Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of Dodecane (1) - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
0.0000 | 293.15 | 0.0013 |
0.1017 | 293.15 | 0.0013 |
0.1996 | 293.15 | 0.0013 |
0.2951 | 293.15 | 0.0013 |
0.4221 | 293.15 | 0.0014 |
0.5126 | 293.15 | 0.0014 |
0.6256 | 293.15 | 0.0014 |
0.7002 | 293.15 | 0.0014 |
0.7989 | 293.15 | 0.0014 |
0.9012 | 293.15 | 0.0015 |
1.0000 | 293.15 | 0.0015 |
0.0000 | 298.15 | 0.0012 |
0.1017 | 298.15 | 0.0012 |
0.1996 | 298.15 | 0.0012 |
0.2951 | 298.15 | 0.0012 |
0.4221 | 298.15 | 0.0013 |
0.5126 | 298.15 | 0.0013 |
0.6256 | 298.15 | 0.0013 |
0.7002 | 298.15 | 0.0013 |
0.7989 | 298.15 | 0.0013 |
0.9012 | 298.15 | 0.0013 |
1.0000 | 298.15 | 0.0014 |
0.0000 | 303.15 | 0.0011 |
0.1017 | 303.15 | 0.0011 |
0.1996 | 303.15 | 0.0011 |
0.2951 | 303.15 | 0.0011 |
0.4221 | 303.15 | 0.0012 |
0.5126 | 303.15 | 0.0012 |
0.6256 | 303.15 | 0.0012 |
0.7002 | 303.15 | 0.0012 |
0.7989 | 303.15 | 0.0012 |
0.9012 | 303.15 | 0.0012 |
1.0000 | 303.15 | 0.0012 |
0.0000 | 308.15 | 0.0010 |
0.1017 | 308.15 | 0.0010 |
0.1996 | 308.15 | 0.0011 |
0.2951 | 308.15 | 0.0011 |
0.4221 | 308.15 | 0.0011 |
0.5126 | 308.15 | 0.0011 |
0.6256 | 308.15 | 0.0011 |
0.7002 | 308.15 | 0.0011 |
0.7989 | 308.15 | 0.0011 |
0.9012 | 308.15 | 0.0011 |
1.0000 | 308.15 | 0.0012 |
0.0000 | 313.15 | 0.0010 |
0.1017 | 313.15 | 0.0010 |
0.1996 | 313.15 | 0.0010 |
0.2951 | 313.15 | 0.0010 |
0.4221 | 313.15 | 0.0010 |
0.5126 | 313.15 | 0.0010 |
0.6256 | 313.15 | 0.0010 |
0.7002 | 313.15 | 0.0010 |
0.7989 | 313.15 | 0.0010 |
0.9012 | 313.15 | 0.0011 |
1.0000 | 313.15 | 0.0011 |
0.0000 | 318.15 | 0.0009 |
0.1017 | 318.15 | 0.0009 |
0.1996 | 318.15 | 0.0009 |
0.2951 | 318.15 | 0.0009 |
0.4221 | 318.15 | 0.0009 |
0.5126 | 318.15 | 0.0009 |
0.6256 | 318.15 | 0.0010 |
0.7002 | 318.15 | 0.0010 |
0.7989 | 318.15 | 0.0010 |
0.9012 | 318.15 | 0.0010 |
1.0000 | 318.15 | 0.0010 |
0.0000 | 323.15 | 0.0008 |
0.1017 | 323.15 | 0.0009 |
0.1996 | 323.15 | 0.0009 |
0.2951 | 323.15 | 0.0009 |
0.4221 | 323.15 | 0.0009 |
0.5126 | 323.15 | 0.0009 |
0.6256 | 323.15 | 0.0009 |
0.7002 | 323.15 | 0.0009 |
0.7989 | 323.15 | 0.0009 |
0.9012 | 323.15 | 0.0009 |
1.0000 | 323.15 | 0.0009 |
0.0000 | 328.15 | 0.0008 |
0.1017 | 328.15 | 0.0008 |
0.1996 | 328.15 | 0.0008 |
0.2951 | 328.15 | 0.0008 |
0.4221 | 328.15 | 0.0008 |
0.5126 | 328.15 | 0.0008 |
0.6256 | 328.15 | 0.0008 |
0.7002 | 328.15 | 0.0008 |
0.7989 | 328.15 | 0.0008 |
0.9012 | 328.15 | 0.0009 |
1.0000 | 328.15 | 0.0009 |
0.0000 | 333.15 | 0.0007 |
0.1017 | 333.15 | 0.0008 |
0.1996 | 333.15 | 0.0008 |
0.2951 | 333.15 | 0.0008 |
0.4221 | 333.15 | 0.0008 |
0.5126 | 333.15 | 0.0008 |
0.6256 | 333.15 | 0.0008 |
0.7002 | 333.15 | 0.0008 |
0.7989 | 333.15 | 0.0008 |
0.9012 | 333.15 | 0.0008 |
1.0000 | 333.15 | 0.0008 |
0.0000 | 338.15 | 0.0007 |
0.1017 | 338.15 | 0.0007 |
0.1996 | 338.15 | 0.0007 |
0.2951 | 338.15 | 0.0007 |
0.4221 | 338.15 | 0.0007 |
0.5126 | 338.15 | 0.0007 |
0.6256 | 338.15 | 0.0007 |
0.7002 | 338.15 | 0.0007 |
0.7989 | 338.15 | 0.0007 |
0.9012 | 338.15 | 0.0008 |
1.0000 | 338.15 | 0.0008 |
0.0000 | 343.15 | 0.0007 |
0.1017 | 343.15 | 0.0007 |
0.1996 | 343.15 | 0.0007 |
0.2951 | 343.15 | 0.0007 |
0.4221 | 343.15 | 0.0007 |
0.5126 | 343.15 | 0.0007 |
0.6256 | 343.15 | 0.0007 |
0.7002 | 343.15 | 0.0007 |
0.7989 | 343.15 | 0.0007 |
0.9012 | 343.15 | 0.0007 |
1.0000 | 343.15 | 0.0007 |
