- 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
- Name
- Benzene, (2-methylpropyl)-
- InChI
- InChI=1S/C10H14/c1-9(2)8-10-6-4-3-5-7-10/h3-7,9H,8H2,1-2H3
- InChI Key
- KXUHSQYYJYAXGZ-UHFFFAOYSA-N
- Formula
- C10H14
- SMILES
- CC(C)Cc1ccccc1
- Mol. Weight (g/mol)
- 134.22
- CAS
- 538-93-2
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Datasets
- η - Viscosity, Pa*s
- Refractive index (other wavelength)
- ρl - Mass density, kg/m3 (2)
- 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 | 0.0013 |
| 4000.00 | 0.0014 |
| 10000.00 | 0.0014 |
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- (1) - Liquid | Wavelength, nm - Liquid | Refractive index (other wavelength) - Liquid |
| 293.15 | 0.1014 | 657.2 | 1.4875 |
| 293.15 | 0.2024 | 657.2 | 1.4925 |
| 293.15 | 0.3032 | 657.2 | 1.4985 |
| 293.15 | 0.4036 | 657.2 | 1.5038 |
| 293.15 | 0.5038 | 657.2 | 1.5097 |
| 293.15 | 0.6036 | 657.2 | 1.5139 |
| 293.15 | 0.7032 | 657.2 | 1.52 |
| 293.15 | 0.8024 | 657.2 | 1.5252 |
| 293.15 | 0.9014 | 657.2 | 1.5314 |
| 293.15 | 0.1014 | 633.2 | 1.4889 |
| 293.15 | 0.2024 | 633.2 | 1.4938 |
| 293.15 | 0.3032 | 633.2 | 1.4992 |
| 293.15 | 0.4036 | 633.2 | 1.5045 |
| 293.15 | 0.5038 | 633.2 | 1.5098 |
| 293.15 | 0.6036 | 633.2 | 1.5153 |
| 293.15 | 0.7032 | 633.2 | 1.5209 |
| 293.15 | 0.8024 | 633.2 | 1.5266 |
| 293.15 | 0.9014 | 633.2 | 1.5323 |
| 293.15 | 0.1014 | 589.3 | 1.4914 |
| 293.15 | 0.2024 | 589.3 | 1.4966 |
| 293.15 | 0.3032 | 589.3 | 1.502 |
| 293.15 | 0.4036 | 589.3 | 1.507 |
| 293.15 | 0.5038 | 589.3 | 1.5127 |
| 293.15 | 0.6036 | 589.3 | 1.5182 |
| 293.15 | 0.7032 | 589.3 | 1.5238 |
| 293.15 | 0.8024 | 589.3 | 1.5296 |
| 293.15 | 0.9014 | 589.3 | 1.5353 |
| 293.15 | 0.1014 | 513.9 | 1.4981 |
| 293.15 | 0.2024 | 513.9 | 1.5032 |
| 293.15 | 0.3032 | 513.9 | 1.5087 |
| 293.15 | 0.4036 | 513.9 | 1.5141 |
| 293.15 | 0.5038 | 513.9 | 1.5196 |
| 293.15 | 0.6036 | 513.9 | 1.5252 |
| 293.15 | 0.7032 | 513.9 | 1.531 |
| 293.15 | 0.8024 | 513.9 | 1.5369 |
| 293.15 | 0.9014 | 513.9 | 1.5427 |
| 293.15 | 0.1014 | 436.1 | 1.5098 |
| 293.15 | 0.2024 | 436.1 | 1.515 |
| 293.15 | 0.3032 | 436.1 | 1.5208 |
| 293.15 | 0.4036 | 436.1 | 1.5261 |
| 293.15 | 0.5038 | 436.1 | 1.5321 |
| 293.15 | 0.6036 | 436.1 | 1.538 |
| 293.15 | 0.7032 | 436.1 | 1.5439 |
| 293.15 | 0.8024 | 436.1 | 1.5501 |
| 293.15 | 0.9014 | 436.1 | 1.5561 |
| 298.15 | 0.1014 | 657.2 | 1.4851 |
