Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 4,7-Methano-1H-indene, octahydro- (2) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0000 | 0.0005 |
| 293.15 | 0.0994 | 0.0006 |
| 293.15 | 0.2004 | 0.0007 |
| 293.15 | 0.2996 | 0.0008 |
| 293.15 | 0.4001 | 0.0009 |
| 293.15 | 0.5008 | 0.0010 |
| 293.15 | 0.5973 | 0.0012 |
| 293.15 | 0.6998 | 0.0015 |
| 293.15 | 0.8016 | 0.0019 |
| 293.15 | 0.8999 | 0.0023 |
| 293.15 | 1.0000 | 0.0030 |
| 298.15 | 0.0000 | 0.0005 |
| 298.15 | 0.0994 | 0.0005 |
| 298.15 | 0.2004 | 0.0006 |
| 298.15 | 0.2996 | 0.0007 |
| 298.15 | 0.4001 | 0.0008 |
| 298.15 | 0.5008 | 0.0010 |
| 298.15 | 0.5973 | 0.0012 |
| 298.15 | 0.6998 | 0.0014 |
| 298.15 | 0.8016 | 0.0017 |
| 298.15 | 0.8999 | 0.0021 |
| 298.15 | 1.0000 | 0.0027 |
| 303.15 | 0.0000 | 0.0005 |
| 303.15 | 0.0994 | 0.0005 |
| 303.15 | 0.2004 | 0.0006 |
| 303.15 | 0.2996 | 0.0007 |
| 303.15 | 0.4001 | 0.0008 |
| 303.15 | 0.5008 | 0.0009 |
| 303.15 | 0.5973 | 0.0011 |
| 303.15 | 0.6998 | 0.0013 |
| 303.15 | 0.8016 | 0.0016 |
| 303.15 | 0.8999 | 0.0019 |
| 303.15 | 1.0000 | 0.0025 |
| 308.15 | 0.0000 | 0.0004 |
| 308.15 | 0.0994 | 0.0005 |
| 308.15 | 0.2004 | 0.0006 |
| 308.15 | 0.2996 | 0.0006 |
| 308.15 | 0.4001 | 0.0007 |
| 308.15 | 0.5008 | 0.0008 |
| 308.15 | 0.5973 | 0.0010 |
| 308.15 | 0.6998 | 0.0012 |
| 308.15 | 0.8016 | 0.0015 |
| 308.15 | 0.8999 | 0.0018 |
| 308.15 | 1.0000 | 0.0022 |
| 313.15 | 0.0000 | 0.0004 |
| 313.15 | 0.0994 | 0.0005 |
| 313.15 | 0.2004 | 0.0005 |
| 313.15 | 0.2996 | 0.0006 |
| 313.15 | 0.4001 | 0.0007 |
| 313.15 | 0.5008 | 0.0008 |
| 313.15 | 0.5973 | 0.0009 |
| 313.15 | 0.6998 | 0.0011 |
| 313.15 | 0.8016 | 0.0014 |
| 313.15 | 0.8999 | 0.0016 |
| 313.15 | 1.0000 | 0.0021 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 4,7-Methano-1H-indene, octahydro- (2) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0000 | 0.0005 |
| 293.15 | 0.0994 | 0.0006 |
| 293.15 | 0.2004 | 0.0007 |
| 293.15 | 0.2996 | 0.0008 |
| 293.15 | 0.4001 | 0.0009 |
| 293.15 | 0.5008 | 0.0010 |
| 293.15 | 0.5973 | 0.0012 |
| 293.15 | 0.6998 | 0.0015 |
| 293.15 | 0.8016 | 0.0019 |
| 293.15 | 0.8999 | 0.0023 |
| 293.15 | 1.0000 | 0.0030 |
| 298.15 | 0.0000 | 0.0005 |
| 298.15 | 0.0994 | 0.0005 |
| 298.15 | 0.2004 | 0.0006 |
| 298.15 | 0.2996 | 0.0007 |
| 298.15 | 0.4001 | 0.0008 |
| 298.15 | 0.5008 | 0.0010 |
| 298.15 | 0.5973 | 0.0012 |
| 298.15 | 0.6998 | 0.0014 |
| 298.15 | 0.8016 | 0.0017 |
| 298.15 | 0.8999 | 0.0021 |
| 298.15 | 1.0000 | 0.0027 |
| 303.15 | 0.0000 | 0.0005 |
| 303.15 | 0.0994 | 0.0005 |
| 303.15 | 0.2004 | 0.0006 |
| 303.15 | 0.2996 | 0.0007 |
