Benzene, 1,3-dimethyl- (CAS 108-38-3)

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Physical Properties
Temperature Dependent Properties
Datasets
Correlations
Similar Compounds
Mixtures
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
T_ig	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
Δ_cH°_liquid	[-4581.40; -4549.56]	kJ/mol
Δ_cH°_liquid	-4549.56 ± 0.54	kJ/mol	NIST
Δ_cH°_liquid	-4551.86 ± 0.63	kJ/mol	NIST
Δ_cH°_liquid	-4567.60	kJ/mol	NIST
Δ_cH°_liquid	-4581.40	kJ/mol	NIST
C_p,liquid	181.38	J/mol×K	Thermodynamics of mixtures involving some (benzene derivatives + benzonitrile)
μ	0.30	debye	KDB
η	[0.0005870; 0.0005870]	Pa×s
η	0.0005870	Pa×s	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
η	0.0005870	Pa×s	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
S_Prot	19.20	J/mol×K	NIST
LFL	1.10	% in Air	KDB
UFL	6.40	% in Air	KDB
T_flash,oc	302.04	K	KDB
Δ_fG°	118.90	kJ/mol	KDB
R_g	3.8970		KDB
Δ_c,grossH	4551.86	kJ/mol	KDB
Δ_c,netH	4331.779	kJ/mol	KDB
Δ_fH°_gas	[17.20; 17.25]	kJ/mol
Δ_fH°_gas	17.25	kJ/mol	KDB
Δ_fH°_gas	17.20 ± 0.75	kJ/mol	NIST
Δ_fH°_liquid	-25.40 ± 0.75	kJ/mol	NIST
Δ_fusH°	10.13	kJ/mol	Joback Calculated Property
Δ_vapH°	[36.40; 43.04]	kJ/mol
Δ_vapH°	42.68	kJ/mol	NIST
Δ_vapH°	42.70	kJ/mol	NIST
Δ_vapH°	43.04	kJ/mol	NIST
Δ_vapH°	36.40	kJ/mol	NIST
Δ_vapH°	42.70 ± 0.10	kJ/mol	NIST
Δ_vapH°	42.65	kJ/mol	NIST
Δ_vapH°	42.60	kJ/mol	NIST
Δ_vapH°	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. Solubility Prediction
log₁₀WS	-2.82		Estimated Solubility
logP_oct/wat	2.303		Crippen Calculated Property
McVol	99.820	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	2		KDB
P_c	[3343.73; 3541.20]	kPa
P_c	3541.00	kPa	KDB
P_c	3540.00 ± 40.00	kPa	NIST
P_c	3541.20 ± 5.00	kPa	NIST
P_c	3541.00 ± 6.00	kPa	NIST
P_c	Outlier 3343.73 ± 151.99	kPa	NIST
P_c	3510.00 ± 3.92	kPa	NIST
ρ_c	[283.46; 284.95]	kg/m³
ρ_c	283.46 ± 4.25	kg/m³	NIST
ρ_c	284.95 ± 5.31	kg/m³	NIST
I_np	[130.11; 908.00]
I_np	859.00		NIST
I_np	848.40		NIST
I_np	855.20		NIST
I_np	852.10		NIST
I_np	850.50		NIST
I_np	852.30		NIST
I_np	856.70		NIST
I_np	882.70		NIST
I_np	888.10		NIST
I_np	849.80		NIST
I_np	852.30		NIST
I_np	854.80		NIST
I_np	857.40		NIST
I_np	859.60		NIST
I_np	860.90		NIST
I_np	863.50		NIST
I_np	856.77		NIST
I_np	876.00		NIST
I_np	876.00		NIST
I_np	876.00		NIST
I_np	863.30		NIST
I_np	871.20		NIST
I_np	856.10		NIST
I_np	856.40		NIST
I_np	856.40		NIST
I_np	856.60		NIST
I_np	855.90		NIST
I_np	865.00		NIST
I_np	857.00		NIST
I_np	857.00		NIST
I_np	867.00		NIST
I_np	867.00		NIST
I_np	856.00		NIST
I_np	865.20		NIST
I_np	866.00		NIST
I_np	866.00		NIST
I_np	866.00		NIST
I_np	854.00		NIST
I_np	850.10		NIST
I_np	855.30		NIST
I_np	865.00		NIST
I_np	865.00		NIST
I_np	866.00		NIST
I_np	866.00		NIST
I_np	868.00		NIST
I_np	862.00		NIST
I_np	864.00		NIST
I_np	850.20		NIST
I_np	880.00		NIST
I_np	866.00		NIST
I_np	867.00		NIST
I_np	866.00		NIST
I_np	867.00		NIST
I_np	862.00		NIST
I_np	864.00		NIST
I_np	860.00		NIST
I_np	856.10		NIST
I_np	856.60		NIST
I_np	859.60		NIST
I_np	876.00		NIST
I_np	864.00		NIST
I_np	867.00		NIST
I_np	871.00		NIST
I_np	877.00		NIST
I_np	861.00		NIST
I_np	863.20		NIST
I_np	866.60		NIST
I_np	871.10		NIST
I_np	876.60		NIST
I_np	859.00		NIST
I_np	863.00		NIST
I_np	850.50		NIST
I_np	855.70		NIST
I_np	860.60		NIST
I_np	860.80		NIST
I_np	861.00		NIST
I_np	861.70		NIST
I_np	856.40		NIST
I_np	857.40		NIST
I_np	861.00		NIST
