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 |
0.0613 |
0.0246 |
0.1281 |
0.0523 |
0.2289 |
0.1011 |
0.3157 |
0.1361 |
0.4371 |
0.1884 |
0.5748 |
0.2795 |
0.6088 |
0.3019 |
0.6813 |
0.3619 |
0.7357 |
0.4167 |
0.8101 |
0.5038 |
0.8530 |
0.5756 |
0.9226 |
0.7249 |
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 |
0.0601 |
0.0293 |
0.1254 |
0.0592 |
0.2256 |
0.1091 |
0.3074 |
0.1491 |
0.4351 |
0.2124 |
0.5578 |
0.3068 |
0.6145 |
0.3453 |
0.6779 |
0.4033 |
0.7300 |
0.4445 |
0.8000 |
0.5392 |
0.8586 |
0.6223 |
0.9188 |
0.7594 |
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 |
0.0613 |
0.0246 |
0.1281 |
0.0523 |
0.2289 |
0.1011 |
0.3157 |
0.1361 |
0.4371 |
0.1884 |
0.5748 |
0.2795 |
0.6088 |
0.3019 |
0.6813 |
0.3619 |
0.7357 |
0.4167 |
0.8101 |
0.5038 |
0.8530 |
0.5756 |
0.9226 |
0.7249 |
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 |
0.0601 |
0.0293 |
0.1254 |
0.0592 |
0.2256 |
0.1091 |
0.3074 |
0.1491 |
0.4351 |
0.2124 |
0.5578 |
0.3068 |
0.6145 |
0.3453 |
0.6779 |
0.4033 |
0.7300 |
0.4445 |
0.8000 |
0.5392 |
0.8586 |
0.6223 |
0.9188 |
0.7594 |
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 |
1.3953 |
298.15 |
0.0450 |
1.3962 |
298.15 |
0.1196 |
1.3976 |
298.15 |
0.2433 |
1.4002 |
298.15 |
0.3412 |
1.4024 |
298.15 |
0.4407 |
1.4047 |
298.15 |
0.5447 |
1.4072 |
298.15 |
0.6463 |
1.4098 |
298.15 |
0.7370 |
1.4123 |
298.15 |
0.8305 |
1.4149 |
298.15 |
0.9157 |
1.4174 |
298.15 |
0.9515 |
1.4185 |
298.15 |
1.0000 |
1.4199 |
313.15 |
0.0000 |
1.3869 |
313.15 |
0.0474 |
1.3878 |
313.15 |
0.1492 |
1.39 |
313.15 |
0.2654 |
1.3926 |
313.15 |
0.3687 |
1.395 |
313.15 |
0.4565 |
1.3972 |
313.15 |
0.5541 |
1.3997 |
313.15 |
0.6426 |
1.4021 |
313.15 |
0.7423 |
1.4049 |
313.15 |
0.8326 |
1.4075 |
313.15 |
0.9112 |
1.4099 |
313.15 |
0.9606 |
1.4114 |
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 |
1.3953 |
298.15 |
0.0450 |
1.3962 |
298.15 |
0.1196 |
1.3976 |
298.15 |
0.2433 |
1.4002 |
298.15 |
0.3412 |
1.4024 |
298.15 |
0.4407 |
1.4047 |
298.15 |
0.5447 |
1.4072 |
298.15 |
0.6463 |
1.4098 |
298.15 |
0.7370 |
1.4123 |
298.15 |
0.8305 |
1.4149 |
298.15 |
0.9157 |
1.4174 |
298.15 |
0.9515 |
1.4185 |
298.15 |
1.0000 |
1.4199 |
313.15 |
0.0000 |
1.3869 |
313.15 |
0.0474 |
1.3878 |
313.15 |
0.1492 |
1.39 |
313.15 |
0.2654 |
1.3926 |
313.15 |
0.3687 |
1.395 |
313.15 |
0.4565 |
1.3972 |
313.15 |
0.5541 |
1.3997 |
313.15 |
0.6426 |
1.4021 |
313.15 |
0.7423 |
1.4049 |
313.15 |
0.8326 |
1.4075 |
313.15 |
0.9112 |
1.4099 |
313.15 |
0.9606 |
1.4114 |
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 |
871.13 |
298.15 |
0.0450 |
876.79 |
298.15 |
0.1196 |
886.36 |
298.15 |
0.2433 |
902.87 |
298.15 |
0.3412 |
916.58 |
298.15 |
0.4407 |
931.19 |
298.15 |
0.5447 |
947.22 |
298.15 |
0.6463 |
963.67 |
298.15 |
0.7370 |
979.04 |
298.15 |
0.8305 |
995.63 |
298.15 |
0.9157 |
1011.45 |
298.15 |
0.9515 |
1018.31 |
298.15 |
1.0000 |
1027.87 |
313.15 |
0.0000 |
853.51 |
313.15 |
0.0474 |
859.42 |
313.15 |
0.1492 |
872.58 |
313.15 |
0.2654 |
888.36 |
313.15 |
0.3687 |
903.12 |
313.15 |
0.4565 |
916.21 |
313.15 |
0.5541 |
931.39 |
313.15 |
0.6426 |
945.76 |
313.15 |
0.7423 |
962.69 |
313.15 |
0.8326 |
978.76 |
313.15 |
0.9112 |
993.38 |
313.15 |
0.9606 |
1002.9 |
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 |
0.0529 |
877.81 |
0.1009 |
883.95 |
0.2001 |
896.98 |
0.3003 |
910.79 |
0.3957 |
924.5 |
0.5022 |
940.58 |
0.5945 |
955.19 |
0.7005 |
