Mixture of Benzene + Isopropyl Alcohol + 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

Isopropyl Alcohol

Name
Isopropyl Alcohol
InChI
InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3
InChI Key
KFZMGEQAYNKOFK-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CC(C)O
Mol. Weight (g/mol)
60.09
CAS
67-63-0

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. Temperature, K x Mole fraction (2)
  2. Vapor Liquid Equilibrium at Constant Pressure (3)

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mole fraction of Benzene (1) - Liquid mixture 1 Mole fraction of Isopropyl Alcohol (2) - Liquid mixture 1 Mole fraction of Benzene (1) - Liquid mixture 2 Mole fraction of Isopropyl Alcohol (2) - Liquid mixture 2
303.00 0.9920 0.0050 0.0020 0.0150
313.00 0.9620 0.0220 0.0070 0.0290
313.00 0.9130 0.0670 0.0130 0.0490
313.00 0.8300 0.1280 0.0190 0.0660
313.00 0.6600 0.2280 0.0260 0.0800
313.00 0.5600 0.2900 0.0250 0.1000
313.00 0.3880 0.3480 0.0290 0.1220
313.00 0.3190 0.3700 0.0280 0.1440
323.00 0.9900 0.0050 0.0150 0.0050
323.00 0.9440 0.0340 0.0240 0.0230
323.00 0.8230 0.1130 0.0330 0.0380
303.00 0.9730 0.0220 0.0030 0.0290
323.00 0.6480 0.2370 0.0370 0.0700
323.00 0.5390 0.2880 0.0380 0.0910
323.00 0.4110 0.3420 0.0380 0.1240
323.00 0.2990 0.3820 0.0390 0.1440
303.00 0.9200 0.0660 0.0010 0.0490
303.00 0.8380 0.1300 0.0020 0.0650
303.00 0.7060 0.2190 0.0030 0.0760
303.00 0.5380 0.3080 0.0040 0.0900
303.00 0.3840 0.3580 0.0060 0.1020
303.00 0.3090 0.4050 0.0080 0.1170
313.00 0.9930 0.0050 0.0030 0.0150

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mole fraction of Benzene (1) - Liquid mixture 1 Mole fraction of Isopropyl Alcohol (2) - Liquid mixture 1 Mole fraction of Benzene (1) - Liquid mixture 2 Mole fraction of Isopropyl Alcohol (2) - Liquid mixture 2
303.00 0.9920 0.0050 0.0020 0.0150
313.00 0.9620 0.0220 0.0070 0.0290
313.00 0.9130 0.0670 0.0130 0.0490
313.00 0.8300 0.1280 0.0190 0.0660
313.00 0.6600 0.2280 0.0260 0.0800
313.00 0.5600 0.2900 0.0250 0.1000
313.00 0.3880 0.3480 0.0290 0.1220
313.00 0.3190 0.3700 0.0280 0.1440
323.00 0.9900 0.0050 0.0150 0.0050
323.00 0.9440 0.0340 0.0240 0.0230
323.00 0.8230 0.1130 0.0330 0.0380
303.00 0.9730 0.0220 0.0030 0.0290
323.00 0.6480 0.2370 0.0370 0.0700
323.00 0.5390 0.2880 0.0380 0.0910
323.00 0.4110 0.3420 0.0380 0.1240
323.00 0.2990 0.3820 0.0390 0.1440
303.00 0.9200 0.0660 0.0010 0.0490
303.00 0.8380 0.1300 0.0020 0.0650
303.00 0.7060 0.2190 0.0030 0.0760
303.00 0.5380 0.3080 0.0040 0.0900
303.00 0.3840 0.3580 0.0060 0.1020
303.00 0.3090 0.4050 0.0080 0.1170
313.00 0.9930 0.0050 0.0030 0.0150

