Mixture of Ethanol + Cyclohexane + Water

Excel

Ethanol

Name
Ethanol
InChI
InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3
InChI Key
LFQSCWFLJHTTHZ-UHFFFAOYSA-N
Formula
C2H6O
SMILES
CCO
Mol. Weight (g/mol)
46.07
CAS
64-17-5

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. Temperature, K x Mole fraction (10)
  2. Vapor Liquid Equilibrium at Constant Temperature (3)

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 Ethanol (1) - Liquid mixture 1 Mole fraction of Ethanol (1) - Liquid mixture 2 Mole fraction of Ethanol (1) - Gas Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of Water (3) - Gas
338.20 0.0110 0.0680 0.1620 0.0020 0.9310 0.2580
337.46 0.0180 0.0990 0.1930 0.0040 0.9000 0.2430
336.55 0.0310 0.1640 0.2320 0.0040 0.8350 0.2250
336.34 0.0350 0.1930 0.2400 0.0040 0.8060 0.2240
335.97 0.0510 0.2720 0.2560 0.0050 0.7240 0.2080
335.84 0.0760 0.3630 0.2720 0.0110 0.6250 0.2030
335.70 0.0940 0.4250 0.2800 0.0130 0.5570 0.1930
335.63 0.1050 0.4630 0.2860 0.0130 0.5090 0.1900
335.55 0.1270 0.5080 0.2900 0.0170 0.4500 0.1890
335.54 0.1510 0.5550 0.2980 0.0200 0.3860 0.1840
335.54 0.1570 0.5690 0.3010 0.0200 0.3570 0.1810

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol (1) - Liquid Mole fraction of Water (3) - Liquid Mole fraction of Water (3) - Gas Mole fraction of Ethanol (1) - Gas
346.06 0.9150 0.0530 0.0500 0.7520
345.95 0.8510 0.1110 0.1110 0.7760
344.77 0.8130 0.1560 0.1270 0.6500
344.67 0.7700 0.2040 0.1630 0.6490
344.93 0.7240 0.2580 0.1850 0.6310
344.83 0.6830 0.3010 0.2090 0.6090
344.00 0.6230 0.3570 0.1940 0.5250
340.98 0.8190 0.0750 0.0350 0.5560
340.24 0.7850 0.1130 0.0890 0.4980
339.47 0.7380 0.1620 0.1060 0.4460
338.76 0.6720 0.2050 0.1190 0.4320
337.81 0.6620 0.2630 0.1270 0.3550
338.25 0.7410 0.0660 0.0610 0.4560
337.37 0.7000 0.1160 0.0910 0.4120
336.63 0.6550 0.1550 0.1320 0.4800
337.80 0.7150 0.0630 0.0610 0.4480
337.00 0.6470 0.1110 0.0900 0.3830
337.43 0.6730 0.0620 0.0640 0.4290
335.78 0.5900 0.2270 0.1660 0.3200
335.60 0.4890 0.1640 0.1680 0.3170
335.56 0.4700 0.1560 0.1680 0.3180
335.93 0.5670 0.1340 0.1440 0.3480
336.28 0.5930 0.1200 0.1330 0.3620
336.04 0.5890 0.1610 0.1490 0.3470
339.37 0.0100 0.0040 0.2580 0.1290
336.65 0.0310 0.0050 0.2200 0.2350
339.64 0.0040 0.0020 0.3190 0.1300

Temperature, K x Pressure, kPa x Mole fraction [ref]

