Chemical Properties of o-Xylene (CAS 95-47-6)

InChI

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

InChI Key

CTQNGGLPUBDAKN-UHFFFAOYSA-N

Formula

C8H10

SMILES

Cc1ccccc1C

Molecular Weight¹

106.17

CAS

95-47-6

Other Names

• 1,2-Dimethylbenzene
• 1,2-Xylene
• 1,2-dimethyl-benzene ( o-xylene)
• 2-Methyltoluene
• 3,4-Xylene
• Benzene, 1,2-dimethyl-
• NSC 60920
• o-Dimethylbenzene
• o-Methyltoluene
• o-Xylol
• ortho-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).
• S_Prot : Protonation entropy at 298K (J/mol×K).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_c,grossH : Heat of Combustion, Gross form (kJ/mol).
• Δ_c,netH : Heat of Combustion, Net Form (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_subH : Enthalpy of sublimation at 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).
• 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_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

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

Physical Properties

Property	Value	Unit	Source
ω	0.3100		KDB
PAff	[791.20; 796.00]	kJ/mol
PAff	796.00	kJ/mol	NIST
PAff	791.20	kJ/mol	NIST
PAff	793.50 ± 1.70	kJ/mol	NIST
Tig	738.15	K	KDB
BasG	[765.30; 772.10]	kJ/mol
BasG	768.30	kJ/mol	NIST
BasG	765.30	kJ/mol	NIST
BasG	772.10 ± 2.20	kJ/mol	NIST
ΔcH°liquid	[-4581.40; -4551.48]	kJ/mol
ΔcH°liquid	-4551.48 ± 0.50	kJ/mol	NIST
ΔcH°liquid	-4552.90 ± 1.00	kJ/mol	NIST
ΔcH°liquid	-4567.60	kJ/mol	NIST
ΔcH°liquid	-4581.40	kJ/mol	NIST
Cp,liquid	187.28	J/mol×K	Thermod...
μ	0.50	debye	KDB
η	[0.0007680; 0.0007690]	Pa×s
η	0.0007680	Pa×s	Viscosi...
η	0.0007690	Pa×s	Viscosi...
SProt	36.90	J/mol×K	NIST
LFL	1.10	% in Air	KDB
UFL	7.00	% in Air	KDB
Tflash,cc	297.04	K	KDB
Tflash,oc	290.37	K	KDB
ΔfG°	122.20	kJ/mol	KDB
Rg	3.7890		KDB
Δc,grossH	4552.86	kJ/mol	KDB
Δc,netH	4332.784	kJ/mol	KDB
ΔfH°gas	[19.00; 19.00]	kJ/mol
ΔfH°gas	19.00	kJ/mol	KDB
ΔfH°gas	19.00 ± 1.10	kJ/mol	NIST
ΔfH°liquid	-24.40 ± 1.10	kJ/mol	NIST
ΔfusH°	10.13	kJ/mol	Joback Calculated Property
ΔvapH°	36.34	kJ/mol	Joback Calculated Property
IE	[8.45; 8.85]	eV
IE	8.56 ± 0.04	eV	NIST
IE	8.56 ± 0.01	eV	NIST
IE	Outlier 8.85 ± 0.05	eV	NIST
IE	8.45 ± 0.02	eV	NIST
IE	8.70	eV	NIST
IE	8.60 ± 0.10	eV	NIST
IE	8.61	eV	NIST
IE	8.55	eV	NIST
IE	8.56 ± 0.01	eV	NIST
IE	8.56 ± 0.02	eV	NIST
IE	8.58 ± 0.01	eV	NIST
IE	8.56	eV	NIST
IE	8.57 ± 0.03	eV	NIST
IE	8.57	eV	NIST
IE	8.75 ± 0.03	eV	NIST
log10WS	[-2.80; -2.80]
log10WS	-2.80		Estimat...
log10WS	-2.80		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	3732.00	kPa	KDB
ρc	[286.54; 287.71]	kg/m3
ρc	286.65 ± 4.25	kg/m3	NIST
ρc	286.54 ± 5.31	kg/m3	NIST
ρc	287.71 ± 4.25	kg/m3	NIST
Inp	[128.10; 933.00]
Inp	879.40		NIST
Inp	874.60		NIST
Inp	875.70		NIST
Inp	873.40		NIST
Inp	871.90		NIST
Inp	874.20		NIST
Inp	878.70		NIST
Inp	918.00		NIST
Inp	908.30		NIST
Inp	915.10		NIST
Inp	874.17		NIST
Inp	874.10		NIST
Inp	874.64		NIST
Inp	900.00		NIST
Inp	868.00		NIST
Inp	870.90		NIST
Inp	873.80		NIST
Inp	876.70		NIST
Inp	879.50		NIST
Inp	882.40		NIST
Inp	885.20		NIST
Inp	877.40		NIST
Inp	878.32		NIST
Inp	890.30		NIST
Inp	880.00		NIST
Inp	892.90		NIST
Inp	877.60		NIST
Inp	877.80		NIST
Inp	878.00		NIST
Inp	878.10		NIST
Inp	877.40		NIST
Inp	884.00		NIST
Inp	877.00		NIST
Inp	878.00		NIST
Inp	889.00		NIST
Inp	889.00		NIST
Inp	878.00		NIST
Inp	889.80		NIST
Inp	895.60		NIST
Inp	888.80		NIST
Inp	888.80		NIST
Inp	889.80		NIST
Inp	887.30		NIST
Inp	888.00		NIST
Inp	889.00		NIST
Inp	874.00		NIST
Inp	879.60		NIST
Inp	889.00		NIST
Inp	875.00		NIST
Inp	868.30		NIST
Inp	874.00		NIST
Inp	895.00		NIST
Inp	914.00		NIST
Inp	889.00		NIST
Inp	889.00		NIST
Inp	889.00		NIST
Inp	889.00		NIST
Inp	893.00		NIST
Inp	885.00		NIST
Inp	884.00		NIST
Inp	868.40		NIST
Inp	905.00		NIST
Inp	881.00		NIST
Inp	890.00		NIST
Inp	888.00		NIST
Inp	891.00		NIST
Inp	885.00		NIST
Inp	884.00		NIST
Inp	882.00		NIST
Inp	877.60		NIST
Inp	878.10		NIST
Inp	882.20		NIST
Inp	900.00		NIST
Inp	885.00		NIST
Inp	890.00		NIST
Inp	896.00		NIST
Inp	903.00		NIST
Inp	844.00		NIST
Inp	880.80		NIST
Inp	883.00		NIST
Inp	890.30		NIST
Inp	896.40		NIST
Inp	903.20		NIST
Inp	895.00		NIST
Inp	880.00		NIST
Inp	868.90		NIST
Inp	880.30		NIST
Inp	880.50		NIST
Inp	880.80		NIST
