Mixture of Benzene + n-Hexane + Ethanol

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

n-Hexane

Name
n-Hexane
InChI
InChI=1S/C6H14/c1-3-5-6-4-2/h3-6H2,1-2H3
InChI Key
VLKZOEOYAKHREP-UHFFFAOYSA-N
Formula
C6H14
SMILES
CCCCCC
Mol. Weight (g/mol)
86.18
CAS
110-54-3

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
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Datasets

  1. Tracer diffusion coefficient, m2/s (4)
  2. Vapor Liquid Equilibrium at Constant Pressure (2)
  3. Vapor Liquid Equilibrium at Constant Temperature

Tracer diffusion coefficient, m2/s of Benzene (1) [ref]

Operational conditions:

Solvent: Mole fraction of n-Hexane (2) - Liquid Tracer diffusion coefficient, m2/s of Benzene (1) - Liquid
0.0000 1.88
0.2024 2.13
0.2864 2.25
0.3942 2.45
0.4739 2.65
0.6082 3.05
0.7083 3.43
0.7796 3.82
0.8913 4.35
1.0000 4.7

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

Solvent: Mole fraction of n-Hexane (2) - Liquid Binary diffusion coefficient, m2/s - Liquid
0.0000 0.0000
0.2024 0.0000
0.2864 0.0000
0.3942 0.0000
0.4739 0.0000
0.6082 0.0000
0.7083 0.0000
0.7796 0.0000
0.8913 0.0000
1.0000 0.0000

Tracer diffusion coefficient, m2/s of Benzene (1) [ref]

Operational conditions:

Solvent: Mole fraction of n-Hexane (2) - Liquid Tracer diffusion coefficient, m2/s of Benzene (1) - Liquid
0.0000 1.88
0.2024 2.13
0.2864 2.25
0.3942 2.45
0.4739 2.65
0.6082 3.05
0.7083 3.43
0.7796 3.82
0.8913 4.35
1.0000 4.7

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

Solvent: Mole fraction of n-Hexane (2) - Liquid Binary diffusion coefficient, m2/s - Liquid
0.0000 0.0000
0.2024 0.0000
0.2864 0.0000
0.3942 0.0000
0.4739 0.0000
0.6082 0.0000
0.7083 0.0000
0.7796 0.0000
0.8913 0.0000
1.0000 0.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Benzene (1) - Liquid x2[mol/mol] of Ethanol (3) - Liquid y1[mol/mol] of Benzene (1) - Vapour y2[mol/mol] of Ethanol (3) - Vapour
334.05 0.1080 0.0520 0.0770 0.2400
334.95 0.2210 0.0460 0.1590 0.2300
333.05 0.2180 0.1850 0.1540 0.3000
334.85 0.3270 0.0730 0.2240 0.2490
333.85 0.3030 0.3070 0.2290 0.3330
337.85 0.6250 0.0790 0.4210 0.2450
339.35 0.7190 0.1830 0.5200 0.3250

