Chemical Properties of Benzene, 1,3-dimethyl- (CAS 108-38-3)

InChI

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

InChI Key

IVSZLXZYQVIEFR-UHFFFAOYSA-N

Formula

C8H10

SMILES

Cc1cccc(C)c1

Molecular Weight¹

106.17

CAS

108-38-3

Other Names

• 1,3-DIMETHYLBENZENE
• 1,3-Xylene
• 1,3-dimethylbenzene (m-xylene)
• 2,4-Xylene
• M-DIMETHYLBENZENE
• M-XYLOL
• NSC 61769
• m-Methyltoluene
• m-Xylene
• meta-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,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_c,grossH : Heat of Combustion, Gross form (kJ/mol).
• Δ_c,netH : Heat of Combustion, Net Form (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• 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	0.3250		KDB
PAff	[809.10; 816.70]	kJ/mol
PAff	812.10	kJ/mol	NIST
PAff	816.70	kJ/mol	NIST
PAff	809.10 ± 1.20	kJ/mol	NIST
Tig	803.15	K	KDB
BasG	[782.40; 787.80]	kJ/mol
BasG	786.20	kJ/mol	NIST
BasG	787.80	kJ/mol	NIST
BasG	782.40 ± 1.80	kJ/mol	NIST
ΔcH°liquid	[-4581.40; -4549.56]	kJ/mol
ΔcH°liquid	-4549.56 ± 0.54	kJ/mol	NIST
ΔcH°liquid	-4551.86 ± 0.63	kJ/mol	NIST
ΔcH°liquid	-4567.60	kJ/mol	NIST
ΔcH°liquid	-4581.40	kJ/mol	NIST
Cp,liquid	181.38	J/mol×K	Thermod...
μ	0.30	debye	KDB
η	[0.0005870; 0.0005870]	Pa×s
η	0.0005870	Pa×s	Viscosi...
η	0.0005870	Pa×s	Viscosi...
SProt	19.20	J/mol×K	NIST
LFL	1.10	% in Air	KDB
UFL	6.40	% in Air	KDB
Tflash,oc	302.04	K	KDB
ΔfG°	118.90	kJ/mol	KDB
Rg	3.8970		KDB
Δc,grossH	4551.86	kJ/mol	KDB
Δc,netH	4331.779	kJ/mol	KDB
ΔfH°gas	[17.20; 17.25]	kJ/mol
ΔfH°gas	17.25	kJ/mol	KDB
ΔfH°gas	17.20 ± 0.75	kJ/mol	NIST
ΔfH°liquid	-25.40 ± 0.75	kJ/mol	NIST
ΔfusH°	10.13	kJ/mol	Joback Calculated Property
ΔvapH°	[36.40; 43.04]	kJ/mol
ΔvapH°	42.68	kJ/mol	NIST
ΔvapH°	42.70	kJ/mol	NIST
ΔvapH°	43.04	kJ/mol	NIST
ΔvapH°	36.40	kJ/mol	NIST
ΔvapH°	42.70 ± 0.10	kJ/mol	NIST
ΔvapH°	42.65	kJ/mol	NIST
ΔvapH°	42.60	kJ/mol	NIST
ΔvapH°	36.40 ± 0.40	kJ/mol	NIST
IE	[8.50; 8.90]	eV
IE	8.55 ± 0.02	eV	NIST
IE	8.56	eV	NIST
IE	8.57 ± 0.01	eV	NIST
IE	Outlier 8.90 ± 0.05	eV	NIST
IE	8.50 ± 0.02	eV	NIST
IE	8.55 ± 0.05	eV	NIST
IE	8.56	eV	NIST
IE	8.56 ± 0.01	eV	NIST
IE	8.56	eV	NIST
IE	8.82	eV	NIST
IE	8.55	eV	NIST
IE	8.71 ± 0.01	eV	NIST
IE	8.75 ± 0.03	eV	NIST
log10WS	[-2.82; -2.82]
log10WS	-2.82		Aq. Sol...
log10WS	-2.82		Estimat...
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; 3541.20]	kPa
Pc	3541.00	kPa	KDB
Pc	3540.00 ± 40.00	kPa	NIST
Pc	3541.20 ± 5.00	kPa	NIST
Pc	3541.00 ± 6.00	kPa	NIST
Pc	Outlier 3343.73 ± 151.99	kPa	NIST
Pc	3510.00 ± 3.92	kPa	NIST
ρc	[283.46; 284.95]	kg/m3
ρc	283.46 ± 4.25	kg/m3	NIST
ρc	284.95 ± 5.31	kg/m3	NIST
Inp	[130.11; 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	882.70		NIST
Inp	888.10		NIST
Inp	849.80		NIST
Inp	852.30		NIST
Inp	854.80		NIST
Inp	857.40		NIST
Inp	859.60		NIST
Inp	860.90		NIST
Inp	863.50		NIST
Inp	856.77		NIST
Inp	876.00		NIST
Inp	876.00		NIST
Inp	876.00		NIST
Inp	863.30		NIST
Inp	871.20		NIST
Inp	856.10		NIST
Inp	856.40		NIST
Inp	856.40		NIST
Inp	856.60		NIST
Inp	855.90		NIST
Inp	865.00		NIST
Inp	857.00		NIST
Inp	857.00		NIST
Inp	867.00		NIST
Inp	867.00		NIST
Inp	856.00		NIST
Inp	865.20		NIST
Inp	866.00		NIST
Inp	866.00		NIST
Inp	866.00		NIST
Inp	854.00		NIST
Inp	850.10		NIST
Inp	855.30		NIST
Inp	865.00		NIST
Inp	865.00		NIST
Inp	866.00		NIST
Inp	866.00		NIST
Inp	868.00		NIST
Inp	862.00		NIST
Inp	864.00		NIST
Inp	850.20		NIST
Inp	880.00		NIST
Inp	866.00		NIST
Inp	867.00		NIST
Inp	866.00		NIST
Inp	867.00		NIST
Inp	862.00		NIST
Inp	864.00		NIST
Inp	860.00		NIST
Inp	856.10		NIST
Inp	856.60		NIST
Inp	859.60		NIST
Inp	876.00		NIST
Inp	864.00		NIST
Inp	867.00		NIST
Inp	871.00		NIST
Inp	877.00		NIST
Inp	861.00		NIST
Inp	863.20		NIST
Inp	866.60		NIST
Inp	871.10		NIST
Inp	876.60		NIST
Inp	859.00		NIST
Inp	863.00		NIST
Inp	850.50		NIST
Inp	855.70		NIST
Inp	860.60		NIST
Inp	860.80		NIST
Inp	861.00		NIST
Inp	861.70		NIST
Inp	856.40		NIST
Inp	857.40		NIST
Inp	861.00		NIST
Inp	855.30		NIST
Inp	855.60		NIST
Inp	861.00		NIST
Inp	863.20		NIST
Inp	865.00		NIST
Inp	862.00		NIST
Inp	862.00		NIST
Inp	857.76		NIST
Inp	863.00		NIST
Inp	882.00		NIST
Inp	886.00		NIST
Inp	868.00		NIST
Inp	857.80		NIST
Inp	863.20		NIST
Inp	866.00		NIST
Inp	857.00		NIST
Inp	865.00		NIST
Inp	869.00		NIST
Inp	871.00		NIST
Inp	874.00		NIST
Inp	878.00		NIST
Inp	852.30		NIST
Inp	861.10		NIST
Inp	863.00		NIST
