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Mixture of Benzene + Acetic acid

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

Acetic acid

Name
Acetic acid
InChI
InChI=1S/C2H4O2/c1-2(3)4/h1H3,(H,3,4)
InChI Key
QTBSBXVTEAMEQO-UHFFFAOYSA-N
Formula
C2H4O2
SMILES
CC(=O)O
Mol. Weight (g/mol)
60.05
CAS
64-19-7
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Datasets

  1. Mole fraction (2)
  2. Tboil - Boiling temperature at pressure P, K (2)
  3. Vapor Liquid Equilibrium at Constant Pressure (2)
  4. Vapor Liquid Equilibrium at Constant Temperature

Mole fraction of Acetic acid (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetic acid (2) - Liquid Mole fraction of Acetic acid (2) - Gas
0.1073 0.0831
0.2168 0.1562
0.3574 0.1987
0.4991 0.2319
0.5707 0.2703
0.6288 0.3045
0.6916 0.3644
0.7583 0.4141
0.7862 0.4467
0.8196 0.4898
0.8545 0.5493
0.9006 0.6202
0.9316 0.7027
0.9499 0.7750
0.9682 0.8347
0.9881 0.9165

Mole fraction of Acetic acid (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetic acid (2) - Liquid Mole fraction of Acetic acid (2) - Gas
0.1073 0.0831
0.2168 0.1562
0.3574 0.1987
0.4991 0.2319
0.5707 0.2703
0.6288 0.3045
0.6916 0.3644
0.7583 0.4141
0.7862 0.4467
0.8196 0.4898
0.8545 0.5493
0.9006 0.6202
0.9316 0.7027
0.9499 0.7750
0.9682 0.8347
0.9881 0.9165

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetic acid (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.1073 353.65
0.2168 354.65
0.3574 355.85
0.4991 357.05
0.5707 358.85
0.6288 359.95
0.6916 361.95
0.7583 364.05
0.7862 365.35
0.8196 367.35
0.8545 369.95
0.9006 372.85
0.9316 375.85
0.9499 378.65
0.9682 380.95
0.9881 383.95

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetic acid (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.1073 353.65
0.2168 354.65
0.3574 355.85
0.4991 357.05
0.5707 358.85
0.6288 359.95
0.6916 361.95
0.7583 364.05
0.7862 365.35
0.8196 367.35
0.8545 369.95
0.9006 372.85
0.9316 375.85
0.9499 378.65
0.9682 380.95
0.9881 383.95

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.06 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Benzene (1) - Liquid y1[mol/mol] of Benzene (1) - Vapour
388.25 0.0090 0.0600
382.15 0.0280 0.2410
373.15 0.0740 0.3950
364.65 0.1730 0.5920
358.95 0.3410 0.7030
355.95 0.5320 0.7930
353.15 0.8820 0.9310
352.95 0.9500 0.9610

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

T [K] - VLE x1[mol/mol] of Benzene (1) - Liquid
391.85 0.0000
382.66 0.0647
379.97 0.0891
376.86 0.1272
372.59 0.1923
369.38 0.2497
367.14 0.2993
364.0 0.3804
362.11 0.4539
357.87 0.6451
353.35 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 323.14 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Benzene (1) - Liquid y1[mol/mol] of Benzene (1) - Vapour
7.386 0.0000 0.0000
7.893 0.0039 0.0431
9.066 0.0115 0.1090
23.371 0.2265 0.6568
25.265 0.2900 0.7071
29.904 0.4981 0.7985
31.464 0.5811 0.8337
32.691 0.6936 0.8678
34.53 0.8280 0.9143
35.25 0.9354 0.9594
35.45 0.9780 0.9812
35.61 1.0000 1.0000

Sources