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

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Pentane, 1-chloro-

Name
Pentane, 1-chloro-
InChI
InChI=1S/C5H11Cl/c1-2-3-4-5-6/h2-5H2,1H3
InChI Key
SQCZQTSHSZLZIQ-UHFFFAOYSA-N
Formula
C5H11Cl
SMILES
CCCCCCl
Mol. Weight (g/mol)
106.59
CAS
543-59-9

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 (2)
  2. ν - Kinematic viscosity, m2/s (2)
  3. Pvap - Vapor or sublimation pressure, kPa (2)
  4. ρl - Mass density, kg/m3 (2)

Mole fraction of 1,4-Dioxane (2) [ref]

Fixed Measured
Mole fraction of 1,4-Dioxane (2) - Liquid Temperature, K - Liquid Mole fraction of 1,4-Dioxane (2) - Gas
0.0000 298.15 0.0000
0.0000 313.15 0.0000
0.0000 328.15 0.0000
0.0795 298.15 0.1345
0.0798 313.15 0.1337
0.0799 328.15 0.1253
0.1551 328.15 0.2256
0.1596 313.15 0.2407
0.1635 298.15 0.2563
0.2098 328.15 0.2903
0.2100 313.15 0.3001
0.2102 298.15 0.3010
0.2702 298.15 0.3596
0.2702 313.15 0.3562
0.2734 328.15 0.3568
0.3816 328.15 0.4506
0.3881 313.15 0.4694
0.3946 298.15 0.4703
0.4700 298.15 0.5306
0.4701 328.15 0.5338
0.4702 313.15 0.5324
0.5691 328.15 0.6131
0.5697 298.15 0.6024
0.5697 313.15 0.5982
0.7058 328.15 0.7114
0.7063 313.15 0.7120
0.7074 298.15 0.7039
0.7949 328.15 0.7780
0.7987 313.15 0.7803
0.8015 298.15 0.7804
0.8412 328.15 0.8264
0.8417 313.15 0.8189
0.8422 298.15 0.8103
0.9196 298.15 0.8905
0.9196 313.15 0.8957
0.9198 328.15 0.8999
0.9724 328.15 0.9640
0.9726 313.15 0.9620
0.9728 298.15 0.9595
1.0000 298.15 1.0000
1.0000 313.15 1.0000
1.0000 328.15 1.0000

Mole fraction of 1,4-Dioxane (2) [ref]

Fixed Measured
Mole fraction of 1,4-Dioxane (2) - Liquid Temperature, K - Liquid Mole fraction of 1,4-Dioxane (2) - Gas
0.0000 298.15 0.0000
0.0000 313.15 0.0000
0.0000 328.15 0.0000
0.0795 298.15 0.1345
0.0798 313.15 0.1337
0.0799 328.15 0.1253
0.1551 328.15 0.2256
0.1596 313.15 0.2407
0.1635 298.15 0.2563
0.2098 328.15 0.2903
0.2100 313.15 0.3001
0.2102 298.15 0.3010
0.2702 298.15 0.3596
0.2702 313.15 0.3562
0.2734 328.15 0.3568
0.3816 328.15 0.4506
0.3881 313.15 0.4694
0.3946 298.15 0.4703
0.4700 298.15 0.5306
0.4701 328.15 0.5338
0.4702 313.15 0.5324
0.5691 328.15 0.6131
0.5697 298.15 0.6024
0.5697 313.15 0.5982
0.7058 328.15 0.7114
0.7063 313.15 0.7120
0.7074 298.15 0.7039
0.7949 328.15 0.7780
0.7987 313.15 0.7803
0.8015 298.15 0.7804
0.8412 328.15 0.8264
0.8417 313.15 0.8189
0.8422 298.15 0.8103
0.9196 298.15 0.8905
0.9196 313.15 0.8957
0.9198 328.15 0.8999
0.9724 328.15 0.9640
0.9726 313.15 0.9620
0.9728 298.15 0.9595
1.0000 298.15 1.0000
1.0000 313.15 1.0000
1.0000 328.15 1.0000

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,4-Dioxane (2) - Liquid Kinematic viscosity, m2/s - Liquid
298.15 0.0000 6.2790e-07
298.15 0.0533 6.3710e-07
298.15 0.0964 6.4480e-07
298.15 0.1997 6.6490e-07
298.15 0.2758 6.8180e-07
298.15 0.3815 7.0990e-07
298.15 0.4966 7.4910e-07
298.15 0.6003 7.9500e-07
298.15 0.7046 8.5490e-07
298.15 0.7615 8.9500e-07
298.15 0.8986 1.0206e-06
298.15 0.9520 1.0835e-06
298.15 1.0000 1.1487e-06
313.15 0.0000 5.4210e-07
313.15 0.0533 5.4970e-07
313.15 0.0964 5.5660e-07
313.15 0.1997 5.7600e-07
313.15 0.2758 5.9300e-07
313.15 0.3815 6.2090e-07
313.15 0.4966 6.5650e-07
313.15 0.6003 6.9570e-07
313.15 0.7046 7.4280e-07
313.15 0.7615 7.7120e-07
313.15 0.8986 8.5040e-07
313.15 0.9520 8.8570e-07
313.15 1.0000 9.2000e-07

