Mixture of Hexadecane + Benzene, hexyl- + Cyclohexane, butyl-

Datasets

1. η - Viscosity, Pa*s (2)
2. ρ_l - Mass density, kg/m3 (2)
3. c_sound,fluid - Speed of Sound, m/s (2)
4. γ - Surface tension liquid-gas, N/m (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 102 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Solvent: Amount ratio of component to other component of binary solvent of Hexadecane (1) - Liquid	Mole fraction of Benzene, hexyl- (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.3335	0.0000	0.0018
293.15	0.3335	0.2004	0.0017
293.15	0.3335	0.4006	0.0017
293.15	0.3335	0.6003	0.0016
293.15	0.3335	0.7997	0.0016
293.15	0.9997	0.0000	0.0023
293.15	0.9997	0.2004	0.0021
293.15	0.9997	0.4008	0.0019
293.15	0.9997	0.6008	0.0018
293.15	0.9997	0.8003	0.0017
293.15	2.9967	0.0000	0.0028
293.15	2.9967	0.2005	0.0025
293.15	2.9967	0.4025	0.0022
293.15	2.9967	0.6007	0.0020
293.15	2.9967	0.8004	0.0018
303.15	0.3335	0.0000	0.0015
303.15	0.3335	0.2004	0.0014
303.15	0.3335	0.4006	0.0014
303.15	0.3335	0.6003	0.0014
303.15	0.3335	0.7997	0.0014
303.15	0.9997	0.0000	0.0019
303.15	0.9997	0.2004	0.0017
303.15	0.9997	0.4008	0.0016
303.15	0.9997	0.6008	0.0015
303.15	0.9997	0.8003	0.0015
303.15	2.9967	0.0000	0.0023
303.15	2.9967	0.2005	0.0021
303.15	2.9967	0.4025	0.0019
303.15	2.9967	0.6007	0.0017
303.15	2.9967	0.8004	0.0015
313.15	0.3335	0.0000	0.0013
313.15	0.3335	0.2004	0.0012
313.15	0.3335	0.4006	0.0012
313.15	0.3335	0.6003	0.0012
313.15	0.3335	0.7997	0.0012
313.15	0.9997	0.0000	0.0016
313.15	0.9997	0.2004	0.0015
313.15	0.9997	0.4008	0.0014
313.15	0.9997	0.6008	0.0013
313.15	0.9997	0.8003	0.0012
313.15	2.9967	0.0000	0.0019
313.15	2.9967	0.2005	0.0017
313.15	2.9967	0.4025	0.0015
313.15	2.9967	0.6007	0.0014
313.15	2.9967	0.8004	0.0013
323.15	0.3335	0.0000	0.0011
323.15	0.3335	0.2004	0.0010
323.15	0.3335	0.4006	0.0010
323.15	0.3335	0.6003	0.0010
323.15	0.3335	0.7997	0.0010
323.15	0.9997	0.0000	0.0013
323.15	0.9997	0.2004	0.0013
323.15	0.9997	0.4008	0.0012
323.15	0.9997	0.6008	0.0011
323.15	0.9997	0.8003	0.0011
323.15	2.9967	0.0000	0.0016
323.15	2.9967	0.2005	0.0014
323.15	2.9967	0.4025	0.0013
323.15	2.9967	0.6007	0.0012
323.15	2.9967	0.8004	0.0011
333.15	0.3335	0.0000	0.0009
333.15	0.3335	0.2004	0.0009
333.15	0.3335	0.4006	0.0009
333.15	0.3335	0.6003	0.0009
333.15	0.3335	0.7997	0.0009
333.15	0.9997	0.0000	0.0011
333.15	0.9997	0.2004	0.0011
333.15	0.9997	0.4008	0.0010
333.15	0.9997	0.6008	0.0010
333.15	0.9997	0.8003	0.0009
333.15	2.9967	0.0000	0.0013
333.15	2.9967	0.2005	0.0012
333.15	2.9967	0.4025	0.0011
333.15	2.9967	0.6007	0.0010
333.15	2.9967	0.8004	0.0010
343.15	0.3335	0.0000	0.0008
343.15	0.3335	0.2004	0.0008
343.15	0.3335	0.4006	0.0008
343.15	0.3335	0.6003	0.0008
343.15	0.3335	0.7997	0.0008
343.15	0.9997	0.0000	0.0010
343.15	0.9997	0.2004	0.0009
343.15	0.9997	0.4008	0.0009
343.15	0.9997	0.6008	0.0009
343.15	0.9997	0.8003	0.0008
343.15	2.9967	0.0000	0.0012
343.15	2.9967	0.2005	0.0011
343.15	2.9967	0.4025	0.0010
343.15	2.9967	0.6007	0.0009
343.15	2.9967	0.8004	0.0008

