Operational condition: Pressure, kPa = 102 (Liquid)
Fixed | Measured | ||
---|---|---|---|
Temperature, K - Liquid | Solvent: Amount ratio of component to other component of binary solvent of Dodecane (2) - Liquid | Mole fraction of Benzene, n-butyl- (1) - Liquid | Viscosity, Pa*s - Liquid |
293.15 | 0.3332 | 0.0000 | 0.0013 |
293.15 | 0.3332 | 0.2001 | 0.0012 |
293.15 | 0.3332 | 0.4003 | 0.0011 |
293.15 | 0.3332 | 0.6003 | 0.0011 |
293.15 | 0.3332 | 0.8000 | 0.0011 |
293.15 | 1.0002 | 0.0000 | 0.0014 |
293.15 | 1.0002 | 0.2005 | 0.0013 |
293.15 | 1.0002 | 0.4007 | 0.0012 |
293.15 | 1.0002 | 0.6008 | 0.0011 |
293.15 | 1.0002 | 0.8005 | 0.0011 |
293.15 | 3.0005 | 0.0000 | 0.0014 |
293.15 | 3.0005 | 0.2007 | 0.0013 |
293.15 | 3.0005 | 0.4011 | 0.0012 |
293.15 | 3.0005 | 0.6013 | 0.0011 |
293.15 | 3.0005 | 0.8007 | 0.0011 |
303.15 | 0.3332 | 0.0000 | 0.0011 |
303.15 | 0.3332 | 0.2001 | 0.0010 |
303.15 | 0.3332 | 0.4003 | 0.0010 |
303.15 | 0.3332 | 0.6003 | 0.0010 |
303.15 | 0.3332 | 0.8000 | 0.0009 |
303.15 | 1.0002 | 0.0000 | 0.0012 |
303.15 | 1.0002 | 0.2005 | 0.0011 |
303.15 | 1.0002 | 0.4007 | 0.0010 |
303.15 | 1.0002 | 0.6008 | 0.0010 |
303.15 | 1.0002 | 0.8005 | 0.0009 |
303.15 | 3.0005 | 0.0000 | 0.0012 |
303.15 | 3.0005 | 0.2007 | 0.0011 |
303.15 | 3.0005 | 0.4011 | 0.0010 |
303.15 | 3.0005 | 0.6013 | 0.0010 |
303.15 | 3.0005 | 0.8007 | 0.0009 |
313.15 | 0.3332 | 0.0000 | 0.0010 |
313.15 | 0.3332 | 0.2001 | 0.0009 |
313.15 | 0.3332 | 0.4003 | 0.0009 |
313.15 | 0.3332 | 0.6003 | 0.0008 |
313.15 | 0.3332 | 0.8000 | 0.0008 |
313.15 | 1.0002 | 0.0000 | 0.0010 |
313.15 | 1.0002 | 0.2005 | 0.0009 |
313.15 | 1.0002 | 0.4007 | 0.0009 |
313.15 | 1.0002 | 0.6008 | 0.0008 |
313.15 | 1.0002 | 0.8005 | 0.0008 |
313.15 | 3.0005 | 0.0000 | 0.0010 |
313.15 | 3.0005 | 0.2007 | 0.0009 |
313.15 | 3.0005 | 0.4011 | 0.0009 |
313.15 | 3.0005 | 0.6013 | 0.0008 |
313.15 | 3.0005 | 0.8007 | 0.0008 |
323.15 | 0.3332 | 0.0000 | 0.0008 |
323.15 | 0.3332 | 0.2001 | 0.0008 |
323.15 | 0.3332 | 0.4003 | 0.0008 |
323.15 | 0.3332 | 0.6003 | 0.0007 |
323.15 | 0.3332 | 0.8000 | 0.0007 |
323.15 | 1.0002 | 0.0000 | 0.0009 |
323.15 | 1.0002 | 0.2005 | 0.0008 |
323.15 | 1.0002 | 0.4007 | 0.0008 |
323.15 | 1.0002 | 0.6008 | 0.0007 |
323.15 | 1.0002 | 0.8005 | 0.0007 |
323.15 | 3.0005 | 0.0000 | 0.0009 |
323.15 | 3.0005 | 0.2007 | 0.0008 |
323.15 | 3.0005 | 0.4011 | 0.0008 |
323.15 | 3.0005 | 0.6013 | 0.0007 |
323.15 | 3.0005 | 0.8007 | 0.0007 |
333.15 | 0.3332 | 0.0000 | 0.0007 |
333.15 | 0.3332 | 0.2001 | 0.0007 |
333.15 | 0.3332 | 0.4003 | 0.0007 |
333.15 | 0.3332 | 0.6003 | 0.0006 |
333.15 | 0.3332 | 0.8000 | 0.0006 |
333.15 | 1.0002 | 0.0000 | 0.0008 |
333.15 | 1.0002 | 0.2005 | 0.0007 |
333.15 | 1.0002 | 0.4007 | 0.0007 |
333.15 | 1.0002 | 0.6008 | 0.0007 |
333.15 | 1.0002 | 0.8005 | 0.0006 |
333.15 | 3.0005 | 0.0000 | 0.0008 |
333.15 | 3.0005 | 0.2007 | 0.0007 |
333.15 | 3.0005 | 0.4011 | 0.0007 |
333.15 | 3.0005 | 0.6013 | 0.0007 |
333.15 | 3.0005 | 0.8007 | 0.0006 |
343.15 | 0.3332 | 0.0000 | 0.0007 |
343.15 | 0.3332 | 0.2001 | 0.0006 |
343.15 | 0.3332 | 0.4003 | 0.0006 |
343.15 | 0.3332 | 0.6003 | 0.0006 |
343.15 | 0.3332 | 0.8000 | 0.0006 |
343.15 | 1.0002 | 0.0000 | 0.0007 |
343.15 | 1.0002 | 0.2005 | 0.0006 |
343.15 | 1.0002 | 0.4007 | 0.0006 |
343.15 | 1.0002 | 0.6008 | 0.0006 |
343.15 | 1.0002 | 0.8005 | 0.0006 |
343.15 | 3.0005 | 0.0000 | 0.0007 |
343.15 | 3.0005 | 0.2007 | 0.0006 |
