Datasets
-
Mole fraction (2)
-
η - Viscosity, Pa*s (2)
-
n0 - Refractive index (Na D-line) (2)
-
ρl - Mass density, kg/m3 (2)
-
csound,fluid - Speed of Sound, m/s (4)
-
Tboil - Boiling temperature at pressure P, K (2)
Mole fraction of 1,4-Dioxane (2)
[ref]
| Fixed |
Measured |
| Mole fraction of 1,4-Dioxane (2) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of 1,4-Dioxane (2) - Gas |
| 0.0481 |
101.30 |
0.0274 |
| 0.0516 |
66.60 |
0.0291 |
| 0.0527 |
40.00 |
0.0265 |
| 0.1135 |
101.30 |
0.0658 |
| 0.1141 |
40.00 |
0.0562 |
| 0.1166 |
66.60 |
0.0640 |
| 0.2051 |
101.30 |
0.1248 |
| 0.2169 |
66.60 |
0.1236 |
| 0.2190 |
40.00 |
0.1209 |
| 0.3043 |
40.00 |
0.1714 |
| 0.3129 |
66.60 |
0.1861 |
| 0.3149 |
101.30 |
0.1969 |
| 0.4085 |
40.00 |
0.2459 |
| 0.4150 |
101.30 |
0.2754 |
| 0.4209 |
66.60 |
0.2643 |
| 0.5008 |
101.30 |
0.3461 |
| 0.5137 |
66.60 |
0.3420 |
| 0.5191 |
40.00 |
0.3385 |
| 0.5990 |
40.00 |
0.4112 |
| 0.6086 |
66.60 |
0.4339 |
| 0.6106 |
101.30 |
0.4450 |
| 0.7002 |
40.00 |
0.5204 |
| 0.7083 |
101.30 |
0.5459 |
| 0.7093 |
66.60 |
0.5394 |
| 0.7973 |
101.30 |
0.6596 |
| 0.8016 |
66.60 |
0.6589 |
| 0.8106 |
40.00 |
0.6621 |
| 0.8839 |
66.60 |
0.7827 |
| 0.8868 |
101.30 |
0.7976 |
| 0.8925 |
40.00 |
0.7793 |
| 0.9217 |
101.30 |
0.8645 |
| 0.9368 |
66.60 |
0.8740 |
| 0.9404 |
40.00 |
0.8772 |
Mole fraction of 1,4-Dioxane (2)
[ref]
| Fixed |
Measured |
| Mole fraction of 1,4-Dioxane (2) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of 1,4-Dioxane (2) - Gas |
| 0.0481 |
101.30 |
0.0274 |
| 0.0516 |
66.60 |
0.0291 |
| 0.0527 |
40.00 |
0.0265 |
| 0.1135 |
101.30 |
0.0658 |
| 0.1141 |
40.00 |
0.0562 |
| 0.1166 |
66.60 |
0.0640 |
| 0.2051 |
101.30 |
0.1248 |
| 0.2169 |
66.60 |
0.1236 |
| 0.2190 |
40.00 |
0.1209 |
| 0.3043 |
40.00 |
0.1714 |
| 0.3129 |
66.60 |
0.1861 |
| 0.3149 |
101.30 |
0.1969 |
| 0.4085 |
40.00 |
0.2459 |
| 0.4150 |
101.30 |
0.2754 |
| 0.4209 |
66.60 |
0.2643 |
| 0.5008 |
101.30 |
0.3461 |
| 0.5137 |
66.60 |
0.3420 |
| 0.5191 |
40.00 |
0.3385 |
| 0.5990 |
40.00 |
0.4112 |
| 0.6086 |
66.60 |
0.4339 |
| 0.6106 |
101.30 |
0.4450 |
| 0.7002 |
40.00 |
0.5204 |
| 0.7083 |
101.30 |
0.5459 |
| 0.7093 |
66.60 |
0.5394 |
| 0.7973 |
101.30 |
0.6596 |
| 0.8016 |
66.60 |
0.6589 |
| 0.8106 |
40.00 |
0.6621 |
| 0.8839 |
66.60 |
0.7827 |
| 0.8868 |
101.30 |
0.7976 |
| 0.8925 |
40.00 |
0.7793 |
| 0.9217 |
101.30 |
0.8645 |
| 0.9368 |
66.60 |
0.8740 |
| 0.9404 |
40.00 |
0.8772 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 1,4-Dioxane (2) - Liquid |
Viscosity, Pa*s - Liquid |
| 293.15 |
0.0000 |
0.0006 |
| 293.15 |
0.0713 |
0.0007 |
| 293.15 |
0.1403 |
0.0007 |
| 293.15 |
0.2123 |
0.0008 |
| 293.15 |
0.2809 |
0.0008 |
| 293.15 |
0.3528 |
0.0009 |
| 293.15 |
0.4195 |
0.0009 |
| 293.15 |
0.5037 |
0.0010 |
| 293.15 |
0.5800 |
0.0010 |
| 293.15 |
0.6504 |
0.0011 |
| 293.15 |
0.7197 |
0.0011 |
| 293.15 |
0.7822 |
0.0012 |
| 293.15 |
0.8561 |
0.0012 |
| 293.15 |
0.9287 |
0.0013 |
| 293.15 |
1.0000 |
0.0013 |
| 298.15 |
0.0000 |
0.0006 |
| 298.15 |
0.0713 |
0.0006 |
| 298.15 |
0.1403 |
0.0007 |
| 298.15 |
0.2123 |
0.0007 |
| 298.15 |
0.2809 |
0.0008 |
| 298.15 |
0.3528 |
0.0008 |
| 298.15 |
0.4195 |
0.0009 |
| 298.15 |
0.5037 |
0.0009 |
| 298.15 |
0.5800 |
0.0010 |
| 298.15 |
0.6504 |
0.0010 |
| 298.15 |
0.7197 |
0.0010 |
| 298.15 |
0.7822 |
0.0011 |
| 298.15 |
0.8561 |
0.0011 |
| 298.15 |
0.9287 |
0.0012 |
| 298.15 |
1.0000 |
0.0012 |
| 303.15 |
0.0000 |
0.0006 |
| 303.15 |
0.0713 |
0.0006 |
| 303.15 |
0.1403 |
0.0006 |
| 303.15 |
0.2123 |
0.0007 |
| 303.15 |
0.2809 |
0.0007 |
| 303.15 |
0.3528 |
0.0008 |
| 303.15 |
0.4195 |
0.0008 |
| 303.15 |
0.5037 |
0.0008 |
| 303.15 |
0.5800 |
0.0009 |
| 303.15 |
0.6504 |
0.0009 |
| 303.15 |
0.7197 |
0.0010 |
| 303.15 |
0.7822 |
0.0010 |
| 303.15 |
0.8561 |
0.0010 |
| 303.15 |
0.9287 |
0.0011 |
| 303.15 |
1.0000 |
0.0011 |
| 308.15 |