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Benzene (1) - Liquid x2[mol/mol] of Ethanol (3) - Liquid y1[mol/mol] of Benzene (1) - Vapour y2[mol/mol] of Ethanol (3) - Vapour
343.15 0.0380 0.1180 0.0700 0.2960
340.25 0.0320 0.2980 0.0760 0.4140
339.85 0.0220 0.4490 0.0250 0.4560
340.05 0.0200 0.5480 0.0700 0.4670
340.65 0.0190 0.6250 0.0740 0.4980
342.95 0.0310 0.7040 0.0810 0.5680
344.25 0.0220 0.8320 0.0820 0.6660
347.05 0.0180 0.9160 0.0750 0.7750
341.45 0.0820 0.1150 0.1260 0.3280
338.15 0.0520 0.4560 0.1240 0.4310
338.15 0.0530 0.5910 0.1530 0.4690
339.65 0.0610 0.6750 0.2100 0.4810
340.45 0.0460 0.7990 0.2480 0.5210
342.65 0.0320 0.8960 0.2420 0.6310
339.65 0.1610 0.1380 0.2610 0.3110
337.35 0.1260 0.3370 0.2620 0.3700
336.65 0.1360 0.4740 0.2890 0.3900
336.65 0.1490 0.5720 0.3140 0.4200
339.65 0.0750 0.7770 0.2790 0.5360
340.35 0.2900 0.1370 0.3480 0.3100
337.95 0.2930 0.1210 0.3660 0.3030
335.65 0.2230 0.3670 0.3500 0.3550
335.35 0.2150 0.4810 0.3660 0.3510
335.65 0.2090 0.6130 0.4660 0.3640
336.65 0.1550 0.7610 0.4680 0.4390
336.15 0.4000 0.1070 0.4220 0.3000
334.65 0.3120 0.3690 0.4330 0.3490
334.15 0.2620 0.5500 0.4970 0.3480
333.95 0.2910 0.6250 0.5570 0.3630
335.15 0.5380 0.1530 0.4880 0.2750
333.35 0.4560 0.3440 0.5340 0.3250
333.65 0.6470 0.1410 0.5760 0.2810
333.65 0.6330 0.1820 0.5790 0.2860
332.35 0.5990 0.3230 0.6350 0.3080
333.15 0.7620 0.1590 0.6580 0.2750
335.85 0.9320 0.0340 0.7920 0.1760
349.15 0.0130 0.9590 0.0560 0.8650
348.15 0.0160 0.0560 0.0310 0.2090

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 328.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Benzene (1) - Liquid x2[mol/mol] of Ethanol (3) - Liquid y1[mol/mol] of Benzene (1) - Vapour y2[mol/mol] of Ethanol (3) - Vapour
64.461 0.0230 0.5480 0.0610 0.4470
62.728 0.0280 0.7590 0.1240 0.5250
54.182 0.0300 0.9280 0.1980 0.6770
62.795 0.0400 0.1410 0.0680 0.3060
54.902 0.0460 0.0380 0.0810 0.1890
69.034 0.0590 0.5260 0.1450 0.3990
72.114 0.0740 0.6400 0.2010 0.4410
72.181 0.0830 0.7260 0.2700 0.4440
73.114 0.0870 0.7930 0.3380 0.4770
70.661 0.0890 0.3450 0.1580 0.3670
74.674 0.0950 0.8430 0.3710 0.4370
67.514 0.1050 0.1190 0.1700 0.3060
69.928 0.1070 0.2340 0.1640 0.3380
74.461 0.1160 0.4590 0.2380 0.3850
58.515 0.1180 0.0140 0.2050 0.1430
73.127 0.1680 0.2010 0.2370 0.3150
80.127 0.1740 0.6300 0.3720 0.4060
77.994 0.1830 0.4340 0.3100 0.3710
82.487 0.1960 0.6940 0.4350 0.4290
71.754 0.2230 0.1040 0.2700 0.2660
81.593 0.2240 0.5230 0.3780 0.3730
77.314 0.2270 0.2810 0.2300 0.3750
84.753 0.2530 0.6330 0.4650 0.4030
81.06 0.2720 0.3720 0.3690 0.3490
83.98 0.2990 0.4610 0.4370 0.3500
73.874 0.3140 0.0990 0.3230 0.2530
86.18 0.3350 0.4870 0.5000 0.3410
81.287 0.3810 0.2070 0.4160 0.3030
88.179 0.3960 0.5280 0.5530 0.3670
79.9 0.4000 0.1380 0.4180 0.2730
77.42 0.4370 0.0790 0.4160 0.2720
89.313 0.4430 0.5350 0.5940 0.3810
85.006 0.4600 0.2710 0.4760 0.3300
67.088 0.4730 0.0150 0.5230 0.0920
88.473 0.5460 0.3380 0.5580 0.3460
85.326 0.5610 0.2130 0.5140 0.3250
82.913 0.5870 0.1170 0.4800 0.2800
84.38 0.6250 0.1430 0.5320 0.2950
87.526 0.6370 0.2330 0.5940 0.3230
86.393 0.7180 0.1450 0.6090 0.3000
75.02 0.7380 0.0260 0.6570 0.1560
87.659 0.7580 0.1860 0.6310 0.3240
80.14 0.8950 0.0420 0.7370 0.2190

Sources