		NIST
I	1122.00		NIST
I	1123.00		NIST
I	1130.00		NIST
I	1132.00		NIST
I	1107.00		NIST
I	1133.00		NIST
I	1135.00		NIST
I	1125.00		NIST
I	1125.00		NIST
I	1121.00		NIST
I	1125.00		NIST
I	1125.00		NIST
I	1122.00		NIST
I	1129.00		NIST
I	1132.00		NIST
I	1132.00		NIST
I	1157.00		NIST
I	Outlier 1168.00		NIST
I	Outlier 1180.00		NIST
I	1135.00		NIST
I	1146.00		NIST
I	1145.00		NIST
I	1144.00		NIST
I	1146.00		NIST
I	1157.00		NIST
I	1166.00		NIST
I	1125.00		NIST
I	1135.00		NIST
I	1111.00		NIST
I	1146.00		NIST
I	1130.00		NIST
I	1130.00		NIST
I	1142.00		NIST
I	1139.00		NIST
I	1130.00		NIST
I	1116.00		NIST
I	1161.00		NIST
I	1104.00		NIST
I	1122.00		NIST
I	1122.00		NIST
I	1119.00		NIST
I	1114.00		NIST
I	1118.00		NIST
I	1141.00		NIST
I	1108.00		NIST
I	1147.00		NIST
I	1116.00		NIST
I	1126.00		NIST
I	1135.00		NIST
I	1125.00		NIST
I	1109.00		NIST
I	1126.00		NIST
I	1124.00		NIST
I	1124.00		NIST
I	1134.00		NIST
I	1139.00		NIST
I	1127.00		NIST
I	1122.00		NIST
I	1119.00		NIST
I	1161.00		NIST
I	1130.00		NIST
I	1161.00		NIST
I	1121.00		NIST
I	1125.00		NIST
I	1127.00		NIST
I	1125.00		NIST
I	1138.00		NIST
I	1161.00		NIST
I	1109.00		NIST
I	1132.00		NIST
I	1129.00		NIST
I	1111.00		NIST
I	1131.00		NIST
I	1129.00		NIST
I	1132.00		NIST
I	1129.00		NIST
I	1117.00		NIST
I	1110.00		NIST
I	1110.00		NIST
I	1117.00		NIST
I	1120.00		NIST
S°gas	360.60 ± 0.50	J/mol×K	NIST
S°liquid	[255.01; 256.10]	J/mol×K
S°liquid	255.01	J/mol×K	NIST
S°liquid	256.10	J/mol×K	NIST
Tboil	[409.25; 409.35]	K
Tboil	409.34	K	KDB
Tboil	409.35	K	Isobari...
Tboil	409.35	K	Isobari...
Tboil	409.32	K	Isobari...
Tboil	409.25	K	Isobari...
Tc	617.15	K	KDB
Tfus	[178.20; 278.29]	K
Tfus	178.20	K	Aq. Sol...
Tfus	178.20	K	KDB
Tfus	278.29	K	Phase E...
Ttriple	[178.00; 178.15]	K
Ttriple	178.15 ± 0.02	K	NIST
Ttriple	178.00 ± 0.30	K	NIST
Vc	[0.374; 0.374]	m3/kmol
Vc	0.374	m3/kmol	KDB
Vc	0.374	m3/kmol	NIST
Zc	0.2630460		KDB
Zra	0.26		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[159.24; 214.02]	J/mol×K	[373.15; 523.15]
Cp,gas	159.24 ± 0.80	J/mol×K	373.15	NIST
Cp,gas	164.25 ± 0.33	J/mol×K	385.65	NIST
Cp,gas	169.25 ± 0.34	J/mol×K	398.15	NIST
Cp,gas	178.96 ± 0.36	J/mol×K	423.15	NIST
Cp,gas	188.28 ± 0.38	J/mol×K	448.15	NIST
Cp,gas	197.35 ± 0.39	J/mol×K	473.15	NIST
Cp,gas	205.94 ± 0.41	J/mol×K	498.15	NIST
Cp,gas	214.02 ± 0.43	J/mol×K	523.15	NIST
Cp,liquid	[161.00; 186.60]	J/mol×K	[293.31; 303.00]
Cp,liquid	184.80	J/mol×K	293.31	NIST
Cp,liquid	161.00	J/mol×K	295.00	NIST
Cp,liquid	181.60	J/mol×K	297.40	NIST
Cp,liquid	185.80	J/mol×K	298.00	NIST
Cp,liquid	184.50	J/mol×K	298.00	NIST
Cp,liquid	185.78	J/mol×K	298.15	NIST
Cp,liquid	186.04	J/mol×K	298.15	NIST
Cp,liquid	185.56	J/mol×K	298.15	NIST
Cp,liquid	185.81	J/mol×K	298.15	NIST
Cp,liquid	186.60	J/mol×K	298.15	NIST
Cp,liquid	185.57	J/mol×K	298.15	NIST
Cp,liquid	183.70	J/mol×K	298.50	NIST
Cp,liquid	178.70	J/mol×K	302.70	NIST
Cp,liquid	178.70	J/mol×K	302.80	NIST
Cp,liquid	181.60	J/mol×K	303.00	NIST
η	[0.0003660; 0.0006793]	Pa×s	[293.15; 353.15]
η	0.0006793	Pa×s	293.15	Viscosi...
η	0.0006280	Pa×s	298.15	Viscosi...
η	0.0006299	Pa×s	298.15	Excess ...
η	0.0006380	Pa×s	298.15	Densiti...
η	0.0006006	Pa×s	303.15	Viscosi...
η	0.0005980	Pa×s	303.15	Densiti...
η	0.0005970	Pa×s	303.15	Viscosi...
η	0.0005986	Pa×s	303.15	Densiti...