Inp	881.50		NIST
Inp	875.60		NIST
Inp	875.90		NIST
Inp	879.90		NIST
Inp	880.80		NIST
Inp	874.30		NIST
Inp	874.50		NIST
Inp	880.80		NIST
Inp	883.00		NIST
Inp	886.00		NIST
Inp	880.00		NIST
Inp	880.00		NIST
Inp	872.00		NIST
Inp	874.00		NIST
Inp	877.26		NIST
Inp	896.00		NIST
Inp	900.00		NIST
Inp	881.00		NIST
Inp	870.00		NIST
Inp	875.00		NIST
Inp	878.90		NIST
Inp	883.70		NIST
Inp	886.00		NIST
Inp	877.00		NIST
Inp	885.00		NIST
Inp	889.00		NIST
Inp	891.00		NIST
Inp	894.00		NIST
Inp	898.00		NIST
Inp	870.70		NIST
Inp	903.00		NIST
Inp	880.00		NIST
Inp	883.00		NIST
Inp	888.40		NIST
Inp	888.10		NIST
Inp	880.10		NIST
Inp	864.00		NIST
Inp	871.00		NIST
Inp	877.00		NIST
Inp	882.00		NIST
Inp	918.00		NIST
Inp	926.00		NIST
Inp	933.00		NIST
Inp	911.00		NIST
Inp	885.00		NIST
Inp	893.00		NIST
Inp	882.00		NIST
Inp	908.00		NIST
Inp	893.20		NIST
Inp	891.00		NIST
Inp	884.00		NIST
Inp	875.00		NIST
Inp	881.00		NIST
Inp	881.00		NIST
Inp	887.00		NIST
Inp	887.00		NIST
Inp	910.00		NIST
Inp	883.80		NIST
Inp	880.00		NIST
Inp	887.00		NIST
Inp	894.00		NIST
Inp	893.00		NIST
Inp	896.00		NIST
Inp	886.00		NIST
Inp	894.00		NIST
Inp	862.00		NIST
Inp	894.00		NIST
Inp	881.80		NIST
Inp	896.00		NIST
Inp	888.00		NIST
Inp	889.90		NIST
Inp	891.20		NIST
Inp	871.00		NIST
Inp	898.40		NIST
Inp	890.00		NIST
Inp	863.00		NIST
Inp	888.00		NIST
Inp	863.00		NIST
Inp	877.70		NIST
Inp	890.00		NIST
Inp	886.00		NIST
Inp	897.00		NIST
Inp	876.00		NIST
Inp	892.10		NIST
Inp	867.90		NIST
Inp	872.30		NIST
Inp	876.70		NIST
Inp	877.00		NIST
Inp	850.00		NIST
Inp	888.00		NIST
Inp	889.90		NIST
Inp	891.20		NIST
Inp	875.31		NIST
Inp	875.68		NIST
Inp	875.00		NIST
Inp	875.88		NIST
Inp	875.89		NIST
Inp	876.00		NIST
Inp	888.00		NIST
Inp	887.00		NIST
Inp	881.30		NIST
Inp	875.60		NIST
Inp	874.60		NIST
Inp	870.77		NIST
Inp	874.14		NIST
Inp	876.31		NIST
Inp	887.70		NIST
Inp	891.29		NIST
Inp	893.63		NIST
Inp	875.00		NIST
Inp	875.12		NIST
Inp	874.00		NIST
Inp	897.40		NIST
Inp	900.00		NIST
Inp	888.00		NIST
Inp	894.00		NIST
Inp	896.00		NIST
Inp	903.66		NIST
Inp	877.00		NIST
Inp	895.00		NIST
Inp	890.00		NIST
Inp	881.00		NIST
Inp	884.00		NIST
Inp	889.00		NIST
Inp	890.00		NIST
Inp	895.00		NIST
Inp	896.00		NIST
Inp	883.00		NIST
Inp	865.00		NIST
Inp	874.00		NIST
Inp	874.00		NIST
Inp	880.00		NIST
Inp	894.00		NIST
Inp	838.00		NIST
Inp	875.00		NIST
Inp	888.00		NIST
Inp	895.00		NIST
Inp	894.00		NIST
Inp	883.00		NIST
Inp	889.00		NIST
Inp	881.00		NIST
Inp	890.00		NIST
Inp	891.00		NIST
Inp	893.00		NIST
Inp	896.00		NIST
Inp	883.00		NIST
Inp	898.00		NIST
Inp	901.00		NIST
Inp	898.00		NIST
Inp	876.00		NIST
Inp	882.00		NIST
Inp	884.00		NIST
Inp	885.00		NIST
Inp	878.00		NIST
Inp	868.00		NIST
Inp	901.00		NIST
Inp	901.00		NIST
Inp	871.00		NIST
Inp	873.00		NIST
Inp	890.00		NIST
Inp	899.00		NIST
Inp	896.00		NIST
Inp	896.00		NIST
Inp	902.00		NIST
Inp	887.00		NIST
Inp	877.74		NIST
Inp	896.00		NIST
Inp	881.00		NIST
Inp	877.00		NIST
Inp	896.00		NIST
Inp	898.00		NIST
Inp	860.00		NIST
Inp	896.50		NIST
Inp	850.00		NIST
Inp	879.00		NIST
Inp	885.00		NIST
Inp	883.00		NIST
Inp	869.00		NIST
Inp	872.00		NIST
Inp	892.00		NIST
Inp	879.00		NIST
Inp	878.00		NIST
Inp	876.00		NIST
Inp	876.00		NIST
Inp	889.00		NIST
Inp	875.60		NIST
Inp	870.50		NIST
Inp	873.40		NIST
Inp	877.30		NIST
Inp	880.10		NIST
Inp	882.50		NIST
Inp	870.00		NIST
Inp	873.00		NIST
Inp	876.00		NIST
Inp	879.00		NIST
Inp	882.00		NIST
Inp	877.00		NIST
Inp	871.00		NIST
Inp	875.00		NIST
Inp	854.00		NIST
Inp	880.00		NIST
Inp	879.00		NIST
Inp	894.00		NIST
Inp	896.00		NIST
Inp	905.00		NIST
Inp	894.00		NIST
Inp	891.00		NIST
Inp	896.00		NIST
Inp	870.00		NIST
Inp	878.00		NIST
Inp	872.00		NIST
Inp	888.00		NIST
Inp	910.00		NIST
Inp	889.00		NIST
Inp	884.00		NIST
Inp	882.00		NIST
Inp	898.00		NIST
Inp	869.52		NIST
Inp	903.00		NIST
Inp	904.00		NIST
Inp	890.00		NIST
Inp	878.00		NIST
Inp	901.00		NIST
Inp	883.00		NIST
Inp	875.00		NIST
Inp	878.00		NIST
Inp	886.00		NIST
Inp	892.00		NIST
Inp	906.00		NIST
Inp	895.00		NIST
Inp	882.00		NIST
Inp	890.00		NIST
Inp	855.00		NIST
Inp	875.00		NIST
Inp	886.00		NIST
Inp	875.00		NIST
Inp	881.00		NIST
Inp	892.00		NIST
Inp	895.00		NIST
Inp	888.20		NIST
Inp	896.40		NIST
Inp	894.90		NIST
Inp	894.80		NIST
Inp	884.00		NIST
Inp	866.00		NIST