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 102 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Solvent: Amount ratio of component to other component of binary solvent of Hexadecane (1) - Liquid	Mole fraction of Benzene, hexyl- (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.3335	0.0000	0.0018
293.15	0.3335	0.2004	0.0017
293.15	0.3335	0.4006	0.0017
293.15	0.3335	0.6003	0.0016
293.15	0.3335	0.7997	0.0016
293.15	0.9997	0.0000	0.0023
293.15	0.9997	0.2004	0.0021
293.15	0.9997	0.4008	0.0019
293.15	0.9997	0.6008	0.0018
293.15	0.9997	0.8003	0.0017
293.15	2.9967	0.0000	0.0028
293.15	2.9967	0.2005	0.0025
293.15	2.9967	0.4025	0.0022
293.15	2.9967	0.6007	0.0020
293.15	2.9967	0.8004	0.0018
303.15	0.3335	0.0000	0.0015
303.15	0.3335	0.2004	0.0014
303.15	0.3335	0.4006	0.0014
303.15	0.3335	0.6003	0.0014
303.15	0.3335	0.7997	0.0014
303.15	0.9997	0.0000	0.0019
303.15	0.9997	0.2004	0.0017
303.15	0.9997	0.4008	0.0016
303.15	0.9997	0.6008	0.0015
303.15	0.9997	0.8003	0.0015
303.15	2.9967	0.0000	0.0023
303.15	2.9967	0.2005	0.0021
303.15	2.9967	0.4025	0.0019
303.15	2.9967	0.6007	0.0017
303.15	2.9967	0.8004	0.0015
313.15	0.3335	0.0000	0.0013
313.15	0.3335	0.2004	0.0012
313.15	0.3335	0.4006	0.0012
313.15	0.3335	0.6003	0.0012
313.15	0.3335	0.7997	0.0012
313.15	0.9997	0.0000	0.0016
313.15	0.9997	0.2004	0.0015
313.15	0.9997	0.4008	0.0014
313.15	0.9997	0.6008	0.0013
313.15	0.9997	0.8003	0.0012
313.15	2.9967	0.0000	0.0019
313.15	2.9967	0.2005	0.0017
313.15	2.9967	0.4025	0.0015
313.15	2.9967	0.6007	0.0014
313.15	2.9967	0.8004	0.0013
323.15	0.3335	0.0000	0.0011
323.15	0.3335	0.2004	0.0010
323.15	0.3335	0.4006	0.0010
323.15	0.3335	0.6003	0.0010
323.15	0.3335	0.7997	0.0010
323.15	0.9997	0.0000	0.0013
323.15	0.9997	0.2004	0.0013
323.15	0.9997	0.4008	0.0012
323.15	0.9997	0.6008	0.0011
323.15	0.9997	0.8003	0.0011
323.15	2.9967	0.0000	0.0016
323.15	2.9967	0.2005	0.0014
323.15	2.9967	0.4025	0.0013
323.15	2.9967	0.6007	0.0012
323.15	2.9967	0.8004	0.0011
333.15	0.3335	0.0000	0.0009
333.15	0.3335	0.2004	0.0009
333.15	0.3335	0.4006	0.0009
333.15	0.3335	0.6003	0.0009
333.15	0.3335	0.7997	0.0009
333.15	0.9997	0.0000	0.0011
333.15	0.9997	0.2004	0.0011
333.15	0.9997	0.4008	0.0010
333.15	0.9997	0.6008	0.0010
333.15	0.9997	0.8003	0.0009
333.15	2.9967	0.0000	0.0013
333.15	2.9967	0.2005	0.0012
333.15	2.9967	0.4025	0.0011
333.15	2.9967	0.6007	0.0010
333.15	2.9967	0.8004	0.0010
343.15	0.3335	0.0000	0.0008
343.15	0.3335	0.2004	0.0008
343.15	0.3335	0.4006	0.0008
343.15	0.3335	0.6003	0.0008
343.15	0.3335	0.7997	0.0008
343.15	0.9997	0.0000	0.0010
343.15	0.9997	0.2004	0.0009
343.15	0.9997	0.4008	0.0009
343.15	0.9997	0.6008	0.0009
343.15	0.9997	0.8003	0.0008
343.15	2.9967	0.0000	0.0012
343.15	2.9967	0.2005	0.0011
343.15	2.9967	0.4025	0.0010
343.15	2.9967	0.6007	0.0009
343.15	2.9967	0.8004	0.0008

