Mixture of Benzene + Ethanol + 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

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

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. Vapor Liquid Equilibrium at Constant Temperature (2)

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Ethanol (2) - Liquid x2[mol/mol] of Benzene (1) - Liquid y1[mol/mol] of Ethanol (2) - Vapour y2[mol/mol] of Benzene (1) - Vapour
349.25 0.2440 0.0042 0.5030 0.1380
348.9 0.2450 0.0050 0.4700 0.1520
348.15 0.2480 0.0062 0.4490 0.1910
347.15 0.2495 0.0073 0.4250 0.2270
346.4 0.2500 0.0085 0.4070 0.2750
345.9 0.2500 0.0097 0.3820 0.3010
345.4 0.2500 0.0110 0.3650 0.3350
344.9 0.2510 0.0126 0.3480 0.3780
344.4 0.2510 0.0140 0.3280 0.4100
343.4 0.2510 0.0157 0.3120 0.4240
343.7 0.2700 0.0180 0.3540 0.3660
343.4 0.2705 0.0195 0.3360 0.4030
342.9 0.2708 0.0212 0.3240 0.4270
342.4 0.2708 0.0232 0.2940 0.4580
340.4 0.2715 0.0322 0.2580 0.5300
339.9 0.2715 0.0343 0.2580 0.5300
341.65 0.2720 0.0270 0.2920 0.4770
340.9 0.2720 0.0305 0.2790 0.5010
339.15 0.3854 0.5390 0.3310 0.5370
339.2 0.3870 0.5400 0.3340 0.5370
339.25 0.3880 0.5400 0.3370 0.5370
339.3 0.3910 0.5410 0.3430 0.5370
339.35 0.3940 0.5410 0.3460 0.5375
339.35 0.3950 0.5420 0.3470 0.5370
339.4 0.3970 0.5415 0.3495 0.5370
343.8 0.4564 0.0416 0.4060 0.3530
344.9 0.4580 0.0342 0.4300 0.3190
349.15 0.4661 0.0139 0.5475 0.1355
349.15 0.4665 0.0135 0.5500 0.1235
348.15 0.4675 0.0198 0.4920 0.2030
348.9 0.4676 0.0154 0.5290 0.1380
348.65 0.4676 0.0174 0.4990 0.1835
348.75 0.8647 0.0317 0.7695 0.1260
349.0 0.8664 0.0296 0.7760 0.1175
349.15 0.8695 0.0265 0.7865 0.1055
349.4 0.8740 0.0240 0.7960 0.0960
349.65 0.8758 0.0222 0.8055 0.0875
349.65 0.8770 0.0200 0.8120 0.0810
349.75 0.8780 0.0180 0.8200 0.0720

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 308.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Ethanol (2) - Liquid x2[mol/mol] of Benzene (1) - Liquid y1[mol/mol] of Ethanol (2) - Vapour y2[mol/mol] of Benzene (1) - Vapour
25.598 0.9820 0.0140 0.7450 0.0920
28.264 0.8990 0.0800 0.6920 0.1790
28.798 0.8160 0.1450 0.6600 0.2000
29.198 0.7460 0.1970 0.6520 0.2080
28.931 0.6490 0.2550 0.6440 0.2160
28.531 0.5080 0.3200 0.6400 0.2200
25.598 0.0010 0.0560 0.7450 0.0920
28.264 0.0030 0.1540 0.6920 0.1790
28.798 0.0150 0.2410 0.6600 0.2000
29.198 0.0330 0.2980 0.6520 0.2080
28.931 0.0640 0.3480 0.6440 0.2160
28.531 0.1240 0.3860 0.6400 0.2200

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 318.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Ethanol (2) - Liquid x2[mol/mol] of Benzene (1) - Liquid y1[mol/mol] of Ethanol (2) - Vapour y2[mol/mol] of Benzene (1) - Vapour
39.73 0.9790 0.0170 0.7320 0.0960
44.796 0.8890 0.0860 0.6360 0.1930
45.863 0.8010 0.1560 0.6450 0.2050
46.13 0.7270 0.2130 0.6300 0.2150
45.863 0.6190 0.2700 0.6350 0.2200
39.73 0.0010 0.0510 0.7320 0.0960
44.796 0.0030 0.1400 0.6360 0.1930
45.863 0.0120 0.2170 0.6450 0.2050
46.13 0.0270 0.2700 0.6300 0.2150
45.863 0.0530 0.3200 0.6350 0.2200

Sources