Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Naphthalene, decahydro-, trans- (2) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0000 | 0.0012 |
| 293.15 | 0.1041 | 0.0012 |
| 293.15 | 0.2052 | 0.0013 |
| 293.15 | 0.3027 | 0.0013 |
| 293.15 | 0.3999 | 0.0014 |
| 293.15 | 0.4997 | 0.0014 |
| 293.15 | 0.5991 | 0.0015 |
| 293.15 | 0.6991 | 0.0016 |
| 293.15 | 0.8019 | 0.0018 |
| 293.15 | 0.8992 | 0.0019 |
| 293.15 | 1.0000 | 0.0021 |
| 298.15 | 0.0000 | 0.0011 |
| 298.15 | 0.1041 | 0.0011 |
| 298.15 | 0.2052 | 0.0012 |
| 298.15 | 0.3027 | 0.0012 |
| 298.15 | 0.3999 | 0.0013 |
| 298.15 | 0.4997 | 0.0013 |
| 298.15 | 0.5991 | 0.0014 |
| 298.15 | 0.6991 | 0.0015 |
| 298.15 | 0.8019 | 0.0016 |
| 298.15 | 0.8992 | 0.0017 |
| 298.15 | 1.0000 | 0.0019 |
| 303.15 | 0.0000 | 0.0010 |
| 303.15 | 0.1041 | 0.0010 |
| 303.15 | 0.2052 | 0.0011 |
| 303.15 | 0.3027 | 0.0011 |
| 303.15 | 0.3999 | 0.0012 |
| 303.15 | 0.4997 | 0.0012 |
| 303.15 | 0.5991 | 0.0013 |
| 303.15 | 0.6991 | 0.0014 |
| 303.15 | 0.8019 | 0.0015 |
| 303.15 | 0.8992 | 0.0016 |
| 303.15 | 1.0000 | 0.0018 |
| 308.15 | 0.0000 | 0.0009 |
| 308.15 | 0.1041 | 0.0010 |
| 308.15 | 0.2052 | 0.0010 |
| 308.15 | 0.3027 | 0.0010 |
| 308.15 | 0.3999 | 0.0011 |
| 308.15 | 0.4997 | 0.0011 |
| 308.15 | 0.5991 | 0.0012 |
| 308.15 | 0.6991 | 0.0013 |
| 308.15 | 0.8019 | 0.0014 |
| 308.15 | 0.8992 | 0.0015 |
| 308.15 | 1.0000 | 0.0016 |
| 313.15 | 0.0000 | 0.0009 |
| 313.15 | 0.1041 | 0.0009 |
| 313.15 | 0.2052 | 0.0009 |
| 313.15 | 0.3027 | 0.0010 |
| 313.15 | 0.3999 | 0.0010 |
| 313.15 | 0.4997 | 0.0011 |
| 313.15 | 0.5991 | 0.0011 |
| 313.15 | 0.6991 | 0.0012 |
| 313.15 | 0.8019 | 0.0013 |
| 313.15 | 0.8992 | 0.0014 |
| 313.15 | 1.0000 | 0.0015 |
| 318.15 | 0.0000 | 0.0008 |
| 318.15 | 0.1041 | 0.0008 |
| 318.15 | 0.2052 | 0.0009 |
| 318.15 | 0.3027 | 0.0009 |
| 318.15 | 0.3999 | 0.0009 |
| 318.15 | 0.4997 | 0.0010 |
| 318.15 | 0.5991 | 0.0010 |
| 318.15 | 0.6991 | 0.0011 |
| 318.15 | 0.8019 | 0.0012 |
| 318.15 | 0.8992 | 0.0013 |
| 318.15 | 1.0000 | 0.0014 |
| 323.15 | 0.0000 | 0.0007 |
| 323.15 | 0.1041 | 0.0008 |
| 323.15 | 0.2052 | 0.0008 |
| 323.15 | 0.3027 | 0.0009 |
| 323.15 | 0.3999 | 0.0009 |
| 323.15 | 0.4997 | 0.0009 |
| 323.15 | 0.5991 | 0.0010 |
| 323.15 | 0.6991 | 0.0010 |
| 323.15 | 0.8019 | 0.0011 |
