p-Xylene (CAS 106-42-3)

Please note that you need to enable javascript to get access to all the properties. Here is how to do it for Internet Explorer and for Firefox.

Physical Properties
Temperature Dependent Properties
Pressure Dependent Properties
Datasets
Correlations
Similar Compounds
Mixtures
Sources

Physical Properties

Property	Value	Unit	Source
ω	0.3200		KDB
PAff	[790.50; 794.40]	kJ/mol
PAff	794.40	kJ/mol	NIST
PAff	793.70	kJ/mol	NIST
PAff	790.50 ± 1.10	kJ/mol	NIST
T_ig	738.71	K	KDB
BasG	[766.80; 771.30]	kJ/mol
BasG	766.80	kJ/mol	NIST
BasG	766.90	kJ/mol	NIST
BasG	771.30 ± 1.40	kJ/mol	NIST
Δ_cH°_liquid	[-4565.90; -4551.44]	kJ/mol
Δ_cH°_liquid	-4551.44 ± 0.50	kJ/mol	NIST
Δ_cH°_liquid	-4552.86 ± 0.92	kJ/mol	NIST
Δ_cH°_liquid	-4551.70	kJ/mol	NIST
Δ_cH°_liquid	-4565.90	kJ/mol	NIST
C_p,liquid	181.73	J/mol×K	Thermodynamics of mixtures involving some (benzene derivatives + benzonitrile)
μ	0.10	debye	KDB
η	[0.0006090; 0.0006090]	Pa×s
η	0.0006090	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	0.0006090	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
EA	0.00 ± 0.00	eV	NIST
S_Prot	44.20	J/mol×K	NIST
LFL	1.10	% in Air	KDB
UFL	6.60	% in Air	KDB
T_flash,oc	300.37	K	KDB
Δ_fG°	121.20	kJ/mol	KDB
R_g	3.7960		KDB
Δ_c,grossH	4552.86	kJ/mol	KDB
Δ_c,netH	4332.784	kJ/mol	KDB
Δ_fH°_gas	[17.90; 17.96]	kJ/mol
Δ_fH°_gas	17.96	kJ/mol	KDB
Δ_fH°_gas	17.90 ± 1.00	kJ/mol	NIST
Δ_fH°_liquid	-24.40 ± 1.00	kJ/mol	NIST
Δ_fusH°	10.13	kJ/mol	Joback Calculated Property
Δ_vapH°	[35.90; 43.00]	kJ/mol
Δ_vapH°	42.42	kJ/mol	NIST
Δ_vapH°	42.30	kJ/mol	NIST
Δ_vapH°	43.00 ± 0.10	kJ/mol	NIST
Δ_vapH°	42.35 ± 0.10	kJ/mol	NIST
Δ_vapH°	42.30 ± 0.01	kJ/mol	NIST
Δ_vapH°	42.30 ± 0.10	kJ/mol	NIST
Δ_vapH°	42.60	kJ/mol	NIST
Δ_vapH°	42.40	kJ/mol	NIST
Δ_vapH°	42.72	kJ/mol	NIST
Δ_vapH°	Outlier 35.90	kJ/mol	NIST
Δ_vapH°	42.40 ± 0.10	kJ/mol	NIST
Δ_vapH°	42.37	kJ/mol	NIST
Δ_vapH°	42.30	kJ/mol	NIST
Δ_vapH°	Outlier 36.00 ± 0.08	kJ/mol	NIST
IE	[8.37; 8.80]	eV
IE	8.44 ± 0.05	eV	NIST
IE	8.52 ± 0.01	eV	NIST
IE	8.44	eV	NIST
IE	Outlier 8.80 ± 0.05	eV	NIST
IE	8.37 ± 0.02	eV	NIST
IE	8.52	eV	NIST
IE	8.45	eV	NIST
IE	8.44 ± 0.02	eV	NIST
IE	8.45 ± 0.01	eV	NIST
IE	8.48	eV	NIST
IE	8.44	eV	NIST
IE	8.43	eV	NIST
IE	8.60 ± 0.03	eV	NIST
log₁₀WS	[-2.77; -2.77]
log₁₀WS	-2.77		Aq. Solubility Prediction
log₁₀WS	-2.77		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; 3617.50]	kPa
P_c	3511.00	kPa	KDB
P_c	3510.00 ± 20.00	kPa	NIST
P_c	3510.70 ± 5.00	kPa	NIST
P_c	3617.50 ± 100.00	kPa	NIST
P_c	3511.00 ± 0.01	kPa	NIST
P_c	3343.73 ± 151.99	kPa	NIST
P_c	3430.00 ± 7.84	kPa	NIST
ρ_c	[280.70; 282.51]	kg/m³
ρ_c	281.34 ± 2.12	kg/m³	NIST
ρ_c	282.51 ± 5.31	kg/m³	NIST
ρ_c	280.70 ± 4.25	kg/m³	NIST
I_np	[120.40; 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	883.20		NIST
I_np	888.10		NIST
I_np	874.28		NIST
I_np	847.60		NIST
I_np	850.20		NIST
I_np	852.70		NIST
I_np	855.30		NIST
I_np	857.80		NIST
I_np	860.90		NIST
I_np	863.50		NIST
I_np	857.70		NIST
I_np	867.50		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	857.10		NIST
I_np	857.00		NIST
I_np	857.40		NIST
I_np	857.60		NIST
I_np	856.90		NIST
I_np	863.00		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	866.80		NIST
I_np	871.30		NIST
I_np	866.70		NIST
I_np	866.00		NIST
I_np	866.00		NIST
I_np	854.20		NIST
I_np	859.00		NIST
I_np	849.10		NIST
I_np	854.00		NIST
I_np	866.00		NIST
I_np	856.00		NIST
I_np	879.00		NIST
I_np	881.00		NIST
I_np	848.00		NIST
I_np	853.10		NIST
I_np	871.00		NIST
I_np	890.00		NIST
I_np	866.00		NIST
I_np	866.00		NIST
I_np	866.00		NIST
I_np	866.00		NIST
I_np	862.00		NIST
I_np	886.00		NIST
I_np	865.00		NIST
I_np	848.00		NIST
I_np	863.00		NIST
I_np	880.00		NIST
I_np	866.00		NIST
I_np	868.00		NIST
I_np	866.00		NIST
I_np	868.00		NIST
I_np	863.00		NIST
I_np	862.00		NIST
I_np	859.00		NIST
I_np	857.10		NIST
I_np	857.60		NIST
I_np	860.80		NIST
I_np	868.00		NIST
I_np	876.00		NIST
I_np	864.00		NIST
I_np	868.00		NIST
I_np	872.00		NIST
I_np	878.00		NIST
I_np	859.00		NIST
I_np	861.20		NIST
I_np	867.70		NIST
I_np	872.50		NIST
I_np	878.30		NIST
I_np	860.00		NIST
I_np	860.30		NIST
I_np	854.20		NIST
I_np	858.00		NIST
I_np	848.30		NIST