Inp	867.10		NIST
Inp	866.30		NIST
Inp	860.30		NIST
Inp	896.00		NIST
Inp	847.00		NIST
Inp	852.00		NIST
Inp	858.00		NIST
Inp	862.00		NIST
Inp	895.00		NIST
Inp	902.00		NIST
Inp	908.00		NIST
Inp	889.00		NIST
Inp	867.00		NIST
Inp	871.00		NIST
Inp	863.00		NIST
Inp	900.00		NIST
Inp	872.50		NIST
Inp	866.00		NIST
Inp	862.00		NIST
Inp	852.00		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	887.00		NIST
Inp	865.05		NIST
Inp	858.00		NIST
Inp	865.00		NIST
Inp	874.00		NIST
Inp	875.00		NIST
Inp	853.20		NIST
Inp	853.20		NIST
Inp	863.00		NIST
Inp	871.00		NIST
Inp	859.40		NIST
Inp	898.00		NIST
Inp	838.00		NIST
Inp	861.70		NIST
Inp	864.40		NIST
Inp	866.50		NIST
Inp	848.20		NIST
Inp	877.80		NIST
Inp	871.00		NIST
Inp	849.00		NIST
Inp	868.00		NIST
Inp	847.00		NIST
Inp	847.00		NIST
Inp	855.50		NIST
Inp	890.21		NIST
Inp	892.69		NIST
Inp	862.00		NIST
Inp	865.00		NIST
Inp	844.60		NIST
Inp	850.20		NIST
Inp	853.80		NIST
Inp	855.40		NIST
Inp	869.30		NIST
Inp	861.70		NIST
Inp	864.40		NIST
Inp	866.50		NIST
Inp	852.91		NIST
Inp	853.44		NIST
Inp	854.00		NIST
Inp	853.38		NIST
Inp	853.85		NIST
Inp	853.00		NIST
Inp	863.00		NIST
Inp	861.00		NIST
Inp	853.96		NIST
Inp	850.24		NIST
Inp	852.98		NIST
Inp	854.72		NIST
Inp	865.16		NIST
Inp	868.16		NIST
Inp	870.12		NIST
Inp	852.00		NIST
Inp	861.50		NIST
Inp	885.00		NIST
Inp	863.00		NIST
Inp	866.00		NIST
Inp	873.00		NIST
Inp	874.00		NIST
Inp	879.49		NIST
Inp	854.00		NIST
Inp	871.00		NIST
Inp	877.00		NIST
Inp	855.00		NIST
Inp	866.00		NIST
Inp	866.00		NIST
Inp	866.00		NIST
Inp	867.00		NIST
Inp	865.00		NIST
Inp	868.00		NIST
Inp	866.00		NIST
Inp	867.00		NIST
Inp	870.00		NIST
Inp	871.00		NIST
Inp	849.00		NIST
Inp	862.00		NIST
Inp	847.00		NIST
Inp	855.00		NIST
Inp	853.00		NIST
Inp	858.00		NIST
Inp	871.00		NIST
Inp	867.00		NIST
Inp	852.00		NIST
Inp	868.00		NIST
Inp	874.00		NIST
Inp	870.00		NIST
Inp	861.00		NIST
Inp	859.00		NIST
Inp	867.00		NIST
Inp	869.00		NIST
Inp	874.00		NIST
Inp	871.00		NIST
Inp	863.00		NIST
Inp	860.00		NIST
Inp	870.00		NIST
Inp	878.00		NIST
Inp	878.00		NIST
Inp	871.20		NIST
Inp	875.00		NIST
Inp	849.00		NIST
Inp	848.00		NIST
Inp	864.00		NIST
Inp	869.00		NIST
Inp	875.00		NIST
Inp	873.00		NIST
Inp	864.00		NIST
Inp	846.40		NIST
Inp	875.00		NIST
Inp	877.00		NIST
Inp	860.00		NIST
Inp	857.00		NIST
Inp	873.00		NIST
Inp	873.00		NIST
Inp	875.30		NIST
Inp	853.00		NIST
Inp	860.00		NIST
Inp	848.00		NIST
Inp	851.00		NIST
Inp	851.00		NIST
Inp	867.00		NIST
Inp	856.00		NIST
Inp	857.00		NIST
Inp	852.00		NIST
Inp	852.00		NIST
Inp	866.00		NIST
Inp	851.20		NIST
Inp	853.20		NIST
Inp	856.10		NIST
Inp	858.20		NIST
Inp	860.00		NIST
Inp	851.00		NIST
Inp	853.00		NIST
Inp	856.00		NIST
Inp	859.00		NIST
Inp	861.00		NIST
Inp	852.00		NIST
Inp	853.00		NIST
Inp	854.00		NIST
Inp	835.00		NIST
Inp	860.00		NIST
Inp	866.00		NIST
Inp	866.00		NIST
Inp	872.00		NIST
Inp	874.00		NIST
Inp	864.00		NIST
Inp	866.00		NIST
Inp	873.00		NIST
Inp	880.00		NIST
Inp	876.00		NIST
Inp	864.00		NIST
Inp	864.00		NIST
Inp	853.00		NIST
Inp	860.00		NIST
Inp	867.00		NIST
Inp	852.00		NIST
Inp	874.00		NIST
Inp	860.00		NIST
Inp	847.12		NIST
Inp	878.00		NIST
Inp	888.00		NIST
Inp	866.00		NIST
Inp	856.00		NIST
Inp	877.00		NIST
Inp	863.00		NIST
Inp	854.00		NIST
Inp	856.00		NIST
Inp	865.00		NIST
Inp	869.00		NIST
Inp	873.00		NIST
Inp	871.00		NIST
Inp	860.00		NIST
Inp	866.00		NIST
Inp	855.00		NIST
Inp	866.00		NIST
Inp	863.00		NIST
Inp	855.00		NIST
Inp	856.00		NIST
Inp	869.00		NIST
Inp	871.00		NIST
Inp	864.40		NIST
Inp	868.00		NIST
Inp	852.00		NIST
Inp	845.00		NIST
Inp	852.00		NIST
Inp	863.00		NIST
Inp	876.00		NIST
Inp	849.00		NIST
Inp	852.00		NIST
Inp	854.00		NIST
Inp	858.00		NIST
Inp	864.00		NIST
Inp	863.00		NIST
Inp	874.00		NIST
Inp	858.00		NIST
Inp	874.00		NIST
Inp	Outlier 130.11		NIST
Inp	874.00		NIST
Inp	871.00		NIST
Inp	864.40		NIST
Inp	849.00		NIST
Inp	890.21		NIST
Inp	850.20		NIST
Inp	853.38		NIST
Inp	853.96		NIST
Inp	868.16		NIST
I	[1099.00; 1195.00]
I	1176.50		NIST
I	Outlier 1188.10		NIST
I	1123.00		NIST
I	1123.00		NIST
I	1134.60		NIST
I	1147.30		NIST
I	1149.90		NIST
I	1151.00		NIST
I	1157.00		NIST
I	1145.00		NIST
I	1166.41		NIST
I	1171.52		NIST
I	1176.29		NIST
I	1151.54		NIST
I	1156.28		NIST
I	1161.65		NIST
I	1145.30		NIST
I	1149.00		NIST
I	1175.80		NIST
I	1175.80		NIST
I	1140.70		NIST
I	1124.30		NIST
I	Outlier 1192.00		NIST
