Mixture of 1-Butanol + Cyclohexane + Water

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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

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 2 Mole fraction of 1-Butanol (1) - Liquid mixture 2 Mole fraction of 1-Butanol (1) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 1
0.9810 0.0190 0.4840 0.5160
0.9820 0.0180 0.5240 0.4210
0.9840 0.0160 0.5250 0.2570
0.9850 0.0150 0.4950 0.2180
0.9860 0.0140 0.4330 0.1550
0.9890 0.0110 0.3990 0.1360
0.9890 0.0110 0.3570 0.1080
0.9890 0.0110 0.2770 0.0630
0.9900 0.0100 0.1540 0.0480
0.9900 0.0100 0.0750 0.0140
1.0000 0.0000 0.0000 0.0100

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 (1) - Liquid mixture 2 Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of 1-Butanol (1) - Liquid mixture 1 Mole fraction of Water (3) - Gas Mole fraction of 1-Butanol (1) - Gas
365.73 0.9790 0.0210 0.6380 0.3620 0.7540 0.2460
358.74 0.9790 0.0210 0.5580 0.4280 0.5890 0.1800
357.51 0.9820 0.0180 0.4790 0.4920 0.5360 0.1530
351.69 0.9840 0.0160 0.4150 0.5200 0.3950 0.1150
346.17 0.9850 0.0150 0.3590 0.5340 0.3350 0.0930
346.11 0.9870 0.0130 0.3060 0.5420 0.3250 0.0810
343.07 0.9870 0.0130 0.1930 0.5310 0.2860 0.0650
343.01 0.9890 0.0110 0.1360 0.4590 0.2840 0.0630
342.51 0.9890 0.0110 0.0810 0.3820 0.2770 0.0590
342.34 0.9900 0.0100 0.0610 0.3230 0.2790 0.0570
342.22 0.9900 0.0100 0.0360 0.2540 0.2750 0.0540
342.16 0.9900 0.0100 0.0360 0.2340 0.2770 0.0530
342.06 0.9910 0.0090 0.0320 0.1780 0.2760 0.0500
341.98 0.9910 0.0090 0.0210 0.1470 0.2730 0.0490
341.97 0.9910 0.0090 0.0120 0.1240 0.2770 0.0460
341.90 0.9920 0.0080 0.0100 0.0960 0.2800 0.0430
341.86 0.9930 0.0070 0.0090 0.0680 0.2810 0.0410
341.96 0.9950 0.0050 0.0080 0.0220 0.2830 0.0310
341.97 0.9960 0.0040 0.0060 0.0160 0.2810 0.0280
342.60 1.0000 0.0000 0.0030 0.0000 0.2990 0.0000

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 (1) - Liquid Mole fraction of 1-Butanol (1) - Gas Mole fraction of Water (3) - Gas
348.67 0.3160 0.5700 0.0940 0.2920
350.09 0.3010 0.5780 0.1190 0.2940
353.41 0.2520 0.6580 0.1250 0.4140
358.41 0.2090 0.7160 0.1640 0.4330
361.49 0.1770 0.7550 0.1940 0.4400
365.54 0.1420 0.8100 0.2380 0.4300
373.12 0.1100 0.8460 0.3640 0.3870
379.92 0.0590 0.9230 0.5630 0.2830
364.57 0.3190 0.6680 0.2370 0.6410
365.33 0.3080 0.6790 0.2470 0.6450
366.85 0.2960 0.6920 0.2680 0.6360
368.77 0.2360 0.7550 0.3010 0.6260
372.04 0.1840 0.8110 0.3610 0.5880
374.71 0.1500 0.8470 0.4160 0.5470
377.93 0.1140 0.8840 0.4980 0.4800
377.82 0.0790 0.9020 0.5310 0.3280
377.96 0.0560 0.9120 0.5430 0.2320
376.19 0.0570 0.8950 0.4860 0.2040
373.92 0.0350 0.8910 0.4340 0.1340
368.69 0.0460 0.8500 0.3390 0.1700
363.77 0.0670 0.7950 0.2600 0.1960
358.64 0.0960 0.7300 0.1920 0.2440
352.99 0.1390 0.6440 0.1280 0.2750
351.06 0.1440 0.6310 0.1060 0.2850
348.12 0.1610 0.5410 0.0870 0.2800
347.19 0.1290 0.5110 0.0850 0.2560
348.06 0.0860 0.5080 0.0910 0.2260
351.66 0.0630 0.5960 0.1180 0.1810
353.66 0.0450 0.6220 0.1380 0.1380
356.26 0.0510 0.6720 0.1630 0.1380
360.17 0.0350 0.7360 0.1970 0.1150
358.61 0.3840 0.5780 0.1770 0.5370

Mole fraction [ref]

Operational conditions:

Fixed Measured
Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of 1-Butanol (1) - Liquid mixture 2 Mole fraction of 1-Butanol (1) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 1
0.9810 0.0190 0.4840 0.5160
0.9820 0.0180 0.5240 0.4210
0.9840 0.0160 0.5250 0.2570
0.9850 0.0150 0.4950 0.2180
0.9860 0.0140 0.4330 0.1550
0.9890 0.0110 0.3990 0.1360
0.9890 0.0110 0.3570 0.1080
0.9890 0.0110 0.2770 0.0630
0.9900 0.0100 0.1540 0.0480
0.9900 0.0100 0.0750 0.0140
1.0000 0.0000 0.0000 0.0100

