Mixture of Benzene, n-butyl- + Hexadecane + 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 (2) - Liquid	Mole fraction of Benzene, n-butyl- (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.3333	0.0000	0.0018
293.15	0.3333	0.2004	0.0016
293.15	0.3333	0.4004	0.0014
293.15	0.3333	0.6003	0.0013
293.15	0.3333	0.8002	0.0011
293.15	0.9992	0.0000	0.0023
293.15	0.9992	0.2009	0.0019
293.15	0.9992	0.4003	0.0016
293.15	0.9992	0.6002	0.0014
293.15	0.9992	0.8000	0.0012
293.15	3.0006	0.0000	0.0028
293.15	3.0006	0.2010	0.0024
293.15	3.0006	0.4009	0.0019
293.15	3.0006	0.6010	0.0016
293.15	3.0006	0.8005	0.0013
303.15	0.3333	0.0000	0.0015
303.15	0.3333	0.2004	0.0013
303.15	0.3333	0.4004	0.0012
303.15	0.3333	0.6003	0.0011
303.15	0.3333	0.8002	0.0010
303.15	0.9992	0.0000	0.0019
303.15	0.9992	0.2009	0.0016
303.15	0.9992	0.4003	0.0014
303.15	0.9992	0.6002	0.0012
303.15	0.9992	0.8000	0.0010
303.15	3.0006	0.0000	0.0023
303.15	3.0006	0.2010	0.0019
303.15	3.0006	0.4009	0.0016
303.15	3.0006	0.6010	0.0013
303.15	3.0006	0.8005	0.0011
313.15	0.3333	0.0000	0.0013
313.15	0.3333	0.2004	0.0011
313.15	0.3333	0.4004	0.0010
313.15	0.3333	0.6003	0.0009
313.15	0.3333	0.8002	0.0009
313.15	0.9992	0.0000	0.0016
313.15	0.9992	0.2009	0.0014
313.15	0.9992	0.4003	0.0012
313.15	0.9992	0.6002	0.0010
313.15	0.9992	0.8000	0.0009
313.15	3.0006	0.0000	0.0019
313.15	3.0006	0.2010	0.0016
313.15	3.0006	0.4009	0.0014
313.15	3.0006	0.6010	0.0011
313.15	3.0006	0.8005	0.0010
323.15	0.3333	0.0000	0.0011
323.15	0.3333	0.2004	0.0010
323.15	0.3333	0.4004	0.0009
323.15	0.3333	0.6003	0.0008
323.15	0.3333	0.8002	0.0008
323.15	0.9992	0.0000	0.0013
323.15	0.9992	0.2009	0.0012
323.15	0.9992	0.4003	0.0010
323.15	0.9992	0.6002	0.0009
323.15	0.9992	0.8000	0.0008
323.15	3.0006	0.0000	0.0016
323.15	3.0006	0.2010	0.0014
323.15	3.0006	0.4009	0.0012
323.15	3.0006	0.6010	0.0010
323.15	3.0006	0.8005	0.0008
333.15	0.3333	0.0000	0.0009
333.15	0.3333	0.2004	0.0009
333.15	0.3333	0.4004	0.0008
333.15	0.3333	0.6003	0.0007
333.15	0.3333	0.8002	0.0007
333.15	0.9992	0.0000	0.0011
333.15	0.9992	0.2009	0.0010
333.15	0.9992	0.4003	0.0009
333.15	0.9992	0.6002	0.0008
333.15	0.9992	0.8000	0.0007
333.15	3.0006	0.0000	0.0013
333.15	3.0006	0.2010	0.0012
333.15	3.0006	0.4009	0.0010
333.15	3.0006	0.6010	0.0009
333.15	3.0006	0.8005	0.0007
343.15	0.3333	0.0000	0.0008
343.15	0.3333	0.2004	0.0008
343.15	0.3333	0.4004	0.0007
343.15	0.3333	0.6003	0.0006
343.15	0.3333	0.8002	0.0006
343.15	0.9992	0.0000	0.0010
343.15	0.9992	0.2009	0.0009
343.15	0.9992	0.4003	0.0008
343.15	0.9992	0.6002	0.0007
343.15	0.9992	0.8000	0.0006
343.15	3.0006	0.0000	0.0012
343.15	3.0006	0.2010	0.0010
343.15	3.0006	0.4009	0.0009
343.15	3.0006	0.6010	0.0008