343.15 | 3.0005 | 0.4011 | 0.0006 |
343.15 | 3.0005 | 0.6013 | 0.0006 |
343.15 | 3.0005 | 0.8007 | 0.0006 |
Operational condition: Pressure, kPa = 102 (Liquid)
Fixed | Measured | ||
---|---|---|---|
Temperature, K - Liquid | Mole fraction of Dodecane (2) - Liquid | Mole fraction of Cyclohexane, butyl- (3) - Liquid | Viscosity, Pa*s - Liquid |
253.15 | 0.2000 | 0.4500 | 0.0027 |
293.15 | 0.2000 | 0.4500 | 0.0012 |
303.15 | 0.2000 | 0.4500 | 0.0010 |
313.15 | 0.2000 | 0.4500 | 0.0009 |
323.15 | 0.2000 | 0.4500 | 0.0008 |
333.15 | 0.2000 | 0.4500 | 0.0007 |
253.15 | 0.3333 | 0.3333 | 0.0028 |
293.15 | 0.3333 | 0.3333 | 0.0012 |
303.15 | 0.3333 | 0.3333 | 0.0010 |
313.15 | 0.3333 | 0.3333 | 0.0009 |
323.15 | 0.3333 | 0.3333 | 0.0008 |
333.15 | 0.3333 | 0.3333 | 0.0007 |
Operational condition: Pressure, kPa = 102 (Liquid)
Fixed | Measured | ||
---|---|---|---|
Temperature, K - Liquid | Solvent: Amount ratio of component to other component of binary solvent of Dodecane (2) - Liquid | Mole fraction of Benzene, n-butyl- (1) - Liquid | Viscosity, Pa*s - Liquid |
293.15 | 0.3332 | 0.0000 | 0.0013 |
293.15 | 0.3332 | 0.2001 | 0.0012 |
293.15 | 0.3332 | 0.4003 | 0.0011 |
293.15 | 0.3332 | 0.6003 | 0.0011 |
293.15 | 0.3332 | 0.8000 | 0.0011 |
293.15 | 1.0002 | 0.0000 | 0.0014 |
293.15 | 1.0002 | 0.2005 | 0.0013 |
293.15 | 1.0002 | 0.4007 | 0.0012 |
293.15 | 1.0002 | 0.6008 | 0.0011 |
293.15 | 1.0002 | 0.8005 | 0.0011 |
293.15 | 3.0005 | 0.0000 | 0.0014 |
293.15 | 3.0005 | 0.2007 | 0.0013 |
293.15 | 3.0005 | 0.4011 | 0.0012 |
293.15 | 3.0005 | 0.6013 | 0.0011 |
293.15 | 3.0005 | 0.8007 | 0.0011 |
303.15 | 0.3332 | 0.0000 | 0.0011 |
303.15 | 0.3332 | 0.2001 | 0.0010 |
303.15 | 0.3332 | 0.4003 | 0.0010 |
303.15 | 0.3332 | 0.6003 | 0.0010 |
303.15 | 0.3332 | 0.8000 | 0.0009 |
303.15 | 1.0002 | 0.0000 | 0.0012 |
303.15 | 1.0002 | 0.2005 | 0.0011 |
303.15 | 1.0002 | 0.4007 | 0.0010 |
303.15 | 1.0002 | 0.6008 | 0.0010 |
303.15 | 1.0002 | 0.8005 | 0.0009 |
303.15 | 3.0005 | 0.0000 | 0.0012 |
303.15 | 3.0005 | 0.2007 | 0.0011 |
303.15 | 3.0005 | 0.4011 | 0.0010 |
303.15 | 3.0005 | 0.6013 | 0.0010 |
303.15 | 3.0005 | 0.8007 | 0.0009 |
313.15 | 0.3332 | 0.0000 | 0.0010 |
313.15 | 0.3332 | 0.2001 | 0.0009 |
313.15 | 0.3332 | 0.4003 | 0.0009 |
313.15 | 0.3332 | 0.6003 | 0.0008 |
313.15 | 0.3332 | 0.8000 | 0.0008 |
313.15 | 1.0002 | 0.0000 | 0.0010 |
313.15 | 1.0002 | 0.2005 | 0.0009 |
313.15 | 1.0002 | 0.4007 | 0.0009 |
313.15 | 1.0002 | 0.6008 | 0.0008 |
313.15 | 1.0002 | 0.8005 | 0.0008 |
313.15 | 3.0005 | 0.0000 | 0.0010 |
313.15 | 3.0005 | 0.2007 | 0.0009 |
313.15 | 3.0005 | 0.4011 | 0.0009 |
313.15 | 3.0005 | 0.6013 | 0.0008 |
313.15 | 3.0005 | 0.8007 | 0.0008 |
323.15 | 0.3332 | 0.0000 | 0.0008 |
323.15 | 0.3332 | 0.2001 | 0.0008 |
323.15 | 0.3332 | 0.4003 | 0.0008 |
323.15 | 0.3332 | 0.6003 | 0.0007 |
323.15 | 0.3332 | 0.8000 | 0.0007 |
323.15 | 1.0002 | 0.0000 | 0.0009 |
323.15 | 1.0002 | 0.2005 | 0.0008 |
323.15 | 1.0002 | 0.4007 | 0.0008 |
323.15 | 1.0002 | 0.6008 | 0.0007 |
323.15 | 1.0002 | 0.8005 | 0.0007 |
323.15 | 3.0005 | 0.0000 | 0.0009 |
323.15 | 3.0005 | 0.2007 | 0.0008 |
323.15 | 3.0005 | 0.4011 | 0.0008 |
323.15 | 3.0005 | 0.6013 | 0.0007 |
323.15 | 3.0005 | 0.8007 | 0.0007 |
333.15 | 0.3332 | 0.0000 | 0.0007 |
333.15 | 0.3332 | 0.2001 | 0.0007 |
333.15 | 0.3332 | 0.4003 | 0.0007 |
333.15 | 0.3332 | 0.6003 | 0.0006 |
333.15 | 0.3332 | 0.8000 | 0.0006 |
