- Name
- Toluene
- InChI
- InChI=1S/C7H8/c1-7-5-3-2-4-6-7/h2-6H,1H3
- InChI Key
- YXFVVABEGXRONW-UHFFFAOYSA-N
- Formula
- C7H8
- SMILES
- Cc1ccccc1
- Mol. Weight (g/mol)
- 92.14
- CAS
- 108-88-3
- Name
- 1-Octanol
- InChI
- InChI=1S/C8H18O/c1-2-3-4-5-6-7-8-9/h9H,2-8H2,1H3
- InChI Key
- KBPLFHHGFOOTCA-UHFFFAOYSA-N
- Formula
- C8H18O
- SMILES
- CCCCCCCCO
- Mol. Weight (g/mol)
- 130.23
- CAS
- 111-87-5
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Datasets
- η - Viscosity, Pa*s (2)
- n0 - Refractive index (Na D-line) (2)
- ρl - Mass density, kg/m3 (4)
- csound,fluid - Speed of Sound, m/s (2)
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Toluene (1) - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 0.0000 | 0.0064 |
| 303.15 | 0.0495 | 0.0056 |
| 303.15 | 0.1104 | 0.0048 |
| 303.15 | 0.1513 | 0.0043 |
| 303.15 | 0.1999 | 0.0038 |
| 303.15 | 0.2517 | 0.0033 |
| 303.15 | 0.2997 | 0.0030 |
| 303.15 | 0.3560 | 0.0025 |
| 303.15 | 0.3998 | 0.0022 |
| 303.15 | 0.4506 | 0.0020 |
| 303.15 | 0.5001 | 0.0018 |
| 303.15 | 0.5513 | 0.0015 |
| 303.15 | 0.6014 | 0.0014 |
| 303.15 | 0.6495 | 0.0012 |
| 303.15 | 0.6997 | 0.0011 |
| 303.15 | 0.7569 | 0.0009 |
| 303.15 | 0.8012 | 0.0008 |
| 303.15 | 0.8527 | 0.0007 |
| 303.15 | 0.9000 | 0.0006 |
| 303.15 | 0.9540 | 0.0006 |
| 303.15 | 1.0000 | 0.0005 |
| 313.15 | 0.0000 | 0.0046 |
| 313.15 | 0.0495 | 0.0041 |
| 313.15 | 0.1104 | 0.0036 |
| 313.15 | 0.1513 | 0.0033 |
| 313.15 | 0.1999 | 0.0028 |
| 313.15 | 0.2517 | 0.0025 |
| 313.15 | 0.2997 | 0.0022 |
| 313.15 | 0.3560 | 0.0019 |
| 313.15 | 0.3998 | 0.0017 |
| 313.15 | 0.4506 | 0.0015 |
| 313.15 | 0.5001 | 0.0014 |
| 313.15 | 0.5513 | 0.0012 |
| 313.15 | 0.6014 | 0.0011 |
| 313.15 | 0.6495 | 0.0009 |
| 313.15 | 0.6997 | 0.0009 |
| 313.15 | 0.7569 | 0.0008 |
| 313.15 | 0.8012 | 0.0007 |
| 313.15 | 0.8527 | 0.0006 |
| 313.15 | 0.9000 | 0.0006 |
| 313.15 | 0.9540 | 0.0005 |
| 313.15 | 1.0000 | 0.0005 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Toluene (1) - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 0.0000 | 0.0064 |
| 303.15 | 0.0495 | 0.0056 |
| 303.15 | 0.1104 | 0.0048 |
| 303.15 | 0.1513 | 0.0043 |
| 303.15 | 0.1999 | 0.0038 |
| 303.15 | 0.2517 | 0.0033 |
| 303.15 | 0.2997 | 0.0030 |
| 303.15 | 0.3560 | 0.0025 |
| 303.15 | 0.3998 | 0.0022 |
| 303.15 | 0.4506 | 0.0020 |
| 303.15 | 0.5001 | 0.0018 |
| 303.15 | 0.5513 | 0.0015 |
| 303.15 | 0.6014 | 0.0014 |
| 303.15 | 0.6495 | 0.0012 |
| 303.15 | 0.6997 | 0.0011 |
