Mixture of Dodecane + 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 Dodecane (1) - Liquid	Mole fraction of Benzene, hexyl- (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.3332	0.0000	0.0013
293.15	0.3332	0.2008	0.0014
293.15	0.3332	0.4002	0.0014
293.15	0.3332	0.6001	0.0015
293.15	0.3332	0.8004	0.0016
293.15	1.0001	0.0000	0.0014
293.15	1.0001	0.2002	0.0014
293.15	1.0001	0.3999	0.0014
293.15	1.0001	0.5973	0.0015
293.15	1.0001	0.8000	0.0015
293.15	2.9949	0.0000	0.0014
293.15	2.9949	0.2008	0.0014
293.15	2.9949	0.3999	0.0014
293.15	2.9949	0.5999	0.0015
293.15	2.9949	0.8002	0.0016
303.15	0.3332	0.0000	0.0011
303.15	0.3332	0.2008	0.0011
303.15	0.3332	0.4002	0.0012
303.15	0.3332	0.6001	0.0012
303.15	0.3332	0.8004	0.0013
303.15	1.0001	0.0000	0.0012
303.15	1.0001	0.2002	0.0012
303.15	1.0001	0.3999	0.0012
303.15	1.0001	0.5973	0.0013
303.15	1.0001	0.8000	0.0013
303.15	2.9949	0.0000	0.0012
303.15	2.9949	0.2008	0.0012
303.15	2.9949	0.3999	0.0012
303.15	2.9949	0.5999	0.0013
303.15	2.9949	0.8002	0.0013
313.15	0.3332	0.0000	0.0010
313.15	0.3332	0.2008	0.0010
313.15	0.3332	0.4002	0.0010
313.15	0.3332	0.6001	0.0011
313.15	0.3332	0.8004	0.0011
313.15	1.0001	0.0000	0.0010
313.15	1.0001	0.2002	0.0010
313.15	1.0001	0.3999	0.0010
313.15	1.0001	0.5973	0.0011
313.15	1.0001	0.8000	0.0011
313.15	2.9949	0.0000	0.0010
313.15	2.9949	0.2008	0.0010
313.15	2.9949	0.3999	0.0010
313.15	2.9949	0.5999	0.0011
313.15	2.9949	0.8002	0.0011
323.15	0.3332	0.0000	0.0008
323.15	0.3332	0.2008	0.0009
323.15	0.3332	0.4002	0.0009
323.15	0.3332	0.6001	0.0009
323.15	0.3332	0.8004	0.0010
323.15	1.0001	0.0000	0.0009
323.15	1.0001	0.2002	0.0009
323.15	1.0001	0.3999	0.0009
323.15	1.0001	0.5973	0.0009
323.15	1.0001	0.8000	0.0010
323.15	2.9949	0.0000	0.0009
323.15	2.9949	0.2008	0.0009
323.15	2.9949	0.3999	0.0009
323.15	2.9949	0.5999	0.0009
323.15	2.9949	0.8002	0.0010
333.15	0.3332	0.0000	0.0007
333.15	0.3332	0.2008	0.0008
333.15	0.3332	0.4002	0.0008
333.15	0.3332	0.6001	0.0008
333.15	0.3332	0.8004	0.0008
333.15	1.0001	0.0000	0.0008
333.15	1.0001	0.2002	0.0008
333.15	1.0001	0.3999	0.0008
333.15	1.0001	0.5973	0.0008
333.15	1.0001	0.8000	0.0009
333.15	2.9949	0.0000	0.0008
333.15	2.9949	0.2008	0.0008
333.15	2.9949	0.3999	0.0008
333.15	2.9949	0.5999	0.0008
333.15	2.9949	0.8002	0.0009
343.15	0.3332	0.0000	0.0007
343.15	0.3332	0.2008	0.0007
343.15	0.3332	0.4002	0.0007
343.15	0.3332	0.6001	0.0007
343.15	0.3332	0.8004	0.0008
343.15	1.0001	0.0000	0.0007
343.15	1.0001	0.2002	0.0007
343.15	1.0001	0.3999	0.0007
343.15	1.0001	0.5973	0.0007
343.15	1.0001	0.8000	0.0008
343.15	2.9949	0.0000	0.0007
343.15	2.9949	0.2008	0.0007
343.15	2.9949	0.3999	0.0007
343.15	2.9949	0.5999	0.0007
