Mixture of p-Xylene + 1-Butanol + Water

Excel

p-Xylene

Name
p-Xylene
InChI
InChI=1S/C8H10/c1-7-3-5-8(2)6-4-7/h3-6H,1-2H3
InChI Key
URLKBWYHVLBVBO-UHFFFAOYSA-N
Formula
C8H10
SMILES
Cc1ccc(C)cc1
Mol. Weight (g/mol)
106.17
CAS
106-42-3

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

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. Mole fraction (6)
  2. Vapor Liquid Equilibrium at Constant Pressure

Mole fraction [ref]

Operational conditions:

Fixed Measured
Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of 1-Butanol (2) - Liquid mixture 1 Mole fraction of 1-Butanol (2) - Liquid mixture 2 Mole fraction of Water (3) - Liquid mixture 2
0.0030 0.0000 0.0000 1.0000
0.0210 0.0970 0.0080 0.9920
0.0990 0.3270 0.0100 0.9900
0.1440 0.4020 0.0110 0.9880
0.1900 0.4590 0.0120 0.9880
0.2260 0.4910 0.0140 0.9850
0.3040 0.5340 0.0130 0.9870
0.3480 0.5430 0.0150 0.9850
0.4270 0.5290 0.0160 0.9840
0.4720 0.5080 0.0180 0.9820
0.5160 0.4840 0.0190 0.9810

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Water (3) - Liquid Mole fraction of 1-Butanol (2) - Liquid Mole fraction of 1-Butanol (2) - Gas Mole fraction of Water (3) - Gas
368.02 0.3120 0.6760 0.2450 0.7370
369.39 0.2640 0.7240 0.2790 0.7040
369.92 0.2530 0.7350 0.2760 0.7080
371.26 0.2310 0.7610 0.3030 0.6840
373.42 0.1840 0.8090 0.3220 0.6670
375.18 0.1520 0.8430 0.3790 0.6120
377.07 0.1260 0.8690 0.4330 0.5600
379.28 0.1000 0.8950 0.4500 0.5440
379.73 0.1090 0.8870 0.5180 0.4760
378.00 0.1090 0.8740 0.4530 0.5240
375.83 0.1340 0.8340 0.3660 0.5970
372.21 0.1780 0.7770 0.3010 0.6520
370.44 0.2040 0.7380 0.2850 0.6590
368.14 0.2530 0.6750 0.2370 0.6930
366.56 0.2860 0.6290 0.2130 0.7070
365.23 0.3160 0.5870 0.2040 0.7030
365.05 0.4180 0.5410 0.2170 0.7260
365.13 0.4430 0.5270 0.2200 0.7330
365.46 0.4200 0.5520 0.2230 0.7340
365.86 0.3960 0.5780 0.2290 0.7350
366.09 0.3810 0.5930 0.2270 0.7360
366.40 0.3570 0.6200 0.2290 0.7370
365.75 0.2420 0.6040 0.1920 0.6950
364.71 0.2740 0.5570 0.1880 0.6870
367.16 0.2300 0.6270 0.2140 0.6850
369.18 0.1950 0.6810 0.2560 0.6490
371.49 0.1720 0.7240 0.2870 0.6270
373.95 0.1380 0.7770 0.3210 0.6040
376.87 0.1060 0.8260 0.4130 0.5200
378.99 0.0920 0.8570 0.5110 0.4350
380.55 0.0830 0.8930 0.5700 0.3990
384.65 0.0480 0.9440 0.7200 0.2670
384.04 0.0480 0.9210 0.6770 0.2830
383.20 0.0470 0.8910 0.6360 0.2950
382.13 0.0570 0.8480 0.6050 0.2990
381.41 0.0530 0.8060 0.5550 0.3180
381.95 0.0430 0.7830 0.5530 0.3010
382.20 0.0390 0.7520 0.5570 0.2760
382.91 0.0370 0.7150 0.5550 0.2610
382.49 0.0330 0.6740 0.5440 0.2550
379.96 0.0430 0.6230 0.4450 0.3590
378.12 0.0540 0.5730 0.3730 0.4360
376.45 0.0560 0.5260 0.3390 0.4680
375.26 0.0590 0.4870 0.3120 0.4960
374.66 0.0550 0.4460 0.2720 0.5480
373.80 0.0600 0.4060 0.2480 0.5740
372.87 0.0630 0.3620 0.2350 0.5850
371.08 0.0580 0.3310 0.2050 0.6180
368.21 0.1400 0.5200 0.2020 0.6550
369.19 0.1330 0.5490 0.2170 0.6410
371.55 0.1070 0.6010 0.2600 0.5970
373.58 0.0970 0.6660 0.3140 0.5450
376.41 0.0820 0.7160 0.3950 0.4650
377.94 0.0810 0.7500 0.4230 0.4480

