Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Naphthalene, decahydro-, trans- (1) - Liquid | Viscosity, Pa*s - Liquid |
293.15 | 0.0000 | 0.0009 |
293.15 | 0.1035 | 0.0010 |
293.15 | 0.2016 | 0.0010 |
293.15 | 0.3001 | 0.0011 |
293.15 | 0.3994 | 0.0012 |
293.15 | 0.5036 | 0.0013 |
293.15 | 0.6062 | 0.0014 |
293.15 | 0.6989 | 0.0015 |
293.15 | 0.7891 | 0.0016 |
293.15 | 0.8949 | 0.0018 |
293.15 | 1.0000 | 0.0021 |
298.15 | 0.0000 | 0.0009 |
298.15 | 0.1035 | 0.0009 |
298.15 | 0.2016 | 0.0010 |
298.15 | 0.3001 | 0.0010 |
298.15 | 0.3994 | 0.0011 |
298.15 | 0.5036 | 0.0012 |
298.15 | 0.6062 | 0.0013 |
298.15 | 0.6989 | 0.0014 |
298.15 | 0.7891 | 0.0015 |
298.15 | 0.8949 | 0.0017 |
298.15 | 1.0000 | 0.0019 |
303.15 | 0.0000 | 0.0008 |
303.15 | 0.1035 | 0.0008 |
303.15 | 0.2016 | 0.0009 |
303.15 | 0.3001 | 0.0009 |
303.15 | 0.3994 | 0.0010 |
303.15 | 0.5036 | 0.0011 |
303.15 | 0.6062 | 0.0012 |
303.15 | 0.6989 | 0.0013 |
303.15 | 0.7891 | 0.0014 |
303.15 | 0.8949 | 0.0016 |
303.15 | 1.0000 | 0.0018 |
308.15 | 0.0000 | 0.0008 |
308.15 | 0.1035 | 0.0008 |
308.15 | 0.2016 | 0.0008 |
308.15 | 0.3001 | 0.0009 |
308.15 | 0.3994 | 0.0009 |
308.15 | 0.5036 | 0.0010 |
308.15 | 0.6062 | 0.0011 |
308.15 | 0.6989 | 0.0012 |
308.15 | 0.7891 | 0.0013 |
308.15 | 0.8949 | 0.0014 |
308.15 | 1.0000 | 0.0016 |
313.15 | 0.0000 | 0.0007 |
313.15 | 0.1035 | 0.0007 |
313.15 | 0.2016 | 0.0008 |
313.15 | 0.3001 | 0.0008 |
313.15 | 0.3994 | 0.0009 |
313.15 | 0.5036 | 0.0009 |
313.15 | 0.6062 | 0.0010 |
313.15 | 0.6989 | 0.0011 |
313.15 | 0.7891 | 0.0012 |
313.15 | 0.8949 | 0.0013 |
313.15 | 1.0000 | 0.0015 |
318.15 | 0.0000 | 0.0007 |
318.15 | 0.1035 | 0.0007 |
318.15 | 0.2016 | 0.0007 |
318.15 | 0.3001 | 0.0008 |
318.15 | 0.3994 | 0.0008 |
318.15 | 0.5036 | 0.0009 |
318.15 | 0.6062 | 0.0010 |
318.15 | 0.6989 | 0.0010 |
318.15 | 0.7891 | 0.0011 |
318.15 | 0.8949 | 0.0012 |
318.15 | 1.0000 | 0.0014 |
323.15 | 0.0000 | 0.0006 |
323.15 | 0.1035 | 0.0007 |
323.15 | 0.2016 | 0.0007 |
323.15 | 0.3001 | 0.0007 |
323.15 | 0.3994 | 0.0008 |
323.15 | 0.5036 | 0.0008 |
323.15 | 0.6062 | 0.0009 |
323.15 | 0.6989 | 0.0010 |
323.15 | 0.7891 | 0.0010 |
323.15 | 0.8949 | 0.0012 |
323.15 | 1.0000 | 0.0013 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Naphthalene, decahydro-, trans- (1) - Liquid | Viscosity, Pa*s - Liquid |
293.15 | 0.0000 | 0.0009 |
293.15 | 0.1035 | 0.0010 |
293.15 | 0.2016 | 0.0010 |
293.15 | 0.3001 | 0.0011 |
293.15 | 0.3994 | 0.0012 |
293.15 | 0.5036 | 0.0013 |
293.15 | 0.6062 | 0.0014 |
293.15 | 0.6989 | 0.0015 |
293.15 | 0.7891 | 0.0016 |
293.15 | 0.8949 | 0.0018 |
293.15 | 1.0000 | 0.0021 |
298.15 | 0.0000 | 0.0009 |
298.15 | 0.1035 | 0.0009 |
298.15 | 0.2016 | 0.0010 |
298.15 | 0.3001 | 0.0010 |