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 102 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Solvent: Amount ratio of component to other component of binary solvent of Hexadecane (1) - Liquid	Mole fraction of Benzene, hexyl- (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.3335	0.0000	789.61
293.15	0.3335	0.2004	801.97
293.15	0.3335	0.4006	814.9
293.15	0.3335	0.6003	828.48
293.15	0.3335	0.7997	842.72
293.15	0.9997	0.0000	782.68
293.15	0.9997	0.2004	794.83
293.15	0.9997	0.4008	808.23
293.15	0.9997	0.6008	823.01
293.15	0.9997	0.8003	839.39
293.15	2.9967	0.0000	777.44
293.15	2.9967	0.2005	789.28
293.15	2.9967	0.4025	802.98
293.15	2.9967	0.6007	818.08
293.15	2.9967	0.8004	836.26
303.15	0.3335	0.0000	782.37
303.15	0.3335	0.2004	794.67
303.15	0.3335	0.4006	807.53
303.15	0.3335	0.6003	821.03
303.15	0.3335	0.7997	835.2
303.15	0.9997	0.0000	775.6
303.15	0.9997	0.2004	787.67
303.15	0.9997	0.4008	800.98
303.15	0.9997	0.6008	815.66
303.15	0.9997	0.8003	831.93
303.15	2.9967	0.0000	770.54
303.15	2.9967	0.2005	782.11
303.15	2.9967	0.4025	795.81
303.15	2.9967	0.6007	810.81
303.15	2.9967	0.8004	828.84
313.15	0.3335	0.0000	775.12
313.15	0.3335	0.2004	787.34
313.15	0.3335	0.4006	800.14
313.15	0.3335	0.6003	813.57
313.15	0.3335	0.7997	827.67
313.15	0.9997	0.0000	768.51
313.15	0.9997	0.2004	780.5
313.15	0.9997	0.4008	793.72
313.15	0.9997	0.6008	808.29
313.15	0.9997	0.8003	824.45
313.15	2.9967	0.0000	763.47
313.15	2.9967	0.2005	775.05
313.15	2.9967	0.4025	788.65
313.15	2.9967	0.6007	803.52
313.15	2.9967	0.8004	821.41
323.15	0.3335	0.0000	767.83
323.15	0.3335	0.2004	780.0
323.15	0.3335	0.4006	792.73
323.15	0.3335	0.6003	806.09
323.15	0.3335	0.7997	820.12
323.15	0.9997	0.0000	761.41
323.15	0.9997	0.2004	773.32
323.15	0.9997	0.4008	786.44
323.15	0.9997	0.6008	800.91
323.15	0.9997	0.8003	816.95
323.15	2.9967	0.0000	756.48
323.15	2.9967	0.2005	767.97
323.15	2.9967	0.4025	781.46
323.15	2.9967	0.6007	796.22
323.15	2.9967	0.8004	813.97
333.15	0.3335	0.0000	760.52
333.15	0.3335	0.2004	772.63
333.15	0.3335	0.4006	785.29
333.15	0.3335	0.6003	798.6
333.15	0.3335	0.7997	812.56
333.15	0.9997	0.0000	754.28
333.15	0.9997	0.2004	766.11
333.15	0.9997	0.4008	779.14
333.15	0.9997	0.6008	793.51
333.15	0.9997	0.8003	809.44
333.15	2.9967	0.0000	749.48
333.15	2.9967	0.2005	760.87
333.15	2.9967	0.4025	774.27
333.15	2.9967	0.6007	788.9
333.15	2.9967	0.8004	806.5
343.15	0.3335	0.0000	753.2
343.15	0.3335	0.2004	765.2
343.15	0.3335	0.4006	777.7
343.15	0.3335	0.6003	791.0
343.15	0.3335	0.7997	804.9
343.15	0.9997	0.0000	747.2
343.15	0.9997	0.2004	758.9
343.15	0.9997	0.4008	771.9
343.15	0.9997	0.6008	786.1
343.15	0.9997	0.8003	802.0
343.15	2.9967	0.0000	742.5
343.15	2.9967	0.2005	753.8
343.15	2.9967	0.4025	767.0
343.15	2.9967	0.6007	781.5
343.15	2.9967	0.8004	798.9