I	Outlier 1185.00		NIST
I	Outlier 1195.00		NIST
I	Outlier 1194.00		NIST
I	1168.00		NIST
I	1176.00		NIST
I	1182.00		NIST
I	1161.00		NIST
I	1143.00		NIST
I	1142.00		NIST
I	1141.00		NIST
I	1143.00		NIST
I	1142.00		NIST
I	1143.00		NIST
I	1149.00		NIST
I	1123.00		NIST
I	1140.00		NIST
I	1149.00		NIST
I	1161.00		NIST
I	1129.00		NIST
I	1143.00		NIST
I	1132.00		NIST
I	1143.00		NIST
I	1150.00		NIST
I	1131.00		NIST
I	1132.00		NIST
I	1148.00		NIST
I	1146.00		NIST
I	1150.00		NIST
I	1129.00		NIST
I	1129.00		NIST
I	1144.00		NIST
I	1136.00		NIST
I	1142.00		NIST
I	1149.00		NIST
I	1142.00		NIST
I	1134.00		NIST
I	1134.00		NIST
I	1158.00		NIST
I	1141.00		NIST
I	1141.00		NIST
I	1138.00		NIST
I	Outlier 1099.00		NIST
I	1123.00		NIST
I	1143.00		NIST
I	1116.00		NIST
I	1118.00		NIST
I	1144.00		NIST
I	1147.00		NIST
I	1162.00		NIST
I	1142.00		NIST
I	1143.00		NIST
I	1132.00		NIST
I	1136.00		NIST
I	1138.00		NIST
I	1160.00		NIST
I	Outlier 1190.00		NIST
I	1172.00		NIST
I	1183.00		NIST
I	Outlier 1193.00		NIST
I	1148.00		NIST
I	1160.00		NIST
I	1161.00		NIST
I	1156.00		NIST
I	1159.00		NIST
I	1170.00		NIST
I	1180.00		NIST
I	Outlier 1195.00		NIST
I	1138.00		NIST
I	1148.00		NIST
I	1124.00		NIST
I	1160.00		NIST
I	1120.00		NIST
I	1136.00		NIST
I	1146.00		NIST
I	1156.00		NIST
I	1121.00		NIST
I	1134.00		NIST
I	1135.00		NIST
I	1133.00		NIST
I	1126.00		NIST
I	1149.00		NIST
I	1132.00		NIST
I	1148.00		NIST
I	1137.00		NIST
I	1124.00		NIST
I	1138.00		NIST
I	1121.00		NIST
I	1138.00		NIST
I	1138.00		NIST
I	1147.00		NIST
I	1144.00		NIST
I	1132.00		NIST
I	1135.00		NIST
I	1131.00		NIST
I	1133.00		NIST
I	1135.00		NIST
I	1132.00		NIST
I	1146.00		NIST
I	1132.00		NIST
I	1136.00		NIST
I	1121.00		NIST
I	1158.00		NIST
I	1161.00		NIST
I	1135.00		NIST
I	1118.00		NIST
I	1147.00		NIST
I	1145.00		NIST
I	1137.00		NIST
I	1124.00		NIST
I	1164.00		NIST
I	1145.00		NIST
I	1138.00		NIST
I	1164.00		NIST
I	1130.00		NIST
I	1147.00		NIST
I	1131.00		NIST
I	1147.00		NIST
I	1150.00		NIST
I	1132.00		NIST
I	1172.00		NIST
I	1161.00		NIST
I	Outlier 1195.00		NIST
I	1160.00		NIST
I	1121.00		NIST
I	1149.00		NIST
I	1138.00		NIST
I	1143.00		NIST
S°gas	358.20 ± 1.30	J/mol×K	NIST
S°liquid	[252.30; 253.80]	J/mol×K
S°liquid	253.80	J/mol×K	NIST
S°liquid	252.30	J/mol×K	NIST
Tboil	[409.00; 413.35]	K
Tboil	412.27	K	KDB
Tboil	412.00	K	Isobari...
Tboil	412.21	K	Isobari...
Tboil	412.15 ± 0.20	K	NIST
Tboil	412.29 ± 0.15	K	NIST
Tboil	412.30	K	NIST
Tboil	412.30	K	NIST
Tboil	412.20 ± 0.20	K	NIST
Tboil	412.40 ± 0.20	K	NIST
Tboil	412.25 ± 1.00	K	NIST
Tboil	Outlier 409.00 ± 8.00	K	NIST
Tboil	412.23 ± 0.20	K	NIST
Tboil	412.30 ± 0.50	K	NIST
Tboil	412.10 ± 0.40	K	NIST
Tboil	412.00 ± 1.50	K	NIST
Tboil	412.40 ± 0.50	K	NIST
Tboil	412.25 ± 0.02	K	NIST
Tboil	412.40 ± 0.60	K	NIST
Tboil	412.30 ± 0.15	K	NIST
Tboil	412.40 ± 0.50	K	NIST
Tboil	412.35 ± 0.50	K	NIST
Tboil	412.25 ± 0.01	K	NIST
Tboil	412.15 ± 1.00	K	NIST
Tboil	412.26 ± 0.06	K	NIST
Tboil	412.35 ± 0.30	K	NIST
Tboil	412.38 ± 0.10	K	NIST
Tboil	412.22 ± 0.20	K	NIST
Tboil	412.35 ± 0.50	K	NIST
Tboil	412.45 ± 0.20	K	NIST
Tboil	412.65 ± 1.20	K	NIST
Tboil	412.20 ± 0.50	K	NIST
Tboil	412.20 ± 0.50	K	NIST
Tboil	412.20 ± 0.50	K	NIST
Tboil	412.50 ± 0.20	K	NIST
Tboil	412.50 ± 0.30	K	NIST
Tboil	412.45 ± 0.40	K	NIST
Tboil	Outlier 409.00 ± 3.00	K	NIST
Tboil	412.15 ± 0.10	K	NIST
Tboil	412.00 ± 2.00	K	NIST
Tboil	412.15 ± 0.30	K	NIST
Tboil	412.00 ± 2.00	K	NIST
Tboil	412.45 ± 0.50	K	NIST
Tboil	412.45 ± 0.50	K	NIST
Tboil	411.90 ± 0.70	K	NIST
Tboil	413.35 ± 1.50	K	NIST
Tboil	412.40 ± 1.50	K	NIST
Tc	617.00	K	KDB
Tfus	[219.55; 226.65]	K
Tfus	225.30	K	KDB
Tfus	225.55	K	Aq. Sol...
Tfus	225.20 ± 0.15	K	NIST
Tfus	225.80 ± 0.30	K	NIST
Tfus	225.22 ± 0.15	K	NIST
Tfus	225.17 ± 0.01	K	NIST
Tfus	225.25 ± 0.10	K	NIST
Tfus	226.65 ± 0.20	K	NIST
Tfus	225.80 ± 0.50	K	NIST
Tfus	223.85 ± 0.30	K	NIST
Tfus	Outlier 219.55 ± 0.40	K	NIST
Ttriple	219.60 ± 0.30	K	NIST
Vc	[0.375; 0.375]	m3/kmol
Vc	0.375	m3/kmol	KDB
Vc	0.375	m3/kmol	NIST
Zc	0.2588420		KDB
Zra	0.26		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[163.60; 190.00]	J/mol×K	[393.00; 463.00]
Cp,gas	163.60 ± 1.70	J/mol×K	393.00	NIST
Cp,gas	177.40 ± 1.70	J/mol×K	428.00	NIST
Cp,gas	190.00 ± 1.70	J/mol×K	463.00	NIST
Cp,liquid	[175.30; 199.20]	J/mol×K	[275.30; 336.00]
Cp,liquid	175.30	J/mol×K	275.30	NIST
Cp,liquid	184.50	J/mol×K	298.00	NIST