| 303.15 | 0.7569 | 0.0009 |
| 303.15 | 0.8012 | 0.0008 |
| 303.15 | 0.8527 | 0.0007 |
| 303.15 | 0.9000 | 0.0006 |
| 303.15 | 0.9540 | 0.0006 |
| 303.15 | 1.0000 | 0.0005 |
| 313.15 | 0.0000 | 0.0046 |
| 313.15 | 0.0495 | 0.0041 |
| 313.15 | 0.1104 | 0.0036 |
| 313.15 | 0.1513 | 0.0033 |
| 313.15 | 0.1999 | 0.0028 |
| 313.15 | 0.2517 | 0.0025 |
| 313.15 | 0.2997 | 0.0022 |
| 313.15 | 0.3560 | 0.0019 |
| 313.15 | 0.3998 | 0.0017 |
| 313.15 | 0.4506 | 0.0015 |
| 313.15 | 0.5001 | 0.0014 |
| 313.15 | 0.5513 | 0.0012 |
| 313.15 | 0.6014 | 0.0011 |
| 313.15 | 0.6495 | 0.0009 |
| 313.15 | 0.6997 | 0.0009 |
| 313.15 | 0.7569 | 0.0008 |
| 313.15 | 0.8012 | 0.0007 |
| 313.15 | 0.8527 | 0.0006 |
| 313.15 | 0.9000 | 0.0006 |
| 313.15 | 0.9540 | 0.0005 |
| 313.15 | 1.0000 | 0.0005 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 94.9 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Octanol (2) - Liquid | Refractive index (Na D-line) - Liquid |
| 293.15 | 0.0000 | 1.4967 |
| 293.15 | 0.1041 | 1.4847 |
| 293.15 | 0.1973 | 1.4763 |
| 293.15 | 0.3018 | 1.4681 |
| 293.15 | 0.4033 | 1.4607 |
| 293.15 | 0.5035 | 1.4544 |
| 293.15 | 0.6007 | 1.4489 |
| 293.15 | 0.6996 | 1.4437 |
| 293.15 | 0.7930 | 1.4391 |
| 293.15 | 0.9044 | 1.4338 |
| 293.15 | 1.0000 | 1.4295 |
| 298.15 | 0.0000 | 1.4939 |
| 298.15 | 0.1041 | 1.4819 |
| 298.15 | 0.1973 | 1.4733 |
| 298.15 | 0.3018 | 1.4651 |
| 298.15 | 0.4033 | 1.458 |
| 298.15 | 0.5035 | 1.4517 |
| 298.15 | 0.6007 | 1.4463 |
| 298.15 | 0.6996 | 1.4412 |
| 298.15 | 0.7930 | 1.4367 |
| 298.15 | 0.9044 | 1.4318 |
| 298.15 | 1.0000 | 1.4275 |
| 303.15 | 0.0000 | 1.4919 |
| 303.15 | 0.1041 | 1.4792 |
| 303.15 | 0.1973 | 1.4704 |
| 303.15 | 0.3018 | 1.4623 |
| 303.15 | 0.4033 | 1.4551 |
| 303.15 | 0.5035 | 1.449 |
| 303.15 | 0.6007 | 1.4438 |
| 303.15 | 0.6996 | 1.4389 |
| 303.15 | 0.7930 | 1.4347 |
| 303.15 | 0.9044 | 1.4298 |
| 303.15 | 1.0000 | 1.4256 |
| 308.15 | 0.0000 | 1.4882 |
| 308.15 | 0.1041 | 1.4763 |
| 308.15 | 0.1973 | 1.4676 |
| 308.15 | 0.3018 | 1.4594 |
| 308.15 | 0.4033 | 1.4523 |
| 308.15 | 0.5035 | 1.4463 |
| 308.15 | 0.6007 | 1.4412 |
| 308.15 | 0.6996 | 1.4365 |
| 308.15 | 0.7930 | 1.4324 |
| 308.15 | 0.9044 | 1.4276 |
| 308.15 | 1.0000 | 1.4237 |
| 313.15 | 0.0000 | 1.4854 |
| 313.15 | 0.1041 | 1.4733 |
| 313.15 | 0.1973 | 1.4646 |
| 313.15 | 0.3018 | 1.4566 |
| 313.15 | 0.4033 | 1.4496 |
| 313.15 | 0.5035 | 1.4436 |
| 313.15 | 0.6007 | 1.4386 |
| 313.15 | 0.6996 | 1.4341 |