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 (1) - Liquid mixture 2 Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of 1-Butanol (1) - Liquid mixture 1 Mole fraction of Water (3) - Gas Mole fraction of 1-Butanol (1) - Gas
365.73 0.9790 0.0210 0.6380 0.3620 0.7540 0.2460
358.74 0.9790 0.0210 0.5580 0.4280 0.5890 0.1800
357.51 0.9820 0.0180 0.4790 0.4920 0.5360 0.1530
351.69 0.9840 0.0160 0.4150 0.5200 0.3950 0.1150
346.17 0.9850 0.0150 0.3590 0.5340 0.3350 0.0930
346.11 0.9870 0.0130 0.3060 0.5420 0.3250 0.0810
343.07 0.9870 0.0130 0.1930 0.5310 0.2860 0.0650
343.01 0.9890 0.0110 0.1360 0.4590 0.2840 0.0630
342.51 0.9890 0.0110 0.0810 0.3820 0.2770 0.0590
342.34 0.9900 0.0100 0.0610 0.3230 0.2790 0.0570
342.22 0.9900 0.0100 0.0360 0.2540 0.2750 0.0540
342.16 0.9900 0.0100 0.0360 0.2340 0.2770 0.0530
342.06 0.9910 0.0090 0.0320 0.1780 0.2760 0.0500
341.98 0.9910 0.0090 0.0210 0.1470 0.2730 0.0490
341.97 0.9910 0.0090 0.0120 0.1240 0.2770 0.0460
341.90 0.9920 0.0080 0.0100 0.0960 0.2800 0.0430
341.86 0.9930 0.0070 0.0090 0.0680 0.2810 0.0410
341.96 0.9950 0.0050 0.0080 0.0220 0.2830 0.0310
341.97 0.9960 0.0040 0.0060 0.0160 0.2810 0.0280
342.60 1.0000 0.0000 0.0030 0.0000 0.2990 0.0000

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 (1) - Liquid Mole fraction of 1-Butanol (1) - Gas Mole fraction of Water (3) - Gas
348.67 0.3160 0.5700 0.0940 0.2920
350.09 0.3010 0.5780 0.1190 0.2940
353.41 0.2520 0.6580 0.1250 0.4140
358.41 0.2090 0.7160 0.1640 0.4330
361.49 0.1770 0.7550 0.1940 0.4400
365.54 0.1420 0.8100 0.2380 0.4300
373.12 0.1100 0.8460 0.3640 0.3870
379.92 0.0590 0.9230 0.5630 0.2830
364.57 0.3190 0.6680 0.2370 0.6410
365.33 0.3080 0.6790 0.2470 0.6450
366.85 0.2960 0.6920 0.2680 0.6360
368.77 0.2360 0.7550 0.3010 0.6260
372.04 0.1840 0.8110 0.3610 0.5880
374.71 0.1500 0.8470 0.4160 0.5470
377.93 0.1140 0.8840 0.4980 0.4800
377.82 0.0790 0.9020 0.5310 0.3280
377.96 0.0560 0.9120 0.5430 0.2320
376.19 0.0570 0.8950 0.4860 0.2040
373.92 0.0350 0.8910 0.4340 0.1340
368.69 0.0460 0.8500 0.3390 0.1700
363.77 0.0670 0.7950 0.2600 0.1960
358.64 0.0960 0.7300 0.1920 0.2440
352.99 0.1390 0.6440 0.1280 0.2750
351.06 0.1440 0.6310 0.1060 0.2850
348.12 0.1610 0.5410 0.0870 0.2800
347.19 0.1290 0.5110 0.0850 0.2560
348.06 0.0860 0.5080 0.0910 0.2260
351.66 0.0630 0.5960 0.1180 0.1810
353.66 0.0450 0.6220 0.1380 0.1380
356.26 0.0510 0.6720 0.1630 0.1380
360.17 0.0350 0.7360 0.1970 0.1150
358.61 0.3840 0.5780 0.1770 0.5370

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 (1) - Liquid y1[mol/mol] of Water (3) - Vapour y2[mol/mol] of 1-Butanol (1) - Vapour
348.67 0.3160 0.5700 0.2920 0.0940
350.09 0.3010 0.5780 0.2940 0.1190
353.41 0.2520 0.6580 0.4140 0.1250
358.41 0.2090 0.7160 0.4330 0.1640
361.49 0.1770 0.7550 0.4400 0.1940
365.54 0.1420 0.8100 0.4300 0.2380
373.12 0.1100 0.8460 0.3870 0.3640
379.92 0.0590 0.9230 0.2830 0.5630
364.57 0.3190 0.6680 0.6410 0.2370
365.33 0.3080 0.6790 0.6450 0.2470
366.85 0.2960 0.6920 0.6360 0.2680
368.77 0.2360 0.7550 0.6260 0.3010
372.04 0.1840 0.8110 0.5880 0.3610
374.71 0.1500 0.8470 0.5470 0.4160
377.93 0.1140 0.8840 0.4800 0.4980
377.82 0.0790 0.9020 0.3280 0.5310
377.96 0.0560 0.9120 0.2320 0.5430
376.19 0.0570 0.8950 0.2040 0.4860
373.92 0.0350 0.8910 0.1340 0.4340
368.69 0.0460 0.8500 0.1700 0.3390
363.77 0.0670 0.7950 0.1960 0.2600
358.64 0.0960 0.7300 0.2440 0.1920
352.99 0.1390 0.6440 0.2750 0.1280
351.06 0.1440 0.6310 0.2850 0.1060
348.12 0.1610 0.5410 0.2800 0.0870
347.19 0.1290 0.5110 0.2560 0.0850
348.06 0.0860 0.5080 0.2260 0.0910
351.66 0.0630 0.5960 0.1810 0.1180
353.66 0.0450 0.6220 0.1380 0.1380
356.26 0.0510 0.6720 0.1380 0.1630
360.17 0.0350 0.7360 0.1150 0.1970
358.61 0.3840 0.5780 0.5370 0.1770

Sources