Mixture of Toluene + n-Butyl ether + Cyclohexane

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

n-Butyl ether

Name
n-Butyl ether
InChI
InChI=1S/C8H18O/c1-3-5-7-9-8-6-4-2/h3-8H2,1-2H3
InChI Key
DURPTKYDGMDSBL-UHFFFAOYSA-N
Formula
C8H18O
SMILES
CCCCOCCCC
Mol. Weight (g/mol)
130.23
CAS
142-96-1

Cyclohexane

Name
Cyclohexane
InChI
InChI=1S/C6H12/c1-2-4-6-5-3-1/h1-6H2
InChI Key
XDTMQSROBMDMFD-UHFFFAOYSA-N
Formula
C6H12
SMILES
C1CCCCC1
Mol. Weight (g/mol)
84.16
CAS
110-82-7
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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 n-Butyl ether (2) - Liquid Mole fraction of Toluene (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 0.0000 24.62
0.0000 0.3183 20.53
0.0000 0.6735 15.12
0.0000 1.0000 7.89
0.0001 0.0000 24.62
0.0001 1.0000 7.89
0.0270 0.3097 20.03
0.0282 0.6545 14.71
0.0508 0.3021 19.59
0.0544 0.6368 14.34
0.0989 0.6069 13.68
0.0993 0.2867 18.69
0.1451 0.2721 17.84
0.1496 0.5726 12.98
0.1520 0.5006 14.16
0.1547 0.3557 16.41
0.1652 0.3798 15.80
0.1673 0.4503 14.60
0.1794 0.4125 14.94
0.1836 0.3967 15.06
0.1953 0.4490 13.95
0.1975 0.3510 15.42
0.1998 0.2546 16.80
0.2045 0.5356 12.21
0.2093 0.4813 13.05
0.2127 0.3013 15.80
0.2244 0.5158 12.03
0.2291 0.2474 16.20
0.2403 0.5526 10.93
0.2430 0.2016 16.52
0.2500 0.2387 15.85
0.2524 0.5034 11.54
0.2584 0.1512 16.85
0.2594 0.5963 9.58
0.2722 0.6258 8.62
0.2762 0.0928 17.22
0.2855 0.6565 7.61
0.2895 0.0488 17.49
0.2932 0.6741 6.99
0.2957 0.0284 17.60
0.3000 0.2227 14.90
0.3007 0.4708 10.88
0.3031 0.6969 6.17
0.3044 0.0000 17.76
0.3176 0.1752 15.18
0.3494 0.1927 14.18
0.3494 0.2070 13.96
0.3522 0.4361 10.17
0.3821 0.5441 7.29
0.3835 0.2115 13.10
0.4006 0.4035 9.52
0.4015 0.1904 12.97
0.4177 0.2303 11.99
0.4223 0.4960 7.18
0.4461 0.2460 11.06
0.4500 0.1750 12.06
0.4502 0.3701 8.86
0.4653 0.4448 7.06
0.4826 0.2661 9.85
0.5010 0.3359 8.19
0.5019 0.1584 11.07
0.5108 0.3905 6.91
0.5120 0.2824 8.84
0.5474 0.3018 7.63
0.5530 0.3401 6.78
0.5770 0.3182 6.59
0.5988 0.2855 6.62
0.6045 0.3334 5.62
0.6191 0.3414 5.11
0.6445 0.3555 4.20
0.6461 0.2291 6.45
0.6916 0.1748 6.28
0.7363 0.1214 6.10
0.7778 0.0719 5.94
0.7943 0.0522 5.87
0.8381 0.0000 5.68
1.0000 0.0000 2.08
1.0000 0.0000 2.08

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Fixed Measured
Mole fraction of n-Butyl ether (2) - Liquid Mole fraction of Toluene (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 0.0000 24.62
0.0000 0.3183 20.53
0.0000 0.6735 15.12
0.0000 1.0000 7.89
0.0001 0.0000 24.62
0.0001 1.0000 7.89
0.0270 0.3097 20.03
0.0282 0.6545 14.71
0.0508 0.3021 19.59
0.0544 0.6368 14.34
0.0989 0.6069 13.68
0.0993 0.2867 18.69
0.1451 0.2721 17.84
0.1496 0.5726 12.98
0.1520 0.5006 14.16
0.1547 0.3557 16.41
0.1652 0.3798 15.80
0.1673 0.4503 14.60
0.1794 0.4125 14.94
0.1836 0.3967 15.06
0.1953 0.4490 13.95
0.1975 0.3510 15.42
0.1998 0.2546 16.80
0.2045 0.5356 12.21
0.2093 0.4813 13.05
0.2127 0.3013 15.80
0.2244 0.5158 12.03
0.2291 0.2474 16.20
0.2403 0.5526 10.93
0.2430 0.2016 16.52
0.2500 0.2387 15.85
0.2524 0.5034 11.54
0.2584 0.1512 16.85
0.2594 0.5963 9.58
0.2722 0.6258 8.62
0.2762 0.0928 17.22
0.2855 0.6565 7.61
0.2895 0.0488 17.49
0.2932 0.6741 6.99
0.2957 0.0284 17.60
0.3000 0.2227 14.90
0.3007 0.4708 10.88
0.3031 0.6969 6.17
0.3044 0.0000 17.76
0.3176 0.1752 15.18
0.3494 0.1927 14.18
0.3494 0.2070 13.96
0.3522 0.4361 10.17
0.3821 0.5441 7.29
0.3835 0.2115 13.10
0.4006 0.4035 9.52
0.4015 0.1904 12.97
0.4177 0.2303 11.99
0.4223 0.4960 7.18
0.4461 0.2460 11.06
0.4500 0.1750 12.06
0.4502 0.3701 8.86
0.4653 0.4448 7.06
0.4826 0.2661 9.85
0.5010 0.3359 8.19
0.5019 0.1584 11.07
0.5108 0.3905 6.91
0.5120 0.2824 8.84
0.5474 0.3018 7.63
0.5530 0.3401 6.78
0.5770 0.3182 6.59
0.5988 0.2855 6.62
0.6045 0.3334 5.62
0.6191 0.3414 5.11
0.6445 0.3555 4.20
0.6461 0.2291 6.45
0.6916 0.1748 6.28
0.7363 0.1214 6.10
0.7778 0.0719 5.94
0.7943 0.0522 5.87
0.8381 0.0000 5.68
1.0000 0.0000 2.08
1.0000 0.0000 2.08

Sources