| 313.15 | 0.7930 | 1.43 |
| 313.15 | 0.9044 | 1.4256 |
| 313.15 | 1.0000 | 1.4217 |
| 318.15 | 0.0000 | 1.4825 |
| 318.15 | 0.1041 | 1.4701 |
| 318.15 | 0.1973 | 1.4619 |
| 318.15 | 0.3018 | 1.4537 |
| 318.15 | 0.4033 | 1.4468 |
| 318.15 | 0.5035 | 1.441 |
| 318.15 | 0.6007 | 1.436 |
| 318.15 | 0.6996 | 1.4315 |
| 318.15 | 0.7930 | 1.4277 |
| 318.15 | 0.9044 | 1.4234 |
| 318.15 | 1.0000 | 1.4197 |
| 323.15 | 0.0000 | 1.4797 |
| 323.15 | 0.1041 | 1.4675 |
| 323.15 | 0.1973 | 1.4588 |
| 323.15 | 0.3018 | 1.4509 |
| 323.15 | 0.4033 | 1.4442 |
| 323.15 | 0.5035 | 1.4384 |
| 323.15 | 0.6007 | 1.4334 |
| 323.15 | 0.6996 | 1.429 |
| 323.15 | 0.7930 | 1.4254 |
| 323.15 | 0.9044 | 1.4214 |
| 323.15 | 1.0000 | 1.4178 |
| 333.15 | 0.0000 | 1.474 |
| 333.15 | 0.1041 | 1.4618 |
| 333.15 | 0.1973 | 1.4531 |
| 333.15 | 0.3018 | 1.4453 |
| 333.15 | 0.4033 | 1.4387 |
| 333.15 | 0.5035 | 1.4331 |
| 333.15 | 0.6007 | 1.4283 |
| 333.15 | 0.6996 | 1.4242 |
| 333.15 | 0.7930 | 1.4209 |
| 333.15 | 0.9044 | 1.4171 |
| 333.15 | 1.0000 | 1.4141 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 94.9 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Octanol (2) - Liquid | Refractive index (Na D-line) - Liquid |
| 293.15 | 0.0000 | 1.4967 |
| 293.15 | 0.1041 | 1.4847 |
| 293.15 | 0.1973 | 1.4763 |
| 293.15 | 0.3018 | 1.4681 |
| 293.15 | 0.4033 | 1.4607 |
| 293.15 | 0.5035 | 1.4544 |
| 293.15 | 0.6007 | 1.4489 |
| 293.15 | 0.6996 | 1.4437 |
| 293.15 | 0.7930 | 1.4391 |
| 293.15 | 0.9044 | 1.4338 |
| 293.15 | 1.0000 | 1.4295 |
| 298.15 | 0.0000 | 1.4939 |
| 298.15 | 0.1041 | 1.4819 |
| 298.15 | 0.1973 | 1.4733 |
| 298.15 | 0.3018 | 1.4651 |
| 298.15 | 0.4033 | 1.458 |
| 298.15 | 0.5035 | 1.4517 |
| 298.15 | 0.6007 | 1.4463 |
| 298.15 | 0.6996 | 1.4412 |
| 298.15 | 0.7930 | 1.4367 |
| 298.15 | 0.9044 | 1.4318 |
| 298.15 | 1.0000 | 1.4275 |
| 303.15 | 0.0000 | 1.4919 |
| 303.15 | 0.1041 | 1.4792 |
| 303.15 | 0.1973 | 1.4704 |
| 303.15 | 0.3018 | 1.4623 |
| 303.15 | 0.4033 | 1.4551 |
| 303.15 | 0.5035 | 1.449 |
| 303.15 | 0.6007 | 1.4438 |
| 303.15 | 0.6996 | 1.4389 |
| 303.15 | 0.7930 | 1.4347 |
| 303.15 | 0.9044 | 1.4298 |
| 303.15 | 1.0000 | 1.4256 |
| 308.15 | 0.0000 | 1.4882 |
| 308.15 | 0.1041 | 1.4763 |
| 308.15 | 0.1973 | 1.4676 |
| 308.15 | 0.3018 | 1.4594 |
| 308.15 | 0.4033 | 1.4523 |
| 308.15 | 0.5035 | 1.4463 |
| 308.15 | 0.6007 | 1.4412 |
| 308.15 | 0.6996 | 1.4365 |
| 308.15 | 0.7930 | 1.4324 |
| 308.15 | 0.9044 | 1.4276 |
| 308.15 | 1.0000 | 1.4237 |