343.15	2.9949	0.8002	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 Dodecane (1) - Liquid	Mole fraction of Benzene, hexyl- (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.3332	0.0000	0.0013
293.15	0.3332	0.2008	0.0014
293.15	0.3332	0.4002	0.0014
293.15	0.3332	0.6001	0.0015
293.15	0.3332	0.8004	0.0016
293.15	1.0001	0.0000	0.0014
293.15	1.0001	0.2002	0.0014
293.15	1.0001	0.3999	0.0014
293.15	1.0001	0.5973	0.0015
293.15	1.0001	0.8000	0.0015
293.15	2.9949	0.0000	0.0014
293.15	2.9949	0.2008	0.0014
293.15	2.9949	0.3999	0.0014
293.15	2.9949	0.5999	0.0015
293.15	2.9949	0.8002	0.0016
303.15	0.3332	0.0000	0.0011
303.15	0.3332	0.2008	0.0011
303.15	0.3332	0.4002	0.0012
303.15	0.3332	0.6001	0.0012
303.15	0.3332	0.8004	0.0013
303.15	1.0001	0.0000	0.0012
303.15	1.0001	0.2002	0.0012
303.15	1.0001	0.3999	0.0012
303.15	1.0001	0.5973	0.0013
303.15	1.0001	0.8000	0.0013
303.15	2.9949	0.0000	0.0012
303.15	2.9949	0.2008	0.0012
303.15	2.9949	0.3999	0.0012
303.15	2.9949	0.5999	0.0013
303.15	2.9949	0.8002	0.0013
313.15	0.3332	0.0000	0.0010
313.15	0.3332	0.2008	0.0010
313.15	0.3332	0.4002	0.0010
313.15	0.3332	0.6001	0.0011
313.15	0.3332	0.8004	0.0011
313.15	1.0001	0.0000	0.0010
313.15	1.0001	0.2002	0.0010
313.15	1.0001	0.3999	0.0010
313.15	1.0001	0.5973	0.0011
313.15	1.0001	0.8000	0.0011
313.15	2.9949	0.0000	0.0010
313.15	2.9949	0.2008	0.0010
313.15	2.9949	0.3999	0.0010
313.15	2.9949	0.5999	0.0011
313.15	2.9949	0.8002	0.0011
323.15	0.3332	0.0000	0.0008
323.15	0.3332	0.2008	0.0009
323.15	0.3332	0.4002	0.0009
323.15	0.3332	0.6001	0.0009
323.15	0.3332	0.8004	0.0010
323.15	1.0001	0.0000	0.0009
323.15	1.0001	0.2002	0.0009
323.15	1.0001	0.3999	0.0009
323.15	1.0001	0.5973	0.0009
323.15	1.0001	0.8000	0.0010
323.15	2.9949	0.0000	0.0009
323.15	2.9949	0.2008	0.0009
323.15	2.9949	0.3999	0.0009
323.15	2.9949	0.5999	0.0009
323.15	2.9949	0.8002	0.0010
333.15	0.3332	0.0000	0.0007
333.15	0.3332	0.2008	0.0008
333.15	0.3332	0.4002	0.0008
333.15	0.3332	0.6001	0.0008
333.15	0.3332	0.8004	0.0008
333.15	1.0001	0.0000	0.0008
333.15	1.0001	0.2002	0.0008
333.15	1.0001	0.3999	0.0008
333.15	1.0001	0.5973	0.0008
333.15	1.0001	0.8000	0.0009
333.15	2.9949	0.0000	0.0008
333.15	2.9949	0.2008	0.0008
333.15	2.9949	0.3999	0.0008
333.15	2.9949	0.5999	0.0008
333.15	2.9949	0.8002	0.0009
343.15	0.3332	0.0000	0.0007
343.15	0.3332	0.2008	0.0007
343.15	0.3332	0.4002	0.0007
343.15	0.3332	0.6001	0.0007
343.15	0.3332	0.8004	0.0008
343.15	1.0001	0.0000	0.0007
343.15	1.0001	0.2002	0.0007
343.15	1.0001	0.3999	0.0007
343.15	1.0001	0.5973	0.0007
343.15	1.0001	0.8000	0.0008
343.15	2.9949	0.0000	0.0007
343.15	2.9949	0.2008	0.0007
343.15	2.9949	0.3999	0.0007
343.15	2.9949	0.5999	0.0007