Operational condition: Pressure, kPa = 102 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Amount ratio of solute to solvent of Dodecane (1) - Liquid | Viscosity, Pa*s - Liquid |
293.15 | 0.3332 | 0.0013 |
293.15 | 1.0002 | 0.0014 |
293.15 | 3.0005 | 0.0014 |
303.15 | 0.3332 | 0.0011 |
303.15 | 1.0002 | 0.0012 |
303.15 | 3.0005 | 0.0012 |
313.15 | 0.3332 | 0.0010 |
313.15 | 1.0002 | 0.0010 |
313.15 | 3.0005 | 0.0010 |
323.15 | 0.3332 | 0.0008 |
323.15 | 1.0002 | 0.0009 |
323.15 | 3.0005 | 0.0009 |
333.15 | 0.3332 | 0.0007 |
333.15 | 1.0002 | 0.0008 |
333.15 | 3.0005 | 0.0008 |
343.15 | 0.3332 | 0.0007 |
343.15 | 1.0002 | 0.0007 |
343.15 | 3.0005 | 0.0007 |
293.15 | 1.0001 | 0.0014 |
293.15 | 2.9949 | 0.0014 |
303.15 | 1.0001 | 0.0012 |
303.15 | 2.9949 | 0.0012 |
313.15 | 0.3332 | 0.0010 |
313.15 | 1.0001 | 0.0010 |
313.15 | 2.9949 | 0.0010 |
323.15 | 0.3332 | 0.0008 |
323.15 | 1.0001 | 0.0009 |
323.15 | 2.9949 | 0.0009 |
333.15 | 0.3332 | 0.0007 |
333.15 | 1.0001 | 0.0008 |
333.15 | 2.9949 | 0.0008 |
343.15 | 1.0001 | 0.0007 |
343.15 | 2.9949 | 0.0007 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Cyclohexane, butyl- (2) - Liquid | Viscosity, Pa*s - Liquid |
293.15 | 0.0000 | 0.0015 |
293.15 | 0.0511 | 0.0015 |
293.15 | 0.0989 | 0.0015 |
293.15 | 0.2004 | 0.0015 |
293.15 | 0.3002 | 0.0014 |
293.15 | 0.4012 | 0.0014 |
293.15 | 0.5005 | 0.0014 |
293.15 | 0.6006 | 0.0014 |
293.15 | 0.7008 | 0.0014 |
293.15 | 0.7998 | 0.0014 |
293.15 | 0.8996 | 0.0013 |
293.15 | 0.9494 | 0.0013 |
293.15 | 1.0000 | 0.0013 |
298.15 | 0.0000 | 0.0014 |
298.15 | 0.0511 | 0.0014 |
298.15 | 0.0989 | 0.0014 |
298.15 | 0.2004 | 0.0013 |
298.15 | 0.3002 | 0.0013 |
298.15 | 0.4012 | 0.0013 |
298.15 | 0.5005 | 0.0013 |
298.15 | 0.6006 | 0.0013 |
298.15 | 0.7008 | 0.0013 |
298.15 | 0.7998 | 0.0012 |
298.15 | 0.8996 | 0.0012 |
298.15 | 0.9494 | 0.0012 |
298.15 | 1.0000 | 0.0012 |
303.15 | 0.0000 | 0.0013 |
303.15 | 0.0511 | 0.0013 |
303.15 | 0.0989 | 0.0013 |
303.15 | 0.2004 | 0.0012 |
303.15 | 0.3002 | 0.0012 |
303.15 | 0.4012 | 0.0012 |
303.15 | 0.5005 | 0.0012 |
303.15 | 0.6006 | 0.0012 |
303.15 | 0.7008 | 0.0012 |
303.15 | 0.7998 | 0.0011 |
303.15 | 0.8996 | 0.0011 |
303.15 | 0.9494 | 0.0011 |
303.15 | 1.0000 | 0.0011 |
308.15 | 0.0000 | 0.0012 |
308.15 | 0.0511 | 0.0012 |
308.15 | 0.0989 | 0.0012 |
308.15 | 0.2004 | 0.0011 |
308.15 | 0.3002 | 0.0011 |
308.15 | 0.4012 | 0.0011 |
308.15 | 0.5005 | 0.0011 |
308.15 | 0.6006 | 0.0011 |
308.15 | 0.7008 | 0.0011 |
308.15 | 0.7998 | 0.0011 |
308.15 | 0.8996 | 0.0010 |
308.15 | 0.9494 | 0.0010 |
308.15 | 1.0000 | 0.0010 |
313.15 | 0.0000 | 0.0011 |
313.15 | 0.0511 | 0.0011 |
313.15 | 0.0989 | 0.0011 |
313.15 | 0.2004 | 0.0011 |
313.15 | 0.3002 | 0.0010 |
313.15 | 0.4012 | 0.0010 |
313.15 | 0.5005 | 0.0010 |
313.15 | 0.6006 | 0.0010 |
313.15 | 0.7008 | 0.0010 |
313.15 | 0.7998 | 0.0010 |
313.15 | 0.8996 | 0.0010 |
313.15 | 0.9494 | 0.0010 |
313.15 | 1.0000 | 0.0010 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of Dodecane (1) - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
0.0000 | 293.15 | 0.0013 |
0.1017 | 293.15 | 0.0013 |
0.1996 | 293.15 | 0.0013 |
0.2951 | 293.15 | 0.0013 |
0.4221 | 293.15 | 0.0014 |
0.5126 | 293.15 | 0.0014 |
0.6256 | 293.15 | 0.0014 |
0.7002 | 293.15 | 0.0014 |
0.7989 | 293.15 | 0.0014 |
0.9012 | 293.15 | 0.0015 |
1.0000 | 293.15 | 0.0015 |
0.0000 | 298.15 | 0.0012 |
0.1017 | 298.15 | 0.0012 |
0.1996 | 298.15 | 0.0012 |
0.2951 | 298.15 | 0.0012 |
0.4221 | 298.15 | 0.0013 |