| 313.15 | 0.0000 | 1.4854 |
| 313.15 | 0.1041 | 1.4733 |
| 313.15 | 0.1973 | 1.4646 |
| 313.15 | 0.3018 | 1.4566 |
| 313.15 | 0.4033 | 1.4496 |
| 313.15 | 0.5035 | 1.4436 |
| 313.15 | 0.6007 | 1.4386 |
| 313.15 | 0.6996 | 1.4341 |
| 313.15 | 0.7930 | 1.43 |
| 313.15 | 0.9044 | 1.4256 |
| 313.15 | 1.0000 | 1.4217 |
| 318.15 | 0.0000 | 1.4825 |
| 318.15 | 0.1041 | 1.4701 |
| 318.15 | 0.1973 | 1.4619 |
| 318.15 | 0.3018 | 1.4537 |
| 318.15 | 0.4033 | 1.4468 |
| 318.15 | 0.5035 | 1.441 |
| 318.15 | 0.6007 | 1.436 |
| 318.15 | 0.6996 | 1.4315 |
| 318.15 | 0.7930 | 1.4277 |
| 318.15 | 0.9044 | 1.4234 |
| 318.15 | 1.0000 | 1.4197 |
| 323.15 | 0.0000 | 1.4797 |
| 323.15 | 0.1041 | 1.4675 |
| 323.15 | 0.1973 | 1.4588 |
| 323.15 | 0.3018 | 1.4509 |
| 323.15 | 0.4033 | 1.4442 |
| 323.15 | 0.5035 | 1.4384 |
| 323.15 | 0.6007 | 1.4334 |
| 323.15 | 0.6996 | 1.429 |
| 323.15 | 0.7930 | 1.4254 |
| 323.15 | 0.9044 | 1.4214 |
| 323.15 | 1.0000 | 1.4178 |
| 333.15 | 0.0000 | 1.474 |
| 333.15 | 0.1041 | 1.4618 |
| 333.15 | 0.1973 | 1.4531 |
| 333.15 | 0.3018 | 1.4453 |
| 333.15 | 0.4033 | 1.4387 |
| 333.15 | 0.5035 | 1.4331 |
| 333.15 | 0.6007 | 1.4283 |
| 333.15 | 0.6996 | 1.4242 |
| 333.15 | 0.7930 | 1.4209 |
| 333.15 | 0.9044 | 1.4171 |
| 333.15 | 1.0000 | 1.4141 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 94.9 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Octanol (2) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 866.68 |
| 293.15 | 0.1041 | 859.2 |
| 293.15 | 0.1973 | 853.95 |
| 293.15 | 0.3018 | 848.87 |
| 293.15 | 0.4033 | 844.52 |
| 293.15 | 0.5035 | 840.66 |
| 293.15 | 0.6007 | 837.23 |
| 293.15 | 0.6996 | 834.03 |
| 293.15 | 0.7930 | 831.2 |
| 293.15 | 0.9044 | 828.07 |
| 293.15 | 1.0000 | 825.57 |
| 298.15 | 0.0000 | 861.74 |
| 298.15 | 0.1041 | 854.47 |
| 298.15 | 0.1973 | 849.33 |
| 298.15 | 0.3018 | 844.4 |
| 298.15 | 0.4033 | 840.2 |
| 298.15 | 0.5035 | 836.46 |
| 298.15 | 0.6007 | 833.15 |
| 298.15 | 0.6996 | 830.05 |
| 298.15 | 0.7930 | 827.33 |
| 298.15 | 0.9044 | 824.31 |
| 298.15 | 1.0000 | 821.9 |
| 303.15 | 0.0000 | 857.39 |
| 303.15 | 0.1041 | 849.63 |
| 303.15 | 0.1973 | 844.59 |
| 303.15 | 0.3018 | 839.8 |
| 303.15 | 0.4033 | 835.73 |
| 303.15 | 0.5035 | 832.13 |
| 303.15 | 0.6007 | 828.94 |
| 303.15 | 0.6996 | 825.95 |
| 303.15 | 0.7930 | 823.32 |
| 303.15 | 0.9044 | 820.4 |
| 303.15 | 1.0000 | 818.08 |
| 308.15 | 0.0000 | 851.69 |
| 308.15 | 0.1041 | 844.83 |
| 308.15 | 0.1973 | 839.89 |
