Chemical Properties of p-Xylene (CAS 106-42-3)

InChI

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

InChI Key

URLKBWYHVLBVBO-UHFFFAOYSA-N

Formula

C8H10

SMILES

Cc1ccc(C)cc1

Molecular Weight¹

106.17

CAS

106-42-3

Other Names

• 1,4-Dimethylbenzene
• 1,4-Xylene
• 1,4-dimethyl-benzene ( p-xylene)
• 4-Methyltoluene
• Benzene, 1,4-dimethyl-
• Chromar
• NSC 72419
• Scintillar
• p-Dimethylbenzene
• p-Methyltoluene
• p-Xylol
• para-Xylene

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• EA : Electron affinity (eV).
• S_Prot : Protonation entropy at 298K (J/mol×K).
• 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 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°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_fus : Melting 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	0.3200		KDB
PAff	[790.50; 794.40]	kJ/mol
PAff	794.40	kJ/mol	NIST
PAff	793.70	kJ/mol	NIST
PAff	790.50 ± 1.10	kJ/mol	NIST
Tig	738.71	K	KDB
BasG	[766.80; 771.30]	kJ/mol
BasG	766.80	kJ/mol	NIST
BasG	766.90	kJ/mol	NIST
BasG	771.30 ± 1.40	kJ/mol	NIST
ΔcH°liquid	[-4565.90; -4551.44]	kJ/mol
ΔcH°liquid	-4551.44 ± 0.50	kJ/mol	NIST
ΔcH°liquid	-4552.86 ± 0.92	kJ/mol	NIST
ΔcH°liquid	-4551.70	kJ/mol	NIST
ΔcH°liquid	-4565.90	kJ/mol	NIST
Cp,liquid	181.73	J/mol×K	Thermod...
μ	0.10	debye	KDB
η	[0.0006090; 0.0006090]	Pa×s
η	0.0006090	Pa×s	Viscosi...
η	0.0006090	Pa×s	Viscosi...
EA	0.00 ± 0.00	eV	NIST
SProt	44.20	J/mol×K	NIST
LFL	1.10	% in Air	KDB
UFL	6.60	% in Air	KDB
Tflash,oc	300.37	K	KDB
ΔfG°	121.20	kJ/mol	KDB
Rg	3.7960		KDB
Δc,grossH	4552.86	kJ/mol	KDB
Δc,netH	4332.784	kJ/mol	KDB
ΔfH°gas	[17.90; 17.96]	kJ/mol
ΔfH°gas	17.96	kJ/mol	KDB
ΔfH°gas	17.90 ± 1.00	kJ/mol	NIST
ΔfH°liquid	-24.40 ± 1.00	kJ/mol	NIST
ΔfusH°	10.13	kJ/mol	Joback Calculated Property
ΔvapH°	36.34	kJ/mol	Joback Calculated Property
IE	[8.37; 8.80]	eV
IE	8.44 ± 0.05	eV	NIST
IE	8.52 ± 0.01	eV	NIST
IE	8.44	eV	NIST
IE	Outlier 8.80 ± 0.05	eV	NIST
IE	8.37 ± 0.02	eV	NIST
IE	8.52	eV	NIST
IE	8.45	eV	NIST
IE	8.44 ± 0.02	eV	NIST
IE	8.45 ± 0.01	eV	NIST
IE	8.48	eV	NIST
IE	8.44	eV	NIST
IE	8.43	eV	NIST
IE	8.60 ± 0.03	eV	NIST
log10WS	[-2.77; -2.77]
log10WS	-2.77		Estimat...
log10WS	-2.77		Aq. Sol...
logPoct/wat	2.303		Crippen Calculated Property
McVol	99.820	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	2		KDB
Pc	[3343.73; 3617.50]	kPa
Pc	3511.00	kPa	KDB
Pc	3510.00 ± 20.00	kPa	NIST
Pc	3510.70 ± 5.00	kPa	NIST
Pc	3617.50 ± 100.00	kPa	NIST
Pc	3511.00 ± 0.01	kPa	NIST
Pc	3343.73 ± 151.99	kPa	NIST
Pc	3430.00 ± 7.84	kPa	NIST
ρc	[280.70; 282.51]	kg/m3
ρc	281.34 ± 2.12	kg/m3	NIST
ρc	282.51 ± 5.31	kg/m3	NIST
ρc	280.70 ± 4.25	kg/m3	NIST
Inp	[120.40; 908.00]
Inp	859.00		NIST
Inp	848.40		NIST
Inp	855.20		NIST
Inp	852.10		NIST
Inp	850.50		NIST
Inp	852.30		NIST
Inp	856.70		NIST
Inp	883.20		NIST
Inp	888.10		NIST
Inp	874.28		NIST
Inp	847.60		NIST
Inp	850.20		NIST
Inp	852.70		NIST
Inp	855.30		NIST
Inp	857.80		NIST
Inp	860.90		NIST
Inp	863.50		NIST
Inp	857.70		NIST
Inp	867.50		NIST
Inp	876.00		NIST
Inp	876.00		NIST
Inp	876.00		NIST
Inp	863.30		NIST
Inp	871.20		NIST
Inp	857.10		NIST
Inp	857.00		NIST
Inp	857.40		NIST
Inp	857.60		NIST
Inp	856.90		NIST
Inp	863.00		NIST
Inp	857.00		NIST
Inp	857.00		NIST
Inp	867.00		NIST
Inp	867.00		NIST
Inp	856.00		NIST
Inp	866.80		NIST
Inp	871.30		NIST
Inp	866.70		NIST
Inp	866.00		NIST
Inp	866.00		NIST
Inp	854.20		NIST
Inp	859.00		NIST
Inp	849.10		NIST
Inp	854.00		NIST
Inp	866.00		NIST
Inp	856.00		NIST
Inp	879.00		NIST
Inp	881.00		NIST
Inp	848.00		NIST
Inp	853.10		NIST
Inp	871.00		NIST
Inp	890.00		NIST
Inp	866.00		NIST
Inp	866.00		NIST
Inp	866.00		NIST
Inp	866.00		NIST
Inp	862.00		NIST
Inp	886.00		NIST
Inp	865.00		NIST
Inp	848.00		NIST
Inp	863.00		NIST
Inp	880.00		NIST
Inp	866.00		NIST
Inp	868.00		NIST
Inp	866.00		NIST
Inp	868.00		NIST
Inp	863.00		NIST
Inp	862.00		NIST
Inp	859.00		NIST
Inp	857.10		NIST
Inp	857.60		NIST
Inp	860.80		NIST
Inp	868.00		NIST
Inp	876.00		NIST
Inp	864.00		NIST
Inp	868.00		NIST
Inp	872.00		NIST
Inp	878.00		NIST
Inp	859.00		NIST
Inp	861.20		NIST
Inp	867.70		NIST
Inp	872.50		NIST
Inp	878.30		NIST
Inp	860.00		NIST
Inp	860.30		NIST
Inp	854.20		NIST
Inp	858.00		NIST
Inp	848.30		NIST
Inp	853.40		NIST
Inp	858.40		NIST
Inp	858.60		NIST
Inp	859.00		NIST
Inp	859.30		NIST
Inp	854.10		NIST
Inp	854.60		NIST
Inp	859.00		NIST
Inp	861.00		NIST
Inp	859.00		NIST
Inp	861.20		NIST
Inp	865.00		NIST
Inp	861.00		NIST
Inp	861.00		NIST
Inp	855.73		NIST
Inp	882.00		NIST
Inp	886.00		NIST
Inp	868.00		NIST
Inp	849.00		NIST
Inp	854.00		NIST
Inp	857.80		NIST
Inp	861.80		NIST
Inp	863.00		NIST
Inp	867.00		NIST
Inp	868.00		NIST
Inp	872.00		NIST
Inp	875.00		NIST
Inp	850.00		NIST
Inp	908.00		NIST
Inp	858.10		NIST
Inp	861.00		NIST
Inp	865.50		NIST
Inp	864.90		NIST
Inp	858.10		NIST
Inp	894.00		NIST
Inp	884.00		NIST
Inp	850.00		NIST
Inp	855.00		NIST
Inp	860.00		NIST
Inp	894.00		NIST
Inp	901.00		NIST
Inp	907.00		NIST
Inp	888.00		NIST
Inp	862.00		NIST
Inp	870.00		NIST
Inp	863.00		NIST
Inp	860.00		NIST
Inp	861.00		NIST
Inp	853.00		NIST
Inp	859.00		NIST
Inp	861.00		NIST
Inp	863.00		NIST
Inp	864.00		NIST
Inp	864.00		NIST
Inp	864.00		NIST
Inp	885.00		NIST
Inp	866.00		NIST
Inp	859.00		NIST
Inp	889.20		NIST
Inp	864.00		NIST
Inp	877.00		NIST
Inp	874.00		NIST
Inp	864.00		NIST
Inp	878.00		NIST
Inp	862.00		NIST
Inp	884.00		NIST
Inp	855.00		NIST
Inp	860.40		NIST
Inp	872.00		NIST
Inp	847.00		NIST
Inp	884.00		NIST
Inp	861.70		NIST
Inp	864.40		NIST
Inp	866.50		NIST
Inp	849.30		NIST
Inp	877.80		NIST
Inp	869.00		NIST
Inp	884.00		NIST
Inp	866.00		NIST
Inp	852.00		NIST
Inp	856.30		NIST
Inp	865.00		NIST
Inp	873.00		NIST
Inp	845.70		NIST
Inp	851.30		NIST
Inp	855.50		NIST
Inp	855.40		NIST
Inp	869.30		NIST
Inp	861.70		NIST
Inp	864.40		NIST
Inp	866.50		NIST
Inp	853.96		NIST
Inp	854.41		NIST
Inp	865.00		NIST
Inp	855.00		NIST
Inp	854.75		NIST
Inp	854.85		NIST
Inp	855.00		NIST
Inp	863.00		NIST
Inp	855.12		NIST
Inp	859.70		NIST
Inp	856.00		NIST
Inp	854.30		NIST
Inp	861.80		NIST
Inp	853.70		NIST