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 102 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Solvent: Amount ratio of component to other component of binary solvent of Hexadecane (1) - Liquid	Mole fraction of Benzene, hexyl- (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.3335	0.0000	789.61
293.15	0.3335	0.2004	801.97
293.15	0.3335	0.4006	814.9
293.15	0.3335	0.6003	828.48
293.15	0.3335	0.7997	842.72
293.15	0.9997	0.0000	782.68
293.15	0.9997	0.2004	794.83
293.15	0.9997	0.4008	808.23
293.15	0.9997	0.6008	823.01
293.15	0.9997	0.8003	839.39
293.15	2.9967	0.0000	777.44
293.15	2.9967	0.2005	789.28
293.15	2.9967	0.4025	802.98
293.15	2.9967	0.6007	818.08
293.15	2.9967	0.8004	836.26
303.15	0.3335	0.0000	782.37
303.15	0.3335	0.2004	794.67
303.15	0.3335	0.4006	807.53
303.15	0.3335	0.6003	821.03
303.15	0.3335	0.7997	835.2
303.15	0.9997	0.0000	775.6
303.15	0.9997	0.2004	787.67
303.15	0.9997	0.4008	800.98
303.15	0.9997	0.6008	815.66
303.15	0.9997	0.8003	831.93
303.15	2.9967	0.0000	770.54
303.15	2.9967	0.2005	782.11
303.15	2.9967	0.4025	795.81
303.15	2.9967	0.6007	810.81
303.15	2.9967	0.8004	828.84
313.15	0.3335	0.0000	775.12
313.15	0.3335	0.2004	787.34
313.15	0.3335	0.4006	800.14
313.15	0.3335	0.6003	813.57
313.15	0.3335	0.7997	827.67
313.15	0.9997	0.0000	768.51
313.15	0.9997	0.2004	780.5
313.15	0.9997	0.4008	793.72
313.15	0.9997	0.6008	808.29
313.15	0.9997	0.8003	824.45
313.15	2.9967	0.0000	763.47
313.15	2.9967	0.2005	775.05
313.15	2.9967	0.4025	788.65
313.15	2.9967	0.6007	803.52
313.15	2.9967	0.8004	821.41
323.15	0.3335	0.0000	767.83
323.15	0.3335	0.2004	780.0
323.15	0.3335	0.4006	792.73
323.15	0.3335	0.6003	806.09
323.15	0.3335	0.7997	820.12
323.15	0.9997	0.0000	761.41
323.15	0.9997	0.2004	773.32
323.15	0.9997	0.4008	786.44
323.15	0.9997	0.6008	800.91
323.15	0.9997	0.8003	816.95
323.15	2.9967	0.0000	756.48
323.15	2.9967	0.2005	767.97
323.15	2.9967	0.4025	781.46
323.15	2.9967	0.6007	796.22
323.15	2.9967	0.8004	813.97
333.15	0.3335	0.0000	760.52
333.15	0.3335	0.2004	772.63
333.15	0.3335	0.4006	785.29
333.15	0.3335	0.6003	798.6
333.15	0.3335	0.7997	812.56
333.15	0.9997	0.0000	754.28
333.15	0.9997	0.2004	766.11
333.15	0.9997	0.4008	779.14
333.15	0.9997	0.6008	793.51
333.15	0.9997	0.8003	809.44
333.15	2.9967	0.0000	749.48
333.15	2.9967	0.2005	760.87
333.15	2.9967	0.4025	774.27
333.15	2.9967	0.6007	788.9
333.15	2.9967	0.8004	806.5
343.15	0.3335	0.0000	753.2
343.15	0.3335	0.2004	765.2
343.15	0.3335	0.4006	777.7
343.15	0.3335	0.6003	791.0
343.15	0.3335	0.7997	804.9
343.15	0.9997	0.0000	747.2
343.15	0.9997	0.2004	758.9
343.15	0.9997	0.4008	771.9
343.15	0.9997	0.6008	786.1
343.15	0.9997	0.8003	802.0
343.15	2.9967	0.0000	742.5
343.15	2.9967	0.2005	753.8
343.15	2.9967	0.4025	767.0
343.15	2.9967	0.6007	781.5
343.15	2.9967	0.8004	798.9

