- Name
- Dodecane
- InChI
- InChI=1S/C12H26/c1-3-5-7-9-11-12-10-8-6-4-2/h3-12H2,1-2H3
- InChI Key
- SNRUBQQJIBEYMU-UHFFFAOYSA-N
- Formula
- C12H26
- SMILES
- CCCCCCCCCCCC
- Mol. Weight (g/mol)
- 170.33
- CAS
- 112-40-3
- Name
- Naphthalene, 1,2,3,4-tetrahydro-
- InChI
- InChI=1S/C10H12/c1-2-6-10-8-4-3-7-9(10)5-1/h1-2,5-6H,3-4,7-8H2
- InChI Key
- CXWXQJXEFPUFDZ-UHFFFAOYSA-N
- Formula
- C10H12
- SMILES
- c1ccc2c(c1)CCCC2
- Mol. Weight (g/mol)
- 132.20
- CAS
- 119-64-2
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Datasets
- η - Viscosity, Pa*s
- Refractive index (other wavelength)
- n0 - Refractive index (Na D-line)
- ρl - Mass density, kg/m3 (3)
- csound,fluid - Speed of Sound, m/s
- Binary diffusion coefficient, m2/s
Viscosity, Pa*s [ref]
Operational conditions:
- Mass fraction = 0.5 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
|---|---|
| 100.00 | 0.0015 |
| 4000.00 | 0.0015 |
| 10000.00 | 0.0016 |
Refractive index (other wavelength) [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Mole fraction of Naphthalene, 1,2,3,4-tetrahydro- (2) - Liquid | Wavelength, nm - Liquid | Refractive index (other wavelength) - Liquid |
| 293.15 | 0.1014 | 657.2 | 1.4288 |
| 293.15 | 0.2024 | 657.2 | 1.439 |
| 293.15 | 0.3032 | 657.2 | 1.4484 |
| 293.15 | 0.4036 | 657.2 | 1.4592 |
| 293.15 | 0.5038 | 657.2 | 1.4708 |
| 293.15 | 0.6036 | 657.2 | 1.4819 |
| 293.15 | 0.7032 | 657.2 | 1.4944 |
| 293.15 | 0.8024 | 657.2 | 1.508 |
| 293.15 | 0.9014 | 657.2 | 1.5223 |
| 293.15 | 0.1014 | 633.2 | 1.4295 |
| 293.15 | 0.2024 | 633.2 | 1.4392 |
| 293.15 | 0.3032 | 633.2 | 1.4492 |
| 293.15 | 0.4036 | 633.2 | 1.46 |
| 293.15 | 0.5038 | 633.2 | 1.4711 |
| 293.15 | 0.6036 | 633.2 | 1.4832 |
| 293.15 | 0.7032 | 633.2 | 1.4955 |
| 293.15 | 0.8024 | 633.2 | 1.5089 |
| 293.15 | 0.9014 | 633.2 | 1.5229 |
| 293.15 | 0.1014 | 589.3 | 1.431 |
| 293.15 | 0.2024 | 589.3 | 1.4409 |
| 293.15 | 0.3032 | 589.3 | 1.451 |
| 293.15 | 0.4036 | 589.3 | 1.462 |
| 293.15 | 0.5038 | 589.3 | 1.4733 |
| 293.15 | 0.6036 | 589.3 | 1.4855 |
| 293.15 | 0.7032 | 589.3 | 1.498 |
| 293.15 | 0.8024 | 589.3 | 1.5116 |
| 293.15 | 0.9014 | 589.3 | 1.5259 |
| 293.15 | 0.1014 | 513.9 | 1.4347 |
| 293.15 | 0.2024 | 513.9 | 1.4449 |
| 293.15 | 0.3032 | 513.9 | 1.4554 |
| 293.15 | 0.4036 | 513.9 | 1.4667 |
| 293.15 | 0.5038 | 513.9 | 1.4784 |
| 293.15 | 0.6036 | 513.9 | 1.4911 |
| 293.15 | 0.7032 | 513.9 | 1.5042 |
| 293.15 | 0.8024 | 513.9 | 1.518 |
| 293.15 | 0.9014 | 513.9 | 1.5328 |
| 293.15 | 0.1014 | 436.1 | 1.4413 |
| 293.15 | 0.2024 | 436.1 | 1.452 |
| 293.15 | 0.3032 | 436.1 | 1.4631 |
| 293.15 | 0.4036 | 436.1 | 1.4751 |
| 293.15 | 0.5038 | 436.1 | 1.4881 |
| 293.15 | 0.6036 | 436.1 | 1.5013 |
| 293.15 | 0.7032 | 436.1 | 1.5148 |