Inp	859.80		NIST
Inp	864.70		NIST
Inp	855.90		NIST
Inp	860.80		NIST
Inp	866.94		NIST
Inp	842.00		NIST
Inp	851.35		NIST
Inp	854.04		NIST
Inp	855.80		NIST
Inp	865.82		NIST
Inp	868.78		NIST
Inp	870.79		NIST
Inp	867.00		NIST
Inp	871.00		NIST
Inp	862.00		NIST
Inp	863.00		NIST
Inp	865.00		NIST
Inp	864.00		NIST
Inp	853.00		NIST
Inp	870.00		NIST
Inp	875.00		NIST
Inp	863.00		NIST
Inp	888.00		NIST
Inp	872.00		NIST
Inp	879.49		NIST
Inp	854.00		NIST
Inp	875.00		NIST
Inp	872.00		NIST
Inp	856.00		NIST
Inp	861.00		NIST
Inp	868.00		NIST
Inp	866.00		NIST
Inp	868.00		NIST
Inp	870.00		NIST
Inp	872.00		NIST
Inp	852.00		NIST
Inp	860.00		NIST
Inp	845.00		NIST
Inp	853.00		NIST
Inp	854.00		NIST
Inp	857.00		NIST
Inp	870.00		NIST
Inp	864.00		NIST
Inp	850.00		NIST
Inp	865.00		NIST
Inp	890.00		NIST
Inp	874.00		NIST
Inp	870.00		NIST
Inp	862.00		NIST
Inp	865.00		NIST
Inp	858.00		NIST
Inp	868.00		NIST
Inp	867.00		NIST
Inp	872.00		NIST
Inp	861.00		NIST
Inp	899.00		NIST
Inp	856.00		NIST
Inp	874.00		NIST
Inp	876.00		NIST
Inp	853.00		NIST
Inp	854.00		NIST
Inp	853.00		NIST
Inp	853.00		NIST
Inp	884.00		NIST
Inp	856.00		NIST
Inp	870.00		NIST
Inp	884.00		NIST
Inp	868.00		NIST
Inp	849.00		NIST
Inp	848.00		NIST
Inp	864.00		NIST
Inp	875.00		NIST
Inp	884.00		NIST
Inp	872.00		NIST
Inp	883.00		NIST
Inp	864.00		NIST
Inp	857.41		NIST
Inp	868.00		NIST
Inp	872.00		NIST
Inp	860.00		NIST
Inp	857.00		NIST
Inp	865.00		NIST
Inp	875.80		NIST
Inp	865.00		NIST
Inp	854.00		NIST
Inp	859.00		NIST
Inp	860.00		NIST
Inp	849.00		NIST
Inp	852.00		NIST
Inp	851.00		NIST
Inp	848.00		NIST
Inp	859.00		NIST
Inp	853.00		NIST
Inp	853.00		NIST
Inp	853.80		NIST
Inp	847.70		NIST
Inp	854.00		NIST
Inp	855.10		NIST
Inp	854.90		NIST
Inp	866.00		NIST
Inp	860.00		NIST
Inp	861.00		NIST
Inp	849.30		NIST
Inp	851.50		NIST
Inp	854.70		NIST
Inp	857.10		NIST
Inp	859.10		NIST
Inp	848.00		NIST
Inp	851.00		NIST
Inp	854.00		NIST
Inp	856.00		NIST
Inp	858.00		NIST
Inp	851.00		NIST
Inp	852.00		NIST
Inp	854.00		NIST
Inp	832.00		NIST
Inp	862.00		NIST
Inp	881.00		NIST
Inp	875.00		NIST
Inp	875.00		NIST
Inp	875.00		NIST
Inp	889.00		NIST
Inp	870.00		NIST
Inp	868.00		NIST
Inp	872.00		NIST
Inp	864.00		NIST
Inp	866.00		NIST
Inp	864.00		NIST
Inp	875.00		NIST
Inp	875.00		NIST
Inp	860.00		NIST
Inp	864.00		NIST
Inp	861.00		NIST
Inp	888.00		NIST
Inp	848.46		NIST
Inp	867.00		NIST
Inp	857.00		NIST
Inp	878.00		NIST
Inp	864.00		NIST
Inp	844.00		NIST
Inp	863.00		NIST
Inp	870.00		NIST
Inp	863.00		NIST
Inp	904.00		NIST
Inp	873.00		NIST
Inp	875.00		NIST
Inp	861.00		NIST
Inp	867.00		NIST
Inp	855.00		NIST
Inp	866.00		NIST
Inp	863.00		NIST
Inp	855.00		NIST
Inp	870.00		NIST
Inp	870.00		NIST
Inp	865.60		NIST
Inp	871.80		NIST
Inp	871.30		NIST
Inp	870.70		NIST
Inp	861.90		NIST
Inp	868.00		NIST
Inp	853.00		NIST
Inp	855.00		NIST
Inp	846.00		NIST
Inp	853.00		NIST
Inp	860.00		NIST
Inp	876.00		NIST
Inp	858.00		NIST
Inp	860.00		NIST
Inp	874.00		NIST
Inp	864.00		NIST
Inp	Outlier 120.40		NIST
Inp	Outlier 120.40		NIST
Inp	Outlier 121.20		NIST
Inp	Outlier 136.39		NIST
Inp	862.00		NIST
Inp	889.00		NIST
Inp	866.00		NIST
Inp	864.00		NIST
Inp	857.00		NIST
Inp	870.00		NIST
Inp	861.00		NIST
Inp	855.00		NIST
Inp	871.30		NIST
Inp	858.00		NIST
Inp	879.49		NIST
Inp	872.00		NIST
Inp	876.00		NIST
Inp	884.00		NIST
Inp	849.00		NIST
Inp	865.00		NIST
Inp	852.00		NIST
Inp	853.00		NIST
Inp	854.90		NIST
Inp	851.50		NIST
Inp	851.00		NIST
I	[1101.00; 1189.00]
I	1169.50		NIST
I	Outlier 1180.40		NIST
I	1123.00		NIST
I	1123.00		NIST
I	1145.00		NIST
I	1159.94		NIST
I	1165.00		NIST
I	1169.77		NIST
I	1145.24		NIST
I	1149.89		NIST
I	1152.22		NIST
I	1138.90		NIST
I	1143.00		NIST
I	1169.20		NIST
I	1134.80		NIST
I	1118.60		NIST
I	Outlier 1189.00		NIST
I	Outlier 1182.00		NIST
I	1163.00		NIST
I	1170.00		NIST
I	Outlier 1178.00		NIST
I	1156.00		NIST
I	1136.00		NIST
I	1142.00		NIST
I	Outlier 1180.00		NIST
I	1129.00		NIST
I	1134.00		NIST
I	1142.00		NIST
I	1154.20		NIST
I	1117.00		NIST
I	1137.00		NIST
I	1137.00		NIST
I	1117.00		NIST
I	1164.00		NIST
I	1139.00		NIST
I	1123.00		NIST
I	1123.00		NIST
I	1137.00		NIST
I	1125.00		NIST
I	1136.00		NIST
I	1130.00		NIST
I	1130.00		NIST
I	1156.00		NIST
I	1134.00		NIST
I	1136.00		NIST
I	1132.00		NIST
I	1135.00		NIST
I	1140.00		NIST
I	1119.00		NIST
I	1136.00		NIST
I	1119.00		NIST
I	1119.00		NIST
I	1137.00		NIST
I	1140.00		NIST
I	1126.00		NIST
I	1129.00		NIST
I	1156.50		NIST
I	1141.30		NIST
I	1150.60		NIST
I	1117.00		NIST
I	1153.20		NIST
I	1143.40		NIST
I	1146.00		NIST
I	1143.90		NIST
I	1148.70		NIST
I	1130.00		NIST
I	1127.00		NIST
I	1129.00		NIST
I	1130.00		NIST
I	1130.00		NIST
I	1125.00		NIST
I	1120.00		NIST
I	1152.00		NIST
I	1137.00		NIST
I	1140.00		NIST
I	1140.00		NIST
I	1165.00		NIST
I	Outlier 1176.00		NIST
I	1142.00		NIST
I	1153.00		NIST
I	1155.00		NIST
I	1150.00		NIST
I	1154.00		NIST
I	1168.00		NIST
I	Outlier 1178.00		NIST
I	1132.00		NIST
I	1141.00		NIST
I	1119.00		NIST
I	1136.00		NIST
I	Outlier 1101.00		NIST
I	1154.00		NIST
I	1114.00		NIST
I	1137.00		NIST
I	1149.00		NIST
I	1111.00		NIST
I	1140.00		NIST
I	1113.00		NIST
I	1149.00		NIST
I	1129.00		NIST
I	1129.00		NIST
I	1133.00		NIST
I	1129.00		NIST
I	1164.00		NIST
I	1146.00		NIST
I	1142.00		NIST
I	1131.00		NIST
I	1138.00		NIST
I	1133.00		NIST
I	1132.00		NIST
I	1115.00		NIST
I	1132.00		NIST
I	1132.00		NIST
I	1140.00		NIST
I	1153.00		NIST
I	1164.00		NIST
I	1138.00		NIST
I	1142.00		NIST
I	1173.00		NIST
I	1137.00		NIST
I	1127.00		NIST
I	1129.00		NIST
I	1120.00		NIST
I	1120.00		NIST
I	1142.00		NIST
I	1123.00		NIST
I	1140.00		NIST
I	1139.00		NIST
I	1137.00		NIST
I	1119.00		NIST
I	1145.00		NIST
I	1155.00		NIST
I	1139.00		NIST
I	1132.00		NIST
I	1138.00		NIST
I	1155.00		NIST
I	1110.00		NIST
I	1126.00		NIST
I	1140.00		NIST
I	1140.00		NIST
I	1150.00		NIST
I	1165.00		NIST
I	1150.00		NIST
I	1141.00		NIST
S°liquid	[243.51; 253.10]	J/mol×K
S°liquid	247.15	J/mol×K	NIST
S°liquid	243.51	J/mol×K	NIST
S°liquid	253.10	J/mol×K	NIST
Tboil	[411.21; 411.52]	K
Tboil	411.52	K	KDB
Tboil	411.40	K	Isobari...