Cp,liquid	181.55	J/mol×K	298.15	NIST
Cp,liquid	181.48	J/mol×K	298.15	NIST
Cp,liquid	183.18	J/mol×K	298.15	NIST
Cp,liquid	184.63	J/mol×K	298.15	NIST
Cp,liquid	178.20	J/mol×K	303.00	NIST
Cp,liquid	199.20	J/mol×K	336.00	NIST
η	[0.0003440; 0.0006660]	Pa×s	[288.15; 353.15]
η	0.0006660	Pa×s	288.15	Viscosi...
η	0.0006190	Pa×s	293.15	Viscosi...
η	0.0005870	Pa×s	298.15	Densiti...
η	0.0005848	Pa×s	298.15	Densiti...
η	0.0005810	Pa×s	298.15	Viscosi...
η	0.0005880	Pa×s	298.15	Ultraso...
η	0.0005820	Pa×s	298.15	Densiti...
η	0.0005892	Pa×s	298.15	Excess ...
η	0.0005540	Pa×s	303.15	Viscome...
η	0.0005490	Pa×s	303.15	Densiti...
η	0.0005501	Pa×s	303.15	Thermod...
η	0.0005471	Pa×s	303.15	Excess ...
η	0.0005531	Pa×s	303.15	Densiti...
η	0.0005570	Pa×s	303.15	Viscosi...
η	0.0005520	Pa×s	303.15	Viscosi...
η	0.0005570	Pa×s	303.15	Thermop...
η	0.0005240	Pa×s	308.15	Viscome...
η	0.0005240	Pa×s	308.15	Densiti...
η	0.0005210	Pa×s	308.15	Density...
η	0.0005201	Pa×s	308.15	Densiti...
η	0.0004990	Pa×s	308.15	Densiti...
η	0.0005229	Pa×s	308.15	Ultraso...
η	0.0005080	Pa×s	313.15	Viscosi...
η	0.0004967	Pa×s	313.15	Densiti...
η	0.0004970	Pa×s	313.15	Densiti...
η	0.0004980	Pa×s	313.15	Viscome...
η	0.0004944	Pa×s	313.15	Thermod...
η	0.0005080	Pa×s	313.15	Thermop...
η	0.0004710	Pa×s	318.15	Densiti...
η	0.0004720	Pa×s	318.15	Viscome...
η	0.0004700	Pa×s	318.15	Density...
η	0.0004817	Pa×s	318.15	Densiti...
η	0.0004684	Pa×s	318.15	Ultraso...
η	0.0004440	Pa×s	323.15	Densiti...
η	0.0004488	Pa×s	323.15	Densiti...
η	0.0004428	Pa×s	323.15	Excess ...
η	0.0004472	Pa×s	323.15	Thermod...
η	0.0004520	Pa×s	323.15	Viscome...
η	0.0004350	Pa×s	328.15	Densiti...
η	0.0004130	Pa×s	333.15	Densiti...
η	0.0004101	Pa×s	333.15	Densiti...
η	0.0003748	Pa×s	343.15	Densiti...
η	0.0003440	Pa×s	353.15	Densiti...
ΔfusH	[11.57; 11.59]	kJ/mol	[225.27; 225.30]
ΔfusH	11.57	kJ/mol	225.27	NIST
ΔfusH	11.59	kJ/mol	225.30	NIST
ΔfusH	11.57	kJ/mol	225.30	NIST
ΔvapH	[35.66; 44.70]	kJ/mol	[284.00; 583.50]
ΔvapH	44.70	kJ/mol	284.00	NIST
ΔvapH	43.20	kJ/mol	303.00	NIST
ΔvapH	40.70	kJ/mol	369.50	NIST
ΔvapH	40.40	kJ/mol	373.00	NIST
ΔvapH	39.20	kJ/mol	385.00	NIST
ΔvapH	38.70	kJ/mol	395.50	NIST
ΔvapH	36.36	kJ/mol	412.20	KDB
ΔvapH	35.66	kJ/mol	412.30	NIST
ΔvapH	37.50	kJ/mol	437.00	NIST
ΔvapH	36.40	kJ/mol	507.50	NIST
ΔvapH	36.20	kJ/mol	583.50	NIST
Pvap	[0.10; 250.00]	kPa	[263.75; 450.10]
Pvap	0.10	kPa	263.75	Vapour ...
Pvap	0.21	kPa	273.47	Vapour ...
Pvap	0.43	kPa	283.35	Vapour ...
Pvap	0.86	kPa	293.29	Vapour ...
Pvap	1.10	kPa	298.15	(Vapour...
Pvap	1.59	kPa	303.28	Vapour ...
Pvap	2.63	kPa	308.15	Vapor-l...
Pvap	3.52	kPa	313.15	Vapor-l...
Pvap	2.77	kPa	313.27	Vapour ...
Pvap	4.37	kPa	318.15	Vapor-l...
Pvap	5.37	kPa	323.15	Vapor-l...
Pvap	4.41	kPa	323.25	Vapour ...
Pvap	6.50	kPa	328.15	Vapor-l...
Pvap	6.58	kPa	333.15	Vapor l...
Pvap	6.59	kPa	333.15	Vapor l...
Pvap	7.75	kPa	333.15	Vapor-l...
Pvap	6.85	kPa	333.22	Vapour ...
Pvap	9.30	kPa	338.15	Vapor-l...
Pvap	10.17	kPa	343.15	Vapor l...
Pvap	11.12	kPa	343.15	Vapor-l...
Pvap	10.48	kPa	343.18	Vapour ...
Pvap	11.00	kPa	345.15	Vapour-...
Pvap	13.44	kPa	350.15	Vapour-...
Pvap	15.09	kPa	353.15	Vapor l...
Pvap	15.12	kPa	353.15	Vapor l...
Pvap	15.97	kPa	353.15	Vapor-l...
Pvap	16.32	kPa	355.15	Vapour-...
Pvap	19.68	kPa	360.15	Vapour-...
Pvap	22.76	kPa	363.15	Vapor-l...
Pvap	23.59	kPa	365.15	Vapour-...
Pvap	32.06	kPa	373.15	Vapor-l...
Pvap	40.00	kPa	380.51	Determi...
Pvap	44.23	kPa	383.15	Vapor-l...
Pvap	53.33	kPa	389.66	Determi...
Pvap	66.66	kPa	397.13	Determi...
Pvap	80.20	kPa	403.15	Vapor-l...
Pvap	79.99	kPa	403.51	Determi...
Pvap	93.32	kPa	409.09	Determi...
Pvap	93.13	kPa	409.13	Refract...
Pvap	101.30	kPa	412.00	Isobari...
Pvap	250.00	kPa	450.10	Isobari...
n0	[1.48440; 1.49990]		[288.15; 318.15]
n0	1.49990		288.15	Refract...
n0	1.49990		288.15	Densiti...
n0	1.49970		288.15	Excess ...
n0	1.49730		293.10	Volumet...
n0	1.49430		293.10	(Liquid...
n0	1.49430		293.10	(Liquid...
n0	1.49730		293.15	Densiti...
n0	1.49720		293.15	Bubble ...
n0	1.49735		293.15	A study...
n0	1.49740		293.15	Refract...
n0	1.49740		293.15	Densiti...
n0	1.49730		293.15	Excess ...
n0	1.49360		293.15	Volumet...
n0	1.49720		293.15	Solubil...
n0	1.49720		293.15	Activit...
n0	1.49720		293.15	Excess ...
n0	1.49480		298.15	Densiti...
n0	1.49730		298.15	Densiti...
n0	1.49460		298.15	Bubble ...
