Mixture of Benzene + 1-Butanol + Cyclohexane

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

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

Cyclohexane

Name
Cyclohexane
InChI
InChI=1S/C6H12/c1-2-4-6-5-3-1/h1-6H2
InChI Key
XDTMQSROBMDMFD-UHFFFAOYSA-N
Formula
C6H12
SMILES
C1CCCCC1
Mol. Weight (g/mol)
84.16
CAS
110-82-7
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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 Benzene (1) - Liquid x2[mol/mol] of Cyclohexane (3) - Liquid y1[mol/mol] of Benzene (1) - Vapour y2[mol/mol] of Cyclohexane (3) - Vapour
351.15 0.4760 0.3400 0.4900 0.4160
351.75 0.4716 0.3140 0.4786 0.4134
352.25 0.6228 0.1550 0.6528 0.2416
352.35 0.6548 0.1280 0.6800 0.2155
352.45 0.5784 0.1640 0.6124 0.2676
352.55 0.4948 0.2160 0.5444 0.2676
352.55 0.5408 0.1800 0.6400 0.2500
352.65 0.4800 0.2180 0.4984 0.3644
352.85 0.3762 0.2734 0.4730 0.4000
353.15 0.0075 0.7340 0.0100 0.8564
353.15 0.6766 0.0380 0.7970 0.0710
353.45 0.7650 0.0010 0.8762 0.0018
353.55 0.7198 0.0120 0.8450 0.0200
353.55 0.7944 0.0010 0.8864 0.0016
353.65 0.0150 0.6780 0.0210 0.8522
353.65 0.6538 0.0432 0.8050 0.0740
353.65 0.7410 0.0020 0.8784 0.0036
353.65 0.8996 0.0040 0.9274 0.0062
353.65 0.9450 0.0110 0.9560 0.0140
353.85 0.9568 0.0012 0.9684 0.0016
353.95 0.5644 0.0836 0.7070 0.1550
354.15 0.3480 0.2336 0.4720 0.3880
354.15 0.4800 0.1312 0.6270 0.2320
354.25 0.0242 0.6160 0.0320 0.8360
354.65 0.0280 0.6024 0.0414 0.8106
354.65 0.3220 0.2308 0.4140 0.4320
354.65 0.3880 0.1882 0.5120 0.3400
354.95 0.3825 0.1950 0.5400 0.3250
355.15 0.2720 0.2510 0.3860 0.4540
355.55 0.0060 0.5280 0.0102 0.8338
355.55 0.2880 0.2228 0.4700 0.3800
355.65 0.4736 0.1080 0.6224 0.2072
355.85 0.3520 0.1692 0.5300 0.3200
356.05 0.3100 0.2120 0.4944 0.3630
356.15 0.3510 0.1942 0.5364 0.3420
356.45 0.0160 0.4952 0.0300 0.8020
356.75 0.1050 0.2992 0.2000 0.6400
357.05 0.0096 0.3810 0.0210 0.8164
357.25 0.0125 0.3760 0.0278 0.7902
357.55 0.3484 0.1444 0.5934 0.2646
357.95 0.0108 0.3220 0.0236 0.7694
357.95 0.2970 0.1480 0.5184 0.2976
358.25 0.2604 0.1570 0.4780 0.3330
358.95 0.2332 0.1630 0.4520 0.3560
358.95 0.2562 0.1416 0.4606 0.3488
359.45 0.1850 0.1720 0.4020 0.3900
359.85 0.1312 0.1920 0.3060 0.4820
360.95 0.1062 0.1802 0.2740 0.4976
362.55 0.1894 0.0908 0.5020 0.3100
363.55 0.0480 0.1400 0.1712 0.5588
365.75 0.0452 0.1320 0.1544 0.5556
367.15 0.1352 0.0878 0.4000 0.3000
369.45 0.0726 0.1018 0.2560 0.4020
371.15 0.0812 0.0244 0.3760 0.1160
372.45 0.1068 0.0132 0.4904 0.0620
372.55 0.0884 0.0040 0.4280 0.0220
378.65 0.0588 0.0068 0.3514 0.0400
383.75 0.0386 0.0126 0.2480 0.0820