333.15 | 1.0002 | 0.0000 | 0.0008 |
333.15 | 1.0002 | 0.2005 | 0.0007 |
333.15 | 1.0002 | 0.4007 | 0.0007 |
333.15 | 1.0002 | 0.6008 | 0.0007 |
333.15 | 1.0002 | 0.8005 | 0.0006 |
333.15 | 3.0005 | 0.0000 | 0.0008 |
333.15 | 3.0005 | 0.2007 | 0.0007 |
333.15 | 3.0005 | 0.4011 | 0.0007 |
333.15 | 3.0005 | 0.6013 | 0.0007 |
333.15 | 3.0005 | 0.8007 | 0.0006 |
343.15 | 0.3332 | 0.0000 | 0.0007 |
343.15 | 0.3332 | 0.2001 | 0.0006 |
343.15 | 0.3332 | 0.4003 | 0.0006 |
343.15 | 0.3332 | 0.6003 | 0.0006 |
343.15 | 0.3332 | 0.8000 | 0.0006 |
343.15 | 1.0002 | 0.0000 | 0.0007 |
343.15 | 1.0002 | 0.2005 | 0.0006 |
343.15 | 1.0002 | 0.4007 | 0.0006 |
343.15 | 1.0002 | 0.6008 | 0.0006 |
343.15 | 1.0002 | 0.8005 | 0.0006 |
343.15 | 3.0005 | 0.0000 | 0.0007 |
343.15 | 3.0005 | 0.2007 | 0.0006 |
343.15 | 3.0005 | 0.4011 | 0.0006 |
343.15 | 3.0005 | 0.6013 | 0.0006 |
343.15 | 3.0005 | 0.8007 | 0.0006 |
Operational condition: Pressure, kPa = 102 (Liquid)
Fixed | Measured | ||
---|---|---|---|
Temperature, K - Liquid | Mole fraction of Dodecane (2) - Liquid | Mole fraction of Cyclohexane, butyl- (3) - Liquid | Viscosity, Pa*s - Liquid |
253.15 | 0.2000 | 0.4500 | 0.0027 |
293.15 | 0.2000 | 0.4500 | 0.0012 |
303.15 | 0.2000 | 0.4500 | 0.0010 |
313.15 | 0.2000 | 0.4500 | 0.0009 |
323.15 | 0.2000 | 0.4500 | 0.0008 |
333.15 | 0.2000 | 0.4500 | 0.0007 |
253.15 | 0.3333 | 0.3333 | 0.0028 |
293.15 | 0.3333 | 0.3333 | 0.0012 |
303.15 | 0.3333 | 0.3333 | 0.0010 |
313.15 | 0.3333 | 0.3333 | 0.0009 |
323.15 | 0.3333 | 0.3333 | 0.0008 |
333.15 | 0.3333 | 0.3333 | 0.0007 |
Operational condition: Pressure, kPa = 102 (Liquid)
Fixed | Measured | ||
---|---|---|---|
Temperature, K - Liquid | Solvent: Amount ratio of component to other component of binary solvent of Dodecane (2) - Liquid | Mole fraction of Benzene, n-butyl- (1) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.3332 | 0.0000 | 783.9 |
293.15 | 0.3332 | 0.2001 | 796.4 |
293.15 | 0.3332 | 0.4003 | 810.2 |
293.15 | 0.3332 | 0.6003 | 825.4 |
293.15 | 0.3332 | 0.8000 | 842.1 |
293.15 | 1.0002 | 0.0000 | 770.6 |
293.15 | 1.0002 | 0.2005 | 784.6 |
293.15 | 1.0002 | 0.4007 | 800.3 |
293.15 | 1.0002 | 0.6008 | 817.9 |
293.15 | 1.0002 | 0.8005 | 838.0 |
293.15 | 3.0005 | 0.0000 | 759.0 |
293.15 | 3.0005 | 0.2007 | 774.0 |
293.15 | 3.0005 | 0.4011 | 791.1 |
293.15 | 3.0005 | 0.6013 | 810.8 |
293.15 | 3.0005 | 0.8007 | 833.6 |
303.15 | 0.3332 | 0.0000 | 776.5 |
303.15 | 0.3332 | 0.2001 | 788.9 |
303.15 | 0.3332 | 0.4003 | 802.6 |
303.15 | 0.3332 | 0.6003 | 817.6 |
303.15 | 0.3332 | 0.8000 | 834.2 |
303.15 | 1.0002 | 0.0000 | 763.3 |
303.15 | 1.0002 | 0.2005 | 777.2 |
303.15 | 1.0002 | 0.4007 | 792.7 |
303.15 | 1.0002 | 0.6008 | 810.2 |
303.15 | 1.0002 | 0.8005 | 830.1 |
303.15 | 3.0005 | 0.0000 | 751.7 |
303.15 | 3.0005 | 0.2007 | 766.6 |
303.15 | 3.0005 | 0.4011 | 783.6 |
303.15 | 3.0005 | 0.6013 | 803.2 |
303.15 | 3.0005 | 0.8007 | 825.8 |
313.15 | 0.3332 | 0.0000 | 769.1 |
313.15 | 0.3332 | 0.2001 | 781.4 |
313.15 | 0.3332 | 0.4003 | 794.9 |
313.15 | 0.3332 | 0.6003 | 809.8 |
313.15 | 0.3332 | 0.8000 | 826.3 |
313.15 | 1.0002 | 0.0000 | 755.9 |
313.15 | 1.0002 | 0.2005 | 769.7 |
313.15 | 1.0002 | 0.4007 | 785.1 |
313.15 | 1.0002 | 0.6008 | 802.5 |
313.15 | 1.0002 | 0.8005 | 822.2 |
313.15 | 3.0005 | 0.0000 | 744.4 |
313.15 | 3.0005 | 0.2007 | 759.2 |
313.15 | 3.0005 | 0.4011 | 776.0 |
313.15 | 3.0005 | 0.6013 | 795.5 |