343.15	2.9949	0.8002	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 Dodecane (1) - Liquid	Mole fraction of Benzene, hexyl- (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.3332	0.0000	783.9
293.15	0.3332	0.2008	798.4
293.15	0.3332	0.4002	812.9
293.15	0.3332	0.6001	827.7
293.15	0.3332	0.8004	842.6
293.15	1.0001	0.0000	770.6
293.15	1.0001	0.2002	786.8
293.15	1.0001	0.3999	803.5
293.15	1.0001	0.5973	820.7
293.15	1.0001	0.8000	839.0
293.15	2.9949	0.0000	759.0
293.15	2.9949	0.2008	776.5
293.15	2.9949	0.3999	794.9
293.15	2.9949	0.5999	814.6
293.15	2.9949	0.8002	835.5
303.15	0.3332	0.0000	776.5
303.15	0.3332	0.2008	790.9
303.15	0.3332	0.4002	805.4
303.15	0.3332	0.6001	820.1
303.15	0.3332	0.8004	835.1
303.15	1.0001	0.0000	763.3
303.15	1.0001	0.2002	779.4
303.15	1.0001	0.3999	796.1
303.15	1.0001	0.5973	813.2
303.15	1.0001	0.8000	831.4
303.15	2.9949	0.0000	751.7
303.15	2.9949	0.2008	769.2
303.15	2.9949	0.3999	787.5
303.15	2.9949	0.5999	807.1
303.15	2.9949	0.8002	828.0
313.15	0.3332	0.0000	769.1
313.15	0.3332	0.2008	783.4
313.15	0.3332	0.4002	797.9
313.15	0.3332	0.6001	812.6
313.15	0.3332	0.8004	827.5
313.15	1.0001	0.0000	755.9
313.15	1.0001	0.2002	772.0
313.15	1.0001	0.3999	788.6
313.15	1.0001	0.5973	805.7
313.15	1.0001	0.8000	823.9
313.15	2.9949	0.0000	744.4
313.15	2.9949	0.2008	761.8
313.15	2.9949	0.3999	780.1
313.15	2.9949	0.5999	799.6
313.15	2.9949	0.8002	820.4
323.15	0.3332	0.0000	761.6
323.15	0.3332	0.2008	775.9
323.15	0.3332	0.4002	790.4
323.15	0.3332	0.6001	805.0
323.15	0.3332	0.8004	819.9
323.15	1.0001	0.0000	748.5
323.15	1.0001	0.2002	764.5
323.15	1.0001	0.3999	781.1
323.15	1.0001	0.5973	798.2
323.15	1.0001	0.8000	816.3
323.15	2.9949	0.0000	737.1
323.15	2.9949	0.2008	754.4
323.15	2.9949	0.3999	772.7
323.15	2.9949	0.5999	792.1
323.15	2.9949	0.8002	812.9
333.15	0.3332	0.0000	754.1
333.15	0.3332	0.2008	768.4
333.15	0.3332	0.4002	782.8
333.15	0.3332	0.6001	797.5
333.15	0.3332	0.8004	812.3
333.15	1.0001	0.0000	741.1
333.15	1.0001	0.2002	757.1
333.15	1.0001	0.3999	773.6
333.15	1.0001	0.5973	790.6
333.15	1.0001	0.8000	808.7
333.15	2.9949	0.0000	729.7
333.15	2.9949	0.2008	747.0
333.15	2.9949	0.3999	765.2
333.15	2.9949	0.5999	784.6
333.15	2.9949	0.8002	805.3
343.15	0.3332	0.0000	746.5
343.15	0.3332	0.2008	760.7
343.15	0.3332	0.4002	775.2
343.15	0.3332	0.6001	789.8
343.15	0.3332	0.8004	804.6
343.15	1.0001	0.0000	733.7
343.15	1.0001	0.2002	749.7
343.15	1.0001	0.3999	766.3
343.15	1.0001	0.5973	783.2
343.15	1.0001	0.8000	801.2
343.15	2.9949	0.0000	722.5
343.15	2.9949	0.2008	739.7
343.15	2.9949	0.3999	757.8
343.15	2.9949	0.5999	777.3
343.15	2.9949	0.8002	797.9