I_np	853.40		NIST
I_np	858.40		NIST
I_np	858.60		NIST
I_np	859.00		NIST
I_np	859.30		NIST
I_np	854.10		NIST
I_np	854.60		NIST
I_np	859.00		NIST
I_np	861.00		NIST
I_np	859.00		NIST
I_np	861.20		NIST
I_np	865.00		NIST
I_np	861.00		NIST
I_np	861.00		NIST
I_np	855.73		NIST
I_np	882.00		NIST
I_np	886.00		NIST
I_np	868.00		NIST
I_np	849.00		NIST
I_np	854.00		NIST
I_np	857.80		NIST
I_np	861.80		NIST
I_np	863.00		NIST
I_np	867.00		NIST
I_np	868.00		NIST
I_np	872.00		NIST
I_np	875.00		NIST
I_np	850.00		NIST
I_np	908.00		NIST
I_np	858.10		NIST
I_np	861.00		NIST
I_np	865.50		NIST
I_np	864.90		NIST
I_np	858.10		NIST
I_np	894.00		NIST
I_np	884.00		NIST
I_np	850.00		NIST
I_np	855.00		NIST
I_np	860.00		NIST
I_np	894.00		NIST
I_np	901.00		NIST
I_np	907.00		NIST
I_np	888.00		NIST
I_np	862.00		NIST
I_np	870.00		NIST
I_np	863.00		NIST
I_np	860.00		NIST
I_np	861.00		NIST
I_np	853.00		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	885.00		NIST
I_np	866.00		NIST
I_np	859.00		NIST
I_np	889.20		NIST
I_np	864.00		NIST
I_np	877.00		NIST
I_np	874.00		NIST
I_np	864.00		NIST
I_np	878.00		NIST
I_np	862.00		NIST
I_np	884.00		NIST
I_np	855.00		NIST
I_np	860.40		NIST
I_np	872.00		NIST
I_np	847.00		NIST
I_np	884.00		NIST
I_np	861.70		NIST
I_np	864.40		NIST
I_np	866.50		NIST
I_np	849.30		NIST
I_np	877.80		NIST
I_np	869.00		NIST
I_np	884.00		NIST
I_np	866.00		NIST
I_np	852.00		NIST
I_np	856.30		NIST
I_np	865.00		NIST
I_np	873.00		NIST
I_np	845.70		NIST
I_np	851.30		NIST
I_np	855.50		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	853.96		NIST
I_np	854.41		NIST
I_np	865.00		NIST
I_np	855.00		NIST
I_np	854.75		NIST
I_np	854.85		NIST
I_np	855.00		NIST
I_np	863.00		NIST
I_np	855.12		NIST
I_np	859.70		NIST
I_np	856.00		NIST
I_np	854.30		NIST
I_np	861.80		NIST
I_np	853.70		NIST
I_np	859.80		NIST
I_np	864.70		NIST
I_np	855.90		NIST
I_np	860.80		NIST
I_np	866.94		NIST
I_np	842.00		NIST
I_np	851.35		NIST
I_np	854.04		NIST
I_np	855.80		NIST
I_np	865.82		NIST
I_np	868.78		NIST
I_np	870.79		NIST
I_np	867.00		NIST
I_np	871.00		NIST
I_np	862.00		NIST
I_np	863.00		NIST
I_np	865.00		NIST
I_np	864.00		NIST
I_np	853.00		NIST
I_np	870.00		NIST
I_np	875.00		NIST
I_np	863.00		NIST
I_np	888.00		NIST
I_np	872.00		NIST
I_np	879.49		NIST
I_np	854.00		NIST
I_np	875.00		NIST
I_np	872.00		NIST
I_np	856.00		NIST
I_np	861.00		NIST
I_np	868.00		NIST
I_np	866.00		NIST
I_np	868.00		NIST
I_np	870.00		NIST
I_np	872.00		NIST
I_np	852.00		NIST
I_np	860.00		NIST
I_np	845.00		NIST
I_np	853.00		NIST
I_np	854.00		NIST
I_np	857.00		NIST
I_np	870.00		NIST
I_np	864.00		NIST
I_np	850.00		NIST
I_np	865.00		NIST
I_np	890.00		NIST
I_np	874.00		NIST
I_np	870.00		NIST
I_np	862.00		NIST
I_np	865.00		NIST
I_np	858.00		NIST
I_np	868.00		NIST
I_np	867.00		NIST
I_np	872.00		NIST
I_np	861.00		NIST
I_np	899.00		NIST
I_np	856.00		NIST
I_np	874.00		NIST
I_np	876.00		NIST
I_np	853.00		NIST
I_np	854.00		NIST
I_np	853.00		NIST
I_np	853.00		NIST
I_np	884.00		NIST
I_np	856.00		NIST
I_np	870.00		NIST
I_np	884.00		NIST
I_np	868.00		NIST
I_np	849.00		NIST
I_np	848.00		NIST
I_np	864.00		NIST
I_np	875.00		NIST
I_np	884.00		NIST
I_np	872.00		NIST
I_np	883.00		NIST
I_np	864.00		NIST
I_np	857.41		NIST
I_np	868.00		NIST
I_np	872.00		NIST
I_np	860.00		NIST
I_np	857.00		NIST
I_np	865.00		NIST
I_np	875.80		NIST
I_np	865.00		NIST
I_np	854.00		NIST
I_np	859.00		NIST
I_np	860.00		NIST
I_np	849.00		NIST
I_np	852.00		NIST
I_np	851.00		NIST
I_np	848.00		NIST
I_np	859.00		NIST
I_np	853.00		NIST
I_np	853.00		NIST
I_np	853.80		NIST
I_np	847.70		NIST
I_np	854.00		NIST
I_np	855.10		NIST
I_np	854.90		NIST
I_np	866.00		NIST
I_np	860.00		NIST
I_np	861.00		NIST
I_np	849.30		NIST
I_np	851.50		NIST
I_np	854.70		NIST
I_np	857.10		NIST
I_np	859.10		NIST
I_np	848.00		NIST
I_np	851.00		NIST
I_np	854.00		NIST
I_np	856.00		NIST
I_np	858.00		NIST
I_np	851.00		NIST
I_np	852.00		NIST
I_np	854.00		NIST
I_np	832.00		NIST
I_np	862.00		NIST
I_np	881.00		NIST
I_np	875.00		NIST
I_np	875.00		NIST
I_np	875.00		NIST
I_np	889.00		NIST
I_np	870.00		NIST
I_np	868.00		NIST
I_np	872.00		NIST
I_np	864.00		NIST
I_np	866.00		NIST
I_np	864.00		NIST
I_np	875.00		NIST
