Mixture of Acetone + Cyclohexane + Methyl Alcohol

Excel

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

Methyl Alcohol

Name
Methyl Alcohol
InChI
InChI=1S/CH4O/c1-2/h2H,1H3
InChI Key
OKKJLVBELUTLKV-UHFFFAOYSA-N
Formula
CH4O
SMILES
CO
Mol. Weight (g/mol)
32.04
CAS
67-56-1
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Datasets

  1. Vapor Liquid Equilibrium at Constant Temperature (3)

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 308.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Acetone (1) - Liquid x2[mol/mol] of Methyl Alcohol (3) - Liquid y1[mol/mol] of Acetone (1) - Vapour y2[mol/mol] of Methyl Alcohol (3) - Vapour
50.103 0.1190 0.1280 0.2920 0.3470
50.343 0.1200 0.2500 0.2350 0.3910
50.249 0.1190 0.3780 0.2090 0.4200
49.689 0.1210 0.5010 0.1820 0.4470
49.396 0.1230 0.6290 0.1850 0.4480
47.783 0.1250 0.7500 0.1850 0.4780
52.196 0.2500 0.1230 0.4250 0.2400
52.489 0.2500 0.2550 0.3620 0.3050
51.929 0.2570 0.3650 0.3250 0.3420
51.716 0.2530 0.4970 0.3070 0.3660
50.316 0.2500 0.6250 0.3240 0.3870
52.329 0.3660 0.1350 0.4950 0.1940
53.316 0.3810 0.2420 0.4480 0.2470
53.169 0.4030 0.3570 0.4300 0.2820
51.822 0.3750 0.5000 0.4300 0.3170
53.262 0.5220 0.1020 0.5750 0.1350
53.836 0.5370 0.2140 0.5350 0.1890
52.529 0.5000 0.3750 0.5200 0.2530
52.982 0.6660 0.0780 0.6440 0.0950
52.769 0.6410 0.2380 0.6070 0.1880
52.076 0.8190 0.0560 0.7310 0.0780

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 318.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Acetone (1) - Liquid x2[mol/mol] of Methyl Alcohol (3) - Liquid y1[mol/mol] of Acetone (1) - Vapour y2[mol/mol] of Methyl Alcohol (3) - Vapour
74.661 0.1170 0.1270 0.2760 0.3670
75.514 0.1180 0.2480 0.2170 0.4240
75.674 0.1180 0.3790 0.1910 0.4520
75.074 0.1210 0.5010 0.1720 0.4660
74.767 0.1230 0.6310 0.1760 0.4710
71.327 0.1250 0.7520 0.1780 0.4970
79.167 0.2490 0.1200 0.4150 0.2520
78.074 0.2480 0.2540 0.3500 0.3220
77.954 0.2550 0.3690 0.3120 0.3670
77.594 0.2540 0.4970 0.2900 0.3910
75.46 0.2500 0.6260 0.3140 0.4120
78.274 0.3700 0.1310 0.4880 0.2000
79.087 0.3820 0.2390 0.4330 0.2670
79.153 0.4050 0.3750 0.4140 0.3030
77.234 0.3790 0.4970 0.4140 0.3430
78.327 0.5240 0.0980 0.5770 0.1340
79.647 0.5370 0.2140 0.5260 0.2020
77.807 0.5110 0.3690 0.5070 0.2750
77.807 0.6690 0.0760 0.6540 0.0880
76.54 0.6470 0.2320 0.6090 0.1930
76.487 0.8220 0.0540 0.7430 0.0760

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 328.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Acetone (1) - Liquid x2[mol/mol] of Methyl Alcohol (3) - Liquid y1[mol/mol] of Acetone (1) - Vapour y2[mol/mol] of Methyl Alcohol (3) - Vapour
109.591 0.1130 0.1260 0.2610 0.3840
111.724 0.1160 0.2450 0.2030 0.4470
111.857 0.1160 0.3790 0.1770 0.4730
111.724 0.1210 0.5010 0.1620 0.4870
111.324 0.1240 0.6340 0.1590 0.4990
107.991 0.1240 0.7560 0.1650 0.5320
111.857 0.2480 0.1150 0.4020 0.2710
114.391 0.2440 0.2520 0.3200 0.3610
114.791 0.2520 0.3750 0.2920 0.3930
114.524 0.2560 0.4950 0.2790 0.4130
111.324 0.2490 0.6300 0.2960 0.4450
112.924 0.3760 0.1220 0.4750 0.2140
115.191 0.3840 0.2350 0.4270 0.2790
115.724 0.4070 0.3730 0.3960 0.3240
113.057 0.3800 0.5000 0.3920 0.3820
113.457 0.5280 0.0900 0.5800 0.1370
115.324 0.5370 0.2140 0.5090 0.2270
113.591 0.5150 0.3650 0.5080 0.2780
114.391 0.6750 0.0740 0.6550 0.0950
112.657 0.6610 0.2180 0.6170 0.1870
110.524 0.8260 0.0520 0.7480 0.0720

Sources