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 | 0.0007 |
| 293.15 | 0.1036 | 0.0008 |
| 293.15 | 0.2018 | 0.0008 |
| 293.15 | 0.3016 | 0.0009 |
| 293.15 | 0.4042 | 0.0010 |
| 293.15 | 0.4954 | 0.0011 |
| 293.15 | 0.6009 | 0.0013 |
| 293.15 | 0.6984 | 0.0014 |
| 293.15 | 0.8001 | 0.0016 |
| 293.15 | 0.8933 | 0.0019 |
| 293.15 | 1.0000 | 0.0021 |
| 298.15 | 0.0000 | 0.0007 |
| 298.15 | 0.1036 | 0.0007 |
| 298.15 | 0.2018 | 0.0008 |
| 298.15 | 0.3016 | 0.0008 |
| 298.15 | 0.4042 | 0.0009 |
| 298.15 | 0.4954 | 0.0010 |
| 298.15 | 0.6009 | 0.0012 |
| 298.15 | 0.6984 | 0.0013 |
| 298.15 | 0.8001 | 0.0015 |
| 298.15 | 0.8933 | 0.0017 |
| 298.15 | 1.0000 | 0.0019 |
| 303.15 | 0.0000 | 0.0006 |
| 303.15 | 0.1036 | 0.0007 |
| 303.15 | 0.2018 | 0.0007 |
| 303.15 | 0.3016 | 0.0008 |
| 303.15 | 0.4042 | 0.0009 |
| 303.15 | 0.4954 | 0.0010 |
| 303.15 | 0.6009 | 0.0011 |
| 303.15 | 0.6984 | 0.0012 |
| 303.15 | 0.8001 | 0.0014 |
| 303.15 | 0.8933 | 0.0016 |
| 303.15 | 1.0000 | 0.0018 |
| 308.15 | 0.0000 | 0.0006 |
| 308.15 | 0.1036 | 0.0006 |
| 308.15 | 0.2018 | 0.0007 |
| 308.15 | 0.3016 | 0.0007 |
| 308.15 | 0.4042 | 0.0008 |
| 308.15 | 0.4954 | 0.0009 |
| 308.15 | 0.6009 | 0.0010 |
| 308.15 | 0.6984 | 0.0011 |
| 308.15 | 0.8001 | 0.0013 |
| 308.15 | 0.8933 | 0.0014 |
| 308.15 | 1.0000 | 0.0016 |
| 313.15 | 0.0000 | 0.0006 |
| 313.15 | 0.1036 | 0.0006 |
| 313.15 | 0.2018 | 0.0006 |
| 313.15 | 0.3016 | 0.0007 |
| 313.15 | 0.4042 | 0.0008 |
| 313.15 | 0.4954 | 0.0008 |
| 313.15 | 0.6009 | 0.0009 |
| 313.15 | 0.6984 | 0.0011 |
| 313.15 | 0.8001 | 0.0012 |
| 313.15 | 0.8933 | 0.0013 |
| 313.15 | 1.0000 | 0.0015 |
| 318.15 | 0.0000 | 0.0005 |
| 318.15 | 0.1036 | 0.0006 |
| 318.15 | 0.2018 | 0.0006 |
| 318.15 | 0.3016 | 0.0007 |
| 318.15 | 0.4042 | 0.0007 |
| 318.15 | 0.4954 | 0.0008 |
| 318.15 | 0.6009 | 0.0009 |
| 318.15 | 0.6984 | 0.0010 |
| 318.15 | 0.8001 | 0.0011 |
| 318.15 | 0.8933 | 0.0012 |
| 318.15 | 1.0000 | 0.0014 |
| 323.15 | 0.0000 | 0.0005 |
| 323.15 | 0.1036 | 0.0005 |
| 323.15 | 0.2018 | 0.0006 |
| 323.15 | 0.3016 | 0.0006 |
| 323.15 | 0.4042 | 0.0007 |
| 323.15 | 0.4954 | 0.0007 |
| 323.15 | 0.6009 | 0.0008 |
| 323.15 | 0.6984 | 0.0009 |
| 323.15 | 0.8001 | 0.0010 |
