Mixture of Isopropyl Alcohol + Acetone + 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

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

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 (2)
  2. Vapor Liquid Equilibrium at Constant Temperature

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 Isopropyl Alcohol (1) - Liquid y1[mol/mol] of Acetone (2) - Vapour y2[mol/mol] of Isopropyl Alcohol (1) - Vapour
363.15 0.0030 0.0120 0.1400 0.1780
355.15 0.0040 0.0750 0.0970 0.4050
353.15 0.0040 0.5900 0.0150 0.6140
353.15 0.0040 0.6440 0.0090 0.6600
353.15 0.0050 0.6900 0.0150 0.6850
353.15 0.0050 0.8020 0.0150 0.7700
353.15 0.0080 0.7440 0.0190 0.7150
353.15 0.0090 0.2430 0.1020 0.4640
353.15 0.0090 0.3860 0.0530 0.5300
353.15 0.0090 0.7660 0.0150 0.7440
363.15 0.0100 0.0080 0.2120 0.1020
353.15 0.0100 0.5200 0.0300 0.5900
353.15 0.0110 0.0740 0.2240 0.3250
355.15 0.0120 0.0620 0.1380 0.3720
353.15 0.0130 0.0720 0.2180 0.3360
355.15 0.0140 0.0440 0.2180 0.2930
353.15 0.0160 0.1510 0.1350 0.4350
353.15 0.0160 0.2780 0.0900 0.4800
353.15 0.0170 0.9410 0.0880 0.8580
353.15 0.0175 0.1750 0.1220 0.4480
355.15 0.0180 0.0450 0.2140 0.2920
355.15 0.0200 0.0190 0.3490 0.1530
353.15 0.0260 0.0200 0.4100 0.1420
350.15 0.0340 0.0360 0.4520 0.1650
348.15 0.0420 0.0190 0.5770 0.0780
348.15 0.0470 0.0220 0.5510 0.1010
350.15 0.0470 0.1780 0.2860 0.3440
346.15 0.0500 0.0400 0.5250 0.1400
350.15 0.0590 0.4660 0.1760 0.4780
348.15 0.0650 0.1300 0.3770 0.2660
346.15 0.0780 0.0950 0.4600 0.2110
348.15 0.0820 0.2940 0.3280 0.3420
343.15 0.0830 0.0360 0.6320 0.0860
348.15 0.0900 0.4800 0.2840 0.4210
348.15 0.1050 0.6100 0.2700 0.4960
348.15 0.1080 0.6750 0.2730 0.5310
342.15 0.1100 0.0500 0.6380 0.1080
346.15 0.1240 0.2900 0.4000 0.2960
341.15 0.1320 0.0530 0.6420 0.1090
346.15 0.1400 0.5800 0.3380 0.4560
342.15 0.1480 0.1140 0.5890 0.1570
343.15 0.1550 0.1500 0.5300 0.1940
339.15 0.1660 0.0240 0.7280 0.0410
341.15 0.1900 0.1200 0.6000 0.1500
343.15 0.1920 0.2810 0.4920 0.2550
338.15 0.1980 0.0340 0.7310 0.0490
339.15 0.2050 0.0680 0.6800 0.0970
342.15 0.2120 0.1820 0.5370 0.2190
343.15 0.2260 0.5320 0.4770 0.3560
343.15 0.2270 0.5500 0.4740 0.3660
342.15 0.2360 0.3360 0.5200 0.2560
338.15 0.2460 0.0570 0.7370 0.0370
339.15 0.2530 0.1100 0.6520 0.1270
342.15 0.2620 0.4920 0.4970 0.3330
341.15 0.2660 0.2820 0.5600 0.2200
337.15 0.2690 0.0520 0.7470 0.0460
341.15 0.2940 0.4840 0.5450 0.3080
339.15 0.3240 0.1970 0.6400 0.1640
338.15 0.3440 0.1750 0.6870 0.1170
336.15 0.3560 0.0640 0.7450 0.0590
339.15 0.3760 0.4210 0.6160 0.2590
338.15 0.3820 0.2740 0.6390 0.1890
337.15 0.3850 0.1750 0.7020 0.1140
337.15 0.3890 0.2120 0.6740 0.1540
338.15 0.3990 0.4150 0.6570 0.2290
335.15 0.4100 0.0390 0.7660 0.0510
338.15 0.4150 0.4650 0.6730 0.2500
337.15 0.4360 0.3860 0.6830 0.2120
337.15 0.4380 0.3000 0.6790 0.1750
336.15 0.4480 0.1750 0.7160 0.1250
335.15 0.4580 0.0650 0.7700 0.0600
336.15 0.4600 0.2280 0.6980 0.1430
336.15 0.4660 0.3100 0.7050 0.1730
335.15 0.5020 0.1610 0.7460 0.0950
334.15 0.5230 0.0670 0.7990 0.0430
335.15 0.5240 0.2670 0.7310 0.1530
335.15 0.5510 0.2970 0.7400 0.1690
333.15 0.5690 0.0500 0.8260 0.0260
334.15 0.5850 0.1770 0.7780 0.1030
334.15 0.6200 0.2610 0.7950 0.1440
333.15 0.6250 0.1260 0.8000 0.0700
332.15 0.6520 0.0620 0.8370 0.0310
333.15 0.6730 0.2110 0.8380 0.1030
332.15 0.6990 0.1050 0.8550 0.0400
332.15 0.7360 0.1730 0.8600 0.0930
331.15 0.7570 0.0590 0.8650 0.0360
331.15 0.8080 0.1300 0.9010 0.0520

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 Isopropyl Alcohol (1) - Liquid y1[mol/mol] of Acetone (2) - Vapour y2[mol/mol] of Isopropyl Alcohol (1) - Vapour
334.05 0.2000 0.6000 0.1040 0.7880
338.4 0.4000 0.4000 0.2220 0.6590
344.6 0.6000 0.2000 0.4140 0.4280
337.25 0.2000 0.4000 0.1140 0.7050
343.85 0.4000 0.2000 0.2970 0.4660
343.01 0.2000 0.2000 0.2090 0.5460

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 348.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Acetone (2) - Liquid x2[mol/mol] of Isopropyl Alcohol (1) - Liquid y1[mol/mol] of Acetone (2) - Vapour y2[mol/mol] of Isopropyl Alcohol (1) - Vapour
158.77 0.3150 0.5850 0.1837 0.7321
154.65 0.2900 0.5200 0.1658 0.7002
150.27 0.2450 0.4550 0.1531 0.6724
144.811 0.2100 0.3900 0.1431 0.6517
139.561 0.1750 0.3250 0.1376 0.6337
134.87 0.1400 0.2600 0.1366 0.6175
128.2 0.1050 0.1950 0.1361 0.5988
123.321 0.0700 0.1300 0.1463 0.5733
105.71 0.0350 0.0650 0.1511 0.5096

Sources