η	0.0005981	Pa×s	303.15	Excess ...
η	0.0005970	Pa×s	303.15	Thermop...
η	0.0005340	Pa×s	308.15	Densiti...
η	0.0005530	Pa×s	308.15	Viscosi...
η	0.0005652	Pa×s	308.15	Viscome...
η	0.0005691	Pa×s	308.15	Densiti...
η	0.0005380	Pa×s	313.15	Viscosi...
η	0.0005370	Pa×s	313.15	Densiti...
η	0.0005372	Pa×s	313.15	Densiti...
η	0.0005294	Pa×s	313.15	Viscome...
η	0.0005355	Pa×s	313.15	Viscosi...
η	0.0005380	Pa×s	313.15	Thermop...
η	0.0005060	Pa×s	318.15	Densiti...
η	0.0004829	Pa×s	323.15	Excess ...
η	0.0004830	Pa×s	323.15	Densiti...
η	0.0004805	Pa×s	323.15	Densiti...
η	0.0004566	Pa×s	328.15	Densiti...
η	0.0004371	Pa×s	333.15	Densiti...
η	0.0004370	Pa×s	333.15	Densiti...
η	0.0003970	Pa×s	343.15	Densiti...
η	0.0003660	Pa×s	353.15	Densiti...
ΔfusH	[9.16; 9.18]	kJ/mol	[178.00; 178.20]
ΔfusH	9.16	kJ/mol	178.00	NIST
ΔfusH	9.18	kJ/mol	178.15	NIST
ΔfusH	9.16	kJ/mol	178.17	NIST
ΔfusH	9.16	kJ/mol	178.20	NIST
ΔfusH	9.16	kJ/mol	178.20	NIST
ΔvapH	[35.50; 42.49]	kJ/mol	[294.01; 583.00]
ΔvapH	42.49	kJ/mol	294.01	NIST
ΔvapH	40.50 ± 0.10	kJ/mol	328.00	NIST
ΔvapH	39.50 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	38.60 ± 0.10	kJ/mol	358.00	NIST
ΔvapH	41.80	kJ/mol	359.00	NIST
ΔvapH	40.60	kJ/mol	360.00	NIST
ΔvapH	40.00	kJ/mol	370.00	NIST
ΔvapH	35.56	kJ/mol	409.20	KDB
ΔvapH	35.57	kJ/mol	409.30	NIST
ΔvapH	37.00	kJ/mol	434.00	NIST
ΔvapH	35.80	kJ/mol	505.50	NIST
ΔvapH	35.50	kJ/mol	583.00	NIST
Pvap	[2.10; 3451.00]	kPa	[308.15; 613.15]
Pvap	2.22	kPa	308.15	Vapor-l...
Pvap	2.10	kPa	313.15	Vapor-l...
Pvap	3.75	kPa	318.15	Vapor-l...
Pvap	4.08	kPa	320.15	Vapour-...
Pvap	4.71	kPa	323.15	Vapor-l...
Pvap	5.00	kPa	324.40	Isobari...
Pvap	5.41	kPa	326.15	Vapour-...
Pvap	5.97	kPa	328.15	Vapor-l...
Pvap	7.09	kPa	332.15	Vapour-...
Pvap	7.45	kPa	333.15	Vapor-l...
Pvap	7.50	kPa	333.40	Isobari...
Pvap	9.19	kPa	338.15	Vapour-...
Pvap	9.25	kPa	338.15	Vapor-l...
Pvap	10.00	kPa	340.00	Isobari...
Pvap	11.41	kPa	343.15	Vapor-l...
Pvap	11.79	kPa	344.15	Vapour-...
Pvap	12.50	kPa	345.50	Isobari...
Pvap	13.79	kPa	348.15	Vapor-l...
Pvap	15.00	kPa	350.10	Isobari...
Pvap	17.50	kPa	354.10	Isobari...
Pvap	20.00	kPa	357.70	Isobari...
Pvap	20.42	kPa	358.15	Vapor-l...
Pvap	22.50	kPa	360.90	Isobari...
Pvap	25.00	kPa	363.80	Isobari...
Pvap	26.66	kPa	365.86	Isobari...
Pvap	29.11	kPa	368.15	Vapor-l...
Pvap	40.00	kPa	377.54	Determi...
Pvap	47.75	kPa	383.15	Vapor-l...
Pvap	53.33	kPa	386.69	Determi...
Pvap	53.33	kPa	386.94	Isobari...
Pvap	66.66	kPa	394.14	Determi...
Pvap	79.99	kPa	400.51	Determi...
Pvap	79.99	kPa	400.70	Isobari...
Pvap	85.64	kPa	403.15	Vapor-l...
Pvap	93.32	kPa	406.12	Determi...
Pvap	93.13	kPa	406.23	Refract...
Pvap	95.30	kPa	406.95	Vapor-l...
Pvap	250.00	kPa	447.20	Isobari...
Pvap	681.00	kPa	498.15	High-Te...
Pvap	1027.00	kPa	523.15	High-Te...
Pvap	1601.00	kPa	553.15	High-Te...
Pvap	2387.00	kPa	583.15	High-Te...