n0	1.49450		298.15	Excess ...
n0	1.49440		298.15	Excess ...
n0	1.49464		298.15	KDB
n0	1.49470		298.15	Solubil...
n0	1.49450		298.15	Densiti...
n0	1.49440		298.15	Isobari...
n0	1.49440		298.15	Densiti...
n0	1.49430		298.15	Liquid-...
n0	1.49460		298.15	(Vapor ...
n0	1.49480		298.15	Refract...
n0	1.49730		298.15	A study...
n0	1.49466		298.15	Density...
n0	1.49468		298.15	Separat...
n0	1.49250		303.15	Excess ...
n0	1.49220		303.15	Densiti...
n0	1.49220		303.15	Refract...
n0	1.49460		308.15	Topolog...
n0	1.48960		308.15	Densiti...
n0	1.48960		308.15	Refract...
n0	1.48653		313.15	Density...
n0	1.48700		313.15	Densiti...
n0	1.48700		313.15	Refract...
n0	1.48440		318.15	Densiti...
n0	1.48440		318.15	Refract...
ρl	[810.51; 868.59]	kg/m3	[288.15; 353.15]
ρl	868.59	kg/m3	288.15	Densiti...
ρl	868.56	kg/m3	288.15	Thermod...
ρl	868.39	kg/m3	288.15	Effect ...
ρl	864.00	kg/m3	293.00	KDB
ρl	864.20	kg/m3	293.10	Vapor-L...
ρl	864.16	kg/m3	293.15	Surface...
ρl	864.31	kg/m3	293.15	Densiti...
ρl	864.11	kg/m3	293.15	Isobari...
ρl	864.20	kg/m3	293.15	Excess ...
ρl	864.27	kg/m3	293.15	Thermod...
ρl	868.12	kg/m3	293.15	Liquid ...
ρl	859.95	kg/m3	298.15	Isobari...
ρl	859.78	kg/m3	298.15	Excess ...
ρl	859.95	kg/m3	298.15	Isobari...
ρl	859.78	kg/m3	298.15	Excess ...
ρl	860.00	kg/m3	298.15	Excess ...
ρl	860.00	kg/m3	298.15	Excess ...
ρl	859.10	kg/m3	298.15	Thermop...
ρl	860.06	kg/m3	298.15	Isobari...
ρl	859.98	kg/m3	298.15	Thermod...
ρl	859.95	kg/m3	298.15	Isobari...
ρl	859.86	kg/m3	298.15	Excess ...
ρl	860.02	kg/m3	298.15	Densiti...
ρl	859.78	kg/m3	298.15	Experim...
ρl	859.83	kg/m3	298.15	Effect ...
ρl	859.87	kg/m3	298.15	Acousti...
ρl	860.06	kg/m3	298.15	Vapor L...
ρl	860.07	kg/m3	298.20	Isobari...
ρl	855.74	kg/m3	303.15	Densiti...
ρl	855.68	kg/m3	303.15	Thermod...
ρl	855.76	kg/m3	303.15	Excess ...
ρl	849.20	kg/m3	308.15	Thermop...
ρl	851.25	kg/m3	308.15	Effect ...
ρl	851.36	kg/m3	308.15	Thermod...
ρl	851.45	kg/m3	308.15	Densiti...
ρl	851.24	kg/m3	308.15	Acousti...
ρl	847.03	kg/m3	313.15	Thermod...
ρl	847.17	kg/m3	313.15	Densiti...
ρl	847.11	kg/m3	313.15	Excess ...
ρl	842.58	kg/m3	318.15	Effect ...
ρl	842.69	kg/m3	318.15	Thermod...
ρl	840.40	kg/m3	318.15	Thermop...
ρl	842.88	kg/m3	318.15	Densiti...
ρl	835.80	kg/m3	323.15	Thermop...
ρl	838.27	kg/m3	323.15	Excess ...
ρl	838.33	kg/m3	323.15	Thermod...
ρl	831.60	kg/m3	328.15	Thermop...
ρl	833.95	kg/m3	328.15	Thermod...
ρl	833.85	kg/m3	328.15	Effect ...
ρl	829.22	kg/m3	333.15	Excess ...
ρl	829.56	kg/m3	333.15	Thermod...
ρl	819.97	kg/m3	343.15	Excess ...
ρl	810.51	kg/m3	353.15	Excess ...
ΔfusS	51.36	J/mol×K	225.27	NIST
csound,fluid	[1219.51; 1362.66]	m/s	[288.15; 323.15]
csound,fluid	1362.66	m/s	288.15	Influen...
csound,fluid	1352.14	m/s	290.65	Influen...
csound,fluid	1341.00	m/s	293.15	Densiti...
csound,fluid	1341.72	m/s	293.15	Influen...
csound,fluid	1346.70	m/s	293.15	Physico...
csound,fluid	1340.00	m/s	293.15	Densiti...
csound,fluid	1331.31	m/s	295.65	Influen...
csound,fluid	1320.92	m/s	298.15	Influen...
csound,fluid	1323.60	m/s	298.15	Physico...
csound,fluid	1310.57	m/s	300.65	Influen...
csound,fluid	1302.40	m/s	303.15	Physico...
csound,fluid	1300.00	m/s	303.15	Densiti...
csound,fluid	1300.27	m/s	303.15	Influen...
csound,fluid	1290.00	m/s	305.65	Influen...
csound,fluid	1282.30	m/s	308.15	Physico...
csound,fluid	1279.79	m/s	308.15	Influen...
csound,fluid	1269.59	m/s	310.65	Influen...
csound,fluid	1259.46	m/s	313.15	Influen...
csound,fluid	1259.00	m/s	313.15	Densiti...
csound,fluid	1262.30	m/s	313.15	Physico...
csound,fluid	1249.33	m/s	315.65	Influen...
csound,fluid	1243.00	m/s	318.15	Physico...
csound,fluid	1239.28	m/s	318.15	Influen...
csound,fluid	1229.26	m/s	320.65	Influen...
csound,fluid	1219.51	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	Experim...
γ	0.03	N/m	298.15	Densiti...
γ	0.03	N/m	303.15	Surface...
γ	0.03	N/m	303.15	Densiti...
γ	0.03	N/m	308.15	Densiti...
γ	0.03	N/m	308.15	Surface...
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	0.02	N/m	333.15	Surface...
γ	0.02	N/m	343.15	Surface...
λ	[0.12; 0.14]	W/m×K	[258.17; 329.22]
λ	0.14	W/m×K	258.17	Thermal...
λ	0.14	W/m×K	258.42	Thermal...
λ	0.14	W/m×K	258.58	Thermal...
λ	0.14	W/m×K	275.04	Thermal...
λ	0.14	W/m×K	275.28	Thermal...
λ	0.14	W/m×K	275.44	Thermal...
λ	0.13	W/m×K	287.36	Thermal...
λ	0.13	W/m×K	287.60	Thermal...