343.15	3.0006	0.8005	0.0007

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 (2) - Liquid	Mole fraction of Benzene, n-butyl- (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.3333	0.0000	0.0018
293.15	0.3333	0.2004	0.0016
293.15	0.3333	0.4004	0.0014
293.15	0.3333	0.6003	0.0013
293.15	0.3333	0.8002	0.0011
293.15	0.9992	0.0000	0.0023
293.15	0.9992	0.2009	0.0019
293.15	0.9992	0.4003	0.0016
293.15	0.9992	0.6002	0.0014
293.15	0.9992	0.8000	0.0012
293.15	3.0006	0.0000	0.0028
293.15	3.0006	0.2010	0.0024
293.15	3.0006	0.4009	0.0019
293.15	3.0006	0.6010	0.0016
293.15	3.0006	0.8005	0.0013
303.15	0.3333	0.0000	0.0015
303.15	0.3333	0.2004	0.0013
303.15	0.3333	0.4004	0.0012
303.15	0.3333	0.6003	0.0011
303.15	0.3333	0.8002	0.0010
303.15	0.9992	0.0000	0.0019
303.15	0.9992	0.2009	0.0016
303.15	0.9992	0.4003	0.0014
303.15	0.9992	0.6002	0.0012
303.15	0.9992	0.8000	0.0010
303.15	3.0006	0.0000	0.0023
303.15	3.0006	0.2010	0.0019
303.15	3.0006	0.4009	0.0016
303.15	3.0006	0.6010	0.0013
303.15	3.0006	0.8005	0.0011
313.15	0.3333	0.0000	0.0013
313.15	0.3333	0.2004	0.0011
313.15	0.3333	0.4004	0.0010
313.15	0.3333	0.6003	0.0009
313.15	0.3333	0.8002	0.0009
313.15	0.9992	0.0000	0.0016
313.15	0.9992	0.2009	0.0014
313.15	0.9992	0.4003	0.0012
313.15	0.9992	0.6002	0.0010
313.15	0.9992	0.8000	0.0009
313.15	3.0006	0.0000	0.0019
313.15	3.0006	0.2010	0.0016
313.15	3.0006	0.4009	0.0014
313.15	3.0006	0.6010	0.0011
313.15	3.0006	0.8005	0.0010
323.15	0.3333	0.0000	0.0011
323.15	0.3333	0.2004	0.0010
323.15	0.3333	0.4004	0.0009
323.15	0.3333	0.6003	0.0008
323.15	0.3333	0.8002	0.0008
323.15	0.9992	0.0000	0.0013
323.15	0.9992	0.2009	0.0012
323.15	0.9992	0.4003	0.0010
323.15	0.9992	0.6002	0.0009
323.15	0.9992	0.8000	0.0008
323.15	3.0006	0.0000	0.0016
323.15	3.0006	0.2010	0.0014
323.15	3.0006	0.4009	0.0012
323.15	3.0006	0.6010	0.0010
323.15	3.0006	0.8005	0.0008
333.15	0.3333	0.0000	0.0009
333.15	0.3333	0.2004	0.0009
333.15	0.3333	0.4004	0.0008
333.15	0.3333	0.6003	0.0007
333.15	0.3333	0.8002	0.0007
333.15	0.9992	0.0000	0.0011
333.15	0.9992	0.2009	0.0010
333.15	0.9992	0.4003	0.0009
333.15	0.9992	0.6002	0.0008
333.15	0.9992	0.8000	0.0007
333.15	3.0006	0.0000	0.0013
333.15	3.0006	0.2010	0.0012
333.15	3.0006	0.4009	0.0010
333.15	3.0006	0.6010	0.0009
333.15	3.0006	0.8005	0.0007
343.15	0.3333	0.0000	0.0008
343.15	0.3333	0.2004	0.0008
343.15	0.3333	0.4004	0.0007
343.15	0.3333	0.6003	0.0006
343.15	0.3333	0.8002	0.0006
343.15	0.9992	0.0000	0.0010
343.15	0.9992	0.2009	0.0009
343.15	0.9992	0.4003	0.0008
343.15	0.9992	0.6002	0.0007
343.15	0.9992	0.8000	0.0006
343.15	3.0006	0.0000	0.0012
343.15	3.0006	0.2010	0.0010
343.15	3.0006	0.4009	0.0009
343.15	3.0006	0.6010	0.0008
343.15	3.0006	0.8005	0.0007