| 308.15 | 0.3018 | 835.26 |
| 308.15 | 0.4033 | 831.33 |
| 308.15 | 0.5035 | 827.86 |
| 308.15 | 0.6007 | 824.78 |
| 308.15 | 0.6996 | 821.9 |
| 308.15 | 0.7930 | 819.36 |
| 308.15 | 0.9044 | 816.55 |
| 308.15 | 1.0000 | 814.31 |
| 313.15 | 0.0000 | 847.82 |
| 313.15 | 0.1041 | 840.03 |
| 313.15 | 0.1973 | 835.16 |
| 313.15 | 0.3018 | 830.67 |
| 313.15 | 0.4033 | 826.9 |
| 313.15 | 0.5035 | 823.56 |
| 313.15 | 0.6007 | 820.6 |
| 313.15 | 0.6996 | 817.82 |
| 313.15 | 0.7930 | 815.37 |
| 313.15 | 0.9044 | 812.65 |
| 313.15 | 1.0000 | 811.09 |
| 318.15 | 0.0000 | 842.88 |
| 318.15 | 0.1041 | 835.18 |
| 318.15 | 0.1973 | 830.43 |
| 318.15 | 0.3018 | 826.08 |
| 318.15 | 0.4033 | 822.45 |
| 318.15 | 0.5035 | 819.25 |
| 318.15 | 0.6007 | 816.41 |
| 318.15 | 0.6996 | 813.74 |
| 318.15 | 0.7930 | 811.38 |
| 318.15 | 0.9044 | 808.77 |
| 318.15 | 1.0000 | 807.7 |
| 323.15 | 0.0000 | 838.42 |
| 323.15 | 0.1041 | 831.72 |
| 323.15 | 0.1973 | 827.05 |
| 323.15 | 0.3018 | 822.76 |
| 323.15 | 0.4033 | 819.26 |
| 323.15 | 0.5035 | 816.18 |
| 323.15 | 0.6007 | 813.46 |
| 323.15 | 0.6996 | 810.87 |
| 323.15 | 0.7930 | 808.58 |
| 323.15 | 0.9044 | 806.05 |
| 323.15 | 1.0000 | 804.05 |
| 333.15 | 0.0000 | 828.94 |
| 333.15 | 0.1041 | 822.45 |
| 333.15 | 0.1973 | 817.92 |
| 333.15 | 0.3018 | 813.92 |
| 333.15 | 0.4033 | 810.68 |
| 333.15 | 0.5035 | 807.88 |
| 333.15 | 0.6007 | 805.4 |
| 333.15 | 0.6996 | 803.05 |
| 333.15 | 0.7930 | 800.97 |
| 333.15 | 0.9044 | 798.68 |
| 333.15 | 1.0000 | 796.88 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Toluene (1) - Liquid | Mass density, kg/m3 - Liquid |
| 303.15 | 0.0000 | 818.38 |
| 303.15 | 0.0495 | 819.62 |
| 303.15 | 0.1104 | 821.19 |
| 303.15 | 0.1513 | 822.25 |
| 303.15 | 0.1999 | 823.55 |
| 303.15 | 0.2517 | 824.98 |
| 303.15 | 0.2997 | 826.34 |
| 303.15 | 0.3560 | 828.02 |
| 303.15 | 0.3998 | 829.32 |
| 303.15 | 0.4506 | 830.99 |
| 303.15 | 0.5001 | 832.63 |
| 303.15 | 0.5513 | 834.46 |
| 303.15 | 0.6014 | 836.31 |
| 303.15 | 0.6495 | 838.22 |
| 303.15 | 0.6997 | 840.36 |
| 303.15 | 0.7569 | 842.9 |
| 303.15 | 0.8012 | 845.02 |
| 303.15 | 0.8527 | 847.7 |
| 303.15 | 0.9000 | 850.32 |
| 303.15 | 0.9540 | 853.6 |
| 303.15 | 1.0000 | 856.62 |
| 313.15 | 0.0000 | 811.05 |
| 313.15 | 0.0495 | 812.14 |
| 313.15 | 0.1104 | 813.56 |
| 313.15 | 0.1513 | 814.55 |
| 313.15 | 0.1999 | 815.73 |
| 313.15 | 0.2517 | 817.04 |
| 313.15 | 0.2997 | 818.29 |
| 313.15 | 0.3560 | 819.85 |
| 313.15 | 0.3998 | 821.03 |
