Mixture of Toluene + 1-Hexene + 1-Butanol

Excel

Toluene

Name
Toluene
InChI
InChI=1S/C7H8/c1-7-5-3-2-4-6-7/h2-6H,1H3
InChI Key
YXFVVABEGXRONW-UHFFFAOYSA-N
Formula
C7H8
SMILES
Cc1ccccc1
Mol. Weight (g/mol)
92.14
CAS
108-88-3

1-Hexene

Name
1-Hexene
InChI
InChI=1S/C6H12/c1-3-5-6-4-2/h3H,1,4-6H2,2H3
InChI Key
LIKMAJRDDDTEIG-UHFFFAOYSA-N
Formula
C6H12
SMILES
C=CCCCC
Mol. Weight (g/mol)
84.16
CAS
592-41-6

1-Butanol

Name
1-Butanol
InChI
InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
InChI Key
LRHPLDYGYMQRHN-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CCCCO
Mol. Weight (g/mol)
74.12
CAS
71-36-3
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Datasets

  1. Pvap - Vapor or sublimation pressure, kPa (2)

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Fixed Measured
Mole fraction of 1-Butanol (3) - Liquid Mole fraction of 1-Hexene (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
1.0000 0.0000 2.51
0.7001 0.2999 32.64
0.6807 0.2916 31.54
0.6647 0.2848 30.62
0.6295 0.2698 28.71
0.5943 0.2548 26.94
0.5592 0.2399 25.29
0.5240 0.2249 23.74
0.4890 0.2099 22.31
0.4539 0.1949 20.96
0.4188 0.1799 19.71
0.3837 0.1649 18.52
0.3487 0.1499 17.41
0.0000 1.0000 44.98
0.3029 0.6971 42.05
0.2952 0.6794 41.11
0.2874 0.6615 40.11
0.2723 0.6267 38.23
0.2569 0.5915 36.38
0.2417 0.5564 34.60
0.2264 0.5214 32.85
0.2112 0.4865 31.16
0.1960 0.4515 29.51
0.1808 0.4166 27.88
0.1656 0.3817 26.28
0.1505 0.3469 24.69
0.0000 0.0000 7.89
0.2987 0.0000 8.23
0.2896 0.0306 10.30
0.2813 0.0582 11.94
0.2681 0.1026 14.44
0.2528 0.1538 17.07
0.2394 0.1986 19.21
0.2242 0.2495 21.47
0.2096 0.2984 23.47
0.1951 0.3468 25.36
0.1797 0.3985 27.26
0.1647 0.4486 29.00
0.1500 0.4978 30.64
1.0000 0.0000 2.52
0.6996 0.0000 6.88
0.6776 0.0313 9.62
0.6631 0.0521 11.99
0.6289 0.1010 16.16
0.5961 0.1479 19.21
0.5609 0.1982 22.64
0.5276 0.2457 25.13
0.4912 0.2977 27.61
0.4574 0.3461 29.59
0.4220 0.3966 31.44
0.3857 0.4485 33.14
0.3506 0.4987 34.62
0.0000 1.0000 44.99
0.0000 0.6975 34.71
0.0255 0.6797 34.96
0.0504 0.6623 34.85
0.1157 0.6168 34.45
0.1507 0.5924 34.22
0.2003 0.5577 33.84
0.2504 0.5228 33.45
0.3009 0.4876 33.01
0.3508 0.4527 32.53
0.4010 0.4178 31.99
0.4510 0.3829 31.33
0.5010 0.3481 30.57
0.0000 0.0000 7.88
0.0000 0.3010 21.12
0.0254 0.2933 21.35
0.0505 0.2857 21.36
0.1002 0.2708 21.23
0.1503 0.2557 21.04
0.2006 0.2405 20.81
0.2506 0.2255 20.55
0.3006 0.2104 20.26
0.3506 0.1954 19.94
0.4006 0.1804 19.57
0.4506 0.1653 19.15
0.5006 0.1503 18.65

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Fixed Measured
Mole fraction of 1-Butanol (3) - Liquid Mole fraction of 1-Hexene (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
1.0000 0.0000 2.51
0.7001 0.2999 32.64
0.6807 0.2916 31.54
0.6647 0.2848 30.62
0.6295 0.2698 28.71
0.5943 0.2548 26.94
0.5592 0.2399 25.29
0.5240 0.2249 23.74
0.4890 0.2099 22.31
0.4539 0.1949 20.96
0.4188 0.1799 19.71
0.3837 0.1649 18.52
0.3487 0.1499 17.41
0.0000 1.0000 44.98
0.3029 0.6971 42.05
0.2952 0.6794 41.11
0.2874 0.6615 40.11
0.2723 0.6267 38.23
0.2569 0.5915 36.38
0.2417 0.5564 34.60
0.2264 0.5214 32.85
0.2112 0.4865 31.16
0.1960 0.4515 29.51
0.1808 0.4166 27.88
0.1656 0.3817 26.28
0.1505 0.3469 24.69
0.0000 0.0000 7.89
0.2987 0.0000 8.23
0.2896 0.0306 10.30
0.2813 0.0582 11.94
0.2681 0.1026 14.44
0.2528 0.1538 17.07
0.2394 0.1986 19.21
0.2242 0.2495 21.47
0.2096 0.2984 23.47
0.1951 0.3468 25.36
0.1797 0.3985 27.26
0.1647 0.4486 29.00
0.1500 0.4978 30.64
1.0000 0.0000 2.52
0.6996 0.0000 6.88
0.6776 0.0313 9.62
0.6631 0.0521 11.99
0.6289 0.1010 16.16
0.5961 0.1479 19.21
0.5609 0.1982 22.64
0.5276 0.2457 25.13
0.4912 0.2977 27.61
0.4574 0.3461 29.59
0.4220 0.3966 31.44
0.3857 0.4485 33.14
0.3506 0.4987 34.62
0.0000 1.0000 44.99
0.0000 0.6975 34.71
0.0255 0.6797 34.96
0.0504 0.6623 34.85
0.1157 0.6168 34.45
0.1507 0.5924 34.22
0.2003 0.5577 33.84
0.2504 0.5228 33.45
0.3009 0.4876 33.01
0.3508 0.4527 32.53
0.4010 0.4178 31.99
0.4510 0.3829 31.33
0.5010 0.3481 30.57
0.0000 0.0000 7.88
0.0000 0.3010 21.12
0.0254 0.2933 21.35
0.0505 0.2857 21.36
0.1002 0.2708 21.23
0.1503 0.2557 21.04
0.2006 0.2405 20.81
0.2506 0.2255 20.55
0.3006 0.2104 20.26
0.3506 0.1954 19.94
0.4006 0.1804 19.57
0.4506 0.1653 19.15
0.5006 0.1503 18.65

Sources