| 298.15 | 0.2024 | 657.2 | 1.4903 |
| 298.15 | 0.3032 | 657.2 | 1.4959 |
| 298.15 | 0.4036 | 657.2 | 1.5013 |
| 298.15 | 0.5038 | 657.2 | 1.5071 |
| 298.15 | 0.6036 | 657.2 | 1.512 |
| 298.15 | 0.7032 | 657.2 | 1.5178 |
| 298.15 | 0.8024 | 657.2 | 1.523 |
| 298.15 | 0.9014 | 657.2 | 1.5294 |
| 298.15 | 0.1014 | 633.2 | 1.4863 |
| 298.15 | 0.2024 | 633.2 | 1.4915 |
| 298.15 | 0.3032 | 633.2 | 1.4968 |
| 298.15 | 0.4036 | 633.2 | 1.5021 |
| 298.15 | 0.5038 | 633.2 | 1.5074 |
| 298.15 | 0.6036 | 633.2 | 1.513 |
| 298.15 | 0.7032 | 633.2 | 1.5185 |
| 298.15 | 0.8024 | 633.2 | 1.5242 |
| 298.15 | 0.9014 | 633.2 | 1.5298 |
| 298.15 | 0.1014 | 589.3 | 1.4893 |
| 298.15 | 0.2024 | 589.3 | 1.4943 |
| 298.15 | 0.3032 | 589.3 | 1.4996 |
| 298.15 | 0.4036 | 589.3 | 1.5045 |
| 298.15 | 0.5038 | 589.3 | 1.5102 |
| 298.15 | 0.6036 | 589.3 | 1.5159 |
| 298.15 | 0.7032 | 589.3 | 1.5215 |
| 298.15 | 0.8024 | 589.3 | 1.5272 |
| 298.15 | 0.9014 | 589.3 | 1.5329 |
| 298.15 | 0.1014 | 513.9 | 1.4955 |
| 298.15 | 0.2024 | 513.9 | 1.5008 |
| 298.15 | 0.3032 | 513.9 | 1.5062 |
| 298.15 | 0.4036 | 513.9 | 1.5116 |
| 298.15 | 0.5038 | 513.9 | 1.5171 |
| 298.15 | 0.6036 | 513.9 | 1.5229 |
| 298.15 | 0.7032 | 513.9 | 1.5286 |
| 298.15 | 0.8024 | 513.9 | 1.5345 |
| 298.15 | 0.9014 | 513.9 | 1.5402 |
| 298.15 | 0.1014 | 436.1 | 1.5072 |
| 298.15 | 0.2024 | 436.1 | 1.5125 |
| 298.15 | 0.3032 | 436.1 | 1.5182 |
| 298.15 | 0.4036 | 436.1 | 1.5236 |
| 298.15 | 0.5038 | 436.1 | 1.5295 |
| 298.15 | 0.6036 | 436.1 | 1.5355 |
| 298.15 | 0.7032 | 436.1 | 1.5414 |
| 298.15 | 0.8024 | 436.1 | 1.5476 |
| 298.15 | 0.9014 | 436.1 | 1.5535 |
| 303.15 | 0.1014 | 657.2 | 1.4828 |
| 303.15 | 0.2024 | 657.2 | 1.4879 |
| 303.15 | 0.3032 | 657.2 | 1.4933 |
| 303.15 | 0.4036 | 657.2 | 1.4989 |
| 303.15 | 0.5038 | 657.2 | 1.5046 |
| 303.15 | 0.6036 | 657.2 | 1.5098 |
| 303.15 | 0.7032 | 657.2 | 1.5153 |
| 303.15 | 0.8024 | 657.2 | 1.5204 |
| 303.15 | 0.9014 | 657.2 | 1.5267 |
| 303.15 | 0.1014 | 633.2 | 1.4841 |
| 303.15 | 0.2024 | 633.2 | 1.4889 |
| 303.15 | 0.3032 | 633.2 | 1.4944 |
| 303.15 | 0.4036 | 633.2 | 1.4993 |
| 303.15 | 0.5038 | 633.2 | 1.5049 |
| 303.15 | 0.6036 | 633.2 | 1.5104 |
| 303.15 | 0.7032 | 633.2 | 1.516 |
| 303.15 | 0.8024 | 633.2 | 1.5218 |
| 303.15 | 0.9014 | 633.2 | 1.5275 |
| 303.15 | 0.1014 | 589.3 | 1.4867 |
| 303.15 | 0.2024 | 589.3 | 1.4916 |
| 303.15 | 0.3032 | 589.3 | 1.4971 |