| 293.15 | 0.8024 | 436.1 | 1.5297 |
| 293.15 | 0.9014 | 436.1 | 1.5456 |
| 298.15 | 0.1014 | 657.2 | 1.4267 |
| 298.15 | 0.2024 | 657.2 | 1.4362 |
| 298.15 | 0.3032 | 657.2 | 1.4463 |
| 298.15 | 0.4036 | 657.2 | 1.4568 |
| 298.15 | 0.5038 | 657.2 | 1.4685 |
| 298.15 | 0.6036 | 657.2 | 1.4797 |
| 298.15 | 0.7032 | 657.2 | 1.4918 |
| 298.15 | 0.8024 | 657.2 | 1.5053 |
| 298.15 | 0.9014 | 657.2 | 1.5199 |
| 298.15 | 0.1014 | 633.2 | 1.4273 |
| 298.15 | 0.2024 | 633.2 | 1.437 |
| 298.15 | 0.3032 | 633.2 | 1.4469 |
| 298.15 | 0.4036 | 633.2 | 1.4577 |
| 298.15 | 0.5038 | 633.2 | 1.4689 |
| 298.15 | 0.6036 | 633.2 | 1.4807 |
| 298.15 | 0.7032 | 633.2 | 1.4932 |
| 298.15 | 0.8024 | 633.2 | 1.5065 |
| 298.15 | 0.9014 | 633.2 | 1.5205 |
| 298.15 | 0.1014 | 589.3 | 1.4288 |
| 298.15 | 0.2024 | 589.3 | 1.4387 |
| 298.15 | 0.3032 | 589.3 | 1.449 |
| 298.15 | 0.4036 | 589.3 | 1.4596 |
| 298.15 | 0.5038 | 589.3 | 1.4708 |
| 298.15 | 0.6036 | 589.3 | 1.483 |
| 298.15 | 0.7032 | 589.3 | 1.4955 |
| 298.15 | 0.8024 | 589.3 | 1.5093 |
| 298.15 | 0.9014 | 589.3 | 1.5235 |
| 298.15 | 0.1014 | 513.9 | 1.4325 |
| 298.15 | 0.2024 | 513.9 | 1.4427 |
| 298.15 | 0.3032 | 513.9 | 1.4533 |
| 298.15 | 0.4036 | 513.9 | 1.4644 |
| 298.15 | 0.5038 | 513.9 | 1.4761 |
| 298.15 | 0.6036 | 513.9 | 1.4887 |
| 298.15 | 0.7032 | 513.9 | 1.5016 |
| 298.15 | 0.8024 | 513.9 | 1.5156 |
| 298.15 | 0.9014 | 513.9 | 1.5305 |
| 298.15 | 0.1014 | 436.1 | 1.439 |
| 298.15 | 0.2024 | 436.1 | 1.4498 |
| 298.15 | 0.3032 | 436.1 | 1.4607 |
| 298.15 | 0.4036 | 436.1 | 1.4728 |
| 298.15 | 0.5038 | 436.1 | 1.4856 |
| 298.15 | 0.6036 | 436.1 | 1.4988 |
| 298.15 | 0.7032 | 436.1 | 1.5124 |
| 298.15 | 0.8024 | 436.1 | 1.5272 |
| 298.15 | 0.9014 | 436.1 | 1.543 |
| 303.15 | 0.1014 | 657.2 | 1.4243 |
| 303.15 | 0.2024 | 657.2 | 1.434 |
| 303.15 | 0.3032 | 657.2 | 1.4439 |
| 303.15 | 0.4036 | 657.2 | 1.4544 |
| 303.15 | 0.5038 | 657.2 | 1.4662 |
| 303.15 | 0.6036 | 657.2 | 1.4773 |
| 303.15 | 0.7032 | 657.2 | 1.4895 |
| 303.15 | 0.8024 | 657.2 | 1.5028 |
| 303.15 | 0.9014 | 657.2 | 1.5174 |
| 303.15 | 0.1014 | 633.2 | 1.425 |
| 303.15 | 0.2024 | 633.2 | 1.4347 |
| 303.15 | 0.3032 | 633.2 | 1.4444 |
| 303.15 | 0.4036 | 633.2 | 1.4555 |
| 303.15 | 0.5038 | 633.2 | 1.4667 |
| 303.15 | 0.6036 | 633.2 | 1.4786 |
| 303.15 | 0.7032 | 633.2 | 1.4908 |
| 303.15 | 0.8024 | 633.2 | 1.5042 |
| 303.15 | 0.9014 | 633.2 | 1.518 |
| 303.15 | 0.1014 | 589.3 | 1.4266 |
| 303.15 | 0.2024 | 589.3 | 1.4364 |
| 303.15 | 0.3032 | 589.3 | 1.4464 |
| 303.15 | 0.4036 | 589.3 | 1.4573 |
| 303.15 | 0.5038 | 589.3 | 1.4684 |
| 303.15 | 0.6036 | 589.3 | 1.4808 |
| 303.15 | 0.7032 | 589.3 | 1.4932 |
| 303.15 | 0.8024 | 589.3 | 1.5069 |
