Mixture of Benzene + 1-Propanol + Diisopropyl ether

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

1-Propanol

Name
1-Propanol
InChI
InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3
InChI Key
BDERNNFJNOPAEC-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CCCO
Mol. Weight (g/mol)
60.09
CAS
71-23-8

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
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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 (3) - Liquid Mole fraction of 1-Propanol (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 0.0000 24.39
0.0000 0.3000 25.46
0.0000 0.7003 21.11
0.0001 0.0000 24.37
0.0002 0.0000 24.39
0.0229 0.6842 21.61
0.0347 0.2896 25.92
0.0576 0.6599 22.40
0.0578 0.2827 26.24
0.0999 0.2700 26.80
0.1122 0.6216 23.66
0.1495 0.3510 26.94
0.1497 0.5014 25.72
0.1508 0.2547 27.48
0.1644 0.3862 26.87
0.1647 0.4514 26.37
0.1681 0.5823 24.90
0.1793 0.4211 26.77
0.1798 0.4013 26.95
0.1942 0.4563 26.64
0.1948 0.3513 27.46
0.2002 0.2399 28.13
0.2092 0.4915 26.47
0.2098 0.3012 27.93
0.2222 0.5444 26.03
0.2240 0.5266 26.25
0.2245 0.2522 28.34
0.2389 0.5617 25.98
0.2399 0.2010 28.74
0.2499 0.2250 28.77
0.2537 0.5967 25.66
0.2550 0.1507 29.09
0.2685 0.6317 25.28
0.2701 0.1004 29.40
0.2755 0.5071 27.07
0.2836 0.6673 24.82
0.2852 0.0499 29.60
0.2908 0.6841 24.58
0.2924 0.0258 29.61
0.2982 0.7018 24.39
0.2999 0.2100 29.40
0.3002 0.0000 29.50
0.3289 0.4697 28.04
0.3498 0.5008 27.97
0.3500 0.1494 30.10
0.3501 0.1949 30.01
0.3810 0.4332 28.93
0.3847 0.4511 28.82
0.3857 0.1647 30.44
0.3999 0.1800 30.60
0.4201 0.4006 29.59
0.4207 0.1796 30.75
0.4323 0.3973 29.75
0.4506 0.1648 31.20
0.4546 0.3513 30.30
0.4558 0.1946 31.06
0.4807 0.3634 30.48
0.4899 0.3010 30.95
0.4908 0.2096 31.35
0.5000 0.1499 31.77
0.5016 0.3487 30.80
0.5250 0.2509 31.57
0.5265 0.2249 31.65
0.5601 0.2008 32.16
0.5612 0.2397 31.92
0.5949 0.1511 32.72
0.5964 0.2548 32.20
0.6307 0.1000 33.27
0.6313 0.2697 32.47
0.6659 0.0498 33.78
0.6666 0.2849 32.73
0.6829 0.0255 34.01
0.6840 0.2923 32.87
0.7006 0.2994 32.96
0.7008 0.0000 34.20
1.0000 0.0000 37.11
1.0000 0.0000 37.11
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 (3) - Liquid Mole fraction of 1-Propanol (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 0.0000 24.39
0.0000 0.3000 25.46
0.0000 0.7003 21.11
0.0001 0.0000 24.37
0.0002 0.0000 24.39
0.0229 0.6842 21.61
0.0347 0.2896 25.92
0.0576 0.6599 22.40
0.0578 0.2827 26.24
0.0999 0.2700 26.80
0.1122 0.6216 23.66
0.1495 0.3510 26.94
0.1497 0.5014 25.72
0.1508 0.2547 27.48
0.1644 0.3862 26.87
0.1647 0.4514 26.37
0.1681 0.5823 24.90
0.1793 0.4211 26.77
0.1798 0.4013 26.95
0.1942 0.4563 26.64
0.1948 0.3513 27.46
0.2002 0.2399 28.13
0.2092 0.4915 26.47
0.2098 0.3012 27.93
0.2222 0.5444 26.03
0.2240 0.5266 26.25
0.2245 0.2522 28.34
0.2389 0.5617 25.98
0.2399 0.2010 28.74
0.2499 0.2250 28.77
0.2537 0.5967 25.66
0.2550 0.1507 29.09
0.2685 0.6317 25.28
0.2701 0.1004 29.40
0.2755 0.5071 27.07
0.2836 0.6673 24.82
0.2852 0.0499 29.60
0.2908 0.6841 24.58
0.2924 0.0258 29.61
0.2982 0.7018 24.39
0.2999 0.2100 29.40
0.3002 0.0000 29.50
0.3289 0.4697 28.04
0.3498 0.5008 27.97
0.3500 0.1494 30.10
0.3501 0.1949 30.01
0.3810 0.4332 28.93
0.3847 0.4511 28.82
0.3857 0.1647 30.44
0.3999 0.1800 30.60
0.4201 0.4006 29.59
0.4207 0.1796 30.75
0.4323 0.3973 29.75
0.4506 0.1648 31.20
0.4546 0.3513 30.30
0.4558 0.1946 31.06
0.4807 0.3634 30.48
0.4899 0.3010 30.95
0.4908 0.2096 31.35
0.5000 0.1499 31.77
0.5016 0.3487 30.80
0.5250 0.2509 31.57
0.5265 0.2249 31.65
0.5601 0.2008 32.16
0.5612 0.2397 31.92
0.5949 0.1511 32.72
0.5964 0.2548 32.20
0.6307 0.1000 33.27
0.6313 0.2697 32.47
0.6659 0.0498 33.78
0.6666 0.2849 32.73
0.6829 0.0255 34.01
0.6840 0.2923 32.87
0.7006 0.2994 32.96
0.7008 0.0000 34.20
1.0000 0.0000 37.11
1.0000 0.0000 37.11
1.0000 0.0000 37.12

Sources