Mixture of n-Hexane + Trichloromethane + Acetone

Excel

n-Hexane

Name
n-Hexane
InChI
InChI=1S/C6H14/c1-3-5-6-4-2/h3-6H2,1-2H3
InChI Key
VLKZOEOYAKHREP-UHFFFAOYSA-N
Formula
C6H14
SMILES
CCCCCC
Mol. Weight (g/mol)
86.18
CAS
110-54-3

Trichloromethane

Name
Trichloromethane
InChI
InChI=1S/CHCl3/c2-1(3)4/h1H
InChI Key
HEDRZPFGACZZDS-UHFFFAOYSA-N
Formula
CHCl3
SMILES
ClC(Cl)Cl
Mol. Weight (g/mol)
119.38
CAS
67-66-3

Acetone

Name
Acetone
InChI
InChI=1S/C3H6O/c1-3(2)4/h1-2H3
InChI Key
CSCPPACGZOOCGX-UHFFFAOYSA-N
Formula
C3H6O
SMILES
CC(C)=O
Mol. Weight (g/mol)
58.08
CAS
67-64-1
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Datasets

  1. Vapor Liquid Equilibrium at Constant Pressure
  2. Vapor Liquid Equilibrium at Constant Temperature (2)

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Acetone (3) - Liquid x2[mol/mol] of Trichloromethane (2) - Liquid y1[mol/mol] of Acetone (3) - Vapour y2[mol/mol] of Trichloromethane (2) - Vapour
334.72 0.1010 0.8000 0.0700 0.7950
335.04 0.2010 0.7000 0.1730 0.6710
333.99 0.1010 0.7010 0.0800 0.6780
335.24 0.3010 0.6000 0.2910 0.5420
334.06 0.2010 0.6000 0.1890 0.5420
333.81 0.1010 0.6000 0.0950 0.5850
334.14 0.4000 0.5020 0.4200 0.4050
333.37 0.3000 0.5000 0.3150 0.4010
333.3 0.2000 0.5010 0.2180 0.4400
333.74 0.1000 0.5000 0.1330 0.4860
333.31 0.4990 0.4020 0.5300 0.2940
331.7 0.4000 0.4010 0.4290 0.2820
332.0 0.3000 0.4000 0.3470 0.3030
332.55 0.1970 0.4000 0.2630 0.3380
333.66 0.1000 0.4000 0.1350 0.4030
330.97 0.6000 0.3000 0.6320 0.1900
330.26 0.5000 0.3000 0.5300 0.1790
329.77 0.4000 0.3010 0.4600 0.1900
330.46 0.3000 0.3000 0.3950 0.2150
331.61 0.1990 0.3010 0.3260 0.2360
333.48 0.0990 0.3000 0.1740 0.3040
329.25 0.7000 0.2010 0.7160 0.1060
327.75 0.6000 0.2000 0.6010 0.0990
327.37 0.5000 0.2000 0.5600 0.0950
327.69 0.3990 0.2020 0.5100 0.1020
328.05 0.2990 0.2010 0.4540 0.1160
330.28 0.1990 0.2000 0.3720 0.1510
333.8 0.0980 0.2000 0.2050 0.2160
327.01 0.8010 0.1000 0.7710 0.0470
325.65 0.7010 0.1010 0.6640 0.0390
325.05 0.6000 0.1000 0.6110 0.0400
325.16 0.4990 0.1000 0.5760 0.0430
325.61 0.4000 0.1000 0.5400 0.0520
326.78 0.2980 0.1000 0.4880 0.0610
328.65 0.1990 0.1000 0.4180 0.0810
332.33 0.0960 0.1000 0.2750 0.0900
333.94 0.0650 0.6000 0.0680 0.5990