| 303.15 | 0.9014 | 589.3 | 1.521 |
| 303.15 | 0.1014 | 513.9 | 1.4302 |
| 303.15 | 0.2024 | 513.9 | 1.4403 |
| 303.15 | 0.3032 | 513.9 | 1.4508 |
| 303.15 | 0.4036 | 513.9 | 1.4622 |
| 303.15 | 0.5038 | 513.9 | 1.4736 |
| 303.15 | 0.6036 | 513.9 | 1.4863 |
| 303.15 | 0.7032 | 513.9 | 1.4992 |
| 303.15 | 0.8024 | 513.9 | 1.5132 |
| 303.15 | 0.9014 | 513.9 | 1.5278 |
| 303.15 | 0.1014 | 436.1 | 1.4367 |
| 303.15 | 0.2024 | 436.1 | 1.4474 |
| 303.15 | 0.3032 | 436.1 | 1.4582 |
| 303.15 | 0.4036 | 436.1 | 1.4705 |
| 303.15 | 0.5038 | 436.1 | 1.4829 |
| 303.15 | 0.6036 | 436.1 | 1.4962 |
| 303.15 | 0.7032 | 436.1 | 1.5098 |
| 303.15 | 0.8024 | 436.1 | 1.5245 |
| 303.15 | 0.9014 | 436.1 | 1.5403 |
| 308.15 | 0.1014 | 657.2 | 1.4222 |
| 308.15 | 0.2024 | 657.2 | 1.4316 |
| 308.15 | 0.3032 | 657.2 | 1.4413 |
| 308.15 | 0.4036 | 657.2 | 1.452 |
| 308.15 | 0.5038 | 657.2 | 1.4639 |
| 308.15 | 0.6036 | 657.2 | 1.475 |
| 308.15 | 0.7032 | 657.2 | 1.4869 |
| 308.15 | 0.8024 | 657.2 | 1.5001 |
| 308.15 | 0.9014 | 657.2 | 1.5152 |
| 308.15 | 0.1014 | 633.2 | 1.423 |
| 308.15 | 0.2024 | 633.2 | 1.4323 |
| 308.15 | 0.3032 | 633.2 | 1.4422 |
| 308.15 | 0.4036 | 633.2 | 1.4532 |
| 308.15 | 0.5038 | 633.2 | 1.4644 |
| 308.15 | 0.6036 | 633.2 | 1.4762 |
| 308.15 | 0.7032 | 633.2 | 1.4886 |
| 308.15 | 0.8024 | 633.2 | 1.5014 |
| 308.15 | 0.9014 | 633.2 | 1.5156 |
| 308.15 | 0.1014 | 589.3 | 1.4245 |
| 308.15 | 0.2024 | 589.3 | 1.434 |
| 308.15 | 0.3032 | 589.3 | 1.4441 |
| 308.15 | 0.4036 | 589.3 | 1.4549 |
| 308.15 | 0.5038 | 589.3 | 1.4662 |
| 308.15 | 0.6036 | 589.3 | 1.4785 |
| 308.15 | 0.7032 | 589.3 | 1.4909 |
| 308.15 | 0.8024 | 589.3 | 1.5043 |
| 308.15 | 0.9014 | 589.3 | 1.5187 |
| 308.15 | 0.1014 | 513.9 | 1.4281 |
| 308.15 | 0.2024 | 513.9 | 1.4379 |
| 308.15 | 0.3032 | 513.9 | 1.4486 |
| 308.15 | 0.4036 | 513.9 | 1.4599 |
| 308.15 | 0.5038 | 513.9 | 1.4712 |
| 308.15 | 0.6036 | 513.9 | 1.4839 |
| 308.15 | 0.7032 | 513.9 | 1.4968 |
| 308.15 | 0.8024 | 513.9 | 1.5108 |
| 308.15 | 0.9014 | 513.9 | 1.5256 |
| 308.15 | 0.1014 | 436.1 | 1.4345 |
| 308.15 | 0.2024 | 436.1 | 1.4449 |
| 308.15 | 0.3032 | 436.1 | 1.4559 |
| 308.15 | 0.4036 | 436.1 | 1.4678 |
| 308.15 | 0.5038 | 436.1 | 1.4805 |
| 308.15 | 0.6036 | 436.1 | 1.4937 |
| 308.15 | 0.7032 | 436.1 | 1.5075 |
| 308.15 | 0.8024 | 436.1 | 1.5218 |
| 308.15 | 0.9014 | 436.1 | 1.538 |
| 313.15 | 0.1014 | 657.2 | 1.42 |
| 313.15 | 0.2024 | 657.2 | 1.4292 |
| 313.15 | 0.3032 | 657.2 | 1.439 |
| 313.15 | 0.4036 | 657.2 | 1.4497 |
| 313.15 | 0.5038 | 657.2 | 1.4616 |
| 313.15 | 0.6036 | 657.2 | 1.4725 |
| 313.15 | 0.7032 | 657.2 | 1.4847 |
| 313.15 | 0.8024 | 657.2 | 1.4976 |
| 313.15 | 0.9014 | 657.2 | 1.5128 |
| 313.15 | 0.1014 | 633.2 | 1.4207 |