I_np	855.30		NIST
I_np	855.60		NIST
I_np	861.00		NIST
I_np	863.20		NIST
I_np	865.00		NIST
I_np	862.00		NIST
I_np	862.00		NIST
I_np	857.76		NIST
I_np	863.00		NIST
I_np	882.00		NIST
I_np	886.00		NIST
I_np	868.00		NIST
I_np	857.80		NIST
I_np	863.20		NIST
I_np	866.00		NIST
I_np	857.00		NIST
I_np	865.00		NIST
I_np	869.00		NIST
I_np	871.00		NIST
I_np	874.00		NIST
I_np	878.00		NIST
I_np	852.30		NIST
I_np	861.10		NIST
I_np	863.00		NIST
I_np	867.10		NIST
I_np	866.30		NIST
I_np	860.30		NIST
I_np	896.00		NIST
I_np	847.00		NIST
I_np	852.00		NIST
I_np	858.00		NIST
I_np	862.00		NIST
I_np	895.00		NIST
I_np	902.00		NIST
I_np	908.00		NIST
I_np	889.00		NIST
I_np	867.00		NIST
I_np	871.00		NIST
I_np	863.00		NIST
I_np	900.00		NIST
I_np	872.50		NIST
I_np	866.00		NIST
I_np	862.00		NIST
I_np	852.00		NIST
I_np	859.00		NIST
I_np	861.00		NIST
I_np	863.00		NIST
I_np	864.00		NIST
I_np	864.00		NIST
I_np	864.00		NIST
I_np	887.00		NIST
I_np	865.05		NIST
I_np	858.00		NIST
I_np	865.00		NIST
I_np	874.00		NIST
I_np	875.00		NIST
I_np	853.20		NIST
I_np	853.20		NIST
I_np	863.00		NIST
I_np	871.00		NIST
I_np	859.40		NIST
I_np	898.00		NIST
I_np	838.00		NIST
I_np	861.70		NIST
I_np	864.40		NIST
I_np	866.50		NIST
I_np	848.20		NIST
I_np	877.80		NIST
I_np	871.00		NIST
I_np	849.00		NIST
I_np	868.00		NIST
I_np	847.00		NIST
I_np	847.00		NIST
I_np	855.50		NIST
I_np	890.21		NIST
I_np	892.69		NIST
I_np	862.00		NIST
I_np	865.00		NIST
I_np	844.60		NIST
I_np	850.20		NIST
I_np	853.80		NIST
I_np	855.40		NIST
I_np	869.30		NIST
I_np	861.70		NIST
I_np	864.40		NIST
I_np	866.50		NIST
I_np	852.91		NIST
I_np	853.44		NIST
I_np	854.00		NIST
I_np	853.38		NIST
I_np	853.85		NIST
I_np	853.00		NIST
I_np	863.00		NIST
I_np	861.00		NIST
I_np	853.96		NIST
I_np	850.24		NIST
I_np	852.98		NIST
I_np	854.72		NIST
I_np	865.16		NIST
I_np	868.16		NIST
I_np	870.12		NIST
I_np	852.00		NIST
I_np	861.50		NIST
I_np	885.00		NIST
I_np	863.00		NIST
I_np	866.00		NIST
I_np	873.00		NIST
I_np	874.00		NIST
I_np	879.49		NIST
I_np	854.00		NIST
I_np	871.00		NIST
I_np	877.00		NIST
I_np	855.00		NIST
I_np	866.00		NIST
I_np	866.00		NIST
I_np	866.00		NIST
I_np	867.00		NIST
I_np	865.00		NIST
I_np	868.00		NIST
I_np	866.00		NIST
I_np	867.00		NIST
I_np	870.00		NIST
I_np	871.00		NIST
I_np	849.00		NIST
I_np	862.00		NIST
I_np	847.00		NIST
I_np	855.00		NIST
I_np	853.00		NIST
I_np	858.00		NIST
I_np	871.00		NIST
I_np	867.00		NIST
I_np	852.00		NIST
I_np	868.00		NIST
I_np	874.00		NIST
I_np	870.00		NIST
I_np	861.00		NIST
I_np	859.00		NIST
I_np	867.00		NIST
I_np	869.00		NIST
I_np	874.00		NIST
I_np	871.00		NIST
I_np	863.00		NIST
I_np	860.00		NIST
I_np	870.00		NIST
I_np	878.00		NIST
I_np	878.00		NIST
I_np	871.20		NIST
I_np	875.00		NIST
I_np	849.00		NIST
I_np	848.00		NIST
I_np	864.00		NIST
I_np	869.00		NIST
I_np	875.00		NIST
I_np	873.00		NIST
I_np	864.00		NIST
I_np	846.40		NIST
I_np	875.00		NIST
I_np	877.00		NIST
I_np	860.00		NIST
I_np	857.00		NIST
I_np	873.00		NIST
I_np	873.00		NIST
I_np	875.30		NIST
I_np	853.00		NIST
I_np	860.00		NIST
I_np	848.00		NIST
I_np	851.00		NIST
I_np	851.00		NIST
I_np	867.00		NIST
I_np	856.00		NIST
I_np	857.00		NIST
I_np	852.00		NIST
I_np	852.00		NIST
I_np	866.00		NIST
I_np	851.20		NIST
I_np	853.20		NIST
I_np	856.10		NIST
I_np	858.20		NIST
I_np	860.00		NIST
I_np	851.00		NIST
I_np	853.00		NIST
I_np	856.00		NIST
I_np	859.00		NIST
I_np	861.00		NIST
I_np	852.00		NIST
I_np	853.00		NIST
I_np	854.00		NIST
I_np	835.00		NIST