313.15 | 3.0005 | 0.8007 | 817.9 |
323.15 | 0.3332 | 0.0000 | 761.6 |
323.15 | 0.3332 | 0.2001 | 773.8 |
323.15 | 0.3332 | 0.4003 | 787.2 |
323.15 | 0.3332 | 0.6003 | 802.0 |
323.15 | 0.3332 | 0.8000 | 818.3 |
323.15 | 1.0002 | 0.0000 | 748.5 |
323.15 | 1.0002 | 0.2005 | 762.2 |
323.15 | 1.0002 | 0.4007 | 777.5 |
323.15 | 1.0002 | 0.6008 | 794.7 |
323.15 | 1.0002 | 0.8005 | 814.3 |
323.15 | 3.0005 | 0.0000 | 737.1 |
323.15 | 3.0005 | 0.2007 | 751.7 |
323.15 | 3.0005 | 0.4011 | 768.5 |
323.15 | 3.0005 | 0.6013 | 787.7 |
323.15 | 3.0005 | 0.8007 | 810.1 |
333.15 | 0.3332 | 0.0000 | 754.1 |
333.15 | 0.3332 | 0.2001 | 766.2 |
333.15 | 0.3332 | 0.4003 | 779.5 |
333.15 | 0.3332 | 0.6003 | 794.2 |
333.15 | 0.3332 | 0.8000 | 810.4 |
333.15 | 1.0002 | 0.0000 | 741.1 |
333.15 | 1.0002 | 0.2005 | 754.6 |
333.15 | 1.0002 | 0.4007 | 769.8 |
333.15 | 1.0002 | 0.6008 | 786.9 |
333.15 | 1.0002 | 0.8005 | 806.3 |
333.15 | 3.0005 | 0.0000 | 729.7 |
333.15 | 3.0005 | 0.2007 | 744.2 |
333.15 | 3.0005 | 0.4011 | 760.8 |
333.15 | 3.0005 | 0.6013 | 780.0 |
333.15 | 3.0005 | 0.8007 | 802.1 |
343.15 | 0.3332 | 0.0000 | 746.5 |
343.15 | 0.3332 | 0.2001 | 758.4 |
343.15 | 0.3332 | 0.4003 | 771.7 |
343.15 | 0.3332 | 0.6003 | 786.2 |
343.15 | 0.3332 | 0.8000 | 802.3 |
343.15 | 1.0002 | 0.0000 | 733.6 |
343.15 | 1.0002 | 0.2005 | 747.0 |
343.15 | 1.0002 | 0.4007 | 762.1 |
343.15 | 1.0002 | 0.6008 | 779.1 |
343.15 | 1.0002 | 0.8005 | 798.3 |
343.15 | 3.0005 | 0.0000 | 722.2 |
343.15 | 3.0005 | 0.2007 | 736.1 |
343.15 | 3.0005 | 0.4011 | 753.1 |
343.15 | 3.0005 | 0.6013 | 772.1 |
343.15 | 3.0005 | 0.8007 | 794.1 |
Operational condition: Pressure, kPa = 102 (Liquid)
Fixed | Measured | ||
---|---|---|---|
Temperature, K - Liquid | Mole fraction of Dodecane (2) - Liquid | Mole fraction of Cyclohexane, butyl- (3) - Liquid | Mass density, kg/m3 - Liquid |
253.15 | 0.2000 | 0.4500 | 834.0 |
288.15 | 0.2000 | 0.4500 | 807.9 |
293.15 | 0.2000 | 0.4500 | 804.1 |
298.15 | 0.2000 | 0.4500 | 800.3 |
303.15 | 0.2000 | 0.4500 | 796.5 |
313.15 | 0.2000 | 0.4500 | 788.9 |
323.15 | 0.2000 | 0.4500 | 781.3 |
333.15 | 0.2000 | 0.4500 | 773.6 |
253.15 | 0.2500 | 0.4000 | 831.0 |
288.15 | 0.2500 | 0.4000 | 804.6 |
293.15 | 0.2500 | 0.4000 | 800.8 |
298.15 | 0.2500 | 0.4000 | 797.1 |
303.15 | 0.2500 | 0.4000 | 793.3 |
313.15 | 0.2500 | 0.4000 | 785.7 |
323.15 | 0.2500 | 0.4000 | 778.1 |
333.15 | 0.2500 | 0.4000 | 770.4 |
253.15 | 0.3333 | 0.3333 | 825.0 |
288.15 | 0.3333 | 0.3333 | 798.5 |
293.15 | 0.3333 | 0.3333 | 794.8 |
298.15 | 0.3333 | 0.3333 | 791.0 |
303.15 | 0.3333 | 0.3333 | 787.3 |
313.15 | 0.3333 | 0.3333 | 779.7 |
323.15 | 0.3333 | 0.3333 | 772.1 |
333.15 | 0.3333 | 0.3333 | 764.5 |
Operational condition: Pressure, kPa = 102 (Liquid)
Fixed | Measured | ||
---|---|---|---|
Temperature, K - Liquid | Solvent: Amount ratio of component to other component of binary solvent of Dodecane (2) - Liquid | Mole fraction of Benzene, n-butyl- (1) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.3332 | 0.0000 | 783.9 |
293.15 | 0.3332 | 0.2001 | 796.4 |
293.15 | 0.3332 | 0.4003 | 810.2 |
293.15 | 0.3332 | 0.6003 | 825.4 |
293.15 | 0.3332 | 0.8000 | 842.1 |
293.15 | 1.0002 | 0.0000 | 770.6 |
293.15 | 1.0002 | 0.2005 | 784.6 |
293.15 | 1.0002 | 0.4007 | 800.3 |
293.15 | 1.0002 | 0.6008 | 817.9 |
293.15 | 1.0002 | 0.8005 | 838.0 |
293.15 | 3.0005 | 0.0000 | 759.0 |
293.15 | 3.0005 | 0.2007 | 774.0 |
