Mixture of Benzene + Diisopropyl ether + 1-Butanol

Excel

Benzene

Name
Benzene
InChI
InChI=1S/C6H6/c1-2-4-6-5-3-1/h1-6H
InChI Key
UHOVQNZJYSORNB-UHFFFAOYSA-N
Formula
C6H6
SMILES
c1ccccc1
Mol. Weight (g/mol)
78.11
CAS
71-43-2

Diisopropyl ether

Name
Diisopropyl ether
InChI
InChI=1S/C6H14O/c1-5(2)7-6(3)4/h5-6H,1-4H3
InChI Key
ZAFNJMIOTHYJRJ-UHFFFAOYSA-N
Formula
C6H14O
SMILES
CC(C)OC(C)C
Mol. Weight (g/mol)
102.17
CAS
108-20-3

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 Diisopropyl ether (2) - Liquid Mole fraction of 1-Butanol (3) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 0.0000 24.39
0.0000 0.3006 22.45
0.0000 0.6922 16.79
0.0000 1.0000 2.51
0.0001 0.0000 24.39
0.0001 1.0000 2.50
0.0328 0.6695 17.57
0.0336 0.2905 22.98
0.0516 0.2851 23.26
0.0569 0.6528 18.18
0.1044 0.6199 19.39
0.1139 0.2663 24.24
0.1489 0.2558 24.78
0.1516 0.5003 22.06
0.1548 0.5849 20.68
0.1648 0.3829 23.72
0.1666 0.4505 22.93
0.1806 0.4195 23.48
0.1820 0.4000 23.73
0.1945 0.4518 23.24
0.1972 0.3498 24.47
0.1988 0.5544 21.77
0.1999 0.2404 25.57
0.2106 0.4895 22.91
0.2123 0.3000 25.15
0.2240 0.5206 22.59
0.2274 0.2502 25.80
0.2406 0.5594 22.13
0.2425 0.2003 26.44
0.2485 0.5200 22.93
0.2517 0.2249 26.35
0.2557 0.5945 21.66
0.2578 0.1497 27.10
0.2707 0.6296 21.13
0.2729 0.0999 27.79
0.2855 0.6643 20.55
0.2881 0.0497 28.58
0.2904 0.6754 20.36
0.2953 0.0259 29.02
0.2980 0.4857 24.02
0.2991 0.2106 27.05
0.3006 0.6994 19.93
0.3032 0.0000 29.51
0.3480 0.4511 25.07
0.3491 0.1955 27.77
0.3497 0.5004 24.37
0.3500 0.1505 28.21
0.3846 0.1654 28.46
0.3847 0.4505 25.46
0.3962 0.1814 28.45
0.3987 0.4160 26.08
0.4198 0.1805 28.71
0.4198 0.4003 26.47
0.4497 0.1653 29.21
0.4503 0.3803 27.06
0.4545 0.3507 27.40
0.4547 0.1956 28.95
0.4893 0.2105 29.18
0.4897 0.3004 28.30
0.4985 0.3469 27.94
0.4999 0.1502 29.93
0.5237 0.2518 29.15
0.5247 0.2257 29.39
0.5594 0.2407 29.61
0.5598 0.2003 30.03
0.5951 0.2560 29.82
0.5954 0.1494 30.94
0.6308 0.0989 31.91
0.6310 0.2715 30.02
0.6643 0.2859 30.20
0.6653 0.0496 32.96
0.6818 0.2934 30.29
0.6832 0.0240 33.58
0.6992 0.3008 30.39
0.7000 0.0000 34.20
0.9999 0.0000 37.13
1.0000 0.0000 37.12

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Fixed Measured
Mole fraction of Diisopropyl ether (2) - Liquid Mole fraction of 1-Butanol (3) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 0.0000 24.39
0.0000 0.3006 22.45
0.0000 0.6922 16.79
0.0000 1.0000 2.51
0.0001 0.0000 24.39
0.0001 1.0000 2.50
0.0328 0.6695 17.57
0.0336 0.2905 22.98
0.0516 0.2851 23.26
0.0569 0.6528 18.18
0.1044 0.6199 19.39
0.1139 0.2663 24.24
0.1489 0.2558 24.78
0.1516 0.5003 22.06
0.1548 0.5849 20.68
0.1648 0.3829 23.72
0.1666 0.4505 22.93
0.1806 0.4195 23.48
0.1820 0.4000 23.73
0.1945 0.4518 23.24
0.1972 0.3498 24.47
0.1988 0.5544 21.77
0.1999 0.2404 25.57
0.2106 0.4895 22.91
0.2123 0.3000 25.15
0.2240 0.5206 22.59
0.2274 0.2502 25.80
0.2406 0.5594 22.13
0.2425 0.2003 26.44
0.2485 0.5200 22.93
0.2517 0.2249 26.35
0.2557 0.5945 21.66
0.2578 0.1497 27.10
0.2707 0.6296 21.13
0.2729 0.0999 27.79
0.2855 0.6643 20.55
0.2881 0.0497 28.58
0.2904 0.6754 20.36
0.2953 0.0259 29.02
0.2980 0.4857 24.02
0.2991 0.2106 27.05
0.3006 0.6994 19.93
0.3032 0.0000 29.51
0.3480 0.4511 25.07
0.3491 0.1955 27.77
0.3497 0.5004 24.37
0.3500 0.1505 28.21
0.3846 0.1654 28.46
0.3847 0.4505 25.46
0.3962 0.1814 28.45
0.3987 0.4160 26.08
0.4198 0.1805 28.71
0.4198 0.4003 26.47
0.4497 0.1653 29.21
0.4503 0.3803 27.06
0.4545 0.3507 27.40
0.4547 0.1956 28.95
0.4893 0.2105 29.18
0.4897 0.3004 28.30
0.4985 0.3469 27.94
0.4999 0.1502 29.93
0.5237 0.2518 29.15
0.5247 0.2257 29.39
0.5594 0.2407 29.61
0.5598 0.2003 30.03
0.5951 0.2560 29.82
0.5954 0.1494 30.94
0.6308 0.0989 31.91
0.6310 0.2715 30.02
0.6643 0.2859 30.20
0.6653 0.0496 32.96
0.6818 0.2934 30.29
0.6832 0.0240 33.58
0.6992 0.3008 30.39
0.7000 0.0000 34.20
0.9999 0.0000 37.13
1.0000 0.0000 37.12

Sources