Mixture of Isopropyl Alcohol + Methyl Alcohol + Water

Excel

Isopropyl Alcohol

Name
Isopropyl Alcohol
InChI
InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3
InChI Key
KFZMGEQAYNKOFK-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CC(C)O
Mol. Weight (g/mol)
60.09
CAS
67-63-0

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 Methyl Alcohol (2) - Liquid x2[mol/mol] of Isopropyl Alcohol (1) - Liquid y1[mol/mol] of Methyl Alcohol (2) - Vapour y2[mol/mol] of Isopropyl Alcohol (1) - Vapour
353.95 0.0500 0.9000 0.0700 0.8500
353.25 0.0570 0.3790 0.1340 0.5020
353.85 0.0700 0.8500 0.0950 0.8200
352.45 0.0760 0.5940 0.1210 0.5840
353.15 0.0780 0.8340 0.1370 0.7490
352.85 0.0820 0.4830 0.1210 0.5350
353.05 0.0840 0.4280 0.1400 0.5070
354.15 0.0850 0.1700 0.1800 0.4000
352.95 0.0870 0.5150 0.1560 0.5210
352.85 0.0910 0.4900 0.1500 0.5280
352.35 0.0920 0.7300 0.1500 0.6500
352.45 0.0950 0.5940 0.1260 0.5880
352.25 0.0950 0.7250 0.1750 0.6500
353.75 0.1000 0.1900 0.2050 0.3850
352.75 0.1000 0.7990 0.1570 0.7190
352.15 0.1200 0.7000 0.1650 0.6400
352.35 0.1400 0.1600 0.2980 0.3250
351.25 0.1500 0.5440 0.2370 0.4990
351.65 0.1710 0.3180 0.2720 0.3910
352.65 0.1740 0.0850 0.3770 0.2400
351.35 0.1760 0.4080 0.2640 0.4290
350.95 0.1820 0.5240 0.2760 0.4750
351.75 0.1860 0.1950 0.3240 0.3140
352.25 0.1900 0.1080 0.3840 0.2440
350.85 0.1970 0.6060 0.3060 0.5040
350.35 0.2400 0.4200 0.3600 0.3900
350.15 0.2450 0.4350 0.3950 0.3750
350.05 0.2700 0.6400 0.3700 0.5250
349.85 0.2900 0.4150 0.4100 0.3650
349.25 0.3150 0.5850 0.4150 0.4700
349.05 0.3230 0.5950 0.4720 0.4420
348.35 0.3560 0.4340 0.4780 0.3510
348.25 0.3580 0.2890 0.4980 0.2750
348.45 0.3650 0.5480 0.5110 0.4050
347.75 0.3850 0.2850 0.5370 0.2560
347.85 0.3850 0.4150 0.5160 0.3260
347.75 0.3880 0.5220 0.5370 0.3620
347.65 0.3950 0.2050 0.5600 0.2050
347.15 0.4080 0.4820 0.5620 0.3370
347.35 0.4100 0.2280 0.5820 0.2080
347.35 0.4160 0.3610 0.5560 0.2880
346.95 0.4450 0.3510 0.5920 0.2660
346.65 0.4640 0.2220 0.6390 0.1750
346.45 0.4820 0.3190 0.6410 0.2320
346.35 0.5000 0.3510 0.6450 0.2510
345.95 0.5010 0.2470 0.6600 0.1920
345.65 0.5400 0.2150 0.7050 0.1600
345.25 0.5620 0.3090 0.7010 0.2080
345.15 0.5700 0.2150 0.7270 0.1560
344.75 0.6150 0.1750 0.7500 0.1400
344.45 0.6300 0.1800 0.7800 0.1100
344.35 0.6400 0.1650 0.7700 0.1300
342.25 0.7620 0.1150 0.8520 0.0800
341.75 0.7910 0.0960 0.8890 0.0640
341.25 0.8110 0.0930 0.8880 0.0600
340.25 0.8870 0.0650 0.9360 0.0380

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Methyl Alcohol (2) - Liquid x2[mol/mol] of Isopropyl Alcohol (1) - Liquid y1[mol/mol] of Methyl Alcohol (2) - Vapour y2[mol/mol] of Isopropyl Alcohol (1) - Vapour
362.75 0.0320 0.0130 0.1920 0.1310
361.65 0.0340 0.0250 0.1740 0.1590
359.05 0.0690 0.0250 0.2270 0.1710
356.05 0.1220 0.0390 0.3530 0.1560
356.35 0.1270 0.0200 0.4110 0.1140
351.95 0.1780 0.3350 0.2290 0.4210
351.25 0.2250 0.2510 0.3240 0.3380
351.25 0.2460 0.1310 0.3980 0.2020
350.95 0.2760 0.1460 0.4360 0.2280
350.35 0.3030 0.0310 0.6160 0.0600
350.15 0.3040 0.1940 0.4320 0.2600
348.35 0.3450 0.0650 0.6280 0.1060
349.15 0.3510 0.1960 0.4880 0.2390
348.45 0.3630 0.5360 0.4950 0.4130
348.25 0.3820 0.1900 0.5330 0.2130
348.05 0.4090 0.0910 0.6220 0.1250
347.15 0.4540 0.0840 0.6660 0.1030
346.25 0.4980 0.1500 0.6670 0.1440
345.95 0.4990 0.3640 0.6410 0.2630
346.05 0.5080 0.1370 0.6820 0.1270
344.65 0.6000 0.0960 0.7590 0.0780
344.25 0.6080 0.1200 0.7760 0.0870
343.85 0.6260 0.1370 0.7800 0.1020
343.45 0.6520 0.1270 0.8010 0.0900
342.15 0.7370 0.0910 0.8460 0.0700
341.75 0.7430 0.1910 0.8570 0.1100
340.55 0.8120 0.1430 0.8920 0.0870

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Methyl Alcohol (2) - Liquid x2[mol/mol] of Isopropyl Alcohol (1) - Liquid y1[mol/mol] of Methyl Alcohol (2) - Vapour y2[mol/mol] of Isopropyl Alcohol (1) - Vapour
353.35 0.0860 0.1410 0.1980 0.4020
351.45 0.1000 0.3150 0.1780 0.4620
350.95 0.1130 0.5150 0.1990 0.4890
353.35 0.1320 0.0730 0.2700 0.3910
353.35 0.1430 0.0540 0.3960 0.2150
350.75 0.1700 0.2050 0.3260 0.3400
352.75 0.1750 0.0580 0.4310 0.2050
351.05 0.1940 0.0710 0.4420 0.2080
352.15 0.1940 0.1480 0.3860 0.2850
350.75 0.2080 0.0910 0.4440 0.2210
350.95 0.2300 0.0900 0.4700 0.1990
349.65 0.2480 0.1540 0.4380 0.2500
348.05 0.3080 0.1790 0.5260 0.2230
346.85 0.4190 0.1340 0.6250 0.1620
345.95 0.4420 0.1300 0.6340 0.1490
344.75 0.5470 0.1030 0.7480 0.0980

Sources