| 303.15 | 0.4036 | 589.3 | 1.5021 |
| 303.15 | 0.5038 | 589.3 | 1.5078 |
| 303.15 | 0.6036 | 589.3 | 1.5135 |
| 303.15 | 0.7032 | 589.3 | 1.519 |
| 303.15 | 0.8024 | 589.3 | 1.5248 |
| 303.15 | 0.9014 | 589.3 | 1.5305 |
| 303.15 | 0.1014 | 513.9 | 1.4931 |
| 303.15 | 0.2024 | 513.9 | 1.4983 |
| 303.15 | 0.3032 | 513.9 | 1.5038 |
| 303.15 | 0.4036 | 513.9 | 1.509 |
| 303.15 | 0.5038 | 513.9 | 1.5146 |
| 303.15 | 0.6036 | 513.9 | 1.5203 |
| 303.15 | 0.7032 | 513.9 | 1.5261 |
| 303.15 | 0.8024 | 513.9 | 1.532 |
| 303.15 | 0.9014 | 513.9 | 1.5378 |
| 303.15 | 0.1014 | 436.1 | 1.5047 |
| 303.15 | 0.2024 | 436.1 | 1.5099 |
| 303.15 | 0.3032 | 436.1 | 1.5157 |
| 303.15 | 0.4036 | 436.1 | 1.5209 |
| 303.15 | 0.5038 | 436.1 | 1.5267 |
| 303.15 | 0.6036 | 436.1 | 1.5331 |
| 303.15 | 0.7032 | 436.1 | 1.5389 |
| 303.15 | 0.8024 | 436.1 | 1.545 |
| 303.15 | 0.9014 | 436.1 | 1.5511 |
| 308.15 | 0.1014 | 657.2 | 1.4804 |
| 308.15 | 0.2024 | 657.2 | 1.4854 |
| 308.15 | 0.3032 | 657.2 | 1.4909 |
| 308.15 | 0.4036 | 657.2 | 1.4967 |
| 308.15 | 0.5038 | 657.2 | 1.5022 |
| 308.15 | 0.6036 | 657.2 | 1.5074 |
| 308.15 | 0.7032 | 657.2 | 1.5127 |
| 308.15 | 0.8024 | 657.2 | 1.5183 |
| 308.15 | 0.9014 | 657.2 | 1.5245 |
| 308.15 | 0.1014 | 633.2 | 1.4814 |
| 308.15 | 0.2024 | 633.2 | 1.4866 |
| 308.15 | 0.3032 | 633.2 | 1.4917 |
| 308.15 | 0.4036 | 633.2 | 1.497 |
| 308.15 | 0.5038 | 633.2 | 1.5022 |
| 308.15 | 0.6036 | 633.2 | 1.5081 |
| 308.15 | 0.7032 | 633.2 | 1.5137 |
| 308.15 | 0.8024 | 633.2 | 1.5194 |
| 308.15 | 0.9014 | 633.2 | 1.5248 |
| 308.15 | 0.1014 | 589.3 | 1.4843 |
| 308.15 | 0.2024 | 589.3 | 1.4894 |
| 308.15 | 0.3032 | 589.3 | 1.4946 |
| 308.15 | 0.4036 | 589.3 | 1.4995 |
| 308.15 | 0.5038 | 589.3 | 1.5051 |
| 308.15 | 0.6036 | 589.3 | 1.511 |
| 308.15 | 0.7032 | 589.3 | 1.5166 |
| 308.15 | 0.8024 | 589.3 | 1.5224 |
| 308.15 | 0.9014 | 589.3 | 1.528 |
| 308.15 | 0.1014 | 513.9 | 1.4905 |
| 308.15 | 0.2024 | 513.9 | 1.4959 |
| 308.15 | 0.3032 | 513.9 | 1.501 |
| 308.15 | 0.4036 | 513.9 | 1.5067 |
| 308.15 | 0.5038 | 513.9 | 1.5122 |
| 308.15 | 0.6036 | 513.9 | 1.5176 |
| 308.15 | 0.7032 | 513.9 | 1.5237 |
| 308.15 | 0.8024 | 513.9 | 1.5295 |
| 308.15 | 0.9014 | 513.9 | 1.5351 |
| 308.15 | 0.1014 | 436.1 | 1.502 |
| 308.15 | 0.2024 | 436.1 | 1.5076 |
| 308.15 | 0.3032 | 436.1 | 1.5129 |
| 308.15 | 0.4036 | 436.1 | 1.5188 |
| 308.15 | 0.5038 | 436.1 | 1.5241 |