298.15 | 0.3994 | 0.0011 |
298.15 | 0.5036 | 0.0012 |
298.15 | 0.6062 | 0.0013 |
298.15 | 0.6989 | 0.0014 |
298.15 | 0.7891 | 0.0015 |
298.15 | 0.8949 | 0.0017 |
298.15 | 1.0000 | 0.0019 |
303.15 | 0.0000 | 0.0008 |
303.15 | 0.1035 | 0.0008 |
303.15 | 0.2016 | 0.0009 |
303.15 | 0.3001 | 0.0009 |
303.15 | 0.3994 | 0.0010 |
303.15 | 0.5036 | 0.0011 |
303.15 | 0.6062 | 0.0012 |
303.15 | 0.6989 | 0.0013 |
303.15 | 0.7891 | 0.0014 |
303.15 | 0.8949 | 0.0016 |
303.15 | 1.0000 | 0.0018 |
308.15 | 0.0000 | 0.0008 |
308.15 | 0.1035 | 0.0008 |
308.15 | 0.2016 | 0.0008 |
308.15 | 0.3001 | 0.0009 |
308.15 | 0.3994 | 0.0009 |
308.15 | 0.5036 | 0.0010 |
308.15 | 0.6062 | 0.0011 |
308.15 | 0.6989 | 0.0012 |
308.15 | 0.7891 | 0.0013 |
308.15 | 0.8949 | 0.0014 |
308.15 | 1.0000 | 0.0016 |
313.15 | 0.0000 | 0.0007 |
313.15 | 0.1035 | 0.0007 |
313.15 | 0.2016 | 0.0008 |
313.15 | 0.3001 | 0.0008 |
313.15 | 0.3994 | 0.0009 |
313.15 | 0.5036 | 0.0009 |
313.15 | 0.6062 | 0.0010 |
313.15 | 0.6989 | 0.0011 |
313.15 | 0.7891 | 0.0012 |
313.15 | 0.8949 | 0.0013 |
313.15 | 1.0000 | 0.0015 |
318.15 | 0.0000 | 0.0007 |
318.15 | 0.1035 | 0.0007 |
318.15 | 0.2016 | 0.0007 |
318.15 | 0.3001 | 0.0008 |
318.15 | 0.3994 | 0.0008 |
318.15 | 0.5036 | 0.0009 |
318.15 | 0.6062 | 0.0010 |
318.15 | 0.6989 | 0.0010 |
318.15 | 0.7891 | 0.0011 |
318.15 | 0.8949 | 0.0012 |
318.15 | 1.0000 | 0.0014 |
323.15 | 0.0000 | 0.0006 |
323.15 | 0.1035 | 0.0007 |
323.15 | 0.2016 | 0.0007 |
323.15 | 0.3001 | 0.0007 |
323.15 | 0.3994 | 0.0008 |
323.15 | 0.5036 | 0.0008 |
323.15 | 0.6062 | 0.0009 |
323.15 | 0.6989 | 0.0010 |
323.15 | 0.7891 | 0.0010 |
323.15 | 0.8949 | 0.0012 |
323.15 | 1.0000 | 0.0013 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Naphthalene, decahydro-, trans- (1) - Liquid | Refractive index (Na D-line) - Liquid |
298.15 | 0.0000 | 1.4098 |
298.15 | 0.1035 | 1.4144 |
298.15 | 0.2016 | 1.4192 |
298.15 | 0.3001 | 1.4243 |
298.15 | 0.3994 | 1.4301 |
298.15 | 0.5036 | 1.4355 |
298.15 | 0.6062 | 1.4414 |
298.15 | 0.6989 | 1.4471 |
298.15 | 0.7891 | 1.4524 |
298.15 | 0.8949 | 1.4592 |
298.15 | 1.0000 | 1.4662 |
308.15 | 0.0000 | 1.4052 |
308.15 | 0.1035 | 1.4099 |
308.15 | 0.2016 | 1.4153 |
308.15 | 0.3001 | 1.4204 |
308.15 | 0.3994 | 1.4256 |
308.15 | 0.5036 | 1.4317 |
308.15 | 0.6062 | 1.4371 |
308.15 | 0.6989 | 1.4431 |
308.15 | 0.7891 | 1.4484 |
308.15 | 0.8949 | 1.4553 |
308.15 | 1.0000 | 1.4618 |
318.15 | 0.0000 | 1.4 |
318.15 | 0.1035 | 1.4055 |
318.15 | 0.2016 | 1.4112 |
318.15 | 0.3001 | 1.4162 |
318.15 | 0.3994 | 1.4211 |
318.15 | 0.5036 | 1.4271 |
318.15 | 0.6062 | 1.4336 |
318.15 | 0.6989 | 1.4389 |
318.15 | 0.7891 | 1.4448 |
318.15 | 0.8949 | 1.4518 |
