Mixture of p-Xylene + Ethanol

Excel

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
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Datasets

  1. Mole fraction (2)
  2. Tboil - Boiling temperature at pressure P, K (4)
  3. Vapor Liquid Equilibrium at Constant Pressure (2)
  4. Vapor Liquid Equilibrium at Constant Temperature

Mole fraction of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (2) - Liquid Mole fraction of Ethanol (2) - Gas
0.0080 0.1890
0.0310 0.4790
0.0820 0.7340
0.1230 0.7950
0.1960 0.8350
0.2550 0.8470
0.3130 0.8570
0.3490 0.8630
0.3970 0.8750
0.4640 0.8810
0.4880 0.8830
0.5530 0.8870
0.6000 0.8930
0.6500 0.8980
0.7060 0.9020
0.7500 0.9060
0.8020 0.9150
0.8500 0.9270
0.8960 0.9400
0.9490 0.9620
0.9790 0.9820

Mole fraction of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (2) - Liquid Mole fraction of Ethanol (2) - Gas
0.0080 0.1890
0.0310 0.4790
0.0820 0.7340
0.1230 0.7950
0.1960 0.8350
0.2550 0.8470
0.3130 0.8570
0.3490 0.8630
0.3970 0.8750
0.4640 0.8810
0.4880 0.8830
0.5530 0.8870
0.6000 0.8930
0.6500 0.8980
0.7060 0.9020
0.7500 0.9060
0.8020 0.9150
0.8500 0.9270
0.8960 0.9400
0.9490 0.9620
0.9790 0.9820

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0080 404.93
0.0310 391.42
0.0820 372.38
0.1230 366.03
0.1960 361.22
0.2550 359.31
0.3130 358.12
0.3490 357.30
0.3970 356.39
0.4640 355.72
0.4880 355.34
0.5530 354.74
0.6000 354.28
0.6500 353.89
0.7060 353.45
0.7500 353.09
0.8020 352.70
0.8500 352.32
0.8960 351.99
0.9490 351.63
0.9790 351.48

Boiling temperature at pressure P, K [ref]

Fixed Measured
Pressure, kPa - Liquid Mole fraction of Ethanol (2) - Liquid Boiling temperature at pressure P, K - Liquid
40.00 0.0000 379.81
40.00 0.1000 339.47
40.00 0.2000 335.39
40.00 0.3007 334.54
40.00 0.4000 333.19
40.00 0.4997 332.04
40.00 0.6000 331.51
40.00 0.7000 330.87
40.00 0.7999 330.53
40.00 0.9000 329.95
40.00 1.0000 329.69
53.33 0.0000 388.96
53.33 0.1000 347.29
53.33 0.1501 344.42
53.33 0.2000 342.87
53.33 0.2499 342.41
53.33 0.3007 341.67
53.33 0.4000 340.31
53.33 0.4997 338.65
53.33 0.6000 338.15
53.33 0.7000 337.48
53.33 0.7999 337.06
53.33 0.9000 336.39
53.33 1.0000 336.07
66.66 0.0000 396.45
66.66 0.1000 353.52
66.66 0.1501 350.52
66.66 0.2000 349.05
66.66 0.3007 347.09
66.66 0.4000 345.78
66.66 0.4997 344.14
66.66 0.6000 343.57
66.66 0.7000 342.89
66.66 0.7999 342.31
66.66 0.9000 341.62
66.66 1.0000 341.23
79.99 0.0000 402.82
79.99 0.1000 359.33
79.99 0.1501 355.63
79.99 0.2000 354.37
79.99 0.2499 353.17
79.99 0.3007 351.39
79.99 0.4000 350.32
79.99 0.4997 348.85
79.99 0.6000 348.18
79.99 0.7000 347.45
79.99 0.7999 346.75
79.99 0.9000 346.03
79.99 1.0000 345.60
93.32 0.0000 408.40
93.32 0.1000 364.14
93.32 0.1501 359.98
93.32 0.2000 359.14
93.32 0.3007 355.86
93.32 0.4000 354.43
93.32 0.4997 352.97
93.32 0.6000 352.21
93.32 0.7000 351.41
93.32 0.7999 350.63
93.32 0.9000 349.87
93.32 1.0000 349.39
101.30 0.0000 411.48
101.30 0.1000 369.38
101.30 0.2000 361.88
101.30 0.2499 359.43
101.30 0.3000 358.12
101.30 0.4000 355.90
101.30 0.4999 355.45
101.30 0.6000 353.98
101.30 0.7000 353.46
101.30 0.8000 352.65
101.30 0.9000 351.90
101.30 1.0000 351.44