| 313.15 | 0.4506 | 822.56 |
| 313.15 | 0.5001 | 824.08 |
| 313.15 | 0.5513 | 825.77 |
| 313.15 | 0.6014 | 827.51 |
| 313.15 | 0.6495 | 829.3 |
| 313.15 | 0.6997 | 831.29 |
| 313.15 | 0.7569 | 833.69 |
| 313.15 | 0.8012 | 835.74 |
| 313.15 | 0.8527 | 838.28 |
| 313.15 | 0.9000 | 840.85 |
| 313.15 | 0.9540 | 844.0 |
| 313.15 | 1.0000 | 847.03 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 94.9 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Octanol (2) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 866.68 |
| 293.15 | 0.1041 | 859.2 |
| 293.15 | 0.1973 | 853.95 |
| 293.15 | 0.3018 | 848.87 |
| 293.15 | 0.4033 | 844.52 |
| 293.15 | 0.5035 | 840.66 |
| 293.15 | 0.6007 | 837.23 |
| 293.15 | 0.6996 | 834.03 |
| 293.15 | 0.7930 | 831.2 |
| 293.15 | 0.9044 | 828.07 |
| 293.15 | 1.0000 | 825.57 |
| 298.15 | 0.0000 | 861.74 |
| 298.15 | 0.1041 | 854.47 |
| 298.15 | 0.1973 | 849.33 |
| 298.15 | 0.3018 | 844.4 |
| 298.15 | 0.4033 | 840.2 |
| 298.15 | 0.5035 | 836.46 |
| 298.15 | 0.6007 | 833.15 |
| 298.15 | 0.6996 | 830.05 |
| 298.15 | 0.7930 | 827.33 |
| 298.15 | 0.9044 | 824.31 |
| 298.15 | 1.0000 | 821.9 |
| 303.15 | 0.0000 | 857.39 |
| 303.15 | 0.1041 | 849.63 |
| 303.15 | 0.1973 | 844.59 |
| 303.15 | 0.3018 | 839.8 |
| 303.15 | 0.4033 | 835.73 |
| 303.15 | 0.5035 | 832.13 |
| 303.15 | 0.6007 | 828.94 |
| 303.15 | 0.6996 | 825.95 |
| 303.15 | 0.7930 | 823.32 |
| 303.15 | 0.9044 | 820.4 |
| 303.15 | 1.0000 | 818.08 |
| 308.15 | 0.0000 | 851.69 |
| 308.15 | 0.1041 | 844.83 |
| 308.15 | 0.1973 | 839.89 |
| 308.15 | 0.3018 | 835.26 |
| 308.15 | 0.4033 | 831.33 |
| 308.15 | 0.5035 | 827.86 |
| 308.15 | 0.6007 | 824.78 |
| 308.15 | 0.6996 | 821.9 |
| 308.15 | 0.7930 | 819.36 |
| 308.15 | 0.9044 | 816.55 |
| 308.15 | 1.0000 | 814.31 |
| 313.15 | 0.0000 | 847.82 |
| 313.15 | 0.1041 | 840.03 |
| 313.15 | 0.1973 | 835.16 |
| 313.15 | 0.3018 | 830.67 |
| 313.15 | 0.4033 | 826.9 |
| 313.15 | 0.5035 | 823.56 |
| 313.15 | 0.6007 | 820.6 |
| 313.15 | 0.6996 | 817.82 |
| 313.15 | 0.7930 | 815.37 |
| 313.15 | 0.9044 | 812.65 |
| 313.15 | 1.0000 | 811.09 |
| 318.15 | 0.0000 | 842.88 |
| 318.15 | 0.1041 | 835.18 |
| 318.15 | 0.1973 | 830.43 |
| 318.15 | 0.3018 | 826.08 |
| 318.15 | 0.4033 | 822.45 |
| 318.15 | 0.5035 | 819.25 |
| 318.15 | 0.6007 | 816.41 |
| 318.15 | 0.6996 | 813.74 |
| 318.15 | 0.7930 | 811.38 |
| 318.15 | 0.9044 | 808.77 |
| 318.15 | 1.0000 | 807.7 |
| 323.15 | 0.0000 | 838.42 |
| 323.15 | 0.1041 | 831.72 |