I_np	860.00		NIST
I_np	866.00		NIST
I_np	866.00		NIST
I_np	872.00		NIST
I_np	874.00		NIST
I_np	864.00		NIST
I_np	866.00		NIST
I_np	873.00		NIST
I_np	880.00		NIST
I_np	876.00		NIST
I_np	864.00		NIST
I_np	864.00		NIST
I_np	853.00		NIST
I_np	860.00		NIST
I_np	867.00		NIST
I_np	852.00		NIST
I_np	874.00		NIST
I_np	860.00		NIST
I_np	847.12		NIST
I_np	878.00		NIST
I_np	888.00		NIST
I_np	866.00		NIST
I_np	856.00		NIST
I_np	877.00		NIST
I_np	863.00		NIST
I_np	854.00		NIST
I_np	856.00		NIST
I_np	865.00		NIST
I_np	869.00		NIST
I_np	873.00		NIST
I_np	871.00		NIST
I_np	860.00		NIST
I_np	866.00		NIST
I_np	855.00		NIST
I_np	866.00		NIST
I_np	863.00		NIST
I_np	855.00		NIST
I_np	856.00		NIST
I_np	869.00		NIST
I_np	871.00		NIST
I_np	864.40		NIST
I_np	868.00		NIST
I_np	852.00		NIST
I_np	845.00		NIST
I_np	852.00		NIST
I_np	863.00		NIST
I_np	876.00		NIST
I_np	849.00		NIST
I_np	852.00		NIST
I_np	854.00		NIST
I_np	858.00		NIST
I_np	864.00		NIST
I_np	863.00		NIST
I_np	874.00		NIST
I_np	858.00		NIST
I_np	874.00		NIST
I_np	Outlier 130.11		NIST
I_np	874.00		NIST
I_np	871.00		NIST
I_np	864.40		NIST
I_np	849.00		NIST
I_np	890.21		NIST
I_np	850.20		NIST
I_np	853.38		NIST
I_np	853.96		NIST
I_np	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
T_boil	[409.00; 413.35]	K
T_boil	412.27	K	KDB
T_boil	412.00	K	Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
T_boil	412.21	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
T_boil	412.15 ± 0.20	K	NIST
T_boil	412.29 ± 0.15	K	NIST
T_boil	412.30	K	NIST
T_boil	412.30	K	NIST
T_boil	412.20 ± 0.20	K	NIST
T_boil	412.40 ± 0.20	K	NIST
T_boil	412.25 ± 1.00	K	NIST
T_boil	Outlier 409.00 ± 8.00	K	NIST
T_boil	412.23 ± 0.20	K	NIST
T_boil	412.30 ± 0.50	K	NIST
T_boil	412.10 ± 0.40	K	NIST
T_boil	412.00 ± 1.50	K	NIST
T_boil	412.40 ± 0.50	K	NIST
T_boil	412.25 ± 0.02	K	NIST
T_boil	412.40 ± 0.60	K	NIST
T_boil	412.30 ± 0.15	K	NIST
T_boil	412.40 ± 0.50	K	NIST
T_boil	412.35 ± 0.50	K	NIST
T_boil	412.25 ± 0.01	K	NIST
T_boil	412.15 ± 1.00	K	NIST
T_boil	412.26 ± 0.06	K	NIST
T_boil	412.35 ± 0.30	K	NIST
T_boil	412.38 ± 0.10	K	NIST
T_boil	412.22 ± 0.20	K	NIST
T_boil	412.35 ± 0.50	K	NIST
T_boil	412.45 ± 0.20	K	NIST
T_boil	412.65 ± 1.20	K	NIST
T_boil	412.20 ± 0.50	K	NIST
T_boil	412.20 ± 0.50	K	NIST
T_boil	412.20 ± 0.50	K	NIST
T_boil	412.50 ± 0.20	K	NIST
T_boil	412.50 ± 0.30	K	NIST
T_boil	412.45 ± 0.40	K	NIST
T_boil	Outlier 409.00 ± 3.00	K	NIST
T_boil	412.15 ± 0.10	K	NIST
T_boil	412.00 ± 2.00	K	NIST
T_boil	412.15 ± 0.30	K	NIST
T_boil	412.00 ± 2.00	K	NIST
T_boil	412.45 ± 0.50	K	NIST
T_boil	412.45 ± 0.50	K	NIST
T_boil	411.90 ± 0.70	K	NIST
T_boil	413.35 ± 1.50	K	NIST
T_boil	412.40 ± 1.50	K	NIST
T_c	617.00	K	KDB
T_fus	[219.55; 226.65]	K
T_fus	225.30	K	KDB
T_fus	225.55	K	Aq. Solubility Prediction
T_fus	225.20 ± 0.15	K	NIST
T_fus	225.80 ± 0.30	K	NIST
T_fus	225.22 ± 0.15	K	NIST
T_fus	225.17 ± 0.01	K	NIST
T_fus	225.25 ± 0.10	K	NIST
T_fus	226.65 ± 0.20	K	NIST
T_fus	225.80 ± 0.50	K	NIST
T_fus	223.85 ± 0.30	K	NIST
T_fus	Outlier 219.55 ± 0.40	K	NIST
T_triple	219.60 ± 0.30	K	NIST
V_c	[0.375; 0.375]	m³/kmol
V_c	0.375	m³/kmol	KDB
V_c	0.375	m³/kmol	NIST
Z_c	0.2588420		KDB
Z_ra	0.26		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[163.60; 190.00]	J/mol×K	[393.00; 463.00]
C_p,gas	163.60 ± 1.70	J/mol×K	393.00	NIST
C_p,gas	177.40 ± 1.70	J/mol×K	428.00	NIST
C_p,gas	190.00 ± 1.70	J/mol×K	463.00	NIST
C_p,liquid	[175.30; 199.20]	J/mol×K	[275.30; 336.00]

