Mixture of 2-Pentanol + 1-Butanol + Water

Excel

2-Pentanol

Name
2-Pentanol
InChI
InChI=1S/C5H12O/c1-3-4-5(2)6/h5-6H,3-4H2,1-2H3
InChI Key
JYVLIDXNZAXMDK-UHFFFAOYSA-N
Formula
C5H12O
SMILES
CCCC(C)O
Mol. Weight (g/mol)
88.15
CAS
6032-29-7

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. Temperature, K x Mole fraction (6)

Temperature, K x Mole fraction [ref]

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

Fixed Measured
Temperature, K - Liquid mixture 1 Mole fraction of 1-Butanol (2) - Liquid mixture 2 Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of 1-Butanol (2) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of 1-Butanol (2) - Gas Mole fraction of Water (3) - Gas
365.85 0.0210 0.9790 0.3620 0.6380 0.2460 0.7540
365.68 0.0200 0.9790 0.3720 0.5500 0.1960 0.7570
365.61 0.0100 0.9870 0.3460 0.4960 0.1650 0.7540
365.59 0.0090 0.9870 0.3030 0.4680 0.1310 0.7550
365.53 0.0070 0.9890 0.2610 0.4630 0.1160 0.7530
365.52 0.0060 0.9900 0.2340 0.4520 0.1000 0.7510
365.49 0.0050 0.9910 0.1960 0.4520 0.0840 0.7520
365.48 0.0040 0.9910 0.1590 0.4500 0.0690 0.7530
365.48 0.0030 0.9920 0.1270 0.4490 0.0540 0.7540
365.47 0.0020 0.9920 0.1060 0.4460 0.0450 0.7510
365.41 0.0020 0.9920 0.0850 0.4340 0.0350 0.7510
365.39 0.0020 0.9920 0.0550 0.4440 0.0220 0.7540
365.37 0.0000 0.9930 0.0000 0.4290 0.0000 0.7500

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 1-Butanol (2) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of 1-Butanol (2) - Liquid mixture 2
303.15 0.4960 0.5040 0.9830 0.0170
303.15 0.0780 0.3400 0.9910 0.0020
303.15 0.0000 0.3640 0.9920 0.0000
313.15 0.4840 0.5160 0.9810 0.0190
313.15 0.4760 0.4750 0.9840 0.0150
313.15 0.4520 0.4480 0.9850 0.0130
313.15 0.4150 0.4300 0.9860 0.0110
313.15 0.3730 0.4090 0.9870 0.0100
313.15 0.3190 0.4050 0.9880 0.0080
313.15 0.2580 0.4060 0.9880 0.0070
313.15 0.2050 0.3860 0.9890 0.0050
303.15 0.4900 0.4620 0.9840 0.0150
313.15 0.1400 0.3840 0.9890 0.0040
313.15 0.0710 0.3720 0.9910 0.0020
313.15 0.0000 0.3800 0.9930 0.0000
303.15 0.4730 0.4250 0.9850 0.0130
303.15 0.4230 0.4190 0.9860 0.0120
303.15 0.3760 0.4070 0.9870 0.0100
303.15 0.3250 0.3950 0.9880 0.0080
365.85 0.3620 0.6380 0.9790 0.0210
365.68 0.3720 0.5500 0.9790 0.0200
365.61 0.3460 0.4960 0.9870 0.0100
365.59 0.3030 0.4680 0.9870 0.0090
365.53 0.2610 0.4630 0.9890 0.0070
303.15 0.2720 0.3770 0.9890 0.0070
365.52 0.2340 0.4520 0.9900 0.0060
365.49 0.1960 0.4520 0.9910 0.0050
365.48 0.1590 0.4500 0.9910 0.0040
365.48 0.1270 0.4490 0.9920 0.0030
365.47 0.1060 0.4460 0.9920 0.0020
365.41 0.0850 0.4340 0.9920 0.0020
365.39 0.0550 0.4440 0.9920 0.0020
365.37 0.0000 0.4290 0.9930 0.0000
303.15 0.2110 0.3620 0.9900 0.0050
303.15 0.1480 0.3500 0.9910 0.0030