293.15 | 3.0005 | 0.4011 | 791.1 |
293.15 | 3.0005 | 0.6013 | 810.8 |
293.15 | 3.0005 | 0.8007 | 833.6 |
303.15 | 0.3332 | 0.0000 | 776.5 |
303.15 | 0.3332 | 0.2001 | 788.9 |
303.15 | 0.3332 | 0.4003 | 802.6 |
303.15 | 0.3332 | 0.6003 | 817.6 |
303.15 | 0.3332 | 0.8000 | 834.2 |
303.15 | 1.0002 | 0.0000 | 763.3 |
303.15 | 1.0002 | 0.2005 | 777.2 |
303.15 | 1.0002 | 0.4007 | 792.7 |
303.15 | 1.0002 | 0.6008 | 810.2 |
303.15 | 1.0002 | 0.8005 | 830.1 |
303.15 | 3.0005 | 0.0000 | 751.7 |
303.15 | 3.0005 | 0.2007 | 766.6 |
303.15 | 3.0005 | 0.4011 | 783.6 |
303.15 | 3.0005 | 0.6013 | 803.2 |
303.15 | 3.0005 | 0.8007 | 825.8 |
313.15 | 0.3332 | 0.0000 | 769.1 |
313.15 | 0.3332 | 0.2001 | 781.4 |
313.15 | 0.3332 | 0.4003 | 794.9 |
313.15 | 0.3332 | 0.6003 | 809.8 |
313.15 | 0.3332 | 0.8000 | 826.3 |
313.15 | 1.0002 | 0.0000 | 755.9 |
313.15 | 1.0002 | 0.2005 | 769.7 |
313.15 | 1.0002 | 0.4007 | 785.1 |
313.15 | 1.0002 | 0.6008 | 802.5 |
313.15 | 1.0002 | 0.8005 | 822.2 |
313.15 | 3.0005 | 0.0000 | 744.4 |
313.15 | 3.0005 | 0.2007 | 759.2 |
313.15 | 3.0005 | 0.4011 | 776.0 |
313.15 | 3.0005 | 0.6013 | 795.5 |
313.15 | 3.0005 | 0.8007 | 817.9 |
323.15 | 0.3332 | 0.0000 | 761.6 |
323.15 | 0.3332 | 0.2001 | 773.8 |
323.15 | 0.3332 | 0.4003 | 787.2 |
323.15 | 0.3332 | 0.6003 | 802.0 |
323.15 | 0.3332 | 0.8000 | 818.3 |
323.15 | 1.0002 | 0.0000 | 748.5 |
323.15 | 1.0002 | 0.2005 | 762.2 |
323.15 | 1.0002 | 0.4007 | 777.5 |
323.15 | 1.0002 | 0.6008 | 794.7 |
323.15 | 1.0002 | 0.8005 | 814.3 |
323.15 | 3.0005 | 0.0000 | 737.1 |
323.15 | 3.0005 | 0.2007 | 751.7 |
323.15 | 3.0005 | 0.4011 | 768.5 |
323.15 | 3.0005 | 0.6013 | 787.7 |
323.15 | 3.0005 | 0.8007 | 810.1 |
333.15 | 0.3332 | 0.0000 | 754.1 |
333.15 | 0.3332 | 0.2001 | 766.2 |
333.15 | 0.3332 | 0.4003 | 779.5 |
333.15 | 0.3332 | 0.6003 | 794.2 |
333.15 | 0.3332 | 0.8000 | 810.4 |
333.15 | 1.0002 | 0.0000 | 741.1 |
333.15 | 1.0002 | 0.2005 | 754.6 |
333.15 | 1.0002 | 0.4007 | 769.8 |
333.15 | 1.0002 | 0.6008 | 786.9 |
333.15 | 1.0002 | 0.8005 | 806.3 |
333.15 | 3.0005 | 0.0000 | 729.7 |
333.15 | 3.0005 | 0.2007 | 744.2 |
333.15 | 3.0005 | 0.4011 | 760.8 |
333.15 | 3.0005 | 0.6013 | 780.0 |
333.15 | 3.0005 | 0.8007 | 802.1 |
343.15 | 0.3332 | 0.0000 | 746.5 |
343.15 | 0.3332 | 0.2001 | 758.4 |
343.15 | 0.3332 | 0.4003 | 771.7 |
343.15 | 0.3332 | 0.6003 | 786.2 |
343.15 | 0.3332 | 0.8000 | 802.3 |
343.15 | 1.0002 | 0.0000 | 733.6 |
343.15 | 1.0002 | 0.2005 | 747.0 |
343.15 | 1.0002 | 0.4007 | 762.1 |
343.15 | 1.0002 | 0.6008 | 779.1 |
343.15 | 1.0002 | 0.8005 | 798.3 |
343.15 | 3.0005 | 0.0000 | 722.2 |
343.15 | 3.0005 | 0.2007 | 736.1 |
343.15 | 3.0005 | 0.4011 | 753.1 |
343.15 | 3.0005 | 0.6013 | 772.1 |
343.15 | 3.0005 | 0.8007 | 794.1 |
Operational condition: Pressure, kPa = 102 (Liquid)
Fixed | Measured | ||
---|---|---|---|
Temperature, K - Liquid | Mole fraction of Dodecane (2) - Liquid | Mole fraction of Cyclohexane, butyl- (3) - Liquid | Mass density, kg/m3 - Liquid |
253.15 | 0.2000 | 0.4500 | 834.0 |
288.15 | 0.2000 | 0.4500 | 807.9 |
293.15 | 0.2000 | 0.4500 | 804.1 |
298.15 | 0.2000 | 0.4500 | 800.3 |
303.15 | 0.2000 | 0.4500 | 796.5 |
313.15 | 0.2000 | 0.4500 | 788.9 |
323.15 | 0.2000 | 0.4500 | 781.3 |
333.15 | 0.2000 | 0.4500 | 773.6 |
253.15 | 0.2500 | 0.4000 | 831.0 |
288.15 | 0.2500 | 0.4000 | 804.6 |
293.15 | 0.2500 | 0.4000 | 800.8 |
298.15 | 0.2500 | 0.4000 | 797.1 |
303.15 | 0.2500 | 0.4000 | 793.3 |