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mole fraction of Ethanol (1) - Liquid Mole fraction of Cyclohexane (2) - Liquid Mole fraction of Cyclohexane (2) - Gas Mole fraction of Ethanol (1) - Gas
323.15 36.94 0.8734 0.0152 0.2315 0.6787
323.15 41.65 0.8603 0.0355 0.3407 0.5832
323.15 44.70 0.8499 0.0509 0.3517 0.5846
323.15 34.81 0.9788 0.0181 0.1515 0.8462
323.15 34.66 0.9416 0.0146 0.1466 0.8127
323.15 34.97 0.8667 0.0101 0.1483 0.7490
323.15 33.24 0.7714 0.0049 0.1122 0.7215
323.15 30.80 0.6334 0.0015 0.0780 0.6777
323.15 40.89 0.9528 0.0448 0.2686 0.7295
323.15 41.89 0.9076 0.0409 0.2797 0.6775
323.15 41.69 0.8162 0.0267 0.2737 0.6144
323.15 47.24 0.7999 0.0468 0.3484 0.5423
323.15 32.81 0.8664 0.0058 0.0969 0.7949
323.15 38.61 0.8541 0.0212 0.2182 0.6835
323.15 30.60 0.7364 0.0013 0.0462 0.7512
323.15 34.20 0.7339 0.0058 0.1262 0.6876
333.15 53.87 0.6403 0.0050 0.1616 0.6145
333.15 51.72 0.6479 0.0035 0.1243 0.6442
333.15 55.44 0.6879 0.0071 0.1685 0.6196
333.15 49.91 0.7065 0.0022 0.0818 0.6995
333.15 55.27 0.7213 0.0072 0.1608 0.6421
333.15 57.07 0.7157 0.0093 0.2219 0.5975
333.15 70.99 0.8925 0.1006 0.3919 0.6013
333.15 73.19 0.8430 0.0960 0.4159 0.5403
333.15 76.44 0.7654 0.0867 0.3733 0.5102
333.15 76.64 0.7062 0.0639 0.3099 0.5192
333.15 54.29 0.9506 0.0462 0.1489 0.8488
333.15 54.48 0.9396 0.0158 0.1362 0.8216
333.15 54.44 0.8663 0.0105 0.1325 0.7617
333.15 53.34 0.7712 0.0065 0.1186 0.7138
333.15 62.98 0.9508 0.0465 0.2500 0.7478
333.15 64.15 0.9063 0.0421 0.2692 0.6850
333.15 65.06 0.8126 0.0307 0.2737 0.6144
333.15 73.40 0.7940 0.0529 0.3061 0.5730
333.15 32.81 0.8660 0.0068 0.0928 0.7960
333.15 59.89 0.8538 0.0225 0.2129 0.6867
333.15 49.02 0.7329 0.0018 0.0501 0.7492
333.15 54.70 0.7294 0.0078 0.0887 0.7163
343.15 72.64 0.8816 0.0000 0.0000 0.8847
343.15 77.60 0.8828 0.0060 0.0693 0.8239
343.15 82.88 0.8750 0.0140 0.1494 0.7501
343.15 89.93 0.8664 0.0262 0.2715 0.6442
343.15 94.54 0.8508 0.0402 0.2933 0.6174
343.15 102.16 0.8338 0.0582 0.3720 0.5444
343.15 84.32 0.7147 0.0098 0.1801 0.6313
343.15 89.49 0.7147 0.0141 0.2468 0.5829
343.15 82.06 0.9785 0.0176 0.1278 0.8694
343.15 82.78 0.9383 0.0163 0.1289 0.8267
343.15 82.32 0.8663 0.0105 0.1232 0.7702
343.15 81.72 0.7714 0.0073 0.1145 0.7161
343.15 76.86 0.6321 0.0025 0.0761 0.6768
343.15 94.14 0.9493 0.0483 0.1798 0.8186
343.15 95.26 0.9072 0.0422 0.2623 0.6915
343.15 98.87 0.8111 0.0359 0.2768 0.6046
343.15 79.64 0.8670 0.0071 0.0875 0.7991
343.15 88.93 0.8536 0.0216 0.1873 0.7081
343.15 75.64 0.7343 0.0023 0.0493 0.7476
343.15 83.12 0.7263 0.0237 0.1360 0.6819