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0080 404.93
0.0310 391.42
0.0820 372.38
0.1230 366.03
0.1960 361.22
0.2550 359.31
0.3130 358.12
0.3490 357.30
0.3970 356.39
0.4640 355.72
0.4880 355.34
0.5530 354.74
0.6000 354.28
0.6500 353.89
0.7060 353.45
0.7500 353.09
0.8020 352.70
0.8500 352.32
0.8960 351.99
0.9490 351.63
0.9790 351.48

Boiling temperature at pressure P, K [ref]

Fixed Measured
Pressure, kPa - Liquid Mole fraction of Ethanol (2) - Liquid Boiling temperature at pressure P, K - Liquid
40.00 0.0000 379.81
40.00 0.1000 339.47
40.00 0.2000 335.39
40.00 0.3007 334.54
40.00 0.4000 333.19
40.00 0.4997 332.04
40.00 0.6000 331.51
40.00 0.7000 330.87
40.00 0.7999 330.53
40.00 0.9000 329.95
40.00 1.0000 329.69
53.33 0.0000 388.96
53.33 0.1000 347.29
53.33 0.1501 344.42
53.33 0.2000 342.87
53.33 0.2499 342.41
53.33 0.3007 341.67
53.33 0.4000 340.31
53.33 0.4997 338.65
53.33 0.6000 338.15
53.33 0.7000 337.48
53.33 0.7999 337.06
53.33 0.9000 336.39
53.33 1.0000 336.07
66.66 0.0000 396.45
66.66 0.1000 353.52
66.66 0.1501 350.52
66.66 0.2000 349.05
66.66 0.3007 347.09
66.66 0.4000 345.78
66.66 0.4997 344.14
66.66 0.6000 343.57
66.66 0.7000 342.89
66.66 0.7999 342.31
66.66 0.9000 341.62
66.66 1.0000 341.23
79.99 0.0000 402.82
79.99 0.1000 359.33
79.99 0.1501 355.63
79.99 0.2000 354.37
79.99 0.2499 353.17
79.99 0.3007 351.39
79.99 0.4000 350.32
79.99 0.4997 348.85
79.99 0.6000 348.18
79.99 0.7000 347.45
79.99 0.7999 346.75
79.99 0.9000 346.03
79.99 1.0000 345.60
93.32 0.0000 408.40
93.32 0.1000 364.14
93.32 0.1501 359.98
93.32 0.2000 359.14
93.32 0.3007 355.86
93.32 0.4000 354.43
93.32 0.4997 352.97
93.32 0.6000 352.21
93.32 0.7000 351.41
93.32 0.7999 350.63
93.32 0.9000 349.87
93.32 1.0000 349.39
101.30 0.0000 411.48
101.30 0.1000 369.38
101.30 0.2000 361.88
101.30 0.2499 359.43
101.30 0.3000 358.12
101.30 0.4000 355.90
101.30 0.4999 355.45
101.30 0.6000 353.98
101.30 0.7000 353.46
101.30 0.8000 352.65
101.30 0.9000 351.90
101.30 1.0000 351.44

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Ethanol (2) - Liquid y1[mol/mol] of Ethanol (2) - Vapour
411.55 0.0000 0.0000
389.45 0.0300 0.6500
370.75 0.0850 0.8150
363.55 0.1450 0.8400
360.25 0.1800 0.8700
357.15 0.3350 0.8900
355.55 0.4450 0.8950
354.25 0.6200 0.9100
353.35 0.7250 0.9100
352.85 0.7880 0.9150
352.65 0.8250 0.9250
352.25 0.8600 0.9300
352.05 0.8900 0.9350
351.95 0.9300 0.9500
351.85 0.9500 0.9620
351.75 0.9650 0.9700
351.55 1.0000 1.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Ethanol (2) - Liquid y1[mol/mol] of Ethanol (2) - Vapour
411.52 0.0000 0.0000
373.82 0.0570 0.6710
365.04 0.1200 0.7700
359.44 0.2110 0.8250
357.26 0.3060 0.8410
353.52 0.6680 0.8810
352.67 0.7800 0.8980
352.08 0.8610 0.9190
351.72 0.9140 0.9400
351.59 0.9420 0.9550
351.49 0.9680 0.9730
351.46 0.9860 0.9870
351.45 1.0000 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 318.15 (VLE)

P [kPa] - VLE x1[mol/mol] of Ethanol (2) - Liquid
4.446 0.0036
4.954 0.0054
5.464 0.0074
5.926 0.0092
7.125 0.0143
7.614 0.0166
8.518 0.0210
10.061 0.0299
11.284 0.0386
12.28 0.0474
13.527 0.0615
14.459 0.0754
15.164 0.0886
15.74 0.1017
16.216 0.1144
16.944 0.1387
17.5 0.1620
17.932 0.1838
18.428 0.2147
18.904 0.2522
19.262 0.2863
19.542 0.3174

Sources