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
372.89 0.7480 0.1940 0.6510 0.3240
375.13 0.8000 0.1550 0.5980 0.3800
378.91 0.8580 0.1120 0.5120 0.4710
381.90 0.9110 0.0690 0.3960 0.5890
365.85 0.3620 0.6380 0.7540 0.2460
365.68 0.3720 0.5500 0.7570 0.1960
365.61 0.3460 0.4960 0.7540 0.1650
365.59 0.3030 0.4680 0.7550 0.1310
365.53 0.2610 0.4630 0.7530 0.1160
365.52 0.2340 0.4520 0.7510 0.1000
365.49 0.1960 0.4520 0.7520 0.0840
365.48 0.1590 0.4500 0.7530 0.0690
365.48 0.1270 0.4490 0.7540 0.0540
365.47 0.1060 0.4460 0.7510 0.0450
365.41 0.0850 0.4340 0.7510 0.0350
365.39 0.0550 0.4440 0.7540 0.0220
365.37 0.0000 0.4290 0.7500 0.0000
365.85 0.0210 0.9790 0.7540 0.2460
365.68 0.0200 0.9790 0.7570 0.1960
365.61 0.0100 0.9870 0.7540 0.1650
365.59 0.0090 0.9870 0.7550 0.1310
365.53 0.0070 0.9890 0.7530 0.1160
365.52 0.0060 0.9900 0.7510 0.1000
365.49 0.0050 0.9910 0.7520 0.0840
365.48 0.0040 0.9910 0.7530 0.0690
365.48 0.0030 0.9920 0.7540 0.0540
365.47 0.0020 0.9920 0.7510 0.0450
365.41 0.0020 0.9920 0.7510 0.0350
365.39 0.0020 0.9920 0.7540 0.0220
365.37 0.0000 0.9930 0.7500 0.0000
365.61 0.4250 0.4780 0.7560 0.1970
372.71 0.7000 0.1780 0.6740 0.2790
380.39 0.8140 0.0730 0.6520 0.3060
373.33 0.7380 0.1570 0.7120 0.2540
377.99 0.7210 0.1000 0.7130 0.2330
381.88 0.6590 0.0590 0.6190 0.2740
384.59 0.5950 0.0470 0.3410 0.4220
386.15 0.5260 0.0340 0.3140 0.3860
388.41 0.4770 0.0230 0.3190 0.3470
377.05 0.3960 0.1200 0.5550 0.2040
371.61 0.3270 0.2090 0.6780 0.1340
375.42 0.2480 0.1400 0.6020 0.1150
377.61 0.2110 0.1140 0.5370 0.1120
369.02 0.1440 0.2600 0.7190 0.0540
376.98 0.0990 0.1130 0.5470 0.0510
366.13 0.3850 0.3470 0.7510 0.1460
368.87 0.5040 0.2710 0.7400 0.1800
370.23 0.4880 0.2350 0.7150 0.1830
371.23 0.5270 0.2140 0.7040 0.2010
374.91 0.6340 0.1460 0.6530 0.2610
383.65 0.8000 0.0330 0.3140 0.5690
367.78 0.5580 0.3220 0.7520 0.2170
366.58 0.5120 0.4170 0.7520 0.2170
367.21 0.5600 0.3680 0.7490 0.2220
368.58 0.6340 0.2980 0.7240 0.2490

Temperature, K x Mole fraction [ref]

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

Fixed Measured
Temperature, K - Liquid mixture 1 Mole fraction of 1-Butanol (2) - Liquid mixture 2 Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of 1-Butanol (2) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of 1-Butanol (2) - Gas Mole fraction of Water (3) - Gas
365.85 0.0210 0.9790 0.3620 0.6380 0.2460 0.7540
365.68 0.0200 0.9790 0.3720 0.5500 0.1960 0.7570
365.61 0.0100 0.9870 0.3460 0.4960 0.1650 0.7540
365.59 0.0090 0.9870 0.3030 0.4680 0.1310 0.7550
365.53 0.0070 0.9890 0.2610 0.4630 0.1160 0.7530
365.52 0.0060 0.9900 0.2340 0.4520 0.1000 0.7510
365.49 0.0050 0.9910 0.1960 0.4520 0.0840 0.7520
365.48 0.0040 0.9910 0.1590 0.4500 0.0690 0.7530
365.48 0.0030 0.9920 0.1270 0.4490 0.0540 0.7540
365.47 0.0020 0.9920 0.1060 0.4460 0.0450 0.7510
365.41 0.0020 0.9920 0.0850 0.4340 0.0350 0.7510
365.39 0.0020 0.9920 0.0550 0.4440 0.0220 0.7540
365.37 0.0000 0.9930 0.0000 0.4290 0.0000 0.7500