Inp	876.00		NIST
Inp	884.00		NIST
Inp	900.00		NIST
Inp	879.00		NIST
Inp	885.00		NIST
Inp	884.00		NIST
Inp	900.00		NIST
Inp	880.00		NIST
Inp	Outlier 128.10		NIST
Inp	Outlier 128.40		NIST
Inp	Outlier 130.67		NIST
Inp	883.80		NIST
I	[1155.00; 1234.30]
I	1221.00		NIST
I	Outlier 1234.30		NIST
I	1174.00		NIST
I	1174.00		NIST
I	1174.60		NIST
I	1188.70		NIST
I	1191.40		NIST
I	1193.00		NIST
I	1200.00		NIST
I	1186.00		NIST
I	1209.84		NIST
I	1215.66		NIST
I	1221.09		NIST
I	1192.98		NIST
I	1198.32		NIST
I	1204.40		NIST
I	1185.70		NIST
I	1191.00		NIST
I	1183.90		NIST
I	1164.90		NIST
I	Outlier 1230.00		NIST
I	Outlier 1232.00		NIST
I	1210.00		NIST
I	1218.00		NIST
I	Outlier 1227.00		NIST
I	1201.00		NIST
I	1184.00		NIST
I	1181.00		NIST
I	1185.00		NIST
I	1185.00		NIST
I	1191.00		NIST
I	1178.00		NIST
I	1183.00		NIST
I	1171.00		NIST
I	1195.00		NIST
I	1159.00		NIST
I	1204.40		NIST
I	1187.00		NIST
I	1174.00		NIST
I	1187.00		NIST
I	1174.00		NIST
I	1189.00		NIST
I	1192.00		NIST
I	1175.00		NIST
I	1188.00		NIST
I	1177.00		NIST
I	1184.00		NIST
I	1187.00		NIST
I	1190.00		NIST
I	1169.00		NIST
I	1183.00		NIST
I	1181.00		NIST
I	1191.00		NIST
I	1190.00		NIST
I	1191.00		NIST
I	1176.00		NIST
I	1190.00		NIST
I	1175.00		NIST
I	1176.00		NIST
I	1189.00		NIST
I	1193.00		NIST
I	1208.00		NIST
I	1186.00		NIST
I	1182.00		NIST
I	1175.00		NIST
I	1186.00		NIST
I	1186.00		NIST
I	1190.00		NIST
I	1188.00		NIST
I	1191.00		NIST
I	1216.00		NIST
I	Outlier 1229.00		NIST
I	1189.00		NIST
I	1203.00		NIST
I	1202.00		NIST
I	1198.00		NIST
I	1201.00		NIST
I	1213.00		NIST
I	Outlier 1225.00		NIST
I	1178.00		NIST
I	1188.00		NIST
I	1165.00		NIST
I	1204.00		NIST
I	1159.00		NIST
I	1177.00		NIST
I	1189.00		NIST
I	1197.00		NIST
I	1173.00		NIST
I	1178.00		NIST
I	1181.00		NIST
I	1174.00		NIST
I	1171.00		NIST
I	1192.00		NIST
I	1180.00		NIST
I	1181.00		NIST
I	Outlier 1155.00		NIST
I	1182.00		NIST
I	1182.00		NIST
I	1182.00		NIST
I	1187.00		NIST
I	Outlier 1225.00		NIST
I	1172.00		NIST
I	1175.00		NIST
I	1182.00		NIST
I	1163.00		NIST
I	1171.00		NIST
I	1175.00		NIST
I	1171.00		NIST
I	1187.00		NIST
I	1166.00		NIST
I	1191.00		NIST
I	1186.00		NIST
I	1188.00		NIST
I	1165.00		NIST
I	Outlier 1232.00		NIST
I	1186.00		NIST
I	1183.00		NIST
I	1183.00		NIST
I	Outlier 1232.00		NIST
I	1171.00		NIST
I	1191.00		NIST
I	1180.00		NIST
I	1190.00		NIST
I	1191.00		NIST
S°gas	353.60 ± 1.30	J/mol×K	NIST
S°liquid	[246.02; 248.10]	J/mol×K
S°liquid	246.02	J/mol×K	NIST
S°liquid	248.10	J/mol×K	NIST
Tboil	[417.43; 417.60]	K
Tboil	417.60	K	KDB
Tboil	417.50	K	Isobari...
Tboil	417.43	K	Measure...
Tboil	417.55	K	Vapor-L...
Tboil	417.56	K	Isobari...
Tc	630.30	K	KDB
Tfus	[247.90; 248.08]	K
Tfus	247.90	K	KDB
Tfus	248.08	K	Aq. Sol...
Ttriple	247.80 ± 0.25	K	NIST
Vc	[0.370; 0.370]	m3/kmol
Vc	0.370	m3/kmol	KDB
Vc	0.370	m3/kmol	NIST
Zc	0.2634870		KDB
Zra	0.26		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[168.20; 192.50]	J/mol×K	[393.00; 463.00]
Cp,gas	168.20 ± 1.70	J/mol×K	393.00	NIST
Cp,gas	182.00 ± 1.70	J/mol×K	428.00	NIST
Cp,gas	192.50 ± 2.10	J/mol×K	463.00	NIST
Cp,liquid	[182.40; 206.70]	J/mol×K	[298.00; 347.00]
Cp,liquid	187.00	J/mol×K	298.00	NIST
Cp,liquid	183.89	J/mol×K	298.10	NIST
Cp,liquid	187.65	J/mol×K	298.15	NIST
Cp,liquid	187.58	J/mol×K	298.15	NIST
Cp,liquid	187.82	J/mol×K	298.15	NIST
Cp,liquid	182.40	J/mol×K	303.00	NIST
Cp,liquid	206.70	J/mol×K	347.00	NIST
η	[0.0004136; 0.0008710]	Pa×s	[288.15; 353.15]
η	0.0008710	Pa×s	288.15	Viscosi...
η	0.0008100	Pa×s	293.15	Viscosi...
η	0.0008092	Pa×s	293.15	Viscosi...
η	0.0007440	Pa×s	298.15	Excess ...
η	0.0007590	Pa×s	298.15	Densiti...
η	0.0007576	Pa×s	298.15	Ultraso...
η	0.0007580	Pa×s	298.15	Densiti...
η	0.0007560	Pa×s	298.15	Viscosi...
η	0.0007610	Pa×s	298.15	Densiti...
η	0.0006950	Pa×s	303.15	Viscosi...
η	0.0007172	Pa×s	303.15	Viscosi...
η	0.0007080	Pa×s	303.15	Viscosi...
η	0.0007100	Pa×s	303.15	Viscome...
η	0.0007095	Pa×s	303.15	Densiti...
η	0.0007062	Pa×s	303.15	Excess ...
η	0.0006950	Pa×s	303.15	Thermop...
η	0.0007404	Pa×s	303.15	Densiti...
η	0.0006900	Pa×s	308.15	Densiti...
η	0.0006580	Pa×s	308.15	Densiti...
η	0.0006690	Pa×s	308.15	Ultraso...
η	0.0006660	Pa×s	308.15	Viscome...
η	0.0006660	Pa×s	308.15	Density...
