Mixture of p-Xylene + Ethanol + Water

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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

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

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 (4)
  2. Vapor Liquid Equilibrium at Constant Pressure (3)

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 Ethanol (2) - Liquid mixture 1 Mole fraction of Ethanol (2) - Liquid mixture 2 Mole fraction of Ethanol (2) - Gas Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of Water (3) - Gas
365.40 0.0000 0.0000 0.0000 0.0070 1.0000 0.7590
358.14 0.0300 0.0410 0.2780 0.0090 0.9590 0.5410
355.33 0.0620 0.0790 0.3690 0.0200 0.9210 0.4800
353.89 0.1040 0.1430 0.4430 0.0400 0.8560 0.4190
352.70 0.1550 0.2100 0.4720 0.0550 0.7860 0.3920
352.26 0.2080 0.2680 0.4860 0.0710 0.7220 0.3790
351.98 0.2480 0.3290 0.5000 0.0950 0.6590 0.3680
351.88 0.3000 0.3700 0.5090 0.1460 0.6050 0.3610
351.83 0.3390 0.3980 0.5090 0.1760 0.5570 0.3620
351.75 0.3690 0.4250 0.5110 0.2080 0.5150 0.3600
351.72 0.3950 0.4420 0.5130 0.2630 0.4600 0.3580

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 Ethanol (2) - Liquid Mole fraction of Ethanol (2) - Gas Mole fraction of Water (3) - Gas
351.51 0.3460 0.5030 0.5480 0.3320
351.56 0.2290 0.4990 0.5700 0.3120
351.53 0.1570 0.6550 0.6960 0.2080
351.27 0.2430 0.6260 0.6420 0.2580
351.59 0.4670 0.4720 0.5470 0.3390
351.83 0.4590 0.5140 0.6090 0.3180
351.23 0.2870 0.6340 0.6520 0.2640
351.19 0.2240 0.7340 0.7470 0.2040
351.16 0.1960 0.7350 0.7390 0.1940
351.27 0.1770 0.7040 0.7160 0.1980
351.26 0.1020 0.8300 0.8310 0.1150
351.65 0.1190 0.7010 0.7410 0.1630
352.19 0.0970 0.5810 0.7070 0.1850
352.59 0.0820 0.4950 0.6880 0.1990
351.41 0.3140 0.6600 0.6980 0.2580

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 Ethanol (2) - Liquid mixture 1 Mole fraction of Ethanol (2) - Liquid mixture 2 Mole fraction of Ethanol (2) - Gas Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of Water (3) - Gas
365.40 0.0000 0.0000 0.0000 0.0070 1.0000 0.7590
358.14 0.0300 0.0410 0.2780 0.0090 0.9590 0.5410
355.33 0.0620 0.0790 0.3690 0.0200 0.9210 0.4800
353.89 0.1040 0.1430 0.4430 0.0400 0.8560 0.4190
352.70 0.1550 0.2100 0.4720 0.0550 0.7860 0.3920
352.26 0.2080 0.2680 0.4860 0.0710 0.7220 0.3790
351.98 0.2480 0.3290 0.5000 0.0950 0.6590 0.3680
351.88 0.3000 0.3700 0.5090 0.1460 0.6050 0.3610
351.83 0.3390 0.3980 0.5090 0.1760 0.5570 0.3620
351.75 0.3690 0.4250 0.5110 0.2080 0.5150 0.3600
351.72 0.3950 0.4420 0.5130 0.2630 0.4600 0.3580

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 Ethanol (2) - Liquid Mole fraction of Ethanol (2) - Gas Mole fraction of Water (3) - Gas
351.51 0.3460 0.5030 0.5480 0.3320
351.56 0.2290 0.4990 0.5700 0.3120
351.53 0.1570 0.6550 0.6960 0.2080
351.27 0.2430 0.6260 0.6420 0.2580
351.59 0.4670 0.4720 0.5470 0.3390
351.83 0.4590 0.5140 0.6090 0.3180
351.23 0.2870 0.6340 0.6520 0.2640
351.19 0.2240 0.7340 0.7470 0.2040
351.16 0.1960 0.7350 0.7390 0.1940
351.27 0.1770 0.7040 0.7160 0.1980
351.26 0.1020 0.8300 0.8310 0.1150
351.65 0.1190 0.7010 0.7410 0.1630
352.19 0.0970 0.5810 0.7070 0.1850
352.59 0.0820 0.4950 0.6880 0.1990
351.41 0.3140 0.6600 0.6980 0.2580