| 303.15 | 0.4001 | 0.0008 |
| 303.15 | 0.5008 | 0.0009 |
| 303.15 | 0.5973 | 0.0011 |
| 303.15 | 0.6998 | 0.0013 |
| 303.15 | 0.8016 | 0.0016 |
| 303.15 | 0.8999 | 0.0019 |
| 303.15 | 1.0000 | 0.0025 |
| 308.15 | 0.0000 | 0.0004 |
| 308.15 | 0.0994 | 0.0005 |
| 308.15 | 0.2004 | 0.0006 |
| 308.15 | 0.2996 | 0.0006 |
| 308.15 | 0.4001 | 0.0007 |
| 308.15 | 0.5008 | 0.0008 |
| 308.15 | 0.5973 | 0.0010 |
| 308.15 | 0.6998 | 0.0012 |
| 308.15 | 0.8016 | 0.0015 |
| 308.15 | 0.8999 | 0.0018 |
| 308.15 | 1.0000 | 0.0022 |
| 313.15 | 0.0000 | 0.0004 |
| 313.15 | 0.0994 | 0.0005 |
| 313.15 | 0.2004 | 0.0005 |
| 313.15 | 0.2996 | 0.0006 |
| 313.15 | 0.4001 | 0.0007 |
| 313.15 | 0.5008 | 0.0008 |
| 313.15 | 0.5973 | 0.0009 |
| 313.15 | 0.6998 | 0.0011 |
| 313.15 | 0.8016 | 0.0014 |
| 313.15 | 0.8999 | 0.0016 |
| 313.15 | 1.0000 | 0.0021 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 4,7-Methano-1H-indene, octahydro- (2) - Liquid | Refractive index (Na D-line) - Liquid |
| 293.15 | 0.0000 | 1.3976 |
| 293.15 | 0.0994 | 1.4064 |
| 293.15 | 0.2004 | 1.4152 |
| 293.15 | 0.2996 | 1.424 |
| 293.15 | 0.4001 | 1.433 |
| 293.15 | 0.5008 | 1.4419 |
| 293.15 | 0.5973 | 1.4506 |
| 293.15 | 0.6998 | 1.4599 |
| 293.15 | 0.8016 | 1.4692 |
| 293.15 | 0.8999 | 1.478 |
| 293.15 | 1.0000 | 1.4871 |
| 298.15 | 0.0000 | 1.3957 |
| 298.15 | 0.0994 | 1.4044 |
| 298.15 | 0.2004 | 1.4133 |
| 298.15 | 0.2996 | 1.4221 |
| 298.15 | 0.4001 | 1.431 |
| 298.15 | 0.5008 | 1.4401 |
| 298.15 | 0.5973 | 1.4488 |
| 298.15 | 0.6998 | 1.4581 |
| 298.15 | 0.8016 | 1.4673 |
| 298.15 | 0.8999 | 1.4762 |
| 298.15 | 1.0000 | 1.4853 |
| 303.15 | 0.0000 | 1.3934 |
| 303.15 | 0.0994 | 1.4015 |
| 303.15 | 0.2004 | 1.4106 |
| 303.15 | 0.2996 | 1.4195 |
| 303.15 | 0.4001 | 1.4285 |
| 303.15 | 0.5008 | 1.4376 |
| 303.15 | 0.5973 | 1.4463 |
| 303.15 | 0.6998 | 1.4553 |
| 303.15 | 0.8016 | 1.4647 |
| 303.15 | 0.8999 | 1.4738 |
| 303.15 | 1.0000 | 1.4833 |
| 308.15 | 0.0000 | 1.391 |
| 308.15 | 0.0994 | 1.3998 |
| 308.15 | 0.2004 | 1.4087 |
| 308.15 | 0.2996 | 1.4172 |
| 308.15 | 0.4001 | 1.426 |
| 308.15 | 0.5008 | 1.435 |
| 308.15 | 0.5973 | 1.4438 |
| 308.15 | 0.6998 | 1.4531 |
| 308.15 | 0.8016 | 1.4623 |
| 308.15 | 0.8999 | 1.4712 |
| 308.15 | 1.0000 | 1.4802 |
| 313.15 | 0.0000 | 1.3892 |
| 313.15 | 0.0994 | 1.3979 |
| 313.15 | 0.2004 | 1.4064 |
| 313.15 | 0.2996 | 1.4151 |
| 313.15 | 0.4001 | 1.4239 |
| 313.15 | 0.5008 | 1.4328 |
| 313.15 | 0.5973 | 1.4414 |
| 313.15 | 0.6998 | 1.4505 |
| 313.15 | 0.8016 | 1.4596 |
| 313.15 | 0.8999 | 1.4684 |