C_p,liquid	175.30	J/mol×K	275.30	NIST
C_p,liquid	184.50	J/mol×K	298.00	NIST
C_p,liquid	184.63	J/mol×K	298.15	NIST
C_p,liquid	181.55	J/mol×K	298.15	NIST
C_p,liquid	181.48	J/mol×K	298.15	NIST
C_p,liquid	183.18	J/mol×K	298.15	NIST
C_p,liquid	178.20	J/mol×K	303.00	NIST
C_p,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	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
η	0.0006190	Pa×s	293.15	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
η	0.0005892	Pa×s	298.15	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
η	0.0005820	Pa×s	298.15	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
η	0.0005848	Pa×s	298.15	Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
η	0.0005810	Pa×s	298.15	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
η	0.0005870	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of Methyl 4-Chlorobutyrate with Aromatic Hydrocarbons at T ) (298.15 to 318.15) K
η	0.0005880	Pa×s	298.15	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
η	0.0005471	Pa×s	303.15	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
η	0.0005501	Pa×s	303.15	Thermodynamic Properties of the Binary Mixture of Hexan-1-ol with m-Xylene at T = (303.15, 313.15, and 323.15) K
η	0.0005531	Pa×s	303.15	Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
η	0.0005540	Pa×s	303.15	Viscometric Studies of Molecular Interactions in Binary Liquid Mixtures of Isomeric Xylenes with Methanol
η	0.0005570	Pa×s	303.15	Thermophysical Properties of Isoamyl Acetate or Methyl Benzoate + Hydrocarbon Binary Mixtures, at (303.15 and 313.15) K
η	0.0005570	Pa×s	303.15	Viscosity, Density, and Refractive Index of Some (Ester + Hydrocarbon) Binary Mixtures at 303.15 K and 313.15 K
η	0.0005490	Pa×s	303.15	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
η	0.0005520	Pa×s	303.15	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
η	0.0005229	Pa×s	308.15	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
η	0.0005240	Pa×s	308.15	Densities and Viscosities of Binary Mixtures of Methyl 4-Chlorobutyrate with Aromatic Hydrocarbons at T ) (298.15 to 318.15) K
η	0.0004990	Pa×s	308.15	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
η	0.0005210	Pa×s	308.15	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
η	0.0005201	Pa×s	308.15	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
η	0.0005240	Pa×s	308.15	Viscometric Studies of Molecular Interactions in Binary Liquid Mixtures of Isomeric Xylenes with Methanol
η	0.0004967	Pa×s	313.15	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
η	0.0004970	Pa×s	313.15	Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
η	0.0004944	Pa×s	313.15	Thermodynamic Properties of the Binary Mixture of Hexan-1-ol with m-Xylene at T = (303.15, 313.15, and 323.15) K
η	0.0004980	Pa×s	313.15	Viscometric Studies of Molecular Interactions in Binary Liquid Mixtures of Isomeric Xylenes with Methanol
η	0.0005080	Pa×s	313.15	Thermophysical Properties of Isoamyl Acetate or Methyl Benzoate + Hydrocarbon Binary Mixtures, at (303.15 and 313.15) K
η	0.0005080	Pa×s	313.15	Viscosity, Density, and Refractive Index of Some (Ester + Hydrocarbon) Binary Mixtures at 303.15 K and 313.15 K
η	0.0004700	Pa×s	318.15	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
η	0.0004720	Pa×s	318.15	Viscometric Studies of Molecular Interactions in Binary Liquid Mixtures of Isomeric Xylenes with Methanol
η	0.0004684	Pa×s	318.15	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
η	0.0004817	Pa×s	318.15	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
η	0.0004710	Pa×s	318.15	Densities and Viscosities of Binary Mixtures of Methyl 4-Chlorobutyrate with Aromatic Hydrocarbons at T ) (298.15 to 318.15) K
η	0.0004520	Pa×s	323.15	Viscometric Studies of Molecular Interactions in Binary Liquid Mixtures of Isomeric Xylenes with Methanol
η	0.0004440	Pa×s	323.15	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
η	0.0004428	Pa×s	323.15	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
η	0.0004488	Pa×s	323.15	Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
η	0.0004472	Pa×s	323.15	Thermodynamic Properties of the Binary Mixture of Hexan-1-ol with m-Xylene at T = (303.15, 313.15, and 323.15) K
η	0.0004350	Pa×s	328.15	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
η	0.0004130	Pa×s	333.15	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
η	0.0004101	Pa×s	333.15	Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
η	0.0003748	Pa×s	343.15	Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
η	0.0003440	Pa×s	353.15	Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
Δ_fusH	[11.57; 11.59]	kJ/mol	[225.27; 225.30]
Δ_fusH	11.57	kJ/mol	225.27	NIST
Δ_fusH	11.59	kJ/mol	225.30	NIST
Δ_fusH	11.57	kJ/mol	225.30	NIST
Δ_vapH	[35.66; 44.70]	kJ/mol	[284.00; 583.50]