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 1-Butanol (2) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of 1-Butanol (2) - Liquid mixture 2
303.15 0.4960 0.5040 0.9830 0.0170
303.15 0.0780 0.3400 0.9910 0.0020
303.15 0.0000 0.3640 0.9920 0.0000
313.15 0.4840 0.5160 0.9810 0.0190
313.15 0.4760 0.4750 0.9840 0.0150
313.15 0.4520 0.4480 0.9850 0.0130
313.15 0.4150 0.4300 0.9860 0.0110
313.15 0.3730 0.4090 0.9870 0.0100
313.15 0.3190 0.4050 0.9880 0.0080
313.15 0.2580 0.4060 0.9880 0.0070
313.15 0.2050 0.3860 0.9890 0.0050
303.15 0.4900 0.4620 0.9840 0.0150
313.15 0.1400 0.3840 0.9890 0.0040
313.15 0.0710 0.3720 0.9910 0.0020
313.15 0.0000 0.3800 0.9930 0.0000
303.15 0.4730 0.4250 0.9850 0.0130
303.15 0.4230 0.4190 0.9860 0.0120
303.15 0.3760 0.4070 0.9870 0.0100
303.15 0.3250 0.3950 0.9880 0.0080
365.85 0.3620 0.6380 0.9790 0.0210
365.68 0.3720 0.5500 0.9790 0.0200
365.61 0.3460 0.4960 0.9870 0.0100
365.59 0.3030 0.4680 0.9870 0.0090
365.53 0.2610 0.4630 0.9890 0.0070
303.15 0.2720 0.3770 0.9890 0.0070
365.52 0.2340 0.4520 0.9900 0.0060
365.49 0.1960 0.4520 0.9910 0.0050
365.48 0.1590 0.4500 0.9910 0.0040
365.48 0.1270 0.4490 0.9920 0.0030
365.47 0.1060 0.4460 0.9920 0.0020
365.41 0.0850 0.4340 0.9920 0.0020
365.39 0.0550 0.4440 0.9920 0.0020
365.37 0.0000 0.4290 0.9930 0.0000
303.15 0.2110 0.3620 0.9900 0.0050
303.15 0.1480 0.3500 0.9910 0.0030

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
372.89 0.7480 0.1940 0.6510 0.3240
375.13 0.8000 0.1550 0.5980 0.3800
378.91 0.8580 0.1120 0.5120 0.4710
381.90 0.9110 0.0690 0.3960 0.5890
365.85 0.3620 0.6380 0.7540 0.2460
365.68 0.3720 0.5500 0.7570 0.1960
365.61 0.3460 0.4960 0.7540 0.1650
365.59 0.3030 0.4680 0.7550 0.1310
365.53 0.2610 0.4630 0.7530 0.1160
365.52 0.2340 0.4520 0.7510 0.1000
365.49 0.1960 0.4520 0.7520 0.0840
365.48 0.1590 0.4500 0.7530 0.0690
365.48 0.1270 0.4490 0.7540 0.0540
365.47 0.1060 0.4460 0.7510 0.0450
365.41 0.0850 0.4340 0.7510 0.0350
365.39 0.0550 0.4440 0.7540 0.0220
365.37 0.0000 0.4290 0.7500 0.0000
365.85 0.0210 0.9790 0.7540 0.2460
365.68 0.0200 0.9790 0.7570 0.1960
365.61 0.0100 0.9870 0.7540 0.1650
365.59 0.0090 0.9870 0.7550 0.1310
365.53 0.0070 0.9890 0.7530 0.1160
365.52 0.0060 0.9900 0.7510 0.1000
365.49 0.0050 0.9910 0.7520 0.0840
365.48 0.0040 0.9910 0.7530 0.0690
365.48 0.0030 0.9920 0.7540 0.0540
365.47 0.0020 0.9920 0.7510 0.0450
365.41 0.0020 0.9920 0.7510 0.0350
365.39 0.0020 0.9920 0.7540 0.0220
365.37 0.0000 0.9930 0.7500 0.0000
365.61 0.4250 0.4780 0.7560 0.1970
372.71 0.7000 0.1780 0.6740 0.2790
380.39 0.8140 0.0730 0.6520 0.3060
373.33 0.7380 0.1570 0.7120 0.2540
377.99 0.7210 0.1000 0.7130 0.2330
381.88 0.6590 0.0590 0.6190 0.2740
384.59 0.5950 0.0470 0.3410 0.4220
386.15 0.5260 0.0340 0.3140 0.3860
388.41 0.4770 0.0230 0.3190 0.3470
377.05 0.3960 0.1200 0.5550 0.2040
371.61 0.3270 0.2090 0.6780 0.1340
375.42 0.2480 0.1400 0.6020 0.1150
377.61 0.2110 0.1140 0.5370 0.1120
369.02 0.1440 0.2600 0.7190 0.0540
376.98 0.0990 0.1130 0.5470 0.0510
366.13 0.3850 0.3470 0.7510 0.1460
368.87 0.5040 0.2710 0.7400 0.1800
370.23 0.4880 0.2350 0.7150 0.1830
371.23 0.5270 0.2140 0.7040 0.2010
374.91 0.6340 0.1460 0.6530 0.2610
383.65 0.8000 0.0330 0.3140 0.5690
367.78 0.5580 0.3220 0.7520 0.2170
366.58 0.5120 0.4170 0.7520 0.2170
367.21 0.5600 0.3680 0.7490 0.2220
368.58 0.6340 0.2980 0.7240 0.2490

Sources