| 313.15 | 0.2024 | 633.2 | 1.4303 |
| 313.15 | 0.3032 | 633.2 | 1.4398 |
| 313.15 | 0.4036 | 633.2 | 1.4507 |
| 313.15 | 0.5038 | 633.2 | 1.4619 |
| 313.15 | 0.6036 | 633.2 | 1.474 |
| 313.15 | 0.7032 | 633.2 | 1.4861 |
| 313.15 | 0.8024 | 633.2 | 1.4993 |
| 313.15 | 0.9014 | 633.2 | 1.5132 |
| 313.15 | 0.1014 | 589.3 | 1.4223 |
| 313.15 | 0.2024 | 589.3 | 1.4318 |
| 313.15 | 0.3032 | 589.3 | 1.4416 |
| 313.15 | 0.4036 | 589.3 | 1.4524 |
| 313.15 | 0.5038 | 589.3 | 1.4637 |
| 313.15 | 0.6036 | 589.3 | 1.4763 |
| 313.15 | 0.7032 | 589.3 | 1.4886 |
| 313.15 | 0.8024 | 589.3 | 1.5017 |
| 313.15 | 0.9014 | 589.3 | 1.5162 |
| 313.15 | 0.1014 | 513.9 | 1.4258 |
| 313.15 | 0.2024 | 513.9 | 1.4357 |
| 313.15 | 0.3032 | 513.9 | 1.4461 |
| 313.15 | 0.4036 | 513.9 | 1.4576 |
| 313.15 | 0.5038 | 513.9 | 1.4688 |
| 313.15 | 0.6036 | 513.9 | 1.4817 |
| 313.15 | 0.7032 | 513.9 | 1.4944 |
| 313.15 | 0.8024 | 513.9 | 1.5083 |
| 313.15 | 0.9014 | 513.9 | 1.5231 |
| 313.15 | 0.1014 | 436.1 | 1.4322 |
| 313.15 | 0.2024 | 436.1 | 1.4428 |
| 313.15 | 0.3032 | 436.1 | 1.4534 |
| 313.15 | 0.4036 | 436.1 | 1.4652 |
| 313.15 | 0.5038 | 436.1 | 1.4782 |
| 313.15 | 0.6036 | 436.1 | 1.4911 |
| 313.15 | 0.7032 | 436.1 | 1.5049 |
| 313.15 | 0.8024 | 436.1 | 1.5194 |
| 313.15 | 0.9014 | 436.1 | 1.5354 |
| 318.15 | 0.1014 | 657.2 | 1.4181 |
| 318.15 | 0.2024 | 657.2 | 1.427 |
| 318.15 | 0.3032 | 657.2 | 1.437 |
| 318.15 | 0.4036 | 657.2 | 1.4472 |
| 318.15 | 0.5038 | 657.2 | 1.4593 |
| 318.15 | 0.6036 | 657.2 | 1.4701 |
| 318.15 | 0.7032 | 657.2 | 1.4822 |
| 318.15 | 0.8024 | 657.2 | 1.4951 |
| 318.15 | 0.9014 | 657.2 | 1.5104 |
| 318.15 | 0.1014 | 633.2 | 1.4186 |
| 318.15 | 0.2024 | 633.2 | 1.4278 |
| 318.15 | 0.3032 | 633.2 | 1.4379 |
| 318.15 | 0.4036 | 633.2 | 1.4483 |
| 318.15 | 0.5038 | 633.2 | 1.4598 |
| 318.15 | 0.6036 | 633.2 | 1.4716 |
| 318.15 | 0.7032 | 633.2 | 1.4839 |
| 318.15 | 0.8024 | 633.2 | 1.4967 |
| 318.15 | 0.9014 | 633.2 | 1.5112 |
| 318.15 | 0.1014 | 589.3 | 1.4201 |
| 318.15 | 0.2024 | 589.3 | 1.4293 |
| 318.15 | 0.3032 | 589.3 | 1.4396 |
| 318.15 | 0.4036 | 589.3 | 1.4499 |
| 318.15 | 0.5038 | 589.3 | 1.4614 |
| 318.15 | 0.6036 | 589.3 | 1.4739 |
| 318.15 | 0.7032 | 589.3 | 1.4862 |
| 318.15 | 0.8024 | 589.3 | 1.4991 |
| 318.15 | 0.9014 | 589.3 | 1.514 |
| 318.15 | 0.1014 | 513.9 | 1.4237 |
| 318.15 | 0.2024 | 513.9 | 1.4333 |
| 318.15 | 0.3032 | 513.9 | 1.4441 |
| 318.15 | 0.4036 | 513.9 | 1.4549 |
| 318.15 | 0.5038 | 513.9 | 1.4665 |
| 318.15 | 0.6036 | 513.9 | 1.4793 |
| 318.15 | 0.7032 | 513.9 | 1.4918 |
| 318.15 | 0.8024 | 513.9 | 1.5057 |
| 318.15 | 0.9014 | 513.9 | 1.5208 |
| 318.15 | 0.1014 | 436.1 | 1.43 |
| 318.15 | 0.2024 | 436.1 | 1.4403 |
| 318.15 | 0.3032 | 436.1 | 1.4508 |