I_np	875.00		NIST
I_np	860.00		NIST
I_np	864.00		NIST
I_np	861.00		NIST
I_np	888.00		NIST
I_np	848.46		NIST
I_np	867.00		NIST
I_np	857.00		NIST
I_np	878.00		NIST
I_np	864.00		NIST
I_np	844.00		NIST
I_np	863.00		NIST
I_np	870.00		NIST
I_np	863.00		NIST
I_np	904.00		NIST
I_np	873.00		NIST
I_np	875.00		NIST
I_np	861.00		NIST
I_np	867.00		NIST
I_np	855.00		NIST
I_np	866.00		NIST
I_np	863.00		NIST
I_np	855.00		NIST
I_np	870.00		NIST
I_np	870.00		NIST
I_np	865.60		NIST
I_np	871.80		NIST
I_np	871.30		NIST
I_np	870.70		NIST
I_np	861.90		NIST
I_np	868.00		NIST
I_np	853.00		NIST
I_np	855.00		NIST
I_np	846.00		NIST
I_np	853.00		NIST
I_np	860.00		NIST
I_np	876.00		NIST
I_np	858.00		NIST
I_np	860.00		NIST
I_np	874.00		NIST
I_np	864.00		NIST
I_np	Outlier 120.40		NIST
I_np	Outlier 120.40		NIST
I_np	Outlier 121.20		NIST
I_np	Outlier 136.39		NIST
I_np	862.00		NIST
I_np	872.00		NIST
I_np	876.00		NIST
I_np	884.00		NIST
I_np	849.00		NIST
I_np	865.00		NIST
I_np	852.00		NIST
I_np	853.00		NIST
I_np	854.90		NIST
I_np	851.50		NIST
I_np	851.00		NIST
I_np	863.00		NIST
I_np	861.00		NIST
I_np	885.00		NIST
I_np	868.00		NIST
I_np	845.00		NIST
I_np	864.00		NIST
I_np	870.00		NIST
I_np	877.00		NIST
I_np	877.80		NIST
I_np	856.30		NIST
I_np	855.50		NIST
I_np	866.50		NIST
I_np	854.75		NIST
I_np	859.70		NIST
I_np	859.80		NIST
I_np	842.00		NIST
I_np	868.78		NIST
I_np	889.00		NIST
I_np	866.00		NIST
I_np	857.00		NIST
I_np	855.00		NIST
I_np	871.30		NIST
I_np	858.00		NIST
I_np	879.49		NIST
I_np	Outlier 120.40		NIST
I	[1101.00; 1189.00]
I	1169.50		NIST
I	Outlier 1180.40		NIST
I	1123.00		NIST
I	1123.00		NIST
I	1145.00		NIST
I	1159.94		NIST
I	1165.00		NIST
I	1169.77		NIST
I	1145.24		NIST
I	1149.89		NIST
I	1152.22		NIST
I	1138.90		NIST
I	1143.00		NIST
I	1169.20		NIST
I	1134.80		NIST
I	1118.60		NIST
I	Outlier 1189.00		NIST
I	Outlier 1182.00		NIST
I	1163.00		NIST
I	1170.00		NIST
I	Outlier 1178.00		NIST
I	1156.00		NIST
I	1136.00		NIST
I	1142.00		NIST
I	Outlier 1180.00		NIST
I	1129.00		NIST
I	1134.00		NIST
I	1142.00		NIST
I	1154.20		NIST
I	1117.00		NIST
I	1137.00		NIST
I	1137.00		NIST
I	1117.00		NIST
I	1164.00		NIST
I	1139.00		NIST
I	1123.00		NIST
I	1123.00		NIST
I	1137.00		NIST
I	1125.00		NIST
I	1136.00		NIST
I	1130.00		NIST
I	1130.00		NIST
I	1156.00		NIST
I	1134.00		NIST
I	1136.00		NIST
I	1132.00		NIST
I	1135.00		NIST
I	1140.00		NIST
I	1119.00		NIST
I	1136.00		NIST
I	1119.00		NIST
I	1119.00		NIST
I	1137.00		NIST
I	1140.00		NIST
I	1126.00		NIST
I	1129.00		NIST
I	1156.50		NIST
I	1141.30		NIST
I	1150.60		NIST
I	1117.00		NIST
I	1153.20		NIST
I	1143.40		NIST
I	1146.00		NIST
I	1143.90		NIST
I	1148.70		NIST
I	1130.00		NIST
I	1127.00		NIST
I	1129.00		NIST
I	1130.00		NIST
I	1130.00		NIST
I	1125.00		NIST
I	1120.00		NIST
I	1152.00		NIST
I	1137.00		NIST
I	1140.00		NIST
I	1140.00		NIST
I	1165.00		NIST
I	Outlier 1176.00		NIST
I	1142.00		NIST
I	1153.00		NIST
I	1155.00		NIST
I	1150.00		NIST
I	1154.00		NIST
I	1168.00		NIST
I	Outlier 1178.00		NIST
I	1132.00		NIST
I	1141.00		NIST
I	1119.00		NIST
I	1136.00		NIST
I	Outlier 1101.00		NIST
I	1154.00		NIST
I	1114.00		NIST
I	1137.00		NIST
I	1149.00		NIST
I	1111.00		NIST
I	1140.00		NIST
I	1113.00		NIST
I	1149.00		NIST
I	1129.00		NIST
I	1129.00		NIST
I	1133.00		NIST
I	1129.00		NIST
I	1164.00		NIST
I	1146.00		NIST
I	1142.00		NIST
I	1131.00		NIST
I	1138.00		NIST
I	1133.00		NIST
I	1132.00		NIST
I	1115.00		NIST
I	1132.00		NIST
I	1132.00		NIST
I	1140.00		NIST
I	1153.00		NIST
I	1164.00		NIST
I	1138.00		NIST
I	1142.00		NIST
I	1173.00		NIST
I	1137.00		NIST
I	1127.00		NIST
I	1129.00		NIST
I	1120.00		NIST
I	1120.00		NIST
I	1142.00		NIST
I	1123.00		NIST
I	1140.00		NIST
I	1139.00		NIST
I	1137.00		NIST
I	1119.00		NIST
I	1145.00		NIST
I	1155.00		NIST
I	1139.00		NIST
I	1132.00		NIST
I	1138.00		NIST
I	1155.00		NIST
I	1110.00		NIST
I	1126.00		NIST
I	1140.00		NIST
I	1140.00		NIST
I	1150.00		NIST
I	1136.00		NIST
I	1169.50		NIST
I	1159.94		NIST
I	1152.22		NIST
I	1118.60		NIST
I	Outlier 1178.00		NIST
I	1165.00		NIST
I	1150.00		NIST
I	1141.00		NIST
S°_liquid	[243.51; 253.10]	J/mol×K
S°_liquid	247.15	J/mol×K	NIST
S°_liquid	243.51	J/mol×K	NIST
S°_liquid	253.10	J/mol×K	NIST