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,4-Dioxane (2) - Liquid Kinematic viscosity, m2/s - Liquid
298.15 0.0000 6.2790e-07
298.15 0.0533 6.3710e-07
298.15 0.0964 6.4480e-07
298.15 0.1997 6.6490e-07
298.15 0.2758 6.8180e-07
298.15 0.3815 7.0990e-07
298.15 0.4966 7.4910e-07
298.15 0.6003 7.9500e-07
298.15 0.7046 8.5490e-07
298.15 0.7615 8.9500e-07
298.15 0.8986 1.0206e-06
298.15 0.9520 1.0835e-06
298.15 1.0000 1.1487e-06
313.15 0.0000 5.4210e-07
313.15 0.0533 5.4970e-07
313.15 0.0964 5.5660e-07
313.15 0.1997 5.7600e-07
313.15 0.2758 5.9300e-07
313.15 0.3815 6.2090e-07
313.15 0.4966 6.5650e-07
313.15 0.6003 6.9570e-07
313.15 0.7046 7.4280e-07
313.15 0.7615 7.7120e-07
313.15 0.8986 8.5040e-07
313.15 0.9520 8.8570e-07
313.15 1.0000 9.2000e-07

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of 1,4-Dioxane (2) - Liquid Temperature, K - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 298.15 4.05
0.0000 313.15 8.45
0.0000 328.15 16.40
0.0795 298.15 4.32
0.0798 313.15 8.99
0.0799 328.15 17.26
0.1551 328.15 17.99
0.1596 313.15 9.41
0.1635 298.15 4.55
0.2098 328.15 18.45
0.2100 313.15 9.71
0.2102 298.15 4.68
0.2702 298.15 4.79
0.2702 313.15 9.98
0.2734 328.15 18.93
0.3816 328.15 19.64
0.3881 313.15 10.40
0.3946 298.15 5.08
0.4700 298.15 5.12
0.4701 328.15 20.02
0.4702 313.15 10.57
0.5691 328.15 20.37
0.5697 298.15 5.21
0.5697 313.15 10.82
0.7058 328.15 20.63
0.7063 313.15 10.83
0.7074 298.15 5.28
0.7949 328.15 20.57
0.7987 313.15 10.76
0.8015 298.15 5.21
0.8412 328.15 20.45
0.8417 313.15 10.70
0.8422 298.15 5.17
0.9196 298.15 5.09
0.9196 313.15 10.53
0.9198 328.15 20.10
0.9724 328.15 19.81
0.9726 313.15 10.36
0.9728 298.15 4.97
1.0000 298.15 4.90
1.0000 313.15 10.17
1.0000 328.15 19.54

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of 1,4-Dioxane (2) - Liquid Temperature, K - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 298.15 4.05
0.0000 313.15 8.45
0.0000 328.15 16.40
0.0795 298.15 4.32
0.0798 313.15 8.99
0.0799 328.15 17.26
0.1551 328.15 17.99
0.1596 313.15 9.41
0.1635 298.15 4.55
0.2098 328.15 18.45
0.2100 313.15 9.71
0.2102 298.15 4.68
0.2702 298.15 4.79
0.2702 313.15 9.98
0.2734 328.15 18.93
0.3816 328.15 19.64
0.3881 313.15 10.40
0.3946 298.15 5.08
0.4700 298.15 5.12
0.4701 328.15 20.02
0.4702 313.15 10.57
0.5691 328.15 20.37
0.5697 298.15 5.21
0.5697 313.15 10.82
0.7058 328.15 20.63
0.7063 313.15 10.83
0.7074 298.15 5.28
0.7949 328.15 20.57
0.7987 313.15 10.76
0.8015 298.15 5.21
0.8412 328.15 20.45
0.8417 313.15 10.70
0.8422 298.15 5.17
0.9196 298.15 5.09
0.9196 313.15 10.53
0.9198 328.15 20.10
0.9724 328.15 19.81
0.9726 313.15 10.36
0.9728 298.15 4.97
1.0000 298.15 4.90
1.0000 313.15 10.17
1.0000 328.15 19.54

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mass fraction of 1,4-Dioxane (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 877.05
298.15 0.0533 882.28
298.15 0.0964 886.79
298.15 0.1997 898.03
298.15 0.2758 906.86
298.15 0.3815 920.13
298.15 0.4966 935.79
298.15 0.6003 951.45
298.15 0.7046 968.65
298.15 0.7615 978.66
298.15 0.8986 1005.49
298.15 0.9520 1016.89
298.15 1.0000 1027.86
313.15 0.0000 861.46
313.15 0.0533 866.84
313.15 0.0964 871.18
313.15 0.1997 882.29
313.15 0.2758 891.06
313.15 0.3815 904.17
313.15 0.4966 919.73
313.15 0.6003 935.17
313.15 0.7046 952.34
313.15 0.7615 962.27
313.15 0.8986 988.71
313.15 0.9520 1000.0
313.15 1.0000 1010.65

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mass fraction of 1,4-Dioxane (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 877.05
298.15 0.0533 882.28
298.15 0.0964 886.79
298.15 0.1997 898.03
298.15 0.2758 906.86
298.15 0.3815 920.13
298.15 0.4966 935.79
298.15 0.6003 951.45
298.15 0.7046 968.65
298.15 0.7615 978.66
298.15 0.8986 1005.49
298.15 0.9520 1016.89
298.15 1.0000 1027.86
313.15 0.0000 861.46
313.15 0.0533 866.84
313.15 0.0964 871.18
313.15 0.1997 882.29
313.15 0.2758 891.06
313.15 0.3815 904.17
313.15 0.4966 919.73
313.15 0.6003 935.17
313.15 0.7046 952.34
313.15 0.7615 962.27
313.15 0.8986 988.71
313.15 0.9520 1000.0
313.15 1.0000 1010.65

Sources