313.15 | 0.2500 | 0.4000 | 785.7 |
323.15 | 0.2500 | 0.4000 | 778.1 |
333.15 | 0.2500 | 0.4000 | 770.4 |
253.15 | 0.3333 | 0.3333 | 825.0 |
288.15 | 0.3333 | 0.3333 | 798.5 |
293.15 | 0.3333 | 0.3333 | 794.8 |
298.15 | 0.3333 | 0.3333 | 791.0 |
303.15 | 0.3333 | 0.3333 | 787.3 |
313.15 | 0.3333 | 0.3333 | 779.7 |
323.15 | 0.3333 | 0.3333 | 772.1 |
333.15 | 0.3333 | 0.3333 | 764.5 |
Operational conditions:
Fixed | Measured | ||
---|---|---|---|
Temperature, K - Liquid | Solvent: Amount ratio of component to other component of binary solvent of Dodecane (2) - Liquid | Mole fraction of Benzene, n-butyl- (1) - Liquid | Speed of sound, m/s - Liquid |
293.15 | 0.3332 | 0.0000 | 1317.5 |
293.15 | 0.3332 | 0.2001 | 1319.8 |
293.15 | 0.3332 | 0.4003 | 1324.5 |
293.15 | 0.3332 | 0.6003 | 1331.0 |
293.15 | 0.3332 | 0.8000 | 1340.2 |
293.15 | 1.0002 | 0.0000 | 1308.8 |
293.15 | 1.0002 | 0.2005 | 1312.2 |
293.15 | 1.0002 | 0.4007 | 1317.6 |
293.15 | 1.0002 | 0.6008 | 1325.7 |
293.15 | 1.0002 | 0.8005 | 1337.1 |
293.15 | 3.0005 | 0.0000 | 1302.6 |
293.15 | 3.0005 | 0.2007 | 1306.3 |
293.15 | 3.0005 | 0.4011 | 1312.3 |
293.15 | 3.0005 | 0.6013 | 1321.3 |
293.15 | 3.0005 | 0.8007 | 1334.3 |
303.15 | 0.3332 | 0.0000 | 1278.4 |
303.15 | 0.3332 | 0.2001 | 1280.9 |
303.15 | 0.3332 | 0.4003 | 1285.6 |
303.15 | 0.3332 | 0.6003 | 1292.3 |
303.15 | 0.3332 | 0.8000 | 1301.4 |
303.15 | 1.0002 | 0.0000 | 1270.1 |
303.15 | 1.0002 | 0.2005 | 1273.7 |
303.15 | 1.0002 | 0.4007 | 1279.2 |
303.15 | 1.0002 | 0.6008 | 1287.2 |
303.15 | 1.0002 | 0.8005 | 1298.5 |
303.15 | 3.0005 | 0.0000 | 1264.3 |
303.15 | 3.0005 | 0.2007 | 1268.0 |
303.15 | 3.0005 | 0.4011 | 1274.1 |
303.15 | 3.0005 | 0.6013 | 1283.0 |
303.15 | 3.0005 | 0.8007 | 1295.8 |
313.15 | 0.3332 | 0.0000 | 1239.9 |
313.15 | 0.3332 | 0.2001 | 1242.5 |
313.15 | 0.3332 | 0.4003 | 1247.3 |
313.15 | 0.3332 | 0.6003 | 1254.0 |
313.15 | 0.3332 | 0.8000 | 1263.2 |
313.15 | 1.0002 | 0.0000 | 1232.0 |
313.15 | 1.0002 | 0.2005 | 1235.7 |
313.15 | 1.0002 | 0.4007 | 1241.3 |
313.15 | 1.0002 | 0.6008 | 1249.3 |
313.15 | 1.0002 | 0.8005 | 1260.4 |
313.15 | 3.0005 | 0.0000 | 1226.5 |
313.15 | 3.0005 | 0.2007 | 1230.4 |
313.15 | 3.0005 | 0.4011 | 1236.4 |
313.15 | 3.0005 | 0.6013 | 1245.3 |
313.15 | 3.0005 | 0.8007 | 1257.9 |
323.15 | 0.3332 | 0.0000 | 1202.0 |
323.15 | 0.3332 | 0.2001 | 1204.8 |
323.15 | 0.3332 | 0.4003 | 1209.7 |
323.15 | 0.3332 | 0.6003 | 1216.4 |
323.15 | 0.3332 | 0.8000 | 1225.7 |
323.15 | 1.0002 | 0.0000 | 1194.6 |
323.15 | 1.0002 | 0.2005 | 1198.4 |
323.15 | 1.0002 | 0.4007 | 1203.9 |
323.15 | 1.0002 | 0.6008 | 1211.9 |
323.15 | 1.0002 | 0.8005 | 1223.1 |
323.15 | 3.0005 | 0.0000 | 1189.3 |
323.15 | 3.0005 | 0.2007 | 1193.3 |
323.15 | 3.0005 | 0.4011 | 1199.3 |
323.15 | 3.0005 | 0.6013 | 1208.1 |
323.15 | 3.0005 | 0.8007 | 1220.6 |
333.15 | 0.3332 | 0.0000 | 1164.8 |
333.15 | 0.3332 | 0.2001 | 1167.8 |
333.15 | 0.3332 | 0.4003 | 1172.9 |
333.15 | 0.3332 | 0.6003 | 1179.6 |
333.15 | 0.3332 | 0.8000 | 1189.1 |
333.15 | 1.0002 | 0.0000 | 1157.9 |
333.15 | 1.0002 | 0.2005 | 1161.7 |
333.15 | 1.0002 | 0.4007 | 1167.3 |
333.15 | 1.0002 | 0.6008 | 1175.3 |
333.15 | 1.0002 | 0.8005 | 1186.5 |
333.15 | 3.0005 | 0.0000 | 1152.9 |
333.15 | 3.0005 | 0.2007 | 1156.9 |
333.15 | 3.0005 | 0.4011 | 1162.9 |
333.15 | 3.0005 | 0.6013 | 1171.7 |
333.15 | 3.0005 | 0.8007 | 1184.1 |
Operational conditions:
Fixed | Measured | ||