0.5126 | 298.15 | 0.0013 |
0.6256 | 298.15 | 0.0013 |
0.7002 | 298.15 | 0.0013 |
0.7989 | 298.15 | 0.0013 |
0.9012 | 298.15 | 0.0013 |
1.0000 | 298.15 | 0.0014 |
0.0000 | 303.15 | 0.0011 |
0.1017 | 303.15 | 0.0011 |
0.1996 | 303.15 | 0.0011 |
0.2951 | 303.15 | 0.0011 |
0.4221 | 303.15 | 0.0012 |
0.5126 | 303.15 | 0.0012 |
0.6256 | 303.15 | 0.0012 |
0.7002 | 303.15 | 0.0012 |
0.7989 | 303.15 | 0.0012 |
0.9012 | 303.15 | 0.0012 |
1.0000 | 303.15 | 0.0012 |
0.0000 | 308.15 | 0.0010 |
0.1017 | 308.15 | 0.0010 |
0.1996 | 308.15 | 0.0011 |
0.2951 | 308.15 | 0.0011 |
0.4221 | 308.15 | 0.0011 |
0.5126 | 308.15 | 0.0011 |
0.6256 | 308.15 | 0.0011 |
0.7002 | 308.15 | 0.0011 |
0.7989 | 308.15 | 0.0011 |
0.9012 | 308.15 | 0.0011 |
1.0000 | 308.15 | 0.0012 |
0.0000 | 313.15 | 0.0010 |
0.1017 | 313.15 | 0.0010 |
0.1996 | 313.15 | 0.0010 |
0.2951 | 313.15 | 0.0010 |
0.4221 | 313.15 | 0.0010 |
0.5126 | 313.15 | 0.0010 |
0.6256 | 313.15 | 0.0010 |
0.7002 | 313.15 | 0.0010 |
0.7989 | 313.15 | 0.0010 |
0.9012 | 313.15 | 0.0011 |
1.0000 | 313.15 | 0.0011 |
0.0000 | 318.15 | 0.0009 |
0.1017 | 318.15 | 0.0009 |
0.1996 | 318.15 | 0.0009 |
0.2951 | 318.15 | 0.0009 |
0.4221 | 318.15 | 0.0009 |
0.5126 | 318.15 | 0.0009 |
0.6256 | 318.15 | 0.0010 |
0.7002 | 318.15 | 0.0010 |
0.7989 | 318.15 | 0.0010 |
0.9012 | 318.15 | 0.0010 |
1.0000 | 318.15 | 0.0010 |
0.0000 | 323.15 | 0.0008 |
0.1017 | 323.15 | 0.0009 |
0.1996 | 323.15 | 0.0009 |
0.2951 | 323.15 | 0.0009 |
0.4221 | 323.15 | 0.0009 |
0.5126 | 323.15 | 0.0009 |
0.6256 | 323.15 | 0.0009 |
0.7002 | 323.15 | 0.0009 |
0.7989 | 323.15 | 0.0009 |
0.9012 | 323.15 | 0.0009 |
1.0000 | 323.15 | 0.0009 |
0.0000 | 328.15 | 0.0008 |
0.1017 | 328.15 | 0.0008 |
0.1996 | 328.15 | 0.0008 |
0.2951 | 328.15 | 0.0008 |
0.4221 | 328.15 | 0.0008 |
0.5126 | 328.15 | 0.0008 |
0.6256 | 328.15 | 0.0008 |
0.7002 | 328.15 | 0.0008 |
0.7989 | 328.15 | 0.0008 |
0.9012 | 328.15 | 0.0009 |
1.0000 | 328.15 | 0.0009 |
0.0000 | 333.15 | 0.0007 |
0.1017 | 333.15 | 0.0008 |
0.1996 | 333.15 | 0.0008 |
0.2951 | 333.15 | 0.0008 |
0.4221 | 333.15 | 0.0008 |
0.5126 | 333.15 | 0.0008 |
0.6256 | 333.15 | 0.0008 |
0.7002 | 333.15 | 0.0008 |
0.7989 | 333.15 | 0.0008 |
0.9012 | 333.15 | 0.0008 |
1.0000 | 333.15 | 0.0008 |
0.0000 | 338.15 | 0.0007 |
0.1017 | 338.15 | 0.0007 |
0.1996 | 338.15 | 0.0007 |
0.2951 | 338.15 | 0.0007 |
0.4221 | 338.15 | 0.0007 |
0.5126 | 338.15 | 0.0007 |
0.6256 | 338.15 | 0.0007 |
0.7002 | 338.15 | 0.0007 |
0.7989 | 338.15 | 0.0007 |
0.9012 | 338.15 | 0.0008 |
1.0000 | 338.15 | 0.0008 |
0.0000 | 343.15 | 0.0007 |
0.1017 | 343.15 | 0.0007 |
0.1996 | 343.15 | 0.0007 |
0.2951 | 343.15 | 0.0007 |
0.4221 | 343.15 | 0.0007 |
0.5126 | 343.15 | 0.0007 |
0.6256 | 343.15 | 0.0007 |
0.7002 | 343.15 | 0.0007 |
0.7989 | 343.15 | 0.0007 |
0.9012 | 343.15 | 0.0007 |
1.0000 | 343.15 | 0.0007 |
Operational condition: Pressure, kPa = 102 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Amount ratio of solute to solvent of Dodecane (1) - Liquid | Viscosity, Pa*s - Liquid |
293.15 | 0.3332 | 0.0013 |
293.15 | 1.0002 | 0.0014 |
293.15 | 3.0005 | 0.0014 |
303.15 | 0.3332 | 0.0011 |
303.15 | 1.0002 | 0.0012 |
303.15 | 3.0005 | 0.0012 |
313.15 | 0.3332 | 0.0010 |
313.15 | 1.0002 | 0.0010 |
313.15 | 3.0005 | 0.0010 |
323.15 | 0.3332 | 0.0008 |
323.15 | 1.0002 | 0.0009 |
323.15 | 3.0005 | 0.0009 |
333.15 | 0.3332 | 0.0007 |
333.15 | 1.0002 | 0.0008 |
333.15 | 3.0005 | 0.0008 |
343.15 | 0.3332 | 0.0007 |