| 313.15 | 1.0000 | 1.4773 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 4,7-Methano-1H-indene, octahydro- (2) - Liquid | Refractive index (Na D-line) - Liquid |
| 293.15 | 0.0000 | 1.3976 |
| 293.15 | 0.0994 | 1.4064 |
| 293.15 | 0.2004 | 1.4152 |
| 293.15 | 0.2996 | 1.424 |
| 293.15 | 0.4001 | 1.433 |
| 293.15 | 0.5008 | 1.4419 |
| 293.15 | 0.5973 | 1.4506 |
| 293.15 | 0.6998 | 1.4599 |
| 293.15 | 0.8016 | 1.4692 |
| 293.15 | 0.8999 | 1.478 |
| 293.15 | 1.0000 | 1.4871 |
| 298.15 | 0.0000 | 1.3957 |
| 298.15 | 0.0994 | 1.4044 |
| 298.15 | 0.2004 | 1.4133 |
| 298.15 | 0.2996 | 1.4221 |
| 298.15 | 0.4001 | 1.431 |
| 298.15 | 0.5008 | 1.4401 |
| 298.15 | 0.5973 | 1.4488 |
| 298.15 | 0.6998 | 1.4581 |
| 298.15 | 0.8016 | 1.4673 |
| 298.15 | 0.8999 | 1.4762 |
| 298.15 | 1.0000 | 1.4853 |
| 303.15 | 0.0000 | 1.3934 |
| 303.15 | 0.0994 | 1.4015 |
| 303.15 | 0.2004 | 1.4106 |
| 303.15 | 0.2996 | 1.4195 |
| 303.15 | 0.4001 | 1.4285 |
| 303.15 | 0.5008 | 1.4376 |
| 303.15 | 0.5973 | 1.4463 |
| 303.15 | 0.6998 | 1.4553 |
| 303.15 | 0.8016 | 1.4647 |
| 303.15 | 0.8999 | 1.4738 |
| 303.15 | 1.0000 | 1.4833 |
| 308.15 | 0.0000 | 1.391 |
| 308.15 | 0.0994 | 1.3998 |
| 308.15 | 0.2004 | 1.4087 |
| 308.15 | 0.2996 | 1.4172 |
| 308.15 | 0.4001 | 1.426 |
| 308.15 | 0.5008 | 1.435 |
| 308.15 | 0.5973 | 1.4438 |
| 308.15 | 0.6998 | 1.4531 |
| 308.15 | 0.8016 | 1.4623 |
| 308.15 | 0.8999 | 1.4712 |
| 308.15 | 1.0000 | 1.4802 |
| 313.15 | 0.0000 | 1.3892 |
| 313.15 | 0.0994 | 1.3979 |
| 313.15 | 0.2004 | 1.4064 |
| 313.15 | 0.2996 | 1.4151 |
| 313.15 | 0.4001 | 1.4239 |
| 313.15 | 0.5008 | 1.4328 |
| 313.15 | 0.5973 | 1.4414 |
| 313.15 | 0.6998 | 1.4505 |
| 313.15 | 0.8016 | 1.4596 |
| 313.15 | 0.8999 | 1.4684 |
| 313.15 | 1.0000 | 1.4773 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 4,7-Methano-1H-indene, octahydro- (2) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 706.37 |
| 293.15 | 0.0994 | 727.98 |
| 293.15 | 0.2004 | 750.25 |
| 293.15 | 0.2996 | 772.38 |
| 293.15 | 0.4001 | 795.07 |
| 293.15 | 0.5008 | 818.02 |
| 293.15 | 0.5973 | 840.34 |
| 293.15 | 0.6998 | 864.25 |
| 293.15 | 0.8016 | 888.3 |
| 293.15 | 0.8999 | 911.7 |
| 293.15 | 1.0000 | 935.66 |
| 298.15 | 0.0000 | 702.3 |
| 298.15 | 0.0994 | 723.92 |
| 298.15 | 0.2004 | 746.18 |
| 298.15 | 0.2996 | 768.34 |
| 298.15 | 0.4001 | 791.05 |
| 298.15 | 0.5008 | 814.01 |
| 298.15 | 0.5973 | 836.35 |
| 298.15 | 0.6998 | 860.28 |
| 298.15 | 0.8016 | 884.36 |
| 298.15 | 0.8999 | 907.78 |
| 298.15 | 1.0000 | 931.79 |
| 303.15 | 0.0000 | 698.2 |
| 303.15 | 0.0994 | 719.83 |
| 303.15 | 0.2004 | 742.1 |
| 303.15 | 0.2996 | 764.27 |
| 303.15 | 0.4001 | 787.0 |
| 303.15 | 0.5008 | 809.98 |