Pvap	3451.00	kPa	613.15	High-Te...
n0	[1.49020; 1.54395]		[283.15; 303.15]
n0	1.50129		283.15	Density...
n0	1.49620		293.10	Densiti...
n0	1.49620		293.10	A study...
n0	1.49220		293.15	Volumet...
n0	1.49620		293.15	Effect ...
n0	1.50090		293.15	Solubil...
n0	1.49600		293.15	Activit...
n0	1.49570		293.15	Densiti...
n0	1.54395		293.15	Bubble ...
n0	1.49620		293.15	Experim...
n0	1.49550		293.15	Infinit...
n0	1.49620		293.15	A study...
n0	1.49320		298.15	KDB
n0	1.49304		298.15	(Liquid...
n0	1.49300		298.15	Experim...
n0	1.49620		298.15	Densiti...
n0	1.49620		298.15	The vol...
n0	1.49304		298.15	Liquid-...
n0	1.49310		298.15	Excess ...
n0	1.49320		298.15	Isobari...
n0	1.49304		298.15	Liquid ...
n0	1.49320		298.15	Bubble ...
n0	1.49316		298.15	Effect ...
n0	1.49304		298.15	Density...
n0	1.49304		298.15	Effect ...
n0	1.49020		303.15	Densiti...
ρl	[794.20; 875.69]	kg/m3	[283.15; 373.15]
ρl	875.69	kg/m3	283.15	The den...
ρl	871.33	kg/m3	288.15	Thermop...
ρl	871.31	kg/m3	288.15	Effect ...
ρl	871.30	kg/m3	288.15	The den...
ρl	867.00	kg/m3	293.00	KDB
ρl	867.10	kg/m3	293.10	Vapor-L...
ρl	867.10	kg/m3	293.15	Densiti...
ρl	866.95	kg/m3	293.15	Density...
ρl	867.10	kg/m3	293.15	Densiti...
ρl	866.90	kg/m3	293.15	The den...
ρl	867.20	kg/m3	293.15	Densiti...
ρl	866.54	kg/m3	293.15	Isobari...
ρl	862.58	kg/m3	298.15	The phy...
ρl	862.50	kg/m3	298.15	Density...
ρl	862.57	kg/m3	298.15	Vapor L...
ρl	862.55	kg/m3	298.15	Excess ...
ρl	862.97	kg/m3	298.15	Phase b...
ρl	862.59	kg/m3	298.15	Liquid-...
ρl	862.50	kg/m3	298.15	Bubble ...
ρl	862.50	kg/m3	298.15	Thermod...
ρl	862.55	kg/m3	298.15	Effect ...
ρl	862.43	kg/m3	298.15	Acousti...
ρl	862.50	kg/m3	298.15	Excess ...
ρl	862.51	kg/m3	298.15	Experim...
ρl	862.70	kg/m3	298.15	Isobari...
ρl	862.51	kg/m3	298.15	Liquid ...
ρl	862.97	kg/m3	298.15	Phase b...
ρl	862.51	kg/m3	298.15	Phase b...
ρl	862.55	kg/m3	298.15	Thermod...
ρl	862.70	kg/m3	298.15	Densiti...
ρl	862.70	kg/m3	298.15	Densiti...
ρl	862.58	kg/m3	298.15	The den...
ρl	862.57	kg/m3	298.15	Isobari...
ρl	862.51	kg/m3	298.15	(Liquid...
ρl	862.37	kg/m3	298.15	Experim...
ρl	862.59	kg/m3	298.15	Thermop...
ρl	862.70	kg/m3	298.15	The den...
ρl	863.54	kg/m3	298.15	Separat...
ρl	862.50	kg/m3	298.15	Excess ...
ρl	858.15	kg/m3	303.15	Density...
ρl	858.10	kg/m3	303.15	Experim...
ρl	858.30	kg/m3	303.15	Densiti...
ρl	858.16	kg/m3	303.15	The den...
ρl	853.61	kg/m3	308.15	Acousti...
ρl	853.75	kg/m3	308.15	Effect ...
ρl	853.77	kg/m3	308.15	Thermop...
ρl	853.80	kg/m3	308.15	The den...
ρl	853.71	kg/m3	308.15	The phy...
ρl	853.68	kg/m3	308.15	Experim...
ρl	849.30	kg/m3	313.15	Densiti...
ρl	849.29	kg/m3	313.15	The phy...
ρl	849.29	kg/m3	313.15	Density...
ρl	849.26	kg/m3	313.15	Experim...
ρl	844.80	kg/m3	318.15	The den...
ρl	844.89	kg/m3	318.15	Thermop...
ρl	844.70	kg/m3	318.15	The phy...
ρl	844.87	kg/m3	318.15	Effect ...
ρl	840.28	kg/m3	323.15	The phy...
ρl	840.30	kg/m3	323.15	Densiti...
ρl	840.38	kg/m3	323.15	Density...
ρl	835.94	kg/m3	328.15	Thermop...
ρl	835.93	kg/m3	328.15	Effect ...
ρl	831.20	kg/m3	333.15	Densiti...
ρl	831.40	kg/m3	333.15	Density...
ρl	822.30	kg/m3	343.15	Density...
ρl	822.10	kg/m3	343.15	Densiti...
ρl	813.10	kg/m3	353.15	Density...
ρl	803.70	kg/m3	363.15	Density...
ρl	794.20	kg/m3	373.15	Density...
ΔfusS	[51.43; 51.54]	J/mol×K	[178.00; 178.17]
ΔfusS	51.48	J/mol×K	178.00	NIST
ΔfusS	51.54	J/mol×K	178.15	NIST
ΔfusS	51.43	J/mol×K	178.17	NIST
csound,fluid	[1213.59; 1360.73]	m/s	[288.15; 323.15]
csound,fluid	1360.73	m/s	288.15	Influen...
csound,fluid	1359.11	m/s	288.15	Tempera...
csound,fluid	1349.91	m/s	290.65	Influen...
csound,fluid	1340.00	m/s	293.15	Densiti...
csound,fluid	1339.40	m/s	293.15	Influen...
csound,fluid	1328.86	m/s	295.65	Influen...
csound,fluid	1318.36	m/s	298.15	Influen...
csound,fluid	1319.00	m/s	298.15	Densiti...