343.15 | 1.0002 | 0.0007 |
343.15 | 3.0005 | 0.0007 |
293.15 | 1.0001 | 0.0014 |
293.15 | 2.9949 | 0.0014 |
303.15 | 1.0001 | 0.0012 |
303.15 | 2.9949 | 0.0012 |
313.15 | 0.3332 | 0.0010 |
313.15 | 1.0001 | 0.0010 |
313.15 | 2.9949 | 0.0010 |
323.15 | 0.3332 | 0.0008 |
323.15 | 1.0001 | 0.0009 |
323.15 | 2.9949 | 0.0009 |
333.15 | 0.3332 | 0.0007 |
333.15 | 1.0001 | 0.0008 |
333.15 | 2.9949 | 0.0008 |
343.15 | 1.0001 | 0.0007 |
343.15 | 2.9949 | 0.0007 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Cyclohexane, butyl- (2) - Liquid | Viscosity, Pa*s - Liquid |
293.15 | 0.0000 | 0.0015 |
293.15 | 0.0511 | 0.0015 |
293.15 | 0.0989 | 0.0015 |
293.15 | 0.2004 | 0.0015 |
293.15 | 0.3002 | 0.0014 |
293.15 | 0.4012 | 0.0014 |
293.15 | 0.5005 | 0.0014 |
293.15 | 0.6006 | 0.0014 |
293.15 | 0.7008 | 0.0014 |
293.15 | 0.7998 | 0.0014 |
293.15 | 0.8996 | 0.0013 |
293.15 | 0.9494 | 0.0013 |
293.15 | 1.0000 | 0.0013 |
298.15 | 0.0000 | 0.0014 |
298.15 | 0.0511 | 0.0014 |
298.15 | 0.0989 | 0.0014 |
298.15 | 0.2004 | 0.0013 |
298.15 | 0.3002 | 0.0013 |
298.15 | 0.4012 | 0.0013 |
298.15 | 0.5005 | 0.0013 |
298.15 | 0.6006 | 0.0013 |
298.15 | 0.7008 | 0.0013 |
298.15 | 0.7998 | 0.0012 |
298.15 | 0.8996 | 0.0012 |
298.15 | 0.9494 | 0.0012 |
298.15 | 1.0000 | 0.0012 |
303.15 | 0.0000 | 0.0013 |
303.15 | 0.0511 | 0.0013 |
303.15 | 0.0989 | 0.0013 |
303.15 | 0.2004 | 0.0012 |
303.15 | 0.3002 | 0.0012 |
303.15 | 0.4012 | 0.0012 |
303.15 | 0.5005 | 0.0012 |
303.15 | 0.6006 | 0.0012 |
303.15 | 0.7008 | 0.0012 |
303.15 | 0.7998 | 0.0011 |
303.15 | 0.8996 | 0.0011 |
303.15 | 0.9494 | 0.0011 |
303.15 | 1.0000 | 0.0011 |
308.15 | 0.0000 | 0.0012 |
308.15 | 0.0511 | 0.0012 |
308.15 | 0.0989 | 0.0012 |
308.15 | 0.2004 | 0.0011 |
308.15 | 0.3002 | 0.0011 |
308.15 | 0.4012 | 0.0011 |
308.15 | 0.5005 | 0.0011 |
308.15 | 0.6006 | 0.0011 |
308.15 | 0.7008 | 0.0011 |
308.15 | 0.7998 | 0.0011 |
308.15 | 0.8996 | 0.0010 |
308.15 | 0.9494 | 0.0010 |
308.15 | 1.0000 | 0.0010 |
313.15 | 0.0000 | 0.0011 |
313.15 | 0.0511 | 0.0011 |
313.15 | 0.0989 | 0.0011 |
313.15 | 0.2004 | 0.0011 |
313.15 | 0.3002 | 0.0010 |
313.15 | 0.4012 | 0.0010 |
313.15 | 0.5005 | 0.0010 |
313.15 | 0.6006 | 0.0010 |
313.15 | 0.7008 | 0.0010 |
313.15 | 0.7998 | 0.0010 |
313.15 | 0.8996 | 0.0010 |
313.15 | 0.9494 | 0.0010 |
313.15 | 1.0000 | 0.0010 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of Dodecane (1) - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
0.0000 | 293.15 | 799.34 |
0.1017 | 293.15 | 792.77 |
0.1996 | 293.15 | 786.82 |
0.2951 | 293.15 | 781.36 |
0.4221 | 293.15 | 774.55 |
0.5126 | 293.15 | 769.99 |
0.6256 | 293.15 | 764.59 |
0.7002 | 293.15 | 761.2 |
0.7989 | 293.15 | 756.92 |
0.9012 | 293.15 | 752.7 |
1.0000 | 293.15 | 748.83 |
0.0000 | 298.15 | 795.59 |
0.1017 | 298.15 | 789.05 |
0.1996 | 298.15 | 783.12 |
0.2951 | 298.15 | 777.68 |
0.4221 | 298.15 | 770.9 |
0.5126 | 298.15 | 766.35 |
0.6256 | 298.15 | 760.96 |
0.7002 | 298.15 | 757.57 |
0.7989 | 298.15 | 753.3 |
0.9012 | 298.15 | 749.09 |
1.0000 | 298.15 | 745.23 |
0.0000 | 303.15 | 791.84 |
0.1017 | 303.15 | 785.32 |
0.1996 | 303.15 | 779.41 |
0.2951 | 303.15 | 773.99 |
0.4221 | 303.15 | 767.22 |
0.5126 | 303.15 | 762.68 |
0.6256 | 303.15 | 757.3 |
0.7002 | 303.15 | 753.92 |
0.7989 | 303.15 | 749.66 |
0.9012 | 303.15 | 745.45 |
1.0000 | 303.15 | 741.6 |
0.0000 | 308.15 | 788.07 |
0.1017 | 308.15 | 781.58 |
0.1996 | 308.15 | 775.69 |
0.2951 | 308.15 | 770.28 |
