Mixture of Tetrahydropyran + Hexane, 1-chloro-

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Tetrahydropyran

Name
Tetrahydropyran
InChI
InChI=1S/C5H10O/c1-2-4-6-5-3-1/h1-5H2
InChI Key
DHXVGJBLRPWPCS-UHFFFAOYSA-N
Formula
C5H10O
SMILES
C1CCOCC1
Mol. Weight (g/mol)
86.13
CAS
142-68-7

Hexane, 1-chloro-

Name
Hexane, 1-chloro-
InChI
InChI=1S/C6H13Cl/c1-2-3-4-5-6-7/h2-6H2,1H3
InChI Key
MLRVZFYXUZQSRU-UHFFFAOYSA-N
Formula
C6H13Cl
SMILES
CCCCCCCl
Mol. Weight (g/mol)
120.62
CAS
544-10-5
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Datasets

  1. Mole fraction (4)
  2. ν - Kinematic viscosity, m2/s (2)
  3. Pvap - Vapor or sublimation pressure, kPa (2)
  4. ρl - Mass density, kg/m3 (2)
  5. Tboil - Boiling temperature at pressure P, K (2)

Mole fraction of Tetrahydropyran (1) [ref]

Fixed Measured
Mole fraction of Tetrahydropyran (1) - Liquid Pressure, kPa - Gas Mole fraction of Tetrahydropyran (1) - Gas
0.0551 101.33 0.1359
0.0598 40.00 0.1653
0.0970 40.00 0.2695
0.1047 101.33 0.2301
0.1378 40.00 0.3503
0.1378 101.33 0.3293
0.1819 101.33 0.4117
0.1891 40.00 0.4634
0.2384 40.00 0.5360
0.2398 101.33 0.5053
0.2618 101.33 0.5438
0.2686 40.00 0.5851
0.3375 40.00 0.6811
0.3400 101.33 0.6405
0.3882 40.00 0.7355
0.3919 101.33 0.6999
0.4670 40.00 0.8039
0.4693 101.33 0.7717
0.5449 101.33 0.8248
0.5483 40.00 0.8576
0.6301 101.33 0.8772
0.6395 40.00 0.8973
0.7155 101.33 0.9147
0.7164 40.00 0.9342
0.8004 101.33 0.9528
0.8074 40.00 0.9668
0.8748 101.33 0.9785
0.8805 40.00 0.9805
0.9505 40.00 0.9900
0.9513 101.33 0.9909

Mole fraction of Tetrahydropyran (1) [ref]

Fixed Measured
Mole fraction of Tetrahydropyran (1) - Liquid Temperature, K - Gas Mole fraction of Tetrahydropyran (1) - Gas
0.0598 298.15 0.2476
0.0614 328.15 0.2008
0.1108 298.15 0.4182
0.1153 328.15 0.3532
0.1527 328.15 0.4499
0.1630 298.15 0.5479
0.2147 298.15 0.6320
0.2175 328.15 0.5793
0.2754 328.15 0.6487
0.2835 298.15 0.7293
0.3323 298.15 0.7708
0.3554 328.15 0.7393
0.4129 328.15 0.7907
0.4227 298.15 0.8384
0.4480 298.15 0.8658
0.4775 328.15 0.8451
0.5019 298.15 0.8797
0.5382 328.15 0.8707
0.5505 298.15 0.9068
0.6080 298.15 0.9303
0.6165 328.15 0.9100
0.7009 328.15 0.9443
0.7048 298.15 0.9591
0.7598 328.15 0.9606
0.7654 298.15 0.9770
0.8576 298.15 0.9850
0.8576 328.15 0.9827
0.9036 298.15 0.9900
0.9044 328.15 0.9890

Mole fraction of Tetrahydropyran (1) [ref]