csound,fluid	1316.23	m/s	298.15	Tempera...
csound,fluid	1307.90	m/s	300.65	Influen...
csound,fluid	1298.00	m/s	303.15	Densiti...
csound,fluid	1297.48	m/s	303.15	Influen...
csound,fluid	1287.09	m/s	305.65	Influen...
csound,fluid	1276.75	m/s	308.15	Influen...
csound,fluid	1276.00	m/s	308.15	Densiti...
csound,fluid	1266.54	m/s	310.65	Influen...
csound,fluid	1256.29	m/s	313.15	Influen...
csound,fluid	1257.00	m/s	313.15	Densiti...
csound,fluid	1246.12	m/s	315.65	Influen...
csound,fluid	1236.06	m/s	318.15	Influen...
csound,fluid	1226.09	m/s	320.65	Influen...
csound,fluid	1213.59	m/s	323.15	Tempera...
csound,fluid	1216.34	m/s	323.15	Influen...
γ	[0.03; 0.03]	N/m	[293.20; 323.15]
γ	0.03	N/m	293.20	KDB
γ	0.03	N/m	298.15	Densiti...
γ	0.03	N/m	303.15	Densiti...
γ	0.03	N/m	303.15	Thermo ...
γ	0.03	N/m	308.15	Densiti...
γ	0.03	N/m	313.15	Thermo ...
γ	0.03	N/m	323.15	Thermo ...
ΔvapS	144.50	J/mol×K	294.01	NIST
λ	[0.12; 0.14]	W/m×K	[258.00; 329.66]
λ	0.14	W/m×K	258.00	Thermal...
λ	0.14	W/m×K	258.29	Thermal...
λ	0.14	W/m×K	258.50	Thermal...
λ	0.13	W/m×K	277.34	Thermal...
λ	0.13	W/m×K	277.65	Thermal...
λ	0.13	W/m×K	277.88	Thermal...
λ	0.13	W/m×K	295.86	Thermal...
λ	0.13	W/m×K	296.19	Thermal...
λ	0.13	W/m×K	296.42	Thermal...
λ	0.12	W/m×K	312.38	Thermal...
λ	0.12	W/m×K	312.72	Thermal...
λ	0.12	W/m×K	312.96	Thermal...
λ	0.12	W/m×K	329.05	Thermal...
λ	0.12	W/m×K	329.41	Thermal...
λ	0.12	W/m×K	329.66	Thermal...

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil	408.75	K	95.30	Excess ...

Datasets

1. Viscosity, Pa*s (1)
2. Refractive index (Na D-line) (1)
3. Mass density, kg/m3 (1)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
253.23	100.00	0.0012
253.22	1000.00	0.0012
253.21	5000.00	0.0013
253.22	10000.00	0.0013
253.24	15000.00	0.0014
253.23	20000.00	0.0014
253.23	25000.00	0.0015
253.24	30000.00	0.0015
253.22	35000.00	0.0016
263.22	100.00	0.0010
263.22	1000.00	0.0010
263.21	5000.00	0.0011
263.20	10000.00	0.0011
263.20	15000.00	0.0012
263.21	20000.00	0.0012
263.21	25000.00	0.0013
263.22	30000.00	0.0013
263.21	35000.00	0.0014
273.21	100.00	0.0009
273.17	1000.00	0.0009
273.15	5000.00	0.0009
273.18	10000.00	0.0010
273.19	15000.00	0.0010
273.15	20000.00	0.0010
273.16	25000.00	0.0011
273.15	30000.00	0.0011
273.15	35000.00	0.0012
283.16	100.00	0.0008
283.13	1000.00	0.0008
283.16	5000.00	0.0008
283.14	10000.00	0.0008
283.17	15000.00	0.0009
283.15	20000.00	0.0009
283.17	25000.00	0.0009
283.16	30000.00	0.0010
283.16	35000.00	0.0010
293.26	100.00	0.0007
293.20	1000.00	0.0007
293.18	5000.00	0.0007
293.24	10000.00	0.0007
293.23	15000.00	0.0008
293.24	20000.00	0.0008
293.22	25000.00	0.0008
293.24	30000.00	0.0008
293.26	35000.00	0.0009
303.15	100.00	0.0006
303.17	1000.00	0.0006
303.18	5000.00	0.0006
303.20	10000.00	0.0006
303.19	15000.00	0.0007
303.17	20000.00	0.0007
303.18	25000.00	0.0007
303.19	30000.00	0.0008
303.18	35000.00	0.0008
313.12	100.00	0.0005
313.12	1000.00	0.0005
313.11	5000.00	0.0006
313.10	10000.00	0.0006
313.12	15000.00	0.0006
313.09	20000.00	0.0006
313.10	25000.00	0.0006
313.08	30000.00	0.0007
313.10	35000.00	0.0007
322.97	100.00	0.0005
322.98	1000.00	0.0005
322.98	5000.00	0.0005
322.98	10000.00	0.0005
322.98	15000.00	0.0005
322.97	20000.00	0.0006
322.98	25000.00	0.0006
322.98	30000.00	0.0006
322.98	35000.00	0.0006
332.91	100.00	0.0004
332.92	1000.00	0.0004
332.91	5000.00	0.0005
332.92	10000.00	0.0005
332.92	15000.00	0.0005
332.92	20000.00	0.0005
332.92	25000.00	0.0005
332.92	30000.00	0.0006
332.92	35000.00	0.0006
342.81	100.00	0.0004
342.80	1000.00	0.0004
342.81	5000.00	0.0004
342.80	10000.00	0.0004
342.80	15000.00	0.0005
342.80	20000.00	0.0005
342.80	25000.00	0.0005
342.80	30000.00	0.0005
342.80	35000.00	0.0005