Tboil	411.45	K	Separat...
Tboil	411.45	K	Vapour-...
Tboil	411.21	K	Investi...
Tboil	411.49	K	Isobari...
Tboil	411.23	K	Isobari...
Tboil	411.37	K	Isobari...
Tc	616.20	K	KDB
Tfus	[285.90; 286.30]	K
Tfus	286.30	K	KDB
Tfus	285.90	K	Aq. Sol...
Ttriple	[286.30; 286.40]	K
Ttriple	286.40 ± 0.01	K	NIST
Ttriple	286.30 ± 0.30	K	NIST
Vc	[0.378; 0.378]	m3/kmol
Vc	0.378	m3/kmol	KDB
Vc	0.378	m3/kmol	NIST
Zc	0.2590380		KDB
Zra	0.26		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[163.20; 211.09]	J/mol×K	[393.00; 523.15]
T(K) Ideal gas heat capacity (J/mol×K) 160 170 180 190 200 210 400 450 500
Cp,gas	163.20 ± 1.70	J/mol×K	393.00	NIST
Cp,gas	166.52 ± 0.33	J/mol×K	398.15	NIST
Cp,gas	175.82 ± 0.35	J/mol×K	423.15	NIST
Cp,gas	178.20 ± 1.70	J/mol×K	428.00	NIST
Cp,gas	185.40 ± 0.37	J/mol×K	448.15	NIST
Cp,gas	189.10 ± 1.70	J/mol×K	463.00	NIST
Cp,gas	194.17 ± 0.39	J/mol×K	473.15	NIST
Cp,gas	202.92 ± 0.41	J/mol×K	498.15	NIST
Cp,gas	211.09 ± 0.42	J/mol×K	523.15	NIST
Cp,liquid	[176.60; 198.70]	J/mol×K	[288.15; 336.00]
T(K) Liquid phase heat capacity (J/mol×K) 175 180 185 190 195 200 300 320
Cp,liquid	178.86	J/mol×K	288.15	Isobari...
Cp,liquid	181.60	J/mol×K	298.00	NIST
Cp,liquid	184.90	J/mol×K	298.00	NIST
Cp,liquid	181.55	J/mol×K	298.15	NIST
Cp,liquid	183.65	J/mol×K	298.15	NIST
Cp,liquid	181.94	J/mol×K	298.15	NIST
Cp,liquid	181.90	J/mol×K	298.15	NIST
Cp,liquid	181.79	J/mol×K	298.15	NIST
Cp,liquid	182.22	J/mol×K	298.15	NIST
Cp,liquid	181.70	J/mol×K	298.15	NIST
Cp,liquid	183.76	J/mol×K	298.15	NIST
Cp,liquid	182.56	J/mol×K	298.15	Isobari...
Cp,liquid	180.30	J/mol×K	299.00	NIST
Cp,liquid	176.60	J/mol×K	303.00	NIST
Cp,liquid	186.15	J/mol×K	308.15	Isobari...
Cp,liquid	198.70	J/mol×K	336.00	NIST
η	[0.0003382; 0.0007010]	Pa×s	[288.15; 353.15]
T(K) Dynamic viscosity (Pa×s) 3.50e-4 4.00e-4 4.50e-4 5.00e-4 5.50e-4 6.00e-4 6.50e-4 7.00e-4 300 320 340
η	0.0007010	Pa×s	288.15	Viscosi...
η	0.0006500	Pa×s	293.15	Viscosi...
η	0.0006162	Pa×s	298.15	Thermod...
η	0.0006090	Pa×s	298.15	Densiti...
η	0.0006110	Pa×s	298.15	Viscosi...
η	0.0006078	Pa×s	298.15	Excess ...
η	0.0006110	Pa×s	298.15	Ultraso...
η	0.0006120	Pa×s	298.15	Densiti...
η	0.0006130	Pa×s	298.15	Densiti...
η	0.0005760	Pa×s	303.15	Viscosi...
η	0.0005660	Pa×s	303.15	Thermop...
η	0.0005726	Pa×s	303.15	Densiti...
η	0.0005740	Pa×s	303.15	Viscome...
η	0.0005660	Pa×s	303.15	Viscosi...
η	0.0005730	Pa×s	303.15	Volumet...
η	0.0005715	Pa×s	303.15	Thermod...
η	0.0005756	Pa×s	303.15	Densiti...
η	0.0005715	Pa×s	303.15	Excess ...
η	0.0005501	Pa×s	308.15	Ultraso...
η	0.0005400	Pa×s	308.15	Densiti...
η	0.0005410	Pa×s	308.15	Densiti...
η	0.0005410	Pa×s	308.15	Density...
η	0.0005420	Pa×s	308.15	Viscome...
η	0.0005374	Pa×s	308.15	Densiti...
η	0.0005170	Pa×s	313.15	Thermop...
η	0.0005170	Pa×s	313.15	Viscosi...
η	0.0005120	Pa×s	313.15	Volumet...
η	0.0005080	Pa×s	313.15	Thermod...
η	0.0005140	Pa×s	313.15	Viscome...
η	0.0005178	Pa×s	313.15	Densiti...
η	0.0005140	Pa×s	313.15	Densiti...
η	0.0004840	Pa×s	318.15	Densiti...
η	0.0004860	Pa×s	318.15	Density...
η	0.0004912	Pa×s	318.15	Ultraso...
η	0.0004882	Pa×s	318.15	Densiti...
η	0.0004860	Pa×s	318.15	Viscome...
η	0.0004599	Pa×s	323.15	Thermod...
η	0.0004610	Pa×s	323.15	Viscome...
η	0.0004641	Pa×s	323.15	Densiti...
η	0.0004610	Pa×s	323.15	Volumet...
η	0.0004595	Pa×s	323.15	Densiti...
η	0.0004599	Pa×s	323.15	Excess ...
η	0.0004439	Pa×s	328.15	Densiti...
η	0.0004171	Pa×s	333.15	Densiti...
η	0.0004298	Pa×s	333.15	Thermod...
η	0.0004189	Pa×s	333.15	Densiti...
η	0.0003809	Pa×s	343.15	Densiti...
η	0.0003783	Pa×s	343.15	Thermod...
η	0.0003487	Pa×s	353.15	Densiti...
η	0.0003382	Pa×s	353.15	Thermod...
ΔfusH	[16.93; 17.12]	kJ/mol	[286.30; 286.40]
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 16.95 17 17.05 17.1 286.3 286.35 286.4
ΔfusH	17.10	kJ/mol	286.30	NIST
ΔfusH	17.11	kJ/mol	286.30	NIST
ΔfusH	17.11	kJ/mol	286.30	NIST
ΔfusH	16.93	kJ/mol	286.30	NIST
ΔfusH	17.11	kJ/mol	286.39	NIST
ΔfusH	17.12	kJ/mol	286.40	NIST
ΔsubH	[59.40; 60.80]	kJ/mol	[266.50; 286.00]
ΔsubH	59.40	kJ/mol	266.50	NIST
ΔsubH	60.80	kJ/mol	286.00	NIST
ΔvapH	[24.70; 42.57]	kJ/mol	[298.00; 583.50]
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 25 30 35 40 300 400 500
ΔvapH	42.57	kJ/mol	298.00	Enthalp...
ΔvapH	41.60	kJ/mol	323.00	NIST
ΔvapH	40.30	kJ/mol	353.00	NIST
ΔvapH	42.40	kJ/mol	369.50	NIST
ΔvapH	40.10	kJ/mol	372.50	NIST
ΔvapH	37.30	kJ/mol	395.00	NIST
ΔvapH	36.00 ± 0.10	kJ/mol	411.00	NIST
ΔvapH	35.98	kJ/mol	411.40	KDB
ΔvapH	35.67	kJ/mol	411.50	NIST
ΔvapH	34.50 ± 0.10	kJ/mol	436.00	NIST
ΔvapH	37.30	kJ/mol	437.00	NIST
ΔvapH	30.50 ± 0.10	kJ/mol	484.00	NIST
ΔvapH	36.10	kJ/mol	506.50	NIST
ΔvapH	24.70 ± 0.10	kJ/mol	540.00	NIST
ΔvapH	36.20	kJ/mol	583.50	NIST
Pvap	[1.12; 250.04]	kPa	[298.15; 449.60]
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 350 400 450
Pvap	1.12	kPa	298.15	(Vapour...
Pvap	1.56	kPa	303.15	Vapor-l...
Pvap	2.49	kPa	313.15	Vapor-l...
Pvap	4.42	kPa	323.15	Vapor-l...
Pvap	7.00	kPa	333.15	Vapor-l...
Pvap	6.85	kPa	333.15	Vapor l...
Pvap	10.63	kPa	343.15	Vapor-l...
Pvap	10.50	kPa	343.15	Vapor l...
Pvap	11.39	kPa	345.15	Vapour-...
Pvap	13.90	kPa	350.15	Vapour-...
Pvap	15.61	kPa	353.15	Vapor l...
Pvap	15.72	kPa	353.15	Vapor-l...
Pvap	16.85	kPa	355.15	Vapour-...
Pvap	19.04	kPa	358.15	Vapor-l...
Pvap	20.30	kPa	360.15	Vapour-...
Pvap	22.80	kPa	363.15	Vapor-l...
Pvap	24.30	kPa	365.15	Vapour-...
Pvap	32.04	kPa	373.15	Vapor-l...
Pvap	40.00	kPa	379.85	Isobari...
Pvap	44.56	kPa	383.15	Vapor-l...
Pvap	60.79	kPa	393.15	Vapor-l...
Pvap	80.87	kPa	403.15	Vapor-l...
Pvap	92.43	kPa	408.15	Vapor-l...
Pvap	93.13	kPa	408.37	Refract...
Pvap	97.30	kPa	410.00	Vapor-L...
Pvap	97.30	kPa	410.00	Isobari...
Pvap	100.04	kPa	410.78	Isobari...
Pvap	101.30	kPa	411.21	Investi...
Pvap	101.30	kPa	411.40	Isobari...
Pvap	101.30	kPa	411.45	Vapour-...
Pvap	101.30	kPa	411.45	Separat...
Pvap	105.00	kPa	412.63	Isobari...
Pvap	124.93	kPa	419.48	Isobari...
Pvap	174.88	kPa	433.57	Isobari...
Pvap	199.86	kPa	439.37	Isobari...