0.4221 | 308.15 | 763.53 |
0.5126 | 308.15 | 759.01 |
0.6256 | 308.15 | 753.64 |
0.7002 | 308.15 | 750.27 |
0.7989 | 308.15 | 746.01 |
0.9012 | 308.15 | 741.81 |
1.0000 | 308.15 | 737.97 |
0.0000 | 313.15 | 784.3 |
0.1017 | 313.15 | 777.82 |
0.1996 | 313.15 | 771.96 |
0.2951 | 313.15 | 766.57 |
0.4221 | 313.15 | 759.84 |
0.5126 | 313.15 | 755.32 |
0.6256 | 313.15 | 749.97 |
0.7002 | 313.15 | 746.6 |
0.7989 | 313.15 | 742.35 |
0.9012 | 313.15 | 738.16 |
1.0000 | 313.15 | 734.33 |
0.0000 | 318.15 | 780.52 |
0.1017 | 318.15 | 774.07 |
0.1996 | 318.15 | 768.22 |
0.2951 | 318.15 | 762.85 |
0.4221 | 318.15 | 756.14 |
0.5126 | 318.15 | 751.63 |
0.6256 | 318.15 | 746.29 |
0.7002 | 318.15 | 742.93 |
0.7989 | 318.15 | 738.69 |
0.9012 | 318.15 | 734.5 |
1.0000 | 318.15 | 730.68 |
0.0000 | 323.15 | 776.74 |
0.1017 | 323.15 | 770.3 |
0.1996 | 323.15 | 764.47 |
0.2951 | 323.15 | 759.12 |
0.4221 | 323.15 | 752.42 |
0.5126 | 323.15 | 747.93 |
0.6256 | 323.15 | 742.6 |
0.7002 | 323.15 | 739.25 |
0.7989 | 323.15 | 735.02 |
0.9012 | 323.15 | 730.84 |
1.0000 | 323.15 | 727.01 |
0.0000 | 328.15 | 772.93 |
0.1017 | 328.15 | 766.52 |
0.1996 | 328.15 | 760.71 |
0.2951 | 328.15 | 755.37 |
0.4221 | 328.15 | 748.7 |
0.5126 | 328.15 | 744.22 |
0.6256 | 328.15 | 738.9 |
0.7002 | 328.15 | 735.56 |
0.7989 | 328.15 | 731.33 |
0.9012 | 328.15 | 727.16 |
1.0000 | 328.15 | 723.35 |
0.0000 | 333.15 | 769.13 |
0.1017 | 333.15 | 762.73 |
0.1996 | 333.15 | 756.94 |
0.2951 | 333.15 | 751.62 |
0.4221 | 333.15 | 744.96 |
0.5126 | 333.15 | 740.49 |
0.6256 | 333.15 | 735.19 |
0.7002 | 333.15 | 731.86 |
0.7989 | 333.15 | 727.64 |
0.9012 | 333.15 | 723.48 |
1.0000 | 333.15 | 719.67 |
0.0000 | 338.15 | 765.3 |
0.1017 | 338.15 | 758.93 |
0.1996 | 338.15 | 753.16 |
0.2951 | 338.15 | 747.85 |
0.4221 | 338.15 | 741.21 |
0.5126 | 338.15 | 736.75 |
0.6256 | 338.15 | 731.47 |
0.7002 | 338.15 | 728.14 |
0.7989 | 338.15 | 723.94 |
0.9012 | 338.15 | 719.78 |
1.0000 | 338.15 | 715.98 |
0.0000 | 343.15 | 761.47 |
0.1017 | 343.15 | 755.12 |
0.1996 | 343.15 | 749.37 |
0.2951 | 343.15 | 744.07 |
0.4221 | 343.15 | 737.45 |
0.5126 | 343.15 | 733.0 |
0.6256 | 343.15 | 727.73 |
0.7002 | 343.15 | 724.41 |
0.7989 | 343.15 | 720.22 |
0.9012 | 343.15 | 716.08 |
1.0000 | 343.15 | 712.28 |
Operational condition: Pressure, kPa = 102 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Amount ratio of solute to solvent of Dodecane (1) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.3332 | 783.9 |
293.15 | 1.0002 | 770.6 |
293.15 | 3.0005 | 759.0 |
303.15 | 0.3332 | 776.5 |
303.15 | 1.0002 | 763.3 |
303.15 | 3.0005 | 751.7 |
313.15 | 0.3332 | 769.1 |
313.15 | 1.0002 | 755.9 |
313.15 | 3.0005 | 744.4 |
323.15 | 0.3332 | 761.6 |
323.15 | 1.0002 | 748.5 |
323.15 | 3.0005 | 737.1 |
333.15 | 0.3332 | 754.1 |
333.15 | 1.0002 | 741.1 |
333.15 | 3.0005 | 729.7 |
343.15 | 0.3332 | 746.5 |
343.15 | 1.0002 | 733.6 |
343.15 | 3.0005 | 722.2 |
293.15 | 1.0001 | 770.6 |
293.15 | 2.9949 | 759.0 |
303.15 | 1.0001 | 763.3 |
303.15 | 2.9949 | 751.7 |
313.15 | 1.0001 | 755.9 |
313.15 | 2.9949 | 744.4 |
323.15 | 1.0001 | 748.5 |
323.15 | 2.9949 | 737.1 |
333.15 | 1.0001 | 741.1 |
333.15 | 2.9949 | 729.7 |
343.15 | 1.0001 | 733.7 |
343.15 | 2.9949 | 722.5 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Cyclohexane, butyl- (2) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.0000 | 749.0 |
293.15 | 0.0511 | 750.97 |
293.15 | 0.0989 | 752.88 |
293.15 | 0.2004 | 757.06 |
