Mixture of Benzene + Acetone + Cyclohexane

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

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

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
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

  1. Binary diffusion coefficient, m2/s (2)
  2. Vapor Liquid Equilibrium at Constant Pressure
  3. Vapor Liquid Equilibrium at Constant Temperature

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

Solvent: Mole fraction of Acetone (2) - Liquid Binary diffusion coefficient, m2/s - Liquid
0.0000 0.0000
0.1900 0.0000
0.3000 0.0000
0.5033 0.0000
0.7449 0.0000
0.8777 0.0000
1.0000 0.0000

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

Solvent: Mole fraction of Acetone (2) - Liquid Binary diffusion coefficient, m2/s - Liquid
0.0000 0.0000
0.1900 0.0000
0.3000 0.0000
0.5033 0.0000
0.7449 0.0000
0.8777 0.0000
1.0000 0.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Acetone (2) - Liquid x2[mol/mol] of Benzene (1) - Liquid y1[mol/mol] of Acetone (2) - Vapour y2[mol/mol] of Benzene (1) - Vapour
350.75 0.0550 0.9300 0.1360 0.8150
350.95 0.0150 0.8850 0.0390 0.8140
350.45 0.0300 0.8300 0.0850 0.7390
345.55 0.0850 0.7150 0.1860 0.5740
341.35 0.1850 0.6550 0.3680 0.4660
342.65 0.1250 0.6150 0.2820 0.4570
342.85 0.1100 0.5700 0.2690 0.4320
344.65 0.0750 0.5250 0.2010 0.4300
340.05 0.1650 0.4650 0.3540 0.3160
337.95 0.2200 0.4300 0.4590 0.2620
335.55 0.3150 0.3750 0.5520 0.2040
334.25 0.3700 0.3400 0.5910 0.1770
331.45 0.4900 0.2750 0.6610 0.1310
333.25 0.4200 0.3350 0.6180 0.1760
334.45 0.4030 0.3800 0.6050 0.2080
336.55 0.3550 0.4850 0.5590 0.2760
337.85 0.3050 0.5400 0.5170 0.3340
337.15 0.3450 0.5200 0.5460 0.3100
335.75 0.4000 0.4700 0.5920 0.2810
333.65 0.5350 0.3750 0.6810 0.2150
332.95 0.5900 0.3250 0.7050 0.1750
332.65 0.6350 0.3050 0.7380 0.1740
331.95 0.5850 0.2850 0.7020 0.1320
330.95 0.5350 0.2600 0.6870 0.1160
330.95 0.4850 0.2350 0.6650 0.1020
331.05 0.4300 0.2150 0.6500 0.0960
331.55 0.3650 0.1950 0.6250 0.0840
333.65 0.3100 0.2550 0.5850 0.1220
335.75 0.2700 0.3410 0.5200 0.1940
336.85 0.2250 0.3150 0.4820 0.1830
338.05 0.1700 0.2800 0.4270 0.1740
340.35 0.1310 0.3360 0.3360 0.2450
342.05 0.1020 0.4150 0.2800 0.3140
342.25 0.0950 0.3700 0.2620 0.2910
329.15 0.9110 0.0650 0.8800 0.0220
329.95 0.8350 0.1300 0.8260 0.0570
330.85 0.7600 0.2000 0.8010 0.1020
329.55 0.7200 0.1800 0.7720 0.0840
328.95 0.6800 0.1750 0.7480 0.0750
327.95 0.7000 0.1350 0.7540 0.0550
327.85 0.7450 0.1150 0.7680 0.0440

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 318.15 (VLE)

Fixed Measured
x1[mol/mol] of Acetone (2) - Liquid x2[mol/mol] of Benzene (1) - Liquid y1[mol/mol] of Acetone (2) - Vapour y2[mol/mol] of Benzene (1) - Vapour
0.6637 0.0841 0.7312 0.0423
0.6210 0.1111 0.7204 0.0508
0.3602 0.2246 0.5474 0.1283
0.1713 0.3283 0.3828 0.2137
0.1050 0.3680 0.3164 0.2505
0.4881 0.0916 0.7061 0.0377
0.2655 0.1476 0.4828 0.0954
0.0930 0.1878 0.2222 0.1800
0.0493 0.1718 0.1022 0.2055
0.0171 0.1295 0.0395 0.1837
0.7151 0.0840 0.7561 0.0247
0.6804 0.1468 0.7233 0.0780
0.5212 0.3198 0.6683 0.1740
0.3318 0.5072 0.5071 0.3232
0.1988 0.6631 0.3661 0.4607

Sources