Mole fraction of Ethanol (1) [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol (1) - Liquid Mole fraction of Cyclohexane (2) - Liquid Mole fraction of Ethanol (1) - Gas
308.15 0.4790 0.0046 0.4651
308.15 0.5096 0.4257 0.2948
308.15 0.5776 0.3814 0.3269
308.15 0.5972 0.3589 0.3201
308.15 0.6675 0.2752 0.3381
308.15 0.7066 0.1073 0.3213
308.15 0.7155 0.2137 0.3369
308.15 0.8100 0.0973 0.4101
308.15 0.8457 0.0678 0.4795
323.15 0.4644 0.0103 0.3796
323.15 0.4902 0.4886 0.3887
323.15 0.5542 0.4095 0.3881
323.15 0.5825 0.3746 0.3861
323.15 0.5982 0.0263 0.4332
323.15 0.6411 0.3065 0.3957
323.15 0.6749 0.1437 0.3603
323.15 0.6753 0.0682 0.4049
323.15 0.6885 0.2439 0.4043
323.15 0.7703 0.1121 0.4274
323.15 0.8324 0.0766 0.5229
338.15 0.5653 0.4041 0.4204
338.15 0.6124 0.3523 0.4271
338.15 0.6822 0.0603 0.4141
338.15 0.7160 0.2370 0.4572
338.15 0.8060 0.1113 0.5175
338.15 0.8098 0.1288 0.5057
338.15 0.8276 0.0786 0.5584
338.15 0.8650 0.0405 0.6221

Mole fraction of Cyclohexane (2) [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol (1) - Liquid Mole fraction of Cyclohexane (2) - Liquid Mole fraction of Cyclohexane (2) - Gas
308.15 0.4790 0.0046 0.2965
308.15 0.5096 0.4257 0.6352
308.15 0.5776 0.3814 0.6251
308.15 0.5972 0.3589 0.6325
308.15 0.6675 0.2752 0.6116
308.15 0.7066 0.1073 0.5809
308.15 0.7155 0.2137 0.6095
308.15 0.8100 0.0973 0.5302
308.15 0.8457 0.0678 0.4640
323.15 0.4644 0.0103 0.4190
323.15 0.4902 0.4886 0.5754
323.15 0.5542 0.4095 0.5668
323.15 0.5825 0.3746 0.5588
323.15 0.5982 0.0263 0.3647
323.15 0.6411 0.3065 0.5503
323.15 0.6749 0.1437 0.5513
323.15 0.6753 0.0682 0.4525
323.15 0.6885 0.2439 0.5344
323.15 0.7703 0.1121 0.4915
323.15 0.8324 0.0766 0.4075
338.15 0.5653 0.4041 0.5327
338.15 0.6124 0.3523 0.5244
338.15 0.6822 0.0603 0.4379
338.15 0.7160 0.2370 0.4957
338.15 0.8060 0.1113 0.4174
338.15 0.8098 0.1288 0.4418
338.15 0.8276 0.0786 0.3672
338.15 0.8650 0.0405 0.3027

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 Ethanol (1) - Liquid mixture 1 Mole fraction of Ethanol (1) - Liquid mixture 2 Mole fraction of Ethanol (1) - Gas Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of Water (3) - Gas
338.20 0.0110 0.0680 0.1620 0.0020 0.9310 0.2580
337.46 0.0180 0.0990 0.1930 0.0040 0.9000 0.2430
336.55 0.0310 0.1640 0.2320 0.0040 0.8350 0.2250
336.34 0.0350 0.1930 0.2400 0.0040 0.8060 0.2240
335.97 0.0510 0.2720 0.2560 0.0050 0.7240 0.2080
335.84 0.0760 0.3630 0.2720 0.0110 0.6250 0.2030
335.70 0.0940 0.4250 0.2800 0.0130 0.5570 0.1930
335.63 0.1050 0.4630 0.2860 0.0130 0.5090 0.1900
335.55 0.1270 0.5080 0.2900 0.0170 0.4500 0.1890
335.54 0.1510 0.5550 0.2980 0.0200 0.3860 0.1840
335.54 0.1570 0.5690 0.3010 0.0200 0.3570 0.1810