293.15 | 0.3002 | 761.38 |
293.15 | 0.4012 | 765.97 |
293.15 | 0.5005 | 770.74 |
293.15 | 0.6006 | 775.82 |
293.15 | 0.7008 | 781.21 |
293.15 | 0.7998 | 786.85 |
293.15 | 0.8996 | 792.92 |
293.15 | 0.9494 | 796.1 |
293.15 | 1.0000 | 799.44 |
298.15 | 0.0000 | 745.38 |
298.15 | 0.0511 | 747.36 |
298.15 | 0.0989 | 749.26 |
298.15 | 0.2004 | 753.44 |
298.15 | 0.3002 | 757.75 |
298.15 | 0.4012 | 762.34 |
298.15 | 0.5005 | 767.1 |
298.15 | 0.6006 | 772.16 |
298.15 | 0.7008 | 777.53 |
298.15 | 0.7998 | 783.16 |
298.15 | 0.8996 | 789.21 |
298.15 | 0.9494 | 792.38 |
298.15 | 1.0000 | 795.7 |
303.15 | 0.0000 | 741.75 |
303.15 | 0.0511 | 743.73 |
303.15 | 0.0989 | 745.63 |
303.15 | 0.2004 | 749.8 |
303.15 | 0.3002 | 754.1 |
303.15 | 0.4012 | 758.68 |
303.15 | 0.5005 | 763.43 |
303.15 | 0.6006 | 768.48 |
303.15 | 0.7008 | 773.83 |
303.15 | 0.7998 | 779.45 |
303.15 | 0.8996 | 785.47 |
303.15 | 0.9494 | 788.64 |
303.15 | 1.0000 | 791.95 |
308.15 | 0.0000 | 738.12 |
308.15 | 0.0511 | 740.1 |
308.15 | 0.0989 | 741.99 |
308.15 | 0.2004 | 746.15 |
308.15 | 0.3002 | 750.45 |
308.15 | 0.4012 | 755.02 |
308.15 | 0.5005 | 759.76 |
308.15 | 0.6006 | 764.8 |
308.15 | 0.7008 | 770.13 |
308.15 | 0.7998 | 775.73 |
308.15 | 0.8996 | 781.73 |
308.15 | 0.9494 | 784.9 |
308.15 | 1.0000 | 788.19 |
313.15 | 0.0000 | 734.48 |
313.15 | 0.0511 | 736.45 |
313.15 | 0.0989 | 738.34 |
313.15 | 0.2004 | 742.5 |
313.15 | 0.3002 | 746.78 |
313.15 | 0.4012 | 751.35 |
313.15 | 0.5005 | 756.07 |
313.15 | 0.6006 | 761.1 |
313.15 | 0.7008 | 766.43 |
313.15 | 0.7998 | 771.99 |
313.15 | 0.8996 | 777.98 |
313.15 | 0.9494 | 781.13 |
313.15 | 1.0000 | 784.41 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of Dodecane (1) - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
0.0000 | 293.15 | 799.34 |
0.1017 | 293.15 | 792.77 |
0.1996 | 293.15 | 786.82 |
0.2951 | 293.15 | 781.36 |
0.4221 | 293.15 | 774.55 |
0.5126 | 293.15 | 769.99 |
0.6256 | 293.15 | 764.59 |
0.7002 | 293.15 | 761.2 |
0.7989 | 293.15 | 756.92 |
0.9012 | 293.15 | 752.7 |
1.0000 | 293.15 | 748.83 |
0.0000 | 298.15 | 795.59 |
0.1017 | 298.15 | 789.05 |
0.1996 | 298.15 | 783.12 |
0.2951 | 298.15 | 777.68 |
0.4221 | 298.15 | 770.9 |
0.5126 | 298.15 | 766.35 |
0.6256 | 298.15 | 760.96 |
0.7002 | 298.15 | 757.57 |
0.7989 | 298.15 | 753.3 |
0.9012 | 298.15 | 749.09 |
1.0000 | 298.15 | 745.23 |
0.0000 | 303.15 | 791.84 |
0.1017 | 303.15 | 785.32 |
0.1996 | 303.15 | 779.41 |
0.2951 | 303.15 | 773.99 |
0.4221 | 303.15 | 767.22 |
0.5126 | 303.15 | 762.68 |
0.6256 | 303.15 | 757.3 |
0.7002 | 303.15 | 753.92 |
0.7989 | 303.15 | 749.66 |
0.9012 | 303.15 | 745.45 |
1.0000 | 303.15 | 741.6 |
0.0000 | 308.15 | 788.07 |
0.1017 | 308.15 | 781.58 |
0.1996 | 308.15 | 775.69 |
0.2951 | 308.15 | 770.28 |
0.4221 | 308.15 | 763.53 |
0.5126 | 308.15 | 759.01 |
0.6256 | 308.15 | 753.64 |
0.7002 | 308.15 | 750.27 |
0.7989 | 308.15 | 746.01 |
0.9012 | 308.15 | 741.81 |
1.0000 | 308.15 | 737.97 |
0.0000 | 313.15 | 784.3 |
0.1017 | 313.15 | 777.82 |
0.1996 | 313.15 | 771.96 |
0.2951 | 313.15 | 766.57 |
0.4221 | 313.15 | 759.84 |
0.5126 | 313.15 | 755.32 |
0.6256 | 313.15 | 749.97 |
0.7002 | 313.15 | 746.6 |
0.7989 | 313.15 | 742.35 |
0.9012 | 313.15 | 738.16 |
1.0000 | 313.15 | 734.33 |
0.0000 | 318.15 | 780.52 |
0.1017 | 318.15 | 774.07 |
0.1996 | 318.15 | 768.22 |
0.2951 | 318.15 | 762.85 |
0.4221 | 318.15 | 756.14 |
0.5126 | 318.15 | 751.63 |
0.6256 | 318.15 | 746.29 |
0.7002 | 318.15 | 742.93 |
