Mixture of Butane, 2-chloro- + 1,4-Dioxane

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Butane, 2-chloro-

Name
Butane, 2-chloro-
InChI
InChI=1S/C4H9Cl/c1-3-4(2)5/h4H,3H2,1-2H3
InChI Key
BSPCSKHALVHRSR-UHFFFAOYSA-N
Formula
C4H9Cl
SMILES
CCC(C)Cl
Mol. Weight (g/mol)
92.57
CAS
78-86-4

1,4-Dioxane

Name
1,4-Dioxane
InChI
InChI=1S/C4H8O2/c1-2-6-4-3-5-1/h1-4H2
InChI Key
RYHBNJHYFVUHQT-UHFFFAOYSA-N
Formula
C4H8O2
SMILES
C1COCCO1
Mol. Weight (g/mol)
88.11
CAS
123-91-1
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Datasets

  1. Mole fraction (4)
  2. n0 - Refractive index (Na D-line) (2)
  3. ρl - Mass density, kg/m3 (4)
  4. γ - Surface tension liquid-gas, N/m (2)
  5. 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:

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:

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

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