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 308.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Acetone (3) - Liquid x2[mol/mol] of Trichloromethane (2) - Liquid y1[mol/mol] of Acetone (3) - Vapour y2[mol/mol] of Trichloromethane (2) - Vapour
38.264 0.1090 0.7990 0.0600 0.7980
37.344 0.2070 0.7000 0.1580 0.6790
39.557 0.1100 0.7040 0.0670 0.6980
36.744 0.3050 0.6010 0.2760 0.5450
39.383 0.2040 0.6030 0.1750 0.5480
40.477 0.1070 0.6000 0.0830 0.5830
38.53 0.3990 0.5140 0.4090 0.4100
39.97 0.3010 0.5020 0.3100 0.4060
40.143 0.2000 0.5040 0.2090 0.4370
40.183 0.0980 0.5020 0.1050 0.4920
39.503 0.4950 0.4110 0.5350 0.2800
42.676 0.3990 0.4060 0.4250 0.2780
41.957 0.2970 0.4030 0.3420 0.2990
41.823 0.1900 0.4040 0.2490 0.3400
40.677 0.0970 0.4000 0.1250 0.4080
43.756 0.6000 0.3030 0.6390 0.1810
45.423 0.4980 0.3050 0.5410 0.1730
45.903 0.4000 0.3040 0.4620 0.1840
45.103 0.2970 0.3020 0.3860 0.2110
43.01 0.1940 0.3040 0.3000 0.2470
40.103 0.0940 0.2990 0.1740 0.3000
47.209 0.6970 0.2080 0.7090 0.1040
50.209 0.5990 0.2030 0.6230 0.0900
49.823 0.4970 0.2040 0.5610 0.0990
49.956 0.3960 0.2080 0.4960 0.1140
48.076 0.2900 0.2070 0.4350 0.1270
44.623 0.1930 0.2020 0.3520 0.1630
40.223 0.0860 0.1970 0.2030 0.2190
51.089 0.8070 0.1040 0.7520 0.0440
53.556 0.7100 0.1070 0.6690 0.0430
55.182 0.5990 0.1030 0.6210 0.0420
54.569 0.4910 0.1020 0.5950 0.0370
54.102 0.3960 0.1030 0.5440 0.0430
51.916 0.2830 0.1020 0.4910 0.0530
48.209 0.1930 0.1000 0.4100 0.0700
42.783 0.0870 0.1000 0.2670 0.0890
40.063 0.0650 0.6000 0.0600 0.6000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 318.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Acetone (3) - Liquid x2[mol/mol] of Trichloromethane (2) - Liquid y1[mol/mol] of Acetone (3) - Vapour y2[mol/mol] of Trichloromethane (2) - Vapour
56.849 0.1030 0.8000 0.0620 0.8060
55.769 0.2050 0.7000 0.1570 0.6780
60.395 0.1070 0.7030 0.0710 0.6920
54.955 0.3040 0.6010 0.2790 0.5450
58.155 0.2030 0.6020 0.1790 0.5480
59.648 0.1050 0.6000 0.0920 0.5830
57.795 0.3990 0.5100 0.4140 0.4080
59.235 0.3010 0.5010 0.3060 0.4050
59.635 0.2000 0.5030 0.2120 0.4420
56.209 0.0980 0.5020 0.1050 0.4950
60.488 0.4960 0.4080 0.5260 0.2880
62.608 0.4000 0.4040 0.4340 0.2760
62.008 0.2980 0.4020 0.3480 0.2990
61.262 0.1930 0.4020 0.2510 0.3450
59.915 0.0980 0.4000 0.1320 0.4060
64.155 0.6000 0.3020 0.6270 0.1830
66.355 0.4990 0.3030 0.5300 0.1860
66.875 0.4000 0.3030 0.4600 0.1930
66.408 0.2980 0.3010 0.4020 0.2150
63.475 0.1960 0.3020 0.2900 0.2550
59.222 0.0960 0.2990 0.1700 0.3100
69.328 0.6980 0.2060 0.7100 0.0990
72.447 0.5990 0.2020 0.6180 0.0930
72.327 0.4980 0.2020 0.5590 0.0990
71.287 0.3970 0.2060 0.5100 0.1060
70.834 0.2930 0.2050 0.4300 0.1280
66.635 0.1950 0.2010 0.3480 0.1560
58.995 0.0900 0.1980 0.2000 0.2190
73.967 0.8050 0.1030 0.7550 0.0400
77.58 0.7070 0.1050 0.6700 0.0370
80.38 0.5990 0.1020 0.6200 0.0360
79.327 0.4940 0.1010 0.5870 0.0390
78.914 0.3970 0.1020 0.5520 0.0420
75.434 0.2880 0.1010 0.4870 0.0540
69.888 0.1950 0.1000 0.4110 0.0690
62.142 0.0900 0.1000 0.2610 0.0960
59.182 0.0650 0.6000 0.0650 0.6000

Sources