Δ_vapH	44.70	kJ/mol	284.00	NIST
Δ_vapH	43.20	kJ/mol	303.00	NIST
Δ_vapH	40.70	kJ/mol	369.50	NIST
Δ_vapH	40.40	kJ/mol	373.00	NIST
Δ_vapH	39.20	kJ/mol	385.00	NIST
Δ_vapH	38.70	kJ/mol	395.50	NIST
Δ_vapH	36.36	kJ/mol	412.20	KDB
Δ_vapH	35.66	kJ/mol	412.30	NIST
Δ_vapH	37.50	kJ/mol	437.00	NIST
Δ_vapH	36.40	kJ/mol	507.50	NIST
Δ_vapH	36.20	kJ/mol	583.50	NIST
P_vap	[0.10; 250.00]	kPa	[263.75; 450.10]

P_vap	0.10	kPa	263.75	Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
P_vap	0.21	kPa	273.47	Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
P_vap	0.43	kPa	283.35	Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
P_vap	0.86	kPa	293.29	Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
P_vap	1.10	kPa	298.15	(Vapour + liquid) equilibria of (1-butanol + benzene, or toluene, or o-, or m-, or p-xylene) at T = 308.15 K
P_vap	1.59	kPa	303.28	Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
P_vap	2.63	kPa	308.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	3.52	kPa	313.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	2.77	kPa	313.27	Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
P_vap	4.37	kPa	318.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	5.37	kPa	323.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	4.41	kPa	323.25	Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
P_vap	6.50	kPa	328.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	7.75	kPa	333.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	6.59	kPa	333.15	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
P_vap	6.58	kPa	333.15	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
P_vap	6.85	kPa	333.22	Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
P_vap	9.30	kPa	338.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	10.17	kPa	343.15	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
P_vap	11.12	kPa	343.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	10.48	kPa	343.18	Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
P_vap	11.00	kPa	345.15	Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
P_vap	13.44	kPa	350.15	Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
P_vap	15.09	kPa	353.15	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
P_vap	15.12	kPa	353.15	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
P_vap	15.97	kPa	353.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	16.32	kPa	355.15	Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
P_vap	19.68	kPa	360.15	Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
P_vap	22.76	kPa	363.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	23.59	kPa	365.15	Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
P_vap	32.06	kPa	373.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	40.00	kPa	380.51	Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
P_vap	44.23	kPa	383.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	53.33	kPa	389.66	Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
P_vap	66.66	kPa	397.13	Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
P_vap	80.20	kPa	403.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	79.99	kPa	403.51	Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
P_vap	93.32	kPa	409.09	Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
P_vap	93.13	kPa	409.13	Refractive Index and Vapor-Liquid Equilibrium Data for the Binary Systems of Anisole with Xylene Isomers at 93.13 kPa
P_vap	101.30	kPa	412.00	Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
P_vap	250.00	kPa	450.10	Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
n₀	[1.48440; 1.49990]		[288.15; 318.15]