352.73	100.00	0.0004
352.73	1000.00	0.0004
352.72	5000.00	0.0004
352.73	10000.00	0.0004
352.73	15000.00	0.0004
352.72	20000.00	0.0004
352.73	25000.00	0.0004
352.73	30000.00	0.0005
352.72	35000.00	0.0005
362.66	100.00	0.0003
362.66	1000.00	0.0003
362.66	5000.00	0.0004
362.67	10000.00	0.0004
362.66	15000.00	0.0004
362.66	20000.00	0.0004
362.66	25000.00	0.0004
362.66	30000.00	0.0004
362.67	35000.00	0.0004
372.61	100.00	0.0003
372.60	1000.00	0.0003
372.59	5000.00	0.0003
372.59	10000.00	0.0003
372.59	15000.00	0.0004
372.59	20000.00	0.0004
372.59	25000.00	0.0004
372.59	30000.00	0.0004
372.59	35000.00	0.0004
Reference

Refractive index (Na D-line)

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Refractive index (Na D-line) - Liquid
93.00	298.15	1.493
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
292.25	100.00	867.0
292.25	5000.00	870.8
292.25	9900.00	874.0
292.25	19700.00	881.3
292.25	29500.00	887.1
292.25	39300.00	893.0
292.25	49100.00	898.5
292.25	58900.00	903.8
313.45	100.00	849.1
313.45	5000.00	853.1
313.45	19700.00	864.4
313.45	29500.00	871.4
313.45	39300.00	877.6
313.45	49100.00	883.6
313.45	58900.00	889.4
336.55	100.00	828.7
336.55	5000.00	833.6
336.55	9900.00	838.5
336.55	19700.00	845.8
336.55	29500.00	854.0
336.55	39300.00	860.9
336.55	49100.00	867.8
336.55	58900.00	873.6
358.81	100.00	808.4
358.81	5000.00	814.5
358.81	9900.00	820.0
358.81	19700.00	827.6
358.81	29500.00	836.8
358.81	39300.00	844.8
358.81	49100.00	852.4
358.81	58900.00	858.6
382.95	5000.00	793.0
382.95	9900.00	799.0
382.95	19700.00	808.1
382.95	29500.00	818.2
382.95	39300.00	827.1
382.95	49100.00	835.1
382.95	58900.00	842.5
408.05	5000.00	770.4
408.05	9900.00	777.3
408.05	19700.00	788.5
408.05	29500.00	799.7
408.05	39300.00	809.5
408.05	49100.00	817.9
408.05	58900.00	826.0
434.45	5000.00	746.0
434.45	9900.00	754.4
434.45	19700.00	768.1
434.45	29500.00	780.5
434.45	39300.00	791.0
434.45	49100.00	800.4
434.45	58900.00	808.6
461.85	5000.00	718.6
461.85	9900.00	728.8
461.85	19700.00	746.2
461.85	29500.00	760.0
461.85	39300.00	771.7
461.85	49100.00	782.3
461.85	58900.00	791.0
490.15	5000.00	687.0
490.15	9900.00	700.0
490.15	19700.00	720.9
490.15	29500.00	737.2
490.15	39300.00	750.7
490.15	49100.00	762.9
490.15	58900.00	773.2
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[297.90; 436.98]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.44625e+01
Coefficient B			-3.59099e+03
Coefficient C			-4.45680e+01
Temperature range, min.			297.90
Temperature range, max.			436.98
Pvap	1.33	kPa	297.90	Calculated Property
Pvap	3.01	kPa	313.35	Calculated Property
Pvap	6.23	kPa	328.81	Calculated Property
Pvap	11.94	kPa	344.26	Calculated Property
Pvap	21.50	kPa	359.71	Calculated Property
Pvap	36.62	kPa	375.17	Calculated Property
Pvap	59.47	kPa	390.62	Calculated Property
Pvap	92.68	kPa	406.07	Calculated Property
Pvap	139.26	kPa	421.53	Calculated Property
Pvap	202.65	kPa	436.98	Calculated Property
Pvap	[4.05e-06; 3587.82]	kPa	[178.15; 617.17]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			7.97937e+01
Coefficient B			-7.63808e+03
Coefficient C			-9.55398e+00
Coefficient D			5.65318e-06
Temperature range, min.			178.15
Temperature range, max.			617.17
Pvap	4.05e-06	kPa	178.15	Calculated Property
Pvap	4.51e-03	kPa	226.93	Calculated Property
Pvap	0.31	kPa	275.71	Calculated Property
Pvap	4.99	kPa	324.49	Calculated Property
Pvap	34.37	kPa	373.27	Calculated Property
Pvap	140.91	kPa	422.05	Calculated Property
Pvap	413.38	kPa	470.83	Calculated Property
Pvap	971.25	kPa	519.61	Calculated Property
Pvap	1964.29	kPa	568.39	Calculated Property
Pvap	3587.82	kPa	617.17	Calculated Property

Similar Compounds

Find more compounds similar to Ethylbenzene.