Pvap	224.86	kPa	444.66	Isobari...
Pvap	250.04	kPa	449.56	Isobari...
Pvap	250.00	kPa	449.60	Isobari...
n0	[1.48300; 1.50040]		[288.15; 318.15]
T(K) Refractive Index 1.49 1.49 1.5 1.5 290 300 310
n0	1.49830		288.15	Excess ...
n0	1.49850		288.15	Refract...
n0	1.49850		288.15	Densiti...
n0	1.49577		293.10	Volumet...
n0	1.49220		293.15	Volumet...
n0	1.48580		293.15	Bubble ...
n0	1.49590		293.15	Refract...
n0	1.48580		293.15	Excess ...
n0	1.49590		293.15	Densiti...
n0	1.49577		293.15	Densiti...
n0	1.48580		293.15	Activit...
n0	1.50040		293.15	Solubil...
n0	1.49580		293.15	Excess ...
n0	1.49577		293.15	A study...
n0	1.49312		298.15	Density...
n0	1.49325		298.15	Isobari...
n0	1.49260		298.15	Excess ...
n0	1.49330		298.15	(Vapor ...
n0	1.49330		298.15	Bubble ...
n0	1.49580		298.15	Densiti...
n0	1.49580		298.15	A study...
n0	1.49325		298.15	KDB
n0	1.49321		298.15	Separat...
n0	1.49250		298.15	Liquid-...
n0	1.49300		298.15	Isobari...
n0	1.49290		298.15	Densiti...
n0	1.49321		298.15	Effect ...
n0	1.49290		298.15	Excess ...
n0	1.49298		298.15	Effect ...
n0	1.49330		298.15	Refract...
n0	1.49330		298.15	Densiti...
n0	1.49070		303.15	Refract...
n0	1.49150		303.15	Excess ...
n0	1.48930		303.15	Excess ...
n0	1.49070		303.15	Densiti...
n0	1.48810		308.15	Refract...
n0	1.48790		308.15	Topolog...
n0	1.48670		308.15	Excess ...
n0	1.48810		308.15	Densiti...
n0	1.48550		313.15	Densiti...
n0	1.48550		313.15	Refract...
n0	1.48444		313.15	Density...
n0	1.48300		318.15	Densiti...
n0	1.48300		318.15	Refract...
ρl	[809.07; 865.52]	kg/m3	[288.15; 353.15]
T(K) Liquid Density (kg/m3) 810 820 830 840 850 860 870 300 320 340
ρl	865.31	kg/m3	288.15	Thermod...
ρl	865.52	kg/m3	288.15	Densiti...
ρl	865.30	kg/m3	288.15	Effect ...
ρl	861.00	kg/m3	293.00	KDB
ρl	861.20	kg/m3	293.10	Vapor-L...
ρl	861.17	kg/m3	293.15	Densiti...
ρl	861.00	kg/m3	293.15	Excess ...
ρl	860.97	kg/m3	293.15	Thermod...
ρl	861.21	kg/m3	293.15	Isobari...
ρl	856.63	kg/m3	298.15	Liquid ...
ρl	856.71	kg/m3	298.15	Isobari...
ρl	856.71	kg/m3	298.15	Isobari...
ρl	856.65	kg/m3	298.15	Evaluat...
ρl	856.78	kg/m3	298.15	Liquid ...
ρl	856.50	kg/m3	298.15	Isobari...
ρl	856.54	kg/m3	298.15	Vapor L...
ρl	856.58	kg/m3	298.15	Molar E...
ρl	856.67	kg/m3	298.15	Excess ...
ρl	856.68	kg/m3	298.15	Ebullio...
ρl	858.63	kg/m3	298.15	Molar E...
ρl	856.85	kg/m3	298.15	Excess ...
ρl	856.61	kg/m3	298.15	Acousti...
ρl	856.82	kg/m3	298.15	Densiti...
ρl	856.85	kg/m3	298.15	Excess ...
ρl	856.70	kg/m3	298.15	Excess ...
ρl	856.70	kg/m3	298.15	Excess ...
ρl	856.62	kg/m3	298.15	Effect ...
ρl	856.71	kg/m3	298.15	Isobari...
ρl	856.50	kg/m3	298.15	Determi...
ρl	856.58	kg/m3	298.15	Thermod...
ρl	856.51	kg/m3	298.15	Experim...
ρl	856.63	kg/m3	298.15	Thermod...
ρl	856.54	kg/m3	298.15	Isobari...
ρl	856.51	kg/m3	298.15	Surface...
ρl	852.27	kg/m3	303.15	Thermod...
ρl	852.47	kg/m3	303.15	Densiti...
ρl	852.28	kg/m3	303.15	Excess ...
ρl	848.12	kg/m3	308.15	Densiti...
ρl	847.97	kg/m3	308.15	Effect ...
ρl	847.88	kg/m3	308.15	Acousti...
ρl	847.91	kg/m3	308.15	Thermod...
ρl	843.58	kg/m3	313.15	Excess ...
ρl	843.77	kg/m3	313.15	Densiti...
ρl	843.53	kg/m3	313.15	Thermod...
ρl	839.42	kg/m3	318.15	Densiti...
ρl	839.14	kg/m3	318.15	Thermod...
ρl	839.21	kg/m3	318.15	Effect ...
ρl	834.74	kg/m3	323.15	Thermod...
ρl	834.92	kg/m3	323.15	Excess ...
ρl	830.39	kg/m3	328.15	Effect ...
ρl	830.32	kg/m3	328.15	Thermod...
ρl	825.88	kg/m3	333.15	Thermod...
ρl	826.27	kg/m3	333.15	Excess ...
ρl	817.66	kg/m3	343.15	Excess ...
ρl	809.07	kg/m3	353.15	Excess ...
ΔfusS	[59.14; 59.77]	J/mol×K	[286.30; 286.40]
ΔfusS	59.73	J/mol×K	286.30	NIST
ΔfusS	59.14	J/mol×K	286.30	NIST
ΔfusS	59.75	J/mol×K	286.39	NIST
ΔfusS	59.77	J/mol×K	286.40	NIST
csound,fluid	[1211.00; 1347.94]	m/s	[288.15; 323.15]
T(K) Speed of sound in fluid (m/s) 1200 1250 1300 1350 290 300 310 320
csound,fluid	1347.94	m/s	288.15	Influen...
csound,fluid	1336.86	m/s	290.65	Influen...
csound,fluid	1326.13	m/s	293.15	Influen...
csound,fluid	1330.00	m/s	293.15	Densiti...
csound,fluid	1328.40	m/s	293.15	Physico...
csound,fluid	1315.60	m/s	295.65	Influen...
csound,fluid	1314.00	m/s	298.15	Densiti...
csound,fluid	1305.39	m/s	298.15	Influen...
csound,fluid	1310.00	m/s	298.15	Isentro...
csound,fluid	1308.00	m/s	298.15	Densiti...
csound,fluid	1307.40	m/s	298.15	Physico...
csound,fluid	1295.34	m/s	300.65	Influen...
csound,fluid	1287.30	m/s	303.15	Physico...
csound,fluid	1289.00	m/s	303.15	Densiti...
csound,fluid	1285.42	m/s	303.15	Influen...
csound,fluid	1275.64	m/s	305.65	Influen...
csound,fluid	1276.00	m/s	308.15	Densiti...
csound,fluid	1272.00	m/s	308.15	Densiti...
csound,fluid	1266.13	m/s	308.15	Influen...
csound,fluid	1267.60	m/s	308.15	Physico...
csound,fluid	1256.41	m/s	310.65	Influen...
csound,fluid	1248.30	m/s	313.15	Physico...
csound,fluid	1246.85	m/s	313.15	Influen...
csound,fluid	1249.00	m/s	313.15	Densiti...
csound,fluid	1237.60	m/s	315.65	Influen...
csound,fluid	1229.80	m/s	318.15	Physico...
csound,fluid	1228.14	m/s	318.15	Influen...
csound,fluid	1220.47	m/s	320.65	Influen...
csound,fluid	1211.00	m/s	323.15	Influen...
γ	[0.03; 0.03]	N/m	[293.20; 308.15]
T(K) Surface Tension (N/m) 0.03 0.03 0.03 0.03 0.03 295 300 305
γ	0.03	N/m	293.20	KDB
γ	0.03	N/m	298.15	Experim...
γ	0.03	N/m	298.15	Surface...
γ	0.03	N/m	298.15	Excess ...
γ	0.03	N/m	298.15	Analysi...
γ	0.03	N/m	298.15	Densiti...
γ	0.03	N/m	303.15	Densiti...
γ	0.03	N/m	303.15	Excess ...
γ	0.03	N/m	308.15	Excess ...
γ	0.03	N/m	308.15	Densiti...
γ	0.03	N/m	308.15	Surface...
λ	[0.12; 0.13]	W/m×K	[287.33; 329.16]
T(K) Liquid thermal conductivity (W/m×K) 0.12 0.12 0.12 0.12 0.13 0.13 0.13 300 320
λ	0.13	W/m×K	287.33	Thermal...
λ	0.13	W/m×K	287.55	Thermal...
λ	0.13	W/m×K	287.73	Thermal...
λ	0.13	W/m×K	294.03	Thermal...
λ	0.13	W/m×K	294.27	Thermal...
λ	0.13	W/m×K	294.44	Thermal...
λ	0.12	W/m×K	311.71	Thermal...
λ	0.12	W/m×K	311.94	Thermal...
λ	0.12	W/m×K	312.11	Thermal...
λ	0.12	W/m×K	328.75	Thermal...
λ	0.12	W/m×K	328.99	Thermal...
λ	0.12	W/m×K	329.16	Thermal...

