Mixture of Decane + 1-Hexanol

Excel

Decane

Name
Decane
InChI
InChI=1S/C10H22/c1-3-5-7-9-10-8-6-4-2/h3-10H2,1-2H3
InChI Key
DIOQZVSQGTUSAI-UHFFFAOYSA-N
Formula
C10H22
SMILES
CCCCCCCCCC
Mol. Weight (g/mol)
142.28
CAS
124-18-5

1-Hexanol

Name
1-Hexanol
InChI
InChI=1S/C6H14O/c1-2-3-4-5-6-7/h7H,2-6H2,1H3
InChI Key
ZSIAUFGUXNUGDI-UHFFFAOYSA-N
Formula
C6H14O
SMILES
CCCCCCO
Mol. Weight (g/mol)
102.17
CAS
111-27-3
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Datasets

  1. Mole fraction (2)
  2. Tboil - Boiling temperature at pressure P, K (2)

Mole fraction of 1-Hexanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Hexanol (2) - Liquid Mole fraction of 1-Hexanol (2) - Gas
1.0000 1.0000
0.9940 0.9820
0.9860 0.9610
0.9770 0.9400
0.9680 0.9220
0.9590 0.9040
0.9480 0.8830
0.9210 0.8360
0.9030 0.8200
0.8960 0.8030
0.8750 0.7680
0.8690 0.7660
0.8610 0.7540
0.8440 0.7340
0.8330 0.7250
0.8160 0.7150
0.7970 0.6990
0.7790 0.6840
0.7680 0.6950
0.7630 0.6710
0.7420 0.6600
0.7250 0.6540
0.5430 0.5740
0.5070 0.5660
0.4970 0.5610
0.4690 0.5420
0.4620 0.5510
0.4440 0.5330
0.4390 0.5390
0.4300 0.5280
0.4180 0.5290
0.4070 0.5250
0.3970 0.5290
0.3740 0.5190
0.3550 0.5070
0.3190 0.5000
0.2870 0.4780
0.2390 0.4530
0.1670 0.3970
0.1250 0.3550
0.0940 0.2970
0.0490 0.2000
0.0340 0.1600
0.0240 0.1250
0.0120 0.0910
0.0000 0.0000

Mole fraction of 1-Hexanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Hexanol (2) - Liquid Mole fraction of 1-Hexanol (2) - Gas
1.0000 1.0000
0.9940 0.9820
0.9860 0.9610
0.9770 0.9400
0.9680 0.9220
0.9590 0.9040
0.9480 0.8830
0.9210 0.8360
0.9030 0.8200
0.8960 0.8030
0.8750 0.7680
0.8690 0.7660
0.8610 0.7540
0.8440 0.7340
0.8330 0.7250
0.8160 0.7150
0.7970 0.6990
0.7790 0.6840
0.7680 0.6950
0.7630 0.6710
0.7420 0.6600
0.7250 0.6540
0.5430 0.5740
0.5070 0.5660
0.4970 0.5610
0.4690 0.5420
0.4620 0.5510
0.4440 0.5330
0.4390 0.5390
0.4300 0.5280
0.4180 0.5290
0.4070 0.5250
0.3970 0.5290
0.3740 0.5190
0.3550 0.5070
0.3190 0.5000
0.2870 0.4780
0.2390 0.4530
0.1670 0.3970
0.1250 0.3550
0.0940 0.2970
0.0490 0.2000
0.0340 0.1600
0.0240 0.1250
0.0120 0.0910
0.0000 0.0000

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of 1-Hexanol (2) - Liquid Boiling temperature at pressure P, K - Liquid
1.0000 402.36
0.9940 402.07
0.9860 401.87
0.9770 401.66
0.9680 401.43
0.9590 401.16
0.9480 400.83
0.9210 400.34
0.9030 400.21
0.8960 399.84
0.8750 399.47
0.8690 399.45
0.8610 399.38
0.8440 399.23
0.8330 399.12
0.8160 399.00
0.7970 398.84
0.7790 398.75
0.7680 398.67
0.7630 398.63
0.7420 398.54
0.7250 398.38
0.5430 398.50
0.5070 398.49
0.4970 398.59
0.4690 398.65
0.4620 398.67
0.4440 398.79
0.4390 398.81
0.4300 398.86
0.4180 398.92
0.4070 398.87
0.3970 399.07
0.3740 399.19
0.3550 399.25
0.3190 399.64
0.2870 400.04
0.2390 400.78
0.1670 402.73
0.1250 403.95
0.0940 405.92
0.0490 408.68
0.0340 409.70
0.0240 410.66
0.0120 411.62
0.0000 414.18

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of 1-Hexanol (2) - Liquid Boiling temperature at pressure P, K - Liquid
1.0000 402.36
0.9940 402.07
0.9860 401.87
0.9770 401.66
0.9680 401.43
0.9590 401.16
0.9480 400.83
0.9210 400.34
0.9030 400.21
0.8960 399.84
0.8750 399.47
0.8690 399.45
0.8610 399.38
0.8440 399.23
0.8330 399.12
0.8160 399.00
0.7970 398.84
0.7790 398.75
0.7680 398.67
0.7630 398.63
0.7420 398.54
0.7250 398.38
0.5430 398.50
0.5070 398.49
0.4970 398.59
0.4690 398.65
0.4620 398.67
0.4440 398.79
0.4390 398.81
0.4300 398.86
0.4180 398.92
0.4070 398.87
0.3970 399.07
0.3740 399.19
0.3550 399.25
0.3190 399.64
0.2870 400.04
0.2390 400.78
0.1670 402.73
0.1250 403.95
0.0940 405.92
0.0490 408.68
0.0340 409.70
0.0240 410.66
0.0120 411.62
0.0000 414.18

Sources