λ	0.13	W/m×K	287.77	Thermal...
λ	0.13	W/m×K	294.07	Thermal...
λ	0.13	W/m×K	294.32	Thermal...
λ	0.13	W/m×K	294.49	Thermal...
λ	0.13	W/m×K	311.74	Thermal...
λ	0.13	W/m×K	312.00	Thermal...
λ	0.13	W/m×K	312.18	Thermal...
λ	0.12	W/m×K	328.79	Thermal...
λ	0.12	W/m×K	329.04	Thermal...
λ	0.12	W/m×K	329.22	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
273.56	100.00	0.0008
273.55	1000.00	0.0008
273.55	5000.00	0.0008
273.54	10000.00	0.0009
273.55	15000.00	0.0009
273.55	20000.00	0.0009
273.54	25000.00	0.0010
273.54	30000.00	0.0010
283.24	100.00	0.0007
283.25	1000.00	0.0007
283.25	5000.00	0.0007
283.24	10000.00	0.0008
283.25	15000.00	0.0008
283.25	20000.00	0.0008
283.25	25000.00	0.0009
283.25	30000.00	0.0009
293.07	100.00	0.0006
293.06	1000.00	0.0006
293.07	5000.00	0.0006
293.07	10000.00	0.0007
293.07	15000.00	0.0007
293.06	20000.00	0.0007
293.06	25000.00	0.0007
293.07	30000.00	0.0008
302.90	100.00	0.0006
302.90	1000.00	0.0006
302.88	5000.00	0.0006
302.90	10000.00	0.0006
302.89	15000.00	0.0006
302.90	20000.00	0.0006
302.88	25000.00	0.0007
302.87	30000.00	0.0007
313.30	100.00	0.0005
313.29	1000.00	0.0005
313.30	5000.00	0.0005
313.30	10000.00	0.0005
313.31	15000.00	0.0006
313.31	20000.00	0.0006
313.31	25000.00	0.0006
313.31	30000.00	0.0006
323.01	100.00	0.0004
323.01	1000.00	0.0005
323.01	5000.00	0.0005
323.00	10000.00	0.0005
323.02	15000.00	0.0005
323.02	20000.00	0.0005
323.02	25000.00	0.0005
323.02	30000.00	0.0006
333.10	100.00	0.0004
333.11	1000.00	0.0004
333.11	5000.00	0.0004
333.11	10000.00	0.0004
333.11	15000.00	0.0005
333.11	20000.00	0.0005
333.12	25000.00	0.0005
333.12	30000.00	0.0005
342.98	100.00	0.0004
342.98	1000.00	0.0004
342.98	5000.00	0.0004
342.98	10000.00	0.0004
342.98	15000.00	0.0004
342.97	20000.00	0.0004
342.97	25000.00	0.0005
342.97	30000.00	0.0005
352.89	100.00	0.0003
352.89	1000.00	0.0003
352.89	5000.00	0.0004
352.89	10000.00	0.0004
352.89	15000.00	0.0004
352.88	20000.00	0.0004
352.88	25000.00	0.0004
352.88	30000.00	0.0004
362.69	100.00	0.0003
362.70	1000.00	0.0003
362.70	5000.00	0.0003
362.70	10000.00	0.0003
362.71	15000.00	0.0004
362.71	20000.00	0.0004
362.71	25000.00	0.0004
362.71	30000.00	0.0004
372.50	100.00	0.0003
372.50	1000.00	0.0003
372.51	5000.00	0.0003
372.51	10000.00	0.0003
372.51	15000.00	0.0003
372.51	20000.00	0.0003
372.51	25000.00	0.0004
372.51	30000.00	0.0004
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.15	100.00	0.0006
298.15	40100.00	0.0008
298.15	41000.00	0.0008
298.15	79700.00	0.0010
298.15	80300.00	0.0010
298.15	80400.00	0.0010
298.15	80800.00	0.0010
298.15	120200.00	0.0013
298.15	120400.00	0.0013
298.15	159100.00	0.0016
298.15	159400.00	0.0016
298.15	160000.00	0.0016
298.15	161300.00	0.0016
298.15	191300.00	0.0019
298.15	198500.00	0.0020
298.15	100.00	0.0006
298.15	100.00	0.0006
298.15	100.00	0.0006
323.15	100.00	0.0004
323.15	41700.00	0.0006
323.15	80500.00	0.0008
323.15	81400.00	0.0008
323.15	121700.00	0.0010
323.15	159200.00	0.0012
323.15	160000.00	0.0012
323.15	189600.00	0.0013
323.15	100.00	0.0004
348.15	100.00	0.0004
348.15	41400.00	0.0005
348.15	80900.00	0.0006
348.15	121200.00	0.0007
348.15	158900.00	0.0009
348.15	160800.00	0.0009
348.15	192300.00	0.0010
348.15	100.00	0.0004
348.15	80900.00	0.0006
373.15	100.00	0.0003
373.15	41800.00	0.0004
373.15	80800.00	0.0005
373.15	81400.00	0.0005
373.15	121100.00	0.0006
373.15	158600.00	0.0007
373.15	160800.00	0.0007
373.15	191300.00	0.0008
373.15	100.00	0.0003
398.15	100.00	0.0002
398.15	39700.00	0.0003
398.15	79700.00	0.0004
398.15	80300.00	0.0004
398.15	119900.00	0.0005
398.15	159700.00	0.0006
398.15	160700.00	0.0006
398.15	197100.00	0.0007
398.15	100.00	0.0002
423.15	21300.00	0.0002
423.15	21800.00	0.0003
423.15	40500.00	0.0003
423.15	80400.00	0.0004
423.15	80600.00	0.0004
423.15	122200.00	0.0004
423.15	160300.00	0.0005
423.15	161600.00	0.0005
423.15	195700.00	0.0006
448.15	19900.00	0.0002
448.15	20900.00	0.0002
448.15	40500.00	0.0003
448.15	79600.00	0.0003
448.15	81000.00	0.0003
448.15	120500.00	0.0004
448.15	161000.00	0.0005
448.15	162300.00	0.0005
448.15	190700.00	0.0005
473.15	19900.00	0.0002
473.15	20100.00	0.0002
473.15	40000.00	0.0002
473.15	79900.00	0.0003
473.15	80200.00	0.0003
473.15	120800.00	0.0004
473.15	163000.00	0.0004
473.15	163800.00	0.0004
473.15	196400.00	0.0005
Reference