T_boil	[409.00; 412.70]	K
T_boil	411.40	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	411.45	K	Separation of azeotrope (2,2,3,3-tetrafluoro-1-propanol + water): Isobaric vapour-liquid phase equilibrium measurements and azeotropic distillation
T_boil	411.45	K	Vapour-liquid equilibrium measurements and extractive distillation process design for separation of azeotropic mixture (dimethyl carbonate + ethanol)
T_boil	411.21	K	Investigation on Thermodynamics in Separation for Ethylene Glycol + Neopentyl Glycol System by Azeotropic Distillation
T_boil	411.49	K	Isobaric Vapor-Liquid Equilibrium Measurements for Separation of Azeotrope (Methanol + Methyl Acetate)
T_boil	411.23	K	Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures of Ethanol, Methylcyclohexane and p-Xylene
T_boil	411.37	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	411.52	K	KDB
T_boil	411.15 ± 0.20	K	NIST
T_boil	411.35 ± 0.20	K	NIST
T_boil	411.50	K	NIST
T_boil	411.35 ± 0.20	K	NIST
T_boil	410.65 ± 0.50	K	NIST
T_boil	411.55 ± 0.30	K	NIST
T_boil	410.65 ± 0.40	K	NIST
T_boil	411.50	K	NIST
T_boil	411.45 ± 0.20	K	NIST
T_boil	411.45 ± 0.20	K	NIST
T_boil	411.60 ± 0.30	K	NIST
T_boil	411.35 ± 0.15	K	NIST
T_boil	411.36 ± 0.30	K	NIST
T_boil	411.52 ± 0.20	K	NIST
T_boil	411.60 ± 0.20	K	NIST
T_boil	411.53 ± 0.15	K	NIST
T_boil	411.60 ± 0.10	K	NIST
T_boil	411.69 ± 0.01	K	NIST
T_boil	411.30 ± 0.80	K	NIST
T_boil	411.50 ± 0.30	K	NIST
T_boil	411.50 ± 0.30	K	NIST
T_boil	Outlier 409.00 ± 1.50	K	NIST
T_boil	412.00 ± 3.00	K	NIST
T_boil	Outlier 412.70 ± 2.00	K	NIST
T_boil	411.00 ± 2.00	K	NIST
T_boil	Outlier 409.90 ± 2.00	K	NIST
T_boil	411.20 ± 0.50	K	NIST
T_boil	411.50 ± 0.20	K	NIST
T_boil	411.60 ± 0.50	K	NIST
T_boil	411.50 ± 0.02	K	NIST
T_boil	411.00 ± 0.50	K	NIST
T_boil	411.00 ± 2.00	K	NIST
T_boil	411.55 ± 0.30	K	NIST
T_boil	411.50 ± 0.20	K	NIST
T_boil	411.50 ± 0.20	K	NIST
T_boil	411.49 ± 0.01	K	NIST
T_boil	412.01 ± 0.20	K	NIST
T_boil	411.20 ± 0.50	K	NIST
T_boil	411.55 ± 1.00	K	NIST
T_boil	411.50 ± 0.20	K	NIST
T_boil	411.15 ± 0.50	K	NIST
T_boil	411.50 ± 0.05	K	NIST
T_boil	411.50 ± 0.02	K	NIST
T_boil	411.70 ± 0.30	K	NIST
T_boil	411.70 ± 0.50	K	NIST
T_boil	411.65 ± 0.10	K	NIST
T_boil	411.50 ± 0.10	K	NIST
T_boil	411.59 ± 0.20	K	NIST
T_boil	411.47 ± 0.30	K	NIST
T_boil	411.55 ± 0.50	K	NIST
T_boil	411.30 ± 0.40	K	NIST
T_boil	411.60 ± 0.40	K	NIST
T_boil	411.55 ± 0.20	K	NIST
T_boil	411.55 ± 0.30	K	NIST
T_boil	411.55 ± 0.30	K	NIST
T_boil	Outlier 410.00 ± 5.00	K	NIST
T_boil	Outlier 410.15 ± 2.00	K	NIST
T_boil	411.50 ± 0.25	K	NIST
T_boil	Outlier 409.00 ± 3.00	K	NIST
T_boil	411.55 ± 0.30	K	NIST
T_boil	411.00 ± 3.00	K	NIST
T_boil	411.00 ± 2.00	K	NIST
T_boil	410.65 ± 0.50	K	NIST
T_boil	411.00 ± 2.00	K	NIST
T_boil	411.30 ± 1.50	K	NIST
T_c	[615.90; 621.70]	K
T_c	616.20	K	KDB
T_c	616.20 ± 0.20	K	NIST
T_c	616.23 ± 0.10	K	NIST
T_c	616.20	K	NIST
T_c	618.20 ± 2.00	K	NIST
T_c	616.20 ± 0.61	K	NIST
T_c	616.20 ± 0.15	K	NIST
T_c	619.00 ± 3.00	K	NIST
T_c	617.45 ± 2.00	K	NIST
T_c	615.90 ± 0.50	K	NIST
T_c	618.20 ± 2.00	K	NIST
T_c	Outlier 621.70 ± 6.00	K	NIST
T_c	617.60 ± 1.50	K	NIST
T_fus	[260.15; 288.00]	K
T_fus	286.30	K	KDB
T_fus	285.90	K	Aq. Solubility Prediction
T_fus	286.36 ± 0.05	K	NIST
T_fus	286.45 ± 0.15	K	NIST
T_fus	286.41 ± 0.03	K	NIST
T_fus	286.38 ± 0.10	K	NIST
T_fus	286.20 ± 2.00	K	NIST
T_fus	286.20 ± 2.00	K	NIST
T_fus	286.53 ± 0.20	K	NIST
T_fus	286.38 ± 0.30	K	NIST
T_fus	287.00 ± 3.00	K	NIST
T_fus	286.30 ± 0.50	K	NIST
T_fus	286.45 ± 0.20	K	NIST
T_fus	286.37 ± 0.01	K	NIST
T_fus	286.43 ± 0.10	K	NIST
T_fus	286.36 ± 0.05	K	NIST
T_fus	286.22 ± 0.15	K	NIST
T_fus	288.00 ± 2.00	K	NIST
T_fus	Outlier 260.15 ± 2.00	K	NIST
T_fus	286.10 ± 0.60	K	NIST
T_fus	286.40 ± 0.40	K	NIST
T_fus	286.35 ± 0.40	K	NIST
T_fus	286.50 ± 0.20	K	NIST
T_fus	286.40 ± 0.50	K	NIST
T_triple	[286.30; 286.40]	K
T_triple	286.40 ± 0.01	K	NIST
T_triple	286.30 ± 0.30	K	NIST
T_triple	286.40 ± 0.01	K	NIST
T_triple	286.30 ± 0.30	K	NIST
V_c	[0.378; 0.378]	m³/kmol
V_c	0.378	m³/kmol	KDB
V_c	0.378	m³/kmol	NIST
Z_c	0.2590380		KDB
Z_ra	0.26		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[163.20; 211.09]	J/mol×K	[393.00; 523.15]