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 (2) - Liquid	Mole fraction of Benzene, n-butyl- (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.3333	0.0000	789.5
293.15	0.3333	0.2004	800.34
293.15	0.3333	0.4004	812.49
293.15	0.3333	0.6003	826.28
293.15	0.3333	0.8002	842.18
293.15	0.9992	0.0000	782.68
293.15	0.9992	0.2009	793.17
293.15	0.9992	0.4003	805.49
293.15	0.9992	0.6002	820.19
293.15	0.9992	0.8000	838.22
293.15	3.0006	0.0000	777.44
293.15	3.0006	0.2010	787.52
293.15	3.0006	0.4009	799.77
293.15	3.0006	0.6010	815.1
293.15	3.0006	0.8005	834.69
303.15	0.3333	0.0000	782.27
303.15	0.3333	0.2004	792.98
303.15	0.3333	0.4004	804.99
303.15	0.3333	0.6003	818.63
303.15	0.3333	0.8002	834.35
303.15	0.9992	0.0000	775.6
303.15	0.9992	0.2009	785.97
303.15	0.9992	0.4003	798.14
303.15	0.9992	0.6002	812.66
303.15	0.9992	0.8000	830.46
303.15	3.0006	0.0000	770.45
303.15	3.0006	0.2010	780.42
303.15	3.0006	0.4009	792.53
303.15	3.0006	0.6010	807.66
303.15	3.0006	0.8005	827.0
313.15	0.3333	0.0000	775.01
313.15	0.3333	0.2004	785.59
313.15	0.3333	0.4004	797.46
313.15	0.3333	0.6003	810.94
313.15	0.3333	0.8002	826.49
313.15	0.9992	0.0000	768.51
313.15	0.9992	0.2009	778.75
313.15	0.9992	0.4003	790.77
313.15	0.9992	0.6002	805.1
313.15	0.9992	0.8000	822.68
313.15	3.0006	0.0000	763.47
313.15	3.0006	0.2010	773.32
313.15	3.0006	0.4009	785.27
313.15	3.0006	0.6010	800.21
313.15	3.0006	0.8005	819.28
323.15	0.3333	0.0000	767.73
323.15	0.3333	0.2004	778.18
323.15	0.3333	0.4004	789.91
323.15	0.3333	0.6003	803.23
323.15	0.3333	0.8002	818.6
323.15	0.9992	0.0000	761.41
323.15	0.9992	0.2009	771.51
323.15	0.9992	0.4003	783.37
323.15	0.9992	0.6002	797.52
323.15	0.9992	0.8000	814.87
323.15	3.0006	0.0000	756.48
323.15	3.0006	0.2010	766.2
323.15	3.0006	0.4009	778.0
323.15	3.0006	0.6010	792.73
323.15	3.0006	0.8005	811.54
333.15	0.3333	0.0000	760.42
333.15	0.3333	0.2004	770.74
333.15	0.3333	0.4004	782.32
333.15	0.3333	0.6003	795.49
333.15	0.3333	0.8002	810.68
333.15	0.9992	0.0000	754.28
333.15	0.9992	0.2009	764.26
333.15	0.9992	0.4003	775.95
333.15	0.9992	0.6002	789.91
333.15	0.9992	0.8000	807.03
333.15	3.0006	0.0000	749.49
333.15	3.0006	0.2010	759.07
333.15	3.0006	0.4009	770.71
333.15	3.0006	0.6010	785.23
333.15	3.0006	0.8005	803.77
343.15	0.3333	0.0000	753.1
343.15	0.3333	0.2004	763.2
343.15	0.3333	0.4004	774.7
343.15	0.3333	0.6003	787.8
343.15	0.3333	0.8002	802.7
343.15	0.9992	0.0000	747.2
343.15	0.9992	0.2009	756.9
343.15	0.9992	0.4003	768.5
343.15	0.9992	0.6002	782.3
343.15	0.9992	0.8000	799.1
343.15	3.0006	0.0000	742.5
343.15	3.0006	0.2010	751.9
343.15	3.0006	0.4009	763.4
343.15	3.0006	0.6010	777.7
343.15	3.0006	0.8005	796.0