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)

Fixed Measured
Temperature, K - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of 1-Butanol (2) - Liquid mixture 2 Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of 1-Butanol (2) - Liquid mixture 1 Mole fraction of 1-Butanol (2) - Gas Mole fraction of Water (3) - Gas
365.40 1.0000 0.0000 0.0100 0.0000 0.0000 0.7590
364.82 0.9990 0.0010 0.0120 0.0160 0.0280 0.7210
364.46 0.9980 0.0020 0.0170 0.0330 0.0490 0.7210
364.21 0.9970 0.0030 0.0170 0.0440 0.0620 0.7120
363.83 0.9960 0.0040 0.0190 0.0660 0.0780 0.7070
363.17 0.9940 0.0060 0.0270 0.1210 0.1130 0.6860
362.93 0.9930 0.0070 0.0460 0.1600 0.1170 0.6870
362.75 0.9920 0.0080 0.0500 0.1940 0.1230 0.6890
362.56 0.9910 0.0090 0.0880 0.2800 0.1370 0.6870
362.42 0.9890 0.0110 0.1270 0.3410 0.1430 0.6880
362.27 0.9880 0.0110 0.1770 0.4260 0.1530 0.6850
362.33 0.9880 0.0120 0.2080 0.4440 0.1570 0.6810
362.36 0.9880 0.0120 0.2110 0.4680 0.1590 0.6830
362.52 0.9880 0.0120 0.2390 0.4850 0.1640 0.6830
362.79 0.9860 0.0140 0.3190 0.5020 0.1720 0.6920
362.86 0.9860 0.0140 0.3420 0.5030 0.1780 0.6880
363.11 0.9850 0.0150 0.3920 0.4990 0.1790 0.6970
363.32 0.9850 0.0150 0.4180 0.4970 0.1870 0.6990
363.93 0.9840 0.0160 0.4760 0.4790 0.2030 0.7140
364.14 0.9830 0.0170 0.5010 0.4640 0.2040 0.7250
365.85 0.9790 0.0210 0.6380 0.3620 0.2460 0.7540

Mole fraction [ref]

Operational conditions:

Fixed Measured
Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of 1-Butanol (2) - Liquid mixture 1 Mole fraction of 1-Butanol (2) - Liquid mixture 2 Mole fraction of Water (3) - Liquid mixture 2
0.0030 0.0000 0.0000 1.0000
0.0210 0.0970 0.0080 0.9920
0.0990 0.3270 0.0100 0.9900
0.1440 0.4020 0.0110 0.9880
0.1900 0.4590 0.0120 0.9880
0.2260 0.4910 0.0140 0.9850
0.3040 0.5340 0.0130 0.9870
0.3480 0.5430 0.0150 0.9850
0.4270 0.5290 0.0160 0.9840
0.4720 0.5080 0.0180 0.9820
0.5160 0.4840 0.0190 0.9810