0.0000 |
0.0005 |
| 308.15 |
0.0713 |
0.0006 |
| 308.15 |
0.1403 |
0.0006 |
| 308.15 |
0.2123 |
0.0006 |
| 308.15 |
0.2809 |
0.0007 |
| 308.15 |
0.3528 |
0.0007 |
| 308.15 |
0.4195 |
0.0007 |
| 308.15 |
0.5037 |
0.0008 |
| 308.15 |
0.5800 |
0.0008 |
| 308.15 |
0.6504 |
0.0009 |
| 308.15 |
0.7197 |
0.0009 |
| 308.15 |
0.7822 |
0.0009 |
| 308.15 |
0.8561 |
0.0009 |
| 308.15 |
0.9287 |
0.0010 |
| 308.15 |
1.0000 |
0.0010 |
| 313.15 |
0.0000 |
0.0005 |
| 313.15 |
0.0713 |
0.0005 |
| 313.15 |
0.1403 |
0.0006 |
| 313.15 |
0.2123 |
0.0006 |
| 313.15 |
0.2809 |
0.0006 |
| 313.15 |
0.3528 |
0.0007 |
| 313.15 |
0.4195 |
0.0007 |
| 313.15 |
0.5037 |
0.0007 |
| 313.15 |
0.5800 |
0.0008 |
| 313.15 |
0.6504 |
0.0008 |
| 313.15 |
0.7197 |
0.0008 |
| 313.15 |
0.7822 |
0.0009 |
| 313.15 |
0.8561 |
0.0009 |
| 313.15 |
0.9287 |
0.0009 |
| 313.15 |
1.0000 |
0.0009 |
| 318.15 |
0.0000 |
0.0005 |
| 318.15 |
0.0713 |
0.0005 |
| 318.15 |
0.1403 |
0.0005 |
| 318.15 |
0.2123 |
0.0006 |
| 318.15 |
0.2809 |
0.0006 |
| 318.15 |
0.3528 |
0.0006 |
| 318.15 |
0.4195 |
0.0006 |
| 318.15 |
0.5037 |
0.0007 |
| 318.15 |
0.5800 |
0.0007 |
| 318.15 |
0.6504 |
0.0007 |
| 318.15 |
0.7197 |
0.0008 |
| 318.15 |
0.7822 |
0.0008 |
| 318.15 |
0.8561 |
0.0008 |
| 318.15 |
0.9287 |
0.0009 |
| 318.15 |
1.0000 |
0.0009 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 1,4-Dioxane (2) - Liquid |
Viscosity, Pa*s - Liquid |
| 293.15 |
0.0000 |
0.0006 |
| 293.15 |
0.0713 |
0.0007 |
| 293.15 |
0.1403 |
0.0007 |
| 293.15 |
0.2123 |
0.0008 |
| 293.15 |
0.2809 |
0.0008 |
| 293.15 |
0.3528 |
0.0009 |
| 293.15 |
0.4195 |
0.0009 |
| 293.15 |
0.5037 |
0.0010 |
| 293.15 |
0.5800 |
0.0010 |
| 293.15 |
0.6504 |
0.0011 |
| 293.15 |
0.7197 |
0.0011 |
| 293.15 |
0.7822 |
0.0012 |
| 293.15 |
0.8561 |
0.0012 |
| 293.15 |
0.9287 |
0.0013 |
| 293.15 |
1.0000 |
0.0013 |
| 298.15 |
0.0000 |
0.0006 |
| 298.15 |
0.0713 |
0.0006 |
| 298.15 |
0.1403 |
0.0007 |
| 298.15 |
0.2123 |
0.0007 |
| 298.15 |
0.2809 |
0.0008 |
| 298.15 |
0.3528 |
0.0008 |
| 298.15 |
0.4195 |
0.0009 |
| 298.15 |
0.5037 |
0.0009 |
| 298.15 |
0.5800 |
0.0010 |
| 298.15 |
0.6504 |
0.0010 |
| 298.15 |
0.7197 |
0.0010 |
| 298.15 |
0.7822 |
0.0011 |
| 298.15 |
0.8561 |
0.0011 |
| 298.15 |
0.9287 |
0.0012 |
| 298.15 |
1.0000 |
0.0012 |
| 303.15 |
0.0000 |
0.0006 |
| 303.15 |
0.0713 |
0.0006 |
| 303.15 |
0.1403 |
0.0006 |
| 303.15 |
0.2123 |
0.0007 |
| 303.15 |
0.2809 |
0.0007 |
| 303.15 |
0.3528 |
0.0008 |
| 303.15 |
0.4195 |
0.0008 |
| 303.15 |
0.5037 |
0.0008 |
| 303.15 |
0.5800 |
0.0009 |
| 303.15 |
0.6504 |
0.0009 |
| 303.15 |
0.7197 |
0.0010 |
| 303.15 |
0.7822 |
0.0010 |
| 303.15 |
0.8561 |
0.0010 |
| 303.15 |
0.9287 |
0.0011 |
| 303.15 |
1.0000 |
0.0011 |
| 308.15 |
0.0000 |
0.0005 |
| 308.15 |
0.0713 |
0.0006 |
| 308.15 |
0.1403 |
0.0006 |
| 308.15 |
0.2123 |
0.0006 |
| 308.15 |
0.2809 |
0.0007 |
| 308.15 |
0.3528 |
0.0007 |
| 308.15 |
0.4195 |
0.0007 |
| 308.15 |
0.5037 |
0.0008 |
| 308.15 |
0.5800 |
0.0008 |
| 308.15 |
0.6504 |
0.0009 |
| 308.15 |
0.7197 |
0.0009 |
| 308.15 |
0.7822 |
0.0009 |
| 308.15 |
0.8561 |
0.0009 |
| 308.15 |
0.9287 |
0.0010 |
| 308.15 |
1.0000 |
0.0010 |
| 313.15 |
0.0000 |
0.0005 |
| 313.15 |
0.0713 |
0.0005 |
| 313.15 |
0.1403 |
0.0006 |
| 313.15 |
0.2123 |
0.0006 |
| 313.15 |
0.2809 |
0.0006 |
| 313.15 |
0.3528 |
0.0007 |
| 313.15 |
0.4195 |
0.0007 |
| 313.15 |
0.5037 |
0.0007 |
| 313.15 |
0.5800 |
0.0008 |
| 313.15 |
0.6504 |
0.0008 |
| 313.15 |
0.7197 |
0.0008 |
| 313.15 |
0.7822 |
0.0009 |
| 313.15 |
0.8561 |
0.0009 |
| 313.15 |
0.9287 |
0.0009 |
| 313.15 |
1.0000 |
0.0009 |
| 318.15 |
0.0000 |
0.0005 |
| 318.15 |
0.0713 |
0.0005 |
| 318.15 |
0.1403 |
0.0005 |
| 318.15 |
0.2123 |
0.0006 |
| 318.15 |
0.2809 |
0.0006 |
| 318.15 |
0.3528 |
0.0006 |
| 318.15 |
0.4195 |
0.0006 |
| 318.15 |
0.5037 |
0.0007 |
| 318.15 |
0.5800 |
0.0007 |
| 318.15 |
0.6504 |
