Mixture of Benzene + Diisopropyl ether + 1-Propanol, 2-methyl-

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-Propanol, 2-methyl-

Name
1-Propanol, 2-methyl-
InChI
InChI=1S/C4H10O/c1-4(2)3-5/h4-5H,3H2,1-2H3
InChI Key
ZXEKIIBDNHEJCQ-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CC(C)CO
Mol. Weight (g/mol)
74.12
CAS
78-83-1
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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-Propanol, 2-methyl- (3) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 0.0000 24.38
0.0000 0.3009 23.23
0.0000 0.6935 18.25
0.0000 1.0000 4.01
0.0001 0.0000 24.36
0.0001 1.0000 4.02
0.0296 0.2920 23.64
0.0317 0.6715 18.87
0.0517 0.2853 23.95
0.0585 0.6529 19.43
0.1013 0.2704 24.66
0.1051 0.6205 20.42
0.1506 0.5005 22.81
0.1518 0.3490 24.58
0.1546 0.2543 25.42
0.1546 0.5862 21.50
0.1658 0.4504 23.61
0.1670 0.3841 24.39
0.1807 0.4009 24.34
0.1811 0.4164 24.19
0.1959 0.3504 25.01
0.1959 0.4506 23.94
0.2026 0.5528 22.53
0.2029 0.2398 26.11
0.2109 0.3007 25.65
0.2124 0.4886 23.60
0.2261 0.2501 26.27
0.2276 0.5238 23.23
0.2409 0.5545 22.86
0.2447 0.1884 27.00
0.2504 0.2255 26.78
0.2514 0.5189 23.54
0.2553 0.5876 22.40
0.2565 0.1495 27.47
0.2714 0.1000 28.08
0.2728 0.6281 21.75
0.2855 0.6576 21.21
0.2865 0.0498 28.77
0.2924 0.6735 20.89
0.2941 0.0246 29.15
0.3007 0.2103 27.48
0.3015 0.0000 29.50
0.3023 0.4836 24.58
0.3027 0.6973 20.39
0.3440 0.1566 28.42
0.3499 0.5005 24.79
0.3500 0.4505 25.51
0.3511 0.1952 28.18
0.3781 0.1721 28.65
0.3847 0.4508 25.84
0.4003 0.4156 26.46
0.4007 0.1802 28.86
0.4128 0.1879 28.89
0.4199 0.4006 26.82
0.4458 0.2030 29.09
0.4509 0.1651 29.55
0.4516 0.3801 27.39
0.4553 0.3500 27.75
0.4812 0.2191 29.30
0.4899 0.3006 28.61
0.5001 0.3464 28.24
0.5013 0.1499 30.23
0.5163 0.2351 29.50
0.5252 0.2502 29.48
0.5513 0.2511 29.68
0.5610 0.1990 30.35
0.5850 0.2664 29.86
0.5959 0.1492 31.22
0.6192 0.2821 30.03
0.6251 0.1075 31.99
0.6476 0.0754 32.60
0.6534 0.2976 30.19
0.6699 0.3052 30.24
0.6815 0.0271 33.60
0.6870 0.3130 30.32
0.7004 0.0000 34.21
1.0000 0.0000 37.09
1.0000 0.0000 37.14

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-Propanol, 2-methyl- (3) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 0.0000 24.38
0.0000 0.3009 23.23
0.0000 0.6935 18.25
0.0000 1.0000 4.01
0.0001 0.0000 24.36
0.0001 1.0000 4.02
0.0296 0.2920 23.64
0.0317 0.6715 18.87
0.0517 0.2853 23.95
0.0585 0.6529 19.43
0.1013 0.2704 24.66
0.1051 0.6205 20.42
0.1506 0.5005 22.81
0.1518 0.3490 24.58
0.1546 0.2543 25.42
0.1546 0.5862 21.50
0.1658 0.4504 23.61
0.1670 0.3841 24.39
0.1807 0.4009 24.34
0.1811 0.4164 24.19
0.1959 0.3504 25.01
0.1959 0.4506 23.94
0.2026 0.5528 22.53
0.2029 0.2398 26.11
0.2109 0.3007 25.65
0.2124 0.4886 23.60
0.2261 0.2501 26.27
0.2276 0.5238 23.23
0.2409 0.5545 22.86
0.2447 0.1884 27.00
0.2504 0.2255 26.78
0.2514 0.5189 23.54
0.2553 0.5876 22.40
0.2565 0.1495 27.47
0.2714 0.1000 28.08
0.2728 0.6281 21.75
0.2855 0.6576 21.21
0.2865 0.0498 28.77
0.2924 0.6735 20.89
0.2941 0.0246 29.15
0.3007 0.2103 27.48
0.3015 0.0000 29.50
0.3023 0.4836 24.58
0.3027 0.6973 20.39
0.3440 0.1566 28.42
0.3499 0.5005 24.79
0.3500 0.4505 25.51
0.3511 0.1952 28.18
0.3781 0.1721 28.65
0.3847 0.4508 25.84
0.4003 0.4156 26.46
0.4007 0.1802 28.86
0.4128 0.1879 28.89
0.4199 0.4006 26.82
0.4458 0.2030 29.09
0.4509 0.1651 29.55
0.4516 0.3801 27.39
0.4553 0.3500 27.75
0.4812 0.2191 29.30
0.4899 0.3006 28.61
0.5001 0.3464 28.24
0.5013 0.1499 30.23
0.5163 0.2351 29.50
0.5252 0.2502 29.48
0.5513 0.2511 29.68
0.5610 0.1990 30.35
0.5850 0.2664 29.86
0.5959 0.1492 31.22
0.6192 0.2821 30.03
0.6251 0.1075 31.99
0.6476 0.0754 32.60
0.6534 0.2976 30.19
0.6699 0.3052 30.24
0.6815 0.0271 33.60
0.6870 0.3130 30.32
0.7004 0.0000 34.21
1.0000 0.0000 37.09
1.0000 0.0000 37.14

Sources