| 318.15 | 0.4036 | 436.1 | 1.4627 |
| 318.15 | 0.5038 | 436.1 | 1.4758 |
| 318.15 | 0.6036 | 436.1 | 1.4886 |
| 318.15 | 0.7032 | 436.1 | 1.5024 |
| 318.15 | 0.8024 | 436.1 | 1.5167 |
| 318.15 | 0.9014 | 436.1 | 1.5331 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Naphthalene, 1,2,3,4-tetrahydro- (2) - Liquid | Refractive index (Na D-line) - Liquid |
| 293.15 | 0.0000 | 1.4222 |
| 293.15 | 0.1021 | 1.4296 |
| 293.15 | 0.2015 | 1.4377 |
| 293.15 | 0.3070 | 1.4469 |
| 293.15 | 0.3998 | 1.4558 |
| 293.15 | 0.4985 | 1.4662 |
| 293.15 | 0.5961 | 1.4777 |
| 293.15 | 0.7019 | 1.4915 |
| 293.15 | 0.8012 | 1.5062 |
| 293.15 | 0.8998 | 1.5227 |
| 293.15 | 1.0000 | 1.5415 |
| 303.15 | 0.0000 | 1.4178 |
| 303.15 | 0.1021 | 1.4254 |
| 303.15 | 0.2015 | 1.4333 |
| 303.15 | 0.3070 | 1.4425 |
| 303.15 | 0.3998 | 1.4515 |
| 303.15 | 0.4985 | 1.4618 |
| 303.15 | 0.5961 | 1.4733 |
| 303.15 | 0.7019 | 1.4872 |
| 303.15 | 0.8012 | 1.5017 |
| 303.15 | 0.8998 | 1.5182 |
| 303.15 | 1.0000 | 1.5369 |
| 313.15 | 0.0000 | 1.4135 |
| 313.15 | 0.1021 | 1.421 |
| 313.15 | 0.2015 | 1.4289 |
| 313.15 | 0.3070 | 1.4382 |
| 313.15 | 0.3998 | 1.4471 |
| 313.15 | 0.4985 | 1.4575 |
| 313.15 | 0.5961 | 1.4688 |
| 313.15 | 0.7019 | 1.4827 |
| 313.15 | 0.8012 | 1.4972 |
| 313.15 | 0.8998 | 1.5136 |
| 313.15 | 1.0000 | 1.5322 |
| 323.15 | 0.0000 | 1.4091 |
| 323.15 | 0.1021 | 1.4166 |
| 323.15 | 0.2015 | 1.4246 |
| 323.15 | 0.3070 | 1.4337 |
| 323.15 | 0.3998 | 1.4426 |
| 323.15 | 0.4985 | 1.453 |
| 323.15 | 0.5961 | 1.4644 |
| 323.15 | 0.7019 | 1.4782 |
| 323.15 | 0.8012 | 1.4927 |
| 323.15 | 0.8998 | 1.509 |
| 323.15 | 1.0000 | 1.5275 |
| 333.15 | 0.0000 | 1.4048 |
| 333.15 | 0.1021 | 1.4122 |
| 333.15 | 0.2015 | 1.4201 |
| 333.15 | 0.3070 | 1.4292 |
| 333.15 | 0.3998 | 1.4382 |
| 333.15 | 0.4985 | 1.4486 |
| 333.15 | 0.5961 | 1.46 |
| 333.15 | 0.7019 | 1.4736 |
| 333.15 | 0.8012 | 1.4882 |
| 333.15 | 0.8998 | 1.5043 |
| 333.15 | 1.0000 | 1.5227 |
| 343.15 | 0.0000 | 1.4002 |
| 343.15 | 0.1021 | 1.4078 |
| 343.15 | 0.2015 | 1.4156 |
| 343.15 | 0.3070 | 1.4248 |
| 343.15 | 0.3998 | 1.4336 |
| 343.15 | 0.4985 | 1.444 |
| 343.15 | 0.5961 | 1.4553 |
| 343.15 | 0.7019 | 1.4691 |
| 343.15 | 0.8012 | 1.4835 |
| 343.15 | 0.8998 | 1.4993 |
| 343.15 | 1.0000 | 1.5179 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Naphthalene, 1,2,3,4-tetrahydro- (2) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 748.92 |
| 293.15 | 0.1021 | 763.04 |
| 293.15 | 0.2015 | 777.99 |
| 293.15 | 0.3070 | 795.31 |
| 293.15 | 0.3998 | 811.97 |
| 293.15 | 0.4985 | 831.41 |
| 293.15 | 0.5961 | 852.66 |
| 293.15 | 0.7019 | 878.22 |
| 293.15 | 0.8012 | 905.15 |
| 293.15 | 0.8998 | 935.03 |
| 293.15 | 1.0000 | 969.52 |