---|---|---|---|
Temperature, K - Liquid | Mole fraction of Dodecane (2) - Liquid | Mole fraction of Cyclohexane, butyl- (3) - Liquid | Speed of sound, m/s - Liquid |
288.15 | 0.2000 | 0.4500 | 1341.6 |
293.15 | 0.2000 | 0.4500 | 1321.8 |
298.15 | 0.2000 | 0.4500 | 1302.0 |
303.15 | 0.2000 | 0.4500 | 1282.5 |
313.15 | 0.2000 | 0.4500 | 1244.0 |
323.15 | 0.2000 | 0.4500 | 1206.4 |
333.15 | 0.2000 | 0.4500 | 1169.6 |
288.15 | 0.2500 | 0.4000 | 1339.4 |
293.15 | 0.2500 | 0.4000 | 1319.8 |
298.15 | 0.2500 | 0.4000 | 1300.3 |
303.15 | 0.2500 | 0.4000 | 1280.9 |
313.15 | 0.2500 | 0.4000 | 1242.7 |
323.15 | 0.2500 | 0.4000 | 1205.0 |
333.15 | 0.2500 | 0.4000 | 1168.2 |
288.15 | 0.3333 | 0.3333 | 1335.9 |
293.15 | 0.3333 | 0.3333 | 1316.3 |
298.15 | 0.3333 | 0.3333 | 1296.7 |
303.15 | 0.3333 | 0.3333 | 1277.4 |
313.15 | 0.3333 | 0.3333 | 1239.2 |
323.15 | 0.3333 | 0.3333 | 1201.8 |
333.15 | 0.3333 | 0.3333 | 1165.1 |
Operational conditions:
Fixed | Measured | ||
---|---|---|---|
Temperature, K - Liquid | Solvent: Amount ratio of component to other component of binary solvent of Dodecane (2) - Liquid | Mole fraction of Benzene, n-butyl- (1) - Liquid | Speed of sound, m/s - Liquid |
293.15 | 0.3332 | 0.0000 | 1317.5 |
293.15 | 0.3332 | 0.2001 | 1319.8 |
293.15 | 0.3332 | 0.4003 | 1324.5 |
293.15 | 0.3332 | 0.6003 | 1331.0 |
293.15 | 0.3332 | 0.8000 | 1340.2 |
293.15 | 1.0002 | 0.0000 | 1308.8 |
293.15 | 1.0002 | 0.2005 | 1312.2 |
293.15 | 1.0002 | 0.4007 | 1317.6 |
293.15 | 1.0002 | 0.6008 | 1325.7 |
293.15 | 1.0002 | 0.8005 | 1337.1 |
293.15 | 3.0005 | 0.0000 | 1302.6 |
293.15 | 3.0005 | 0.2007 | 1306.3 |
293.15 | 3.0005 | 0.4011 | 1312.3 |
293.15 | 3.0005 | 0.6013 | 1321.3 |
293.15 | 3.0005 | 0.8007 | 1334.3 |
303.15 | 0.3332 | 0.0000 | 1278.4 |
303.15 | 0.3332 | 0.2001 | 1280.9 |
303.15 | 0.3332 | 0.4003 | 1285.6 |
303.15 | 0.3332 | 0.6003 | 1292.3 |
303.15 | 0.3332 | 0.8000 | 1301.4 |
303.15 | 1.0002 | 0.0000 | 1270.1 |
303.15 | 1.0002 | 0.2005 | 1273.7 |
303.15 | 1.0002 | 0.4007 | 1279.2 |
303.15 | 1.0002 | 0.6008 | 1287.2 |
303.15 | 1.0002 | 0.8005 | 1298.5 |
303.15 | 3.0005 | 0.0000 | 1264.3 |
303.15 | 3.0005 | 0.2007 | 1268.0 |
303.15 | 3.0005 | 0.4011 | 1274.1 |
303.15 | 3.0005 | 0.6013 | 1283.0 |
303.15 | 3.0005 | 0.8007 | 1295.8 |
313.15 | 0.3332 | 0.0000 | 1239.9 |
313.15 | 0.3332 | 0.2001 | 1242.5 |
313.15 | 0.3332 | 0.4003 | 1247.3 |
313.15 | 0.3332 | 0.6003 | 1254.0 |
313.15 | 0.3332 | 0.8000 | 1263.2 |
313.15 | 1.0002 | 0.0000 | 1232.0 |
313.15 | 1.0002 | 0.2005 | 1235.7 |
313.15 | 1.0002 | 0.4007 | 1241.3 |
313.15 | 1.0002 | 0.6008 | 1249.3 |
313.15 | 1.0002 | 0.8005 | 1260.4 |
313.15 | 3.0005 | 0.0000 | 1226.5 |
313.15 | 3.0005 | 0.2007 | 1230.4 |
313.15 | 3.0005 | 0.4011 | 1236.4 |
313.15 | 3.0005 | 0.6013 | 1245.3 |
313.15 | 3.0005 | 0.8007 | 1257.9 |
323.15 | 0.3332 | 0.0000 | 1202.0 |
323.15 | 0.3332 | 0.2001 | 1204.8 |
323.15 | 0.3332 | 0.4003 | 1209.7 |
323.15 | 0.3332 | 0.6003 | 1216.4 |
323.15 | 0.3332 | 0.8000 | 1225.7 |
323.15 | 1.0002 | 0.0000 | 1194.6 |
323.15 | 1.0002 | 0.2005 | 1198.4 |
323.15 | 1.0002 | 0.4007 | 1203.9 |
323.15 | 1.0002 | 0.6008 | 1211.9 |
323.15 | 1.0002 | 0.8005 | 1223.1 |
323.15 | 3.0005 | 0.0000 | 1189.3 |
323.15 | 3.0005 | 0.2007 | 1193.3 |
323.15 | 3.0005 | 0.4011 | 1199.3 |
323.15 | 3.0005 | 0.6013 | 1208.1 |
323.15 | 3.0005 | 0.8007 | 1220.6 |
333.15 | 0.3332 | 0.0000 | 1164.8 |
333.15 | 0.3332 | 0.2001 | 1167.8 |