Fixed Measured
Mole fraction of Tetrahydropyran (1) - Liquid Pressure, kPa - Gas Mole fraction of Tetrahydropyran (1) - Gas
0.0551 101.33 0.1359
0.0598 40.00 0.1653
0.0970 40.00 0.2695
0.1047 101.33 0.2301
0.1378 40.00 0.3503
0.1378 101.33 0.3293
0.1819 101.33 0.4117
0.1891 40.00 0.4634
0.2384 40.00 0.5360
0.2398 101.33 0.5053
0.2618 101.33 0.5438
0.2686 40.00 0.5851
0.3375 40.00 0.6811
0.3400 101.33 0.6405
0.3882 40.00 0.7355
0.3919 101.33 0.6999
0.4670 40.00 0.8039
0.4693 101.33 0.7717
0.5449 101.33 0.8248
0.5483 40.00 0.8576
0.6301 101.33 0.8772
0.6395 40.00 0.8973
0.7155 101.33 0.9147
0.7164 40.00 0.9342
0.8004 101.33 0.9528
0.8074 40.00 0.9668
0.8748 101.33 0.9785
0.8805 40.00 0.9805
0.9505 40.00 0.9900
0.9513 101.33 0.9909

Mole fraction of Tetrahydropyran (1) [ref]

Fixed Measured
Mole fraction of Tetrahydropyran (1) - Liquid Temperature, K - Gas Mole fraction of Tetrahydropyran (1) - Gas
0.0598 298.15 0.2476
0.0614 328.15 0.2008
0.1108 298.15 0.4182
0.1153 328.15 0.3532
0.1527 328.15 0.4499
0.1630 298.15 0.5479
0.2147 298.15 0.6320
0.2175 328.15 0.5793
0.2754 328.15 0.6487
0.2835 298.15 0.7293
0.3323 298.15 0.7708
0.3554 328.15 0.7393
0.4129 328.15 0.7907
0.4227 298.15 0.8384
0.4480 298.15 0.8658
0.4775 328.15 0.8451
0.5019 298.15 0.8797
0.5382 328.15 0.8707
0.5505 298.15 0.9068
0.6080 298.15 0.9303
0.6165 328.15 0.9100
0.7009 328.15 0.9443
0.7048 298.15 0.9591
0.7598 328.15 0.9606
0.7654 298.15 0.9770
0.8576 298.15 0.9850
0.8576 328.15 0.9827
0.9036 298.15 0.9900
0.9044 328.15 0.9890

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (1) - Liquid Kinematic viscosity, m2/s - Liquid
283.15 0.0000 9.4780e-07
283.15 0.0501 9.5130e-07
283.15 0.1152 9.5730e-07
283.15 0.2090 9.6710e-07
283.15 0.2924 9.7640e-07
283.15 0.4074 9.9000e-07
283.15 0.4975 1.0009e-06
283.15 0.5988 1.0150e-06
283.15 0.6961 1.0313e-06
283.15 0.7996 1.0536e-06
283.15 0.8975 1.0815e-06
283.15 0.9493 1.0999e-06
283.15 1.0000 1.1205e-06
298.15 0.0000 7.9480e-07
298.15 0.0501 7.9790e-07
298.15 0.1152 8.0220e-07
298.15 0.2090 8.0800e-07
298.15 0.2924 8.1380e-07
298.15 0.4074 8.2250e-07
298.15 0.4975 8.3060e-07
298.15 0.5988 8.4000e-07
298.15 0.6961 8.5150e-07
298.15 0.7996 8.6620e-07
298.15 0.8975 8.8520e-07
298.15 0.9493 8.9630e-07
298.15 1.0000 9.1000e-07
313.15 0.0000 6.7660e-07
313.15 0.0501 6.7860e-07
313.15 0.1152 6.8170e-07
313.15 0.2090 6.8630e-07
313.15 0.2924 6.9060e-07
313.15 0.4074 6.9660e-07
313.15 0.4975 7.0230e-07
313.15 0.5988 7.0920e-07
313.15 0.6961 7.1680e-07
313.15 0.7996 7.2760e-07
313.15 0.8975 7.3970e-07
313.15 0.9493 7.4750e-07
313.15 1.0000 7.5710e-07