318.15 | 1.0000 | 1.4581 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Naphthalene, decahydro-, trans- (1) - Liquid | Refractive index (Na D-line) - Liquid |
298.15 | 0.0000 | 1.4098 |
298.15 | 0.1035 | 1.4144 |
298.15 | 0.2016 | 1.4192 |
298.15 | 0.3001 | 1.4243 |
298.15 | 0.3994 | 1.4301 |
298.15 | 0.5036 | 1.4355 |
298.15 | 0.6062 | 1.4414 |
298.15 | 0.6989 | 1.4471 |
298.15 | 0.7891 | 1.4524 |
298.15 | 0.8949 | 1.4592 |
298.15 | 1.0000 | 1.4662 |
308.15 | 0.0000 | 1.4052 |
308.15 | 0.1035 | 1.4099 |
308.15 | 0.2016 | 1.4153 |
308.15 | 0.3001 | 1.4204 |
308.15 | 0.3994 | 1.4256 |
308.15 | 0.5036 | 1.4317 |
308.15 | 0.6062 | 1.4371 |
308.15 | 0.6989 | 1.4431 |
308.15 | 0.7891 | 1.4484 |
308.15 | 0.8949 | 1.4553 |
308.15 | 1.0000 | 1.4618 |
318.15 | 0.0000 | 1.4 |
318.15 | 0.1035 | 1.4055 |
318.15 | 0.2016 | 1.4112 |
318.15 | 0.3001 | 1.4162 |
318.15 | 0.3994 | 1.4211 |
318.15 | 0.5036 | 1.4271 |
318.15 | 0.6062 | 1.4336 |
318.15 | 0.6989 | 1.4389 |
318.15 | 0.7891 | 1.4448 |
318.15 | 0.8949 | 1.4518 |
318.15 | 1.0000 | 1.4581 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Naphthalene, decahydro-, trans- (1) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.0000 | 731.14 |
293.15 | 0.1035 | 743.5 |
293.15 | 0.2016 | 755.54 |
293.15 | 0.3001 | 768.0 |
293.15 | 0.3994 | 781.01 |
293.15 | 0.5036 | 795.1 |
293.15 | 0.6062 | 809.53 |
293.15 | 0.6989 | 822.98 |
293.15 | 0.7891 | 836.46 |
293.15 | 0.8949 | 852.8 |
293.15 | 1.0000 | 869.78 |
298.15 | 0.0000 | 727.43 |
298.15 | 0.1035 | 739.74 |
298.15 | 0.2016 | 751.79 |
298.15 | 0.3001 | 764.27 |
298.15 | 0.3994 | 777.28 |
298.15 | 0.5036 | 791.38 |
298.15 | 0.6062 | 805.81 |
298.15 | 0.6989 | 819.26 |
298.15 | 0.7891 | 832.75 |
298.15 | 0.8949 | 849.09 |
298.15 | 1.0000 | 866.07 |
303.15 | 0.0000 | 723.64 |
303.15 | 0.1035 | 735.97 |
303.15 | 0.2016 | 748.02 |
303.15 | 0.3001 | 760.51 |
303.15 | 0.3994 | 773.52 |
303.15 | 0.5036 | 787.63 |
303.15 | 0.6062 | 802.07 |
303.15 | 0.6989 | 815.53 |
303.15 | 0.7891 | 829.02 |
303.15 | 0.8949 | 845.37 |
303.15 | 1.0000 | 862.34 |
308.15 | 0.0000 | 719.84 |
308.15 | 0.1035 | 732.17 |
308.15 | 0.2016 | 744.24 |
308.15 | 0.3001 | 756.74 |
308.15 | 0.3994 | 769.76 |
308.15 | 0.5036 | 783.88 |
308.15 | 0.6062 | 798.32 |
308.15 | 0.6989 | 811.79 |
308.15 | 0.7891 | 825.29 |
308.15 | 0.8949 | 841.64 |
308.15 | 1.0000 | 858.61 |
313.15 | 0.0000 | 716.03 |
313.15 | 0.1035 | 728.37 |
313.15 | 0.2016 | 740.45 |
313.15 | 0.3001 | 752.95 |
313.15 | 0.3994 | 765.99 |
313.15 | 0.5036 | 780.11 |
313.15 | 0.6062 | 794.56 |
313.15 | 0.6989 | 808.04 |
313.15 | 0.7891 | 821.54 |
313.15 | 0.8949 | 837.9 |
313.15 | 1.0000 | 854.88 |
318.15 | 0.0000 | 712.2 |
318.15 | 0.1035 | 724.55 |
318.15 | 0.2016 | 736.64 |
318.15 | 0.3001 | 749.16 |