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 (2) - Liquid	Mole fraction of Benzene, n-butyl- (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.3333	0.0000	789.5
293.15	0.3333	0.2004	800.34
293.15	0.3333	0.4004	812.49
293.15	0.3333	0.6003	826.28
293.15	0.3333	0.8002	842.18
293.15	0.9992	0.0000	782.68
293.15	0.9992	0.2009	793.17
293.15	0.9992	0.4003	805.49
293.15	0.9992	0.6002	820.19
293.15	0.9992	0.8000	838.22
293.15	3.0006	0.0000	777.44
293.15	3.0006	0.2010	787.52
293.15	3.0006	0.4009	799.77
293.15	3.0006	0.6010	815.1
293.15	3.0006	0.8005	834.69
303.15	0.3333	0.0000	782.27
303.15	0.3333	0.2004	792.98
303.15	0.3333	0.4004	804.99
303.15	0.3333	0.6003	818.63
303.15	0.3333	0.8002	834.35
303.15	0.9992	0.0000	775.6
303.15	0.9992	0.2009	785.97
303.15	0.9992	0.4003	798.14
303.15	0.9992	0.6002	812.66
303.15	0.9992	0.8000	830.46
303.15	3.0006	0.0000	770.45
303.15	3.0006	0.2010	780.42
303.15	3.0006	0.4009	792.53
303.15	3.0006	0.6010	807.66
303.15	3.0006	0.8005	827.0
313.15	0.3333	0.0000	775.01
313.15	0.3333	0.2004	785.59
313.15	0.3333	0.4004	797.46
313.15	0.3333	0.6003	810.94
313.15	0.3333	0.8002	826.49
313.15	0.9992	0.0000	768.51
313.15	0.9992	0.2009	778.75
313.15	0.9992	0.4003	790.77
313.15	0.9992	0.6002	805.1
313.15	0.9992	0.8000	822.68
313.15	3.0006	0.0000	763.47
313.15	3.0006	0.2010	773.32
313.15	3.0006	0.4009	785.27
313.15	3.0006	0.6010	800.21
313.15	3.0006	0.8005	819.28
323.15	0.3333	0.0000	767.73
323.15	0.3333	0.2004	778.18
323.15	0.3333	0.4004	789.91
323.15	0.3333	0.6003	803.23
323.15	0.3333	0.8002	818.6
323.15	0.9992	0.0000	761.41
323.15	0.9992	0.2009	771.51
323.15	0.9992	0.4003	783.37
323.15	0.9992	0.6002	797.52
323.15	0.9992	0.8000	814.87
323.15	3.0006	0.0000	756.48
323.15	3.0006	0.2010	766.2
323.15	3.0006	0.4009	778.0
323.15	3.0006	0.6010	792.73
323.15	3.0006	0.8005	811.54
333.15	0.3333	0.0000	760.42
333.15	0.3333	0.2004	770.74
333.15	0.3333	0.4004	782.32
333.15	0.3333	0.6003	795.49
333.15	0.3333	0.8002	810.68
333.15	0.9992	0.0000	754.28
333.15	0.9992	0.2009	764.26
333.15	0.9992	0.4003	775.95
333.15	0.9992	0.6002	789.91
333.15	0.9992	0.8000	807.03
333.15	3.0006	0.0000	749.49
333.15	3.0006	0.2010	759.07
333.15	3.0006	0.4009	770.71
333.15	3.0006	0.6010	785.23
333.15	3.0006	0.8005	803.77
343.15	0.3333	0.0000	753.1
343.15	0.3333	0.2004	763.2
343.15	0.3333	0.4004	774.7
343.15	0.3333	0.6003	787.8
343.15	0.3333	0.8002	802.7
343.15	0.9992	0.0000	747.2
343.15	0.9992	0.2009	756.9
343.15	0.9992	0.4003	768.5
343.15	0.9992	0.6002	782.3
343.15	0.9992	0.8000	799.1
343.15	3.0006	0.0000	742.5
343.15	3.0006	0.2010	751.9
343.15	3.0006	0.4009	763.4
343.15	3.0006	0.6010	777.7
343.15	3.0006	0.8005	796.0

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 (2) - Liquid	Mole fraction of Benzene, n-butyl- (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.3333	0.0000	1335.5