| 308.15 | 0.6036 | 436.1 | 1.5304 |
| 308.15 | 0.7032 | 436.1 | 1.5364 |
| 308.15 | 0.8024 | 436.1 | 1.5425 |
| 308.15 | 0.9014 | 436.1 | 1.5482 |
| 313.15 | 0.1014 | 657.2 | 1.4781 |
| 313.15 | 0.2024 | 657.2 | 1.4831 |
| 313.15 | 0.3032 | 657.2 | 1.4887 |
| 313.15 | 0.4036 | 657.2 | 1.4942 |
| 313.15 | 0.5038 | 657.2 | 1.4995 |
| 313.15 | 0.6036 | 657.2 | 1.5049 |
| 313.15 | 0.7032 | 657.2 | 1.5103 |
| 313.15 | 0.8024 | 657.2 | 1.5157 |
| 313.15 | 0.9014 | 657.2 | 1.5217 |
| 313.15 | 0.1014 | 633.2 | 1.4792 |
| 313.15 | 0.2024 | 633.2 | 1.4841 |
| 313.15 | 0.3032 | 633.2 | 1.4896 |
| 313.15 | 0.4036 | 633.2 | 1.4942 |
| 313.15 | 0.5038 | 633.2 | 1.4996 |
| 313.15 | 0.6036 | 633.2 | 1.5054 |
| 313.15 | 0.7032 | 633.2 | 1.5113 |
| 313.15 | 0.8024 | 633.2 | 1.5171 |
| 313.15 | 0.9014 | 633.2 | 1.5225 |
| 313.15 | 0.1014 | 589.3 | 1.482 |
| 313.15 | 0.2024 | 589.3 | 1.487 |
| 313.15 | 0.3032 | 589.3 | 1.4922 |
| 313.15 | 0.4036 | 589.3 | 1.497 |
| 313.15 | 0.5038 | 589.3 | 1.5026 |
| 313.15 | 0.6036 | 589.3 | 1.5085 |
| 313.15 | 0.7032 | 589.3 | 1.5142 |
| 313.15 | 0.8024 | 589.3 | 1.52 |
| 313.15 | 0.9014 | 589.3 | 1.5256 |
| 313.15 | 0.1014 | 513.9 | 1.4882 |
| 313.15 | 0.2024 | 513.9 | 1.4932 |
| 313.15 | 0.3032 | 513.9 | 1.4989 |
| 313.15 | 0.4036 | 513.9 | 1.5041 |
| 313.15 | 0.5038 | 513.9 | 1.5098 |
| 313.15 | 0.6036 | 513.9 | 1.5151 |
| 313.15 | 0.7032 | 513.9 | 1.5212 |
| 313.15 | 0.8024 | 513.9 | 1.5272 |
| 313.15 | 0.9014 | 513.9 | 1.5326 |
| 313.15 | 0.1014 | 436.1 | 1.4996 |
| 313.15 | 0.2024 | 436.1 | 1.5048 |
| 313.15 | 0.3032 | 436.1 | 1.5104 |
| 313.15 | 0.4036 | 436.1 | 1.5163 |
| 313.15 | 0.5038 | 436.1 | 1.5215 |
| 313.15 | 0.6036 | 436.1 | 1.5281 |
| 313.15 | 0.7032 | 436.1 | 1.5339 |
| 313.15 | 0.8024 | 436.1 | 1.54 |
| 313.15 | 0.9014 | 436.1 | 1.5457 |
| 318.15 | 0.1014 | 657.2 | 1.4756 |
| 318.15 | 0.2024 | 657.2 | 1.4806 |
| 318.15 | 0.3032 | 657.2 | 1.486 |
| 318.15 | 0.4036 | 657.2 | 1.4918 |
| 318.15 | 0.5038 | 657.2 | 1.4969 |
| 318.15 | 0.6036 | 657.2 | 1.5022 |
| 318.15 | 0.7032 | 657.2 | 1.5076 |
| 318.15 | 0.8024 | 657.2 | 1.5139 |
| 318.15 | 0.9014 | 657.2 | 1.519 |
| 318.15 | 0.1014 | 633.2 | 1.4766 |
| 318.15 | 0.2024 | 633.2 | 1.4818 |
| 318.15 | 0.3032 | 633.2 | 1.4869 |
| 318.15 | 0.4036 | 633.2 | 1.4918 |
| 318.15 | 0.5038 | 633.2 | 1.4972 |
| 318.15 | 0.6036 | 633.2 | 1.5032 |
| 318.15 | 0.7032 | 633.2 | 1.5089 |
