Mixture of Toluene + 1-Butanol + Water

Excel

Toluene

Name
Toluene
InChI
InChI=1S/C7H8/c1-7-5-3-2-4-6-7/h2-6H,1H3
InChI Key
YXFVVABEGXRONW-UHFFFAOYSA-N
Formula
C7H8
SMILES
Cc1ccccc1
Mol. Weight (g/mol)
92.14
CAS
108-88-3

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 (10)

Mole fraction [ref]

Operational conditions:

Fixed Measured
Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of 1-Butanol (2) - Liquid mixture 2 Mole fraction of 1-Butanol (2) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 1
0.9999 0.0000 0.0000 0.0080
0.9940 0.0060 0.0960 0.0190
0.9910 0.0090 0.3100 0.0870
0.9900 0.0100 0.3800 0.1310
0.9890 0.0110 0.4210 0.1620
0.9890 0.0110 0.4510 0.1870
0.9880 0.0120 0.5010 0.2530
0.9870 0.0130 0.5170 0.2870
0.9870 0.0130 0.5220 0.3300
0.9860 0.0140 0.5300 0.3830
0.9850 0.0150 0.5050 0.4420
0.9840 0.0160 0.4870 0.5000
0.9810 0.0190 0.4840 0.5160

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol (2) - Liquid Mole fraction of Water (3) - Liquid Mole fraction of Water (3) - Gas Mole fraction of 1-Butanol (2) - Gas
376.91 0.6330 0.0220 0.1110 0.4220
377.28 0.6880 0.0270 0.1410 0.4350
384.81 0.9150 0.0290 0.1440 0.6980
379.13 0.8000 0.0300 0.1760 0.5080
377.80 0.7410 0.0300 0.1590 0.4660
381.06 0.8440 0.0330 0.1730 0.5590
378.06 0.7390 0.0350 0.1620 0.4830
378.37 0.8010 0.0500 0.2240 0.4960
379.25 0.8370 0.0500 0.2650 0.5090
368.81 0.3590 0.0570 0.4150 0.1680
370.42 0.6010 0.0600 0.3300 0.2750
381.70 0.9180 0.0630 0.2960 0.6410
379.86 0.8680 0.0640 0.2910 0.5550
380.90 0.8990 0.0640 0.3090 0.5870
368.37 0.4520 0.0640 0.3620 0.2190
379.09 0.8670 0.0650 0.3190 0.5230
369.65 0.5240 0.0700 0.3880 0.2220
366.90 0.4720 0.0710 0.3890 0.2120
372.41 0.7100 0.0760 0.3810 0.2920
375.73 0.8170 0.0910 0.4140 0.3910
372.23 0.7760 0.1030 0.4440 0.3340
368.76 0.6210 0.1150 0.4450 0.2300
376.64 0.8580 0.1270 0.4800 0.4760
369.17 0.7180 0.1300 0.4980 0.2650
374.76 0.8360 0.1390 0.5190 0.4130
369.87 0.7540 0.1630 0.5180 0.3210
372.61 0.7990 0.1700 0.5480 0.3780
367.93 0.7750 0.1770 0.6020 0.2930
370.27 0.7790 0.1840 0.5860 0.3220
364.74 0.6090 0.1950 0.5170 0.2170
366.79 0.6870 0.2030 0.5460 0.2610
360.51 0.5290 0.2120 0.5470 0.1570
362.43 0.5660 0.2120 0.5470 0.1690
364.27 0.6580 0.2130 0.5640 0.2200
363.42 0.6330 0.2260 0.5670 0.2100
361.76 0.5820 0.2590 0.5760 0.1810
365.94 0.6790 0.2660 0.6210 0.2620
360.88 0.5590 0.2680 0.5730 0.1700
359.19 0.5050 0.2780 0.5680 0.1450
364.07 0.6440 0.2900 0.6300 0.2330
363.00 0.5980 0.3330 0.6420 0.2020
361.64 0.5590 0.3630 0.6360 0.1880
360.71 0.5130 0.4000 0.6290 0.1770