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 Dodecane (1) - Liquid	Mole fraction of Benzene, hexyl- (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.3332	0.0000	783.9
293.15	0.3332	0.2008	798.4
293.15	0.3332	0.4002	812.9
293.15	0.3332	0.6001	827.7
293.15	0.3332	0.8004	842.6
293.15	1.0001	0.0000	770.6
293.15	1.0001	0.2002	786.8
293.15	1.0001	0.3999	803.5
293.15	1.0001	0.5973	820.7
293.15	1.0001	0.8000	839.0
293.15	2.9949	0.0000	759.0
293.15	2.9949	0.2008	776.5
293.15	2.9949	0.3999	794.9
293.15	2.9949	0.5999	814.6
293.15	2.9949	0.8002	835.5
303.15	0.3332	0.0000	776.5
303.15	0.3332	0.2008	790.9
303.15	0.3332	0.4002	805.4
303.15	0.3332	0.6001	820.1
303.15	0.3332	0.8004	835.1
303.15	1.0001	0.0000	763.3
303.15	1.0001	0.2002	779.4
303.15	1.0001	0.3999	796.1
303.15	1.0001	0.5973	813.2
303.15	1.0001	0.8000	831.4
303.15	2.9949	0.0000	751.7
303.15	2.9949	0.2008	769.2
303.15	2.9949	0.3999	787.5
303.15	2.9949	0.5999	807.1
303.15	2.9949	0.8002	828.0
313.15	0.3332	0.0000	769.1
313.15	0.3332	0.2008	783.4
313.15	0.3332	0.4002	797.9
313.15	0.3332	0.6001	812.6
313.15	0.3332	0.8004	827.5
313.15	1.0001	0.0000	755.9
313.15	1.0001	0.2002	772.0
313.15	1.0001	0.3999	788.6
313.15	1.0001	0.5973	805.7
313.15	1.0001	0.8000	823.9
313.15	2.9949	0.0000	744.4
313.15	2.9949	0.2008	761.8
313.15	2.9949	0.3999	780.1
313.15	2.9949	0.5999	799.6
313.15	2.9949	0.8002	820.4
323.15	0.3332	0.0000	761.6
323.15	0.3332	0.2008	775.9
323.15	0.3332	0.4002	790.4
323.15	0.3332	0.6001	805.0
323.15	0.3332	0.8004	819.9
323.15	1.0001	0.0000	748.5
323.15	1.0001	0.2002	764.5
323.15	1.0001	0.3999	781.1
323.15	1.0001	0.5973	798.2
323.15	1.0001	0.8000	816.3
323.15	2.9949	0.0000	737.1
323.15	2.9949	0.2008	754.4
323.15	2.9949	0.3999	772.7
323.15	2.9949	0.5999	792.1
323.15	2.9949	0.8002	812.9
333.15	0.3332	0.0000	754.1
333.15	0.3332	0.2008	768.4
333.15	0.3332	0.4002	782.8
333.15	0.3332	0.6001	797.5
333.15	0.3332	0.8004	812.3
333.15	1.0001	0.0000	741.1
333.15	1.0001	0.2002	757.1
333.15	1.0001	0.3999	773.6
333.15	1.0001	0.5973	790.6
333.15	1.0001	0.8000	808.7
333.15	2.9949	0.0000	729.7
333.15	2.9949	0.2008	747.0
333.15	2.9949	0.3999	765.2
333.15	2.9949	0.5999	784.6
333.15	2.9949	0.8002	805.3
343.15	0.3332	0.0000	746.5
343.15	0.3332	0.2008	760.7
343.15	0.3332	0.4002	775.2
343.15	0.3332	0.6001	789.8
343.15	0.3332	0.8004	804.6
343.15	1.0001	0.0000	733.7
343.15	1.0001	0.2002	749.7
343.15	1.0001	0.3999	766.3
343.15	1.0001	0.5973	783.2
343.15	1.0001	0.8000	801.2
343.15	2.9949	0.0000	722.5
343.15	2.9949	0.2008	739.7
343.15	2.9949	0.3999	757.8
343.15	2.9949	0.5999	777.3
343.15	2.9949	0.8002	797.9

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 Dodecane (1) - Liquid	Mole fraction of Benzene, hexyl- (2) - Liquid	Speed of sound, m/s - Liquid