η	0.0006650	Pa×s	308.15	Densiti...
η	0.0006210	Pa×s	313.15	Thermop...
η	0.0006210	Pa×s	313.15	Viscosi...
η	0.0006292	Pa×s	313.15	Viscosi...
η	0.0006261	Pa×s	313.15	Densiti...
η	0.0006451	Pa×s	313.15	Densiti...
η	0.0006280	Pa×s	313.15	Viscome...
η	0.0005972	Pa×s	318.15	Ultraso...
η	0.0005910	Pa×s	318.15	Viscome...
η	0.0006117	Pa×s	318.15	Densiti...
η	0.0005890	Pa×s	318.15	Densiti...
η	0.0005910	Pa×s	318.15	Density...
η	0.0005554	Pa×s	323.15	Excess ...
η	0.0005600	Pa×s	323.15	Viscome...
η	0.0005584	Pa×s	323.15	Densiti...
η	0.0005711	Pa×s	323.15	Densiti...
η	0.0005433	Pa×s	328.15	Densiti...
η	0.0005105	Pa×s	333.15	Densiti...
η	0.0005020	Pa×s	333.15	Densiti...
η	0.0004544	Pa×s	343.15	Densiti...
η	0.0004136	Pa×s	353.15	Densiti...
ΔfusH	[13.60; 13.60]	kJ/mol	[247.80; 247.82]
ΔfusH	13.60	kJ/mol	247.80	NIST
ΔfusH	13.60	kJ/mol	247.80	NIST
ΔfusH	13.60	kJ/mol	247.82	NIST
ΔsubH	60.10	kJ/mol	248.00	NIST
ΔvapH	[36.24; 45.00]	kJ/mol	[298.00; 598.50]
ΔvapH	43.07	kJ/mol	298.00	Enthalp...
ΔvapH	45.00	kJ/mol	298.00	NIST
ΔvapH	41.10	kJ/mol	376.00	NIST
ΔvapH	40.80	kJ/mol	378.00	NIST
ΔvapH	39.80	kJ/mol	401.00	NIST
ΔvapH	36.82	kJ/mol	417.50	KDB
ΔvapH	36.24	kJ/mol	417.60	NIST
ΔvapH	38.00	kJ/mol	444.50	NIST
ΔvapH	36.70	kJ/mol	521.00	NIST
ΔvapH	36.70	kJ/mol	598.50	NIST
Pvap	[0.88; 250.00]	kPa	[298.15; 456.10]
Pvap	0.88	kPa	298.15	(Vapour...
Pvap	2.05	kPa	313.15	Vapor-l...
Pvap	3.60	kPa	323.15	Vapor-L...
Pvap	3.46	kPa	323.15	Vapor-l...
Pvap	5.44	kPa	333.15	Vapor l...
Pvap	5.32	kPa	333.15	Vapor l...
Pvap	5.61	kPa	333.15	Vapor-l...
Pvap	5.45	kPa	333.15	Vapor l...
Pvap	8.54	kPa	343.15	Vapor-l...
Pvap	8.47	kPa	343.15	Vapor l...
Pvap	9.18	kPa	345.15	Vapour-...
Pvap	11.27	kPa	350.15	Vapour-...
Pvap	12.66	kPa	353.15	Vapor l...
Pvap	12.73	kPa	353.15	Vapor-l...
Pvap	12.80	kPa	353.15	Vapor l...
Pvap	12.71	kPa	353.15	Vapor l...
Pvap	13.73	kPa	355.15	Vapour-...
Pvap	14.75	kPa	357.30	Extensi...
Pvap	16.62	kPa	360.15	Vapour-...
Pvap	18.65	kPa	363.15	Vapor-l...
Pvap	20.00	kPa	365.15	Vapour-...
Pvap	20.40	kPa	365.49	Vapor l...
Pvap	26.73	kPa	373.15	Vapor-l...
Pvap	29.61	kPa	376.70	Extensi...
Pvap	30.14	kPa	376.75	Vapor l...
Pvap	31.66	kPa	378.15	Vapor-l...
Pvap	37.35	kPa	383.15	Vapor-l...
Pvap	40.20	kPa	385.55	Vapor l...
Pvap	43.63	kPa	388.15	Vapor-l...
Pvap	49.44	kPa	392.70	Extensi...
Pvap	50.43	kPa	392.87	Vapor l...
Pvap	50.60	kPa	393.04	Vapor-L...
Pvap	51.01	kPa	393.15	Vapor-l...
Pvap	60.03	kPa	398.66	Vapor l...
Pvap	64.27	kPa	401.50	Extensi...
Pvap	68.42	kPa	403.15	Vapor-l...
Pvap	70.27	kPa	404.09	Vapor l...
Pvap	80.41	kPa	408.83	Vapor l...
Pvap	90.54	kPa	413.06	Vapor l...
Pvap	90.18	kPa	413.15	Vapor-l...
Pvap	90.39	kPa	413.15	Vapor-L...
Pvap	93.13	kPa	414.41	Refract...
Pvap	101.85	kPa	417.28	Vapor l...
Pvap	101.30	kPa	417.43	Measure...
Pvap	102.78	kPa	418.60	Extensi...
Pvap	250.00	kPa	456.10	Isobari...
n0	[1.48580; 1.50830]		[288.15; 318.15]
n0	1.50830		288.15	Densiti...
n0	1.50720		288.15	Excess ...
n0	1.50830		288.15	Refract...
n0	1.50570		293.10	Volumet...
n0	1.48580		293.15	Activit...
n0	1.50150		293.15	Volumet...
n0	1.50550		293.15	Excess ...
n0	1.50550		293.15	Bubble ...
n0	1.50570		293.15	Densiti...
n0	1.50573		293.15	A study...
n0	1.50550		293.15	Refract...
n0	1.50470		293.15	Excess ...
n0	1.50550		293.15	Solubil...
n0	1.50550		293.15	Densiti...
n0	1.50260		298.00	Vapor-L...
n0	1.50180		298.15	Excess ...
n0	1.50280		298.15	Phase e...
n0	1.50280		298.15	Phase e...
n0	1.50180		298.15	Liquid-...
n0	1.50200		298.15	Isobari...
n0	1.50260		298.15	Vapor-L...
n0	1.50570		298.15	A study...
n0	1.50240		298.15	Densiti...
n0	1.50262		298.15	Density...
n0	1.50300		298.15	Bubble ...
n0	1.50290		298.15	Refract...
n0	1.50290		298.15	Densiti...
n0	1.50570		298.15	Densiti...
n0	1.50295		298.15	KDB
n0	1.50000		303.15	Excess ...
n0	1.50020		303.15	Refract...
n0	1.50020		303.15	Densiti...
n0	1.49750		308.15	Densiti...
n0	1.49750		308.15	Refract...
n0	1.50310		308.15	Topolog...
n0	1.49480		313.15	Densiti...
n0	1.49480		313.15	Refract...
n0	1.49466		313.15	Density...
n0	1.49210		318.15	Refract...
n0	1.49210		318.15	Densiti...
ρl	[746.76; 884.09]	kg/m3	[288.15; 353.15]
ρl	883.91	kg/m3	288.15	Thermod...
ρl	884.09	kg/m3	288.15	Densiti...