293.15	0.3333	0.2004	1334.5
293.15	0.3333	0.4004	1335.4
293.15	0.3333	0.6003	1338.4
293.15	0.3333	0.8002	1343.7
293.15	0.9992	0.0000	1342.9
293.15	0.9992	0.2009	1340.5
293.15	0.9992	0.4003	1339.3
293.15	0.9992	0.6002	1340.5
293.15	0.9992	0.8000	1343.9
293.15	3.0006	0.0000	1350.0
293.15	3.0006	0.2010	1345.9
293.15	3.0006	0.4009	1343.3
293.15	3.0006	0.6010	1342.4
293.15	3.0006	0.8005	1344.4
303.15	0.3333	0.0000	1297.1
303.15	0.3333	0.2004	1296.1
303.15	0.3333	0.4004	1297.0
303.15	0.3333	0.6003	1299.9
303.15	0.3333	0.8002	1305.2
303.15	0.9992	0.0000	1305.2
303.15	0.9992	0.2009	1302.8
303.15	0.9992	0.4003	1301.6
303.15	0.9992	0.6002	1302.5
303.15	0.9992	0.8000	1305.6
303.15	3.0006	0.0000	1312.7
303.15	3.0006	0.2010	1308.6
303.15	3.0006	0.4009	1305.9
303.15	3.0006	0.6010	1304.8
303.15	3.0006	0.8005	1306.4
313.15	0.3333	0.0000	1259.3
313.15	0.3333	0.2004	1258.3
313.15	0.3333	0.4004	1259.2
313.15	0.3333	0.6003	1262.1
313.15	0.3333	0.8002	1267.1
313.15	0.9992	0.0000	1268.2
313.15	0.9992	0.2009	1265.7
313.15	0.9992	0.4003	1264.3
313.15	0.9992	0.6002	1265.2
313.15	0.9992	0.8000	1268.0
313.15	3.0006	0.0000	1276.0
313.15	3.0006	0.2010	1272.0
313.15	3.0006	0.4009	1269.1
313.15	3.0006	0.6010	1267.8
313.15	3.0006	0.8005	1269.0
323.15	0.3333	0.0000	1222.1
323.15	0.3333	0.2004	1221.1
323.15	0.3333	0.4004	1222.0
323.15	0.3333	0.6003	1224.8
323.15	0.3333	0.8002	1229.8
323.15	0.9992	0.0000	1231.8
323.15	0.9992	0.2009	1229.2
323.15	0.9992	0.4003	1227.7
323.15	0.9992	0.6002	1228.4
323.15	0.9992	0.8000	1230.8
323.15	3.0006	0.0000	1240.1
323.15	3.0006	0.2010	1235.9
323.15	3.0006	0.4009	1232.9
323.15	3.0006	0.6010	1231.4
323.15	3.0006	0.8005	1232.2
333.15	0.3333	0.0000	1185.7
333.15	0.3333	0.2004	1184.8
333.15	0.3333	0.4004	1185.6
333.15	0.3333	0.6003	1188.3
333.15	0.3333	0.8002	1193.2
333.15	0.9992	0.0000	1196.2
333.15	0.9992	0.2009	1193.6
333.15	0.9992	0.4003	1191.9
333.15	0.9992	0.6002	1192.0
333.15	0.9992	0.8000	1194.5
333.15	3.0006	0.0000	1205.0
333.15	3.0006	0.2010	1200.7
333.15	3.0006	0.4009	1197.5
333.15	3.0006	0.6010	1195.8
333.15	3.0006	0.8005	1196.1

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 (2) - Liquid	Mole fraction of Benzene, n-butyl- (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.3333	0.0000	1335.5
293.15	0.3333	0.2004	1334.5
293.15	0.3333	0.4004	1335.4
293.15	0.3333	0.6003	1338.4
293.15	0.3333	0.8002	1343.7
293.15	0.9992	0.0000	1342.9
293.15	0.9992	0.2009	1340.5
293.15	0.9992	0.4003	1339.3
293.15	0.9992	0.6002	1340.5
293.15	0.9992	0.8000	1343.9
293.15	3.0006	0.0000	1350.0
293.15	3.0006	0.2010	1345.9
293.15	3.0006	0.4009	1343.3
293.15	3.0006	0.6010	1342.4