Mixtures

• Acetic acid, butyl ester + Ethylbenzene
• Propane, 2-methoxy-2-methyl- + Ethylbenzene
• n-Hexane + Ethylbenzene
• Toluene + Ethylbenzene
• Ethylbenzene + Heptane
• Benzene + Ethylbenzene
• Cyclooctane + Ethylbenzene
• Ethylbenzene + Ethane, 1,1,2,2-tetrachloro-
• Benzene, 1,3-dimethyl- + Ethylbenzene
• Ethylbenzene + Dimethyl Sulfoxide
• Ethylbenzene + 2-Propanol, 1,1'-[(1-methyl-1,2-ethanediyl)bis(oxy)]bis-
• Ethylbenzene + Cyclohexanone
• Ethylbenzene + Acetophenone
• Ethylbenzene + 1-Pentanol
• 2-Propenenitrile + Ethylbenzene
• N,N-Dimethylacetamide + Ethylbenzene
• Methyl Isobutyl Ketone + Ethylbenzene
• Pyridine, 2-methyl- + Ethylbenzene
• Benzene, nitro- + Ethylbenzene
• Ethylbenzene + 1-Propanone, 1-phenyl-

Find more mixtures with Ethylbenzene.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• Effect of Temperature on the Change of Refractive Index on Mixing for Butyl Acetate + Aromatic Hydrocarbons
• Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
• Experimental Study of the Dynamic Viscosity Deviations in the Binary Systems: Hexane + Ethylbenzene, + o-Xylene, + m-Xylene, + p-Xylene at 298.15 K
• Viscometric and Volumetric Properties of 10 Regular Binary Systems at 308.15 K and 313.15 K
• Densities and Kinematic Viscosities of One Quinary Regular Liquid System and Its Five Quaternary Sub-Systems at Temperatures (293.15 and 298.15) K
• Densities and Kinematic Viscosities of a Quinary Regular Liquid System and Its Five Quaternary Subsystems at 293.15A K and 298.15A K
• 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
• Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
• Vapor-liquid equilibrium for the binary mixtures of dimethylsulfoxide with substituted benzenes
• Limiting activity coefficients in binary mixtures of 1-alkanols and ethylbenzene
• Excess enthalpies of dimethylsulfoxide with substituted benzenes at 298.15K
• Thermodynamics of dissolution for 1-naphtol N-methylcarbamate in pure, mineral and Mediterranean sea water by dynamic saturation method
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
• Solubility of pyrene in simple and mixed solvent systems
• 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
• 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 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
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Binary and ternary vapor-liquid equilibrium data of the system ethylbenzene + styrene + 3-methyl-N-butylpyridinium tetracyanoborate at vacuum conditions and liquid-liquid equilibrium data of their binary systems
• Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
• (Liquid + liquid) equilibria for the ternary system of (N-formylmorpholine + ethylbenzene + 2,2,4-trimethylpentane) at temperatures (303.15, 313.15, and 323.15) K
• Effect of 1-methyl 3-octylimidazolium thiocyanate on vapor-liquid equilibria of binary mixtures of hydrocarbons
• Distribution of MEG and methanol in well-defined hydrocarbon and water systems: Experimental measurement and modeling using the CPA EoS
• 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
• Vapor-liquid equilibria of binary mixtures of propylene oxide witheither ethyl benzene, 2-methylpentane, or 2-methyl-1-pentene
• Phase equilibria of binary mixtures (ionic liquid + aromatic hydrocarbon): Effect of the structure of the components on the solubility
• Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
• Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
• 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
• 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
• Experimental study on liquid - liquid equilibria of ionic liquids + alkane + ethyl benzene or p-xylene at 298.15 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
• Vapor-liquid equilibria for n-heptane + (benzene, toluene, pxylene, or ethylbenzene) + {[4empy][Tf2N] (0.3) + [emim][DCA] (0.7)} binary ionic liquid mixture
• Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
• Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 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
• 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
• Measurement and modeling of infinite dilution activity coefficients of organic compounds in an equimolar ionic liquid mixture of [Bmim]Cl and [Bmim][Tf2N]
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• (Liquid + liquid) phase behavior for systems containing (aromatic + TBA + methylcyclohexane)
• 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
• Bubble temperature measurements on seven binary mixtures formed by ethylbenzene at 94.7 kPa
• 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
• 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)
• 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
• Bubble points of the binary mixtures formed by ethylbenzene with some chloroaliphatics and substituted benzenes at p = 94.7 kPa
• Densities and volumetric properties of N-methyl-2-pyrrolidone with aromatic hydrocarbon at different temperature
• Densities and excess volumes of binary mixtures of N,N-dimethylformamide with aromatic hydrocarbon at different temperature
• Thermodynamics of mixtures involving some (benzene derivatives + benzonitrile)
• A study on densities and excess volumes in the (c-butyrolactone + aromatic hydrocarbon) system at various temperatures
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
• Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
• Solubility of ethylbenzene and xylene in pure water and aqueous alkanolamine solutions
• Bubble point measurements of binary mixtures formed by ethyl benzene with selected compounds at 95.35 kPa
• 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
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
• Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
• Experimental densities, refractive indices, and speeds of sound of 12 binary mixtures containing alkanes and aromatic compounds at T = 313.15 K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
• 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
• 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
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate [EMIM][TCB] using gas liquid chromatography
• Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
• Activity coefficients at infinite dilution of organic solutes in N-alkylpyridinium bis(trifluoromethylsulfonyl)imide ([CnPY][NTf2], n = 2, 4, 5) using gas liquid chromatography
• Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
• 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
• (Liquid + liquid) equilibrium data for the ternary systems (cycloalkane + ethylbenzene + 1-ethyl-3-methylimidazolium ethylsulfate) at T = 298.15 K and atmospheric pressure
• 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
• Thermophysical properties and phase equilibria study of the binary systems {N-hexylquinolinium bis(trifluoromethylsulfonyl)imide + aromatic hydrocarbons, or an alcohol}
