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

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Butane, 1-chloro-

Name
Butane, 1-chloro-
InChI
InChI=1S/C4H9Cl/c1-2-3-4-5/h2-4H2,1H3
InChI Key
VFWCMGCRMGJXDK-UHFFFAOYSA-N
Formula
C4H9Cl
SMILES
CCCCCl
Mol. Weight (g/mol)
92.57
CAS
109-69-3

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
0.0459 0.0259
0.1087 0.0620
0.1892 0.1078
0.2117 0.1210
0.3047 0.1744
0.4315 0.2539
0.5225 0.3149
0.6099 0.3833
0.6822 0.4456
0.7616 0.5336
0.8129 0.6135
0.9005 0.7393
0.9400 0.8368

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
0.0424 0.0264
0.1031 0.0634
0.2075 0.1255
0.2931 0.1814
0.4225 0.2693
0.5256 0.3567
0.6150 0.4180
0.6712 0.4858
0.7441 0.5475
0.7577 0.5590
0.8339 0.6608
0.8558 0.7010
0.8815 0.7335
0.9378 0.8385

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
0.0459 0.0259
0.1087 0.0620
0.1892 0.1078
0.2117 0.1210
0.3047 0.1744
0.4315 0.2539
0.5225 0.3149
0.6099 0.3833
0.6822 0.4456
0.7616 0.5336
0.8129 0.6135
0.9005 0.7393
0.9400 0.8368

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
0.0424 0.0264
0.1031 0.0634
0.2075 0.1255
0.2931 0.1814
0.4225 0.2693
0.5256 0.3567
0.6150 0.4180
0.6712 0.4858
0.7441 0.5475
0.7577 0.5590
0.8339 0.6608
0.8558 0.7010
0.8815 0.7335
0.9378 0.8385

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 1.3995
298.15 0.0418 1.4001
298.15 0.1141 1.4012
298.15 0.2426 1.4033
298.15 0.3358 1.4049
298.15 0.4518 1.4071
298.15 0.5509 1.4091
298.15 0.5914 1.4099
298.15 0.7380 1.4132
298.15 0.8235 1.4153
298.15 0.9104 1.4175
298.15 0.9870 1.4196
298.15 1.0000 1.4199
313.15 0.0000 1.3913
313.15 0.0344 1.3919
313.15 0.1170 1.3932
313.15 0.2279 1.3951
313.15 0.3499 1.3973
313.15 0.4442 1.3992
313.15 0.5500 1.4014
313.15 0.6450 1.4035
313.15 0.7456 1.4059
313.15 0.8238 1.4079
313.15 0.9143 1.4102
313.15 0.9636 1.4116
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 1.3995
298.15 0.0418 1.4001
298.15 0.1141 1.4012
298.15 0.2426 1.4033
298.15 0.3358 1.4049
298.15 0.4518 1.4071
298.15 0.5509 1.4091
298.15 0.5914 1.4099
298.15 0.7380 1.4132
298.15 0.8235 1.4153
298.15 0.9104 1.4175
298.15 0.9870 1.4196
298.15 1.0000 1.4199
313.15 0.0000 1.3913
313.15 0.0344 1.3919
313.15 0.1170 1.3932
313.15 0.2279 1.3951
313.15 0.3499 1.3973
313.15 0.4442 1.3992
313.15 0.5500 1.4014
313.15 0.6450 1.4035
313.15 0.7456 1.4059
313.15 0.8238 1.4079
313.15 0.9143 1.4102
313.15 0.9636 1.4116
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 880.69
298.15 0.0418 885.54
298.15 0.1141 894.14
298.15 0.2426 910.06
298.15 0.3358 922.21
298.15 0.4518 938.11
298.15 0.5509 952.44
298.15 0.5914 958.52
298.15 0.7380 981.64
298.15 0.8235 995.99
298.15 0.9104 1011.29
298.15 0.9870 1025.41
298.15 1.0000 1027.87
313.15 0.0000 863.82
313.15 0.0344 867.83
313.15 0.1170 877.61
313.15 0.2279 891.26
313.15 0.3499 907.15
313.15 0.4442 920.15
313.15 0.5500 935.51
313.15 0.6450 950.02
313.15 0.7456 966.15
313.15 0.8238 979.22
313.15 0.9143 995.01
313.15 0.9636 1003.94
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
0.0422 885.61
0.0947 891.8
0.2055 905.35
0.2766 914.45
0.4083 932.02
0.4852 942.87
0.6082 961.08
0.6587 968.92
0.7939 990.92
0.8940 1008.37
0.9509 1018.71