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (1) - Liquid Kinematic viscosity, m2/s - Liquid
283.15 0.0000 9.4780e-07
283.15 0.0501 9.5130e-07
283.15 0.1152 9.5730e-07
283.15 0.2090 9.6710e-07
283.15 0.2924 9.7640e-07
283.15 0.4074 9.9000e-07
283.15 0.4975 1.0009e-06
283.15 0.5988 1.0150e-06
283.15 0.6961 1.0313e-06
283.15 0.7996 1.0536e-06
283.15 0.8975 1.0815e-06
283.15 0.9493 1.0999e-06
283.15 1.0000 1.1205e-06
298.15 0.0000 7.9480e-07
298.15 0.0501 7.9790e-07
298.15 0.1152 8.0220e-07
298.15 0.2090 8.0800e-07
298.15 0.2924 8.1380e-07
298.15 0.4074 8.2250e-07
298.15 0.4975 8.3060e-07
298.15 0.5988 8.4000e-07
298.15 0.6961 8.5150e-07
298.15 0.7996 8.6620e-07
298.15 0.8975 8.8520e-07
298.15 0.9493 8.9630e-07
298.15 1.0000 9.1000e-07
313.15 0.0000 6.7660e-07
313.15 0.0501 6.7860e-07
313.15 0.1152 6.8170e-07
313.15 0.2090 6.8630e-07
313.15 0.2924 6.9060e-07
313.15 0.4074 6.9660e-07
313.15 0.4975 7.0230e-07
313.15 0.5988 7.0920e-07
313.15 0.6961 7.1680e-07
313.15 0.7996 7.2760e-07
313.15 0.8975 7.3970e-07
313.15 0.9493 7.4750e-07
313.15 1.0000 7.5710e-07

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of Tetrahydropyran (1) - Liquid Temperature, K - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0598 298.15 1.50
0.0614 328.15 7.00
0.1108 298.15 1.83
0.1153 328.15 8.22
0.1527 328.15 9.10
0.1630 298.15 2.23
0.2147 298.15 2.60
0.2175 328.15 10.80
0.2754 328.15 12.35
0.2835 298.15 3.21
0.3323 298.15 3.66
0.3554 328.15 14.60
0.4129 328.15 16.14
0.4227 298.15 4.33
0.4480 298.15 4.70
0.4775 328.15 18.21
0.5019 298.15 5.00
0.5382 328.15 19.89
0.5505 298.15 5.50
0.6080 298.15 6.04
0.6165 328.15 22.29
0.7009 328.15 25.00
0.7048 298.15 6.92
0.7598 328.15 26.75
0.7654 298.15 7.41
0.8576 298.15 8.17
0.8576 328.15 29.63
0.9036 298.15 8.63
0.9044 328.15 30.95

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of Tetrahydropyran (1) - Liquid Temperature, K - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0598 298.15 1.50
0.0614 328.15 7.00
0.1108 298.15 1.83
0.1153 328.15 8.22
0.1527 328.15 9.10
0.1630 298.15 2.23
0.2147 298.15 2.60
0.2175 328.15 10.80
0.2754 328.15 12.35
0.2835 298.15 3.21
0.3323 298.15 3.66
0.3554 328.15 14.60
0.4129 328.15 16.14
0.4227 298.15 4.33
0.4480 298.15 4.70
0.4775 328.15 18.21
0.5019 298.15 5.00
0.5382 328.15 19.89
0.5505 298.15 5.50
0.6080 298.15 6.04
0.6165 328.15 22.29
0.7009 328.15 25.00
0.7048 298.15 6.92
0.7598 328.15 26.75
0.7654 298.15 7.41
0.8576 298.15 8.17
0.8576 328.15 29.63
0.9036 298.15 8.63
0.9044 328.15 30.95

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (1) - Liquid Mass density, kg/m3 - Liquid
283.15 0.0000 887.11
283.15 0.0501 887.31
283.15 0.1152 887.6
283.15 0.2090 888.02
283.15 0.2924 888.37
283.15 0.4074 888.89
283.15 0.4975 889.4
283.15 0.5988 889.95
283.15 0.6961 890.62
283.15 0.7996 891.42
283.15 0.8975 892.37
283.15 0.9493 892.99
283.15 1.0000 893.62
298.15 0.0000 873.55
298.15 0.0501 873.67
298.15 0.1152 873.97
298.15 0.2090 874.26
298.15 0.2924 874.54
298.15 0.4074 875.02
298.15 0.4975 875.39
298.15 0.5988 875.83
298.15 0.6961 876.34
298.15 0.7996 876.93
298.15 0.8975 877.77
298.15 0.9493 878.28
298.15 1.0000 878.79
313.15 0.0000 859.0
313.15 0.0501 859.12
313.15 0.1152 859.32
313.15 0.2090 859.68
313.15 0.2924 859.83
313.15 0.4074 860.32
313.15 0.4975 860.6
313.15 0.5988 860.97
313.15 0.6961 861.47
313.15 0.7996 862.01
313.15 0.8975 862.78
313.15 0.9493 863.14
313.15 1.0000 863.69