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Densities, viscosities, speed of sound, and IR spectroscopic studies of binary mixtures of tert-butyl acetate with benzene, methylbenzene, and ethylbenzene at T = (298.15 and 308.15) K
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
• Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
• Isobaric (vapour + liquid) equilibria for sulfolane with toluene, ethylbenzene, and isopropylbenzene at 101.33 kPa
• Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Binary and ternary LLE data of the system (ethylbenzene + styrene + 1-ethyl-3-methylimidazolium thiocyanate) and binary VLE data of the system (styrene + 1-ethyl-3-methylimidazolium thiocyanate)
• Volumetric properties of binary mixtures of tributylamine with benzene derivatives and comparison with ERAS model results at temperatures from (293.15 to 333.15) K
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium hexafluorophosphate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 363.15) K
• 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
• 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
• Isobaric (vapour + liquid) equilibria for N-formylmorpholine with ethylbenzene, n-butylbenzene, iso-propylbenzene and 1,2,4-trimethylbenzene at 101.33 kPa
• Liquid-liquid extraction of aromatics from their mixtures with alkanes using 1-methyl 3-octylimidazolium thiocyanate ionic liquid
• 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 coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
• Effect of temperature and composition on the density, refractive index, and excess quantities of binary mixtures of 2,4,6,8-tetramethyl-2,4,6,8- tetraethenylcyclotetrasiloxane with aromatic hydrocarbons
• 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
• 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
• Acoustic and thermodynamic properties of binary mixtures of 1-nonanol with o-xylene, m-xylene, p-xylene, ethylbenzene and mesitylene at T = (298.15 and 308.15) K
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
• 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
• Experimental density, viscosity, interfacial tension and water solubility of ethyl benzene - a-methyl benzyl alcohol - water system
• 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
• 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
• 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
• Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
• Phase behavior of ternary mixtures {aliphatic hydrocarbon + aromatic hydrocarbon + ionic liquid}: Experimental LLE data and their modeling by COSMO-RS
• The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
• (Liquid + liquid) equilibrium at T = 298.15 K for ternary mixtures of alkane + aromatic compounds + imidazolium-based ionic liquids
• Thermophysical properties of binary mixtures of triethoxysilane, methyltriethoxysilane, vinyltriethoxysilane and 3-mercaptopropyltriethoxysilane with ethylbenzene at various temperatures
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Thermodynamics of solvation in propylene glycol and methyl cellosolve
• Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
• Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
• Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
• Experimental and correlational study of phase equilibria in aqueous mixtures of phosphoric acid with aromatic hydrocarbons at various temperatures
• Viscosity measurements of ortho-xylene, meta-xylene, para-xylene and ethylbenzene
• The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) 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
• 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
• Solubility determination and thermodynamic modelling of 2,4-dihydro-5-methyl-2-(4-methylphenyl)-3H-pyrazol-3-one in twelve organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Separation of ethylbenzene/styrene systems using ionic liquids in ternary LLE
• Thermodynamic study of solubility for 2-amino-4-chloro-6-methoxypyrimidine in twelve organic solvents at temperatures from 273.15 K to 323.15 K
• Solubility determination and thermodynamic modelling for 2-amino-4-chlorobenzoic acid in eleven organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• 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
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
• Liquid-liquid equilibria for the ternary system of water + furfural + solvents at 303.15 and 323.15 K under atmospheric pressure
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• Liquid-liquid extraction of styrene from ethylbenzene using ionic liquids
• 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
• The density, the refractive index and the adjustment of the excess thermodynamic properties by means of the multiple linear regression method for the ternary system ethylbenzene-octane-propylbenzene
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Isobaric Vapor Liquid Equilibrium for the Binary Systems of Diethyl Carbonate with Xylene Isomers and Ethylbenzene at 101.33 kPa
• Liquid Phase Equilibria of Aqueous Mixtures of Carboxylic Acids (C1-C4) with Ethylbenzene: Thermodynamic and Mathematical Modeling
• Mutual solubility of aromatic hydrocarbons in pyrrolidinium and ammonium-based ionic liquids and its modeling using the Cubic-Plus-Association (CPA) Equation of State
• Liquid Liquid Equilibria Data for Ethylbenzene or p-Xylene with Alkane and 1-Butylpyridinium Nitrate Ionic Liquid at 298.15 K
• Isobaric Vapor Liquid Equilibrium Data for the Binary Systems of Dimethyl Carbonate with Xylene Isomers at 93.13 kPa
• Measurement and Correlation of the Solubilities of Sulfur S8 in 10 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
• Solubility of 2-Chlorophenylacetic Acid in 12 Pure Solvents from T = (273.15/283.15 to 318.15) K: Determination and Modeling
• Isobaric Vapor-Liquid Equilibrium for Binary and Ternary Systems of 2-Methoxyethanol, Ethylbenzene, and Dimethyl Sulfoxide at 100.00 kPa
• Refractive Index and Vapor-Liquid Equilibrium Data for the Binary Systems of Anisole with Xylene Isomers at 93.13 kPa
• Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
• Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
• o-Nitrophenylacetonitrile Solubility in Several Pure Solvents: Measurement, Correlation, and Solvent Effect Analysis
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• Excess Molar Entalpies of Dimethyl Carbonate with o-Xylene, m-Xylene, p-Xylene, Ethylbenzene, or Ethyl Benzoate at 298.15 K
• Solubility of 1-Alkyl-3-methylimidazolium Hexafluorophosphate in Hydrocarbons
• Excess Molar Enthalpies for Dimethyl Carbonate with o-Xylene, m-Xylene, p-Xylene, Ethylbenzene or Ethyl Benzoate at 298.15 K and 10.2 MPa
• Thermodynamics of Ternary Liquid Mixtures Containing Toluene, Ethylbenzene, and Chlorobenzene