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 880.69
298.15 0.0418 885.54
298.15 0.1141 894.14
298.15 0.2426 910.06
298.15 0.3358 922.21
298.15 0.4518 938.11
298.15 0.5509 952.44
298.15 0.5914 958.52
298.15 0.7380 981.64
298.15 0.8235 995.99
298.15 0.9104 1011.29
298.15 0.9870 1025.41
298.15 1.0000 1027.87
313.15 0.0000 863.82
313.15 0.0344 867.83
313.15 0.1170 877.61
313.15 0.2279 891.26
313.15 0.3499 907.15
313.15 0.4442 920.15
313.15 0.5500 935.51
313.15 0.6450 950.02
313.15 0.7456 966.15
313.15 0.8238 979.22
313.15 0.9143 995.01
313.15 0.9636 1003.94
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
0.0422 885.61
0.0947 891.8
0.2055 905.35
0.2766 914.45
0.4083 932.02
0.4852 942.87
0.6082 961.08
0.6587 968.92
0.7939 990.92
0.8940 1008.37
0.9509 1018.71

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 0.0418 0.0236
298.15 0.1141 0.0240
298.15 0.2426 0.0247
298.15 0.3358 0.0253
298.15 0.4518 0.0260
298.15 0.5509 0.0268
298.15 0.5914 0.0272
298.15 0.7380 0.0287
298.15 0.8235 0.0298
298.15 0.9104 0.0312
298.15 0.9870 0.0326
313.15 0.0344 0.0217
313.15 0.1170 0.0221
313.15 0.2279 0.0228
313.15 0.3499 0.0236
313.15 0.4442 0.0242
313.15 0.5500 0.0250
313.15 0.6450 0.0258
313.15 0.7456 0.0269
313.15 0.8238 0.0279
313.15 0.9143 0.0293
313.15 0.9636 0.0301

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 0.0418 0.0236
298.15 0.1141 0.0240
298.15 0.2426 0.0247
298.15 0.3358 0.0253
298.15 0.4518 0.0260
298.15 0.5509 0.0268
298.15 0.5914 0.0272
298.15 0.7380 0.0287
298.15 0.8235 0.0298
298.15 0.9104 0.0312
298.15 0.9870 0.0326
313.15 0.0344 0.0217
313.15 0.1170 0.0221
313.15 0.2279 0.0228
313.15 0.3499 0.0236
313.15 0.4442 0.0242
313.15 0.5500 0.0250
313.15 0.6450 0.0258
313.15 0.7456 0.0269
313.15 0.8238 0.0279
313.15 0.9143 0.0293
313.15 0.9636 0.0301

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
0.0459 324.94
0.1087 325.49
0.1892 326.44
0.2117 326.73
0.3047 327.83
0.4315 329.80
0.5225 331.24
0.6099 332.84
0.6822 334.32
0.7616 336.55
0.8129 338.56
0.9005 341.15
0.9400 343.19

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
0.0424 352.45
0.1031 353.34
0.2075 354.17
0.2931 355.64
0.4225 356.98
0.5256 358.97
0.6150 360.71
0.6712 361.97
0.7441 363.72
0.7577 364.32
0.8339 366.68
0.8558 367.43
0.8815 368.33
0.9378 371.01

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
0.0459 324.94
0.1087 325.49
0.1892 326.44
0.2117 326.73
0.3047 327.83
0.4315 329.80
0.5225 331.24
0.6099 332.84
0.6822 334.32
0.7616 336.55
0.8129 338.56
0.9005 341.15
0.9400 343.19

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
0.0424 352.45
0.1031 353.34
0.2075 354.17
0.2931 355.64
0.4225 356.98
0.5256 358.97
0.6150 360.71
0.6712 361.97
0.7441 363.72
0.7577 364.32
0.8339 366.68
0.8558 367.43
0.8815 368.33
0.9378 371.01

Sources