C_p,gas	163.20 ± 1.70	J/mol×K	393.00	NIST
C_p,gas	166.52 ± 0.33	J/mol×K	398.15	NIST
C_p,gas	175.82 ± 0.35	J/mol×K	423.15	NIST
C_p,gas	178.20 ± 1.70	J/mol×K	428.00	NIST
C_p,gas	185.40 ± 0.37	J/mol×K	448.15	NIST
C_p,gas	189.10 ± 1.70	J/mol×K	463.00	NIST
C_p,gas	194.17 ± 0.39	J/mol×K	473.15	NIST
C_p,gas	202.92 ± 0.41	J/mol×K	498.15	NIST
C_p,gas	211.09 ± 0.42	J/mol×K	523.15	NIST
C_p,liquid	[176.60; 198.70]	J/mol×K	[288.15; 336.00]

C_p,liquid	178.86	J/mol×K	288.15	Isobaric molar heat capacities of the ternary system dimethyl carbonate + p-xylene + n-decane
C_p,liquid	184.90	J/mol×K	298.00	NIST
C_p,liquid	181.60	J/mol×K	298.00	NIST
C_p,liquid	183.65	J/mol×K	298.15	NIST
C_p,liquid	182.22	J/mol×K	298.15	NIST
C_p,liquid	181.94	J/mol×K	298.15	NIST
C_p,liquid	181.90	J/mol×K	298.15	NIST
C_p,liquid	181.79	J/mol×K	298.15	NIST
C_p,liquid	181.55	J/mol×K	298.15	NIST
C_p,liquid	181.70	J/mol×K	298.15	NIST
C_p,liquid	182.56	J/mol×K	298.15	Isobaric molar heat capacities of the ternary system dimethyl carbonate + p-xylene + n-decane
C_p,liquid	183.76	J/mol×K	298.15	NIST
C_p,liquid	180.30	J/mol×K	299.00	NIST
C_p,liquid	176.60	J/mol×K	303.00	NIST
C_p,liquid	186.15	J/mol×K	308.15	Isobaric molar heat capacities of the ternary system dimethyl carbonate + p-xylene + n-decane
C_p,liquid	198.70	J/mol×K	336.00	NIST
η	[0.0003382; 0.0007010]	Pa×s	[288.15; 353.15]

η	0.0007010	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	0.0006500	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	0.0006078	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	0.0006090	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	0.0006120	Pa×s	298.15	Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
η	0.0006110	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	0.0006162	Pa×s	298.15	Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
η	0.0006110	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	0.0006130	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	0.0005660	Pa×s	303.15	Viscosity, Density, and Refractive Index of Some (Ester + Hydrocarbon) Binary Mixtures at 303.15 K and 313.15 K
η	0.0005660	Pa×s	303.15	Thermophysical Properties of Isoamyl Acetate or Methyl Benzoate + Hydrocarbon Binary Mixtures, at (303.15 and 313.15) K
η	0.0005715	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	0.0005730	Pa×s	303.15	Volumetric and Viscometric Behavior of the Binary System: (Hexan-1-ol + p-Xylene)
η	0.0005760	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	0.0005740	Pa×s	303.15	Viscometric Studies of Molecular Interactions in Binary Liquid Mixtures of Isomeric Xylenes with Methanol
η	0.0005726	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	0.0005715	Pa×s	303.15	Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
η	0.0005756	Pa×s	303.15	Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
η	0.0005374	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	0.0005420	Pa×s	308.15	Viscometric Studies of Molecular Interactions in Binary Liquid Mixtures of Isomeric Xylenes with Methanol
η	0.0005501	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	0.0005410	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	0.0005410	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	0.0005400	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	0.0005178	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	0.0005080	Pa×s	313.15	Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
η	0.0005170	Pa×s	313.15	Thermophysical Properties of Isoamyl Acetate or Methyl Benzoate + Hydrocarbon Binary Mixtures, at (303.15 and 313.15) K
η	0.0005140	Pa×s	313.15	Viscometric Studies of Molecular Interactions in Binary Liquid Mixtures of Isomeric Xylenes with Methanol
η	0.0005170	Pa×s	313.15	Viscosity, Density, and Refractive Index of Some (Ester + Hydrocarbon) Binary Mixtures at 303.15 K and 313.15 K
η	0.0005120	Pa×s	313.15	Volumetric and Viscometric Behavior of the Binary System: (Hexan-1-ol + p-Xylene)
η	0.0005140	Pa×s	313.15	Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
η	0.0004860	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	0.0004840	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	0.0004860	Pa×s	318.15	Viscometric Studies of Molecular Interactions in Binary Liquid Mixtures of Isomeric Xylenes with Methanol
η	0.0004912	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	0.0004882	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	0.0004610	Pa×s	323.15	Volumetric and Viscometric Behavior of the Binary System: (Hexan-1-ol + p-Xylene)
η	0.0004641	Pa×s	323.15	Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
η	0.0004599	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	0.0004610	Pa×s	323.15	Viscometric Studies of Molecular Interactions in Binary Liquid Mixtures of Isomeric Xylenes with Methanol
η	0.0004599	Pa×s	323.15	Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
η	0.0004595	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	0.0004439	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	0.0004189	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	0.0004298	Pa×s	333.15	Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
η	0.0004171	Pa×s	333.15	Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
η	0.0003783	Pa×s	343.15	Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
η	0.0003809	Pa×s	343.15	Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
η	0.0003382	Pa×s	353.15	Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
η	0.0003487	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	[16.93; 17.12]	kJ/mol	[286.30; 286.40]