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Water (3) - Liquid Mole fraction of 1-Butanol (2) - Liquid Mole fraction of 1-Butanol (2) - Gas Mole fraction of Water (3) - Gas
368.02 0.3120 0.6760 0.2450 0.7370
369.39 0.2640 0.7240 0.2790 0.7040
369.92 0.2530 0.7350 0.2760 0.7080
371.26 0.2310 0.7610 0.3030 0.6840
373.42 0.1840 0.8090 0.3220 0.6670
375.18 0.1520 0.8430 0.3790 0.6120
377.07 0.1260 0.8690 0.4330 0.5600
379.28 0.1000 0.8950 0.4500 0.5440
379.73 0.1090 0.8870 0.5180 0.4760
378.00 0.1090 0.8740 0.4530 0.5240
375.83 0.1340 0.8340 0.3660 0.5970
372.21 0.1780 0.7770 0.3010 0.6520
370.44 0.2040 0.7380 0.2850 0.6590
368.14 0.2530 0.6750 0.2370 0.6930
366.56 0.2860 0.6290 0.2130 0.7070
365.23 0.3160 0.5870 0.2040 0.7030
365.05 0.4180 0.5410 0.2170 0.7260
365.13 0.4430 0.5270 0.2200 0.7330
365.46 0.4200 0.5520 0.2230 0.7340
365.86 0.3960 0.5780 0.2290 0.7350
366.09 0.3810 0.5930 0.2270 0.7360
366.40 0.3570 0.6200 0.2290 0.7370
365.75 0.2420 0.6040 0.1920 0.6950
364.71 0.2740 0.5570 0.1880 0.6870
367.16 0.2300 0.6270 0.2140 0.6850
369.18 0.1950 0.6810 0.2560 0.6490
371.49 0.1720 0.7240 0.2870 0.6270
373.95 0.1380 0.7770 0.3210 0.6040
376.87 0.1060 0.8260 0.4130 0.5200
378.99 0.0920 0.8570 0.5110 0.4350
380.55 0.0830 0.8930 0.5700 0.3990
384.65 0.0480 0.9440 0.7200 0.2670
384.04 0.0480 0.9210 0.6770 0.2830
383.20 0.0470 0.8910 0.6360 0.2950
382.13 0.0570 0.8480 0.6050 0.2990
381.41 0.0530 0.8060 0.5550 0.3180
381.95 0.0430 0.7830 0.5530 0.3010
382.20 0.0390 0.7520 0.5570 0.2760
382.91 0.0370 0.7150 0.5550 0.2610
382.49 0.0330 0.6740 0.5440 0.2550
379.96 0.0430 0.6230 0.4450 0.3590
378.12 0.0540 0.5730 0.3730 0.4360
376.45 0.0560 0.5260 0.3390 0.4680
375.26 0.0590 0.4870 0.3120 0.4960
374.66 0.0550 0.4460 0.2720 0.5480
373.80 0.0600 0.4060 0.2480 0.5740
372.87 0.0630 0.3620 0.2350 0.5850
371.08 0.0580 0.3310 0.2050 0.6180
368.21 0.1400 0.5200 0.2020 0.6550
369.19 0.1330 0.5490 0.2170 0.6410
371.55 0.1070 0.6010 0.2600 0.5970
373.58 0.0970 0.6660 0.3140 0.5450
376.41 0.0820 0.7160 0.3950 0.4650
377.94 0.0810 0.7500 0.4230 0.4480

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)

Fixed Measured
Temperature, K - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of 1-Butanol (2) - Liquid mixture 2 Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of 1-Butanol (2) - Liquid mixture 1 Mole fraction of 1-Butanol (2) - Gas Mole fraction of Water (3) - Gas
365.40 1.0000 0.0000 0.0100 0.0000 0.0000 0.7590
364.82 0.9990 0.0010 0.0120 0.0160 0.0280 0.7210
364.46 0.9980 0.0020 0.0170 0.0330 0.0490 0.7210
364.21 0.9970 0.0030 0.0170 0.0440 0.0620 0.7120
363.83 0.9960 0.0040 0.0190 0.0660 0.0780 0.7070
363.17 0.9940 0.0060 0.0270 0.1210 0.1130 0.6860
362.93 0.9930 0.0070 0.0460 0.1600 0.1170 0.6870
362.75 0.9920 0.0080 0.0500 0.1940 0.1230 0.6890
362.56 0.9910 0.0090 0.0880 0.2800 0.1370 0.6870
362.42 0.9890 0.0110 0.1270 0.3410 0.1430 0.6880
362.27 0.9880 0.0110 0.1770 0.4260 0.1530 0.6850
362.33 0.9880 0.0120 0.2080 0.4440 0.1570 0.6810
362.36 0.9880 0.0120 0.2110 0.4680 0.1590 0.6830
362.52 0.9880 0.0120 0.2390 0.4850 0.1640 0.6830
362.79 0.9860 0.0140 0.3190 0.5020 0.1720 0.6920
362.86 0.9860 0.0140 0.3420 0.5030 0.1780 0.6880
363.11 0.9850 0.0150 0.3920 0.4990 0.1790 0.6970
363.32 0.9850 0.0150 0.4180 0.4970 0.1870 0.6990
363.93 0.9840 0.0160 0.4760 0.4790 0.2030 0.7140
364.14 0.9830 0.0170 0.5010 0.4640 0.2040 0.7250
365.85 0.9790 0.0210 0.6380 0.3620 0.2460 0.7540