333.15 | 0.3332 | 0.4003 | 1172.9 |
333.15 | 0.3332 | 0.6003 | 1179.6 |
333.15 | 0.3332 | 0.8000 | 1189.1 |
333.15 | 1.0002 | 0.0000 | 1157.9 |
333.15 | 1.0002 | 0.2005 | 1161.7 |
333.15 | 1.0002 | 0.4007 | 1167.3 |
333.15 | 1.0002 | 0.6008 | 1175.3 |
333.15 | 1.0002 | 0.8005 | 1186.5 |
333.15 | 3.0005 | 0.0000 | 1152.9 |
333.15 | 3.0005 | 0.2007 | 1156.9 |
333.15 | 3.0005 | 0.4011 | 1162.9 |
333.15 | 3.0005 | 0.6013 | 1171.7 |
333.15 | 3.0005 | 0.8007 | 1184.1 |
Operational conditions:
Fixed | Measured | ||
---|---|---|---|
Temperature, K - Liquid | Mole fraction of Dodecane (2) - Liquid | Mole fraction of Cyclohexane, butyl- (3) - Liquid | Speed of sound, m/s - Liquid |
288.15 | 0.2000 | 0.4500 | 1341.6 |
293.15 | 0.2000 | 0.4500 | 1321.8 |
298.15 | 0.2000 | 0.4500 | 1302.0 |
303.15 | 0.2000 | 0.4500 | 1282.5 |
313.15 | 0.2000 | 0.4500 | 1244.0 |
323.15 | 0.2000 | 0.4500 | 1206.4 |
333.15 | 0.2000 | 0.4500 | 1169.6 |
288.15 | 0.2500 | 0.4000 | 1339.4 |
293.15 | 0.2500 | 0.4000 | 1319.8 |
298.15 | 0.2500 | 0.4000 | 1300.3 |
303.15 | 0.2500 | 0.4000 | 1280.9 |
313.15 | 0.2500 | 0.4000 | 1242.7 |
323.15 | 0.2500 | 0.4000 | 1205.0 |
333.15 | 0.2500 | 0.4000 | 1168.2 |
288.15 | 0.3333 | 0.3333 | 1335.9 |
293.15 | 0.3333 | 0.3333 | 1316.3 |
298.15 | 0.3333 | 0.3333 | 1296.7 |
303.15 | 0.3333 | 0.3333 | 1277.4 |
313.15 | 0.3333 | 0.3333 | 1239.2 |
323.15 | 0.3333 | 0.3333 | 1201.8 |
333.15 | 0.3333 | 0.3333 | 1165.1 |
Operational condition: Temperature, K = 294.5 (Liquid)
Fixed | Measured | |
---|---|---|
Solvent: Amount ratio of component to other component of binary solvent of Dodecane (2) - Liquid | Mole fraction of Benzene, n-butyl- (1) - Liquid | Surface tension liquid-gas, N/m - Liquid |
0.3332 | 0.0000 | 0.0261 |
0.3332 | 0.2001 | 0.0263 |
0.3332 | 0.4003 | 0.0267 |
0.3332 | 0.6003 | 0.0273 |
0.3332 | 0.8000 | 0.0278 |
1.0002 | 0.0000 | 0.0256 |
1.0002 | 0.2005 | 0.0260 |
1.0002 | 0.4007 | 0.0265 |
1.0002 | 0.6008 | 0.0271 |
1.0002 | 0.8005 | 0.0278 |
3.0005 | 0.0000 | 0.0253 |
3.0005 | 0.2007 | 0.0257 |
3.0005 | 0.4011 | 0.0262 |
3.0005 | 0.6013 | 0.0268 |
3.0005 | 0.8007 | 0.0278 |
Operational condition: Temperature, K = 295 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of Dodecane (2) - Liquid | Mole fraction of Cyclohexane, butyl- (3) - Liquid | Surface tension liquid-gas, N/m - Liquid |
0.2000 | 0.4500 | 0.0266 |
0.2500 | 0.4000 | 0.0265 |
0.3333 | 0.3333 | 0.0263 |
Operational condition: Temperature, K = 294.5 (Liquid)
Fixed | Measured | |
---|---|---|
Solvent: Amount ratio of component to other component of binary solvent of Dodecane (2) - Liquid | Mole fraction of Benzene, n-butyl- (1) - Liquid | Surface tension liquid-gas, N/m - Liquid |
0.3332 | 0.0000 | 0.0261 |
0.3332 | 0.2001 | 0.0263 |
0.3332 | 0.4003 | 0.0267 |
0.3332 | 0.6003 | 0.0273 |
0.3332 | 0.8000 | 0.0278 |
1.0002 | 0.0000 | 0.0256 |
1.0002 | 0.2005 | 0.0260 |
1.0002 | 0.4007 | 0.0265 |
1.0002 | 0.6008 | 0.0271 |
1.0002 | 0.8005 | 0.0278 |
3.0005 | 0.0000 | 0.0253 |
3.0005 | 0.2007 | 0.0257 |
3.0005 | 0.4011 | 0.0262 |
3.0005 | 0.6013 | 0.0268 |
3.0005 | 0.8007 | 0.0278 |
Operational condition: Temperature, K = 295 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of Dodecane (2) - Liquid | Mole fraction of Cyclohexane, butyl- (3) - Liquid | Surface tension liquid-gas, N/m - Liquid |
0.2000 | 0.4500 | 0.0266 |
0.2500 | 0.4000 | 0.0265 |
0.3333 | 0.3333 | 0.0263 |