Δ_fusH	17.10	kJ/mol	286.30	NIST
Δ_fusH	17.11	kJ/mol	286.30	NIST
Δ_fusH	17.11	kJ/mol	286.30	NIST
Δ_fusH	16.93	kJ/mol	286.30	NIST
Δ_fusH	16.93	kJ/mol	286.30	NIST
Δ_fusH	17.11	kJ/mol	286.39	NIST
Δ_fusH	17.12	kJ/mol	286.40	NIST
Δ_fusH	17.12	kJ/mol	286.40	NIST
Δ_subH	[59.40; 60.80]	kJ/mol	[266.50; 286.00]
Δ_subH	59.40	kJ/mol	266.50	NIST
Δ_subH	60.80	kJ/mol	286.00	NIST
Δ_vapH	[24.70; 42.57]	kJ/mol	[298.00; 583.50]

Δ_vapH	42.57	kJ/mol	298.00	Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
Δ_vapH	41.60	kJ/mol	323.00	NIST
Δ_vapH	40.30	kJ/mol	353.00	NIST
Δ_vapH	42.40	kJ/mol	369.50	NIST
Δ_vapH	40.10	kJ/mol	372.50	NIST
Δ_vapH	37.30	kJ/mol	395.00	NIST
Δ_vapH	36.00 ± 0.10	kJ/mol	411.00	NIST
Δ_vapH	35.98	kJ/mol	411.40	KDB
Δ_vapH	35.67	kJ/mol	411.50	NIST
Δ_vapH	34.50 ± 0.10	kJ/mol	436.00	NIST
Δ_vapH	37.30	kJ/mol	437.00	NIST
Δ_vapH	30.50 ± 0.10	kJ/mol	484.00	NIST
Δ_vapH	36.10	kJ/mol	506.50	NIST
Δ_vapH	24.70 ± 0.10	kJ/mol	540.00	NIST
Δ_vapH	36.20	kJ/mol	583.50	NIST
P_vap	[1.12; 250.04]	kPa	[298.15; 449.60]

P_vap	1.12	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	1.56	kPa	303.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	2.49	kPa	313.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	4.42	kPa	323.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	7.00	kPa	333.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	6.85	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	10.50	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	10.63	kPa	343.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	11.39	kPa	345.15	Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
P_vap	13.90	kPa	350.15	Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
P_vap	15.72	kPa	353.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	15.61	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	16.85	kPa	355.15	Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
P_vap	19.04	kPa	358.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	20.30	kPa	360.15	Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
P_vap	22.80	kPa	363.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	24.30	kPa	365.15	Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
P_vap	32.04	kPa	373.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	40.00	kPa	379.85	Isobaric Vapor Liquid Equilibria for Binary Systems Comprising 1-Chloro-2-ethylhexane, 2-Ethyl-1-hexanol, p-Xylene, and N-Methylpyrrolidone (NMP) at 40.0 kPa
P_vap	44.56	kPa	383.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	60.79	kPa	393.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	80.87	kPa	403.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	92.43	kPa	408.15	Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
P_vap	93.13	kPa	408.37	Refractive Index and Vapor-Liquid Equilibrium Data for the Binary Systems of Anisole with Xylene Isomers at 93.13 kPa
P_vap	97.30	kPa	410.00	Isobaric Vapor-Liquid Equilibria at 97.3 kPa and Excess Properties at (303.15, 308.15, and 313.15) K of Binary Mixture of p-Xylene + Decane
P_vap	97.30	kPa	410.00	Vapor-Liquid Equilibria and Excess Properties of the Binary System Vinyl Acetate + p-Xylene
P_vap	100.04	kPa	410.78	Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
P_vap	101.30	kPa	411.21	Investigation on Thermodynamics in Separation for Ethylene Glycol + Neopentyl Glycol System by Azeotropic Distillation
P_vap	101.30	kPa	411.40	Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
P_vap	101.30	kPa	411.45	Separation of azeotrope (2,2,3,3-tetrafluoro-1-propanol + water): Isobaric vapour-liquid phase equilibrium measurements and azeotropic distillation
P_vap	101.30	kPa	411.45	Vapour-liquid equilibrium measurements and extractive distillation process design for separation of azeotropic mixture (dimethyl carbonate + ethanol)
P_vap	105.00	kPa	412.63	Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
P_vap	124.93	kPa	419.48	Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
P_vap	174.88	kPa	433.57	Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
P_vap	199.86	kPa	439.37	Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
P_vap	224.86	kPa	444.66	Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
P_vap	250.04	kPa	449.56	Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
P_vap	250.00	kPa	449.60	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	[1.48300; 1.50040]		[288.15; 318.15]