Refractive index (Na D-line)

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Refractive index (Na D-line) - Liquid
93.00	298.15	1.4943
Reference

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	293.15	864.2
1000.00	293.15	864.4
3000.00	293.15	865.8
5000.00	293.15	866.9
10000.00	293.15	870.5
15000.00	293.15	873.8
20000.00	293.15	877.0
25000.00	293.15	880.2
30000.00	293.15	883.2
35000.00	293.15	886.0
40000.00	293.15	888.7
50000.00	293.15	894.4
60000.00	293.15	899.1
100.00	303.15	855.0
1000.00	303.15	855.4
3000.00	303.15	857.5
5000.00	303.15	858.8
10000.00	303.15	862.3
15000.00	303.15	865.8
20000.00	303.15	869.0
25000.00	303.15	872.2
30000.00	303.15	875.3
35000.00	303.15	878.2
40000.00	303.15	881.0
50000.00	303.15	886.7
60000.00	303.15	892.0
100.00	313.15	846.7
1000.00	313.15	846.9
3000.00	313.15	848.6
5000.00	313.15	850.1
10000.00	313.15	854.0
15000.00	313.15	857.6
20000.00	313.15	861.1
25000.00	313.15	864.5
30000.00	313.15	867.7
35000.00	313.15	870.9
40000.00	313.15	873.8
50000.00	313.15	879.8
60000.00	313.15	885.1
100.00	323.15	837.7
1000.00	323.15	838.6
3000.00	323.15	840.2
5000.00	323.15	841.9
10000.00	323.15	845.9
15000.00	323.15	849.8
20000.00	323.15	853.6
25000.00	323.15	857.0
30000.00	323.15	860.4
35000.00	323.15	863.7
40000.00	323.15	866.9
50000.00	323.15	873.0
60000.00	323.15	878.8
100.00	333.15	829.0
1000.00	333.15	829.8
3000.00	333.15	831.7
5000.00	333.15	833.4
10000.00	333.15	837.6
15000.00	333.15	841.6
20000.00	333.15	845.6
25000.00	333.15	849.3
30000.00	333.15	852.8
35000.00	333.15	856.2
40000.00	333.15	859.7
50000.00	333.15	866.0
60000.00	333.15	871.9
100.00	343.15	820.0
1000.00	343.15	821.1
3000.00	343.15	823.0
5000.00	343.15	825.0
10000.00	343.15	829.4
15000.00	343.15	833.6
20000.00	343.15	837.9
25000.00	343.15	841.7
30000.00	343.15	845.5
35000.00	343.15	849.2
40000.00	343.15	852.5
50000.00	343.15	859.1
60000.00	343.15	865.0
100.00	353.15	811.3
1000.00	353.15	812.2
3000.00	353.15	814.3
5000.00	353.15	816.2
10000.00	353.15	821.0
15000.00	353.15	825.7
20000.00	353.15	829.8
25000.00	353.15	834.0
30000.00	353.15	838.0
35000.00	353.15	841.7
40000.00	353.15	845.3
50000.00	353.15	852.1
60000.00	353.15	858.5
100.00	363.15	802.2
1000.00	363.15	803.3
3000.00	363.15	805.5
5000.00	363.15	807.6
10000.00	363.15	812.4
15000.00	363.15	817.6
20000.00	363.15	821.8
25000.00	363.15	826.0
30000.00	363.15	830.2
35000.00	363.15	834.2
40000.00	363.15	838.1
50000.00	363.15	845.2
60000.00	363.15	852.0
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[300.97; 439.80]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.45202e+01
Coefficient B			-3.62202e+03
Coefficient C			-4.64790e+01
Temperature range, min.			300.97
Temperature range, max.			439.80
Pvap	1.33	kPa	300.97	Calculated Property
Pvap	3.01	kPa	316.40	Calculated Property
Pvap	6.21	kPa	331.82	Calculated Property
Pvap	11.91	kPa	347.25	Calculated Property
Pvap	21.44	kPa	362.67	Calculated Property
Pvap	36.52	kPa	378.10	Calculated Property
Pvap	59.35	kPa	393.52	Calculated Property
Pvap	92.54	kPa	408.95	Calculated Property
Pvap	139.14	kPa	424.37	Calculated Property
Pvap	202.63	kPa	439.80	Calculated Property
Pvap	[3.23e-03; 3526.67]	kPa	[225.30; 617.05]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			7.68670e+01
Coefficient B			-7.55661e+03
Coefficient C			-9.10668e+00
Coefficient D			5.40363e-06
Temperature range, min.			225.30
Temperature range, max.			617.05
Pvap	3.23e-03	kPa	225.30	Calculated Property
Pvap	0.17	kPa	268.83	Calculated Property
Pvap	2.44	kPa	312.36	Calculated Property
Pvap	16.77	kPa	355.88	Calculated Property
Pvap	70.86	kPa	399.41	Calculated Property
Pvap	216.17	kPa	442.94	Calculated Property
Pvap	527.17	kPa	486.47	Calculated Property
Pvap	1098.76	kPa	529.99	Calculated Property
Pvap	2048.41	kPa	573.52	Calculated Property
Pvap	3526.67	kPa	617.05	Calculated Property

Similar Compounds

Find more compounds similar to Benzene, 1,3-dimethyl-.

