Mixture of Ethanol + 1-Butanol + 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

1-Butanol

Name
1-Butanol
InChI
InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
InChI Key
LRHPLDYGYMQRHN-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CCCCO
Mol. Weight (g/mol)
74.12
CAS
71-36-3

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 (3)

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 96.66 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Ethyl Acetate (3) - Liquid x2[mol/mol] of Ethanol (1) - Liquid y1[mol/mol] of Ethyl Acetate (3) - Vapour y2[mol/mol] of Ethanol (1) - Vapour
346.15 0.2191 0.6598 0.3360 0.5763
346.05 0.2345 0.5937 0.3358 0.6018
346.95 0.3084 0.4581 0.4063 0.5523
346.15 0.3805 0.3992 0.4652 0.4877
346.85 0.5544 0.2082 0.5925 0.2551
347.15 0.6880 0.1011 0.6811 0.1626
345.35 0.4725 0.3698 0.4931 0.4740
348.65 0.0796 0.7861 0.1734 0.7418
348.65 0.3930 0.3822 0.5152 0.4359
347.95 0.4130 0.3563 0.5101 0.4038
348.15 0.4243 0.2374 0.5229 0.2882
348.85 0.5039 0.2519 0.5915 0.3514
348.65 0.6124 0.1101 0.6632 0.1508
348.55 0.7188 0.0509 0.7483 0.0741
348.15 0.8098 0.0408 0.8102 0.0515
347.35 0.8072 0.0933 0.8072 0.1746
354.95 0.1437 0.4143 0.3135 0.5609
352.95 0.2010 0.4168 0.3769 0.5319
349.45 0.2443 0.4855 0.3768 0.5651
349.65 0.6725 0.0615 0.7309 0.0949
361.15 0.1058 0.2806 0.2749 0.5266
358.65 0.1177 0.2894 0.2816 0.4673
360.05 0.1031 0.3217 0.2765 0.5484
358.55 0.1298 0.3154 0.3242 0.5021
358.45 0.1707 0.2058 0.3793 0.3105
363.35 0.1780 0.1562 0.4603 0.2907
364.95 0.1158 0.1774 0.3434 0.3845
366.75 0.1161 0.1517 0.4130 0.2781
361.55 0.1009 0.1629 0.2678 0.4864
367.25 0.0821 0.1375 0.2696 0.4009
369.65 0.0935 0.0657 0.3542 0.2355
371.25 0.0621 0.0687 0.2218 0.3667
375.85 0.0389 0.0634 0.1699 0.3017
381.05 0.0195 0.0311 0.0913 0.2097
387.9 0.0077 0.0088 0.0513 0.0310