n₀	1.49830		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	1.49850		288.15	Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n₀	1.49850		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	1.49577		293.10	Volumetric properties of (cyclohexanone + a xylene) at temperature between (293.15 and 353.15) K
n₀	1.48580		293.15	Excess Gibbs' energies of the binary mixtures formed by N,N-dimethylformamide with xylenes and cresols at 95.1 kPa
n₀	1.49590		293.15	Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n₀	1.48580		293.15	Bubble points of some binary mixtures formed by o-cresol at 95.75 kPa
n₀	1.49590		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	1.49577		293.15	Densities and volumetric properties of a (xylene + dimethyl sulfoxide) at temperature from (293.15 to 353.15) K
n₀	1.49577		293.15	A study of densities and volumetric properties of binary mixtures containing nitrobenzene at T = (293.15 to 353.15) K
n₀	1.50040		293.15	Solubilities of Methyldiphenylphosphine Oxide in Selected Solvents
n₀	1.49220		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	1.48580		293.15	Activity coefficients and excess Gibbs free energy of some binary mixtures formed by p-cresol at 95.23 kPa
n₀	1.49580		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	1.49260		298.15	Excess and deviation properties for the binary mixtures of methylcyclohexane with benzene, toluene, p-xylene, mesitylene, and anisole at T = (298.15, 303.15, and 308.15) K
n₀	1.49300		298.15	Isobaric Vapor-Liquid Equilibria for the Binary Mixtures of Styrene with Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene
n₀	1.49290		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	1.49325		298.15	KDB
n₀	1.49580		298.15	Densities and volumetric properties of binary mixtures of xylene with N,N-dimethylformamide at different temperatures
n₀	1.49580		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	1.49312		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	1.49298		298.15	Effect of Temperature on the Change of Refractive Index on Mixing for Butyl Acetate + Aromatic Hydrocarbons
n₀	1.49250		298.15	Liquid-liquid equilibria for mixtures of (Furfural + an Aromatic hydrocarbon + an alkane) at T=298.15 K
n₀	1.49330		298.15	Bubble temperature measurements on the binary mixtures formed by decane with a variety of compounds at 95.8 kPa
n₀	1.49290		298.15	Densities, Excess Molar Volumes, Viscosity, and Refractive Indices of Binary Mixtures of Ethanoic Acid and Trichloroethylene with Dimethylbenzenes at Different Temperatures
n₀	1.49321		298.15	Effect of an Ionic Liquid (IL) Cation on the Ternary System (IL + p-Xylene + Hexane) at T= 298.15 K
n₀	1.49330		298.15	(Vapor + liquid) equilibria of binary mixtures formed by iso-octane with a variety of compounds at 95.8 kPa
n₀	1.49321		298.15	Separation of aromatic hydrocarbons from alkanes using ammonium ionic liquid C2NTf2 at T = 298.15K
n₀	1.49330		298.15	Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n₀	1.49325		298.15	Isobaric Vapor Liquid Equilibria of 1-Butanol p-Xylene System1
n₀	1.49330		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	1.49070		303.15	Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n₀	1.49070		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	1.48930		303.15	Excess and deviation properties for the binary mixtures of methylcyclohexane with benzene, toluene, p-xylene, mesitylene, and anisole at T = (298.15, 303.15, and 308.15) K
n₀	1.49150		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	1.48790		308.15	Topological and thermodynamic investigations of molecular interactions in binary mixtures: Molar excess volumes and molar excess enthalpies
n₀	1.48810		308.15	Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n₀	1.48810		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	1.48670		308.15	Excess and deviation properties for the binary mixtures of methylcyclohexane with benzene, toluene, p-xylene, mesitylene, and anisole at T = (298.15, 303.15, and 308.15) K
n₀	1.48550		313.15	Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n₀	1.48550		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	1.48444		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	1.48300		318.15	Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n₀	1.48300		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	[809.07; 865.52]	kg/m³	[288.15; 353.15]

ρ_l	865.52	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	865.31	kg/m³	288.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρ_l	865.30	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	861.00	kg/m³	293.00	KDB
ρ_l	861.20	kg/m³	293.10	Vapor-Liquid Equilibria Data for Binary Systems of Ethylbenzene + Xylene Isomers at 100.65 kPa
ρ_l	861.00	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	861.17	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	861.21	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	860.97	kg/m³	293.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρ_l	856.50	kg/m³	298.15	Isobaric vapor-liquid equilibrium of the binary system sec-butyl acetate + para-xylene and the quaternary system methyl acetate + para-xylene + sec-butyl acetate + acetic acid at 101.3 kPa
ρ_l	856.68	kg/m³	298.15	Ebulliometric Determination and Prediction of Vapor Liquid Equilibria for Binary Mixtures of Ethanol and Ethyl Hexanoate
ρ_l	856.71	kg/m³	298.15	Isobaric vapor-liquid equilibrium for n-undecane + p-, o-, m-xylene at 10 kPa
ρ_l	856.78	kg/m³	298.15	Liquid liquid equilibria in the ternary systems {hexadecane + BTX aromatics + 2-methoxyethanol or acetonitrile} at 298.15 K
ρ_l	856.51	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	856.71	kg/m³	298.15	Isobaric vapor-liquid equilibrium of binary systems of decane with p-, o-, m-xylene at 20 kPa
ρ_l	856.54	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	856.58	kg/m³	298.15	Thermodynamic Properties of Ternary Liquid Mixtures of 2-Pyrrolidinone with Aromatic Hydrocarbons
ρ_l	856.51	kg/m³	298.15	Surface Tension Deviations and Excess Molar Volumes on the Ternary System Propyl Propanoate + Hexane + p-Xylene at 298.15 K
ρ_l	858.63	kg/m³	298.15	Molar Excess Volumes and Excess Isentropic Compressibilities of {2-Methylaniline (i) + Benzene (j) + Methylbenzene}, {2-Methylaniline (i) + Benzene (j) + 1,2-Dimethylbenzene (k)}, and {2-Methylaniline (i) + Benzene (j) + 1,4-Dimethylbenzene (k)} at T = 308.15 K
ρ_l	856.58	kg/m³	298.15	Molar Excess Volumes and Excess Isentropic Compressibilities of Ternary Mixtures of o-Toluidine
ρ_l	856.54	kg/m³	298.15	Vapor Liquid Equilibrium for 2-Methyl-1-butanol + Ethylbenzene + Xylene Isomers at 101.33 kPa
ρ_l	856.65	kg/m³	298.15	Evaluation of the Performance of Four Solvents for the Liquid Liquid Extraction of Acrylic Acid from Water
ρ_l	856.82	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	856.67	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	856.63	kg/m³	298.15	Liquid Liquid Equilibria, Equilibrium Phase Densities, and Refractive Indices for the Quaternary Mixtures Containing 2-Propanol or 2-Methyl-2-Propanol of Fuel Oxygenate at T = 298.15 and 318.15 K
ρ_l	856.62	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	856.61	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	856.50	kg/m³	298.15	Determination and Correlation of Liquid-Liquid Equilibria Data for Water + Cyclohexanol + (Mesityl Oxide, Toluene, and p-Xylene) Ternary Systems at Different Temperatures
ρ_l	856.85	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	856.85	kg/m³	298.15	Excess Molar Volumes and Surface Tensions of Xylene with Acetone or 2-Butanone at 298.15 K
ρ_l	856.63	kg/m³	298.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρ_l	856.70	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	856.71	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	856.85	kg/m³	298.15	Excess Molar Volumes and Surface Tensions of Xylene with 2-propanol or 2-methyl-2-propanol at 298.15 K
ρ_l	856.70	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	852.27	kg/m³	303.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρ_l	852.47	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	852.28	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	847.91	kg/m³	308.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρ_l	848.12	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	847.88	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	847.97	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	843.58	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	843.53	kg/m³	313.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρ_l	843.77	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	839.42	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	839.14	kg/m³	318.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρ_l	839.21	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	834.74	kg/m³	323.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρ_l	834.92	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	830.39	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	830.32	kg/m³	328.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρ_l	826.27	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	825.88	kg/m³	333.15	Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρ_l	817.66	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	809.07	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	[59.14; 59.77]	J/mol×K	[286.30; 286.40]

