Mixture of Propane, 1-chloro-2-methyl- + 1,4-Dioxane

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Propane, 1-chloro-2-methyl-

Name
Propane, 1-chloro-2-methyl-
InChI
InChI=1S/C4H9Cl/c1-4(2)3-5/h4H,3H2,1-2H3
InChI Key
QTBFPMKWQKYFLR-UHFFFAOYSA-N
Formula
C4H9Cl
SMILES
CC(C)CCl
Mol. Weight (g/mol)
92.57
CAS
513-36-0

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
0.0613 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:

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:

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