972.78 |
0.7926 |
988.8 |
0.8978 |
1008.04 |
0.9371 |
1015.61 |
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 |
871.13 |
298.15 |
0.0450 |
876.79 |
298.15 |
0.1196 |
886.36 |
298.15 |
0.2433 |
902.87 |
298.15 |
0.3412 |
916.58 |
298.15 |
0.4407 |
931.19 |
298.15 |
0.5447 |
947.22 |
298.15 |
0.6463 |
963.67 |
298.15 |
0.7370 |
979.04 |
298.15 |
0.8305 |
995.63 |
298.15 |
0.9157 |
1011.45 |
298.15 |
0.9515 |
1018.31 |
298.15 |
1.0000 |
1027.87 |
313.15 |
0.0000 |
853.51 |
313.15 |
0.0474 |
859.42 |
313.15 |
0.1492 |
872.58 |
313.15 |
0.2654 |
888.36 |
313.15 |
0.3687 |
903.12 |
313.15 |
0.4565 |
916.21 |
313.15 |
0.5541 |
931.39 |
313.15 |
0.6426 |
945.76 |
313.15 |
0.7423 |
962.69 |
313.15 |
0.8326 |
978.76 |
313.15 |
0.9112 |
993.38 |
313.15 |
0.9606 |
1002.9 |
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 |
0.0529 |
877.81 |
0.1009 |
883.95 |
0.2001 |
896.98 |
0.3003 |
910.79 |
0.3957 |
924.5 |
0.5022 |
940.58 |
0.5945 |
955.19 |
0.7005 |
972.78 |
0.7926 |
988.8 |
0.8978 |
1008.04 |
0.9371 |
1015.61 |
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 |
0.0450 |
0.0222 |
298.15 |
0.1196 |
0.0228 |
298.15 |
0.2433 |
0.0237 |
298.15 |
0.3412 |
0.0243 |
298.15 |
0.4407 |
0.0250 |
298.15 |
0.5447 |
0.0259 |
298.15 |
0.6429 |
0.0269 |
298.15 |
0.7370 |
0.0280 |
298.15 |
0.8305 |
0.0293 |
298.15 |
0.9157 |
0.0308 |
298.15 |
0.9515 |
0.0316 |
313.15 |
0.0474 |
0.0195 |
313.15 |
0.1492 |
0.0203 |
313.15 |
0.2654 |
0.0213 |
313.15 |
0.3687 |
0.0222 |
313.15 |
0.4565 |
0.0230 |
313.15 |
0.5541 |
0.0240 |
313.15 |
0.6426 |
0.0249 |
313.15 |
0.7423 |
0.0261 |
313.15 |
0.8326 |
0.0274 |
313.15 |
0.9112 |
0.0289 |
313.15 |
0.9606 |
0.0299 |
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 |
0.0450 |
0.0222 |
298.15 |
0.1196 |
0.0228 |
298.15 |
0.2433 |
0.0237 |
298.15 |
0.3412 |
0.0243 |
298.15 |
0.4407 |
0.0250 |
298.15 |
0.5447 |
0.0259 |
298.15 |
0.6429 |
0.0269 |
298.15 |
0.7370 |
0.0280 |
298.15 |
0.8305 |
0.0293 |
298.15 |
0.9157 |
0.0308 |
298.15 |
0.9515 |
0.0316 |
313.15 |
0.0474 |
0.0195 |
313.15 |
0.1492 |
0.0203 |
313.15 |
0.2654 |
0.0213 |
313.15 |
0.3687 |
0.0222 |
313.15 |
0.4565 |
0.0230 |
313.15 |
0.5541 |
0.0240 |
313.15 |
0.6426 |
0.0249 |
313.15 |
0.7423 |
0.0261 |
313.15 |
0.8326 |
0.0274 |
313.15 |
0.9112 |
0.0289 |
313.15 |
0.9606 |
0.0299 |
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 |
0.0613 |
316.33 |
0.1281 |
317.50 |
0.2289 |
319.09 |
0.3157 |
320.61 |
0.4371 |
322.93 |
0.5748 |
326.12 |
0.6088 |
326.83 |
0.6813 |
328.99 |
0.7357 |
330.92 |
0.8101 |
333.92 |
0.8530 |
336.17 |
0.9226 |
340.03 |
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 |
0.0601 |
342.77 |
0.1254 |
343.83 |
0.2256 |
345.82 |
0.3074 |
347.17 |
0.4351 |
349.81 |
0.5578 |
353.07 |
0.6145 |
354.45 |
0.6779 |
356.55 |
0.7300 |
358.34 |
0.8000 |
361.10 |
0.8586 |
364.16 |
0.9188 |
367.96 |
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 |
0.0613 |
316.33 |
0.1281 |
317.50 |
0.2289 |
319.09 |
0.3157 |
320.61 |
0.4371 |
322.93 |
0.5748 |
326.12 |
0.6088 |
326.83 |
0.6813 |
328.99 |
0.7357 |
330.92 |
0.8101 |
333.92 |
0.8530 |
336.17 |
0.9226 |
340.03 |
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 |
0.0601 |
342.77 |
0.1254 |
343.83 |
0.2256 |
345.82 |
0.3074 |
347.17 |
0.4351 |
349.81 |
0.5578 |
353.07 |
0.6145 |
354.45 |
0.6779 |
356.55 |
0.7300 |
358.34 |
0.8000 |
361.10 |
0.8586 |
364.16 |
0.9188 |
367.96 |
Sources