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of 1-Butanol (2) - 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) - Gas Mole fraction of 1-Butanol (2) - Gas
357.34 0.0120 0.0000 0.9997 0.0000 0.5610 0.0000
357.15 0.0140 0.0120 0.9997 0.0000 0.5480 0.0150
357.18 0.0140 0.0440 0.9980 0.0010 0.5360 0.0380
356.59 0.0250 0.1020 0.9960 0.0030 0.5270 0.0660
356.54 0.0330 0.1350 0.9950 0.0050 0.5280 0.0730
356.53 0.0340 0.1560 0.9950 0.0050 0.5310 0.0770
356.57 0.0540 0.1960 0.9940 0.0060 0.5310 0.0840
356.59 0.0540 0.2340 0.9940 0.0060 0.5300 0.0890
356.64 0.0770 0.2640 0.9930 0.0070 0.5340 0.0930
356.76 0.0950 0.3130 0.9930 0.0070 0.5360 0.0970
356.89 0.1450 0.3660 0.9920 0.0080 0.5420 0.1040
357.04 0.1560 0.4040 0.9920 0.0080 0.5450 0.1080
357.37 0.2040 0.4610 0.9910 0.0090 0.5480 0.1170
357.85 0.2640 0.4960 0.9900 0.0100 0.5610 0.1300
358.17 0.2990 0.5060 0.9890 0.0110 0.5620 0.1380
358.69 0.3750 0.4970 0.9880 0.0120 0.5860 0.1520
359.20 0.4040 0.4940 0.9870 0.0130 0.6030 0.1590
359.76 0.4360 0.4830 0.9870 0.0130 0.6130 0.1650
360.55 0.4780 0.4680 0.9860 0.0140 0.6330 0.1760
361.53 0.5150 0.4510 0.9860 0.0140 0.6610 0.1940
362.49 0.5370 0.4400 0.9850 0.0150 0.6900 0.2040
362.96 0.5490 0.4320 0.9840 0.0160 0.6970 0.2110

Mass fraction [ref]

Operational conditions:

Fixed Measured
Mass fraction of Water (3) - Liquid mixture 2 Mass fraction of Toluene (1) - Liquid mixture 2 Mass fraction of Water (3) - Liquid mixture 1 Mass fraction of Toluene (1) - Liquid mixture 1
0.9638 0.0010 0.0035 0.9153
0.9644 0.0020 0.0140 0.7409
0.9623 0.0029 0.0306 0.5890
0.9491 0.0054 0.0521 0.4631
0.9515 0.0005 0.0871 0.2944

Mass fraction of Toluene (1) [ref]

Operational conditions:

Mass fraction of Water (3) - Liquid mixture 1 Mass fraction of Toluene (1) - Liquid mixture 1
0.0000 0.9986
0.0035 0.9153
0.0069 0.8261
0.0140 0.7409
0.0219 0.6621
0.0306 0.5890
0.0413 0.5232
0.0521 0.4631
0.0648 0.3981
0.0731 0.3493
0.0872 0.2944
0.1007 0.2569
0.1284 0.1801
0.1544 0.1078
0.1927 0.0000

Mole fraction [ref]

Operational conditions:

Fixed Measured
Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of 1-Butanol (2) - Liquid mixture 2 Mole fraction of 1-Butanol (2) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 1
0.9999 0.0000 0.0000 0.0080
0.9940 0.0060 0.0960 0.0190
0.9910 0.0090 0.3100 0.0870
0.9900 0.0100 0.3800 0.1310
0.9890 0.0110 0.4210 0.1620
0.9890 0.0110 0.4510 0.1870
0.9880 0.0120 0.5010 0.2530
0.9870 0.0130 0.5170 0.2870
0.9870 0.0130 0.5220 0.3300
0.9860 0.0140 0.5300 0.3830
0.9850 0.0150 0.5050 0.4420
0.9840 0.0160 0.4870 0.5000
0.9810 0.0190 0.4840 0.5160

