Datasets
-
Mole fraction (4)
-
n0 - Refractive index (Na D-line) (2)
-
ρl - Mass density, kg/m3 (4)
-
γ - Surface tension liquid-gas, N/m (2)
-
Tboil - Boiling temperature at pressure P, K (4)
Mole fraction of 1,4-Dioxane (2)
[ref]
Operational condition: Pressure, kPa =
40 (Liquid)
Mole fraction of 1,4-Dioxane (2) - Liquid |
Mole fraction of 1,4-Dioxane (2) - Gas |
0.0980 |
0.0537 |
0.1650 |
0.0682 |
0.2703 |
0.1154 |
0.3581 |
0.1504 |
0.4779 |
0.2093 |
0.5845 |
0.2724 |
0.6429 |
0.3210 |
0.7167 |
0.3758 |
0.7792 |
0.4451 |
0.8404 |
0.5413 |
0.8871 |
0.6248 |
0.9360 |
0.7440 |
Mole fraction of 1,4-Dioxane (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of 1,4-Dioxane (2) - Liquid |
Mole fraction of 1,4-Dioxane (2) - Gas |
0.0508 |
0.0247 |
0.1615 |
0.0762 |
0.2636 |
0.1251 |
0.3544 |
0.1778 |
0.4805 |
0.2498 |
0.5745 |
0.3021 |
0.6201 |
0.3425 |
0.7162 |
0.4174 |
0.7741 |
0.4970 |
0.8284 |
0.5634 |
0.8640 |
0.6216 |
0.9218 |
0.7533 |
Mole fraction of 1,4-Dioxane (2)
[ref]
Operational condition: Pressure, kPa =
40 (Liquid)
Mole fraction of 1,4-Dioxane (2) - Liquid |
Mole fraction of 1,4-Dioxane (2) - Gas |
0.0980 |
0.0537 |
0.1650 |
0.0682 |
0.2703 |
0.1154 |
0.3581 |
0.1504 |
0.4779 |
0.2093 |
0.5845 |
0.2724 |
0.6429 |
0.3210 |
0.7167 |
0.3758 |
0.7792 |
0.4451 |
0.8404 |
0.5413 |
0.8871 |
0.6248 |
0.9360 |
0.7440 |
Mole fraction of 1,4-Dioxane (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of 1,4-Dioxane (2) - Liquid |
Mole fraction of 1,4-Dioxane (2) - Gas |
0.0508 |
0.0247 |
0.1615 |
0.0762 |
0.2636 |
0.1251 |
0.3544 |
0.1778 |
0.4805 |
0.2498 |
0.5745 |
0.3021 |
0.6201 |
0.3425 |
0.7162 |
0.4174 |
0.7741 |
0.4970 |
0.8284 |
0.5634 |
0.8640 |
0.6216 |
0.9218 |
0.7533 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1,4-Dioxane (2) - Liquid |
Refractive index (Na D-line) - Liquid |
298.15 |
0.0000 |
1.394 |
298.15 |
0.0417 |
1.3949 |
298.15 |
0.1061 |
1.3963 |
298.15 |
0.2514 |
1.3996 |
298.15 |
0.3493 |
1.4019 |
298.15 |
0.4771 |
1.4051 |
298.15 |
0.5563 |
1.4072 |
298.15 |
0.6462 |
1.4096 |
298.15 |
0.7343 |
1.4121 |
298.15 |
0.8244 |
1.4147 |
298.15 |
0.9112 |
1.4172 |
298.15 |
0.9891 |
1.4196 |
298.15 |
1.0000 |
1.4199 |
313.15 |
0.0000 |
1.3857 |
313.15 |
0.0475 |
1.3867 |
313.15 |
0.1318 |
1.3886 |
313.15 |
0.2390 |
1.3912 |
313.15 |
0.3413 |
1.3938 |
313.15 |
0.4574 |
1.3968 |
313.15 |
0.5546 |
1.3995 |
313.15 |
0.6429 |
1.402 |
313.15 |
0.7326 |
1.4045 |
313.15 |
0.8209 |
1.4071 |
313.15 |
0.9121 |
1.4099 |
313.15 |
0.9525 |
1.4111 |
313.15 |
1.0000 |
1.4126 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1,4-Dioxane (2) - Liquid |
Refractive index (Na D-line) - Liquid |
298.15 |
0.0000 |
1.394 |
298.15 |
0.0417 |
1.3949 |
298.15 |
0.1061 |
1.3963 |
298.15 |
0.2514 |
1.3996 |
298.15 |
0.3493 |
1.4019 |
298.15 |
0.4771 |