• Infinite Dilution Activity Coefficients of Hydrocarbons in Triethylene Glycol and Tetraethylene Glycol
• Viscosities, Densities, and Ultrasonic Velocities of 3-Pentanone + Ethylbenzene and 3-Pentanone + o-Xylene at (293.15, 303.15, and 313.15) K
• Isobaric Vapor-Liquid Equilibria of the Ternary System Toluene + Ethylbenzene + Amyl Acetate
• 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
• High-Temperature VLE for the Ethylbenzene + Quinoline System
• Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
• 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
• Solubility of Alkylbenzenes and a Model for Predicting the Solubility of Liquid Organics in High-Temperature Water
• Viscosity, Density, and Refractive Index of Some (Ester + Hydrocarbon) Binary Mixtures at 303.15 K and 313.15 K
• Phase Behaviors, Density, and Isothermal Compressibility of Styrene + CO2, Ethylbenzene + CO2, and Ethylbezene + Styrene + CO2 Systems
• Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
• Vapor-Liquid Equilibria Data for Binary Systems of Ethylbenzene + Xylene Isomers at 100.65 kPa
• Solubility of Hexafluorobenzene in Aqueous Salt Solutions from (280 to 340) K
• Viscosities, Densities, and Ultrasonic Velocities of Binary Mixtures of Ethylbenzene with Ethanol, 1-Propanol, and 1-Butanol at (298.15 and 308.15)K
• Liquid-Liquid Equilibria for Cyclohexane + Ethylbenzene + Sulfolane at (303.15, 313.15, and 323.15) K
• Densities, Viscosities, and Refractive Indices of Binary Mixtures of Anisole with Benzene, Methylbenzene, Ethylbenzene, Propylbenzene, and Butylbenzene at (293.15 and 303.15) K
• Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
• Activity Coefficients at Infinite Dilution of Cylcohexylamine + Octane, Toluene, Ethylbenzene, or Aniline and Excess Molar Volumes in Binary Mixtures of Cyclohexylamine + Heptane, Octane, Nonane, Decane, Undecane, Aniline, or Water
• 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
• 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
• Isobaric Vapor-Liquid Equilibria for the Binary Mixtures of Styrene with Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene
• Solubilities at High Dilution of Toluene, Ethylbenzene, 1,2,4-Trimethylbenzene, and Hexane in Di-2-ethylhexyl, Diisoheptyl, and Diisononyl Phthalates
• Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Thermodynamic Properties of Mixtures Containing Ionic Liquids: Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Propyl Boronic Acid-3-Alkylimidazolium Bromide and 1-Propenyl-3-alkylimidazolium Bromide Using Inverse Gas Chromatography
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Liquid-Liquid Equilibria of Ternary and Six-Component Systems Including Cyclohexane, Benzene, Toluene, Ethylbenzene, Cumene, and Sulfolane at 303.15 K
• Ternary Liquid-Liquid Equilibria for Mixtures of an Aromatic + an Aliphatic Hydrocarbon + 4-Methyl-N-butylpyridinium Tetrafluoroborate
• 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
• Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Densities and Surface Tensions of Propyl Acetate + Xylenes or + Ethylbenzene from (298.15 to 308.15) K
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
• Liquid-Liquid Equilibria in Ternary Systems of Aromatic Hydrocarbons (Toluene or Ethylbenzene) + Phenols + Water
• Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
• Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
• Densities, Speeds of Sound, and Isentropic Compressibilities of Binary Mixtures of {Alkan-1-ols + 1,2-Dimethylbenzene, or 1,3-Dimethylbenzene, or 1,4-Dimethylbenzene, or Ethylbenzene} at (293.15, 303.15, and 313.15) K
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• 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
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Butyl-3-methylimidazolium Nitrate Using Gas-Liquid Chromatography
• Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• 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
• Isobaric Vapor-Liquid Equilibium for the Binary Systems of Methyl Formate with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 101.33 kPa
• Isobaric vapor liquid equilibium for the binary systerms of 1-butanol with o-xylene, m-xylene, p-xylene, and ethylbenzene at 101.33 kPa
• Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
• Binary and Ternary Vapor-Liquid Equilibrium Data of the System (Ethylbenzene + Styrene + 4-Methyl-N-butylpyridinium Tetrafluoroborate) at Vacuum Conditions and Liquid-Liquid Equilibrium Data of Their Binary Systems
• 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
• Vapor Liquid Equilibrium for 2-Methyl-1-butanol + Ethylbenzene + Xylene Isomers at 101.33 kPa
• 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
• Isobaric Vapor Liquid Equilibrium of Binary and Ternary Systems with 2-Ethoxyethanol + Ethylbenzene + Dimethyl Sulfoxide
• Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
• Liquid-Liquid Equilibrium for the Ternary System Water + Ethylbenzene + Acetophenone and Water + Ethylbenzene + 1-Phenylethanol
• Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
• 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
• Measurement of Activity Coefficient at Infinite Dilution of Hydrocarbons in Sulfolane Using Gas-Liquid Chromatography
• Solubility of 2,6-Diaminopyridine in Toluene, o-Xylene, Ethylbenzene, Methanol, Ethanol, 2-Propanol, and Sodium Hydroxide Solutions
• Excess Enthalpies of Chloroalkylbenzene + Alkylbenzene Mixtures
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• Solubilities of Vitamin K3 in Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene between (299.44 and 344.24) K
• 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
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Hexyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Thermo Physical Properties of 4-Hydroxy 4-Methyl Pentanone with Nitrobenzene or Ethyl Benzene at Temperatures of (303.15, 313.15, and 323.15) K and a Pressure of 0.1 MPa
• Thermophysical Properties of Isoamyl Acetate or Methyl Benzoate + Hydrocarbon Binary Mixtures, at (303.15 and 313.15) 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
• Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
• Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
• Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes and Aromatic Compounds at T = 313.15 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
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Phase Equilibria of (1-Hexyl-3-methylimidazolium Thiocyanate + Water, Alcohol, or Hydrocarbon) Binary Systems
• 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
• Liquid-Liquid Equilibrium for Ternary Mixtures of Hexane + Aromatic Compounds + [EMpy][ESO4] at T = 298.15 K
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
• 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
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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