0.0007 |
| 318.15 |
0.7197 |
0.0008 |
| 318.15 |
0.7822 |
0.0008 |
| 318.15 |
0.8561 |
0.0008 |
| 318.15 |
0.9287 |
0.0009 |
| 318.15 |
1.0000 |
0.0009 |
Refractive index (Na D-line)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 1,4-Dioxane (2) - Liquid |
Refractive index (Na D-line) - Liquid |
| 288.15 |
0.0000 |
1.5042 |
| 288.15 |
0.0713 |
1.4982 |
| 288.15 |
0.1403 |
1.4924 |
| 288.15 |
0.2123 |
1.4864 |
| 288.15 |
0.2809 |
1.4807 |
| 288.15 |
0.3528 |
1.4748 |
| 288.15 |
0.4195 |
1.4694 |
| 288.15 |
0.5037 |
1.4626 |
| 288.15 |
0.5800 |
1.4565 |
| 288.15 |
0.6504 |
1.451 |
| 288.15 |
0.7197 |
1.4456 |
| 288.15 |
0.7822 |
1.4408 |
| 288.15 |
0.8561 |
1.4352 |
| 288.15 |
0.9287 |
1.4298 |
| 288.15 |
1.0000 |
1.4245 |
| 293.15 |
0.0000 |
1.5011 |
| 293.15 |
0.0713 |
1.4951 |
| 293.15 |
0.1403 |
1.4894 |
| 293.15 |
0.2123 |
1.4835 |
| 293.15 |
0.2809 |
1.4778 |
| 293.15 |
0.3528 |
1.472 |
| 293.15 |
0.4195 |
1.4666 |
| 293.15 |
0.5037 |
1.4599 |
| 293.15 |
0.5800 |
1.4539 |
| 293.15 |
0.6504 |
1.4484 |
| 293.15 |
0.7197 |
1.4432 |
| 293.15 |
0.7822 |
1.4384 |
| 293.15 |
0.8561 |
1.4329 |
| 293.15 |
0.9287 |
1.4276 |
| 293.15 |
1.0000 |
1.4224 |
| 298.15 |
0.0000 |
1.498 |
| 298.15 |
0.0713 |
1.4921 |
| 298.15 |
0.1403 |
1.4864 |
| 298.15 |
0.2123 |
1.4805 |
| 298.15 |
0.2809 |
1.4749 |
| 298.15 |
0.3528 |
1.4692 |
| 298.15 |
0.4195 |
1.4639 |
| 298.15 |
0.5037 |
1.4573 |
| 298.15 |
0.5800 |
1.4513 |
| 298.15 |
0.6504 |
1.4459 |
| 298.15 |
0.7197 |
1.4407 |
| 298.15 |
0.7822 |
1.436 |
| 298.15 |
0.8561 |
1.4306 |
| 298.15 |
0.9287 |
1.4254 |
| 298.15 |
1.0000 |
1.4203 |
| 303.15 |
0.0000 |
1.4949 |
| 303.15 |
0.0713 |
1.489 |
| 303.15 |
0.1403 |
1.4834 |
| 303.15 |
0.2123 |
1.4775 |
| 303.15 |
0.2809 |
1.472 |
| 303.15 |
0.3528 |
1.4663 |
| 303.15 |
0.4195 |
1.4611 |
| 303.15 |
0.5037 |
1.4546 |
| 303.15 |
0.5800 |
1.4487 |
| 303.15 |
0.6504 |
1.4434 |
| 303.15 |
0.7197 |
1.4382 |
| 303.15 |
0.7822 |
1.4336 |
| 303.15 |
0.8561 |
1.4283 |
| 303.15 |
0.9287 |
1.4232 |
| 303.15 |
1.0000 |
1.4182 |
| 308.15 |
0.0000 |
1.4918 |
| 308.15 |
0.0713 |
1.4859 |
| 308.15 |
0.1403 |
1.4803 |
| 308.15 |
0.2123 |
1.4746 |
| 308.15 |
0.2809 |
1.4691 |
| 308.15 |
0.3528 |
1.4635 |
| 308.15 |
0.4195 |
1.4583 |
| 308.15 |
0.5037 |
1.4519 |
| 308.15 |
0.5800 |
1.4461 |
| 308.15 |
0.6504 |
1.4409 |
| 308.15 |
0.7197 |
1.4358 |
| 308.15 |
0.7822 |
1.4312 |
| 308.15 |
0.8561 |
1.426 |
| 308.15 |
0.9287 |
1.421 |
| 308.15 |
1.0000 |
1.4161 |
| 313.15 |
0.0000 |
1.4887 |
| 313.15 |
0.0713 |
1.4829 |
| 313.15 |
0.1403 |
1.4773 |
| 313.15 |
0.2123 |
1.4716 |
| 313.15 |
0.2809 |
1.4662 |
| 313.15 |
0.3528 |
1.4607 |
| 313.15 |
0.4195 |
1.4556 |
| 313.15 |
0.5037 |
1.4492 |
| 313.15 |
0.5800 |
1.4435 |
| 313.15 |
0.6504 |
1.4383 |
| 313.15 |
0.7197 |
1.4332 |
| 313.15 |
0.7822 |
1.4287 |
| 313.15 |
0.8561 |
1.4236 |
| 313.15 |
0.9287 |
1.4187 |
| 313.15 |
1.0000 |
1.4139 |
| 318.15 |
0.0000 |
1.4856 |
| 318.15 |
0.0713 |
1.4798 |
| 318.15 |
0.1403 |
1.4743 |
| 318.15 |
0.2123 |
1.4686 |
| 318.15 |
0.2809 |
1.4633 |
| 318.15 |
0.3528 |
1.4578 |
| 318.15 |
0.4195 |
1.4528 |
| 318.15 |
0.5037 |
1.4465 |
| 318.15 |
0.5800 |
1.4409 |
| 318.15 |
0.6504 |
1.4357 |
| 318.15 |
0.7197 |
1.4307 |
| 318.15 |
0.7822 |
1.4263 |
| 318.15 |
0.8561 |
1.4212 |
| 318.15 |
0.9287 |
1.4164 |
| 318.15 |
1.0000 |
1.4117 |
Refractive index (Na D-line)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 1,4-Dioxane (2) - Liquid |
Refractive index (Na D-line) - Liquid |
| 288.15 |
0.0000 |
1.5042 |
| 288.15 |
0.0713 |
1.4982 |
| 288.15 |
0.1403 |
1.4924 |
| 288.15 |
0.2123 |
1.4864 |
| 288.15 |
0.2809 |
1.4807 |
| 288.15 |
0.3528 |
1.4748 |
| 288.15 |
0.4195 |
1.4694 |
| 288.15 |
0.5037 |
1.4626 |
| 288.15 |
0.5800 |
1.4565 |
| 288.15 |
0.6504 |
1.451 |
| 288.15 |
0.7197 |
1.4456 |
| 288.15 |
0.7822 |
1.4408 |
| 288.15 |
0.8561 |