1.4051 |
298.15 |
0.5563 |
1.4072 |
298.15 |
0.6462 |
1.4096 |
298.15 |
0.7343 |
1.4121 |
298.15 |
0.8244 |
1.4147 |
298.15 |
0.9112 |
1.4172 |
298.15 |
0.9891 |
1.4196 |
298.15 |
1.0000 |
1.4199 |
313.15 |
0.0000 |
1.3857 |
313.15 |
0.0475 |
1.3867 |
313.15 |
0.1318 |
1.3886 |
313.15 |
0.2390 |
1.3912 |
313.15 |
0.3413 |
1.3938 |
313.15 |
0.4574 |
1.3968 |
313.15 |
0.5546 |
1.3995 |
313.15 |
0.6429 |
1.402 |
313.15 |
0.7326 |
1.4045 |
313.15 |
0.8209 |
1.4071 |
313.15 |
0.9121 |
1.4099 |
313.15 |
0.9525 |
1.4111 |
313.15 |
1.0000 |
1.4126 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1,4-Dioxane (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0000 |
867.4 |
298.15 |
0.0417 |
872.75 |
298.15 |
0.1061 |
881.2 |
298.15 |
0.2514 |
901.2 |
298.15 |
0.3493 |
915.42 |
298.15 |
0.4771 |
934.94 |
298.15 |
0.5563 |
947.61 |
298.15 |
0.6462 |
962.58 |
298.15 |
0.7343 |
977.89 |
298.15 |
0.8244 |
994.21 |
298.15 |
0.9112 |
1010.56 |
298.15 |
0.9891 |
1025.72 |
298.15 |
1.0000 |
1027.87 |
313.15 |
0.0000 |
850.13 |
313.15 |
0.0475 |
856.2 |
313.15 |
0.1318 |
867.4 |
313.15 |
0.2390 |
882.36 |
313.15 |
0.3413 |
897.3 |
313.15 |
0.4574 |
915.03 |
313.15 |
0.5546 |
930.53 |
313.15 |
0.6429 |
945.17 |
313.15 |
0.7326 |
960.65 |
313.15 |
0.8209 |
976.52 |
313.15 |
0.9121 |
993.58 |
313.15 |
0.9525 |
1001.37 |
313.15 |
1.0000 |
1010.69 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1,4-Dioxane (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0522 |
874.11 |
0.0886 |
878.88 |
0.1892 |
892.48 |
0.2923 |
907.06 |
0.3647 |
917.71 |
0.4928 |
937.42 |
0.6155 |
957.41 |
0.7149 |
974.47 |
0.8019 |
990.07 |
0.9068 |
1009.72 |
0.9410 |
1016.33 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1,4-Dioxane (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0000 |
867.4 |
298.15 |
0.0417 |
872.75 |
298.15 |
0.1061 |
881.2 |
298.15 |
0.2514 |
901.2 |
298.15 |
0.3493 |
915.42 |
298.15 |
0.4771 |
934.94 |
298.15 |
0.5563 |
947.61 |
298.15 |
0.6462 |
962.58 |
298.15 |
0.7343 |
977.89 |
298.15 |
0.8244 |
994.21 |
298.15 |
0.9112 |
1010.56 |
298.15 |
0.9891 |
1025.72 |
298.15 |
1.0000 |
1027.87 |
313.15 |
0.0000 |
850.13 |
313.15 |
0.0475 |
856.2 |
313.15 |
0.1318 |
867.4 |
313.15 |
0.2390 |
882.36 |
313.15 |
0.3413 |
897.3 |
313.15 |
0.4574 |
915.03 |
313.15 |
0.5546 |
930.53 |
313.15 |
0.6429 |
945.17 |
313.15 |
0.7326 |
960.65 |
313.15 |
0.8209 |
976.52 |
313.15 |
0.9121 |
993.58 |
313.15 |
0.9525 |
1001.37 |
313.15 |
1.0000 |
1010.69 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1,4-Dioxane (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0522 |
874.11 |
0.0886 |
878.88 |
0.1892 |
892.48 |
0.2923 |
907.06 |
0.3647 |
917.71 |
0.4928 |
937.42 |
0.6155 |
957.41 |
0.7149 |
974.47 |
0.8019 |
990.07 |
0.9068 |
1009.72 |
0.9410 |