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol (1) - Liquid Mole fraction of Water (3) - Liquid Mole fraction of Water (3) - Gas Mole fraction of Ethanol (1) - Gas
346.06 0.9150 0.0530 0.0500 0.7520
345.95 0.8510 0.1110 0.1110 0.7760
344.77 0.8130 0.1560 0.1270 0.6500
344.67 0.7700 0.2040 0.1630 0.6490
344.93 0.7240 0.2580 0.1850 0.6310
344.83 0.6830 0.3010 0.2090 0.6090
344.00 0.6230 0.3570 0.1940 0.5250
340.98 0.8190 0.0750 0.0350 0.5560
340.24 0.7850 0.1130 0.0890 0.4980
339.47 0.7380 0.1620 0.1060 0.4460
338.76 0.6720 0.2050 0.1190 0.4320
337.81 0.6620 0.2630 0.1270 0.3550
338.25 0.7410 0.0660 0.0610 0.4560
337.37 0.7000 0.1160 0.0910 0.4120
336.63 0.6550 0.1550 0.1320 0.4800
337.80 0.7150 0.0630 0.0610 0.4480
337.00 0.6470 0.1110 0.0900 0.3830
337.43 0.6730 0.0620 0.0640 0.4290
335.78 0.5900 0.2270 0.1660 0.3200
335.60 0.4890 0.1640 0.1680 0.3170
335.56 0.4700 0.1560 0.1680 0.3180
335.93 0.5670 0.1340 0.1440 0.3480
336.28 0.5930 0.1200 0.1330 0.3620
336.04 0.5890 0.1610 0.1490 0.3470
339.37 0.0100 0.0040 0.2580 0.1290
336.65 0.0310 0.0050 0.2200 0.2350
339.64 0.0040 0.0020 0.3190 0.1300

Temperature, K x Pressure, kPa x Mole fraction [ref]

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mole fraction of Ethanol (1) - Liquid Mole fraction of Cyclohexane (2) - Liquid Mole fraction of Cyclohexane (2) - Gas Mole fraction of Ethanol (1) - Gas
323.15 36.94 0.8734 0.0152 0.2315 0.6787
323.15 41.65 0.8603 0.0355 0.3407 0.5832
323.15 44.70 0.8499 0.0509 0.3517 0.5846
323.15 34.81 0.9788 0.0181 0.1515 0.8462
323.15 34.66 0.9416 0.0146 0.1466 0.8127
323.15 34.97 0.8667 0.0101 0.1483 0.7490
323.15 33.24 0.7714 0.0049 0.1122 0.7215
323.15 30.80 0.6334 0.0015 0.0780 0.6777
323.15 40.89 0.9528 0.0448 0.2686 0.7295
323.15 41.89 0.9076 0.0409 0.2797 0.6775
323.15 41.69 0.8162 0.0267 0.2737 0.6144
323.15 47.24 0.7999 0.0468 0.3484 0.5423
323.15 32.81 0.8664 0.0058 0.0969 0.7949
323.15 38.61 0.8541 0.0212 0.2182 0.6835
323.15 30.60 0.7364 0.0013 0.0462 0.7512
323.15 34.20 0.7339 0.0058 0.1262 0.6876
333.15 53.87 0.6403 0.0050 0.1616 0.6145
333.15 51.72 0.6479 0.0035 0.1243 0.6442
333.15 55.44 0.6879 0.0071 0.1685 0.6196
333.15 49.91 0.7065 0.0022 0.0818 0.6995
333.15 55.27 0.7213 0.0072 0.1608 0.6421
333.15 57.07 0.7157 0.0093 0.2219 0.5975
333.15 70.99 0.8925 0.1006 0.3919 0.6013
333.15 73.19 0.8430 0.0960 0.4159 0.5403
333.15 76.44 0.7654 0.0867 0.3733 0.5102
333.15 76.64 0.7062 0.0639 0.3099 0.5192
333.15 54.29 0.9506 0.0462 0.1489 0.8488
333.15 54.48 0.9396 0.0158 0.1362 0.8216
333.15 54.44 0.8663 0.0105 0.1325 0.7617
333.15 53.34 0.7712 0.0065 0.1186 0.7138
333.15 62.98 0.9508 0.0465 0.2500 0.7478
333.15 64.15 0.9063 0.0421 0.2692 0.6850
333.15 65.06 0.8126 0.0307 0.2737 0.6144
333.15 73.40 0.7940 0.0529 0.3061 0.5730
333.15 32.81 0.8660 0.0068 0.0928 0.7960
333.15 59.89 0.8538 0.0225 0.2129 0.6867
333.15 49.02 0.7329 0.0018 0.0501 0.7492
333.15 54.70 0.7294 0.0078 0.0887 0.7163
343.15 72.64 0.8816 0.0000 0.0000 0.8847
343.15 77.60 0.8828 0.0060 0.0693 0.8239
343.15 82.88 0.8750 0.0140 0.1494 0.7501
343.15 89.93 0.8664 0.0262 0.2715 0.6442
343.15 94.54 0.8508 0.0402 0.2933 0.6174
343.15 102.16 0.8338 0.0582 0.3720 0.5444
343.15 84.32 0.7147 0.0098 0.1801 0.6313
343.15 89.49 0.7147 0.0141 0.2468 0.5829
343.15 82.06 0.9785 0.0176 0.1278 0.8694
343.15 82.78 0.9383 0.0163 0.1289 0.8267
343.15 82.32 0.8663 0.0105 0.1232 0.7702
343.15 81.72 0.7714 0.0073 0.1145 0.7161
343.15 76.86 0.6321 0.0025 0.0761 0.6768
343.15 94.14 0.9493 0.0483 0.1798 0.8186
343.15 95.26 0.9072 0.0422 0.2623 0.6915
343.15 98.87 0.8111 0.0359 0.2768 0.6046
343.15 79.64 0.8670 0.0071 0.0875 0.7991
343.15 88.93 0.8536 0.0216 0.1873 0.7081
343.15 75.64 0.7343 0.0023 0.0493 0.7476
343.15 83.12 0.7263 0.0237 0.1360 0.6819