1.4352 |
| 288.15 |
0.9287 |
1.4298 |
| 288.15 |
1.0000 |
1.4245 |
| 293.15 |
0.0000 |
1.5011 |
| 293.15 |
0.0713 |
1.4951 |
| 293.15 |
0.1403 |
1.4894 |
| 293.15 |
0.2123 |
1.4835 |
| 293.15 |
0.2809 |
1.4778 |
| 293.15 |
0.3528 |
1.472 |
| 293.15 |
0.4195 |
1.4666 |
| 293.15 |
0.5037 |
1.4599 |
| 293.15 |
0.5800 |
1.4539 |
| 293.15 |
0.6504 |
1.4484 |
| 293.15 |
0.7197 |
1.4432 |
| 293.15 |
0.7822 |
1.4384 |
| 293.15 |
0.8561 |
1.4329 |
| 293.15 |
0.9287 |
1.4276 |
| 293.15 |
1.0000 |
1.4224 |
| 298.15 |
0.0000 |
1.498 |
| 298.15 |
0.0713 |
1.4921 |
| 298.15 |
0.1403 |
1.4864 |
| 298.15 |
0.2123 |
1.4805 |
| 298.15 |
0.2809 |
1.4749 |
| 298.15 |
0.3528 |
1.4692 |
| 298.15 |
0.4195 |
1.4639 |
| 298.15 |
0.5037 |
1.4573 |
| 298.15 |
0.5800 |
1.4513 |
| 298.15 |
0.6504 |
1.4459 |
| 298.15 |
0.7197 |
1.4407 |
| 298.15 |
0.7822 |
1.436 |
| 298.15 |
0.8561 |
1.4306 |
| 298.15 |
0.9287 |
1.4254 |
| 298.15 |
1.0000 |
1.4203 |
| 303.15 |
0.0000 |
1.4949 |
| 303.15 |
0.0713 |
1.489 |
| 303.15 |
0.1403 |
1.4834 |
| 303.15 |
0.2123 |
1.4775 |
| 303.15 |
0.2809 |
1.472 |
| 303.15 |
0.3528 |
1.4663 |
| 303.15 |
0.4195 |
1.4611 |
| 303.15 |
0.5037 |
1.4546 |
| 303.15 |
0.5800 |
1.4487 |
| 303.15 |
0.6504 |
1.4434 |
| 303.15 |
0.7197 |
1.4382 |
| 303.15 |
0.7822 |
1.4336 |
| 303.15 |
0.8561 |
1.4283 |
| 303.15 |
0.9287 |
1.4232 |
| 303.15 |
1.0000 |
1.4182 |
| 308.15 |
0.0000 |
1.4918 |
| 308.15 |
0.0713 |
1.4859 |
| 308.15 |
0.1403 |
1.4803 |
| 308.15 |
0.2123 |
1.4746 |
| 308.15 |
0.2809 |
1.4691 |
| 308.15 |
0.3528 |
1.4635 |
| 308.15 |
0.4195 |
1.4583 |
| 308.15 |
0.5037 |
1.4519 |
| 308.15 |
0.5800 |
1.4461 |
| 308.15 |
0.6504 |
1.4409 |
| 308.15 |
0.7197 |
1.4358 |
| 308.15 |
0.7822 |
1.4312 |
| 308.15 |
0.8561 |
1.426 |
| 308.15 |
0.9287 |
1.421 |
| 308.15 |
1.0000 |
1.4161 |
| 313.15 |
0.0000 |
1.4887 |
| 313.15 |
0.0713 |
1.4829 |
| 313.15 |
0.1403 |
1.4773 |
| 313.15 |
0.2123 |
1.4716 |
| 313.15 |
0.2809 |
1.4662 |
| 313.15 |
0.3528 |
1.4607 |
| 313.15 |
0.4195 |
1.4556 |
| 313.15 |
0.5037 |
1.4492 |
| 313.15 |
0.5800 |
1.4435 |
| 313.15 |
0.6504 |
1.4383 |
| 313.15 |
0.7197 |
1.4332 |
| 313.15 |
0.7822 |
1.4287 |
| 313.15 |
0.8561 |
1.4236 |
| 313.15 |
0.9287 |
1.4187 |
| 313.15 |
1.0000 |
1.4139 |
| 318.15 |
0.0000 |
1.4856 |
| 318.15 |
0.0713 |
1.4798 |
| 318.15 |
0.1403 |
1.4743 |
| 318.15 |
0.2123 |
1.4686 |
| 318.15 |
0.2809 |
1.4633 |
| 318.15 |
0.3528 |
1.4578 |
| 318.15 |
0.4195 |
1.4528 |
| 318.15 |
0.5037 |
1.4465 |
| 318.15 |
0.5800 |
1.4409 |
| 318.15 |
0.6504 |
1.4357 |
| 318.15 |
0.7197 |
1.4307 |
| 318.15 |
0.7822 |
1.4263 |
| 318.15 |
0.8561 |
1.4212 |
| 318.15 |
0.9287 |
1.4164 |
| 318.15 |
1.0000 |
1.4117 |
Mass density, kg/m3
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 1,4-Dioxane (2) - Liquid |
Mass density, kg/m3 - Liquid |
| 288.15 |
0.0000 |
884.3 |
| 288.15 |
0.0713 |
895.16 |
| 288.15 |
0.1403 |
905.71 |
| 288.15 |
0.2123 |
916.74 |
| 288.15 |
0.2809 |
927.28 |
| 288.15 |
0.3528 |
938.34 |
| 288.15 |
0.4195 |
948.63 |
| 288.15 |
0.5037 |
961.65 |
| 288.15 |
0.5800 |
973.48 |
| 288.15 |
0.6504 |
984.43 |
| 288.15 |
0.7197 |
995.23 |
| 288.15 |
0.7822 |
1005.0 |
| 288.15 |
0.8561 |
1016.58 |
| 288.15 |
0.9287 |
1027.99 |
| 288.15 |
1.0000 |
1039.23 |
| 293.15 |
0.0000 |
878.95 |
| 293.15 |
0.0713 |
889.77 |
| 293.15 |
0.1403 |
900.28 |
| 293.15 |
0.2123 |
911.28 |
| 293.15 |
0.2809 |
921.79 |
| 293.15 |
0.3528 |
932.82 |
| 293.15 |
0.4195 |
943.09 |
| 293.15 |
0.5037 |
956.08 |
| 293.15 |
0.5800 |
967.89 |
| 293.15 |
0.6504 |
978.82 |
| 293.15 |
0.7197 |
989.61 |
| 293.15 |
0.7822 |
999.37 |
| 293.15 |
0.8561 |
1010.94 |
| 293.15 |
0.9287 |
1022.35 |
| 293.15 |
1.0000 |
1033.59 |
| 298.15 |
0.0000 |
873.61 |
| 298.15 |
0.0713 |
884.38 |
| 298.15 |
0.1403 |
894.85 |
| 298.15 |
0.2123 |
905.82 |
| 298.15 |
0.2809 |
916.3 |
| 298.15 |
0.3528 |
927.31 |
| 298.15 |