ρl	884.07	kg/m3	288.15	Effect ...
ρl	880.00	kg/m3	293.00	KDB
ρl	879.68	kg/m3	293.15	Isobari...
ρl	879.72	kg/m3	293.15	Thermod...
ρl	879.83	kg/m3	293.15	Densiti...
ρl	878.60	kg/m3	293.15	Excess ...
ρl	875.36	kg/m3	298.15	Acousti...
ρl	875.81	kg/m3	298.15	Vapor L...
ρl	875.90	kg/m3	298.15	Bubble ...
ρl	859.54	kg/m3	298.15	Isobari...
ρl	859.54	kg/m3	298.15	Isobari...
ρl	875.50	kg/m3	298.15	Isobari...
ρl	875.52	kg/m3	298.15	Evaluat...
ρl	875.91	kg/m3	298.15	Thermod...
ρl	875.72	kg/m3	298.15	Excess ...
ρl	875.99	kg/m3	298.15	Molar E...
ρl	875.92	kg/m3	298.15	Excess ...
ρl	875.92	kg/m3	298.15	Excess ...
ρl	875.00	kg/m3	298.15	Excess ...
ρl	875.00	kg/m3	298.15	Excess ...
ρl	875.60	kg/m3	298.15	Volumet...
ρl	875.81	kg/m3	298.15	Isobari...
ρl	875.57	kg/m3	298.15	Densiti...
ρl	875.51	kg/m3	298.15	Thermod...
ρl	875.99	kg/m3	298.15	Thermod...
ρl	874.89	kg/m3	298.15	Experim...
ρl	875.67	kg/m3	298.15	Effect ...
ρl	875.91	kg/m3	298.15	Heat ca...
ρl	875.90	kg/m3	298.15	Molar E...
ρl	875.50	kg/m3	298.20	Isobari...
ρl	871.70	kg/m3	303.15	Heat ca...
ρl	871.30	kg/m3	303.15	Thermod...
ρl	872.25	kg/m3	303.15	Excess ...
ρl	871.70	kg/m3	303.15	Thermod...
ρl	871.31	kg/m3	303.15	Densiti...
ρl	871.50	kg/m3	303.15	Densiti...
ρl	867.48	kg/m3	308.15	Thermod...
ρl	867.05	kg/m3	308.15	Densiti...
ρl	867.30	kg/m3	308.15	Effect ...
ρl	867.48	kg/m3	308.15	Heat ca...
ρl	867.07	kg/m3	308.15	Thermod...
ρl	867.20	kg/m3	308.15	Densiti...
ρl	866.51	kg/m3	308.15	Acousti...
ρl	862.79	kg/m3	313.15	Densiti...
ρl	862.80	kg/m3	313.15	Densiti...
ρl	862.83	kg/m3	313.15	Thermod...
ρl	859.67	kg/m3	313.15	Excess ...
ρl	858.81	kg/m3	318.15	Effect ...
ρl	858.57	kg/m3	318.15	Thermod...
ρl	858.53	kg/m3	318.15	Densiti...
ρl	858.80	kg/m3	318.15	Densiti...
ρl	840.84	kg/m3	323.15	Excess ...
ρl	854.30	kg/m3	323.15	Thermod...
ρl	854.30	kg/m3	323.15	Densiti...
ρl	850.24	kg/m3	328.15	Effect ...
ρl	850.01	kg/m3	328.15	Thermod...
ρl	845.71	kg/m3	333.15	Thermod...
ρl	815.74	kg/m3	333.15	Excess ...
ρl	784.38	kg/m3	343.15	Excess ...
ρl	746.76	kg/m3	353.15	Excess ...
ΔfusS	54.87	J/mol×K	247.82	NIST
csound,fluid	[1240.87; 1381.29]	m/s	[288.15; 323.15]
csound,fluid	1381.29	m/s	288.15	Influen...
csound,fluid	1371.75	m/s	290.65	Influen...
csound,fluid	1362.16	m/s	293.15	Influen...
csound,fluid	1369.00	m/s	293.15	Densiti...
csound,fluid	1367.70	m/s	293.15	Physico...
csound,fluid	1351.83	m/s	295.65	Influen...
csound,fluid	1347.50	m/s	298.15	Physico...
csound,fluid	1341.51	m/s	298.15	Influen...
csound,fluid	1346.00	m/s	298.15	Isentro...
csound,fluid	1331.21	m/s	300.65	Influen...
csound,fluid	1320.96	m/s	303.15	Influen...
csound,fluid	1329.40	m/s	303.15	Physico...
csound,fluid	1328.00	m/s	303.15	Densiti...
csound,fluid	1310.79	m/s	305.65	Influen...
csound,fluid	1300.66	m/s	308.15	Influen...
csound,fluid	1313.30	m/s	308.15	Physico...
csound,fluid	1290.59	m/s	310.65	Influen...
csound,fluid	1298.50	m/s	313.15	Physico...
csound,fluid	1280.61	m/s	313.15	Influen...
csound,fluid	1289.00	m/s	313.15	Densiti...
csound,fluid	1270.55	m/s	315.65	Influen...
csound,fluid	1285.20	m/s	318.15	Physico...
csound,fluid	1260.62	m/s	318.15	Influen...
csound,fluid	1250.66	m/s	320.65	Influen...
csound,fluid	1240.87	m/s	323.15	Influen...
γ	[0.02; 0.03]	N/m	[293.20; 343.15]
γ	0.03	N/m	293.20	KDB
γ	0.03	N/m	298.15	Densiti...
γ	0.03	N/m	298.15	Excess ...
γ	0.03	N/m	298.15	Experim...
γ	0.03	N/m	303.15	Excess ...
γ	0.03	N/m	303.15	Surface...
γ	0.03	N/m	303.15	Densiti...
γ	0.03	N/m	308.15	Excess ...
γ	0.03	N/m	308.15	Surface...
γ	0.03	N/m	308.15	Densiti...
γ	0.03	N/m	313.15	Surface...
γ	0.03	N/m	318.15	Surface...
γ	0.03	N/m	323.15	Surface...
γ	0.03	N/m	333.15	Surface...
γ	0.02	N/m	343.15	Surface...
λ	[0.12; 0.14]	W/m×K	[257.75; 329.09]
λ	0.14	W/m×K	257.75	Thermal...
λ	0.14	W/m×K	257.96	Thermal...
λ	0.14	W/m×K	258.10	Thermal...
λ	0.13	W/m×K	277.07	Thermal...
λ	0.13	W/m×K	277.27	Thermal...
λ	0.13	W/m×K	277.42	Thermal...
λ	0.13	W/m×K	295.56	Thermal...
λ	0.13	W/m×K	295.78	Thermal...
λ	0.13	W/m×K	295.91	Thermal...
λ	0.13	W/m×K	312.07	Thermal...
λ	0.13	W/m×K	312.29	Thermal...
λ	0.13	W/m×K	312.44	Thermal...
λ	0.12	W/m×K	328.72	Thermal...
λ	0.12	W/m×K	328.94	Thermal...
λ	0.12	W/m×K	329.09	Thermal...