| 318.15 | 0.8024 | 633.2 | 1.5146 |
| 318.15 | 0.9014 | 633.2 | 1.5199 |
| 318.15 | 0.1014 | 589.3 | 1.4795 |
| 318.15 | 0.2024 | 589.3 | 1.4846 |
| 318.15 | 0.3032 | 589.3 | 1.4896 |
| 318.15 | 0.4036 | 589.3 | 1.4946 |
| 318.15 | 0.5038 | 589.3 | 1.4999 |
| 318.15 | 0.6036 | 589.3 | 1.5061 |
| 318.15 | 0.7032 | 589.3 | 1.5117 |
| 318.15 | 0.8024 | 589.3 | 1.5176 |
| 318.15 | 0.9014 | 589.3 | 1.5229 |
| 318.15 | 0.1014 | 513.9 | 1.4856 |
| 318.15 | 0.2024 | 513.9 | 1.4908 |
| 318.15 | 0.3032 | 513.9 | 1.4961 |
| 318.15 | 0.4036 | 513.9 | 1.5014 |
| 318.15 | 0.5038 | 513.9 | 1.5075 |
| 318.15 | 0.6036 | 513.9 | 1.513 |
| 318.15 | 0.7032 | 513.9 | 1.5189 |
| 318.15 | 0.8024 | 513.9 | 1.5247 |
| 318.15 | 0.9014 | 513.9 | 1.5301 |
| 318.15 | 0.1014 | 436.1 | 1.4968 |
| 318.15 | 0.2024 | 436.1 | 1.5025 |
| 318.15 | 0.3032 | 436.1 | 1.5078 |
| 318.15 | 0.4036 | 436.1 | 1.5137 |
| 318.15 | 0.5038 | 436.1 | 1.519 |
| 318.15 | 0.6036 | 436.1 | 1.5253 |
| 318.15 | 0.7032 | 436.1 | 1.5312 |
| 318.15 | 0.8024 | 436.1 | 1.5375 |
| 318.15 | 0.9014 | 436.1 | 1.543 |
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 | 907.9 |
| 100.00 | 295.65 | 905.7 |
| 100.00 | 298.15 | 903.6 |
| 100.00 | 300.65 | 901.5 |
| 100.00 | 303.15 | 900.0 |
| 2000.00 | 293.15 | 909.1 |
| 2000.00 | 295.65 | 906.8 |
| 2000.00 | 298.15 | 904.7 |
| 2000.00 | 300.65 | 902.9 |
| 2000.00 | 303.15 | 901.3 |
| 4000.00 | 293.15 | 910.3 |
| 4000.00 | 295.65 | 908.1 |
| 4000.00 | 298.15 | 906.1 |
| 4000.00 | 300.65 | 904.2 |
| 4000.00 | 303.15 | 902.6 |
| 6000.00 | 293.15 | 911.6 |
| 6000.00 | 295.65 | 909.3 |
| 6000.00 | 298.15 | 907.5 |
| 6000.00 | 300.65 | 905.4 |
| 6000.00 | 303.15 | 904.0 |
| 8000.00 | 293.15 | 913.0 |
| 8000.00 | 295.65 | 910.6 |
| 8000.00 | 298.15 | 908.8 |
| 8000.00 | 300.65 | 906.8 |
| 8000.00 | 303.15 | 905.3 |
| 10000.00 | 293.15 | 914.3 |
| 10000.00 | 295.65 | 911.9 |
| 10000.00 | 298.15 | 910.1 |
| 10000.00 | 300.65 | 908.0 |
| 10000.00 | 303.15 | 906.5 |
| 12000.00 | 293.15 | 915.4 |
| 12000.00 | 295.65 | 913.1 |
| 12000.00 | 298.15 | 911.3 |
| 12000.00 | 300.65 | 909.2 |
| 12000.00 | 303.15 | 907.8 |
| 14000.00 | 293.15 | 916.6 |
| 14000.00 | 295.65 | 914.3 |
| 14000.00 | 298.15 | 912.5 |
| 14000.00 | 300.65 | 910.4 |
| 14000.00 | 303.15 | 909.0 |
| 16000.00 | 293.15 | 917.7 |
| 16000.00 | 295.65 | 915.4 |
| 16000.00 | 298.15 | 913.7 |
| 16000.00 | 300.65 | 911.6 |