318.15 | 0.3994 | 762.2 |
318.15 | 0.5036 | 776.34 |
318.15 | 0.6062 | 790.8 |
318.15 | 0.6989 | 804.28 |
318.15 | 0.7891 | 817.79 |
318.15 | 0.8949 | 834.16 |
318.15 | 1.0000 | 851.14 |
323.15 | 0.0000 | 708.36 |
323.15 | 0.1035 | 720.72 |
323.15 | 0.2016 | 732.82 |
323.15 | 0.3001 | 745.35 |
323.15 | 0.3994 | 758.4 |
323.15 | 0.5036 | 772.55 |
323.15 | 0.6062 | 787.02 |
323.15 | 0.6989 | 800.51 |
323.15 | 0.7891 | 814.04 |
323.15 | 0.8949 | 830.41 |
323.15 | 1.0000 | 847.4 |
Operational condition: Pressure, kPa = 100 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Naphthalene, decahydro-, trans- (1) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.0000 | 731.14 |
293.15 | 0.1035 | 743.5 |
293.15 | 0.2016 | 755.54 |
293.15 | 0.3001 | 768.0 |
293.15 | 0.3994 | 781.01 |
293.15 | 0.5036 | 795.1 |
293.15 | 0.6062 | 809.53 |
293.15 | 0.6989 | 822.98 |
293.15 | 0.7891 | 836.46 |
293.15 | 0.8949 | 852.8 |
293.15 | 1.0000 | 869.78 |
298.15 | 0.0000 | 727.43 |
298.15 | 0.1035 | 739.74 |
298.15 | 0.2016 | 751.79 |
298.15 | 0.3001 | 764.27 |
298.15 | 0.3994 | 777.28 |
298.15 | 0.5036 | 791.38 |
298.15 | 0.6062 | 805.81 |
298.15 | 0.6989 | 819.26 |
298.15 | 0.7891 | 832.75 |
298.15 | 0.8949 | 849.09 |
298.15 | 1.0000 | 866.07 |
303.15 | 0.0000 | 723.64 |
303.15 | 0.1035 | 735.97 |
303.15 | 0.2016 | 748.02 |
303.15 | 0.3001 | 760.51 |
303.15 | 0.3994 | 773.52 |
303.15 | 0.5036 | 787.63 |
303.15 | 0.6062 | 802.07 |
303.15 | 0.6989 | 815.53 |
303.15 | 0.7891 | 829.02 |
303.15 | 0.8949 | 845.37 |
303.15 | 1.0000 | 862.34 |
308.15 | 0.0000 | 719.84 |
308.15 | 0.1035 | 732.17 |
308.15 | 0.2016 | 744.24 |
308.15 | 0.3001 | 756.74 |
308.15 | 0.3994 | 769.76 |
308.15 | 0.5036 | 783.88 |
308.15 | 0.6062 | 798.32 |
308.15 | 0.6989 | 811.79 |
308.15 | 0.7891 | 825.29 |
308.15 | 0.8949 | 841.64 |
308.15 | 1.0000 | 858.61 |
313.15 | 0.0000 | 716.03 |
313.15 | 0.1035 | 728.37 |
313.15 | 0.2016 | 740.45 |
313.15 | 0.3001 | 752.95 |
313.15 | 0.3994 | 765.99 |
313.15 | 0.5036 | 780.11 |
313.15 | 0.6062 | 794.56 |
313.15 | 0.6989 | 808.04 |
313.15 | 0.7891 | 821.54 |
313.15 | 0.8949 | 837.9 |
313.15 | 1.0000 | 854.88 |
318.15 | 0.0000 | 712.2 |
318.15 | 0.1035 | 724.55 |
318.15 | 0.2016 | 736.64 |
318.15 | 0.3001 | 749.16 |
318.15 | 0.3994 | 762.2 |
318.15 | 0.5036 | 776.34 |
318.15 | 0.6062 | 790.8 |
318.15 | 0.6989 | 804.28 |
318.15 | 0.7891 | 817.79 |
318.15 | 0.8949 | 834.16 |
318.15 | 1.0000 | 851.14 |
323.15 | 0.0000 | 708.36 |
323.15 | 0.1035 | 720.72 |
323.15 | 0.2016 | 732.82 |
323.15 | 0.3001 | 745.35 |
323.15 | 0.3994 | 758.4 |
323.15 | 0.5036 | 772.55 |
323.15 | 0.6062 | 787.02 |
323.15 | 0.6989 | 800.51 |
323.15 | 0.7891 | 814.04 |
323.15 | 0.8949 | 830.41 |
323.15 | 1.0000 | 847.4 |