Datasets

1. Viscosity, Pa*s (2)
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
273.48	100.00	0.0011
273.48	1000.00	0.0011
273.48	5000.00	0.0012
273.48	10000.00	0.0012
273.48	15000.00	0.0013
273.48	20000.00	0.0013
273.48	25000.00	0.0014
273.48	30000.00	0.0014
283.22	100.00	0.0009
283.22	1000.00	0.0010
283.22	5000.00	0.0010
283.21	10000.00	0.0010
283.21	15000.00	0.0011
283.21	20000.00	0.0011
283.21	25000.00	0.0012
283.21	30000.00	0.0012
293.04	100.00	0.0008
293.04	1000.00	0.0008
293.04	5000.00	0.0009
293.04	10000.00	0.0009
293.05	15000.00	0.0009
293.05	20000.00	0.0010
293.05	25000.00	0.0010
293.06	30000.00	0.0010
302.87	100.00	0.0007
302.87	1000.00	0.0007
302.88	5000.00	0.0007
302.88	10000.00	0.0008
302.88	15000.00	0.0008
302.87	20000.00	0.0008
302.87	25000.00	0.0009
302.87	30000.00	0.0009
312.66	100.00	0.0006
312.67	1000.00	0.0006
312.67	5000.00	0.0007
312.66	10000.00	0.0007
312.67	15000.00	0.0007
312.66	20000.00	0.0007
312.66	25000.00	0.0008
312.66	30000.00	0.0008
321.85	100.00	0.0006
321.85	1000.00	0.0006
321.86	5000.00	0.0006
321.85	10000.00	0.0006
321.85	15000.00	0.0006
321.86	20000.00	0.0007
321.86	25000.00	0.0007
321.85	30000.00	0.0007
332.47	100.00	0.0005
332.47	1000.00	0.0005
332.48	5000.00	0.0005
332.48	10000.00	0.0006
332.48	15000.00	0.0006
332.48	20000.00	0.0006
332.48	25000.00	0.0006
332.48	30000.00	0.0007
343.06	100.00	0.0005
343.07	1000.00	0.0005
343.07	5000.00	0.0005
343.07	10000.00	0.0005
343.08	15000.00	0.0005
343.09	20000.00	0.0005
343.08	25000.00	0.0006
343.08	30000.00	0.0006
353.04	100.00	0.0004
353.04	1000.00	0.0004
353.03	5000.00	0.0004
353.02	10000.00	0.0005
353.02	15000.00	0.0005
353.02	20000.00	0.0005
353.02	25000.00	0.0005
353.01	30000.00	0.0005
362.85	100.00	0.0004
362.85	1000.00	0.0004
362.85	5000.00	0.0004
362.85	10000.00	0.0004
362.86	15000.00	0.0004
362.86	20000.00	0.0005
362.87	25000.00	0.0005
362.87	30000.00	0.0005
372.83	100.00	0.0004
372.84	1000.00	0.0004
372.84	5000.00	0.0004
372.85	10000.00	0.0004
372.86	15000.00	0.0004
372.86	20000.00	0.0004
372.85	25000.00	0.0004
372.86	30000.00	0.0004
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.15	101.30	0.0007
Reference

Refractive index (Na D-line)