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Ethyl Acetate (3) - Liquid x2[mol/mol] of Ethanol (1) - Liquid y1[mol/mol] of Ethyl Acetate (3) - Vapour y2[mol/mol] of Ethanol (1) - Vapour
347.95 0.4390 0.4640 0.4960 0.4720
347.85 0.4610 0.4410 0.5100 0.4630
347.85 0.4800 0.4100 0.5280 0.4450
348.05 0.5020 0.4000 0.5450 0.4300
347.95 0.5290 0.3710 0.5620 0.4110
348.05 0.5560 0.3420 0.5880 0.3890
348.25 0.6610 0.2410 0.6650 0.3090
349.75 0.7560 0.1410 0.7700 0.2030
353.85 0.2030 0.5150 0.3410 0.5840
352.85 0.3400 0.3930 0.4750 0.4600
352.75 0.3520 0.3810 0.4880 0.4460
352.65 0.3780 0.3610 0.5060 0.4270
352.15 0.4020 0.3430 0.5280 0.4080
352.25 0.4220 0.3240 0.5400 0.3950
352.25 0.4410 0.3060 0.5600 0.3760
352.35 0.4550 0.2930 0.5740 0.3610
352.45 0.4870 0.2690 0.6010 0.3360
352.35 0.5430 0.2250 0.6380 0.2980
354.45 0.5560 0.1380 0.7040 0.2050
352.55 0.5590 0.2020 0.6580 0.2750
355.75 0.6210 0.0695 0.7870 0.1130
359.75 0.0296 0.5830 0.0716 0.7960
358.55 0.1280 0.4590 0.2650 0.5990
358.05 0.3240 0.2400 0.5200 0.3450
357.45 0.3580 0.2100 0.5590 0.3060
357.35 0.3820 0.1910 0.5880 0.2830
357.65 0.4110 0.1810 0.6080 0.2640
357.45 0.4240 0.1570 0.6300 0.2400
357.75 0.4460 0.1370 0.6570 0.2120
357.95 0.4660 0.1190 0.6820 0.1870
358.25 0.4990 0.0883 0.7210 0.1420
358.75 0.5300 0.0608 0.7580 0.0996
363.75 0.0233 0.4770 0.0599 0.7520
362.65 0.0975 0.3810 0.2310 0.5810
361.75 0.1880 0.2660 0.4020 0.4110
362.05 0.3120 0.1300 0.5710 0.2230
362.55 0.3250 0.1070 0.5950 0.1900
362.55 0.3390 0.1050 0.6110 0.1850
362.15 0.3740 0.0931 0.6440 0.1620
361.45 0.3960 0.0852 0.6620 0.1440
361.35 0.4280 0.0594 0.7000 0.1050
361.05 0.4590 0.0399 0.7320 0.0725
362.85 0.4690 0.0184 0.7650 0.0337
367.95 0.0368 0.3460 0.1010 0.6240
366.95 0.0969 0.2480 0.2670 0.4720
367.15 0.1440 0.1890 0.3620 0.3570
366.75 0.2210 0.1070 0.5020 0.2140
366.75 0.2920 0.0597 0.6010 0.1140
366.85 0.3010 0.0451 0.6270 0.0912
366.65 0.3170 0.0377 0.6470 0.0756
366.15 0.3520 0.0234 0.6810 0.0478
366.05 0.3660 0.0163 0.6920 0.0324
365.85 0.3820 0.0093 0.7260 0.0191
372.05 0.0275 0.2520 0.0775 0.5410
371.25 0.0530 0.2210 0.1520 0.4800
370.95 0.0799 0.1940 0.2240 0.4110
370.65 0.1020 0.1600 0.2890 0.3450
370.25 0.1340 0.1260 0.3710 0.2710
369.45 0.1610 0.1110 0.4270 0.2330
369.55 0.1750 0.0954 0.4480 0.1990
369.55 0.1870 0.0797 0.4780 0.1680
369.25 0.2120 0.0679 0.5210 0.1470
369.35 0.2160 0.0491 0.5290 0.1040
369.45 0.2290 0.0341 0.5610 0.0769
369.65 0.2400 0.0206 0.5900 0.0462
369.65 0.2650 0.0088 0.6100 0.0204
377.95 0.0148 0.1370 0.0562 0.3810
377.95 0.0155 0.1410 0.0569 0.3880
377.05 0.0285 0.1330 0.1010 0.3730
377.05 0.0461 0.1250 0.1490 0.3230
377.05 0.0574 0.1040 0.1950 0.2730
377.05 0.0733 0.0864 0.2400 0.2290
376.85 0.0918 0.0684 0.2900 0.1780
376.55 0.0949 0.0577 0.3330 0.1620
376.35 0.1160 0.0536 0.3500 0.1300
375.95 0.1210 0.0442 0.3820 0.1150
375.85 0.1340 0.0370 0.4150 0.0965
375.55 0.1490 0.0287 0.4340 0.0718
375.65 0.1510 0.0183 0.4590 0.0475
375.45 0.1660 0.0095 0.4780 0.0240
383.65 0.0091 0.0768 0.0361 0.2510
383.15 0.0190 0.0789 0.0661 0.2330
383.05 0.0308 0.0495 0.1180 0.1630
382.45 0.0501 0.0367 0.1770 0.1130
382.45 0.0661 0.0175 0.2350 0.0537
382.45 0.0734 0.0018 0.2830 0.0166
382.45 0.0761 0.0033 0.2810 0.0113
382.45 0.0761 0.0019 0.2860 0.0067

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Ethyl Acetate (3) - Liquid x2[mol/mol] of Ethanol (1) - Liquid
348.9 0.3803 0.4579
352.2 0.7184 0.0510
365.7 0.1061 0.2801

Sources