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 Cyclohexane (3) - Liquid y1[mol/mol] of Benzene (1) - Vapour y2[mol/mol] of Cyclohexane (3) - Vapour
382.65 0.0320 0.0200 0.0970 0.0650
362.0 0.0420 0.2100 0.1030 0.5500
357.75 0.0350 0.3150 0.0660 0.7030
355.3 0.0440 0.4100 0.0690 0.7470
353.75 0.0660 0.4980 0.0920 0.7670
353.5 0.0630 0.5780 0.0800 0.7830
353.15 0.0480 0.6760 0.0580 0.8190
352.75 0.0340 0.7460 0.0420 0.8520
352.45 0.0540 0.7900 0.0650 0.8450
352.35 0.0350 0.8620 0.0440 0.8670
351.72 0.1290 0.7800 0.1500 0.7730
351.24 0.2210 0.6850 0.2400 0.6870
351.8 0.2020 0.5740 0.2380 0.6590
351.4 0.2710 0.5360 0.3070 0.5990
351.1 0.3240 0.5110 0.3540 0.5590
351.15 0.3240 0.5350 0.3500 0.5680
351.13 0.2810 0.6180 0.3060 0.6240
350.81 0.3850 0.5260 0.3960 0.5360
350.72 0.4670 0.4490 0.4670 0.4650
350.8 0.5600 0.3660 0.5510 0.3890
351.03 0.6510 0.2840 0.6290 0.3180
351.33 0.7320 0.2010 0.7030 0.2430
351.78 0.8060 0.1480 0.7780 0.1780
351.98 0.8420 0.1220 0.8120 0.1560
352.52 0.7610 0.1010 0.7700 0.1410
352.6 0.8370 0.0640 0.8340 0.0930
353.02 0.8370 0.0390 0.8520 0.0650
353.53 0.7300 0.0540 0.8020 0.0870
354.6 0.6260 0.0570 0.7630 0.0920
356.65 0.5190 0.0450 0.7330 0.0830
357.75 0.4080 0.0520 0.6970 0.1130
361.0 0.2980 0.0510 0.6070 0.1320
365.75 0.2070 0.0380 0.5100 0.1320
369.85 0.1440 0.0370 0.4000 0.1530
359.95 0.1350 0.1420 0.3070 0.4080
355.45 0.1300 0.2580 0.2390 0.5720
353.1 0.1290 0.3880 0.1940 0.6490
352.75 0.1310 0.5050 0.1760 0.6960
352.55 0.1340 0.5960 0.1630 0.7230
351.92 0.1430 0.6830 0.1680 0.7420
351.48 0.5710 0.2630 0.5880 0.3210
351.83 0.6360 0.2120 0.6500 0.2630
351.83 0.6920 0.1670 0.6960 0.2180
352.05 0.6950 0.1490 0.7090 0.1970
351.75 0.5880 0.2220 0.6150 0.2880
353.35 0.4850 0.1940 0.5840 0.2820
352.69 0.5960 0.1440 0.6750 0.2130
353.03 0.6930 0.1070 0.7430 0.1450
354.3 0.4500 0.1480 0.6130 0.2540
353.43 0.3590 0.2710 0.4630 0.3970
355.1 0.3290 0.2000 0.4890 0.3470
357.1 0.2460 0.1540 0.4500 0.3390
362.6 0.1640 0.0960 0.3940 0.2930
355.5 0.2460 0.2210 0.3980 0.4270
354.1 0.2440 0.2930 0.3560 0.4900
352.8 0.2500 0.3870 0.3240 0.5460
351.82 0.2510 0.4780 0.2990 0.5900
352.1 0.3480 0.3790 0.4060 0.4890
351.79 0.3540 0.4160 0.3970 0.4950
351.8 0.4420 0.3380 0.4800 0.4060
352.25 0.4390 0.2790 0.5050 0.3690
352.45 0.5180 0.2260 0.5770 0.3060
351.59 0.5230 0.2620 0.5600 0.3370
351.35 0.4160 0.4010 0.4440 0.4650
351.13 0.4750 0.3660 0.4900 0.4190
350.72 0.4910 0.4760 0.4910 0.4770
350.73 0.5320 0.4260 0.5270 0.4370
350.77 0.5450 0.4330 0.5400 0.4390
350.82 0.4660 0.5130 0.4750 0.5060
350.85 0.4620 0.5200 0.4700 0.5130
350.98 0.4180 0.5630 0.4330 0.5530
390.85 0.0000 0.0000 0.0000 0.0000
353.26 1.0000 0.0000 1.0000 0.0000
353.81 0.0000 1.0000 0.0000 1.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 82.66 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Benzene (1) - Liquid x2[mol/mol] of Cyclohexane (3) - Liquid y1[mol/mol] of Benzene (1) - Vapour y2[mol/mol] of Cyclohexane (3) - Vapour
351.55 0.2033 0.1621 0.4469 0.3305
351.95 0.2425 0.1651 0.4578 0.3702
347.8 0.1087 0.2985 0.3354 0.5264
347.25 0.3853 0.2255 0.5320 0.3570
346.35 0.3424 0.2760 0.3980 0.4682
346.3 0.4984 0.2477 0.5274 0.3137
346.05 0.4039 0.3022 0.4851 0.4227
345.8 0.6031 0.1938 0.6973 0.2346
345.55 0.2928 0.4688 0.3758 0.5649
346.0 0.6519 0.1601 0.6956 0.2190
345.15 0.9510 0.0069 0.9620 0.0129
345.75 0.2192 0.5423 0.2937 0.6103
344.75 0.5334 0.3215 0.5480 0.3775
344.15 0.2647 0.6849 0.2647 0.6849
343.95 0.3071 0.6028 0.3320 0.6046
343.85 0.4169 0.5765 0.4211 0.5676
342.8 0.5188 0.3824 0.5192 0.4046
351.85 0.4621 0.0223 0.8035 0.0574
381.45 0.0093 0.0101 0.0201 0.0155

Sources