0.4195 |
937.55 |
| 298.15 |
0.5037 |
950.51 |
| 298.15 |
0.5800 |
962.3 |
| 298.15 |
0.6504 |
973.21 |
| 298.15 |
0.7197 |
983.99 |
| 298.15 |
0.7822 |
993.74 |
| 298.15 |
0.8561 |
1005.3 |
| 298.15 |
0.9287 |
1016.71 |
| 298.15 |
1.0000 |
1027.95 |
| 303.15 |
0.0000 |
868.26 |
| 303.15 |
0.0713 |
878.99 |
| 303.15 |
0.1403 |
889.42 |
| 303.15 |
0.2123 |
900.36 |
| 303.15 |
0.2809 |
910.81 |
| 303.15 |
0.3528 |
921.8 |
| 303.15 |
0.4195 |
932.01 |
| 303.15 |
0.5037 |
944.94 |
| 303.15 |
0.5800 |
956.71 |
| 303.15 |
0.6504 |
967.6 |
| 303.15 |
0.7197 |
978.37 |
| 303.15 |
0.7822 |
988.11 |
| 303.15 |
0.8561 |
999.66 |
| 303.15 |
0.9287 |
1011.07 |
| 303.15 |
1.0000 |
1022.32 |
| 308.15 |
0.0000 |
862.9 |
| 308.15 |
0.0713 |
873.6 |
| 308.15 |
0.1403 |
883.99 |
| 308.15 |
0.2123 |
894.9 |
| 308.15 |
0.2809 |
905.32 |
| 308.15 |
0.3528 |
916.28 |
| 308.15 |
0.4195 |
926.47 |
| 308.15 |
0.5037 |
939.38 |
| 308.15 |
0.5800 |
951.12 |
| 308.15 |
0.6504 |
962.0 |
| 308.15 |
0.7197 |
972.75 |
| 308.15 |
0.7822 |
982.48 |
| 308.15 |
0.8561 |
994.02 |
| 308.15 |
0.9287 |
1005.43 |
| 308.15 |
1.0000 |
1016.68 |
| 313.15 |
0.0000 |
857.56 |
| 313.15 |
0.0713 |
868.22 |
| 313.15 |
0.1403 |
878.58 |
| 313.15 |
0.2123 |
889.45 |
| 313.15 |
0.2809 |
899.84 |
| 313.15 |
0.3528 |
910.77 |
| 313.15 |
0.4195 |
920.94 |
| 313.15 |
0.5037 |
933.82 |
| 313.15 |
0.5800 |
945.54 |
| 313.15 |
0.6504 |
956.4 |
| 313.15 |
0.7197 |
967.13 |
| 313.15 |
0.7822 |
976.85 |
| 313.15 |
0.8561 |
988.39 |
| 313.15 |
0.9287 |
999.79 |
| 313.15 |
1.0000 |
1011.05 |
| 318.15 |
0.0000 |
852.23 |
| 318.15 |
0.0713 |
862.84 |
| 318.15 |
0.1403 |
873.17 |
| 318.15 |
0.2123 |
884.0 |
| 318.15 |
0.2809 |
894.36 |
| 318.15 |
0.3528 |
905.26 |
| 318.15 |
0.4195 |
915.41 |
| 318.15 |
0.5037 |
928.26 |
| 318.15 |
0.5800 |
939.96 |
| 318.15 |
0.6504 |
950.8 |
| 318.15 |
0.7197 |
961.52 |
| 318.15 |
0.7822 |
971.23 |
| 318.15 |
0.8561 |
982.76 |
| 318.15 |
0.9287 |
994.15 |
| 318.15 |
1.0000 |
1005.42 |
Mass density, kg/m3
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 1,4-Dioxane (2) - Liquid |
Mass density, kg/m3 - Liquid |
| 288.15 |
0.0000 |
884.3 |
| 288.15 |
0.0713 |
895.16 |
| 288.15 |
0.1403 |
905.71 |
| 288.15 |
0.2123 |
916.74 |
| 288.15 |
0.2809 |
927.28 |
| 288.15 |
0.3528 |
938.34 |
| 288.15 |
0.4195 |
948.63 |
| 288.15 |
0.5037 |
961.65 |
| 288.15 |
0.5800 |
973.48 |
| 288.15 |
0.6504 |
984.43 |
| 288.15 |
0.7197 |
995.23 |
| 288.15 |
0.7822 |
1005.0 |
| 288.15 |
0.8561 |
1016.58 |
| 288.15 |
0.9287 |
1027.99 |
| 288.15 |
1.0000 |
1039.23 |
| 293.15 |
0.0000 |
878.95 |
| 293.15 |
0.0713 |
889.77 |
| 293.15 |
0.1403 |
900.28 |
| 293.15 |
0.2123 |
911.28 |
| 293.15 |
0.2809 |
921.79 |
| 293.15 |
0.3528 |
932.82 |
| 293.15 |
0.4195 |
943.09 |
| 293.15 |
0.5037 |
956.08 |
| 293.15 |
0.5800 |
967.89 |
| 293.15 |
0.6504 |
978.82 |
| 293.15 |
0.7197 |
989.61 |
| 293.15 |
0.7822 |
999.37 |
| 293.15 |
0.8561 |
1010.94 |
| 293.15 |
0.9287 |
1022.35 |
| 293.15 |
1.0000 |
1033.59 |
| 298.15 |
0.0000 |
873.61 |
| 298.15 |
0.0713 |
884.38 |
| 298.15 |
0.1403 |
894.85 |
| 298.15 |
0.2123 |
905.82 |
| 298.15 |
0.2809 |
916.3 |
| 298.15 |
0.3528 |
927.31 |
| 298.15 |
0.4195 |
937.55 |
| 298.15 |
0.5037 |
950.51 |
| 298.15 |
0.5800 |
962.3 |
| 298.15 |
0.6504 |
973.21 |
| 298.15 |
0.7197 |
983.99 |
| 298.15 |
0.7822 |
993.74 |
| 298.15 |
0.8561 |
1005.3 |
| 298.15 |
0.9287 |
1016.71 |
| 298.15 |
1.0000 |
1027.95 |
| 303.15 |
0.0000 |
868.26 |
| 303.15 |
0.0713 |
878.99 |
| 303.15 |
0.1403 |
889.42 |
| 303.15 |
0.2123 |
900.36 |
| 303.15 |
0.2809 |
910.81 |
| 303.15 |
0.3528 |
921.8 |
| 303.15 |
0.4195 |
932.01 |
| 303.15 |
0.5037 |
944.94 |
| 303.15 |
0.5800 |
956.71 |
| 303.15 |
0.6504 |
967.6 |
| 303.15 |
0.7197 |
978.37 |
| 303.15 |
0.7822 |
988.11 |
| 303.15 |
0.8561 |
999.66 |
| 303.15 |
0.9287 |
1011.07 |
| 303.15 |
1.0000 |