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Isopropyl Alcohol (2) - Liquid x2[mol/mol] of Benzene (1) - Liquid y1[mol/mol] of Isopropyl Alcohol (2) - Vapour y2[mol/mol] of Benzene (1) - Vapour
339.66 0.2000 0.6400 0.1650 0.5000
340.81 0.4000 0.4800 0.2700 0.5000
343.6 0.6000 0.3200 0.3850 0.4800
347.92 0.8000 0.1600 0.5950 0.3250
339.55 0.2000 0.4800 0.1830 0.4750
340.46 0.4000 0.3600 0.2450 0.4750
343.58 0.6000 0.2400 0.3450 0.4450
348.21 0.8000 0.1200 0.6050 0.2700
339.6 0.2000 0.3200 0.1920 0.4650
340.65 0.4000 0.2400 0.2400 0.4500
344.3 0.6000 0.1600 0.3500 0.4000
349.33 0.8000 0.0800 0.6400 0.2000
339.91 0.2000 0.1600 0.1950 0.4600
342.15 0.4000 0.1200 0.3200 0.3300
346.65 0.6000 0.0800 0.4350 0.2700
350.89 0.8000 0.0400 0.7000 0.1000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Isopropyl Alcohol (2) - Liquid x2[mol/mol] of Benzene (1) - Liquid y1[mol/mol] of Isopropyl Alcohol (2) - Vapour y2[mol/mol] of Benzene (1) - Vapour
352.15 0.7992 0.1330 0.7820 0.1304
351.35 0.7965 0.1241 0.7771 0.0444
351.65 0.7931 0.1387 0.7870 0.0442
351.95 0.7470 0.2441 0.6360 0.2427
349.05 0.7239 0.2189 0.5146 0.2460
349.65 0.7126 0.2634 0.5604 0.2337
349.45 0.7092 0.1976 0.6436 0.0712
346.95 0.6513 0.1569 0.3629 0.2509
347.15 0.6571 0.1672 0.3580 0.2376
346.15 0.6425 0.2685 0.4043 0.2383
350.35 0.6147 0.3785 0.5667 0.2740
345.35 0.5683 0.1332 0.3451 0.2105
351.65 0.5613 0.4063 0.5123 0.2691
350.15 0.5559 0.3778 0.4252 0.2975
350.65 0.5514 0.4400 0.5545 0.3287
348.35 0.5228 0.4089 0.4653 0.2724
351.15 0.5171 0.4607 0.5451 0.2926
343.05 0.5164 0.0225 0.3388 0.1654
352.15 0.4315 0.5610 0.5688 0.3304
343.55 0.4312 0.0593 0.3184 0.1571
342.85 0.4204 0.4067 0.2776 0.3155
352.95 0.4115 0.5659 0.5495 0.3433
341.05 0.3939 0.2866 0.2551 0.1778
342.65 0.3745 0.4864 0.2765 0.2435
340.85 0.3684 0.2788 0.2421 0.2269
343.95 0.3453 0.0606 0.2010 0.1226
344.15 0.2885 0.6245 0.2599 0.2522
341.25 0.2644 0.6155 0.2227 0.2648
340.05 0.2512 0.4986 0.2402 0.2686
354.55 0.2512 0.7451 0.5664 0.3768
339.85 0.2458 0.2878 0.1913 0.2459
348.45 0.2210 0.7531 0.3797 0.2870
343.45 0.2015 0.7665 0.2896 0.2494
340.85 0.1959 0.6288 0.2182 0.2336
341.05 0.1836 0.7740 0.2443 0.2454
340.25 0.1806 0.5563 0.1508 0.3005
340.15 0.1786 0.6933 0.2147 0.3696
339.85 0.1735 0.5784 0.1979 0.2508
355.45 0.1581 0.8406 0.5848 0.3880
339.85 0.1573 0.2817 0.1792 0.2163
343.85 0.1267 0.6941 0.1761 0.2468
354.15 0.1247 0.8232 0.0770 0.1762
345.15 0.1246 0.8656 0.3511 0.2942
341.15 0.1195 0.8493 0.2132 0.2628
340.15 0.1161 0.7645 0.2065 0.2450
340.15 0.1070 0.7102 0.2099 0.2333
345.15 0.1041 0.8727 0.2799 0.2831
343.65 0.1009 0.8268 0.1269 0.2552
356.45 0.0939 0.9050 0.5677 0.4247
341.15 0.0922 0.8590 0.1895 0.2244
342.15 0.0888 0.8906 0.2372 0.2406
340.35 0.0875 0.8932 0.2020 0.2291
353.45 0.0746 0.9221 0.3728 0.4425
354.15 0.0631 0.9342 0.3401 0.5122
358.35 0.0604 0.9388 0.5522 0.4371
347.85 0.0601 0.8528 0.1803 0.2275
340.15 0.0593 0.8865 0.1754 0.2020
354.45 0.0560 0.9413 0.3577 0.4474
340.75 0.0451 0.7621 0.1504 0.2034
346.65 0.0445 0.2762 0.1510 0.0560
348.75 0.0430 0.8484 0.1599 0.1570
359.15 0.0379 0.9616 0.3026 0.5965
345.05 0.0327 0.4066 0.1089 0.0565
361.65 0.0316 0.9679 0.2460 0.6947
363.55 0.0295 0.9700 0.1842 0.6377
362.75 0.0292 0.9705 0.4544 0.5437
366.65 0.0265 0.9728 0.0669 0.6485
343.45 0.0236 0.5556 0.0798 0.0291
367.95 0.0234 0.9763 0.3915 0.6067
363.25 0.0189 0.9802 0.1641 0.6476
363.35 0.0188 0.9809 0.2549 0.6846
360.45 0.0188 0.9809 0.1297 0.5746
368.15 0.0175 0.9820 0.1190 0.7807
365.05 0.0167 0.9826 0.3117 0.5952
345.55 0.0114 0.6945 0.0334 0.4105
370.15 0.0105 0.9888 0.0668 0.9043

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 26.664 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Isopropyl Alcohol (2) - Liquid x2[mol/mol] of Benzene (1) - Liquid y1[mol/mol] of Isopropyl Alcohol (2) - Vapour y2[mol/mol] of Benzene (1) - Vapour
307.47 0.9127 0.0746 0.6775 0.1269
307.47 0.0010 0.0493 0.6775 0.1269
307.2 0.7722 0.1837 0.6517 0.1571
307.2 0.0013 0.0636 0.6517 0.1571
307.41 0.6100 0.2691 0.6475 0.1647
307.41 0.0019 0.0751 0.6475 0.1647
307.67 0.3053 0.3624 0.6329 0.1800
307.67 0.0046 0.0981 0.6329 0.1800

Sources