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.3 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Water (3) - Liquid x2[mol/mol] of 1-Butanol (2) - Liquid y1[mol/mol] of Water (3) - Vapour y2[mol/mol] of 1-Butanol (2) - Vapour
368.02 0.3120 0.6760 0.7370 0.2450
369.39 0.2640 0.7240 0.7040 0.2790
369.92 0.2530 0.7350 0.7080 0.2760
371.26 0.2310 0.7610 0.6840 0.3030
373.42 0.1840 0.8090 0.6670 0.3220
375.18 0.1520 0.8430 0.6120 0.3790
377.07 0.1260 0.8690 0.5600 0.4330
379.28 0.1000 0.8950 0.5440 0.4500
379.73 0.1090 0.8870 0.4760 0.5180
378.0 0.1090 0.8740 0.5240 0.4530
375.83 0.1340 0.8340 0.5970 0.3660
372.21 0.1780 0.7770 0.6520 0.3010
370.44 0.2040 0.7380 0.6590 0.2850
368.14 0.2530 0.6750 0.6930 0.2370
366.56 0.2860 0.6290 0.7070 0.2130
365.23 0.3160 0.5870 0.7030 0.2040
365.05 0.4180 0.5410 0.7260 0.2170
365.13 0.4430 0.5270 0.7330 0.2200
365.43 0.4200 0.5520 0.7340 0.2230
365.86 0.3960 0.5780 0.7350 0.2290
366.09 0.3810 0.5930 0.7360 0.2270
366.4 0.3570 0.6200 0.7370 0.2290
365.75 0.2420 0.6040 0.6950 0.1920
364.71 0.2740 0.5570 0.6870 0.1880
367.16 0.2300 0.6270 0.6850 0.2140
369.18 0.1950 0.6810 0.6490 0.2560
371.49 0.1720 0.7240 0.6270 0.2870
373.95 0.1380 0.7770 0.6040 0.3210
376.87 0.1060 0.8260 0.5200 0.4130
378.99 0.0920 0.8570 0.4350 0.5110
380.55 0.0830 0.8930 0.3990 0.5700
384.65 0.0480 0.9440 0.2670 0.7200
384.04 0.0480 0.9210 0.2830 0.6770
383.2 0.0470 0.8910 0.2950 0.6360
382.13 0.0570 0.8480 0.2990 0.6050
381.41 0.0530 0.8060 0.3180 0.5550
381.95 0.0430 0.7830 0.3010 0.5530
382.2 0.0390 0.7520 0.2760 0.5570
382.91 0.0370 0.7150 0.2610 0.5550
382.49 0.0330 0.6740 0.2550 0.5440
379.96 0.0430 0.6230 0.3590 0.4450
378.12 0.0540 0.5730 0.4360 0.3730
376.45 0.0560 0.5260 0.4680 0.3390
375.26 0.0590 0.4870 0.4960 0.3120
374.66 0.0550 0.4460 0.5480 0.2720
373.8 0.0600 0.4060 0.5740 0.2480
372.87 0.0630 0.3620 0.5850 0.2350
371.08 0.0580 0.3310 0.6180 0.2050
368.21 0.1400 0.5200 0.6550 0.2020
369.19 0.1330 0.5490 0.6410 0.2170
371.55 0.1070 0.6010 0.5970 0.2600
373.58 0.0970 0.6660 0.5450 0.3140
376.41 0.0820 0.7160 0.4650 0.3950
377.94 0.0810 0.7500 0.4480 0.4230

Sources