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Refractive index (Na D-line) - Liquid
93.00	298.15	1.5022
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	890.5
283.15	1000.00	890.8
283.15	3000.00	892.4
283.15	5000.00	893.5
283.15	10000.00	896.7
283.15	15000.00	899.0
283.15	20000.00	902.6
283.15	25000.00	905.3
283.15	30000.00	908.1
283.15	35000.00	910.9
283.15	40000.00	913.3
283.15	50000.00	918.2
283.15	60000.00	923.0
293.15	100.00	879.7
293.15	1000.00	879.9
293.15	3000.00	881.4
293.15	5000.00	882.4
293.15	10000.00	885.9
293.15	15000.00	888.9
293.15	20000.00	892.0
293.15	25000.00	894.9
293.15	30000.00	897.8
293.15	35000.00	900.5
293.15	40000.00	903.1
293.15	50000.00	908.5
293.15	60000.00	913.1
303.15	100.00	870.9
303.15	1000.00	871.6
303.15	3000.00	873.0
303.15	5000.00	874.4
303.15	10000.00	877.8
303.15	15000.00	881.1
303.15	20000.00	884.2
303.15	25000.00	887.3
303.15	30000.00	890.3
303.15	35000.00	893.1
303.15	40000.00	895.9
303.15	50000.00	901.2
303.15	60000.00	906.4
313.15	100.00	862.7
313.15	1000.00	862.9
313.15	3000.00	864.5
313.15	5000.00	865.9
313.15	10000.00	869.6
313.15	15000.00	873.0
313.15	20000.00	876.3
313.15	25000.00	879.6
313.15	30000.00	882.7
313.15	35000.00	885.7
313.15	40000.00	888.4
313.15	50000.00	894.2
313.15	60000.00	899.2
323.15	100.00	853.8
323.15	1000.00	854.6
323.15	3000.00	856.1
323.15	5000.00	857.7
323.15	10000.00	861.5
323.15	15000.00	865.2
323.15	20000.00	868.8
323.15	25000.00	872.0
323.15	30000.00	875.3
323.15	35000.00	878.4
323.15	40000.00	881.5
323.15	50000.00	887.3
323.15	60000.00	892.8
333.15	100.00	845.1
333.15	1000.00	846.0
333.15	3000.00	847.8
333.15	5000.00	849.4
333.15	10000.00	853.3
333.15	15000.00	857.1
333.15	20000.00	860.9
333.15	25000.00	864.4
333.15	30000.00	867.8
333.15	35000.00	871.0
333.15	40000.00	874.3
333.15	50000.00	880.3
333.15	60000.00	886.0
343.15	100.00	836.3
343.15	1000.00	837.2
343.15	3000.00	839.0
343.15	5000.00	840.9
343.15	10000.00	844.9
343.15	15000.00	849.0
343.15	20000.00	853.0
343.15	25000.00	856.6
343.15	30000.00	860.2
343.15	35000.00	863.7
343.15	40000.00	866.8
343.15	50000.00	873.2
343.15	60000.00	878.9
353.15	100.00	827.8
353.15	1000.00	828.6
353.15	3000.00	830.6
353.15	5000.00	832.4
353.15	10000.00	836.9
353.15	15000.00	841.2
353.15	20000.00	845.1
353.15	25000.00	849.1
353.15	30000.00	852.8
353.15	35000.00	856.4
353.15	40000.00	859.8
353.15	50000.00	866.3
353.15	60000.00	872.5
363.15	100.00	819.3
363.15	1000.00	820.3
363.15	3000.00	822.4
363.15	5000.00	824.3
363.15	10000.00	828.7
363.15	15000.00	833.6
363.15	20000.00	837.6
363.15	25000.00	841.5
363.15	30000.00	845.5
363.15	35000.00	849.3
363.15	40000.00	853.1
363.15	50000.00	859.8
363.15	60000.00	866.3
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[305.32; 445.43]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.44465e+01
Coefficient B			-3.60720e+03
Coefficient C			-5.05540e+01
Temperature range, min.			305.32
Temperature range, max.			445.43
Pvap	1.33	kPa	305.32	Calculated Property
Pvap	3.01	kPa	320.89	Calculated Property
Pvap	6.23	kPa	336.46	Calculated Property
Pvap	11.95	kPa	352.02	Calculated Property
Pvap	21.51	kPa	367.59	Calculated Property
Pvap	36.64	kPa	383.16	Calculated Property
Pvap	59.51	kPa	398.73	Calculated Property
Pvap	92.72	kPa	414.29	Calculated Property
Pvap	139.29	kPa	429.86	Calculated Property
Pvap	202.65	kPa	445.43	Calculated Property
Pvap	[0.02; 3724.86]	kPa	[247.98; 630.37]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			8.33218e+01
Coefficient B			-7.94623e+03
Coefficient C			-1.00606e+01
Coefficient D			5.93974e-06
Temperature range, min.			247.98
Temperature range, max.			630.37
Pvap	0.02	kPa	247.98	Calculated Property
Pvap	0.55	kPa	290.47	Calculated Property
Pvap	5.38	kPa	332.96	Calculated Property
Pvap	28.61	kPa	375.44	Calculated Property
Pvap	102.23	kPa	417.93	Calculated Property
Pvap	278.49	kPa	460.42	Calculated Property
Pvap	628.00	kPa	502.91	Calculated Property
Pvap	1238.99	kPa	545.39	Calculated Property
Pvap	2222.36	kPa	587.88	Calculated Property
Pvap	3724.86	kPa	630.37	Calculated Property

Similar Compounds

Find more compounds similar to o-Xylene.

Mixtures

• n-Hexane + o-Xylene
• Toluene + 2-Pyrrolidinone + o-Xylene
• 2-Propenoic acid, butyl ester + o-Xylene
• Benzene + Tetrahydropyran + o-Xylene
• Toluene + Tetrahydropyran + o-Xylene
• Decane + o-Xylene
• Propanoic acid, propyl ester + o-Xylene
• Acetic acid, butyl ester + o-Xylene
• Phenol, 2-methyl- + o-Xylene
• o-Xylene + Tetrahydrofuran
• Formamide, N,N-dimethyl- + o-Xylene
• Propane, 2-methoxy-2-methyl- + o-Xylene
• Propane, 2-ethoxy-2-methyl- + o-Xylene
• Toluene + o-Xylene
• o-Xylene + Thiophene, tetrahydro-, 1,1-dioxide
• Thiophene, tetrahydro- + o-Xylene
• Formamide, N-methyl- + o-Xylene
• Thiophene, 3-methyl- + o-Xylene
• 1-Hexanol + o-Xylene
• Octane + o-Xylene