1016.33 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1,4-Dioxane (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
298.15 |
0.0417 |
0.0221 |
298.15 |
0.1061 |
0.0225 |
298.15 |
0.2514 |
0.0235 |
298.15 |
0.3493 |
0.0242 |
298.15 |
0.4771 |
0.0251 |
298.15 |
0.5563 |
0.0259 |
298.15 |
0.6462 |
0.0268 |
298.15 |
0.7343 |
0.0279 |
298.15 |
0.8244 |
0.0293 |
298.15 |
0.9112 |
0.0309 |
298.15 |
0.9891 |
0.0326 |
313.15 |
0.0475 |
0.0197 |
313.15 |
0.1318 |
0.0204 |
313.15 |
0.2390 |
0.0213 |
313.15 |
0.3414 |
0.0222 |
313.15 |
0.4574 |
0.0232 |
313.15 |
0.5546 |
0.0241 |
313.15 |
0.6429 |
0.0249 |
313.15 |
0.7326 |
0.0260 |
313.15 |
0.8209 |
0.0272 |
313.15 |
0.9121 |
0.0289 |
313.15 |
0.9525 |
0.0297 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1,4-Dioxane (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
298.15 |
0.0417 |
0.0221 |
298.15 |
0.1061 |
0.0225 |
298.15 |
0.2514 |
0.0235 |
298.15 |
0.3493 |
0.0242 |
298.15 |
0.4771 |
0.0251 |
298.15 |
0.5563 |
0.0259 |
298.15 |
0.6462 |
0.0268 |
298.15 |
0.7343 |
0.0279 |
298.15 |
0.8244 |
0.0293 |
298.15 |
0.9112 |
0.0309 |
298.15 |
0.9891 |
0.0326 |
313.15 |
0.0475 |
0.0197 |
313.15 |
0.1318 |
0.0204 |
313.15 |
0.2390 |
0.0213 |
313.15 |
0.3414 |
0.0222 |
313.15 |
0.4574 |
0.0232 |
313.15 |
0.5546 |
0.0241 |
313.15 |
0.6429 |
0.0249 |
313.15 |
0.7326 |
0.0260 |
313.15 |
0.8209 |
0.0272 |
313.15 |
0.9121 |
0.0289 |
313.15 |
0.9525 |
0.0297 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
40 (Liquid)
Mole fraction of 1,4-Dioxane (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0980 |
315.61 |
0.1650 |
316.96 |
0.2703 |
317.92 |
0.3581 |
320.14 |
0.4779 |
321.89 |
0.5845 |
324.41 |
0.6429 |
326.68 |
0.7167 |
329.39 |
0.7792 |
332.04 |
0.8404 |
334.59 |
0.8871 |
337.31 |
0.9360 |
340.49 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of 1,4-Dioxane (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0508 |
342.05 |
0.1615 |
343.80 |
0.2636 |
345.38 |
0.3544 |
347.17 |
0.4805 |
350.10 |
0.5745 |
352.15 |
0.6201 |
353.96 |
0.7162 |
356.78 |
0.7741 |
358.93 |
0.8284 |
361.90 |
0.8640 |
363.74 |
0.9218 |
367.88 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
40 (Liquid)
Mole fraction of 1,4-Dioxane (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0980 |
315.61 |
0.1650 |
316.96 |
0.2703 |
317.92 |
0.3581 |
320.14 |
0.4779 |
321.89 |
0.5845 |
324.41 |
0.6429 |
326.68 |
0.7167 |
329.39 |
0.7792 |
332.04 |
0.8404 |
334.59 |
0.8871 |
337.31 |
0.9360 |
340.49 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of 1,4-Dioxane (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0508 |
342.05 |
0.1615 |
343.80 |
0.2636 |
345.38 |
0.3544 |
347.17 |
0.4805 |
350.10 |
0.5745 |
352.15 |
0.6201 |
353.96 |
0.7162 |
356.78 |
0.7741 |
358.93 |
0.8284 |
361.90 |
0.8640 |
363.74 |
0.9218 |
367.88 |
Sources