| 303.15 | 0.5973 | 832.33 |
| 303.15 | 0.6998 | 856.29 |
| 303.15 | 0.8016 | 880.39 |
| 303.15 | 0.8999 | 903.84 |
| 303.15 | 1.0000 | 927.88 |
| 308.15 | 0.0000 | 694.08 |
| 308.15 | 0.0994 | 715.72 |
| 308.15 | 0.2004 | 738.01 |
| 308.15 | 0.2996 | 760.19 |
| 308.15 | 0.4001 | 782.94 |
| 308.15 | 0.5008 | 805.94 |
| 308.15 | 0.5973 | 828.31 |
| 308.15 | 0.6998 | 852.28 |
| 308.15 | 0.8016 | 876.41 |
| 308.15 | 0.8999 | 899.9 |
| 308.15 | 1.0000 | 923.97 |
| 313.15 | 0.0000 | 689.93 |
| 313.15 | 0.0994 | 711.59 |
| 313.15 | 0.2004 | 733.9 |
| 313.15 | 0.2996 | 756.09 |
| 313.15 | 0.4001 | 778.86 |
| 313.15 | 0.5008 | 801.88 |
| 313.15 | 0.5973 | 824.27 |
| 313.15 | 0.6998 | 848.27 |
| 313.15 | 0.8016 | 872.43 |
| 313.15 | 0.8999 | 895.94 |
| 313.15 | 1.0000 | 920.05 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 4,7-Methano-1H-indene, octahydro- (2) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 706.37 |
| 293.15 | 0.0994 | 727.98 |
| 293.15 | 0.2004 | 750.25 |
| 293.15 | 0.2996 | 772.38 |
| 293.15 | 0.4001 | 795.07 |
| 293.15 | 0.5008 | 818.02 |
| 293.15 | 0.5973 | 840.34 |
| 293.15 | 0.6998 | 864.25 |
| 293.15 | 0.8016 | 888.3 |
| 293.15 | 0.8999 | 911.7 |
| 293.15 | 1.0000 | 935.66 |
| 298.15 | 0.0000 | 702.3 |
| 298.15 | 0.0994 | 723.92 |
| 298.15 | 0.2004 | 746.18 |
| 298.15 | 0.2996 | 768.34 |
| 298.15 | 0.4001 | 791.05 |
| 298.15 | 0.5008 | 814.01 |
| 298.15 | 0.5973 | 836.35 |
| 298.15 | 0.6998 | 860.28 |
| 298.15 | 0.8016 | 884.36 |
| 298.15 | 0.8999 | 907.78 |
| 298.15 | 1.0000 | 931.79 |
| 303.15 | 0.0000 | 698.2 |
| 303.15 | 0.0994 | 719.83 |
| 303.15 | 0.2004 | 742.1 |
| 303.15 | 0.2996 | 764.27 |
| 303.15 | 0.4001 | 787.0 |
| 303.15 | 0.5008 | 809.98 |
| 303.15 | 0.5973 | 832.33 |
| 303.15 | 0.6998 | 856.29 |
| 303.15 | 0.8016 | 880.39 |
| 303.15 | 0.8999 | 903.84 |
| 303.15 | 1.0000 | 927.88 |
| 308.15 | 0.0000 | 694.08 |
| 308.15 | 0.0994 | 715.72 |
| 308.15 | 0.2004 | 738.01 |
| 308.15 | 0.2996 | 760.19 |
| 308.15 | 0.4001 | 782.94 |
| 308.15 | 0.5008 | 805.94 |
| 308.15 | 0.5973 | 828.31 |
| 308.15 | 0.6998 | 852.28 |
| 308.15 | 0.8016 | 876.41 |
| 308.15 | 0.8999 | 899.9 |
| 308.15 | 1.0000 | 923.97 |
| 313.15 | 0.0000 | 689.93 |
| 313.15 | 0.0994 | 711.59 |
| 313.15 | 0.2004 | 733.9 |
| 313.15 | 0.2996 | 756.09 |
| 313.15 | 0.4001 | 778.86 |
| 313.15 | 0.5008 | 801.88 |
| 313.15 | 0.5973 | 824.27 |
| 313.15 | 0.6998 | 848.27 |
| 313.15 | 0.8016 | 872.43 |
| 313.15 | 0.8999 | 895.94 |
| 313.15 | 1.0000 | 920.05 |
Note: These property values are available through the Cheméo API. A free account gives you an access key.