1022.32 |
| 308.15 |
0.0000 |
862.9 |
| 308.15 |
0.0713 |
873.6 |
| 308.15 |
0.1403 |
883.99 |
| 308.15 |
0.2123 |
894.9 |
| 308.15 |
0.2809 |
905.32 |
| 308.15 |
0.3528 |
916.28 |
| 308.15 |
0.4195 |
926.47 |
| 308.15 |
0.5037 |
939.38 |
| 308.15 |
0.5800 |
951.12 |
| 308.15 |
0.6504 |
962.0 |
| 308.15 |
0.7197 |
972.75 |
| 308.15 |
0.7822 |
982.48 |
| 308.15 |
0.8561 |
994.02 |
| 308.15 |
0.9287 |
1005.43 |
| 308.15 |
1.0000 |
1016.68 |
| 313.15 |
0.0000 |
857.56 |
| 313.15 |
0.0713 |
868.22 |
| 313.15 |
0.1403 |
878.58 |
| 313.15 |
0.2123 |
889.45 |
| 313.15 |
0.2809 |
899.84 |
| 313.15 |
0.3528 |
910.77 |
| 313.15 |
0.4195 |
920.94 |
| 313.15 |
0.5037 |
933.82 |
| 313.15 |
0.5800 |
945.54 |
| 313.15 |
0.6504 |
956.4 |
| 313.15 |
0.7197 |
967.13 |
| 313.15 |
0.7822 |
976.85 |
| 313.15 |
0.8561 |
988.39 |
| 313.15 |
0.9287 |
999.79 |
| 313.15 |
1.0000 |
1011.05 |
| 318.15 |
0.0000 |
852.23 |
| 318.15 |
0.0713 |
862.84 |
| 318.15 |
0.1403 |
873.17 |
| 318.15 |
0.2123 |
884.0 |
| 318.15 |
0.2809 |
894.36 |
| 318.15 |
0.3528 |
905.26 |
| 318.15 |
0.4195 |
915.41 |
| 318.15 |
0.5037 |
928.26 |
| 318.15 |
0.5800 |
939.96 |
| 318.15 |
0.6504 |
950.8 |
| 318.15 |
0.7197 |
961.52 |
| 318.15 |
0.7822 |
971.23 |
| 318.15 |
0.8561 |
982.76 |
| 318.15 |
0.9287 |
994.15 |
| 318.15 |
1.0000 |
1005.42 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 1,4-Dioxane (2) - Liquid |
Speed of sound, m/s - Liquid |
| 283.15 |
0.0521 |
1370.8 |
| 283.15 |
0.0942 |
1372.6 |
| 283.15 |
0.1987 |
1376.5 |
| 283.15 |
0.2956 |
1380.2 |
| 283.15 |
0.3936 |
1383.8 |
| 283.15 |
0.4947 |
1387.4 |
| 283.15 |
0.5964 |
1391.1 |
| 283.15 |
0.6956 |
1395.1 |
| 283.15 |
0.7963 |
1399.3 |
| 283.15 |
0.8949 |
1404.1 |
| 283.15 |
0.9526 |
1407.1 |
| 298.15 |
0.0516 |
1300.8 |
| 298.15 |
0.0888 |
1302.4 |
| 298.15 |
0.1966 |
1307.3 |
| 298.15 |
0.3160 |
1312.2 |
| 298.15 |
0.4145 |
1316.3 |
| 298.15 |
0.5004 |
1320.0 |
| 298.15 |
0.5975 |
1324.1 |
| 298.15 |
0.6932 |
1328.4 |
| 298.15 |
0.7962 |
1333.1 |
| 298.15 |
0.8938 |
1338.0 |
| 298.15 |
0.9535 |
1341.1 |
| 313.15 |
0.0568 |
1232.1 |
| 313.15 |
0.0913 |
1233.6 |
| 313.15 |
0.2021 |
1239.2 |
| 313.15 |
0.2963 |
1243.7 |
| 313.15 |
0.3981 |
1248.6 |
| 313.15 |
0.4975 |
1253.1 |
| 313.15 |
0.5981 |
1257.9 |
| 313.15 |
0.6972 |
1262.7 |
| 313.15 |
0.7941 |
1267.5 |
| 313.15 |
0.9034 |
1273.3 |
| 313.15 |
0.9424 |
1275.5 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Frequency, MHz = 3 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 1,4-Dioxane (2) - Liquid |
Speed of sound, m/s - Liquid |
| 293.15 |
0.0000 |
1324.4 |
| 293.15 |
0.0713 |
1329.8 |
| 293.15 |
0.1403 |
1334.5 |
| 293.15 |
0.2123 |
1339.4 |
| 293.15 |
0.2809 |
1343.6 |
| 293.15 |
0.3528 |
1347.9 |
| 293.15 |
0.4195 |
1351.5 |
| 293.15 |
0.5037 |
1355.8 |
| 293.15 |
0.5800 |
1359.2 |
| 293.15 |
0.6504 |
1362.2 |
| 293.15 |
0.7197 |
1364.2 |
| 293.15 |
0.7822 |
1365.4 |
| 293.15 |
0.8561 |
1366.9 |
| 293.15 |
0.9287 |
1367.4 |
| 293.15 |
1.0000 |
1367.2 |
| 298.15 |
0.0000 |
1299.5 |
| 298.15 |
0.0713 |
1304.0 |
| 298.15 |
0.1403 |
1308.1 |
| 298.15 |
0.2123 |
1312.5 |
| 298.15 |
0.2809 |
1316.5 |
| 298.15 |
0.3528 |
1320.5 |
| 298.15 |
0.4195 |
1324.0 |
| 298.15 |
0.5037 |
1328.2 |
| 298.15 |
0.5800 |
1332.0 |
| 298.15 |
0.6504 |
1335.1 |
| 298.15 |
0.7197 |
1337.5 |
| 298.15 |
0.7822 |
1339.8 |
| 298.15 |
0.8561 |
1342.0 |
| 298.15 |
0.9287 |
1343.7 |
| 298.15 |
1.0000 |
1344.7 |
| 303.15 |
0.0000 |
1275.7 |
| 303.15 |
0.0713 |
1279.4 |
| 303.15 |
0.1403 |
1283.0 |
| 303.15 |
0.2123 |
1287.0 |
| 303.15 |
0.2809 |
1290.6 |
| 303.15 |
0.3528 |
1294.2 |
| 303.15 |
0.4195 |
1297.6 |
| 303.15 |
0.5037 |
1301.8 |
| 303.15 |
0.5800 |
1305.7 |
| 303.15 |
0.6504 |
1309.2 |
| 303.15 |
0.7197 |
1312.3 |
| 303.15 |
0.7822 |
1315.1 |
| 303.15 |
0.8561 |
1318.2 |
| 303.15 |
0.9287 |
1320.8 |
| 303.15 |
1.0000 |