| 323.15 | 0.8992 | 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- (2) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0000 | 0.0012 |
| 293.15 | 0.1041 | 0.0012 |
| 293.15 | 0.2052 | 0.0013 |
| 293.15 | 0.3027 | 0.0013 |
| 293.15 | 0.3999 | 0.0014 |
| 293.15 | 0.4997 | 0.0014 |
| 293.15 | 0.5991 | 0.0015 |
| 293.15 | 0.6991 | 0.0016 |
| 293.15 | 0.8019 | 0.0018 |
| 293.15 | 0.8992 | 0.0019 |
| 293.15 | 1.0000 | 0.0021 |
| 298.15 | 0.0000 | 0.0011 |
| 298.15 | 0.1041 | 0.0011 |
| 298.15 | 0.2052 | 0.0012 |
| 298.15 | 0.3027 | 0.0012 |
| 298.15 | 0.3999 | 0.0013 |
| 298.15 | 0.4997 | 0.0013 |
| 298.15 | 0.5991 | 0.0014 |
| 298.15 | 0.6991 | 0.0015 |
| 298.15 | 0.8019 | 0.0016 |
| 298.15 | 0.8992 | 0.0017 |
| 298.15 | 1.0000 | 0.0019 |
| 303.15 | 0.0000 | 0.0010 |
| 303.15 | 0.1041 | 0.0010 |
| 303.15 | 0.2052 | 0.0011 |
| 303.15 | 0.3027 | 0.0011 |
| 303.15 | 0.3999 | 0.0012 |
| 303.15 | 0.4997 | 0.0012 |
| 303.15 | 0.5991 | 0.0013 |
| 303.15 | 0.6991 | 0.0014 |
| 303.15 | 0.8019 | 0.0015 |
| 303.15 | 0.8992 | 0.0016 |
| 303.15 | 1.0000 | 0.0018 |
| 308.15 | 0.0000 | 0.0009 |
| 308.15 | 0.1041 | 0.0010 |
| 308.15 | 0.2052 | 0.0010 |
| 308.15 | 0.3027 | 0.0010 |
| 308.15 | 0.3999 | 0.0011 |
| 308.15 | 0.4997 | 0.0011 |
| 308.15 | 0.5991 | 0.0012 |
| 308.15 | 0.6991 | 0.0013 |
| 308.15 | 0.8019 | 0.0014 |
| 308.15 | 0.8992 | 0.0015 |
| 308.15 | 1.0000 | 0.0016 |
| 313.15 | 0.0000 | 0.0009 |
| 313.15 | 0.1041 | 0.0009 |
| 313.15 | 0.2052 | 0.0009 |
| 313.15 | 0.3027 | 0.0010 |
| 313.15 | 0.3999 | 0.0010 |
| 313.15 | 0.4997 | 0.0011 |
| 313.15 | 0.5991 | 0.0011 |
| 313.15 | 0.6991 | 0.0012 |
| 313.15 | 0.8019 | 0.0013 |
| 313.15 | 0.8992 | 0.0014 |
| 313.15 | 1.0000 | 0.0015 |
| 318.15 | 0.0000 | 0.0008 |
| 318.15 | 0.1041 | 0.0008 |
| 318.15 | 0.2052 | 0.0009 |
| 318.15 | 0.3027 | 0.0009 |
| 318.15 | 0.3999 | 0.0009 |
| 318.15 | 0.4997 | 0.0010 |
| 318.15 | 0.5991 | 0.0010 |
| 318.15 | 0.6991 | 0.0011 |
| 318.15 | 0.8019 | 0.0012 |
| 318.15 | 0.8992 | 0.0013 |
| 318.15 | 1.0000 | 0.0014 |
| 323.15 | 0.0000 | 0.0007 |
| 323.15 | 0.1041 | 0.0008 |
| 323.15 | 0.2052 | 0.0008 |
| 323.15 | 0.3027 | 0.0009 |
| 323.15 | 0.3999 | 0.0009 |
| 323.15 | 0.4997 | 0.0009 |
| 323.15 | 0.5991 | 0.0010 |
| 323.15 | 0.6991 | 0.0010 |
| 323.15 | 0.8019 | 0.0011 |