| 323.15 | 0.8933 | 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 | 0.0007 |
| 293.15 | 0.1036 | 0.0008 |
| 293.15 | 0.2018 | 0.0008 |
| 293.15 | 0.3016 | 0.0009 |
| 293.15 | 0.4042 | 0.0010 |
| 293.15 | 0.4954 | 0.0011 |
| 293.15 | 0.6009 | 0.0013 |
| 293.15 | 0.6984 | 0.0014 |
| 293.15 | 0.8001 | 0.0016 |
| 293.15 | 0.8933 | 0.0019 |
| 293.15 | 1.0000 | 0.0021 |
| 298.15 | 0.0000 | 0.0007 |
| 298.15 | 0.1036 | 0.0007 |
| 298.15 | 0.2018 | 0.0008 |
| 298.15 | 0.3016 | 0.0008 |
| 298.15 | 0.4042 | 0.0009 |
| 298.15 | 0.4954 | 0.0010 |
| 298.15 | 0.6009 | 0.0012 |
| 298.15 | 0.6984 | 0.0013 |
| 298.15 | 0.8001 | 0.0015 |
| 298.15 | 0.8933 | 0.0017 |
| 298.15 | 1.0000 | 0.0019 |
| 303.15 | 0.0000 | 0.0006 |
| 303.15 | 0.1036 | 0.0007 |
| 303.15 | 0.2018 | 0.0007 |
| 303.15 | 0.3016 | 0.0008 |
| 303.15 | 0.4042 | 0.0009 |
| 303.15 | 0.4954 | 0.0010 |
| 303.15 | 0.6009 | 0.0011 |
| 303.15 | 0.6984 | 0.0012 |
| 303.15 | 0.8001 | 0.0014 |
| 303.15 | 0.8933 | 0.0016 |
| 303.15 | 1.0000 | 0.0018 |
| 308.15 | 0.0000 | 0.0006 |
| 308.15 | 0.1036 | 0.0006 |
| 308.15 | 0.2018 | 0.0007 |
| 308.15 | 0.3016 | 0.0007 |
| 308.15 | 0.4042 | 0.0008 |
| 308.15 | 0.4954 | 0.0009 |
| 308.15 | 0.6009 | 0.0010 |
| 308.15 | 0.6984 | 0.0011 |
| 308.15 | 0.8001 | 0.0013 |
| 308.15 | 0.8933 | 0.0014 |
| 308.15 | 1.0000 | 0.0016 |
| 313.15 | 0.0000 | 0.0006 |
| 313.15 | 0.1036 | 0.0006 |
| 313.15 | 0.2018 | 0.0006 |
| 313.15 | 0.3016 | 0.0007 |
| 313.15 | 0.4042 | 0.0008 |
| 313.15 | 0.4954 | 0.0008 |
| 313.15 | 0.6009 | 0.0009 |
| 313.15 | 0.6984 | 0.0011 |
| 313.15 | 0.8001 | 0.0012 |
| 313.15 | 0.8933 | 0.0013 |
| 313.15 | 1.0000 | 0.0015 |
| 318.15 | 0.0000 | 0.0005 |
| 318.15 | 0.1036 | 0.0006 |
| 318.15 | 0.2018 | 0.0006 |
| 318.15 | 0.3016 | 0.0007 |
| 318.15 | 0.4042 | 0.0007 |
| 318.15 | 0.4954 | 0.0008 |
| 318.15 | 0.6009 | 0.0009 |
| 318.15 | 0.6984 | 0.0010 |
| 318.15 | 0.8001 | 0.0011 |
| 318.15 | 0.8933 | 0.0012 |
| 318.15 | 1.0000 | 0.0014 |
| 323.15 | 0.0000 | 0.0005 |
| 323.15 | 0.1036 | 0.0005 |
| 323.15 | 0.2018 | 0.0006 |
| 323.15 | 0.3016 | 0.0006 |
| 323.15 | 0.4042 | 0.0007 |
| 323.15 | 0.4954 | 0.0007 |
| 323.15 | 0.6009 | 0.0008 |
| 323.15 | 0.6984 | 0.0009 |