Mole fraction of Ethanol (1) [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol (1) - Liquid Mole fraction of Cyclohexane (2) - Liquid Mole fraction of Ethanol (1) - Gas
308.15 0.4790 0.0046 0.4651
308.15 0.5096 0.4257 0.2948
308.15 0.5776 0.3814 0.3269
308.15 0.5972 0.3589 0.3201
308.15 0.6675 0.2752 0.3381
308.15 0.7066 0.1073 0.3213
308.15 0.7155 0.2137 0.3369
308.15 0.8100 0.0973 0.4101
308.15 0.8457 0.0678 0.4795
323.15 0.4644 0.0103 0.3796
323.15 0.4902 0.4886 0.3887
323.15 0.5542 0.4095 0.3881
323.15 0.5825 0.3746 0.3861
323.15 0.5982 0.0263 0.4332
323.15 0.6411 0.3065 0.3957
323.15 0.6749 0.1437 0.3603
323.15 0.6753 0.0682 0.4049
323.15 0.6885 0.2439 0.4043
323.15 0.7703 0.1121 0.4274
323.15 0.8324 0.0766 0.5229
338.15 0.5653 0.4041 0.4204
338.15 0.6124 0.3523 0.4271
338.15 0.6822 0.0603 0.4141
338.15 0.7160 0.2370 0.4572
338.15 0.8060 0.1113 0.5175
338.15 0.8098 0.1288 0.5057
338.15 0.8276 0.0786 0.5584
338.15 0.8650 0.0405 0.6221

Mole fraction of Cyclohexane (2) [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol (1) - Liquid Mole fraction of Cyclohexane (2) - Liquid Mole fraction of Cyclohexane (2) - Gas
308.15 0.4790 0.0046 0.2965
308.15 0.5096 0.4257 0.6352
308.15 0.5776 0.3814 0.6251
308.15 0.5972 0.3589 0.6325
308.15 0.6675 0.2752 0.6116
308.15 0.7066 0.1073 0.5809
308.15 0.7155 0.2137 0.6095
308.15 0.8100 0.0973 0.5302
308.15 0.8457 0.0678 0.4640
323.15 0.4644 0.0103 0.4190
323.15 0.4902 0.4886 0.5754
323.15 0.5542 0.4095 0.5668
323.15 0.5825 0.3746 0.5588
323.15 0.5982 0.0263 0.3647
323.15 0.6411 0.3065 0.5503
323.15 0.6749 0.1437 0.5513
323.15 0.6753 0.0682 0.4525
323.15 0.6885 0.2439 0.5344
323.15 0.7703 0.1121 0.4915
323.15 0.8324 0.0766 0.4075
338.15 0.5653 0.4041 0.5327
338.15 0.6124 0.3523 0.5244
338.15 0.6822 0.0603 0.4379
338.15 0.7160 0.2370 0.4957
338.15 0.8060 0.1113 0.4174
338.15 0.8098 0.1288 0.4418
338.15 0.8276 0.0786 0.3672
338.15 0.8650 0.0405 0.3027