293.15	0.3332	0.0000	1317.3
293.15	0.3332	0.2008	1326.5
293.15	0.3332	0.4002	1337.1
293.15	0.3332	0.6001	1348.5
293.15	0.3332	0.8004	1361.1
293.15	1.0001	0.0000	1309.0
293.15	1.0001	0.2002	1319.1
293.15	1.0001	0.3999	1330.3
293.15	1.0001	0.5973	1343.3
293.15	1.0001	0.8000	1358.3
293.15	2.9949	0.0000	1302.4
293.15	2.9949	0.2008	1312.9
293.15	2.9949	0.3999	1325.0
293.15	2.9949	0.5999	1339.2
293.15	2.9949	0.8002	1355.8
303.15	0.3332	0.0000	1278.1
303.15	0.3332	0.2008	1287.8
303.15	0.3332	0.4002	1298.7
303.15	0.3332	0.6001	1310.5
303.15	0.3332	0.8004	1323.4
303.15	1.0001	0.0000	1270.4
303.15	1.0001	0.2002	1280.8
303.15	1.0001	0.3999	1292.2
303.15	1.0001	0.5973	1305.5
303.15	1.0001	0.8000	1320.6
303.15	2.9949	0.0000	1264.0
303.15	2.9949	0.2008	1274.8
303.15	2.9949	0.3999	1287.1
303.15	2.9949	0.5999	1301.5
303.15	2.9949	0.8002	1318.4
313.15	0.3332	0.0000	1239.7
313.15	0.3332	0.2008	1249.7
313.15	0.3332	0.4002	1261.0
313.15	0.3332	0.6001	1273.1
313.15	0.3332	0.8004	1286.3
313.15	1.0001	0.0000	1232.3
313.15	1.0001	0.2002	1243.1
313.15	1.0001	0.3999	1254.8
313.15	1.0001	0.5973	1268.2
313.15	1.0001	0.8000	1283.6
313.15	2.9949	0.0000	1226.2
313.15	2.9949	0.2008	1237.3
313.15	2.9949	0.3999	1249.9
313.15	2.9949	0.5999	1264.5
313.15	2.9949	0.8002	1281.4
323.15	0.3332	0.0000	1201.8
323.15	0.3332	0.2008	1212.3
323.15	0.3332	0.4002	1223.9
323.15	0.3332	0.6001	1236.3
323.15	0.3332	0.8004	1249.8
323.15	1.0001	0.0000	1194.8
323.15	1.0001	0.2002	1206.0
323.15	1.0001	0.3999	1217.9
323.15	1.0001	0.5973	1231.6
323.15	1.0001	0.8000	1247.1
323.15	2.9949	0.0000	1189.0
323.15	2.9949	0.2008	1200.4
323.15	2.9949	0.3999	1213.2
323.15	2.9949	0.5999	1228.0
323.15	2.9949	0.8002	1245.1
333.15	0.3332	0.0000	1164.7
333.15	0.3332	0.2008	1175.6
333.15	0.3332	0.4002	1187.5
333.15	0.3332	0.6001	1200.4
333.15	0.3332	0.8004	1214.2
333.15	1.0001	0.0000	1158.1
333.15	1.0001	0.2002	1169.6
333.15	1.0001	0.3999	1181.9
333.15	1.0001	0.5973	1195.9
333.15	1.0001	0.8000	1211.6
333.15	2.9949	0.0000	1152.5
333.15	2.9949	0.2008	1164.2
333.15	2.9949	0.3999	1177.3
333.15	2.9949	0.5999	1192.2
333.15	2.9949	0.8002	1209.5

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 Dodecane (1) - Liquid	Mole fraction of Benzene, hexyl- (2) - Liquid	Speed of sound, m/s - Liquid
293.15	0.3332	0.0000	1317.3
293.15	0.3332	0.2008	1326.5
293.15	0.3332	0.4002	1337.1
293.15	0.3332	0.6001	1348.5
293.15	0.3332	0.8004	1361.1
293.15	1.0001	0.0000	1309.0
293.15	1.0001	0.2002	1319.1
293.15	1.0001	0.3999	1330.3
293.15	1.0001	0.5973	1343.3
293.15	1.0001	0.8000	1358.3
293.15	2.9949	0.0000	1302.4
293.15	2.9949	0.2008	1312.9
293.15	2.9949	0.3999	1325.0
293.15	2.9949	0.5999	1339.2
293.15	2.9949	0.8002	1355.8