| 323.15 | 0.8992 | 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- (2) - Liquid | Refractive index (Na D-line) - Liquid |
| 298.15 | 0.0000 | 1.4138 |
| 298.15 | 0.1041 | 1.4188 |
| 298.15 | 0.2052 | 1.423 |
| 298.15 | 0.3027 | 1.4272 |
| 298.15 | 0.3999 | 1.4319 |
| 298.15 | 0.4997 | 1.4367 |
| 298.15 | 0.5991 | 1.4421 |
| 298.15 | 0.6991 | 1.4476 |
| 298.15 | 0.8019 | 1.4535 |
| 298.15 | 0.8992 | 1.4594 |
| 298.15 | 1.0000 | 1.4662 |
| 308.15 | 0.0000 | 1.4095 |
| 308.15 | 0.1041 | 1.4143 |
| 308.15 | 0.2052 | 1.419 |
| 308.15 | 0.3027 | 1.4232 |
| 308.15 | 0.3999 | 1.428 |
| 308.15 | 0.4997 | 1.4331 |
| 308.15 | 0.5991 | 1.4378 |
| 308.15 | 0.6991 | 1.4434 |
| 308.15 | 0.8019 | 1.4496 |
| 308.15 | 0.8992 | 1.4559 |
| 308.15 | 1.0000 | 1.4618 |
| 318.15 | 0.0000 | 1.4058 |
| 318.15 | 0.1041 | 1.4099 |
| 318.15 | 0.2052 | 1.4146 |
| 318.15 | 0.3027 | 1.4191 |
| 318.15 | 0.3999 | 1.4236 |
| 318.15 | 0.4997 | 1.4281 |
| 318.15 | 0.5991 | 1.4332 |
| 318.15 | 0.6991 | 1.439 |
| 318.15 | 0.8019 | 1.4452 |
| 318.15 | 0.8992 | 1.4515 |
| 318.15 | 1.0000 | 1.4581 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Naphthalene, decahydro-, trans- (2) - Liquid | Refractive index (Na D-line) - Liquid |
| 298.15 | 0.0000 | 1.4138 |
| 298.15 | 0.1041 | 1.4188 |
| 298.15 | 0.2052 | 1.423 |
| 298.15 | 0.3027 | 1.4272 |
| 298.15 | 0.3999 | 1.4319 |
| 298.15 | 0.4997 | 1.4367 |
| 298.15 | 0.5991 | 1.4421 |
| 298.15 | 0.6991 | 1.4476 |
| 298.15 | 0.8019 | 1.4535 |
| 298.15 | 0.8992 | 1.4594 |
| 298.15 | 1.0000 | 1.4662 |
| 308.15 | 0.0000 | 1.4095 |
| 308.15 | 0.1041 | 1.4143 |
| 308.15 | 0.2052 | 1.419 |
| 308.15 | 0.3027 | 1.4232 |
| 308.15 | 0.3999 | 1.428 |
| 308.15 | 0.4997 | 1.4331 |
| 308.15 | 0.5991 | 1.4378 |
| 308.15 | 0.6991 | 1.4434 |
| 308.15 | 0.8019 | 1.4496 |
| 308.15 | 0.8992 | 1.4559 |
| 308.15 | 1.0000 | 1.4618 |
| 318.15 | 0.0000 | 1.4058 |
| 318.15 | 0.1041 | 1.4099 |
| 318.15 | 0.2052 | 1.4146 |
| 318.15 | 0.3027 | 1.4191 |
| 318.15 | 0.3999 | 1.4236 |
| 318.15 | 0.4997 | 1.4281 |
| 318.15 | 0.5991 | 1.4332 |
| 318.15 | 0.6991 | 1.439 |
| 318.15 | 0.8019 | 1.4452 |
| 318.15 | 0.8992 | 1.4515 |
| 318.15 | 1.0000 | 1.4581 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Naphthalene, decahydro-, trans- (2) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 740.28 |