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tfus	286.45	K	100.00	Activit...

Datasets

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

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
293.04	100.00	0.0006
293.04	1000.00	0.0006
293.04	5000.00	0.0007
293.04	10000.00	0.0007
293.03	15000.00	0.0007
293.03	20000.00	0.0008
293.03	25000.00	0.0008
293.03	30000.00	0.0008
302.86	100.00	0.0006
302.86	1000.00	0.0006
302.87	5000.00	0.0006
302.87	10000.00	0.0006
302.88	15000.00	0.0006
302.88	20000.00	0.0007
302.88	25000.00	0.0007
302.89	30000.00	0.0007
312.76	100.00	0.0005
312.76	1000.00	0.0005
312.77	5000.00	0.0005
312.77	10000.00	0.0006
312.76	15000.00	0.0006
312.76	20000.00	0.0006
312.76	25000.00	0.0006
312.76	30000.00	0.0006
322.62	100.00	0.0005
322.63	1000.00	0.0005
322.64	5000.00	0.0005
322.64	10000.00	0.0005
322.64	15000.00	0.0005
322.64	20000.00	0.0005
322.64	25000.00	0.0006
322.65	30000.00	0.0006
332.58	100.00	0.0004
332.58	1000.00	0.0004
332.58	5000.00	0.0004
332.58	10000.00	0.0005
332.58	15000.00	0.0005
332.58	20000.00	0.0005
332.58	25000.00	0.0005
332.57	30000.00	0.0005
342.27	100.00	0.0004
342.27	1000.00	0.0004
342.28	5000.00	0.0004
342.28	10000.00	0.0004
342.29	15000.00	0.0004
342.28	20000.00	0.0004
342.29	25000.00	0.0005
342.29	30000.00	0.0005
352.21	100.00	0.0003
352.21	1000.00	0.0004
352.20	5000.00	0.0004
352.20	10000.00	0.0004
352.20	15000.00	0.0004
352.20	20000.00	0.0004
352.20	25000.00	0.0004
352.20	30000.00	0.0004
362.73	100.00	0.0003
362.74	1000.00	0.0003
362.75	5000.00	0.0003
362.76	10000.00	0.0003
362.76	15000.00	0.0004
362.77	20000.00	0.0004
362.81	25000.00	0.0004
362.82	30000.00	0.0004
372.71	100.00	0.0003
372.71	1000.00	0.0003
372.71	5000.00	0.0003
372.70	10000.00	0.0003
372.70	15000.00	0.0003
372.69	20000.00	0.0003
372.69	25000.00	0.0004
372.69	30000.00	0.0004
Reference

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

Refractive index (Na D-line)

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Refractive index (Na D-line) - Liquid
93.00	298.15	1.4929
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	862.7
293.15	1000.00	863.3
293.15	3000.00	864.7
293.15	5000.00	865.9
293.15	10000.00	869.6
293.15	15000.00	873.0
293.15	20000.00	876.3
293.15	25000.00	879.6
303.15	100.00	852.9
303.15	1000.00	853.8
303.15	3000.00	855.3
303.15	5000.00	856.9
303.15	10000.00	860.6
303.15	15000.00	864.3
303.15	20000.00	867.6
303.15	25000.00	871.0
303.15	30000.00	874.3
303.15	35000.00	877.4
303.15	40000.00	880.3
303.15	50000.00	886.3
303.15	60000.00	892.5
313.15	100.00	843.6
313.15	1000.00	844.7
313.15	3000.00	846.5
313.15	5000.00	848.1
313.15	10000.00	852.0
313.15	15000.00	855.8
313.15	20000.00	859.5
313.15	25000.00	863.0
313.15	30000.00	866.4
313.15	35000.00	869.6
313.15	40000.00	872.8
313.15	50000.00	879.1
313.15	60000.00	884.5
323.15	100.00	835.7
323.15	1000.00	836.7
323.15	3000.00	838.5
323.15	5000.00	840.2
323.15	10000.00	844.5
323.15	15000.00	848.4
323.15	20000.00	852.3
323.15	25000.00	855.7
323.15	30000.00	859.2
323.15	35000.00	862.6
323.15	40000.00	866.1
323.15	50000.00	872.8
323.15	60000.00	878.1
333.15	100.00	827.0
333.15	1000.00	827.8
333.15	3000.00	829.7
333.15	5000.00	831.5
333.15	10000.00	835.9
333.15	15000.00	840.0
333.15	20000.00	844.1
333.15	25000.00	847.9
333.15	30000.00	851.6
333.15	35000.00	855.0
333.15	40000.00	858.8
333.15	50000.00	865.1
333.15	60000.00	871.1
343.15	100.00	817.8
343.15	1000.00	818.8
343.15	3000.00	820.6
343.15	5000.00	823.0
343.15	10000.00	827.2
343.15	15000.00	831.7
343.15	20000.00	836.3
343.15	25000.00	840.0
343.15	30000.00	843.9
343.15	35000.00	847.6
343.15	40000.00	851.0
343.15	50000.00	858.0
343.15	60000.00	864.1
353.15	100.00	808.7
353.15	1000.00	809.6
353.15	3000.00	811.5
353.15	5000.00	813.6
353.15	10000.00	818.1
353.15	15000.00	822.8
353.15	20000.00	827.6
353.15	25000.00	831.5
353.15	30000.00	835.8
353.15	35000.00	839.8
353.15	40000.00	843.4
353.15	50000.00	850.6
353.15	60000.00	856.9
363.15	100.00	799.5
363.15	1000.00	800.7
363.15	3000.00	802.9
363.15	5000.00	805.3
363.15	10000.00	810.2
363.15	15000.00	815.5
363.15	20000.00	819.9
363.15	25000.00	824.1
363.15	30000.00	828.5
363.15	35000.00	832.7
363.15	40000.00	836.7
363.15	50000.00	844.0
363.15	60000.00	850.8
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
288.15	100.00	864.9
298.15	100.00	856.2
308.15	100.00	847.5
288.15	5000.00	868.3
298.15	5000.00	860.2
308.15	5000.00	851.4
288.15	10000.00	871.8
298.15	10000.00	863.5
308.15	10000.00	855.2
288.15	20000.00	878.1
298.15	20000.00	870.1
308.15	20000.00	862.1
288.15	30000.00	884.0
298.15	30000.00	876.5
308.15	30000.00	868.6
288.15	40000.00	889.7
298.15	40000.00	882.2
308.15	40000.00	874.8
Reference