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 413.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Ethanol (1) - Liquid x2[mol/mol] of Water (3) - Liquid
755.932 1.0000 0.0000
361.352 0.0000 1.0000
452.271 0.0000 0.0000
593.854 0.0476 0.0001
670.42 0.0909 0.0002
778.861 0.1839 0.0004
827.103 0.2463 0.0005
855.347 0.2971 0.0006
876.289 0.3451 0.0007
894.162 0.4028 0.0009
905.757 0.4506 0.0010
914.171 0.4948 0.0012
919.764 0.5495 0.0013
924.256 0.6019 0.0015
926.13 0.6523 0.0016
927.365 0.7014 0.0018
924.02 0.7512 0.0019
913.562 0.8000 0.0020
901.321 0.8401 0.0021
923.873 0.7968 0.0536
941.373 0.7569 0.1009
957.716 0.7124 0.1537
970.067 0.6758 0.1972
982.554 0.6330 0.2480
960.46 0.6704 0.0498
991.154 0.6301 0.1085
1008.717 0.5971 0.1562
1023.08 0.5663 0.2007
996.954 0.6329 0.1701
1010.558 0.5973 0.2173
1020.884 0.5628 0.2631
1033.759 0.5269 0.3106
851.431 0.8100 0.1480
915.543 0.7691 0.1400
951.831 0.7273 0.1319
974.256 0.6852 0.1239
987.403 0.6489 0.1171
1001.715 0.5540 0.0995
1004.875 0.5092 0.0914
1006.044 0.4669 0.0839
1005.932 0.4248 0.0765
1004.368 0.3825 0.0692
1001.975 0.3418 0.0622
963.375 0.6325 0.2734
1003.58 0.5988 0.2580
1036.859 0.5574 0.2394
1043.479 0.5173 0.2217
1049.927 0.4781 0.2047
1053.779 0.4394 0.1880
1057.098 0.4011 0.1717
1058.973 0.3621 0.1553
1061.362 0.3258 0.1402
1061.434 0.3104 0.1338
868.97 0.9033 0.0023
886.551 0.8490 0.0630
898.706 0.8054 0.1116
908.927 0.7626 0.1594
916.538 0.7248 0.2015
924.728 0.6815 0.2499
933.13 0.6414 0.2945
940.211 0.5920 0.3496
949.065 0.5472 0.3995
959.313 0.5040 0.4475
973.692 0.4536 0.5034
990.938 0.4074 0.5547
1012.37 0.3630 0.6038
1043.149 0.3163 0.6554
1066.642 0.2710 0.7050