293.15	3.0006	0.8005	1344.4
303.15	0.3333	0.0000	1297.1
303.15	0.3333	0.2004	1296.1
303.15	0.3333	0.4004	1297.0
303.15	0.3333	0.6003	1299.9
303.15	0.3333	0.8002	1305.2
303.15	0.9992	0.0000	1305.2
303.15	0.9992	0.2009	1302.8
303.15	0.9992	0.4003	1301.6
303.15	0.9992	0.6002	1302.5
303.15	0.9992	0.8000	1305.6
303.15	3.0006	0.0000	1312.7
303.15	3.0006	0.2010	1308.6
303.15	3.0006	0.4009	1305.9
303.15	3.0006	0.6010	1304.8
303.15	3.0006	0.8005	1306.4
313.15	0.3333	0.0000	1259.3
313.15	0.3333	0.2004	1258.3
313.15	0.3333	0.4004	1259.2
313.15	0.3333	0.6003	1262.1
313.15	0.3333	0.8002	1267.1
313.15	0.9992	0.0000	1268.2
313.15	0.9992	0.2009	1265.7
313.15	0.9992	0.4003	1264.3
313.15	0.9992	0.6002	1265.2
313.15	0.9992	0.8000	1268.0
313.15	3.0006	0.0000	1276.0
313.15	3.0006	0.2010	1272.0
313.15	3.0006	0.4009	1269.1
313.15	3.0006	0.6010	1267.8
313.15	3.0006	0.8005	1269.0
323.15	0.3333	0.0000	1222.1
323.15	0.3333	0.2004	1221.1
323.15	0.3333	0.4004	1222.0
323.15	0.3333	0.6003	1224.8
323.15	0.3333	0.8002	1229.8
323.15	0.9992	0.0000	1231.8
323.15	0.9992	0.2009	1229.2
323.15	0.9992	0.4003	1227.7
323.15	0.9992	0.6002	1228.4
323.15	0.9992	0.8000	1230.8
323.15	3.0006	0.0000	1240.1
323.15	3.0006	0.2010	1235.9
323.15	3.0006	0.4009	1232.9
323.15	3.0006	0.6010	1231.4
323.15	3.0006	0.8005	1232.2
333.15	0.3333	0.0000	1185.7
333.15	0.3333	0.2004	1184.8
333.15	0.3333	0.4004	1185.6
333.15	0.3333	0.6003	1188.3
333.15	0.3333	0.8002	1193.2
333.15	0.9992	0.0000	1196.2
333.15	0.9992	0.2009	1193.6
333.15	0.9992	0.4003	1191.9
333.15	0.9992	0.6002	1192.0
333.15	0.9992	0.8000	1194.5
333.15	3.0006	0.0000	1205.0
333.15	3.0006	0.2010	1200.7
333.15	3.0006	0.4009	1197.5
333.15	3.0006	0.6010	1195.8
333.15	3.0006	0.8005	1196.1

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 (2) - Liquid	Mole fraction of Benzene, n-butyl- (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.3333	0.0000	0.0267
0.3333	0.2004	0.0267
0.3333	0.4004	0.0274
0.3333	0.6003	0.0277
0.3333	0.8002	0.0282
0.9992	0.0000	0.0269
0.9992	0.2009	0.0271
0.9992	0.4003	0.0274
0.9992	0.6002	0.0278
0.9992	0.8000	0.0281
3.0006	0.0000	0.0270
3.0006	0.2010	0.0271
3.0006	0.4009	0.0273
3.0006	0.6010	0.0276
3.0006	0.8005	0.0281

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 (2) - Liquid	Mole fraction of Benzene, n-butyl- (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.3333	0.0000	0.0267
0.3333	0.2004	0.0267
0.3333	0.4004	0.0274
0.3333	0.6003	0.0277
0.3333	0.8002	0.0282
0.9992	0.0000	0.0269
0.9992	0.2009	0.0271
0.9992	0.4003	0.0274
0.9992	0.6002	0.0278
0.9992	0.8000	0.0281
3.0006	0.0000	0.0270
3.0006	0.2010	0.0271
3.0006	0.4009	0.0273
3.0006	0.6010	0.0276
3.0006	0.8005	0.0281

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)