Speed of sound, m/s

Operational condition: Frequency, MHz = 5 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
305.99	1000.00	1281.77
306.07	2050.00	1287.1
306.02	2050.00	1287.22
305.93	3690.00	1296.49
306.00	4900.00	1302.49
305.98	5250.00	1304.38
306.05	6960.00	1312.94
306.03	9400.00	1325.57
306.00	13840.00	1347.72
306.07	16500.00	1360.11
306.06	19900.00	1376.19
306.07	24630.00	1397.78
306.14	26930.00	1407.8
306.18	28370.00	1413.93
306.10	29650.00	1419.72
306.00	30490.00	1423.77
305.99	35160.00	1443.56
305.97	40270.00	1464.54
305.98	45030.00	1483.47
305.98	50870.00	1505.99
323.56	210.00	1206.43
323.57	490.00	1208.1
323.54	1060.00	1211.51
323.57	2600.00	1220.4
323.58	5070.00	1234.53
323.54	6060.00	1240.28
323.58	6090.00	1240.29
323.59	7490.00	1248.03
323.57	10070.00	1262.13
323.58	11110.00	1267.65
323.53	11470.00	1269.76
323.60	15130.00	1288.59
323.59	17890.00	1302.54
323.55	18570.00	1306.1
323.57	20900.00	1317.51
323.59	25130.00	1337.71
323.59	30210.00	1361.29
323.52	30290.00	1361.83
323.48	34540.00	1381.14
323.58	34830.00	1382.01
323.57	39580.00	1402.7
323.47	41260.00	1410.19
323.54	44230.00	1422.37
323.57	44830.00	1424.72
323.54	45010.00	1425.56
323.49	46870.00	1433.42
323.51	49380.00	1443.5
323.47	49810.00	1445.32
323.48	54770.00	1464.84
323.48	55430.00	1467.39
323.47	59650.00	1483.53
323.51	65910.00	1506.74
335.99	280.00	1158.02
335.99	570.00	1159.79
335.98	1230.00	1163.95
335.98	2630.00	1172.56
335.98	5600.00	1190.42
336.00	10270.00	1217.21
335.99	10300.00	1217.47
336.01	14980.00	1243.1
335.99	20370.00	1271.42
336.01	20750.00	1273.3
336.00	24830.00	1293.84
336.00	30890.00	1322.99
336.06	31080.00	1323.64
336.00	34840.00	1341.19
336.02	40670.00	1367.23
336.05	41270.00	1369.78
336.03	41380.00	1370.31
335.98	45230.00	1387.08
335.97	50590.00	1409.56
335.95	55000.00	1427.54
335.96	61040.00	1451.3
335.95	65380.00	1467.88
348.25	40.00	1108.83
348.32	1270.00	1116.85
348.30	2110.00	1122.26
348.27	2120.00	1122.47
348.29	2590.00	1125.51
348.28	4090.00	1135.15
348.32	8600.00	1162.9
348.32	8900.00	1164.69
348.35	10880.00	1176.32
348.37	14620.00	1197.72
348.36	15220.00	1201.14
348.36	20050.00	1227.6
348.45	24930.00	1252.9
348.43	29340.00	1275.02
348.43	33900.00	1297.21
348.43	39830.00	1324.82
348.42	45170.00	1348.71
348.42	49930.00	1369.38
348.42	54750.00	1389.61
348.39	59820.00	1410.34
348.41	59890.00	1410.6
348.37	60580.00	1413.43
348.39	64180.00	1427.64
348.40	64670.00	1429.6
355.98	270.00	1081.04
355.95	490.00	1082.63
355.94	920.00	1085.65
355.95	2620.00	1097.05
355.98	5370.00	1115.13
355.96	10930.00	1149.89
355.89	12280.00	1158.25
355.92	15640.00	1177.67
355.94	20950.00	1207.26
355.95	25050.00	1229.15
355.95	31130.00	1260.21
356.05	34600.00	1276.89
356.02	41360.00	1308.87
356.02	45060.00	1325.7
356.08	50520.00	1349.51
356.04	54960.00	1368.53
356.00	59390.00	1387.08
355.98	65160.00	1410.32
373.59	240.00	1014.61
373.58	570.00	1017.06
373.55	950.00	1020.07
373.53	2520.00	1031.71
373.54	2530.00	1031.73
373.53	5450.00	1052.49
373.60	10260.00	1084.6
373.61	14920.00	1114.21
373.60	19750.00	1143.36
373.62	20290.00	1146.4
373.63	24920.00	1172.65
373.60	29800.00	1199.11
373.60	29850.00	1199.31
373.60	35000.00	1226.08
373.62	39790.00	1249.82
373.62	40800.00	1254.88
373.57	44340.00	1271.77
373.58	49640.00	1296.23
373.63	54980.00	1319.83
373.62	58970.00	1337.14
373.61	59070.00	1337.54
373.64	64880.00	1361.68
398.20	220.00	923.76
398.21	500.00	926.17
398.22	1040.00	930.76
398.25	2490.00	942.77
398.24	5190.00	964.55
398.25	10300.00	1002.89
398.26	12650.00	1019.53
398.24	15110.00	1036.53
398.25	19720.00	1066.63
398.22	20010.00	1068.47
398.22	24890.00	1098.56
398.20	29920.00	1127.9
398.25	31220.00	1135.23
398.24	31220.00	1135.21
398.21	34890.00	1155.44
398.19	37260.00	1168.3
398.20	37270.00	1168.29
398.20	40070.00	1182.91
398.21	44950.00	1207.53
398.23	50040.00	1232.26
398.20	54810.00	1254.71
398.20	60130.00	1278.81
398.21	64730.00	1298.96
422.73	190.00	834.7
422.72	550.00	838.3
422.75	780.00	840.37
422.74	1230.00	844.88
422.65	2630.00	858.44
422.57	5690.00	886.27
422.74	9190.00	915.48
422.75	10020.00	922.14
422.70	14830.00	959.38
422.75	19940.00	995.75
422.75	24810.00	1028.16
422.73	28590.00	1052.11
422.75	29890.00	1060.03
422.77	34850.00	1089.33
422.77	40720.00	1122.29
422.74	44830.00	1144.36
422.72	50170.00	1171.8
422.73	54780.00	1194.57
422.76	59900.00	1218.69
422.75	64580.00	1240.21
447.07	300.00	748.43
447.07	580.00	751.73
447.02	1020.00	756.94
446.94	5130.00	800.91
447.01	7300.00	821.88
446.99	10180.00	848.37
446.99	14830.00	887.97
447.00	19890.00	927.32
447.03	22500.00	946.32
447.02	24900.00	963.22
447.09	30510.00	1000.66
447.13	35270.00	1030.41
447.12	40150.00	1059.45
447.13	45010.00	1086.93
447.08	49880.00	1113.32
447.11	54450.00	1136.99
447.13	59760.00	1163.32
447.08	64750.00	1187.32
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[0.58; 202.65]	kPa	[286.41; 439.06]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.44593e+01
Coefficient B			-3.57809e+03
Coefficient C			-4.79200e+01
Temperature range, min.			286.41
Temperature range, max.			439.06
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400
Pvap	0.58	kPa	286.41	Calculated Property
Pvap	1.57	kPa	303.37	Calculated Property
Pvap	3.76	kPa	320.33	Calculated Property
Pvap	8.12	kPa	337.29	Calculated Property
Pvap	16.10	kPa	354.25	Calculated Property
Pvap	29.72	kPa	371.22	Calculated Property
Pvap	51.60	kPa	388.18	Calculated Property
Pvap	85.01	kPa	405.14	Calculated Property
Pvap	133.86	kPa	422.10	Calculated Property
Pvap	202.65	kPa	439.06	Calculated Property
Pvap	[0.58; 3449.39]	kPa	[286.41; 616.26]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			7.95572e+01
Coefficient B			-7.63795e+03
Coefficient C			-9.52735e+00
Coefficient D			5.74897e-06
Temperature range, min.			286.41
Temperature range, max.			616.26
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 300 400 500 600
Pvap	0.58	kPa	286.41	Calculated Property
Pvap	4.34	kPa	323.06	Calculated Property
Pvap	20.01	kPa	359.71	Calculated Property
Pvap	66.32	kPa	396.36	Calculated Property
Pvap	173.76	kPa	433.01	Calculated Property
Pvap	383.85	kPa	469.66	Calculated Property
Pvap	747.85	kPa	506.31	Calculated Property
Pvap	1327.08	kPa	542.96	Calculated Property
Pvap	2196.10	kPa	579.61	Calculated Property
Pvap	3449.39	kPa	616.26	Calculated Property

Similar Compounds

Find more compounds similar to p-Xylene.

