Mixture of Ethanol + Acetone + Ethyl Acetate

Excel

Ethanol

Name
Ethanol
InChI
InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3
InChI Key
LFQSCWFLJHTTHZ-UHFFFAOYSA-N
Formula
C2H6O
SMILES
CCO
Mol. Weight (g/mol)
46.07
CAS
64-17-5

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

Ethyl Acetate

Name
Ethyl Acetate
InChI
InChI=1S/C4H8O2/c1-3-6-4(2)5/h3H2,1-2H3
InChI Key
XEKOWRVHYACXOJ-UHFFFAOYSA-N
Formula
C4H8O2
SMILES
CCOC(C)=O
Mol. Weight (g/mol)
88.11
CAS
141-78-6
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Datasets

  1. Vapor Liquid Equilibrium at Constant Pressure (2)

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 Ethyl Acetate (3) - Liquid y1[mol/mol] of Acetone (2) - Vapour y2[mol/mol] of Ethyl Acetate (3) - Vapour
333.45 0.6690 0.1440 0.7500 0.1030
334.05 0.5820 0.1680 0.6850 0.1230
334.25 0.5960 0.1710 0.7020 0.1260
334.65 0.5870 0.2600 0.6840 0.1900
334.95 0.5690 0.2290 0.6660 0.1710
335.45 0.5450 0.0410 0.6730 0.0330
336.25 0.4520 0.2330 0.5780 0.1810
336.65 0.4910 0.3890 0.5890 0.2940
337.05 0.4280 0.3000 0.5140 0.2480
337.25 0.4200 0.0240 0.6030 0.0250
337.65 0.3900 0.1620 0.5110 0.1500
338.05 0.3290 0.3580 0.4700 0.2850
338.25 0.3450 0.2640 0.4460 0.2330
338.95 0.3770 0.5130 0.4960 0.3810
339.05 0.2890 0.4260 0.4120 0.3370
339.25 0.2950 0.2770 0.4080 0.2550
339.35 0.3550 0.0540 0.5040 0.0570
339.45 0.3460 0.0900 0.4740 0.0980
339.55 0.2670 0.3270 0.3810 0.2900
340.75 0.1970 0.4390 0.2820 0.3800
340.75 0.2420 0.5640 0.3560 0.4470
340.75 0.3030 0.6120 0.4180 0.4790
341.05 0.2230 0.1720 0.3360 0.1830
341.35 0.1640 0.4170 0.2390 0.3830
341.55 0.1850 0.6310 0.2760 0.5180
341.55 0.2390 0.0370 0.3930 0.0460
341.65 0.1520 0.3510 0.2380 0.3360
342.25 0.1990 0.1860 0.2920 0.2090
342.35 0.1150 0.5130 0.1830 0.4620
342.75 0.1710 0.6790 0.2480 0.5660
342.75 0.1830 0.1200 0.2930 0.1380
342.85 0.1110 0.6260 0.1670 0.5500
343.05 0.1570 0.1360 0.2530 0.1610
343.05 0.1870 0.0500 0.3130 0.0730
343.25 0.2280 0.7620 0.3410 0.6320
343.35 0.0690 0.4670 0.1070 0.4640
343.35 0.0740 0.4090 0.1180 0.4060
343.35 0.1330 0.7330 0.2040 0.6260
343.45 0.0750 0.3490 0.1210 0.3850
343.45 0.0910 0.2650 0.1490 0.2950
343.45 0.0950 0.2710 0.1460 0.3030
343.85 0.1710 0.0820 0.2830 0.1010
344.05 0.1260 0.1170 0.2110 0.1500
344.15 0.0740 0.2250 0.1290 0.2660
344.25 0.0660 0.7200 0.1060 0.6280
344.95 0.0550 0.1820 0.1030 0.2380
345.35 0.1160 0.0800 0.2040 0.1110
345.45 0.0600 0.1400 0.1200 0.1870
345.55 0.0830 0.8280 0.1350 0.7460
345.85 0.0120 0.2910 0.0260 0.3440
346.25 0.0340 0.2070 0.0380 0.2650
346.65 0.0570 0.8860 0.0940 0.8160
346.75 0.0960 0.0510 0.1840 0.0740
347.95 0.0210 0.1240 0.0320 0.1860
348.55 0.0510 0.0290 0.1140 0.0510
349.15 0.0040 0.0740 0.0160 0.1190
349.95 0.0200 0.0110 0.0560 0.0220

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 Ethyl Acetate (3) - Liquid y1[mol/mol] of Acetone (2) - Vapour y2[mol/mol] of Ethyl Acetate (3) - Vapour
343.15 0.1754 0.2069 0.2512 0.2439
339.95 0.3192 0.1691 0.4135 0.1790
336.65 0.4872 0.1224 0.6288 0.1073
333.55 0.7127 0.0638 0.7993 0.0586
343.15 0.0976 0.4052 0.1623 0.3974
339.45 0.2702 0.3441 0.4076 0.2813
334.25 0.4658 0.2382 0.5803 0.2037
333.65 0.6737 0.1415 0.7417 0.1314
343.35 0.0937 0.6040 0.1731 0.5186
339.25 0.2634 0.4973 0.4023 0.3904
336.05 0.4502 0.3795 0.5920 0.2610
333.55 0.6295 0.2372 0.7786 0.1428
344.35 0.0935 0.7595 0.1821 0.6255
339.45 0.2770 0.6074 0.4172 0.4599
335.95 0.4365 0.4771 0.5826 0.3364
333.15 0.6311 0.3064 0.7352 0.2226

Sources