Mixture of Benzene + Diisopropyl ether + Isopropyl Alcohol

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

Isopropyl Alcohol

Name
Isopropyl Alcohol
InChI
InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3
InChI Key
KFZMGEQAYNKOFK-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CC(C)O
Mol. Weight (g/mol)
60.09
CAS
67-63-0
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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 Isopropyl Alcohol (3) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 0.0000 24.38
0.0000 0.2996 29.52
0.0000 0.7020 26.72
0.0000 1.0000 13.89
0.0253 0.2920 29.85
0.0327 0.6790 27.49
0.0562 0.2828 30.25
0.0580 0.6612 28.07
0.0991 0.6323 28.98
0.1014 0.2692 30.82
0.1505 0.5000 30.76
0.1510 0.3490 31.36
0.1520 0.5951 30.06
0.1524 0.2539 31.43
0.1655 0.4504 31.20
0.1663 0.3844 31.48
0.1809 0.3992 31.58
0.1813 0.4190 31.55
0.1956 0.3503 31.87
0.1963 0.4539 31.59
0.1997 0.2397 31.96
0.2001 0.5613 30.97
0.2106 0.3003 32.10
0.2114 0.4888 31.60
0.2259 0.2497 32.26
0.2265 0.5239 31.58
0.2407 0.2004 32.33
0.2416 0.5588 31.50
0.2498 0.5264 31.84
0.2521 0.2240 32.53
0.2562 0.1490 32.27
0.2566 0.5937 31.39
0.2709 0.6268 31.21
0.2714 0.0984 32.00
0.2858 0.0505 31.28
0.2869 0.6642 30.95
0.2938 0.0240 30.54
0.2944 0.6815 30.80
0.2993 0.4916 32.63
0.3005 0.2095 33.02
0.3010 0.0000 29.52
0.3016 0.6984 30.66
0.3486 0.1490 33.27
0.3499 0.1947 33.49
0.3500 0.4561 33.37
0.3580 0.5002 33.25
0.3873 0.1655 33.76
0.3936 0.4506 33.86
0.4000 0.1797 33.95
0.4002 0.4208 34.04
0.4185 0.1789 34.15
0.4296 0.4003 34.39
0.4494 0.1649 34.37
0.4496 0.3861 34.64
0.4529 0.1936 34.55
0.4653 0.3505 34.84
0.4873 0.2083 34.94
0.4998 0.1498 34.78
0.4998 0.3509 35.20
0.5011 0.3006 35.20
0.5218 0.2231 35.33
0.5371 0.2503 35.51
0.5563 0.2379 35.70
0.5726 0.2008 35.72
0.5914 0.2529 36.07
0.6097 0.1489 35.82
0.6257 0.2676 36.43
0.6422 0.1035 35.75
0.6600 0.2823 36.79
0.6767 0.2895 36.95
0.6803 0.0504 35.34
0.6983 0.0253 34.94
0.7004 0.2996 37.13
0.7164 0.0000 34.36
1.0000 0.0000 37.11
0.0000 0.0000 24.38
0.0000 1.0000 13.89
1.0000 0.0000 37.13

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 Isopropyl Alcohol (3) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 0.0000 24.38
0.0000 0.2996 29.52
0.0000 0.7020 26.72
0.0000 1.0000 13.89
0.0253 0.2920 29.85
0.0327 0.6790 27.49
0.0562 0.2828 30.25
0.0580 0.6612 28.07
0.0991 0.6323 28.98
0.1014 0.2692 30.82
0.1505 0.5000 30.76
0.1510 0.3490 31.36
0.1520 0.5951 30.06
0.1524 0.2539 31.43
0.1655 0.4504 31.20
0.1663 0.3844 31.48
0.1809 0.3992 31.58
0.1813 0.4190 31.55
0.1956 0.3503 31.87
0.1963 0.4539 31.59
0.1997 0.2397 31.96
0.2001 0.5613 30.97
0.2106 0.3003 32.10
0.2114 0.4888 31.60
0.2259 0.2497 32.26
0.2265 0.5239 31.58
0.2407 0.2004 32.33
0.2416 0.5588 31.50
0.2498 0.5264 31.84
0.2521 0.2240 32.53
0.2562 0.1490 32.27
0.2566 0.5937 31.39
0.2709 0.6268 31.21
0.2714 0.0984 32.00
0.2858 0.0505 31.28
0.2869 0.6642 30.95
0.2938 0.0240 30.54
0.2944 0.6815 30.80
0.2993 0.4916 32.63
0.3005 0.2095 33.02
0.3010 0.0000 29.52
0.3016 0.6984 30.66
0.3486 0.1490 33.27
0.3499 0.1947 33.49
0.3500 0.4561 33.37
0.3580 0.5002 33.25
0.3873 0.1655 33.76
0.3936 0.4506 33.86
0.4000 0.1797 33.95
0.4002 0.4208 34.04
0.4185 0.1789 34.15
0.4296 0.4003 34.39
0.4494 0.1649 34.37
0.4496 0.3861 34.64
0.4529 0.1936 34.55
0.4653 0.3505 34.84
0.4873 0.2083 34.94
0.4998 0.1498 34.78
0.4998 0.3509 35.20
0.5011 0.3006 35.20
0.5218 0.2231 35.33
0.5371 0.2503 35.51
0.5563 0.2379 35.70
0.5726 0.2008 35.72
0.5914 0.2529 36.07
0.6097 0.1489 35.82
0.6257 0.2676 36.43
0.6422 0.1035 35.75
0.6600 0.2823 36.79
0.6767 0.2895 36.95
0.6803 0.0504 35.34
0.6983 0.0253 34.94
0.7004 0.2996 37.13
0.7164 0.0000 34.36
1.0000 0.0000 37.11
0.0000 0.0000 24.38
0.0000 1.0000 13.89
1.0000 0.0000 37.13

Sources