Mixture of Ethyl Acetate + Methyl Alcohol + Water

Excel

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

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
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

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 Methyl Alcohol (2) - Liquid x2[mol/mol] of Ethyl Acetate (1) - Liquid y1[mol/mol] of Methyl Alcohol (2) - Vapour y2[mol/mol] of Ethyl Acetate (1) - Vapour
346.85 0.0210 0.9420 0.0570 0.8500
345.05 0.0580 0.9010 0.1460 0.7770
345.55 0.0610 0.9110 0.1710 0.7780
342.65 0.0640 0.8740 0.1520 0.7090
343.35 0.0670 0.8380 0.1460 0.6900
342.75 0.0670 0.8430 0.0990 0.6940
343.75 0.0820 0.8670 0.1880 0.7160
340.95 0.1150 0.6890 0.1940 0.6040
341.35 0.1190 0.7060 0.2040 0.5900
340.85 0.1200 0.7340 0.2280 0.6180
340.85 0.1210 0.7430 0.2190 0.6170
342.55 0.1220 0.8330 0.2600 0.6810
341.05 0.1310 0.5540 0.1830 0.5720
353.15 0.1390 0.0050 0.4310 0.1720
355.15 0.1580 0.0140 0.5260 0.0470
340.05 0.1960 0.7260 0.3020 0.5960
340.25 0.2040 0.5280 0.2900 0.5220
340.65 0.2160 0.3760 0.2690 0.5190
339.95 0.2190 0.5620 0.2890 0.5200
340.55 0.2200 0.3870 0.2350 0.5470
349.15 0.2480 0.0110 0.5360 0.1550
340.55 0.2540 0.2970 0.3010 0.4810
339.95 0.2600 0.4300 0.3120 0.4900
347.55 0.2620 0.0040 0.6140 0.0620
339.95 0.2870 0.3570 0.3330 0.4610
341.25 0.2890 0.1380 0.3560 0.4190
342.55 0.2940 0.0650 0.4130 0.3490
339.55 0.2970 0.4220 0.3500 0.4680
339.35 0.3040 0.4630 0.3790 0.4820
338.45 0.3060 0.6320 0.4290 0.5140
339.95 0.3130 0.3250 0.3610 0.4410
340.45 0.3240 0.2180 0.3740 0.4210
340.65 0.3280 0.1800 0.3830 0.4110
340.05 0.3290 0.2880 0.3710 0.4290
338.05 0.3290 0.5930 0.4450 0.4810
346.25 0.3300 0.0190 0.5720 0.1730
347.75 0.3570 0.0090 0.6540 0.0800
340.85 0.3680 0.1370 0.4340 0.3570
338.45 0.3780 0.4440 0.4570 0.4350
340.15 0.3810 0.2080 0.4270 0.3820
342.65 0.3850 0.0590 0.5220 0.2640
341.75 0.3880 0.0870 0.4880 0.3090
339.25 0.4050 0.2750 0.4450 0.3940
344.25 0.4190 0.0310 0.6130 0.1750
340.55 0.4250 0.1380 0.4860 0.3290
339.35 0.4380 0.2210 0.4800 0.3610
341.85 0.4710 0.0680 0.5800 0.2370
344.95 0.4870 0.0150 0.7140 0.0830
338.35 0.5140 0.2560 0.5440 0.3390
342.25 0.5240 0.0500 0.6540 0.1790
340.55 0.5280 0.0970 0.5940 0.2500
340.85 0.5330 0.0800 0.6220 0.2220
336.85 0.5470 0.3670 0.5950 0.3570
340.25 0.5520 0.1060 0.6050 0.2450
343.25 0.5700 0.0210 0.7350 0.0840
340.95 0.5890 0.0630 0.6800 0.1730
336.95 0.6080 0.2840 0.6210 0.3160
339.05 0.6260 0.1260 0.6590 0.2380
336.35 0.6390 0.2880 0.6560 0.3040
339.55 0.6660 0.0830 0.7200 0.1840
341.25 0.6700 0.0280 0.7970 0.0820
337.05 0.6970 0.1780 0.6810 0.2610
336.45 0.7070 0.2110 0.7080 0.2580
336.85 0.7830 0.1360 0.7690 0.1960
338.65 0.8300 0.0470 0.8580 0.0880

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 Ethyl Acetate (1) - Liquid y1[mol/mol] of Methyl Alcohol (2) - Vapour y2[mol/mol] of Ethyl Acetate (1) - Vapour
335.85 0.7150 0.2410 0.6960 0.2660
343.1 0.7500 0.1820 0.7390 0.2230
336.2 0.5860 0.3410 0.6210 0.3280
336.55 0.6450 0.2560 0.6470 0.2890
336.55 0.5550 0.3670 0.5970 0.3420
336.9 0.4350 0.5230 0.5460 0.4050
337.1 0.7850 0.1120 0.7810 0.1420
337.15 0.4650 0.4500 0.5370 0.3820
337.25 0.5080 0.3730 0.5590 0.3550
337.5 0.5200 0.3280 0.5570 0.3430
337.6 0.6800 0.1630 0.6870 0.2160
337.65 0.3500 0.5990 0.4780 0.4480
337.9 0.3690 0.4860 0.4540 0.4300
338.0 0.8450 0.0460 0.8670 0.0630
338.2 0.4030 0.4030 0.4560 0.4000
338.25 0.5530 0.2250 0.5810 0.3080
338.3 0.3000 0.6260 0.4380 0.4730
338.5 0.2300 0.1530 0.4970 0.1720
338.7 0.4880 0.2360 0.5270 0.3310
338.85 0.6050 0.1510 0.6370 0.2310
338.95 0.2690 0.6100 0.3870 0.4860
339.0 0.6310 0.1290 0.6630 0.2000
339.0 0.6960 0.0930 0.7330 0.1000
339.05 0.3370 0.4070 0.3850 0.4360
339.15 0.2360 0.7090 0.4010 0.5170
339.55 0.3900 0.2600 0.4340 0.3800
339.55 0.2710 0.4610 0.3330 0.4720
339.6 0.7180 0.0600 0.7770 0.0820
339.8 0.3160 0.3250 0.3600 0.4380
339.95 0.4370 0.1810 0.4990 0.3230
340.05 0.3310 0.2660 0.3790 0.4150
340.05 0.6310 0.0730 0.7090 0.1120
340.05 0.3870 0.2080 0.4430 0.3620
340.4 0.5060 0.1040 0.6010 0.2060
340.45 0.4450 0.1260 0.5380 0.2770
340.7 0.7500 0.0220 0.8470 0.0300
340.75 0.5360 0.0780 0.6470 0.1540
340.75 0.2700 0.2340 0.3290 0.4580
340.8 0.1250 0.7030 0.2000 0.5740
341.0 0.6500 0.0410 0.7630 0.0570
341.15 0.5050 0.0640 0.6300 0.1540
341.65 0.2520 0.1520 0.3500 0.4460
342.35 0.6760 0.0130 0.8220 0.0160
343.15 0.5550 0.0360 0.7230 0.0690
345.2 0.3920 0.0400 0.5820 0.1680
346.25 0.3300 0.0350 0.5430 0.1770
346.4 0.3210 0.0400 0.5300 0.1690
346.4 0.2680 0.0560 0.4570 0.3130
347.2 0.2280 0.0470 0.4330 0.3250
342.25 0.3610 0.0870 0.4950 0.2820

Sources