1323.1 |
| 308.15 |
0.0000 |
1252.4 |
| 308.15 |
0.0713 |
1255.4 |
| 308.15 |
0.1403 |
1258.7 |
| 308.15 |
0.2123 |
1262.0 |
| 308.15 |
0.2809 |
1265.1 |
| 308.15 |
0.3528 |
1268.7 |
| 308.15 |
0.4195 |
1272.0 |
| 308.15 |
0.5037 |
1276.1 |
| 308.15 |
0.5800 |
1280.2 |
| 308.15 |
0.6504 |
1284.0 |
| 308.15 |
0.7197 |
1287.4 |
| 308.15 |
0.7822 |
1290.8 |
| 308.15 |
0.8561 |
1294.5 |
| 308.15 |
0.9287 |
1297.9 |
| 308.15 |
1.0000 |
1301.2 |
| 313.15 |
0.0000 |
1229.3 |
| 313.15 |
0.0713 |
1231.7 |
| 313.15 |
0.1403 |
1234.3 |
| 313.15 |
0.2123 |
1237.2 |
| 313.15 |
0.2809 |
1240.5 |
| 313.15 |
0.3528 |
1244.0 |
| 313.15 |
0.4195 |
1247.1 |
| 313.15 |
0.5037 |
1251.3 |
| 313.15 |
0.5800 |
1255.5 |
| 313.15 |
0.6504 |
1259.4 |
| 313.15 |
0.7197 |
1263.5 |
| 313.15 |
0.7822 |
1266.8 |
| 313.15 |
0.8561 |
1271.2 |
| 313.15 |
0.9287 |
1275.3 |
| 313.15 |
1.0000 |
1279.7 |
| 318.15 |
0.0000 |
1207.8 |
| 318.15 |
0.0713 |
1209.6 |
| 318.15 |
0.1403 |
1211.9 |
| 318.15 |
0.2123 |
1214.5 |
| 318.15 |
0.2809 |
1217.2 |
| 318.15 |
0.3528 |
1220.5 |
| 318.15 |
0.4195 |
1223.6 |
| 318.15 |
0.5037 |
1227.9 |
| 318.15 |
0.5800 |
1232.1 |
| 318.15 |
0.6504 |
1236.0 |
| 318.15 |
0.7197 |
1240.1 |
| 318.15 |
0.7822 |
1243.9 |
| 318.15 |
0.8561 |
1248.8 |
| 318.15 |
0.9287 |
1253.6 |
| 318.15 |
1.0000 |
1258.6 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 1,4-Dioxane (2) - Liquid |
Speed of sound, m/s - Liquid |
| 283.15 |
0.0521 |
1370.8 |
| 283.15 |
0.0942 |
1372.6 |
| 283.15 |
0.1987 |
1376.5 |
| 283.15 |
0.2956 |
1380.2 |
| 283.15 |
0.3936 |
1383.8 |
| 283.15 |
0.4947 |
1387.4 |
| 283.15 |
0.5964 |
1391.1 |
| 283.15 |
0.6956 |
1395.1 |
| 283.15 |
0.7963 |
1399.3 |
| 283.15 |
0.8949 |
1404.1 |
| 283.15 |
0.9526 |
1407.1 |
| 298.15 |
0.0516 |
1300.8 |
| 298.15 |
0.0888 |
1302.4 |
| 298.15 |
0.1966 |
1307.3 |
| 298.15 |
0.3160 |
1312.2 |
| 298.15 |
0.4145 |
1316.3 |
| 298.15 |
0.5004 |
1320.0 |
| 298.15 |
0.5975 |
1324.1 |
| 298.15 |
0.6932 |
1328.4 |
| 298.15 |
0.7962 |
1333.1 |
| 298.15 |
0.8938 |
1338.0 |
| 298.15 |
0.9535 |
1341.1 |
| 313.15 |
0.0568 |
1232.1 |
| 313.15 |
0.0913 |
1233.6 |
| 313.15 |
0.2021 |
1239.2 |
| 313.15 |
0.2963 |
1243.7 |
| 313.15 |
0.3981 |
1248.6 |
| 313.15 |
0.4975 |
1253.1 |
| 313.15 |
0.5981 |
1257.9 |
| 313.15 |
0.6972 |
1262.7 |
| 313.15 |
0.7941 |
1267.5 |
| 313.15 |
0.9034 |
1273.3 |
| 313.15 |
0.9424 |
1275.5 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Frequency, MHz = 3 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 1,4-Dioxane (2) - Liquid |
Speed of sound, m/s - Liquid |
| 293.15 |
0.0000 |
1324.4 |
| 293.15 |
0.0713 |
1329.8 |
| 293.15 |
0.1403 |
1334.5 |
| 293.15 |
0.2123 |
1339.4 |
| 293.15 |
0.2809 |
1343.6 |
| 293.15 |
0.3528 |
1347.9 |
| 293.15 |
0.4195 |
1351.5 |
| 293.15 |
0.5037 |
1355.8 |
| 293.15 |
0.5800 |
1359.2 |
| 293.15 |
0.6504 |
1362.2 |
| 293.15 |
0.7197 |
1364.2 |
| 293.15 |
0.7822 |
1365.4 |
| 293.15 |
0.8561 |
1366.9 |
| 293.15 |
0.9287 |
1367.4 |
| 293.15 |
1.0000 |
1367.2 |
| 298.15 |
0.0000 |
1299.5 |
| 298.15 |
0.0713 |
1304.0 |
| 298.15 |
0.1403 |
1308.1 |
| 298.15 |
0.2123 |
1312.5 |
| 298.15 |
0.2809 |
1316.5 |
| 298.15 |
0.3528 |
1320.5 |
| 298.15 |
0.4195 |
1324.0 |
| 298.15 |
0.5037 |
1328.2 |
| 298.15 |
0.5800 |
1332.0 |
| 298.15 |
0.6504 |
1335.1 |
| 298.15 |
0.7197 |
1337.5 |
| 298.15 |
0.7822 |
1339.8 |
| 298.15 |
0.8561 |
1342.0 |
| 298.15 |
0.9287 |
1343.7 |
| 298.15 |
1.0000 |
1344.7 |
| 303.15 |
0.0000 |
1275.7 |
| 303.15 |
0.0713 |
1279.4 |
| 303.15 |
0.1403 |
1283.0 |
| 303.15 |
0.2123 |
1287.0 |
| 303.15 |
0.2809 |
1290.6 |
| 303.15 |
0.3528 |
1294.2 |
| 303.15 |
0.4195 |
1297.6 |
| 303.15 |
0.5037 |
1301.8 |
| 303.15 |
0.5800 |
1305.7 |
| 303.15 |
0.6504 |
1309.2 |
| 303.15 |
0.7197 |
1312.3 |
| 303.15 |
0.7822 |
1315.1 |
| 303.15 |
0.8561 |
1318.2 |
| 303.15 |
0.9287 |
1320.8 |
| 303.15 |
1.0000 |