| 303.15 | 0.0000 | 741.66 |
| 303.15 | 0.1021 | 755.74 |
| 303.15 | 0.2015 | 770.65 |
| 303.15 | 0.3070 | 787.92 |
| 303.15 | 0.3998 | 804.53 |
| 303.15 | 0.4985 | 823.91 |
| 303.15 | 0.5961 | 845.1 |
| 303.15 | 0.7019 | 870.59 |
| 303.15 | 0.8012 | 897.44 |
| 303.15 | 0.8998 | 927.23 |
| 303.15 | 1.0000 | 961.59 |
| 313.15 | 0.0000 | 734.38 |
| 313.15 | 0.1021 | 748.42 |
| 313.15 | 0.2015 | 763.25 |
| 313.15 | 0.3070 | 780.5 |
| 313.15 | 0.3998 | 797.07 |
| 313.15 | 0.4985 | 816.39 |
| 313.15 | 0.5961 | 837.52 |
| 313.15 | 0.7019 | 862.94 |
| 313.15 | 0.8012 | 889.71 |
| 313.15 | 0.8998 | 919.41 |
| 313.15 | 1.0000 | 953.66 |
| 323.15 | 0.0000 | 727.07 |
| 323.15 | 0.1021 | 741.07 |
| 323.15 | 0.2015 | 755.85 |
| 323.15 | 0.3070 | 773.06 |
| 323.15 | 0.3998 | 789.61 |
| 323.15 | 0.4985 | 808.85 |
| 323.15 | 0.5961 | 829.89 |
| 323.15 | 0.7019 | 855.26 |
| 323.15 | 0.8012 | 881.98 |
| 323.15 | 0.8998 | 911.58 |
| 323.15 | 1.0000 | 945.72 |
| 333.15 | 0.0000 | 719.73 |
| 333.15 | 0.1021 | 733.68 |
| 333.15 | 0.2015 | 748.42 |
| 333.15 | 0.3070 | 765.58 |
| 333.15 | 0.3998 | 782.08 |
| 333.15 | 0.4985 | 801.28 |
| 333.15 | 0.5961 | 822.25 |
| 333.15 | 0.7019 | 847.55 |
| 333.15 | 0.8012 | 874.21 |
| 333.15 | 0.8998 | 903.72 |
| 333.15 | 1.0000 | 937.77 |
| 343.15 | 0.0000 | 712.34 |
| 343.15 | 0.1021 | 726.25 |
| 343.15 | 0.2015 | 740.94 |
| 343.15 | 0.3070 | 758.06 |
| 343.15 | 0.3998 | 774.5 |
| 343.15 | 0.4985 | 793.67 |
| 343.15 | 0.5961 | 814.59 |
| 343.15 | 0.7019 | 839.81 |
| 343.15 | 0.8012 | 866.35 |
| 343.15 | 0.8998 | 895.83 |
| 343.15 | 1.0000 | 929.8 |
Mass density, kg/m3 [ref]
Operational condition: Mass fraction = 0.5 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 293.15 | 844.4 |
| 100.00 | 295.65 | 842.4 |
| 100.00 | 298.15 | 840.7 |
| 100.00 | 300.65 | 838.8 |
| 100.00 | 303.15 | 837.3 |
| 2000.00 | 293.15 | 845.7 |
| 2000.00 | 295.65 | 843.6 |
| 2000.00 | 298.15 | 842.0 |
| 2000.00 | 300.65 | 840.0 |
| 2000.00 | 303.15 | 838.5 |
| 4000.00 | 293.15 | 846.8 |
| 4000.00 | 295.65 | 844.9 |
| 4000.00 | 298.15 | 843.4 |
| 4000.00 | 300.65 | 841.3 |
| 4000.00 | 303.15 | 839.9 |
| 6000.00 | 293.15 | 848.0 |
| 6000.00 | 295.65 | 846.0 |
| 6000.00 | 298.15 | 844.7 |
| 6000.00 | 300.65 | 842.5 |
| 6000.00 | 303.15 | 841.1 |
| 8000.00 | 293.15 | 849.5 |
| 8000.00 | 295.65 | 847.4 |
| 8000.00 | 298.15 | 845.9 |
| 8000.00 | 300.65 | 843.8 |
| 8000.00 | 303.15 | 842.4 |
| 10000.00 | 293.15 | 850.8 |
| 10000.00 | 295.65 | 848.6 |
| 10000.00 | 298.15 | 847.1 |
| 10000.00 | 300.65 | 845.0 |
| 10000.00 | 303.15 | 843.6 |
| 12000.00 | 293.15 | 851.9 |
| 12000.00 | 295.65 | 849.8 |
| 12000.00 | 298.15 | 848.4 |
| 12000.00 | 300.65 | 846.3 |
| 12000.00 | 303.15 | 844.9 |