Mixtures

• p-Xylene + Acetic acid, butyl ester
• p-Xylene + 1-Butanol
• n-Hexane + p-Xylene
• Toluene + 2-Pyrrolidinone + p-Xylene
• p-Xylene + 2-Propenoic acid, butyl ester
• Benzene + p-Xylene + Tetrahydropyran
• Toluene + p-Xylene + Tetrahydropyran
• p-Xylene + Decane
• p-Xylene + Tetradecanoic acid, ethyl ester
• Propanoic acid, propyl ester + p-Xylene
• p-Xylene + Carbonic acid, dimethyl ester
• p-Xylene + Carbonic acid, dimethyl ester + Decane
• Phenol, 2-methyl- + p-Xylene
• p-Xylene + Tetrahydrofuran
• p-Xylene + Formamide, N,N-dimethyl-
• p-Xylene + Propane, 2-methoxy-2-methyl-
• p-Xylene + Propane, 2-ethoxy-2-methyl-
• p-Xylene + Formamide, N-methyl-
• p-Xylene + Nonane
• p-Xylene + Octane

Find more mixtures with p-Xylene.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Effect of Temperature on the Change of Refractive Index on Mixing for Butyl Acetate + Aromatic Hydrocarbons
• Isobaric Vapor Liquid Equilibria of 1-Butanol p-Xylene System1
• Experimental Study of the Dynamic Viscosity Deviations in the Binary Systems: Hexane + Ethylbenzene, + o-Xylene, + m-Xylene, + p-Xylene at 298.15 K
• Thermodynamic Properties of Ternary Liquid Mixtures of 2-Pyrrolidinone with Aromatic Hydrocarbons
• Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
• Isentropic Compressibilities Changes of Mixing of Tetrahydropyran and Aromatic Hydrocarbons Ternary Mixtures at 308.15 K
• Bubble temperature measurements on the binary mixtures formed by decane with a variety of compounds at 95.8 kPa
• Activity coefficient at infinite dilution, azeotropic data, excess enthalpies and solid liquid-equilibria for binary systems of alkanes and aromatics with esters
• Experimental and theoretical surface tension deviations in the binary systems propyl propanoate + o-, m- and p-xylene at 298.15K
• Isobaric molar heat capacities of the ternary system dimethyl carbonate + p-xylene + n-decane
• Topological and thermodynamic investigations of molecular interactions in binary mixtures: Molar excess volumes and molar excess enthalpies
• Bubble points of some binary mixtures formed by o-cresol at 95.75 kPa
• 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
• Measurement and prediction of pyrene solubility in pure, binary, ternary and quaternary solvent systems
• Excess Gibbs' energies of the binary mixtures formed by N,N-dimethylformamide with xylenes and cresols at 95.1 kPa
• Influence of temperature on thermodynamics of ethers + xylenes
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
• Isobaric vapor liquid liquid equilibrium and vapor liquid equilibrium for the system water ethanol-1,4-dimethylbenzene at 101.3 kPa
• 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 o-xylene + NMF, m-xylene +NMF and p-xylene +NMF at 333.15 K, 343.15 K and 353.15 K from 0 kPa to 101.3 kPa
• Isomer effect in the separation of octane and xylenes using the ionic liquid 1-ethyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}amide
• Application of [EMpy][ESO4] ionic liquid as solvent for the liquid extraction of xylenes from hexane
• Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
• Study of [EMim][ESO4] ionic liquid as solvent in the liquid-liquid extraction of xylenes from their mixtures with hexane
• 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
• Solubility of elemental sulfur in pure organic solvents and organic solvent-ionic liquid mixtures from 293.15 to 353.15 K
• Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid ethyl(2-hydroxyethyl)dimethyl-ammonium diethylphosphate using gas liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
• Liquid-liquid equilibrium (LLE) data for ternary mixtures of {aliphatic + p-xylene + [EMpy][ESO4]} at T = 313.15 K
• 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
• Solubility and partition coefficient of p-toluic acid in p-xylene and water
• Isobaric vapor-liquid equilibrium data of the binary systems of octane with p, o, m-xylene at 20 kPa
• Phase equilibria of binary mixtures (ionic liquid + aromatic hydrocarbon): Effect of the structure of the components on the solubility
• Isobaric vapor-liquid equilibrium for n-undecane + p-, o-, m-xylene at 10 kPa
• 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
• Liquid liquid equilibria in the ternary systems {hexadecane + BTX aromatics + 2-methoxyethanol or acetonitrile} at 298.15 K
• Isobaric vapor-liquid equilibrium of the binary system sec-butyl acetate + para-xylene and the quaternary system methyl acetate + para-xylene + sec-butyl acetate + acetic acid at 101.3 kPa
• 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
• Liquid-liquid extraction of p-xylene from their mixtures with alkanes using 1-butyl-1-methylmorpholinium tricyanomethanide and 1- butyl-3-methylimidazolium tricyanomethanide ionic liquids
• 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
• Liquid-liquid equilibria for the extraction of furfural from aqueous solution using different solvents
• 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
• Liquid densities for n-decane + p-xylene mixtures from 293.15 K to 363.15 K at pressures up to 60 MPa
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• 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
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
• New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• (Vapour + liquid) equilibria of (1-butanol + benzene, or toluene, or o-, or m-, or p-xylene) at T = 308.15 K
• Volumetric properties of (cyclohexanone + a xylene) at temperature between (293.15 and 353.15) K
• Densities and volumetric properties of a (xylene + dimethyl sulfoxide) at temperature from (293.15 to 353.15) K
• A study of densities and volumetric properties of binary mixtures containing nitrobenzene at T = (293.15 to 353.15) K
• Excess volumes and partial molar volumes of binary mixtures of 1,2-propanediol carbonate with xylene in the temperature range of (293.15 to 353.15) K
• Liquid phase behaviour of 1-hexyloxymethyl-3-methyl-imidazolium-based ionic liquids with hydrocarbons: The influence of anion
• (Vapor + liquid) equilibria of binary mixtures formed by iso-octane with a variety of compounds at 95.8 kPa
• 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)
• 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 binary mixtures of xylene with N,N-dimethylformamide at different temperatures
• Thermodynamics of mixtures involving some (benzene derivatives + benzonitrile)
• A study of densities and volumetric properties of binary mixtures of N-methyl-2-pyrrolidone with xylene at different temperatures and atmospheric pressure
• Activity coefficients and excess Gibbs free energy of some binary mixtures formed by p-cresol at 95.23 kPa
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• 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 and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
• Surface tension, density, and speed of sound for the ternary mixture {diethyl carbonate + p-xylene + decane}
• 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
• Excess thermodynamic functions derived from densities and surface tensions of (p- or o-xylene + ethylene glycol dimethyl ether) between the temperatures (298.15 and 308.15) K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
• (Liquid + liquid) equilibria in the binary systems (aliphatic, or aromatic hydrocarbons + 1-ethyl-3-methylimidazolium ethylsulfate, or 1-butyl-3-methylimidazolium methylsulfate ionic liquids)
• LLE data for the ionic liquid 3-methyl-N-butyl pyridinium dicyanamide with several aromatic and aliphatic hydrocarbons
• Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
• 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
• Excess molar volumes, excess molar enthalpies, and excess isentropic compressibilities of tetrahydropyran with aromatic hydrocarbons
• 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 measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
• 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
• Thermophysical properties for (diethyl carbonate + p-xylene + octane) ternary system
• 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
• 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 and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
• Measurement and correlation of phase equilibria for (water + aromatic hydrocarbon) binary mixtures at T = (573 to 623) K using microfluidic mixing
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
• Liquid-liquid 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
• 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
• 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
• 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
• Phase equilibria for the [{water + 1-methylnaphthalene + p-xylene}] system at T = (573, 623 and 653) K
• 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 and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Phase behaviour of aqueous mixtures of acetic acid with isomers of xylene
• 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
• Experimental and Nitta-Chao model prediction of high pressure density of p-xylene with dialkyl carbonates or n-alkanes
• 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
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium methyl sulfate
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Thermodynamics of solvation in propylene glycol and methyl cellosolve
• Isothermal (liquid + liquid) equilibrium data at T = 313.15 K and isobaric (vapor + liquid + liquid) equilibrium data at 101.3 kPa for the ternary system (water + 1-butanol + p-xylene)
• Measurement and correlation of solubility of 4-chloro-2,5-dimethoxynitrobenzene and 4-chloro-2,5- dimethoxyaniline in methanol, ethanol, xylene and toluene
• 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
• Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
• Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution of alkanes, alkenes, alkyl benzenes in dimethylphosphate based ionic liquids using gas liquid chromatography
• Viscosity measurements of ortho-xylene, meta-xylene, para-xylene and ethylbenzene
• 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
• Liquid-liquid equilibria for ternary systems polyoxymethylene dimethyl ethers + para-xylene + water
• 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
• Determination of melting temperatures in hydrocarbon mixtures by differential scanning calorimetry
