Mixture of Benzene + Acetic acid, butyl ester + Ethyl Acetate + Water

Excel

Benzene

Name
Benzene
InChI
InChI=1S/C6H6/c1-2-4-6-5-3-1/h1-6H
InChI Key
UHOVQNZJYSORNB-UHFFFAOYSA-N
Formula
C6H6
SMILES
c1ccccc1
Mol. Weight (g/mol)
78.11
CAS
71-43-2

Acetic acid, butyl ester

Name
Acetic acid, butyl ester
InChI
InChI=1S/C6H12O2/c1-3-4-5-8-6(2)7/h3-5H2,1-2H3
InChI Key
DKPFZGUDAPQIHT-UHFFFAOYSA-N
Formula
C6H12O2
SMILES
CCCCOC(C)=O
Mol. Weight (g/mol)
116.16
CAS
123-86-4

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

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 Ethyl Acetate (3) - Liquid x2[mol/mol] of Water (4) - Liquid x3[mol/mol] of Benzene (1) - Liquid y1[mol/mol] of Ethyl Acetate (3) - Vapour y2[mol/mol] of Water (4) - Vapour y3[mol/mol] of Benzene (1) - Vapour
347.58 0.2000 0.6400 0.0640 0.4390 0.4010 0.1310
345.55 0.4000 0.4800 0.0480 0.5380 0.3700 0.0760
344.68 0.6000 0.3200 0.0320 0.6190 0.3330 0.0390
344.81 0.8000 0.1600 0.0160 0.6600 0.3220 0.0140
349.22 0.2000 0.4800 0.1280 0.3200 0.4270 0.2030
346.79 0.4000 0.3600 0.0960 0.4880 0.3460 0.1380
345.76 0.6000 0.2400 0.0640 0.5810 0.3340 0.0700
345.89 0.8000 0.1200 0.0320 0.6780 0.2840 0.0300
350.24 0.2000 0.3200 0.1920 0.2790 0.4010 0.2560
347.7 0.4000 0.2400 0.1440 0.4100 0.3870 0.1660
346.57 0.6000 0.1600 0.0960 0.5270 0.3550 0.0980
347.56 0.8000 0.0800 0.0480 0.6860 0.2660 0.0380
351.19 0.2000 0.1600 0.2560 0.2290 0.4490 0.2730
350.33 0.4000 0.1200 0.1920 0.3750 0.3970 0.1860
349.37 0.6000 0.0800 0.1280 0.5510 0.3000 0.1200
349.9 0.8000 0.0400 0.0640 0.7480 0.1770 0.0590
348.35 0.2000 0.6400 0.0320 0.4600 0.3990 0.0850
345.65 0.4000 0.4800 0.0240 0.5450 0.3920 0.0390
344.25 0.6000 0.3200 0.0160 0.6220 0.3420 0.0250
344.15 0.8000 0.1600 0.0080 0.6790 0.3050 0.0110
350.15 0.2000 0.4800 0.0640 0.3940 0.4100 0.1090
347.65 0.4000 0.3600 0.0480 0.5200 0.3800 0.0650
345.55 0.6000 0.2400 0.0320 0.5950 0.3500 0.0400
345.75 0.8000 0.1200 0.0160 0.7030 0.2690 0.0200
351.75 0.2000 0.3200 0.0960 0.3060 0.4240 0.1640
349.05 0.4000 0.2400 0.0720 0.4590 0.3860 0.0910
347.15 0.6000 0.1600 0.0480 0.5670 0.3460 0.0540
346.95 0.8000 0.0800 0.0240 0.7350 0.2290 0.0250
353.45 0.2000 0.1600 0.1280 0.2680 0.4490 0.1630
351.05 0.4000 0.1200 0.0960 0.4870 0.3160 0.1200
349.85 0.6000 0.0800 0.0640 0.6300 0.2590 0.0670
348.75 0.8000 0.0400 0.0320 0.7780 0.1700 0.0370
345.25 0.2000 0.6400 0.0960 0.4330 0.3210 0.2280
344.25 0.4000 0.4800 0.0720 0.5720 0.2950 0.1230
343.75 0.6000 0.3200 0.0480 0.6370 0.3040 0.0540
344.15 0.8000 0.1600 0.0240 0.6830 0.2920 0.0220
346.35 0.2000 0.4800 0.1920 0.3350 0.3100 0.3360
345.25 0.4000 0.3600 0.1440 0.4790 0.3080 0.1970
344.15 0.6000 0.2400 0.0960 0.5890 0.2900 0.1100
345.05 0.8000 0.1200 0.0480 0.6980 0.2530 0.0450
347.15 0.2000 0.3200 0.2880 0.2600 0.3030 0.3900
345.45 0.4000 0.2400 0.2160 0.4180 0.2950 0.2600
345.15 0.6000 0.1600 0.1440 0.5420 0.3010 0.1410
345.95 0.8000 0.0800 0.0720 0.7100 0.2170 0.0670
347.55 0.2000 0.1600 0.3840 0.2240 0.3130 0.4260
346.35 0.4000 0.1200 0.2880 0.3800 0.3160 0.2760
345.95 0.6000 0.0800 0.1920 0.5540 0.2510 0.1780
348.35 0.8000 0.0400 0.0960 0.7350 0.1800 0.0790

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
x1[mol/mol] of Ethyl Acetate (3) - Liquid x2[mol/mol] of Water (4) - Liquid x3[mol/mol] of Benzene (1) - Liquid y1[mol/mol] of Ethyl Acetate (3) - Vapour y2[mol/mol] of Water (4) - Vapour y3[mol/mol] of Benzene (1) - Vapour
0.6400 0.2000 0.1280 0.2970 0.4030 0.2890
0.4800 0.4000 0.0960 0.2930 0.5410 0.1610
0.3180 0.6020 0.0640 0.3420 0.5810 0.0750
0.1600 0.8000 0.0320 0.3340 0.6340 0.0310
0.4820 0.1980 0.2560 0.2960 0.2920 0.3970
0.3280 0.3630 0.2470 0.2870 0.4030 0.3000
0.2380 0.6000 0.1280 0.3350 0.5290 0.1320
0.8000 0.1200 0.0640 0.2810 0.6580 0.0590
0.3200 0.2000 0.3840 0.3490 0.2240 0.4110
0.2400 0.4000 0.2880 0.3000 0.3940 0.2940
0.1580 0.6020 0.1920 0.3000 0.5110 0.1830
0.0800 0.8000 0.0960 0.2840 0.6210 0.0920
0.2000 0.2500 0.4400 0.3050 0.2430 0.4360
0.1200 0.4000 0.3840 0.3510 0.3240 0.3120
0.0800 0.6000 0.2560 0.2740 0.5140 0.2020
0.0400 0.8000 0.1230 0.1230 0.7580 0.1140

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 Water (4) - Liquid x3[mol/mol] of Benzene (1) - Liquid
344.75 0.3000 0.1500 0.4400
343.85 0.3000 0.3500 0.2800
343.45 0.2980 0.5510 0.1210
344.45 0.6000 0.3000 0.0800
343.45 0.6000 0.1000 0.2400
343.75 0.6000 0.2000 0.1600
348.15 0.0100 0.8480 0.1040
345.85 0.1000 0.7700 0.0140
344.65 0.1490 0.7290 0.0980

Sources