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (1) - Liquid Mass density, kg/m3 - Liquid
283.15 0.0000 887.11
283.15 0.0501 887.31
283.15 0.1152 887.6
283.15 0.2090 888.02
283.15 0.2924 888.37
283.15 0.4074 888.89
283.15 0.4975 889.4
283.15 0.5988 889.95
283.15 0.6961 890.62
283.15 0.7996 891.42
283.15 0.8975 892.37
283.15 0.9493 892.99
283.15 1.0000 893.62
298.15 0.0000 873.55
298.15 0.0501 873.67
298.15 0.1152 873.97
298.15 0.2090 874.26
298.15 0.2924 874.54
298.15 0.4074 875.02
298.15 0.4975 875.39
298.15 0.5988 875.83
298.15 0.6961 876.34
298.15 0.7996 876.93
298.15 0.8975 877.77
298.15 0.9493 878.28
298.15 1.0000 878.79
313.15 0.0000 859.0
313.15 0.0501 859.12
313.15 0.1152 859.32
313.15 0.2090 859.68
313.15 0.2924 859.83
313.15 0.4074 860.32
313.15 0.4975 860.6
313.15 0.5988 860.97
313.15 0.6961 861.47
313.15 0.7996 862.01
313.15 0.8975 862.78
313.15 0.9493 863.14
313.15 1.0000 863.69

Boiling temperature at pressure P, K [ref]

Fixed Measured
Mole fraction of Tetrahydropyran (1) - Liquid Pressure, kPa - Liquid Boiling temperature at pressure P, K - Liquid
0.0551 101.33 404.54
0.0598 40.00 373.55
0.0970 40.00 370.81
0.1047 101.33 402.25
0.1378 40.00 368.34
0.1378 101.33 399.31
0.1819 101.33 395.97
0.1891 40.00 364.72
0.2384 40.00 362.31
0.2398 101.33 392.31
0.2618 101.33 390.57
0.2686 40.00 360.02
0.3375 40.00 356.52
0.3400 101.33 387.04
0.3882 40.00 353.88
0.3919 101.33 384.62
0.4670 40.00 350.61
0.4693 101.33 380.49
0.5449 101.33 377.19
0.5483 40.00 347.17
0.6301 101.33 373.55
0.6395 40.00 344.15
0.7155 101.33 370.57
0.7164 40.00 341.44
0.8004 101.33 367.26
0.8074 40.00 338.51
0.8748 101.33 364.96
0.8805 40.00 336.62
0.9505 40.00 334.72
0.9513 101.33 362.73
1.0000 101.33 361.23

Boiling temperature at pressure P, K [ref]

Fixed Measured
Mole fraction of Tetrahydropyran (1) - Liquid Pressure, kPa - Liquid Boiling temperature at pressure P, K - Liquid
0.0551 101.33 404.54
0.0598 40.00 373.55
0.0970 40.00 370.81
0.1047 101.33 402.25
0.1378 40.00 368.34
0.1378 101.33 399.31
0.1819 101.33 395.97
0.1891 40.00 364.72
0.2384 40.00 362.31
0.2398 101.33 392.31
0.2618 101.33 390.57
0.2686 40.00 360.02
0.3375 40.00 356.52
0.3400 101.33 387.04
0.3882 40.00 353.88
0.3919 101.33 384.62
0.4670 40.00 350.61
0.4693 101.33 380.49
0.5449 101.33 377.19
0.5483 40.00 347.17
0.6301 101.33 373.55
0.6395 40.00 344.15
0.7155 101.33 370.57
0.7164 40.00 341.44
0.8004 101.33 367.26
0.8074 40.00 338.51
0.8748 101.33 364.96
0.8805 40.00 336.62
0.9505 40.00 334.72
0.9513 101.33 362.73
1.0000 101.33 361.23

Sources