| 14000.00 | 293.15 | 853.1 |
| 14000.00 | 295.65 | 851.0 |
| 14000.00 | 298.15 | 849.5 |
| 14000.00 | 300.65 | 847.5 |
| 14000.00 | 303.15 | 846.1 |
| 16000.00 | 293.15 | 854.2 |
| 16000.00 | 295.65 | 852.1 |
| 16000.00 | 298.15 | 850.7 |
| 16000.00 | 300.65 | 848.8 |
| 16000.00 | 303.15 | 847.5 |
| 18000.00 | 293.15 | 855.4 |
| 18000.00 | 295.65 | 853.3 |
| 18000.00 | 298.15 | 851.9 |
| 18000.00 | 300.65 | 849.9 |
| 18000.00 | 303.15 | 848.7 |
| 20000.00 | 293.15 | 856.6 |
| 20000.00 | 295.65 | 854.4 |
| 20000.00 | 298.15 | 853.0 |
| 20000.00 | 300.65 | 851.0 |
| 20000.00 | 303.15 | 849.8 |
Mass density, kg/m3 [ref]
Operational condition: Temperature, K = 298.15 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Mass fraction of Naphthalene, 1,2,3,4-tetrahydro- (2) - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 0.4800 | 835.7 |
| 100.00 | 0.4900 | 838.4 |
| 100.00 | 0.5000 | 840.7 |
| 100.00 | 0.5100 | 842.7 |
| 100.00 | 0.5200 | 844.8 |
| 2000.00 | 0.4800 | 836.9 |
| 2000.00 | 0.4900 | 839.7 |
| 2000.00 | 0.5000 | 842.0 |
| 2000.00 | 0.5100 | 844.0 |
| 2000.00 | 0.5200 | 846.1 |
| 4000.00 | 0.4800 | 838.3 |
| 4000.00 | 0.4900 | 841.0 |
| 4000.00 | 0.5000 | 843.4 |
| 4000.00 | 0.5100 | 845.3 |
| 4000.00 | 0.5200 | 847.5 |
| 6000.00 | 0.4800 | 839.6 |
| 6000.00 | 0.4900 | 842.2 |
| 6000.00 | 0.5000 | 844.7 |
| 6000.00 | 0.5100 | 846.5 |
| 6000.00 | 0.5200 | 848.7 |
| 8000.00 | 0.4800 | 840.9 |
| 8000.00 | 0.4900 | 843.5 |
| 8000.00 | 0.5000 | 845.9 |
| 8000.00 | 0.5100 | 847.8 |
| 8000.00 | 0.5200 | 849.9 |
| 10000.00 | 0.4800 | 842.1 |
| 10000.00 | 0.4900 | 844.7 |
| 10000.00 | 0.5000 | 847.1 |
| 10000.00 | 0.5100 | 848.8 |
| 10000.00 | 0.5200 | 851.1 |
| 12000.00 | 0.4800 | 843.3 |
| 12000.00 | 0.4900 | 845.9 |
| 12000.00 | 0.5000 | 848.4 |
| 12000.00 | 0.5100 | 850.3 |
| 12000.00 | 0.5200 | 852.2 |
| 14000.00 | 0.4800 | 844.6 |
| 14000.00 | 0.4900 | 847.1 |
| 14000.00 | 0.5000 | 849.5 |
| 14000.00 | 0.5100 | 851.5 |
| 14000.00 | 0.5200 | 853.5 |
| 16000.00 | 0.4800 | 845.7 |
| 16000.00 | 0.4900 | 848.3 |
| 16000.00 | 0.5000 | 850.7 |
| 16000.00 | 0.5100 | 852.7 |
| 16000.00 | 0.5200 | 854.6 |
| 18000.00 | 0.4800 | 846.9 |
| 18000.00 | 0.4900 | 849.3 |
| 18000.00 | 0.5000 | 851.9 |
| 18000.00 | 0.5100 | 853.8 |
| 18000.00 | 0.5200 | 855.7 |
| 20000.00 | 0.4800 | 848.1 |
| 20000.00 | 0.4900 | 850.6 |
| 20000.00 | 0.5000 | 853.0 |
| 20000.00 | 0.5100 | 855.0 |
| 20000.00 | 0.5200 | 857.0 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Naphthalene, 1,2,3,4-tetrahydro- (2) - Liquid | Speed of sound, m/s - Liquid |
| 293.15 | 0.0000 | 1297.9 |
| 293.15 | 0.1021 | 1308.1 |
| 293.15 | 0.2015 | 1318.1 |
| 293.15 | 0.3070 | 1331.6 |
| 293.15 | 0.3998 | 1344.0 |