Mixtures

• n-Hexane + Benzene, 1,3-dimethyl-
• Benzene, 1,3-dimethyl- + 2-Propenoic acid, butyl ester
• Benzene, 1,3-dimethyl- + Decane
• Propanoic acid, propyl ester + Benzene, 1,3-dimethyl-
• Benzene, 1,3-dimethyl- + Acetic acid, butyl ester
• Phenol, 2-methyl- + Benzene, 1,3-dimethyl-
• Benzene, 1,3-dimethyl- + Ethylbenzene
• Diisopropyl ether + Benzene, 1,3-dimethyl-
• Benzene, 1,3-dimethyl- + Tetrahydrofuran
• Formamide, N,N-dimethyl- + Benzene, 1,3-dimethyl-
• Benzene, 1,3-dimethyl- + Propane, 2-methoxy-2-methyl-
• Benzene, 1,3-dimethyl- + Propane, 2-ethoxy-2-methyl-
• Benzene, 1,3-dimethyl- + Thiophene, tetrahydro-, 1,1-dioxide
• Benzene, 1,3-dimethyl- + Formamide, N-methyl-
• Benzene, 1,3-dimethyl- + Nonane
• Benzene, 1,3-dimethyl- + Octane
• Undecane + Benzene, 1,3-dimethyl-
• Benzene, 1,3-dimethyl- + 2-Propanol, 1,1'-[(1-methyl-1,2-ethanediyl)bis(oxy)]bis-
• Benzene, 1,3-dimethyl- + 1-Butanol
• Benzene, 1,3-dimethyl- + Cyclohexanone

Find more mixtures with Benzene, 1,3-dimethyl-.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Experimental Study of the Dynamic Viscosity Deviations in the Binary Systems: Hexane + Ethylbenzene, + o-Xylene, + m-Xylene, + p-Xylene at 298.15 K
• Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
• 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
• Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
• Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
• 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
• Liquid liquid equilibrium of ternary systems 1-butyl-3-methylimidazolium hexafluorophosphate + aromatic + aliphatic
• 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
• Isothermal vapor liquid equilibria for binary mixtures of benzene, toluene, m-xylene, and N-methylformamide at 333.15K and 353.15K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
• Vapor liquid equilibria and density measurement for binary mixtures of toluene, benzene, o-xylene, m-xylene, sulfolane and nonane at 333.15K and 353.15K
• Vapor liquid 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
• Liquid liquid equilibrium of ternary systems 1-octyl-3-methylimidazolium hexafluorophosphate + aromatic + aliphatic hydrocarbons
• 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
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Study of [EMim][ESO4] ionic liquid as solvent in the liquid-liquid extraction of xylenes from their mixtures with hexane
• 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
• Solubility of hydrofluorocarbons in aromatic solvents and alcohols: Experimental data and modeling with CPA EoS
• Isobaric vapor-liquid equilibrium of binary systems of decane with p-, o-, m-xylene at 20 kPa
• Isobaric vapor-liquid equilibrium data of the binary systems of octane with p, o, m-xylene at 20 kPa
• (Liquid-liquid) equilibria for ternary and quaternary systems of representative compounds of gasoline + methanol at 293.15 K: Experimental data and correlation
• 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 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
• (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
• Excess molar volumes of (acetophenone + benzene, or toluene, or 1,3-xylene, or 1,3,5-trimethylbenzene) at temperatures (298.15 and 328.15) K
• A study of densities and volumetric properties of binary mixtures containing nitrobenzene at T = (293.15 to 353.15) K
• Liquid + liquid equilibria for ternary mixtures of (solvent + aromatic hydrocarbon + alkane)
• 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
• (Liquid + liquid) equilibria for ternary mixtures of (methanol or ethanol + toluene or m-xylene + n-dodecane)
• (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 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
• (Liquid + liquid) equilibria of three ternary systems: (heptane + benzene + N-formylmorpholine), (heptane + toluene + N-formylmorpholine), (heptane + xylene + N-formylmorpholine) from T = (298.15 to 353.15) K
• (Liquid + liquid) equilibria of ternary and quaternary systems containing n-hexane, toluene, m-xylene, propanol, sulfolane, and water at T = 303.15 K
• 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
• (Liquid + liquid) equilibria of {heptane + xylene + N-formylmorpholine} ternary system
• Excess molar volumes of (octane + benzene, or toluene, or 1,3-xylene, or 1,3,5-trimethylbenzene) at temperatures between (298.15 and 328.15) K
• 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
• 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
• Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Volumetric properties of binary mixtures of tributylamine with benzene derivatives and comparison with ERAS model results at temperatures from (293.15 to 333.15) K
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution 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
• Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• Acoustic and thermodynamic properties of binary mixtures of 1-nonanol with o-xylene, m-xylene, p-xylene, ethylbenzene and mesitylene at T = (298.15 and 308.15) K
• 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
• Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• 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
• Surface tension and density of mixtures of m-xylene + n-alkane at 293.15 K: Analysis under the extended Langmuir and Shereshefsky models
• 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
• 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
• P.rho.T measurements and modelling of (n-decane + m-xylene) mixtures from 293.15 K to 363.15 K at pressures up to 60 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 Enthalpies for Binary and Ternary Mixtures containing Cyclic Ether, 2-Methylaniline and Aromatic Hydrocarbons
• 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
• Mutual solubility of aromatic hydrocarbons in pyrrolidinium and ammonium-based ionic liquids and its modeling using the Cubic-Plus-Association (CPA) Equation of State
• Measurement and Correlation of the Solubility of e-CL-20 in 12 Organic Solvents at Temperatures Ranging from 278.15 to 318.15 K
• 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
• 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
• Thermophysical Study of Binary Systems of tert-Amyl Methyl Ether with n-Hexane and m-Xylene
• 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
• 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
• 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
• Solubilities of Bis (2,2,6,6-Tetramethyl-4-Piperidinyl) Maleate in Hexane, Heptane, Octane, m-Xylene and Tetrahydrofuran from (253.15 to 310.15) 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
• Solubility of Alkylbenzenes and a Model for Predicting the Solubility of Liquid Organics in High-Temperature Water
• 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
• 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
• Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
• Densities, Surface Tensions, and Refractive Indexes of Propyl Propanoate + Hexane + m-Xylene at 298.15 K
• Isobaric Vapor-Liquid Equilibria for the Binary Mixtures of Styrene with Ethylbenzene, o-Xylene, m-Xylene, and p-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
• 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
• Ternary Liquid-Liquid Equilibria for Mixtures of an Aromatic + an Aliphatic Hydrocarbon + 4-Methyl-N-butylpyridinium Tetrafluoroborate
• Ternary and Quaternary Liquid + Liquid Equilibria for Systems of (Water + Toluene + m-Xylene + Phenol)
• 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
• 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
• 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
• Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
• Excess Molar Volumes of 2,4,6,8-Tetramethylcyclotetrasiloxane with Benzene, Toluene, and Xylene at T = (288.15, 298.15, and 308.15) K
• 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
• 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
• 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
• 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
• 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
• Influence of the Temperature on the Liquid Liquid Equilibria of Heptane + Toluene + Sulfolane and Heptane + m-Xylene + Sulfolane
• Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Hexyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• 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
• Viscosity and Density of Five Hydrocarbon Liquids at Pressures up to 200 MPa and Temperatures up to 473 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
• Solubility of Acenaphthene in Different Solvents from (283.00 to 323.00) K
• Densities and Viscosities of Binary Mixtures of Methyl 4-Chlorobutyrate with Aromatic Hydrocarbons at T ) (298.15 to 318.15) K
• Thermodynamic Properties of the Binary Mixture of Hexan-1-ol with m-Xylene at T = (303.15, 313.15, and 323.15) 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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