| 293.15 | 0.1041 | 751.02 |
| 293.15 | 0.2052 | 761.89 |
| 293.15 | 0.3027 | 772.86 |
| 293.15 | 0.3999 | 784.34 |
| 293.15 | 0.4997 | 796.76 |
| 293.15 | 0.5991 | 809.74 |
| 293.15 | 0.6991 | 823.47 |
| 293.15 | 0.8019 | 838.4 |
| 293.15 | 0.8992 | 853.35 |
| 293.15 | 1.0000 | 869.78 |
| 298.15 | 0.0000 | 736.63 |
| 298.15 | 0.1041 | 747.37 |
| 298.15 | 0.2052 | 758.22 |
| 298.15 | 0.3027 | 769.19 |
| 298.15 | 0.3999 | 780.66 |
| 298.15 | 0.4997 | 793.09 |
| 298.15 | 0.5991 | 806.06 |
| 298.15 | 0.6991 | 819.79 |
| 298.15 | 0.8019 | 834.72 |
| 298.15 | 0.8992 | 849.65 |
| 298.15 | 1.0000 | 866.07 |
| 303.15 | 0.0000 | 732.93 |
| 303.15 | 0.1041 | 743.67 |
| 303.15 | 0.2052 | 754.53 |
| 303.15 | 0.3027 | 765.5 |
| 303.15 | 0.3999 | 776.97 |
| 303.15 | 0.4997 | 789.4 |
| 303.15 | 0.5991 | 802.37 |
| 303.15 | 0.6991 | 816.09 |
| 303.15 | 0.8019 | 831.02 |
| 303.15 | 0.8992 | 845.94 |
| 303.15 | 1.0000 | 862.34 |
| 308.15 | 0.0000 | 729.22 |
| 308.15 | 0.1041 | 739.97 |
| 308.15 | 0.2052 | 750.83 |
| 308.15 | 0.3027 | 761.8 |
| 308.15 | 0.3999 | 773.28 |
| 308.15 | 0.4997 | 785.7 |
| 308.15 | 0.5991 | 798.67 |
| 308.15 | 0.6991 | 812.39 |
| 308.15 | 0.8019 | 827.31 |
| 308.15 | 0.8992 | 842.22 |
| 308.15 | 1.0000 | 858.61 |
| 313.15 | 0.0000 | 725.51 |
| 313.15 | 0.1041 | 736.25 |
| 313.15 | 0.2052 | 747.11 |
| 313.15 | 0.3027 | 758.09 |
| 313.15 | 0.3999 | 769.57 |
| 313.15 | 0.4997 | 781.99 |
| 313.15 | 0.5991 | 794.96 |
| 313.15 | 0.6991 | 808.67 |
| 313.15 | 0.8019 | 823.59 |
| 313.15 | 0.8992 | 838.5 |
| 313.15 | 1.0000 | 854.88 |
| 318.15 | 0.0000 | 721.78 |
| 318.15 | 0.1041 | 732.53 |
| 318.15 | 0.2052 | 743.39 |
| 318.15 | 0.3027 | 754.37 |
| 318.15 | 0.3999 | 765.85 |
| 318.15 | 0.4997 | 778.27 |
| 318.15 | 0.5991 | 791.24 |
| 318.15 | 0.6991 | 804.95 |
| 318.15 | 0.8019 | 819.87 |
| 318.15 | 0.8992 | 834.77 |
| 318.15 | 1.0000 | 851.14 |
| 323.15 | 0.0000 | 718.04 |
| 323.15 | 0.1041 | 728.79 |
| 323.15 | 0.2052 | 739.66 |
| 323.15 | 0.3027 | 750.64 |
| 323.15 | 0.3999 | 762.12 |
| 323.15 | 0.4997 | 774.54 |
| 323.15 | 0.5991 | 787.51 |
| 323.15 | 0.6991 | 801.22 |
| 323.15 | 0.8019 | 816.14 |
| 323.15 | 0.8992 | 831.03 |