| 323.15 | 0.1973 | 827.05 |
| 323.15 | 0.3018 | 822.76 |
| 323.15 | 0.4033 | 819.26 |
| 323.15 | 0.5035 | 816.18 |
| 323.15 | 0.6007 | 813.46 |
| 323.15 | 0.6996 | 810.87 |
| 323.15 | 0.7930 | 808.58 |
| 323.15 | 0.9044 | 806.05 |
| 323.15 | 1.0000 | 804.05 |
| 333.15 | 0.0000 | 828.94 |
| 333.15 | 0.1041 | 822.45 |
| 333.15 | 0.1973 | 817.92 |
| 333.15 | 0.3018 | 813.92 |
| 333.15 | 0.4033 | 810.68 |
| 333.15 | 0.5035 | 807.88 |
| 333.15 | 0.6007 | 805.4 |
| 333.15 | 0.6996 | 803.05 |
| 333.15 | 0.7930 | 800.97 |
| 333.15 | 0.9044 | 798.68 |
| 333.15 | 1.0000 | 796.88 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Toluene (1) - Liquid | Mass density, kg/m3 - Liquid |
| 303.15 | 0.0000 | 818.38 |
| 303.15 | 0.0495 | 819.62 |
| 303.15 | 0.1104 | 821.19 |
| 303.15 | 0.1513 | 822.25 |
| 303.15 | 0.1999 | 823.55 |
| 303.15 | 0.2517 | 824.98 |
| 303.15 | 0.2997 | 826.34 |
| 303.15 | 0.3560 | 828.02 |
| 303.15 | 0.3998 | 829.32 |
| 303.15 | 0.4506 | 830.99 |
| 303.15 | 0.5001 | 832.63 |
| 303.15 | 0.5513 | 834.46 |
| 303.15 | 0.6014 | 836.31 |
| 303.15 | 0.6495 | 838.22 |
| 303.15 | 0.6997 | 840.36 |
| 303.15 | 0.7569 | 842.9 |
| 303.15 | 0.8012 | 845.02 |
| 303.15 | 0.8527 | 847.7 |
| 303.15 | 0.9000 | 850.32 |
| 303.15 | 0.9540 | 853.6 |
| 303.15 | 1.0000 | 856.62 |
| 313.15 | 0.0000 | 811.05 |
| 313.15 | 0.0495 | 812.14 |
| 313.15 | 0.1104 | 813.56 |
| 313.15 | 0.1513 | 814.55 |
| 313.15 | 0.1999 | 815.73 |
| 313.15 | 0.2517 | 817.04 |
| 313.15 | 0.2997 | 818.29 |
| 313.15 | 0.3560 | 819.85 |
| 313.15 | 0.3998 | 821.03 |
| 313.15 | 0.4506 | 822.56 |
| 313.15 | 0.5001 | 824.08 |
| 313.15 | 0.5513 | 825.77 |
| 313.15 | 0.6014 | 827.51 |
| 313.15 | 0.6495 | 829.3 |
| 313.15 | 0.6997 | 831.29 |
| 313.15 | 0.7569 | 833.69 |
| 313.15 | 0.8012 | 835.74 |
| 313.15 | 0.8527 | 838.28 |
| 313.15 | 0.9000 | 840.85 |
| 313.15 | 0.9540 | 844.0 |
| 313.15 | 1.0000 | 847.03 |
Speed of sound, m/s [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Frequency, MHz = 2 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Toluene (1) - Liquid | Speed of sound, m/s - Liquid |
| 303.15 | 0.0000 | 1334.0 |
| 303.15 | 0.0495 | 1329.0 |
| 303.15 | 0.1104 | 1325.0 |
| 303.15 | 0.1513 | 1321.0 |
| 303.15 | 0.1999 | 1316.0 |
| 303.15 | 0.2517 | 1310.0 |
| 303.15 | 0.2997 | 1304.0 |
| 303.15 | 0.3560 | 1297.0 |
| 303.15 | 0.3998 | 1291.0 |
| 303.15 | 0.4506 | 1286.0 |
| 303.15 | 0.5001 | 1281.0 |
| 303.15 | 0.5513 | 1276.0 |
| 303.15 | 0.6014 | 1272.0 |