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 102 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Solvent: Amount ratio of component to other component of binary solvent of Hexadecane (1) - Liquid	Mole fraction of Benzene, hexyl- (2) - Liquid	Speed of sound, m/s - Liquid
293.15	0.3335	0.0000	1335.2
293.15	0.3335	0.2004	1340.3
293.15	0.3335	0.4006	1346.7
293.15	0.3335	0.6003	1354.5
293.15	0.3335	0.7997	1363.3
293.15	0.9997	0.0000	1342.9
293.15	0.9997	0.2004	1345.5
293.15	0.9997	0.4008	1349.7
293.15	0.9997	0.6008	1355.7
293.15	0.9997	0.8003	1363.8
293.15	2.9967	0.0000	1349.7
293.15	2.9967	0.2005	1350.7
293.15	2.9967	0.4025	1353.1
293.15	2.9967	0.6007	1357.1
293.15	2.9967	0.8004	1364.0
303.15	0.3335	0.0000	1296.8
303.15	0.3335	0.2004	1302.1
303.15	0.3335	0.4006	1308.8
303.15	0.3335	0.6003	1316.8
303.15	0.3335	0.7997	1325.7
303.15	0.9997	0.0000	1305.2
303.15	0.9997	0.2004	1307.9
303.15	0.9997	0.4008	1312.2
303.15	0.9997	0.6008	1318.4
303.15	0.9997	0.8003	1326.5
303.15	2.9967	0.0000	1312.4
303.15	2.9967	0.2005	1313.6
303.15	2.9967	0.4025	1316.0
303.15	2.9967	0.6007	1320.0
303.15	2.9967	0.8004	1326.8
313.15	0.3335	0.0000	1259.1
313.15	0.3335	0.2004	1264.5
313.15	0.3335	0.4006	1271.5
313.15	0.3335	0.6003	1279.6
313.15	0.3335	0.7997	1288.6
313.15	0.9997	0.0000	1268.2
313.15	0.9997	0.2004	1270.9
313.15	0.9997	0.4008	1275.4
313.15	0.9997	0.6008	1281.6
313.15	0.9997	0.8003	1289.7
313.15	2.9967	0.0000	1275.9
313.15	2.9967	0.2005	1277.1
313.15	2.9967	0.4025	1279.5
313.15	2.9967	0.6007	1283.6
313.15	2.9967	0.8004	1290.2
323.15	0.3335	0.0000	1222.0
323.15	0.3335	0.2004	1227.7
323.15	0.3335	0.4006	1234.8
323.15	0.3335	0.6003	1243.2
323.15	0.3335	0.7997	1252.3
323.15	0.9997	0.0000	1231.8
323.15	0.9997	0.2004	1234.6
323.15	0.9997	0.4008	1239.2
323.15	0.9997	0.6008	1245.5
323.15	0.9997	0.8003	1253.5
323.15	2.9967	0.0000	1239.9
323.15	2.9967	0.2005	1241.2
323.15	2.9967	0.4025	1243.6
323.15	2.9967	0.6007	1247.6
323.15	2.9967	0.8004	1254.2
333.15	0.3335	0.0000	1185.6
333.15	0.3335	0.2004	1191.5
333.15	0.3335	0.4006	1198.8
333.15	0.3335	0.6003	1207.5
333.15	0.3335	0.7997	1217.0
333.15	0.9997	0.0000	1196.2
333.15	0.9997	0.2004	1199.1
333.15	0.9997	0.4008	1203.7
333.15	0.9997	0.6008	1210.1
333.15	0.9997	0.8003	1218.0
333.15	2.9967	0.0000	1204.7
333.15	2.9967	0.2005	1206.1
333.15	2.9967	0.4025	1208.5
333.15	2.9967	0.6007	1212.5
333.15	2.9967	0.8004	1218.9