n₀	1.49990		288.15	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
n₀	1.49990		288.15	Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n₀	1.49970		288.15	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
n₀	1.49730		293.10	Volumetric properties of (cyclohexanone + a xylene) at temperature between (293.15 and 353.15) K
n₀	1.49430		293.10	(Liquid + liquid) equilibria of {heptane + xylene + N-formylmorpholine} ternary system
n₀	1.49430		293.10	(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
n₀	1.49360		293.15	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
n₀	1.49730		293.15	Densities and volumetric properties of a (xylene + dimethyl sulfoxide) at temperature from (293.15 to 353.15) K
n₀	1.49735		293.15	A study of densities and volumetric properties of binary mixtures containing nitrobenzene at T = (293.15 to 353.15) K
n₀	1.49720		293.15	Solubilities of Methyldiphenylphosphine Oxide in Selected Solvents
n₀	1.49720		293.15	Excess Gibbs' energies of the binary mixtures formed by N,N-dimethylformamide with xylenes and cresols at 95.1 kPa
n₀	1.49730		293.15	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
n₀	1.49740		293.15	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
n₀	1.49740		293.15	Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n₀	1.49720		293.15	Bubble points of some binary mixtures formed by o-cresol at 95.75 kPa
n₀	1.49720		293.15	Activity coefficients and excess Gibbs free energy of some binary mixtures formed by p-cresol at 95.23 kPa
n₀	1.49468		298.15	Separation of aromatic hydrocarbons from alkanes using ammonium ionic liquid C2NTf2 at T = 298.15K
n₀	1.49480		298.15	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
n₀	1.49730		298.15	Densities and volumetric properties of binary mixtures of xylene with N,N-dimethylformamide at different temperatures
n₀	1.49450		298.15	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
n₀	1.49464		298.15	KDB
n₀	1.49430		298.15	Liquid-liquid equilibria for mixtures of (Furfural + an Aromatic hydrocarbon + an alkane) at T=298.15 K
n₀	1.49470		298.15	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
n₀	1.49450		298.15	Densities, Surface Tensions, and Refractive Indexes of Propyl Propanoate + Hexane + m-Xylene at 298.15 K
n₀	1.49440		298.15	Isobaric Vapor-Liquid Equilibria for the Binary Mixtures of Styrene with Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene
n₀	1.49440		298.15	Densities, Excess Molar Volumes, Viscosity, and Refractive Indices of Binary Mixtures of Ethanoic Acid and Trichloroethylene with Dimethylbenzenes at Different Temperatures
n₀	1.49466		298.15	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
n₀	1.49460		298.15	(Vapor + liquid) equilibria of binary mixtures formed by iso-octane with a variety of compounds at 95.8 kPa
n₀	1.49480		298.15	Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n₀	1.49730		298.15	A study of densities and volumetric properties of binary mixtures of N-methyl-2-pyrrolidone with xylene at different temperatures and atmospheric pressure
n₀	1.49440		298.15	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
n₀	1.49460		298.15	Bubble temperature measurements on the binary mixtures formed by decane with a variety of compounds at 95.8 kPa
n₀	1.49220		303.15	Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n₀	1.49220		303.15	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
n₀	1.49250		303.15	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
n₀	1.48960		308.15	Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n₀	1.48960		308.15	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
n₀	1.49460		308.15	Topological and thermodynamic investigations of molecular interactions in binary mixtures: Molar excess volumes and molar excess enthalpies
n₀	1.48700		313.15	Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n₀	1.48700		313.15	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
n₀	1.48653		313.15	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
n₀	1.48440		318.15	Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n₀	1.48440		318.15	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
ρ_l	[810.51; 868.59]	kg/m³	[288.15; 353.15]