| 323.15 | 0.8001 | 0.0010 |
| 323.15 | 0.8933 | 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 | Refractive index (Na D-line) - Liquid |
| 298.15 | 0.0000 | 1.4026 |
| 298.15 | 0.1036 | 1.4084 |
| 298.15 | 0.2018 | 1.4146 |
| 298.15 | 0.3016 | 1.4205 |
| 298.15 | 0.4042 | 1.4273 |
| 298.15 | 0.4954 | 1.4326 |
| 298.15 | 0.6009 | 1.4397 |
| 298.15 | 0.6984 | 1.4459 |
| 298.15 | 0.8001 | 1.4526 |
| 298.15 | 0.8933 | 1.4591 |
| 298.15 | 1.0000 | 1.4662 |
| 308.15 | 0.0000 | 1.3983 |
| 308.15 | 0.1036 | 1.4038 |
| 308.15 | 0.2018 | 1.4105 |
| 308.15 | 0.3016 | 1.4163 |
| 308.15 | 0.4042 | 1.423 |
| 308.15 | 0.4954 | 1.4286 |
| 308.15 | 0.6009 | 1.435 |
| 308.15 | 0.6984 | 1.4418 |
| 308.15 | 0.8001 | 1.4486 |
| 308.15 | 0.8933 | 1.455 |
| 308.15 | 1.0000 | 1.4618 |
| 318.15 | 0.0000 | 1.3937 |
| 318.15 | 0.1036 | 1.3993 |
| 318.15 | 0.2018 | 1.406 |
| 318.15 | 0.3016 | 1.4122 |
| 318.15 | 0.4042 | 1.4187 |
| 318.15 | 0.4954 | 1.4249 |
| 318.15 | 0.6009 | 1.4312 |
| 318.15 | 0.6984 | 1.4379 |
| 318.15 | 0.8001 | 1.4445 |
| 318.15 | 0.8933 | 1.4509 |
| 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 | Refractive index (Na D-line) - Liquid |
| 298.15 | 0.0000 | 1.4026 |
| 298.15 | 0.1036 | 1.4084 |
| 298.15 | 0.2018 | 1.4146 |
| 298.15 | 0.3016 | 1.4205 |
| 298.15 | 0.4042 | 1.4273 |
| 298.15 | 0.4954 | 1.4326 |
| 298.15 | 0.6009 | 1.4397 |
| 298.15 | 0.6984 | 1.4459 |
| 298.15 | 0.8001 | 1.4526 |
| 298.15 | 0.8933 | 1.4591 |
| 298.15 | 1.0000 | 1.4662 |
| 308.15 | 0.0000 | 1.3983 |
| 308.15 | 0.1036 | 1.4038 |
| 308.15 | 0.2018 | 1.4105 |
| 308.15 | 0.3016 | 1.4163 |
| 308.15 | 0.4042 | 1.423 |
| 308.15 | 0.4954 | 1.4286 |
| 308.15 | 0.6009 | 1.435 |
| 308.15 | 0.6984 | 1.4418 |
| 308.15 | 0.8001 | 1.4486 |
| 308.15 | 0.8933 | 1.455 |
| 308.15 | 1.0000 | 1.4618 |
| 318.15 | 0.0000 | 1.3937 |
| 318.15 | 0.1036 | 1.3993 |
| 318.15 | 0.2018 | 1.406 |
| 318.15 | 0.3016 | 1.4122 |
| 318.15 | 0.4042 | 1.4187 |
| 318.15 | 0.4954 | 1.4249 |
| 318.15 | 0.6009 | 1.4312 |
| 318.15 | 0.6984 | 1.4379 |
| 318.15 | 0.8001 | 1.4445 |
| 318.15 | 0.8933 | 1.4509 |
| 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 | 717.94 |
| 293.15 | 0.1036 | 732.72 |