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 102 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Solvent: Amount ratio of component to other component of binary solvent of Hexadecane (1) - Liquid	Mole fraction of Benzene, hexyl- (2) - Liquid	Speed of sound, m/s - Liquid
293.15	0.3335	0.0000	1335.2
293.15	0.3335	0.2004	1340.3
293.15	0.3335	0.4006	1346.7
293.15	0.3335	0.6003	1354.5
293.15	0.3335	0.7997	1363.3
293.15	0.9997	0.0000	1342.9
293.15	0.9997	0.2004	1345.5
293.15	0.9997	0.4008	1349.7
293.15	0.9997	0.6008	1355.7
293.15	0.9997	0.8003	1363.8
293.15	2.9967	0.0000	1349.7
293.15	2.9967	0.2005	1350.7
293.15	2.9967	0.4025	1353.1
293.15	2.9967	0.6007	1357.1
293.15	2.9967	0.8004	1364.0
303.15	0.3335	0.0000	1296.8
303.15	0.3335	0.2004	1302.1
303.15	0.3335	0.4006	1308.8
303.15	0.3335	0.6003	1316.8
303.15	0.3335	0.7997	1325.7
303.15	0.9997	0.0000	1305.2
303.15	0.9997	0.2004	1307.9
303.15	0.9997	0.4008	1312.2
303.15	0.9997	0.6008	1318.4
303.15	0.9997	0.8003	1326.5
303.15	2.9967	0.0000	1312.4
303.15	2.9967	0.2005	1313.6
303.15	2.9967	0.4025	1316.0
303.15	2.9967	0.6007	1320.0
303.15	2.9967	0.8004	1326.8
313.15	0.3335	0.0000	1259.1
313.15	0.3335	0.2004	1264.5
313.15	0.3335	0.4006	1271.5
313.15	0.3335	0.6003	1279.6
313.15	0.3335	0.7997	1288.6
313.15	0.9997	0.0000	1268.2
313.15	0.9997	0.2004	1270.9
313.15	0.9997	0.4008	1275.4
313.15	0.9997	0.6008	1281.6
313.15	0.9997	0.8003	1289.7
313.15	2.9967	0.0000	1275.9
313.15	2.9967	0.2005	1277.1
313.15	2.9967	0.4025	1279.5
313.15	2.9967	0.6007	1283.6
313.15	2.9967	0.8004	1290.2
323.15	0.3335	0.0000	1222.0
323.15	0.3335	0.2004	1227.7
323.15	0.3335	0.4006	1234.8
323.15	0.3335	0.6003	1243.2
323.15	0.3335	0.7997	1252.3
323.15	0.9997	0.0000	1231.8
323.15	0.9997	0.2004	1234.6
323.15	0.9997	0.4008	1239.2
323.15	0.9997	0.6008	1245.5
323.15	0.9997	0.8003	1253.5
323.15	2.9967	0.0000	1239.9
323.15	2.9967	0.2005	1241.2
323.15	2.9967	0.4025	1243.6
323.15	2.9967	0.6007	1247.6
323.15	2.9967	0.8004	1254.2
333.15	0.3335	0.0000	1185.6
333.15	0.3335	0.2004	1191.5
333.15	0.3335	0.4006	1198.8
333.15	0.3335	0.6003	1207.5
333.15	0.3335	0.7997	1217.0
333.15	0.9997	0.0000	1196.2
333.15	0.9997	0.2004	1199.1
333.15	0.9997	0.4008	1203.7
333.15	0.9997	0.6008	1210.1
333.15	0.9997	0.8003	1218.0
333.15	2.9967	0.0000	1204.7
333.15	2.9967	0.2005	1206.1
333.15	2.9967	0.4025	1208.5
333.15	2.9967	0.6007	1212.5
333.15	2.9967	0.8004	1218.9

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 294.5 (Liquid)

Fixed		Measured
Solvent: Amount ratio of component to other component of binary solvent of Hexadecane (1) - Liquid	Mole fraction of Benzene, hexyl- (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.3335	0.0000	0.0269
0.3335	0.2004	0.0272
0.3335	0.4006	0.0274
0.3335	0.6003	0.0282
0.3335	0.7997	0.0285
0.9997	0.0000	0.0269
0.9997	0.2004	0.0270
0.9997	0.4008	0.0277
0.9997	0.6008	0.0282
0.9997	0.8003	0.0286
2.9967	0.0000	0.0271
2.9967	0.2005	0.0274
2.9967	0.4025	0.0274
2.9967	0.6007	0.0279
2.9967	0.8004	0.0286

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 294.5 (Liquid)

Fixed		Measured
Solvent: Amount ratio of component to other component of binary solvent of Hexadecane (1) - Liquid	Mole fraction of Benzene, hexyl- (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.3335	0.0000	0.0269
0.3335	0.2004	0.0272
0.3335	0.4006	0.0274
0.3335	0.6003	0.0282
0.3335	0.7997	0.0285
0.9997	0.0000	0.0269
0.9997	0.2004	0.0270
0.9997	0.4008	0.0277
0.9997	0.6008	0.0282
0.9997	0.8003	0.0286
2.9967	0.0000	0.0271
2.9967	0.2005	0.0274
2.9967	0.4025	0.0274
2.9967	0.6007	0.0279
2.9967	0.8004	0.0286

Sources

• Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)