ρ_l	868.59	kg/m³	288.15	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
ρ_l	868.56	kg/m³	288.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρ_l	868.39	kg/m³	288.15	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
ρ_l	864.00	kg/m³	293.00	KDB
ρ_l	864.20	kg/m³	293.10	Vapor-Liquid Equilibria Data for Binary Systems of Ethylbenzene + Xylene Isomers at 100.65 kPa
ρ_l	864.20	kg/m³	293.15	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
ρ_l	864.11	kg/m³	293.15	Isobaric vapor liquid equilibium for the binary systerms of 1-butanol with o-xylene, m-xylene, p-xylene, and ethylbenzene at 101.33 kPa
ρ_l	864.31	kg/m³	293.15	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
ρ_l	864.27	kg/m³	293.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρ_l	864.16	kg/m³	293.15	Surface tension and density of mixtures of m-xylene + n-alkane at 293.15 K: Analysis under the extended Langmuir and Shereshefsky models
ρ_l	868.12	kg/m³	293.15	Liquid liquid equilibrium of ternary systems 1-butyl-3-methylimidazolium hexafluorophosphate + aromatic + aliphatic
ρ_l	859.87	kg/m³	298.15	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
ρ_l	859.83	kg/m³	298.15	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
ρ_l	859.95	kg/m³	298.15	Isobaric vapor-liquid equilibrium data of the binary systems of octane with p, o, m-xylene at 20 kPa
ρ_l	860.06	kg/m³	298.15	Isobaric Vapor Liquid Equilibrium for the Binary Systems of Diethyl Carbonate with Xylene Isomers and Ethylbenzene at 101.33 kPa
ρ_l	860.00	kg/m³	298.15	Excess Molar Entalpies of Dimethyl Carbonate with o-Xylene, m-Xylene, p-Xylene, Ethylbenzene, or Ethyl Benzoate at 298.15 K
ρ_l	860.06	kg/m³	298.15	Vapor Liquid Equilibrium for 2-Methyl-1-butanol + Ethylbenzene + Xylene Isomers at 101.33 kPa
ρ_l	860.00	kg/m³	298.15	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
ρ_l	859.78	kg/m³	298.15	Experimental Study of the Dynamic Viscosity Deviations in the Binary Systems: Hexane + Ethylbenzene, + o-Xylene, + m-Xylene, + p-Xylene at 298.15 K
ρ_l	859.86	kg/m³	298.15	Excess Molar Volumes of 2,4,6,8-Tetramethylcyclotetrasiloxane with Benzene, Toluene, and Xylene at T = (288.15, 298.15, and 308.15) K
ρ_l	859.95	kg/m³	298.15	Isobaric vapor-liquid equilibrium of binary systems of decane with p-, o-, m-xylene at 20 kPa
ρ_l	859.78	kg/m³	298.15	Excess Molar Volumes and Surface Tensions of Xylene with Acetone or 2-Butanone at 298.15 K
ρ_l	859.95	kg/m³	298.15	Isobaric vapor-liquid equilibrium for n-undecane + p-, o-, m-xylene at 10 kPa
ρ_l	860.02	kg/m³	298.15	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
ρ_l	859.10	kg/m³	298.15	Thermophysical Study of Binary Systems of tert-Amyl Methyl Ether with n-Hexane and m-Xylene
ρ_l	859.78	kg/m³	298.15	Excess Molar Volumes and Surface Tensions of Xylene with Isopropyl Ether or Methyl tert-Butyl Ether at 298.15 K
ρ_l	859.98	kg/m³	298.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρ_l	860.07	kg/m³	298.20	Isobaric Vapor Liquid Equilibrium of Binary Systems of Hexane or Octane with 1,2-Dimethylbenzene or 1,3-Dimethylbenzene at 101.3 kPa
ρ_l	855.74	kg/m³	303.15	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
ρ_l	855.68	kg/m³	303.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρ_l	855.76	kg/m³	303.15	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
ρ_l	851.45	kg/m³	308.15	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
ρ_l	851.24	kg/m³	308.15	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
ρ_l	851.36	kg/m³	308.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρ_l	851.25	kg/m³	308.15	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
ρ_l	849.20	kg/m³	308.15	Thermophysical Study of Binary Systems of tert-Amyl Methyl Ether with n-Hexane and m-Xylene
ρ_l	847.17	kg/m³	313.15	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
ρ_l	847.03	kg/m³	313.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρ_l	847.11	kg/m³	313.15	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
ρ_l	842.58	kg/m³	318.15	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
ρ_l	842.69	kg/m³	318.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρ_l	840.40	kg/m³	318.15	Thermophysical Study of Binary Systems of tert-Amyl Methyl Ether with n-Hexane and m-Xylene
ρ_l	842.88	kg/m³	318.15	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
ρ_l	835.80	kg/m³	323.15	Thermophysical Study of Binary Systems of tert-Amyl Methyl Ether with n-Hexane and m-Xylene
ρ_l	838.27	kg/m³	323.15	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
ρ_l	838.33	kg/m³	323.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρ_l	831.60	kg/m³	328.15	Thermophysical Study of Binary Systems of tert-Amyl Methyl Ether with n-Hexane and m-Xylene
ρ_l	833.95	kg/m³	328.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρ_l	833.85	kg/m³	328.15	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
ρ_l	829.22	kg/m³	333.15	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
ρ_l	829.56	kg/m³	333.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρ_l	819.97	kg/m³	343.15	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
ρ_l	810.51	kg/m³	353.15	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
Δ_fusS	51.36	J/mol×K	225.27	NIST
c_sound,fluid	[1219.51; 1362.66]	m/s	[288.15; 323.15]