0.7989 | 318.15 | 738.69 |
0.9012 | 318.15 | 734.5 |
1.0000 | 318.15 | 730.68 |
0.0000 | 323.15 | 776.74 |
0.1017 | 323.15 | 770.3 |
0.1996 | 323.15 | 764.47 |
0.2951 | 323.15 | 759.12 |
0.4221 | 323.15 | 752.42 |
0.5126 | 323.15 | 747.93 |
0.6256 | 323.15 | 742.6 |
0.7002 | 323.15 | 739.25 |
0.7989 | 323.15 | 735.02 |
0.9012 | 323.15 | 730.84 |
1.0000 | 323.15 | 727.01 |
0.0000 | 328.15 | 772.93 |
0.1017 | 328.15 | 766.52 |
0.1996 | 328.15 | 760.71 |
0.2951 | 328.15 | 755.37 |
0.4221 | 328.15 | 748.7 |
0.5126 | 328.15 | 744.22 |
0.6256 | 328.15 | 738.9 |
0.7002 | 328.15 | 735.56 |
0.7989 | 328.15 | 731.33 |
0.9012 | 328.15 | 727.16 |
1.0000 | 328.15 | 723.35 |
0.0000 | 333.15 | 769.13 |
0.1017 | 333.15 | 762.73 |
0.1996 | 333.15 | 756.94 |
0.2951 | 333.15 | 751.62 |
0.4221 | 333.15 | 744.96 |
0.5126 | 333.15 | 740.49 |
0.6256 | 333.15 | 735.19 |
0.7002 | 333.15 | 731.86 |
0.7989 | 333.15 | 727.64 |
0.9012 | 333.15 | 723.48 |
1.0000 | 333.15 | 719.67 |
0.0000 | 338.15 | 765.3 |
0.1017 | 338.15 | 758.93 |
0.1996 | 338.15 | 753.16 |
0.2951 | 338.15 | 747.85 |
0.4221 | 338.15 | 741.21 |
0.5126 | 338.15 | 736.75 |
0.6256 | 338.15 | 731.47 |
0.7002 | 338.15 | 728.14 |
0.7989 | 338.15 | 723.94 |
0.9012 | 338.15 | 719.78 |
1.0000 | 338.15 | 715.98 |
0.0000 | 343.15 | 761.47 |
0.1017 | 343.15 | 755.12 |
0.1996 | 343.15 | 749.37 |
0.2951 | 343.15 | 744.07 |
0.4221 | 343.15 | 737.45 |
0.5126 | 343.15 | 733.0 |
0.6256 | 343.15 | 727.73 |
0.7002 | 343.15 | 724.41 |
0.7989 | 343.15 | 720.22 |
0.9012 | 343.15 | 716.08 |
1.0000 | 343.15 | 712.28 |
Operational condition: Pressure, kPa = 102 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Amount ratio of solute to solvent of Dodecane (1) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.3332 | 783.9 |
293.15 | 1.0002 | 770.6 |
293.15 | 3.0005 | 759.0 |
303.15 | 0.3332 | 776.5 |
303.15 | 1.0002 | 763.3 |
303.15 | 3.0005 | 751.7 |
313.15 | 0.3332 | 769.1 |
313.15 | 1.0002 | 755.9 |
313.15 | 3.0005 | 744.4 |
323.15 | 0.3332 | 761.6 |
323.15 | 1.0002 | 748.5 |
323.15 | 3.0005 | 737.1 |
333.15 | 0.3332 | 754.1 |
333.15 | 1.0002 | 741.1 |
333.15 | 3.0005 | 729.7 |
343.15 | 0.3332 | 746.5 |
343.15 | 1.0002 | 733.6 |
343.15 | 3.0005 | 722.2 |
293.15 | 1.0001 | 770.6 |
293.15 | 2.9949 | 759.0 |
303.15 | 1.0001 | 763.3 |
303.15 | 2.9949 | 751.7 |
313.15 | 1.0001 | 755.9 |
313.15 | 2.9949 | 744.4 |
323.15 | 1.0001 | 748.5 |
323.15 | 2.9949 | 737.1 |
333.15 | 1.0001 | 741.1 |
333.15 | 2.9949 | 729.7 |
343.15 | 1.0001 | 733.7 |
343.15 | 2.9949 | 722.5 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Cyclohexane, butyl- (2) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.0000 | 749.0 |
293.15 | 0.0511 | 750.97 |
293.15 | 0.0989 | 752.88 |
293.15 | 0.2004 | 757.06 |
293.15 | 0.3002 | 761.38 |
293.15 | 0.4012 | 765.97 |
293.15 | 0.5005 | 770.74 |
293.15 | 0.6006 | 775.82 |
293.15 | 0.7008 | 781.21 |
293.15 | 0.7998 | 786.85 |
293.15 | 0.8996 | 792.92 |
293.15 | 0.9494 | 796.1 |
293.15 | 1.0000 | 799.44 |
298.15 | 0.0000 | 745.38 |
298.15 | 0.0511 | 747.36 |
298.15 | 0.0989 | 749.26 |
298.15 | 0.2004 | 753.44 |
298.15 | 0.3002 | 757.75 |
298.15 | 0.4012 | 762.34 |
298.15 | 0.5005 | 767.1 |
298.15 | 0.6006 | 772.16 |
298.15 | 0.7008 | 777.53 |
298.15 | 0.7998 | 783.16 |
298.15 | 0.8996 | 789.21 |
298.15 | 0.9494 | 792.38 |
298.15 | 1.0000 | 795.7 |
303.15 | 0.0000 | 741.75 |
303.15 | 0.0511 | 743.73 |
303.15 | 0.0989 | 745.63 |
303.15 | 0.2004 | 749.8 |
