Mixture of Acetone + Methyl Alcohol + Water

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

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

Water

Name
Water
InChI
InChI=1S/H2O/h1H2
InChI Key
XLYOFNOQVPJJNP-UHFFFAOYSA-N
Formula
H2O
SMILES
O
Mol. Weight (g/mol)
18.02
CAS
7732-18-5
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Datasets

  1. Vapor Liquid Equilibrium at Constant Pressure (3)

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Acetone (1) - Liquid x2[mol/mol] of Methyl Alcohol (2) - Liquid y1[mol/mol] of Acetone (1) - Vapour y2[mol/mol] of Methyl Alcohol (2) - Vapour
345.95 0.0188 0.3778 0.0912 0.6450
340.65 0.0253 0.6722 0.0773 0.7869
342.35 0.0331 0.5564 0.0953 0.7191
337.35 0.0429 0.8710 0.0945 0.8710
337.55 0.0449 0.8439 0.1018 0.8496
343.15 0.0628 0.3042 0.2731 0.4420
345.95 0.0639 0.1166 0.4383 0.2690
340.65 0.0724 0.4985 0.2176 0.6139
337.85 0.0757 0.7150 0.1830 0.7230
342.85 0.0840 0.0401 0.6037 0.0858
340.75 0.0905 0.3940 0.3042 0.4955
342.85 0.0910 0.1828 0.4154 0.3280
341.75 0.0952 0.2668 0.3817 0.3746
337.55 0.0971 0.6271 0.2352 0.6615
335.65 0.1120 0.7580 0.2312 0.7180
338.75 0.1314 0.3729 0.3633 0.4565
338.25 0.1515 0.4050 0.3827 0.4400
338.75 0.1665 0.2395 0.4771 0.2904
334.25 0.1696 0.7026 0.2960 0.6407
337.85 0.1697 0.3776 0.4226 0.4126
337.05 0.1758 0.4412 0.3955 0.4543
337.05 0.1954 0.3476 0.4190 0.3970
337.35 0.2191 0.1954 0.5742 0.2206
333.45 0.2238 0.6497 0.3800 0.5694
336.75 0.2365 0.0795 0.6920 0.1055
334.05 0.2708 0.4974 0.4574 0.4505
335.95 0.2712 0.2395 0.5813 0.2482
333.75 0.2712 0.5115 0.4612 0.4500
334.65 0.2950 0.3475 0.5210 0.3543
333.45 0.3155 0.4865 0.4865 0.4265
334.85 0.3314 0.2956 0.5614 0.2563
335.25 0.3330 0.1383 0.7007 0.1461
331.85 0.3343 0.5475 0.5000 0.4550
331.75 0.3510 0.4905 0.4935 0.4700
330.65 0.3842 0.5793 0.4972 0.4871
333.75 0.3875 0.3073 0.5952 0.2795
334.05 0.4085 0.1134 0.7150 0.1039
332.95 0.4242 0.2615 0.6447 0.2145
334.25 0.4315 0.0940 0.7437 0.0966
329.65 0.4715 0.4745 0.5726 0.4050
333.15 0.4722 0.1043 0.7366 0.1088
332.65 0.4778 0.1572 0.7239 0.1185
332.55 0.5290 0.0865 0.7910 0.0605
329.65 0.5590 0.3807 0.6334 0.3396
331.25 0.5702 0.2035 0.7211 0.1687
330.65 0.6140 0.2002 0.7315 0.1770
330.95 0.6209 0.1633 0.7545 0.1388
330.75 0.6750 0.1025 0.7865 0.1080
329.15 0.7444 0.1880 0.7832 0.1805
329.25 0.7529 0.1708 0.7852 0.1764
329.65 0.8100 0.0871 0.8370 0.0933
330.15 0.8220 0.0406 0.8686 0.0633
329.35 0.8536 0.0497 0.8846 0.0569
329.65 0.8993 0.0370 0.9391 0.0434

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Acetone (1) - Liquid x2[mol/mol] of Methyl Alcohol (2) - Liquid y1[mol/mol] of Acetone (1) - Vapour y2[mol/mol] of Methyl Alcohol (2) - Vapour
343.15 0.1000 0.1000 0.6100 0.1300
343.15 0.1000 0.2000 0.5200 0.2400
342.55 0.1000 0.3000 0.4300 0.3550
341.95 0.1000 0.4000 0.3700 0.4500
341.15 0.1000 0.5000 0.3200 0.5400
339.65 0.1000 0.6000 0.2600 0.6300
338.15 0.1000 0.7000 0.2200 0.7100
336.65 0.1000 0.8000 0.1850 0.7800
338.15 0.2000 0.1000 0.7200 0.0700
338.65 0.2000 0.2000 0.6350 0.1800
338.65 0.2000 0.3000 0.5600 0.2800
337.65 0.2000 0.4000 0.5000 0.3700
336.65 0.2000 0.5000 0.4400 0.4700
335.65 0.2000 0.6000 0.3850 0.5500
334.15 0.2000 0.7000 0.3400 0.6250
335.95 0.3000 0.1000 0.7600 0.0650
335.85 0.3000 0.2000 0.7000 0.1500
335.45 0.3000 0.3000 0.6250 0.2550
334.65 0.3000 0.4000 0.5700 0.3450
333.65 0.3000 0.5000 0.5200 0.4150
332.65 0.3000 0.6000 0.4650 0.5000
334.65 0.4000 0.1000 0.7900 0.0600
333.95 0.4000 0.2000 0.7250 0.1550
333.15 0.4000 0.3000 0.6700 0.2420
332.55 0.4000 0.4000 0.6150 0.3220
331.55 0.4000 0.5000 0.5650 0.4020
333.15 0.5000 0.1000 0.8100 0.0650
332.55 0.5000 0.2000 0.7500 0.1600
331.75 0.5000 0.3000 0.7000 0.2320
330.75 0.5000 0.4000 0.6500 0.3170
332.25 0.6000 0.1000 0.8200 0.0800
331.45 0.6000 0.2000 0.7700 0.1630
330.45 0.6000 0.3000 0.7200 0.2450
331.35 0.7000 0.1000 0.8270 0.0950
330.35 0.7000 0.2000 0.7780 0.1840
330.35 0.8000 0.1000 0.8600 0.1000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Acetone (1) - Liquid x2[mol/mol] of Methyl Alcohol (2) - Liquid y1[mol/mol] of Acetone (1) - Vapour y2[mol/mol] of Methyl Alcohol (2) - Vapour
337.9 0.2000 0.2000 0.2290 0.5970
337.21 0.4000 0.2000 0.4140 0.4540
335.2 0.6000 0.2000 0.5570 0.3710
333.67 0.2000 0.4000 0.1910 0.6820
332.33 0.4000 0.4000 0.3480 0.5800
331.0 0.2000 0.6000 0.1840 0.7350

Sources