c_sound,fluid	1362.66	m/s	288.15	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1352.14	m/s	290.65	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1340.00	m/s	293.15	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
c_sound,fluid	1341.72	m/s	293.15	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1346.70	m/s	293.15	Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
c_sound,fluid	1341.00	m/s	293.15	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
c_sound,fluid	1331.31	m/s	295.65	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1320.92	m/s	298.15	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1323.60	m/s	298.15	Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
c_sound,fluid	1310.57	m/s	300.65	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1300.00	m/s	303.15	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
c_sound,fluid	1300.27	m/s	303.15	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1302.40	m/s	303.15	Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
c_sound,fluid	1290.00	m/s	305.65	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1282.30	m/s	308.15	Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
c_sound,fluid	1279.79	m/s	308.15	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1269.59	m/s	310.65	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1262.30	m/s	313.15	Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
c_sound,fluid	1259.46	m/s	313.15	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1259.00	m/s	313.15	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
c_sound,fluid	1249.33	m/s	315.65	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1239.28	m/s	318.15	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1243.00	m/s	318.15	Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
c_sound,fluid	1229.26	m/s	320.65	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1219.51	m/s	323.15	Influence of temperature on thermodynamics of ethers + xylenes
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	Experimental and theoretical surface tension deviations in the binary systems propyl propanoate + o-, m- and p-xylene at 298.15K
γ	0.03	N/m	298.15	Densities and Surface Tensions of Propyl Acetate + Xylenes or + Ethylbenzene from (298.15 to 308.15) K
γ	0.03	N/m	303.15	Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K
γ	0.03	N/m	303.15	Densities and Surface Tensions of Propyl Acetate + Xylenes or + Ethylbenzene from (298.15 to 308.15) K
γ	0.03	N/m	308.15	Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K
γ	0.03	N/m	308.15	Densities and Surface Tensions of Propyl Acetate + Xylenes or + Ethylbenzene from (298.15 to 308.15) K
γ	0.03	N/m	313.15	Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K
γ	0.03	N/m	318.15	Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K
γ	0.03	N/m	323.15	Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K
γ	0.02	N/m	333.15	Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K
γ	0.02	N/m	343.15	Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K
λ	[0.12; 0.14]	W/m×K	[258.17; 329.22]

λ	0.14	W/m×K	258.17	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.14	W/m×K	258.42	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.14	W/m×K	258.58	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.14	W/m×K	275.04	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.14	W/m×K	275.28	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.14	W/m×K	275.44	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.13	W/m×K	287.36	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.13	W/m×K	287.60	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.13	W/m×K	287.77	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.13	W/m×K	294.07	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.13	W/m×K	294.32	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.13	W/m×K	294.49	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.13	W/m×K	311.74	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.13	W/m×K	312.00	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.13	W/m×K	312.18	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.12	W/m×K	328.79	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.12	W/m×K	329.04	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.12	W/m×K	329.22	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons

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
P_vap	[1.33; 202.63]	kPa	[300.97; 439.80]	The Yaws Handbook of Vapor Pressure
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

P_vap	1.33	kPa	300.97	Calculated Property
P_vap	3.01	kPa	316.40	Calculated Property
P_vap	6.21	kPa	331.82	Calculated Property
P_vap	11.91	kPa	347.25	Calculated Property
P_vap	21.44	kPa	362.67	Calculated Property
P_vap	36.52	kPa	378.10	Calculated Property
P_vap	59.35	kPa	393.52	Calculated Property
P_vap	92.54	kPa	408.95	Calculated Property
P_vap	139.14	kPa	424.37	Calculated Property
P_vap	202.63	kPa	439.80	Calculated Property
P_vap	[3.23e-03; 3526.67]	kPa	[225.30; 617.05]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + Cln(T) + DT^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

P_vap	3.23e-03	kPa	225.30	Calculated Property
P_vap	0.17	kPa	268.83	Calculated Property
P_vap	2.44	kPa	312.36	Calculated Property
P_vap	16.77	kPa	355.88	Calculated Property
P_vap	70.86	kPa	399.41	Calculated Property
P_vap	216.17	kPa	442.94	Calculated Property
P_vap	527.17	kPa	486.47	Calculated Property
P_vap	1098.76	kPa	529.99	Calculated Property
P_vap	2048.41	kPa	573.52	Calculated Property
P_vap	3526.67	kPa	617.05	Calculated Property

Similar Compounds

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Mixtures

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Sources

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

Contents