Mixture of Benzene + n-Hexane + Ethanol + Acetone

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

n-Hexane

Name
n-Hexane
InChI
InChI=1S/C6H14/c1-3-5-6-4-2/h3-6H2,1-2H3
InChI Key
VLKZOEOYAKHREP-UHFFFAOYSA-N
Formula
C6H14
SMILES
CCCCCC
Mol. Weight (g/mol)
86.18
CAS
110-54-3

Ethanol

Name
Ethanol
InChI
InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3
InChI Key
LFQSCWFLJHTTHZ-UHFFFAOYSA-N
Formula
C2H6O
SMILES
CCO
Mol. Weight (g/mol)
46.07
CAS
64-17-5

Acetone

Name
Acetone
InChI
InChI=1S/C3H6O/c1-3(2)4/h1-2H3
InChI Key
CSCPPACGZOOCGX-UHFFFAOYSA-N
Formula
C3H6O
SMILES
CC(C)=O
Mol. Weight (g/mol)
58.08
CAS
67-64-1
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Datasets

  1. Vapor Liquid Equilibrium at Constant Pressure
  2. Vapor Liquid Equilibrium at Constant Temperature (2)

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Ethanol (3) - Liquid x2[mol/mol] of Acetone (4) - Liquid x3[mol/mol] of Benzene (1) - Liquid
330.4 0.3320 0.2648 0.2213
330.04 0.3029 0.3596 0.2023
329.78 0.3000 0.5188 0.1088
328.04 0.1024 0.7143 0.1052
331.17 0.4655 0.3708 0.0892
333.61 0.6034 0.2399 0.0918
330.97 0.1049 0.5023 0.3117
332.62 0.2947 0.3407 0.2875
334.85 0.4797 0.1840 0.2682
334.23 0.1149 0.3211 0.4845
336.23 0.3068 0.1458 0.4776
337.48 0.1131 0.1417 0.6619
330.38 0.0999 0.3328 0.3403
333.83 0.1109 0.1433 0.4898
326.04 0.1006 0.5345 0.1121
328.35 0.1259 0.1534 0.1231
326.01 0.0983 0.3810 0.1109
330.76 0.1129 0.1547 0.2963
326.31 0.1134 0.3149 0.1131
331.19 0.0965 0.1483 0.3300
330.44 0.1018 0.2405 0.3500
335.09 0.1082 0.0872 0.5338
351.3 1.0000 0.0000 0.0000
329.34 0.0000 1.0000 0.0000
353.26 0.0000 0.0000 1.0000
341.95 0.0000 0.0000 0.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 308.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Ethanol (3) - Liquid x2[mol/mol] of Acetone (4) - Liquid x3[mol/mol] of Benzene (1) - Liquid
43.83 0.3320 0.2648 0.2213
44.71 0.3029 0.3596 0.2023
44.99 0.3000 0.5188 0.1088
48.9 0.1024 0.7143 0.1052
42.65 0.4655 0.3708 0.0892
38.26 0.6034 0.2399 0.0918
43.53 0.1049 0.5023 0.3117
40.319 0.2947 0.3407 0.2875
36.19 0.4797 0.1840 0.2682
38.41 0.1149 0.3211 0.4845
34.131 0.3068 0.1458 0.4776
33.58 0.1131 0.1417 0.6619
44.6 0.0999 0.3328 0.3403
39.079 0.1109 0.1433 0.4898
52.58 0.1006 0.5345 0.1121
47.549 0.1259 0.1534 0.1231
52.48 0.0983 0.3810 0.1109
43.66 0.1129 0.1547 0.2963
51.8 0.1134 0.3149 0.1131
43.04 0.0965 0.1483 0.3300
44.24 0.1018 0.2405 0.3500
36.94 0.1082 0.0872 0.5338

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 318.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Ethanol (3) - Liquid x2[mol/mol] of Acetone (4) - Liquid x3[mol/mol] of Benzene (1) - Liquid
64.851 0.3320 0.2648 0.2213
65.92 0.3029 0.3596 0.2023
66.631 0.3000 0.5188 0.1088
71.539 0.1024 0.7143 0.1052
63.109 0.4655 0.3708 0.0892
57.21 0.6034 0.2399 0.0918
64.109 0.1049 0.5023 0.3117
59.84 0.2947 0.3407 0.2875
54.4 0.4797 0.1840 0.2682
56.95 0.1149 0.3211 0.4845
51.6 0.3068 0.1458 0.4776
50.271 0.1131 0.1417 0.6619
65.631 0.0999 0.3328 0.3403
57.681 0.1109 0.1433 0.4898
76.68 0.1006 0.5345 0.1121
70.05 0.1259 0.1534 0.1231
76.59 0.0983 0.3810 0.1109
64.389 0.1129 0.1547 0.2963
75.69 0.1134 0.3149 0.1131
63.509 0.0965 0.1483 0.3300
65.24 0.1018 0.2405 0.3500
54.979 0.1082 0.0872 0.5338

Sources