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 49.4 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Water (3) - Liquid x2[mol/mol] of Ethanol (2) - Liquid y1[mol/mol] of Water (3) - Vapour y2[mol/mol] of Ethanol (2) - Vapour
334.07 0.1267 0.8532 0.1266 0.8495
333.97 0.1280 0.8292 0.1361 0.8199
334.02 0.1315 0.8025 0.1446 0.7941
334.04 0.1340 0.7744 0.1532 0.7729
334.04 0.1380 0.7432 0.1659 0.7489
334.02 0.1403 0.7147 0.1793 0.7260
334.16 0.1430 0.6804 0.1935 0.7042
334.29 0.1805 0.8102 0.1792 0.8069
334.15 0.1847 0.7860 0.1767 0.7875
334.13 0.1862 0.7623 0.1863 0.7570
334.08 0.1903 0.7341 0.1983 0.7265
334.08 0.1943 0.7069 0.2103 0.7051
334.07 0.2007 0.6771 0.2274 0.6765
334.1 0.2057 0.6433 0.2428 0.6504
334.03 0.2242 0.6995 0.2229 0.6979
334.19 0.2326 0.7489 0.2059 0.7656
333.97 0.2353 0.7259 0.2140 0.7334
334.06 0.2424 0.6969 0.2308 0.6975
334.02 0.2449 0.6846 0.2366 0.6846
333.91 0.2475 0.6698 0.2438 0.6694
333.86 0.2531 0.6406 0.2565 0.6452
334.39 0.3229 0.6604 0.2656 0.6993
334.14 0.3306 0.6347 0.2718 0.6672
333.93 0.3373 0.6074 0.2774 0.6345
334.61 0.4078 0.5786 0.3069 0.6592
334.32 0.4137 0.5543 0.3156 0.6123
334.78 0.4786 0.5102 0.3275 0.6207

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 90.4 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Water (3) - Liquid x2[mol/mol] of Ethanol (2) - Liquid y1[mol/mol] of Water (3) - Vapour y2[mol/mol] of Ethanol (2) - Vapour
348.38 0.1236 0.8557 0.1259 0.8521
348.36 0.1293 0.8283 0.1378 0.8214
348.4 0.1266 0.8067 0.1442 0.7992
348.44 0.1344 0.7734 0.1551 0.7759
348.51 0.1381 0.7429 0.1674 0.7527
348.59 0.1399 0.7122 0.1807 0.7288
348.64 0.1427 0.6771 0.1944 0.7065
348.53 0.1778 0.8118 0.1698 0.8165
348.44 0.1836 0.7852 0.1784 0.7868
348.4 0.1870 0.7618 0.1885 0.7592
348.38 0.1909 0.7329 0.2001 0.7310
348.44 0.1981 0.7003 0.2174 0.7020
348.47 0.2018 0.6728 0.2305 0.6807
348.5 0.2080 0.6385 0.2490 0.6530
348.48 0.2265 0.7553 0.2112 0.7632
348.38 0.2353 0.7264 0.2205 0.7331
348.36 0.2435 0.6957 0.2348 0.6995
348.34 0.2466 0.6687 0.2477 0.6708
348.37 0.2541 0.6389 0.2618 0.6456
348.71 0.3236 0.6601 0.2629 0.7034
348.55 0.3308 0.6338 0.2746 0.6691
348.47 0.3379 0.6069 0.2890 0.6332
348.99 0.4025 0.5815 0.3057 0.6540
348.79 0.4163 0.5540 0.3054 0.6258
349.27 0.4775 0.5091 0.3370 0.6174

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 Ethanol (2) - Liquid y1[mol/mol] of Water (3) - Vapour y2[mol/mol] of Ethanol (2) - Vapour
351.51 0.3460 0.5030 0.3320 0.5480
351.56 0.2290 0.4990 0.3120 0.5700
351.53 0.1570 0.6550 0.2080 0.6960
351.27 0.2430 0.6260 0.2580 0.6420
351.59 0.4670 0.4720 0.3390 0.5470
351.83 0.4590 0.5140 0.3180 0.6090
351.23 0.2870 0.6340 0.2640 0.6520
351.19 0.2240 0.7340 0.2040 0.7470
351.16 0.1960 0.7350 0.1940 0.7390
351.27 0.1770 0.7040 0.1980 0.7160
351.26 0.1020 0.8300 0.1150 0.8310
351.65 0.1190 0.7010 0.1630 0.7410
352.19 0.0970 0.5810 0.1850 0.7070
352.59 0.0820 0.4950 0.1990 0.6880
351.41 0.3140 0.6600 0.2580 0.6980

Sources