| 293.15 | 0.4985 | 1359.7 |
| 293.15 | 0.5961 | 1377.0 |
| 293.15 | 0.7019 | 1399.4 |
| 293.15 | 0.8012 | 1423.8 |
| 293.15 | 0.8998 | 1453.4 |
| 293.15 | 1.0000 | 1489.5 |
| 303.15 | 0.0000 | 1259.5 |
| 303.15 | 0.1021 | 1269.8 |
| 303.15 | 0.2015 | 1280.0 |
| 303.15 | 0.3070 | 1293.4 |
| 303.15 | 0.3998 | 1306.0 |
| 303.15 | 0.4985 | 1321.7 |
| 303.15 | 0.5961 | 1339.0 |
| 303.15 | 0.7019 | 1361.2 |
| 303.15 | 0.8012 | 1385.4 |
| 303.15 | 0.8998 | 1414.7 |
| 303.15 | 1.0000 | 1450.1 |
| 313.15 | 0.0000 | 1221.6 |
| 313.15 | 0.1021 | 1232.1 |
| 313.15 | 0.2015 | 1242.2 |
| 313.15 | 0.3070 | 1255.9 |
| 313.15 | 0.3998 | 1268.5 |
| 313.15 | 0.4985 | 1284.3 |
| 313.15 | 0.5961 | 1301.5 |
| 313.15 | 0.7019 | 1323.6 |
| 313.15 | 0.8012 | 1347.6 |
| 313.15 | 0.8998 | 1376.6 |
| 313.15 | 1.0000 | 1411.5 |
| 323.15 | 0.0000 | 1184.4 |
| 323.15 | 0.1021 | 1194.9 |
| 323.15 | 0.2015 | 1205.4 |
| 323.15 | 0.3070 | 1218.9 |
| 323.15 | 0.3998 | 1231.6 |
| 323.15 | 0.4985 | 1247.4 |
| 323.15 | 0.5961 | 1264.5 |
| 323.15 | 0.7019 | 1286.7 |
| 323.15 | 0.8012 | 1310.5 |
| 323.15 | 0.8998 | 1339.2 |
| 323.15 | 1.0000 | 1373.6 |
| 333.15 | 0.0000 | 1147.8 |
| 333.15 | 0.1021 | 1158.3 |
| 333.15 | 0.2015 | 1168.6 |
| 333.15 | 0.3070 | 1182.6 |
| 333.15 | 0.3998 | 1195.2 |
| 333.15 | 0.4985 | 1211.0 |
| 333.15 | 0.5961 | 1228.2 |
| 333.15 | 0.7019 | 1250.3 |
| 333.15 | 0.8012 | 1274.0 |
| 333.15 | 0.8998 | 1302.5 |
| 333.15 | 1.0000 | 1336.4 |
| 343.15 | 0.0000 | 1111.8 |
| 343.15 | 0.1021 | 1122.2 |
| 343.15 | 0.2015 | 1132.6 |
| 343.15 | 0.3070 | 1146.8 |
| 343.15 | 0.3998 | 1159.3 |
| 343.15 | 0.4985 | 1175.4 |
| 343.15 | 0.5961 | 1192.4 |
| 343.15 | 0.7019 | 1214.6 |
| 343.15 | 0.8012 | 1238.2 |
| 343.15 | 0.8998 | 1266.4 |
| 343.15 | 1.0000 | 1299.8 |
Binary diffusion coefficient, m2/s [ref]
| Fixed | Measured | ||
|---|---|---|---|
| Mass fraction of Naphthalene, 1,2,3,4-tetrahydro- (2) - Liquid | Pressure, kPa - Liquid | Temperature, K - Liquid | Binary diffusion coefficient, m2/s - Liquid |
| 0.5000 | 101.00 | 298.20 | 0.0000 |
Sources
- Thermodynamic modeling and experimental speeds of sound, densities, and refractive indexes of (tetralin + n-dodecane)
- Prediction and Experimental Measurement of Refractive Index in Ternary Hydrocarbon Mixtures
- Mass Diffusion Coefficient and Soret Coefficient of o-Dichlorobenzene Solutions of PCBM and [60]Fullerene by the Soret Forced Rayleigh Scattering Method
- Comparison between Experimental and Theoretical Estimations of the Thermal Expansion, Concentration Expansion Coefficients, and Viscosity for Binary Mixtures under Pressures up to 20 MPa
Note: These property values are available through the Cheméo API. A free account gives you an access key.