Find more mixtures with o-Xylene.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• 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
• Experimental and theoretical surface tension deviations in the binary systems propyl propanoate + o-, m- and p-xylene at 298.15K
• 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
• 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
• 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
• Phase equilibria on four binary systems containing 3-methylthiophene
• Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
• Vapor liquid equilibria and density measurement for binary mixtures of toluene, benzene, o-xylene, m-xylene, sulfolane and nonane at 333.15K and 353.15K
• Phase equilibria of binary systems of 3-methylthiophene with four different hydrocarbons
• Vapor liquid equilibrium for the binary systems tetrahydrothiophene + toluene and tetrahydrothiophene + o-xylene at 368.15 K and 383.15 K
• 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
• Phase equilibria on five binary systems containing 1-butanethiol and 3-methylthiophene in hydrocarbons
• Application of [EMpy][ESO4] ionic liquid as solvent for the liquid extraction of xylenes from hexane
• Bubble point measurements of binary mixtures formed by 1-hexanol with selected nitro-compounds and substituted benzenes at 95.6 kPa
• 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
• 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
• Isobaric vapor-liquid equilibrium of binary systems of decane with p-, o-, m-xylene at 20 kPa
• Isobaric vapor-liquid equilibrium data of the binary systems of octane with p, o, m-xylene at 20 kPa
• Isobaric vapor-liquid equilibrium for binary systemsof toluene + o-xylene, benzene + o-xylene, nonane + benzene and nonane + heptane at 101.3 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
• Towards automated characterisation of liquid-liquid equilibria
• Prediction and measurement of phase equilibria for the extraction of BTX from naphtha reformate using BMIMPF6 ionic liquid
• 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
• Heat capacities of binary and ternary mixtures containing o-chlorotoluene, cyclic ether and aromatic hydrocarbons
• Extraction of benzene, ethylbenzene, and xylenes from n-heptane using binary mixtures of [4empy][Tf2N] and [emim][DCA] ionic liquids
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• 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
• 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
• 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
• 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
• High-pressure densities of n-decane+o-xylene mixtures: Measurement and modelling
• (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
• 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 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
• 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)
• Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
• Thermochemistry of ionic liquid-catalysed reactions. Isomerisation and transalkylation of tert-alkyl-benzenes. Are these systems ideal?
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate [EMIM][TCB] using gas liquid chromatography
• 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
• Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
• Volumetric properties of binary mixtures of tributylamine with benzene derivatives and comparison with ERAS model results at temperatures from (293.15 to 333.15) K
• 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
• 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
• 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
• 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
• 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
• 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
• 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
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
• Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
• 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
• 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
• 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
• Extension of the DSC method to measuring vapor pressures of narrow boiling range oil cuts
• Liquid-Liquid Equilibrium for Ternary Systems Water + Acetic Acid + m-Xylene and Water + Acetic Acid + o-Xylene at (303.2 to 343.2) K
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Isobaric Vapor Liquid Equilibrium for the Binary Systems of Diethyl Carbonate with Xylene Isomers and Ethylbenzene at 101.33 kPa
• Solubilities of Phthalic Acid and o-Toluic Acid in Binary Acetic Acid + Water and Acetic Acid + o-Xylene Solvent Mixtures
• Mutual solubility of aromatic hydrocarbons in pyrrolidinium and ammonium-based ionic liquids and its modeling using the Cubic-Plus-Association (CPA) Equation of State
• Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
• Isobaric Vapor Liquid Equilibrium Data for the Binary Systems of Dimethyl Carbonate with Xylene Isomers at 93.13 kPa
• Viscometric Studies of Molecular Interactions in Binary Liquid Mixtures of Isomeric Xylenes with Methanol
• Densities and Dynamic Viscosities of Alicyclic Cyclohexane with Toluene, o-Xylene, and Mesitylene at T = (303.15 to 323.15) K and Atmospheric Pressure
• 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
• Volumetric Properties of the D2EHPA-o-Xylene-Neodymium (Samarium, Europium, Gadolinium, Terbium, Dysprosium) Di(2-ethylhexyl)phosphate Systems at 298.15 K
• Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
• Liquid-Liquid Equilibrium for Ternary Systems of Polyoxymethylene Dimethyl Ethers + o-Xylene + Water at 293.15 K
• Measuring Activity Coefficient at Infinite Dilution of Hydrocarbons in Ionic Liquids and Evaluation of Other Thermodynamic Properties using Gas Chromatography
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• Measurement and Correlation of Vapor-Liquid Equilibrium for Binary Systems of Dimethyl Carbonate with Butyl Butyrate, o-Xylene, and Cyclohexanone at 101.3 kPa
• 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
• Viscosities, Densities, and Ultrasonic Velocities of 3-Pentanone + Ethylbenzene and 3-Pentanone + o-Xylene at (293.15, 303.15, and 313.15) K
• Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for CmH2m+1(OCH2CH2)nOH (m ) 1 or 2 or 4 andn ) 1) + Benzene, + Toluene, + (o-, m-, and p-) Xylenes, + Ethylbenzene, and + Cyclohexane
• Analysis and Evaluation of the Liquid-Liquid Equilibrium Data of the Extraction of Aromatics from Hydrocarbons by Tetraethylene Glycol
• 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
• Density, Viscosity, and Excess Properties of Binary Liquid Mixtures of Propylene Carbonate with Polar and Nonpolar Solvents
• 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
• Liquid-Liquid Equilibrium for the System Heptane + o-Xylene + Diethylene Glycol over the Temperature Range of 288.15 K to 318.15 K
• Vapor-Liquid Equilibria Data for Binary Systems of Ethylbenzene + Xylene Isomers at 100.65 kPa
• 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 for the Binary Mixtures of Styrene with Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene
• Vapor-Liquid Equilibrium of Binary Mixtures. 2. Ethanol + 2,2,4-Trimethylpentane, 1-Butanol + 2,2,4-Trimethylpentane, and Ethanol + o-Xylene
• Thermodynamic Properties of Mixtures Containing Ionic Liquids: Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Propyl Boronic Acid-3-Alkylimidazolium Bromide and 1-Propenyl-3-alkylimidazolium Bromide Using Inverse Gas Chromatography
• Solubilities of Benzene, Toluene, and Xylene Isomers in 1-Butyl-3-methylimidazolium Tetrafluoroborate
• Vapor-Liquid Equilibrium for Binary System of 1-Propanethiol, Thiophene, and Diethyl Sulfide with Toluene at 90.03 kPa
• 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
• Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 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
• Vapor-Liquid Equilibrium Data, Excess Enthalpy Data, and Azeotropic Data for the Binary System Dibutyl Ether + o-Xylene
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
• 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, 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
• Vapor-Liquid Equilibrium for Dimethyl Disulfide + Butane, + trans-But-2-ene, + 2-Methylpropane, + 2-Methylpropene, + Ethanol, and 2-Ethoxy-2-methylpropane
• 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
• 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
• Isobaric Vapor Liquid Equilibrium of Binary Systems of Hexane or Octane with 1,2-Dimethylbenzene or 1,3-Dimethylbenzene at 101.3 kPa
• 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
• 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
• Liquid Liquid Equilibria for the Ternary Systems of Perfluamine + Hydrofluoroether + Benzene, Toluene, or Xylene at 298.15 K or 313.15 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
• Thermodynamic Properties of Ternary Liquid Mixtures Containing o-Chlorotoluene: Excess Molar Volumes and Excess Isentropic Compressibilities
• 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
• Solubility of 2,6-Diaminopyridine in Toluene, o-Xylene, Ethylbenzene, Methanol, Ethanol, 2-Propanol, and Sodium Hydroxide Solutions
• 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
• Solubilities of Vitamin K3 in Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene between (299.44 and 344.24) 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
• 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
• 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
• Solubility of Bis(benzoxazolyl-2-methyl) Sulfide in Different Pure Solvents and Ethanol + Water Binary Mixtures between (273.25 and 325.25) K
• Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
• 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
• 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
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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