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 358.05 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Ethanol (1) - Liquid x2[mol/mol] of Water (3) - Liquid
114.86 0.0000 0.0000
130.74 1.0000 0.0000
57.51 0.0000 1.0000
174.428 0.9027 0.0007
192.016 0.8047 0.0006
199.514 0.7003 0.0005
202.074 0.6011 0.0005
202.87 0.4971 0.0004
146.089 0.0467 0.0000
182.548 0.0908 0.0001
192.143 0.1517 0.0001
195.755 0.1968 0.0001
198.246 0.2455 0.0002
199.966 0.2984 0.0002
201.099 0.3480 0.0003
201.881 0.4016 0.0003
202.502 0.5007 0.0004
177.116 0.7671 0.1812
195.871 0.7319 0.1728
206.919 0.6926 0.1634
213.172 0.6514 0.1536
216.544 0.6116 0.1442
218.517 0.5710 0.1346
219.978 0.5300 0.1249
220.974 0.4903 0.1156
221.788 0.4498 0.1061
222.642 0.4096 0.0966
223.282 0.3742 0.0883
199.001 0.5761 0.3758
219.494 0.5458 0.3558
224.987 0.5157 0.3361
226.151 0.4933 0.3214
225.943 0.4953 0.3120
225.973 0.4805 0.2791
192.048 0.8024 0.0006
198.02 0.7637 0.0491
203.561 0.7268 0.0952
212.762 0.6446 0.1979
216.572 0.6060 0.2461
220.341 0.5669 0.2949
225.149 0.5084 0.3748
212.007 0.1992 0.7986
190.236 0.2995 0.6950
171.718 0.3991 0.5927
206.684 0.4548 0.5172
185.501 0.6708 0.2780
206.786 0.6310 0.2613
220.245 0.5653 0.2339
222.596 0.5301 0.2193
223.852 0.4946 0.2046
224.599 0.4581 0.1895
225.229 0.4226 0.1748
225.761 0.3877 0.1604
226.229 0.3519 0.1457
165.512 0.8541 0.0965
185.177 0.8099 0.0915
196.918 0.7641 0.0862
207.17 0.6752 0.0761
209.911 0.6303 0.0710
211.78 0.5854 0.0660
213.1 0.5407 0.0609
213.822 0.4953 0.0558
214.808 0.4321 0.0488
215.373 0.3804 0.0430
157.946 0.9487 0.0007
185.409 0.8511 0.0006
196.704 0.7487 0.0006
200.833 0.6502 0.0005
202.317 0.5538 0.0004
202.57 0.4984 0.0004

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 393.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Ethanol (1) - Liquid x2[mol/mol] of Water (3) - Liquid
428.39 1.0000 0.0000
198.53 0.0000 1.0000
288.24 0.0000 0.0000
533.296 0.6608 0.2920
586.564 0.6253 0.2755
610.307 0.5912 0.2600
621.389 0.5604 0.2462
630.052 0.5182 0.2273
635.841 0.4829 0.2117
638.117 0.4476 0.1962
640.297 0.4148 0.1818
642.276 0.3762 0.1649
643.799 0.3414 0.1498
645.291 0.3046 0.1339
576.067 0.5211 0.4310
624.986 0.4954 0.4089
638.002 0.4683 0.3861
643.066 0.4410 0.3633
647.716 0.4145 0.3412
577.328 0.5394 0.0466
603.876 0.5075 0.1038
621.044 0.4799 0.1531
632.692 0.4525 0.2019
640.813 0.4237 0.2531
645.392 0.3921 0.3091
391.546 0.0449 0.0001
465.18 0.1015 0.0003
501.559 0.1623 0.0004
520.28 0.2171 0.0005
534.991 0.2756 0.0006
543.257 0.3210 0.0007
549.429 0.3395 0.0008
555.632 0.4412 0.0011
558.261 0.4957 0.0012
560.793 0.5472 0.0014
561.095 0.5959 0.0015
562.07 0.6453 0.0016
560.065 0.6928 0.0018
556.788 0.7387 0.0019
550.425 0.7852 0.0020
541.398 0.8264 0.0021
534.681 0.8488 0.0022
582.672 0.6705 0.0578
598.263 0.6355 0.1074
616.852 0.5772 0.1896
619.673 0.5497 0.2284
628.851 0.5258 0.2621
634.972 0.4930 0.3083
640.927 0.4518 0.3662
598.345 0.4233 0.0502
620.662 0.4039 0.0943
634.024 0.3856 0.1355
640.722 0.3686 0.1739
611.295 0.3283 0.0647
633.931 0.3141 0.1060
634.012 0.3019 0.1413
561.534 0.4384 0.5363
620.688 0.4263 0.5213
640.991 0.4146 0.5067
506.164 0.8282 0.1176
542.939 0.7884 0.1117
568.54 0.7364 0.1040
582.092 0.7067 0.0997
593.089 0.6576 0.0926
597.464 0.6157 0.0866
598.611 0.5744 0.0808
601.24 0.5276 0.0742
603.852 0.4843 0.0681
604.641 0.4393 0.0619
604.754 0.3975 0.0561
604.217 0.3491 0.0495

Sources