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol (2) - Liquid Mole fraction of Water (3) - Liquid Mole fraction of Water (3) - Gas Mole fraction of 1-Butanol (2) - Gas
376.91 0.6330 0.0220 0.1110 0.4220
377.28 0.6880 0.0270 0.1410 0.4350
384.81 0.9150 0.0290 0.1440 0.6980
379.13 0.8000 0.0300 0.1760 0.5080
377.80 0.7410 0.0300 0.1590 0.4660
381.06 0.8440 0.0330 0.1730 0.5590
378.06 0.7390 0.0350 0.1620 0.4830
378.37 0.8010 0.0500 0.2240 0.4960
379.25 0.8370 0.0500 0.2650 0.5090
368.81 0.3590 0.0570 0.4150 0.1680
370.42 0.6010 0.0600 0.3300 0.2750
381.70 0.9180 0.0630 0.2960 0.6410
379.86 0.8680 0.0640 0.2910 0.5550
380.90 0.8990 0.0640 0.3090 0.5870
368.37 0.4520 0.0640 0.3620 0.2190
379.09 0.8670 0.0650 0.3190 0.5230
369.65 0.5240 0.0700 0.3880 0.2220
366.90 0.4720 0.0710 0.3890 0.2120
372.41 0.7100 0.0760 0.3810 0.2920
375.73 0.8170 0.0910 0.4140 0.3910
372.23 0.7760 0.1030 0.4440 0.3340
368.76 0.6210 0.1150 0.4450 0.2300
376.64 0.8580 0.1270 0.4800 0.4760
369.17 0.7180 0.1300 0.4980 0.2650
374.76 0.8360 0.1390 0.5190 0.4130
369.87 0.7540 0.1630 0.5180 0.3210
372.61 0.7990 0.1700 0.5480 0.3780
367.93 0.7750 0.1770 0.6020 0.2930
370.27 0.7790 0.1840 0.5860 0.3220
364.74 0.6090 0.1950 0.5170 0.2170
366.79 0.6870 0.2030 0.5460 0.2610
360.51 0.5290 0.2120 0.5470 0.1570
362.43 0.5660 0.2120 0.5470 0.1690
364.27 0.6580 0.2130 0.5640 0.2200
363.42 0.6330 0.2260 0.5670 0.2100
361.76 0.5820 0.2590 0.5760 0.1810
365.94 0.6790 0.2660 0.6210 0.2620
360.88 0.5590 0.2680 0.5730 0.1700
359.19 0.5050 0.2780 0.5680 0.1450
364.07 0.6440 0.2900 0.6300 0.2330
363.00 0.5980 0.3330 0.6420 0.2020
361.64 0.5590 0.3630 0.6360 0.1880
360.71 0.5130 0.4000 0.6290 0.1770

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of 1-Butanol (2) - 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) - Gas Mole fraction of 1-Butanol (2) - Gas
357.34 0.0120 0.0000 0.9997 0.0000 0.5610 0.0000
357.15 0.0140 0.0120 0.9997 0.0000 0.5480 0.0150
357.18 0.0140 0.0440 0.9980 0.0010 0.5360 0.0380
356.59 0.0250 0.1020 0.9960 0.0030 0.5270 0.0660
356.54 0.0330 0.1350 0.9950 0.0050 0.5280 0.0730
356.53 0.0340 0.1560 0.9950 0.0050 0.5310 0.0770
356.57 0.0540 0.1960 0.9940 0.0060 0.5310 0.0840
356.59 0.0540 0.2340 0.9940 0.0060 0.5300 0.0890
356.64 0.0770 0.2640 0.9930 0.0070 0.5340 0.0930
356.76 0.0950 0.3130 0.9930 0.0070 0.5360 0.0970
356.89 0.1450 0.3660 0.9920 0.0080 0.5420 0.1040
357.04 0.1560 0.4040 0.9920 0.0080 0.5450 0.1080
357.37 0.2040 0.4610 0.9910 0.0090 0.5480 0.1170
357.85 0.2640 0.4960 0.9900 0.0100 0.5610 0.1300
358.17 0.2990 0.5060 0.9890 0.0110 0.5620 0.1380
358.69 0.3750 0.4970 0.9880 0.0120 0.5860 0.1520
359.20 0.4040 0.4940 0.9870 0.0130 0.6030 0.1590
359.76 0.4360 0.4830 0.9870 0.0130 0.6130 0.1650
360.55 0.4780 0.4680 0.9860 0.0140 0.6330 0.1760
361.53 0.5150 0.4510 0.9860 0.0140 0.6610 0.1940
362.49 0.5370 0.4400 0.9850 0.0150 0.6900 0.2040
362.96 0.5490 0.4320 0.9840 0.0160 0.6970 0.2110

Mass fraction [ref]

Operational conditions:

Fixed Measured
Mass fraction of Water (3) - Liquid mixture 2 Mass fraction of Toluene (1) - Liquid mixture 2 Mass fraction of Water (3) - Liquid mixture 1 Mass fraction of Toluene (1) - Liquid mixture 1
0.9638 0.0010 0.0035 0.9153
0.9644 0.0020 0.0140 0.7409
0.9623 0.0029 0.0306 0.5890
0.9491 0.0054 0.0521 0.4631
0.9515 0.0005 0.0871 0.2944

Mass fraction of Toluene (1) [ref]

Operational conditions:

Mass fraction of Water (3) - Liquid mixture 1 Mass fraction of Toluene (1) - Liquid mixture 1
0.0000 0.9986
0.0035 0.9153
0.0069 0.8261
0.0140 0.7409
0.0219 0.6621
0.0306 0.5890
0.0413 0.5232
0.0521 0.4631
0.0648 0.3981
0.0731 0.3493
0.0872 0.2944
0.1007 0.2569
0.1284 0.1801
0.1544 0.1078
0.1927 0.0000

Sources