| 293.15 | 0.2018 | 746.84 |
| 293.15 | 0.3016 | 761.45 |
| 293.15 | 0.4042 | 776.68 |
| 293.15 | 0.4954 | 790.42 |
| 293.15 | 0.6009 | 806.55 |
| 293.15 | 0.6984 | 821.69 |
| 293.15 | 0.8001 | 837.66 |
| 293.15 | 0.8933 | 852.53 |
| 293.15 | 1.0000 | 869.78 |
| 298.15 | 0.0000 | 714.11 |
| 298.15 | 0.1036 | 728.87 |
| 298.15 | 0.2018 | 743.0 |
| 298.15 | 0.3016 | 757.63 |
| 298.15 | 0.4042 | 772.88 |
| 298.15 | 0.4954 | 786.63 |
| 298.15 | 0.6009 | 802.78 |
| 298.15 | 0.6984 | 817.94 |
| 298.15 | 0.8001 | 833.93 |
| 298.15 | 0.8933 | 848.8 |
| 298.15 | 1.0000 | 866.07 |
| 303.15 | 0.0000 | 710.2 |
| 303.15 | 0.1036 | 724.99 |
| 303.15 | 0.2018 | 739.14 |
| 303.15 | 0.3016 | 753.79 |
| 303.15 | 0.4042 | 769.06 |
| 303.15 | 0.4954 | 782.83 |
| 303.15 | 0.6009 | 798.99 |
| 303.15 | 0.6984 | 814.17 |
| 303.15 | 0.8001 | 830.18 |
| 303.15 | 0.8933 | 845.07 |
| 303.15 | 1.0000 | 862.34 |
| 308.15 | 0.0000 | 706.29 |
| 308.15 | 0.1036 | 721.09 |
| 308.15 | 0.2018 | 735.26 |
| 308.15 | 0.3016 | 749.94 |
| 308.15 | 0.4042 | 765.23 |
| 308.15 | 0.4954 | 779.01 |
| 308.15 | 0.6009 | 795.19 |
| 308.15 | 0.6984 | 810.39 |
| 308.15 | 0.8001 | 826.41 |
| 308.15 | 0.8933 | 841.33 |
| 308.15 | 1.0000 | 858.61 |
| 313.15 | 0.0000 | 702.35 |
| 313.15 | 0.1036 | 717.18 |
| 313.15 | 0.2018 | 731.37 |
| 313.15 | 0.3016 | 746.07 |
| 313.15 | 0.4042 | 761.38 |
| 313.15 | 0.4954 | 775.18 |
| 313.15 | 0.6009 | 791.38 |
| 313.15 | 0.6984 | 806.6 |
| 313.15 | 0.8001 | 822.64 |
| 313.15 | 0.8933 | 837.57 |
| 313.15 | 1.0000 | 854.88 |
| 318.15 | 0.0000 | 698.4 |
| 318.15 | 0.1036 | 713.25 |
| 318.15 | 0.2018 | 727.46 |
| 318.15 | 0.3016 | 742.18 |
| 318.15 | 0.4042 | 757.52 |
| 318.15 | 0.4954 | 771.34 |
| 318.15 | 0.6009 | 787.56 |
| 318.15 | 0.6984 | 802.8 |
| 318.15 | 0.8001 | 818.86 |
| 318.15 | 0.8933 | 833.81 |
| 318.15 | 1.0000 | 851.14 |
| 323.15 | 0.0000 | 694.43 |
| 323.15 | 0.1036 | 709.3 |
| 323.15 | 0.2018 | 723.54 |
| 323.15 | 0.3016 | 738.28 |
| 323.15 | 0.4042 | 753.64 |
| 323.15 | 0.4954 | 767.48 |
| 323.15 | 0.6009 | 783.73 |
| 323.15 | 0.6984 | 798.99 |
| 323.15 | 0.8001 | 815.08 |
| 323.15 | 0.8933 | 830.05 |
| 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 | 717.94 |