• 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 azeotrope (2,2,3,3-tetrafluoro-1-propanol + water): Isobaric vapour-liquid phase equilibrium measurements and azeotropic distillation
• Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
• Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• 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
• Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
• Vapour-liquid equilibrium measurements and extractive distillation process design for separation of azeotropic mixture (dimethyl carbonate + ethanol)
• Speed of sound and derived thermodynamic properties of para-xylene at temperatures between (306 and 448) K and at pressures up to 66 MPa
• Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
• Molecular interactions in binary mixtures containing o-toluidine
• Excess molar volumes and excess isentropic compressibilities of 2-pyrrolidinone at 308.15K
• Excess Molar Enthalpies for Binary and Ternary Mixtures containing Cyclic Ether, 2-Methylaniline and Aromatic Hydrocarbons
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Investigation on Thermodynamics in Separation for Ethylene Glycol + Neopentyl Glycol System by Azeotropic Distillation
• Liquid Liquid Equilibria, Equilibrium Phase Densities, and Refractive Indices for the Quaternary Mixtures Containing 2-Propanol or 2-Methyl-2-Propanol of Fuel Oxygenate at T = 298.15 and 318.15 K
• Isobaric Vapor Liquid Equilibrium for the Binary Systems of Diethyl Carbonate with Xylene Isomers and Ethylbenzene at 101.33 kPa
• Mutual solubility of aromatic hydrocarbons in pyrrolidinium and ammonium-based ionic liquids and its modeling using the Cubic-Plus-Association (CPA) Equation of State
• Elimination of Tar in Biomass Gasification Process: Liquid Liquid Equilibrium of Ternary Systems {Water + Solvent (p-Xylene and Methyl Hexadecanoate) + Model Molecules of Tar (Thiophene, Pyridine, Naphthalene, Phenathrene, and Anthracene)}
• Isobaric Vapor Liquid Equilibrium for Binary Systems of Cyclohexanone + Benzene, Cyclohexanone + Toluene, and Cyclohexanone + p-Xylene at 101.3 kPa
• Liquid Liquid Equilibria Data for Ethylbenzene or p-Xylene with Alkane and 1-Butylpyridinium Nitrate Ionic Liquid at 298.15 K
• Liquid Liquid Equilibria of Binary, Ternary, and Quaternary Systems Involving Monoethylene Glycol, Water, Toluene, p-Xylene, Hexane, and Octane
• Experimental Determination and Correlation of Liquid Liquid Equilibria for Water + Cyclohexanone + Solvents (Toluene or p-Xylene) Ternary Systems at 303.15 and 323.15 K under 101.3 kPa
• Isobaric Vapor Liquid Equilibrium Data for the Binary Systems of Dimethyl Carbonate with Xylene Isomers at 93.13 kPa
• Determination and Correlation of Liquid-Liquid Equilibria Data for Water + Cyclohexanol + (Mesityl Oxide, Toluene, and p-Xylene) Ternary Systems at Different Temperatures
• Viscometric Studies of Molecular Interactions in Binary Liquid Mixtures of Isomeric Xylenes with Methanol
• 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
• Refractive Index and Vapor-Liquid Equilibrium Data for the Binary Systems of Anisole with Xylene Isomers at 93.13 kPa
• Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
• Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
• Isobaric Vapor-Liquid Equilibrium Measurements for Separation of Azeotrope (Methanol + Methyl Acetate)
• Separation of Alkylbenzenes from n-Heptane Using Binary Mixtures of Ionic Solvents
• Determination and Correlation of Solubility of Borneol, Camphor, and Isoborneol in Different Solvents
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• Liquid-liquid equilibria for mixtures of (Furfural + an Aromatic hydrocarbon + an alkane) at T=298.15 K
• 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
• 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
• Excess Molar Volumes and Surface Tensions of Xylene with Acetone or 2-Butanone at 298.15 K
• 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
• Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures of Ethanol, Methylcyclohexane and p-Xylene
• Excess Molar Volumes and Surface Tensions of Xylene with Isopropyl Ether or Methyl tert-Butyl Ether at 298.15 K
• Viscosity, Density, and Refractive Index of Some (Ester + Hydrocarbon) Binary Mixtures at 303.15 K and 313.15 K
• Vapor-Liquid Equilibria Data for Binary Systems of Ethylbenzene + Xylene Isomers at 100.65 kPa
• Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
• Viscosities, Densities, and Speeds of Sound of Binary Mixtures of o-Xylene, m-Xylene, p-Xylene, and Isopropylbenzene with 2-Butanone at 298.15 K
• Viscosities, Densities, and Speeds of Sound of Binary Mixtures of o-Xylene, m-Xylene, p-Xylene, and Isopropylbenzene with 4-Methylpentan-2-one at 298.15 K
• Isobaric Vapor-Liquid Equilibria at 97.3 kPa and Excess Properties at (303.15, 308.15, and 313.15) K of Binary Mixture of p-Xylene + Decane
• Vapor-Liquid Equilibria and Excess Properties of the Binary System Vinyl Acetate + p-Xylene
• Solubilities of 2-(6-Oxido-6H-dibenz[c,e][1,2]oxaphosphorin-6-yl)-methanol in the Selected Solvents
• Isobaric Vapor-Liquid Equilibria for the Binary Mixtures of Styrene with Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene
• Solubilities of Benzene, Toluene, and Xylene Isomers in 1-Butyl-3-methylimidazolium Tetrafluoroborate
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• 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
• 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
• 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
• Volumetric and Viscometric Behavior of the Binary System: (Hexan-1-ol + p-Xylene)
• Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
• Vapor-Liquid Equilibria and Density Measurement for Binary Mixtures of Benzene + Nonane, Methylbenzene + 1,2-Dimethylbenzene, 1,3-Dimethylbenzene + 2,3,4,5-Tetrahydrothiophene-1,1-dioxide (Sulfolane), 1,2-Dimethylbenzene + Sulfolane, 1,2-Dimethylbenzene + N-Methylformamide (NMF), 1,3-Dimethylbenzene + NMF, and 1,4-Dimethylbenzene + NMF from (333.15 to 353.15) K at Vacuum Conditions
• 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
• Density and Viscosity of the Binary Mixtures of Hexan-1-ol with Isomeric Xylenes at T = (308.15 and 318.15) K and Atmospheric Pressure
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
• 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
• Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
• Ebulliometric Determination and Prediction of Vapor Liquid Equilibria for Binary Mixtures of Ethanol and Ethyl Hexanoate
• Excess Molar Volumes of 2,4,6,8-Tetramethylcyclotetrasiloxane with Benzene, Toluene, and Xylene at T = (288.15, 298.15, and 308.15) K
• 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
• Evaluation of the Performance of Four Solvents for the Liquid Liquid Extraction of Acrylic Acid from Water
• Densities, Excess Molar Volumes, Viscosity, and Refractive Indices of Binary Mixtures of Ethanoic Acid and Trichloroethylene with Dimethylbenzenes at Different Temperatures
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Dibutylphosphate Using Gas Liquid Chromatography
• Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
• Isobaric Vapor Liquid Equilibria for Binary Systems Comprising 1-Chloro-2-ethylhexane, 2-Ethyl-1-hexanol, p-Xylene, and N-Methylpyrrolidone (NMP) at 40.0 kPa
• 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
• Surface Tension of Dialkyl Carbonates + (Alkanes or 1,4-Dimethylbenzene) and 1,4-Dimethylbenzene + Alkanes Binary Mixtures at T = 308.15 K
• 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
• Liquid Liquid Equilibria for the Ternary Systems of 4-Methyl-1,3-dioxolan-2-one + 1,4-Dimethylbenzene + Octane, Decane, or Dodecane and the Ternary Systems of Acetonitrile + Morpholine + Octane, Decane, or Dodecane at 313.15 K or 298.15 K
• 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
• Liquid Liquid Equilibria at Three Temperatures (between 280.15 K and 333.15 K) of Binary, Ternary, and Quaternary Systems Involving Monoethylene Glycol, Water, Cyclohexane, para-Xylene, trans- and cis-Dimethylcyclohexane, and trans- and cis-Decahydronaphthalene
• Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
• 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
• Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
• 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
• Effect of an Ionic Liquid (IL) Cation on the Ternary System (IL + p-Xylene + Hexane) at T= 298.15 K
• Solubilities of Vitamin K3 in Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene between (299.44 and 344.24) K
• Excess Enthalpies of (N-Methylformamide or N-Methylacetamide) + Aromatic Compounds at 303.15 K
• 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
• 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
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Hexyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
• Molar Excess Volumes and Excess Isentropic Compressibilities of Ternary Mixtures of o-Toluidine
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Measurement of Infinite Dilution Activity Coefficients of Alcohols, Ketones, and Aromatic Hydrocarbons in 4-Methyl-N-butylpyridinium Tetrafluoroborate and 1-Butyl-3-methylimidazolium Hexafluorophosphate by Gas-Liquid Chromatography
• Thermophysical Properties of Isoamyl Acetate or Methyl Benzoate + Hydrocarbon Binary Mixtures, at (303.15 and 313.15) K
• Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
• Analysis of Surface Tension, Density, and Speed of Sound for the Ternary Mixture Dimethyl Carbonate + p-Xylene + n-Octane
• Viscosities of p-Xylene, Acetic Acid, and p-Xylene + Acetic Acid at (313.15 to 473.15) K and (0.10 to 3.20) MPa: Determined by the Rolling-Ball Method
• Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
• 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
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Surface Tension Deviations and Excess Molar Volumes on the Ternary System Propyl Propanoate + Hexane + p-Xylene at 298.15 K
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
• 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
• Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes with o-Xylene, m-Xylene, p-Xylene, and Mesitylene at T = (298.15 and 313.15) K
• Solubility of Triadimefon in Organic Solvents at Temperatures between (288.15 and 333.15) 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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