1323.1 |
| 308.15 |
0.0000 |
1252.4 |
| 308.15 |
0.0713 |
1255.4 |
| 308.15 |
0.1403 |
1258.7 |
| 308.15 |
0.2123 |
1262.0 |
| 308.15 |
0.2809 |
1265.1 |
| 308.15 |
0.3528 |
1268.7 |
| 308.15 |
0.4195 |
1272.0 |
| 308.15 |
0.5037 |
1276.1 |
| 308.15 |
0.5800 |
1280.2 |
| 308.15 |
0.6504 |
1284.0 |
| 308.15 |
0.7197 |
1287.4 |
| 308.15 |
0.7822 |
1290.8 |
| 308.15 |
0.8561 |
1294.5 |
| 308.15 |
0.9287 |
1297.9 |
| 308.15 |
1.0000 |
1301.2 |
| 313.15 |
0.0000 |
1229.3 |
| 313.15 |
0.0713 |
1231.7 |
| 313.15 |
0.1403 |
1234.3 |
| 313.15 |
0.2123 |
1237.2 |
| 313.15 |
0.2809 |
1240.5 |
| 313.15 |
0.3528 |
1244.0 |
| 313.15 |
0.4195 |
1247.1 |
| 313.15 |
0.5037 |
1251.3 |
| 313.15 |
0.5800 |
1255.5 |
| 313.15 |
0.6504 |
1259.4 |
| 313.15 |
0.7197 |
1263.5 |
| 313.15 |
0.7822 |
1266.8 |
| 313.15 |
0.8561 |
1271.2 |
| 313.15 |
0.9287 |
1275.3 |
| 313.15 |
1.0000 |
1279.7 |
| 318.15 |
0.0000 |
1207.8 |
| 318.15 |
0.0713 |
1209.6 |
| 318.15 |
0.1403 |
1211.9 |
| 318.15 |
0.2123 |
1214.5 |
| 318.15 |
0.2809 |
1217.2 |
| 318.15 |
0.3528 |
1220.5 |
| 318.15 |
0.4195 |
1223.6 |
| 318.15 |
0.5037 |
1227.9 |
| 318.15 |
0.5800 |
1232.1 |
| 318.15 |
0.6504 |
1236.0 |
| 318.15 |
0.7197 |
1240.1 |
| 318.15 |
0.7822 |
1243.9 |
| 318.15 |
0.8561 |
1248.8 |
| 318.15 |
0.9287 |
1253.6 |
| 318.15 |
1.0000 |
1258.6 |
Boiling temperature at pressure P, K
[ref]
| Fixed |
Measured |
| Mole fraction of 1,4-Dioxane (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
101.30 |
353.20 |
| 0.0481 |
101.30 |
353.63 |
| 0.0516 |
66.60 |
340.91 |
| 0.0527 |
40.00 |
326.27 |
| 0.1135 |
101.30 |
354.55 |
| 0.1141 |
40.00 |
327.17 |
| 0.1166 |
66.60 |
341.67 |
| 0.2051 |
101.30 |
356.12 |
| 0.2169 |
66.60 |
343.08 |
| 0.2190 |
40.00 |
329.01 |
| 0.3043 |
40.00 |
330.29 |
| 0.3129 |
66.60 |
344.58 |
| 0.3149 |
101.30 |
358.08 |
| 0.4085 |
40.00 |
332.27 |
| 0.4150 |
101.30 |
359.97 |
| 0.4209 |
66.60 |
346.75 |
| 0.5008 |
101.30 |
361.54 |
| 0.5137 |
66.60 |
348.75 |
| 0.5191 |
40.00 |
334.36 |
| 0.5990 |
40.00 |
336.06 |
| 0.6086 |
66.60 |
350.66 |
| 0.6106 |
101.30 |
363.77 |
| 0.7002 |
40.00 |
338.32 |
| 0.7083 |
101.30 |
365.96 |
| 0.7093 |
66.60 |
352.90 |
| 0.7973 |
101.30 |
368.27 |
| 0.8016 |
66.60 |
355.14 |
| 0.8106 |
40.00 |
340.65 |
| 0.8839 |
66.60 |
357.56 |
| 0.8868 |
101.30 |
370.86 |
| 0.8925 |
40.00 |
343.11 |
| 0.9217 |
101.30 |
372.26 |
| 0.9368 |
66.60 |
359.19 |
| 0.9404 |
40.00 |
344.78 |
| 1.0000 |
101.30 |
375.52 |
Boiling temperature at pressure P, K
[ref]
| Fixed |
Measured |
| Mole fraction of 1,4-Dioxane (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
101.30 |
353.20 |
| 0.0481 |
101.30 |
353.63 |
| 0.0516 |
66.60 |
340.91 |
| 0.0527 |
40.00 |
326.27 |
| 0.1135 |
101.30 |
354.55 |
| 0.1141 |
40.00 |
327.17 |
| 0.1166 |
66.60 |
341.67 |
| 0.2051 |
101.30 |
356.12 |
| 0.2169 |
66.60 |
343.08 |
| 0.2190 |
40.00 |
329.01 |
| 0.3043 |
40.00 |
330.29 |
| 0.3129 |
66.60 |
344.58 |
| 0.3149 |
101.30 |
358.08 |
| 0.4085 |
40.00 |
332.27 |
| 0.4150 |
101.30 |
359.97 |
| 0.4209 |
66.60 |
346.75 |
| 0.5008 |
101.30 |
361.54 |
| 0.5137 |
66.60 |
348.75 |
| 0.5191 |
40.00 |
334.36 |
| 0.5990 |
40.00 |
336.06 |
| 0.6086 |
66.60 |
350.66 |
| 0.6106 |
101.30 |
363.77 |
| 0.7002 |
40.00 |
338.32 |
| 0.7083 |
101.30 |
365.96 |
| 0.7093 |
66.60 |
352.90 |
| 0.7973 |
101.30 |
368.27 |
| 0.8016 |
66.60 |
355.14 |
| 0.8106 |
40.00 |
340.65 |
| 0.8839 |
66.60 |
357.56 |
| 0.8868 |
101.30 |
370.86 |
| 0.8925 |
40.00 |
343.11 |
| 0.9217 |
101.30 |
372.26 |
| 0.9368 |
66.60 |
359.19 |
| 0.9404 |
40.00 |
344.78 |
| 1.0000 |
101.30 |
375.52 |
Sources
-
Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
-
Experimental and predicted vapour liquid equilibrium of 1,4-dioxane with cycloalkanes and benzene
-
Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
-
Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K