| 323.15 | 1.0000 | 847.4 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Naphthalene, decahydro-, trans- (2) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 740.28 |
| 293.15 | 0.1041 | 751.02 |
| 293.15 | 0.2052 | 761.89 |
| 293.15 | 0.3027 | 772.86 |
| 293.15 | 0.3999 | 784.34 |
| 293.15 | 0.4997 | 796.76 |
| 293.15 | 0.5991 | 809.74 |
| 293.15 | 0.6991 | 823.47 |
| 293.15 | 0.8019 | 838.4 |
| 293.15 | 0.8992 | 853.35 |
| 293.15 | 1.0000 | 869.78 |
| 298.15 | 0.0000 | 736.63 |
| 298.15 | 0.1041 | 747.37 |
| 298.15 | 0.2052 | 758.22 |
| 298.15 | 0.3027 | 769.19 |
| 298.15 | 0.3999 | 780.66 |
| 298.15 | 0.4997 | 793.09 |
| 298.15 | 0.5991 | 806.06 |
| 298.15 | 0.6991 | 819.79 |
| 298.15 | 0.8019 | 834.72 |
| 298.15 | 0.8992 | 849.65 |
| 298.15 | 1.0000 | 866.07 |
| 303.15 | 0.0000 | 732.93 |
| 303.15 | 0.1041 | 743.67 |
| 303.15 | 0.2052 | 754.53 |
| 303.15 | 0.3027 | 765.5 |
| 303.15 | 0.3999 | 776.97 |
| 303.15 | 0.4997 | 789.4 |
| 303.15 | 0.5991 | 802.37 |
| 303.15 | 0.6991 | 816.09 |
| 303.15 | 0.8019 | 831.02 |
| 303.15 | 0.8992 | 845.94 |
| 303.15 | 1.0000 | 862.34 |
| 308.15 | 0.0000 | 729.22 |
| 308.15 | 0.1041 | 739.97 |
| 308.15 | 0.2052 | 750.83 |
| 308.15 | 0.3027 | 761.8 |
| 308.15 | 0.3999 | 773.28 |
| 308.15 | 0.4997 | 785.7 |
| 308.15 | 0.5991 | 798.67 |
| 308.15 | 0.6991 | 812.39 |
| 308.15 | 0.8019 | 827.31 |
| 308.15 | 0.8992 | 842.22 |
| 308.15 | 1.0000 | 858.61 |
| 313.15 | 0.0000 | 725.51 |
| 313.15 | 0.1041 | 736.25 |
| 313.15 | 0.2052 | 747.11 |
| 313.15 | 0.3027 | 758.09 |
| 313.15 | 0.3999 | 769.57 |
| 313.15 | 0.4997 | 781.99 |
| 313.15 | 0.5991 | 794.96 |
| 313.15 | 0.6991 | 808.67 |
| 313.15 | 0.8019 | 823.59 |
| 313.15 | 0.8992 | 838.5 |
| 313.15 | 1.0000 | 854.88 |
| 318.15 | 0.0000 | 721.78 |
| 318.15 | 0.1041 | 732.53 |
| 318.15 | 0.2052 | 743.39 |
| 318.15 | 0.3027 | 754.37 |
| 318.15 | 0.3999 | 765.85 |
| 318.15 | 0.4997 | 778.27 |
| 318.15 | 0.5991 | 791.24 |
| 318.15 | 0.6991 | 804.95 |
| 318.15 | 0.8019 | 819.87 |
| 318.15 | 0.8992 | 834.77 |
| 318.15 | 1.0000 | 851.14 |
| 323.15 | 0.0000 | 718.04 |
| 323.15 | 0.1041 | 728.79 |
| 323.15 | 0.2052 | 739.66 |
| 323.15 | 0.3027 | 750.64 |
| 323.15 | 0.3999 | 762.12 |
| 323.15 | 0.4997 | 774.54 |
| 323.15 | 0.5991 | 787.51 |
| 323.15 | 0.6991 | 801.22 |
| 323.15 | 0.8019 | 816.14 |
| 323.15 | 0.8992 | 831.03 |
| 323.15 | 1.0000 | 847.4 |