| 293.15 | 0.1036 | 732.72 |
| 293.15 | 0.2018 | 746.84 |
| 293.15 | 0.3016 | 761.45 |
| 293.15 | 0.4042 | 776.68 |
| 293.15 | 0.4954 | 790.42 |
| 293.15 | 0.6009 | 806.55 |
| 293.15 | 0.6984 | 821.69 |
| 293.15 | 0.8001 | 837.66 |
| 293.15 | 0.8933 | 852.53 |
| 293.15 | 1.0000 | 869.78 |
| 298.15 | 0.0000 | 714.11 |
| 298.15 | 0.1036 | 728.87 |
| 298.15 | 0.2018 | 743.0 |
| 298.15 | 0.3016 | 757.63 |
| 298.15 | 0.4042 | 772.88 |
| 298.15 | 0.4954 | 786.63 |
| 298.15 | 0.6009 | 802.78 |
| 298.15 | 0.6984 | 817.94 |
| 298.15 | 0.8001 | 833.93 |
| 298.15 | 0.8933 | 848.8 |
| 298.15 | 1.0000 | 866.07 |
| 303.15 | 0.0000 | 710.2 |
| 303.15 | 0.1036 | 724.99 |
| 303.15 | 0.2018 | 739.14 |
| 303.15 | 0.3016 | 753.79 |
| 303.15 | 0.4042 | 769.06 |
| 303.15 | 0.4954 | 782.83 |
| 303.15 | 0.6009 | 798.99 |
| 303.15 | 0.6984 | 814.17 |
| 303.15 | 0.8001 | 830.18 |
| 303.15 | 0.8933 | 845.07 |
| 303.15 | 1.0000 | 862.34 |
| 308.15 | 0.0000 | 706.29 |
| 308.15 | 0.1036 | 721.09 |
| 308.15 | 0.2018 | 735.26 |
| 308.15 | 0.3016 | 749.94 |
| 308.15 | 0.4042 | 765.23 |
| 308.15 | 0.4954 | 779.01 |
| 308.15 | 0.6009 | 795.19 |
| 308.15 | 0.6984 | 810.39 |
| 308.15 | 0.8001 | 826.41 |
| 308.15 | 0.8933 | 841.33 |
| 308.15 | 1.0000 | 858.61 |
| 313.15 | 0.0000 | 702.35 |
| 313.15 | 0.1036 | 717.18 |
| 313.15 | 0.2018 | 731.37 |
| 313.15 | 0.3016 | 746.07 |
| 313.15 | 0.4042 | 761.38 |
| 313.15 | 0.4954 | 775.18 |
| 313.15 | 0.6009 | 791.38 |
| 313.15 | 0.6984 | 806.6 |
| 313.15 | 0.8001 | 822.64 |
| 313.15 | 0.8933 | 837.57 |
| 313.15 | 1.0000 | 854.88 |
| 318.15 | 0.0000 | 698.4 |
| 318.15 | 0.1036 | 713.25 |
| 318.15 | 0.2018 | 727.46 |
| 318.15 | 0.3016 | 742.18 |
| 318.15 | 0.4042 | 757.52 |
| 318.15 | 0.4954 | 771.34 |
| 318.15 | 0.6009 | 787.56 |
| 318.15 | 0.6984 | 802.8 |
| 318.15 | 0.8001 | 818.86 |
| 318.15 | 0.8933 | 833.81 |
| 318.15 | 1.0000 | 851.14 |
| 323.15 | 0.0000 | 694.43 |
| 323.15 | 0.1036 | 709.3 |
| 323.15 | 0.2018 | 723.54 |
| 323.15 | 0.3016 | 738.28 |
| 323.15 | 0.4042 | 753.64 |
| 323.15 | 0.4954 | 767.48 |
| 323.15 | 0.6009 | 783.73 |
| 323.15 | 0.6984 | 798.99 |
| 323.15 | 0.8001 | 815.08 |
| 323.15 | 0.8933 | 830.05 |
| 323.15 | 1.0000 | 847.4 |