| 16000.00 | 303.15 | 910.3 |
| 18000.00 | 293.15 | 918.8 |
| 18000.00 | 295.65 | 916.6 |
| 18000.00 | 298.15 | 914.9 |
| 18000.00 | 300.65 | 912.8 |
| 18000.00 | 303.15 | 911.4 |
| 20000.00 | 293.15 | 920.1 |
| 20000.00 | 295.65 | 917.7 |
| 20000.00 | 298.15 | 916.1 |
| 20000.00 | 300.65 | 914.0 |
| 20000.00 | 303.15 | 912.6 |
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- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 0.4800 | 901.3 |
| 100.00 | 0.4900 | 902.5 |
| 100.00 | 0.5000 | 903.6 |
| 100.00 | 0.5100 | 905.0 |
| 100.00 | 0.5200 | 906.0 |
| 2000.00 | 0.4800 | 902.6 |
| 2000.00 | 0.4900 | 903.8 |
| 2000.00 | 0.5000 | 904.7 |
| 2000.00 | 0.5100 | 906.2 |
| 2000.00 | 0.5200 | 907.3 |
| 4000.00 | 0.4800 | 904.0 |
| 4000.00 | 0.4900 | 905.1 |
| 4000.00 | 0.5000 | 906.1 |
| 4000.00 | 0.5100 | 907.6 |
| 4000.00 | 0.5200 | 908.8 |
| 6000.00 | 0.4800 | 905.3 |
| 6000.00 | 0.4900 | 906.4 |
| 6000.00 | 0.5000 | 907.5 |
| 6000.00 | 0.5100 | 908.8 |
| 6000.00 | 0.5200 | 910.0 |
| 8000.00 | 0.4800 | 906.6 |
| 8000.00 | 0.4900 | 907.7 |
| 8000.00 | 0.5000 | 908.8 |
| 8000.00 | 0.5100 | 910.1 |
| 8000.00 | 0.5200 | 911.2 |
| 10000.00 | 0.4800 | 907.8 |
| 10000.00 | 0.4900 | 909.0 |
| 10000.00 | 0.5000 | 910.1 |
| 10000.00 | 0.5100 | 911.2 |
| 10000.00 | 0.5200 | 912.4 |
| 12000.00 | 0.4800 | 909.0 |
| 12000.00 | 0.4900 | 910.2 |
| 12000.00 | 0.5000 | 911.3 |
| 12000.00 | 0.5100 | 912.5 |
| 12000.00 | 0.5200 | 913.6 |
| 14000.00 | 0.4800 | 910.2 |
| 14000.00 | 0.4900 | 911.5 |
| 14000.00 | 0.5000 | 912.5 |
| 14000.00 | 0.5100 | 913.7 |
| 14000.00 | 0.5200 | 914.8 |
| 16000.00 | 0.4800 | 911.4 |
| 16000.00 | 0.4900 | 912.6 |
| 16000.00 | 0.5000 | 913.7 |
| 16000.00 | 0.5100 | 915.0 |
| 16000.00 | 0.5200 | 916.0 |
| 18000.00 | 0.4800 | 912.6 |
| 18000.00 | 0.4900 | 913.7 |
| 18000.00 | 0.5000 | 914.9 |
| 18000.00 | 0.5100 | 916.1 |
| 18000.00 | 0.5200 | 917.1 |
| 20000.00 | 0.4800 | 913.8 |
| 20000.00 | 0.4900 | 914.9 |
| 20000.00 | 0.5000 | 916.1 |
| 20000.00 | 0.5100 | 917.2 |
| 20000.00 | 0.5200 | 918.2 |
Binary diffusion coefficient, m2/s [ref]
| Fixed | Measured | ||
|---|---|---|---|
| Mass fraction of Naphthalene, 1,2,3,4-tetrahydro- (1) - Liquid | Pressure, kPa - Liquid | Temperature, K - Liquid | Binary diffusion coefficient, m2/s - Liquid |
| 0.5000 | 101.00 | 298.20 | 0.0000 |
Sources
- 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.