Δ_fusS	59.73	J/mol×K	286.30	NIST
Δ_fusS	59.14	J/mol×K	286.30	NIST
Δ_fusS	59.14	J/mol×K	286.30	NIST
Δ_fusS	59.75	J/mol×K	286.39	NIST
Δ_fusS	59.77	J/mol×K	286.40	NIST
Δ_fusS	59.77	J/mol×K	286.40	NIST
c_sound,fluid	[1211.00; 1347.94]	m/s	[288.15; 323.15]

c_sound,fluid	1347.94	m/s	288.15	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1336.86	m/s	290.65	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1330.00	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	1326.13	m/s	293.15	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1328.40	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	1315.60	m/s	295.65	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1305.39	m/s	298.15	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1314.00	m/s	298.15	Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
c_sound,fluid	1308.00	m/s	298.15	Densities, Excess Molar Volumes at T = (298.15 to 313.15) K, Speeds of Sound, Excess Isentropic Compressibilities, Relative Permittivities and Deviations in Molar Polarizations at T = (298.15 and 308.15) K for Methyl Methacrylate + 2-Butoxyethanol or + Dibutyl Ether + Benzene, + Toluene and + p-Xylene
c_sound,fluid	1310.00	m/s	298.15	Isentropic Compressibilities Changes of Mixing of Tetrahydropyran and Aromatic Hydrocarbons Ternary Mixtures at 308.15 K
c_sound,fluid	1307.40	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	1295.34	m/s	300.65	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1287.30	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	1289.00	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	1285.42	m/s	303.15	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1275.64	m/s	305.65	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1272.00	m/s	308.15	Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
c_sound,fluid	1267.60	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	1266.13	m/s	308.15	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1276.00	m/s	308.15	Densities, Excess Molar Volumes at T = (298.15 to 313.15) K, Speeds of Sound, Excess Isentropic Compressibilities, Relative Permittivities and Deviations in Molar Polarizations at T = (298.15 and 308.15) K for Methyl Methacrylate + 2-Butoxyethanol or + Dibutyl Ether + Benzene, + Toluene and + p-Xylene
c_sound,fluid	1256.41	m/s	310.65	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1249.00	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	1246.85	m/s	313.15	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1248.30	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	1237.60	m/s	315.65	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1229.80	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	1228.14	m/s	318.15	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1220.47	m/s	320.65	Influence of temperature on thermodynamics of ethers + xylenes
c_sound,fluid	1211.00	m/s	323.15	Influence of temperature on thermodynamics of ethers + xylenes
γ	[0.03; 0.03]	N/m	[293.20; 308.15]

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	Surface tension, density, and speed of sound for the ternary mixture {diethyl carbonate + p-xylene + decane}
γ	0.03	N/m	298.15	Excess thermodynamic functions derived from densities and surface tensions of (p- or o-xylene + ethylene glycol dimethyl ether) between the temperatures (298.15 and 308.15) K
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	298.15	Analysis of Surface Tension, Density, and Speed of Sound for the Ternary Mixture Dimethyl Carbonate + p-Xylene + n-Octane
γ	0.03	N/m	303.15	Excess thermodynamic functions derived from densities and surface tensions of (p- or o-xylene + ethylene glycol dimethyl ether) between the temperatures (298.15 and 308.15) K
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	Excess thermodynamic functions derived from densities and surface tensions of (p- or o-xylene + ethylene glycol dimethyl ether) between the temperatures (298.15 and 308.15) K
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	308.15	Surface Tension of Dialkyl Carbonates + (Alkanes or 1,4-Dimethylbenzene) and 1,4-Dimethylbenzene + Alkanes Binary Mixtures at T = 308.15 K
λ	[0.12; 0.13]	W/m×K	[287.33; 329.16]

λ	0.13	W/m×K	287.33	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.13	W/m×K	287.55	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.13	W/m×K	287.73	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.13	W/m×K	294.03	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.13	W/m×K	294.27	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.13	W/m×K	294.44	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.12	W/m×K	311.71	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.12	W/m×K	311.94	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.12	W/m×K	312.11	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.12	W/m×K	328.75	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.12	W/m×K	328.99	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ	0.12	W/m×K	329.16	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
T_fus	286.45	K	100.00	Activity coefficient at infinite dilution, azeotropic data, excess enthalpies and solid liquid-equilibria for binary systems of alkanes and aromatics with esters

Viscosity, Pa*s

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

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

Refractive index (Na D-line)

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

Mass density, kg/m3

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

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

Speed of sound, m/s

Operational condition: Frequency, MHz = 5 (Liquid)

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

Correlations

Property	Value	Unit	Temperature (K)	Source
P_vap	[0.58; 202.65]	kPa	[286.41; 439.06]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.44593e+01
Coefficient B			-3.57809e+03
Coefficient C			-4.79200e+01
Temperature range, min.			286.41
Temperature range, max.			439.06

P_vap	0.58	kPa	286.41	Calculated Property
P_vap	1.57	kPa	303.37	Calculated Property
P_vap	3.76	kPa	320.33	Calculated Property
P_vap	8.12	kPa	337.29	Calculated Property
P_vap	16.10	kPa	354.25	Calculated Property
P_vap	29.72	kPa	371.22	Calculated Property
P_vap	51.60	kPa	388.18	Calculated Property
P_vap	85.01	kPa	405.14	Calculated Property
P_vap	133.86	kPa	422.10	Calculated Property
P_vap	202.65	kPa	439.06	Calculated Property
P_vap	[0.58; 3449.39]	kPa	[286.41; 616.26]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + Cln(T) + DT^2
Coefficient A			7.95572e+01
Coefficient B			-7.63795e+03
Coefficient C			-9.52735e+00
Coefficient D			5.74897e-06
Temperature range, min.			286.41
Temperature range, max.			616.26

P_vap	0.58	kPa	286.41	Calculated Property
P_vap	4.34	kPa	323.06	Calculated Property
P_vap	20.01	kPa	359.71	Calculated Property
P_vap	66.32	kPa	396.36	Calculated Property
P_vap	173.76	kPa	433.01	Calculated Property
P_vap	383.85	kPa	469.66	Calculated Property
P_vap	747.85	kPa	506.31	Calculated Property
P_vap	1327.08	kPa	542.96	Calculated Property
P_vap	2196.10	kPa	579.61	Calculated Property
P_vap	3449.39	kPa	616.26	Calculated Property

Similar Compounds

Find more compounds similar to p-Xylene.

Mixtures

Find more mixtures with p-Xylene.

Sources

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.
Outlier This icon means that the value is more than 2 standard deviations away from the property mean.
These property values are available through the Cheméo API. A free account gives you an access key.

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

Contents