| 303.15 | 0.6495 | 1270.0 |
| 303.15 | 0.6997 | 1268.0 |
| 303.15 | 0.7569 | 1267.0 |
| 303.15 | 0.8012 | 1268.0 |
| 303.15 | 0.8527 | 1269.0 |
| 303.15 | 0.9000 | 1273.0 |
| 303.15 | 0.9540 | 1280.0 |
| 303.15 | 1.0000 | 1289.0 |
| 313.15 | 0.0000 | 1304.0 |
| 313.15 | 0.0495 | 1300.0 |
| 313.15 | 0.1104 | 1293.0 |
| 313.15 | 0.1513 | 1287.0 |
| 313.15 | 0.1999 | 1282.0 |
| 313.15 | 0.2517 | 1274.0 |
| 313.15 | 0.2997 | 1268.0 |
| 313.15 | 0.3560 | 1262.0 |
| 313.15 | 0.3998 | 1255.0 |
| 313.15 | 0.4506 | 1250.0 |
| 313.15 | 0.5001 | 1242.0 |
| 313.15 | 0.5513 | 1238.0 |
| 313.15 | 0.6014 | 1234.0 |
| 313.15 | 0.6495 | 1231.0 |
| 313.15 | 0.6997 | 1228.0 |
| 313.15 | 0.7569 | 1228.0 |
| 313.15 | 0.8012 | 1229.0 |
| 313.15 | 0.8527 | 1232.0 |
| 313.15 | 0.9000 | 1236.0 |
| 313.15 | 0.9540 | 1245.0 |
| 313.15 | 1.0000 | 1256.0 |
Speed of sound, m/s [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Frequency, MHz = 2 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Toluene (1) - Liquid | Speed of sound, m/s - Liquid |
| 303.15 | 0.0000 | 1334.0 |
| 303.15 | 0.0495 | 1329.0 |
| 303.15 | 0.1104 | 1325.0 |
| 303.15 | 0.1513 | 1321.0 |
| 303.15 | 0.1999 | 1316.0 |
| 303.15 | 0.2517 | 1310.0 |
| 303.15 | 0.2997 | 1304.0 |
| 303.15 | 0.3560 | 1297.0 |
| 303.15 | 0.3998 | 1291.0 |
| 303.15 | 0.4506 | 1286.0 |
| 303.15 | 0.5001 | 1281.0 |
| 303.15 | 0.5513 | 1276.0 |
| 303.15 | 0.6014 | 1272.0 |
| 303.15 | 0.6495 | 1270.0 |
| 303.15 | 0.6997 | 1268.0 |
| 303.15 | 0.7569 | 1267.0 |
| 303.15 | 0.8012 | 1268.0 |
| 303.15 | 0.8527 | 1269.0 |
| 303.15 | 0.9000 | 1273.0 |
| 303.15 | 0.9540 | 1280.0 |
| 303.15 | 1.0000 | 1289.0 |
| 313.15 | 0.0000 | 1304.0 |
| 313.15 | 0.0495 | 1300.0 |
| 313.15 | 0.1104 | 1293.0 |
| 313.15 | 0.1513 | 1287.0 |
| 313.15 | 0.1999 | 1282.0 |
| 313.15 | 0.2517 | 1274.0 |
| 313.15 | 0.2997 | 1268.0 |
| 313.15 | 0.3560 | 1262.0 |
| 313.15 | 0.3998 | 1255.0 |
| 313.15 | 0.4506 | 1250.0 |
| 313.15 | 0.5001 | 1242.0 |
| 313.15 | 0.5513 | 1238.0 |
| 313.15 | 0.6014 | 1234.0 |
| 313.15 | 0.6495 | 1231.0 |
| 313.15 | 0.6997 | 1228.0 |
| 313.15 | 0.7569 | 1228.0 |
| 313.15 | 0.8012 | 1229.0 |
| 313.15 | 0.8527 | 1232.0 |
| 313.15 | 0.9000 | 1236.0 |
| 313.15 | 0.9540 | 1245.0 |
| 313.15 | 1.0000 | 1256.0 |
Sources
- Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
- Densities, Viscosities, and Speed of Sound Studies of Binary Mixtures of Methylbenzene with Heptan-1-ol, Octan-1-ol, and Decan-1-ol at (303.15 and 313.15) K