303.15	0.3332	0.0000	1278.1
303.15	0.3332	0.2008	1287.8
303.15	0.3332	0.4002	1298.7
303.15	0.3332	0.6001	1310.5
303.15	0.3332	0.8004	1323.4
303.15	1.0001	0.0000	1270.4
303.15	1.0001	0.2002	1280.8
303.15	1.0001	0.3999	1292.2
303.15	1.0001	0.5973	1305.5
303.15	1.0001	0.8000	1320.6
303.15	2.9949	0.0000	1264.0
303.15	2.9949	0.2008	1274.8
303.15	2.9949	0.3999	1287.1
303.15	2.9949	0.5999	1301.5
303.15	2.9949	0.8002	1318.4
313.15	0.3332	0.0000	1239.7
313.15	0.3332	0.2008	1249.7
313.15	0.3332	0.4002	1261.0
313.15	0.3332	0.6001	1273.1
313.15	0.3332	0.8004	1286.3
313.15	1.0001	0.0000	1232.3
313.15	1.0001	0.2002	1243.1
313.15	1.0001	0.3999	1254.8
313.15	1.0001	0.5973	1268.2
313.15	1.0001	0.8000	1283.6
313.15	2.9949	0.0000	1226.2
313.15	2.9949	0.2008	1237.3
313.15	2.9949	0.3999	1249.9
313.15	2.9949	0.5999	1264.5
313.15	2.9949	0.8002	1281.4
323.15	0.3332	0.0000	1201.8
323.15	0.3332	0.2008	1212.3
323.15	0.3332	0.4002	1223.9
323.15	0.3332	0.6001	1236.3
323.15	0.3332	0.8004	1249.8
323.15	1.0001	0.0000	1194.8
323.15	1.0001	0.2002	1206.0
323.15	1.0001	0.3999	1217.9
323.15	1.0001	0.5973	1231.6
323.15	1.0001	0.8000	1247.1
323.15	2.9949	0.0000	1189.0
323.15	2.9949	0.2008	1200.4
323.15	2.9949	0.3999	1213.2
323.15	2.9949	0.5999	1228.0
323.15	2.9949	0.8002	1245.1
333.15	0.3332	0.0000	1164.7
333.15	0.3332	0.2008	1175.6
333.15	0.3332	0.4002	1187.5
333.15	0.3332	0.6001	1200.4
333.15	0.3332	0.8004	1214.2
333.15	1.0001	0.0000	1158.1
333.15	1.0001	0.2002	1169.6
333.15	1.0001	0.3999	1181.9
333.15	1.0001	0.5973	1195.9
333.15	1.0001	0.8000	1211.6
333.15	2.9949	0.0000	1152.5
333.15	2.9949	0.2008	1164.2
333.15	2.9949	0.3999	1177.3
333.15	2.9949	0.5999	1192.2
333.15	2.9949	0.8002	1209.5

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 Dodecane (1) - Liquid	Mole fraction of Benzene, hexyl- (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.3335	0.0000	0.0261
0.3335	0.2001	0.0267
0.3335	0.4002	0.0269
0.3335	0.6000	0.0277
0.3335	0.7997	0.0283
0.9998	0.0000	0.0258
0.9998	0.1999	0.0263
0.9998	0.4002	0.0269
0.9998	0.6001	0.0276
0.9998	0.7999	0.0280
2.9968	0.0000	0.0254
2.9968	0.1999	0.0259
2.9968	0.4002	0.0264
2.9968	0.5998	0.0271
2.9968	0.7998	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 Dodecane (1) - Liquid	Mole fraction of Benzene, hexyl- (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.3335	0.0000	0.0261
0.3335	0.2001	0.0267
0.3335	0.4002	0.0269
0.3335	0.6000	0.0277
0.3335	0.7997	0.0283
0.9998	0.0000	0.0258
0.9998	0.1999	0.0263
0.9998	0.4002	0.0269
0.9998	0.6001	0.0276
0.9998	0.7999	0.0280
2.9968	0.0000	0.0254
2.9968	0.1999	0.0259
2.9968	0.4002	0.0264
2.9968	0.5998	0.0271
2.9968	0.7998	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)