303.15 | 0.3002 | 754.1 |
303.15 | 0.4012 | 758.68 |
303.15 | 0.5005 | 763.43 |
303.15 | 0.6006 | 768.48 |
303.15 | 0.7008 | 773.83 |
303.15 | 0.7998 | 779.45 |
303.15 | 0.8996 | 785.47 |
303.15 | 0.9494 | 788.64 |
303.15 | 1.0000 | 791.95 |
308.15 | 0.0000 | 738.12 |
308.15 | 0.0511 | 740.1 |
308.15 | 0.0989 | 741.99 |
308.15 | 0.2004 | 746.15 |
308.15 | 0.3002 | 750.45 |
308.15 | 0.4012 | 755.02 |
308.15 | 0.5005 | 759.76 |
308.15 | 0.6006 | 764.8 |
308.15 | 0.7008 | 770.13 |
308.15 | 0.7998 | 775.73 |
308.15 | 0.8996 | 781.73 |
308.15 | 0.9494 | 784.9 |
308.15 | 1.0000 | 788.19 |
313.15 | 0.0000 | 734.48 |
313.15 | 0.0511 | 736.45 |
313.15 | 0.0989 | 738.34 |
313.15 | 0.2004 | 742.5 |
313.15 | 0.3002 | 746.78 |
313.15 | 0.4012 | 751.35 |
313.15 | 0.5005 | 756.07 |
313.15 | 0.6006 | 761.1 |
313.15 | 0.7008 | 766.43 |
313.15 | 0.7998 | 771.99 |
313.15 | 0.8996 | 777.98 |
313.15 | 0.9494 | 781.13 |
313.15 | 1.0000 | 784.41 |
Operational conditions:
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Amount ratio of solute to solvent of Dodecane (1) - Liquid | Speed of sound, m/s - Liquid |
293.15 | 0.3332 | 1317.5 |
293.15 | 1.0002 | 1308.8 |
293.15 | 3.0005 | 1302.6 |
303.15 | 0.3332 | 1278.4 |
303.15 | 1.0002 | 1270.1 |
303.15 | 3.0005 | 1264.3 |
313.15 | 0.3332 | 1239.9 |
313.15 | 1.0002 | 1232.0 |
313.15 | 3.0005 | 1226.5 |
323.15 | 0.3332 | 1202.0 |
323.15 | 1.0002 | 1194.6 |
323.15 | 3.0005 | 1189.3 |
333.15 | 0.3332 | 1164.8 |
333.15 | 1.0002 | 1157.9 |
333.15 | 3.0005 | 1152.9 |
293.15 | 0.3332 | 1317.3 |
293.15 | 1.0001 | 1309.0 |
293.15 | 2.9949 | 1302.4 |
303.15 | 0.3332 | 1278.1 |
303.15 | 1.0001 | 1270.4 |
303.15 | 2.9949 | 1264.0 |
313.15 | 0.3332 | 1239.7 |
313.15 | 1.0001 | 1232.3 |
313.15 | 2.9949 | 1226.2 |
323.15 | 0.3332 | 1201.8 |
323.15 | 1.0001 | 1194.8 |
323.15 | 2.9949 | 1189.0 |
333.15 | 0.3332 | 1164.7 |
333.15 | 1.0001 | 1158.1 |
333.15 | 2.9949 | 1152.5 |
Operational conditions:
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Amount ratio of solute to solvent of Dodecane (1) - Liquid | Speed of sound, m/s - Liquid |
293.15 | 0.3332 | 1317.5 |
293.15 | 1.0002 | 1308.8 |
293.15 | 3.0005 | 1302.6 |
303.15 | 0.3332 | 1278.4 |
303.15 | 1.0002 | 1270.1 |
303.15 | 3.0005 | 1264.3 |
313.15 | 0.3332 | 1239.9 |
313.15 | 1.0002 | 1232.0 |
313.15 | 3.0005 | 1226.5 |
323.15 | 0.3332 | 1202.0 |
323.15 | 1.0002 | 1194.6 |
323.15 | 3.0005 | 1189.3 |
333.15 | 0.3332 | 1164.8 |
333.15 | 1.0002 | 1157.9 |
333.15 | 3.0005 | 1152.9 |
293.15 | 0.3332 | 1317.3 |
293.15 | 1.0001 | 1309.0 |
293.15 | 2.9949 | 1302.4 |
303.15 | 0.3332 | 1278.1 |
303.15 | 1.0001 | 1270.4 |
303.15 | 2.9949 | 1264.0 |
313.15 | 0.3332 | 1239.7 |
313.15 | 1.0001 | 1232.3 |
313.15 | 2.9949 | 1226.2 |
323.15 | 0.3332 | 1201.8 |
323.15 | 1.0001 | 1194.8 |
323.15 | 2.9949 | 1189.0 |
333.15 | 0.3332 | 1164.7 |
333.15 | 1.0001 | 1158.1 |
333.15 | 2.9949 | 1152.5 |
Operational condition: Temperature, K = 294.5 (Liquid)
Amount ratio of solute to solvent of Dodecane (1) - Liquid | Surface tension liquid-gas, N/m - Liquid |
---|---|
0.3332 | 0.0261 |
1.0002 | 0.0256 |
3.0005 | 0.0253 |
0.3335 | 0.0261 |
0.9998 | 0.0258 |
2.9968 | 0.0254 |
Operational condition: Temperature, K = 294.5 (Liquid)
Amount ratio of solute to solvent of Dodecane (1) - Liquid | Surface tension liquid-gas, N/m - Liquid |
---|---|
0.3332 | 0.0261 |
1.0002 | 0.0256 |
3.0005 | 0.0253 |
0.3335 | 0.0261 |
0.9998 | 0.0258 |
2.9968 | 0.0254 |