Mixture of n-Hexane + Trichloromethane + Ethanol

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

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. 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 Ethanol (3) - Liquid x2[mol/mol] of Trichloromethane (2) - Liquid y1[mol/mol] of Ethanol (3) - Vapour y2[mol/mol] of Trichloromethane (2) - Vapour
331.77 0.0990 0.8020 0.1390 0.7430
331.48 0.2040 0.7000 0.1820 0.6850
331.19 0.0990 0.7020 0.1660 0.6280
331.58 0.3060 0.5980 0.2170 0.6330
330.83 0.2020 0.6010 0.1870 0.5840
330.87 0.0980 0.6020 0.1660 0.5560
331.97 0.4060 0.4970 0.2460 0.5800
330.86 0.3020 0.4990 0.2200 0.5200
330.61 0.2020 0.4990 0.1970 0.4900
330.93 0.0920 0.5010 0.1650 0.4840
332.7 0.5100 0.3910 0.2790 0.5120
331.31 0.4040 0.3990 0.2400 0.4570
330.66 0.3030 0.3980 0.2190 0.4220
330.51 0.2000 0.3980 0.2020 0.4030
330.98 0.0980 0.4000 0.1760 0.4010
333.43 0.6100 0.2940 0.3160 0.4300
331.42 0.5100 0.2940 0.2490 0.3880
330.95 0.4110 0.2970 0.2670 0.3360
330.66 0.3020 0.2990 0.2480 0.3170
330.73 0.2000 0.2990 0.2320 0.3090
331.31 0.0960 0.2950 0.2060 0.3130
334.64 0.7100 0.1920 0.3510 0.3250
332.35 0.6060 0.1990 0.3030 0.2760
331.46 0.5090 0.1960 0.2930 0.2490
330.99 0.4050 0.1990 0.2960 0.2230
330.88 0.3040 0.1990 0.2810 0.2160
330.95 0.1920 0.1990 0.2730 0.2100
331.58 0.0920 0.1990 0.2510 0.2150
336.86 0.8150 0.0950 0.4060 0.1730
333.37 0.7050 0.0980 0.3570 0.1390
331.98 0.6090 0.1000 0.3250 0.1210
331.49 0.5050 0.1000 0.3280 0.1120
331.29 0.4100 0.0990 0.3070 0.1090
331.12 0.3010 0.1000 0.3000 0.1070
331.34 0.1990 0.0990 0.2990 0.1070
331.94 0.0900 0.0980 0.2770 0.1130

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 308.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Ethanol (3) - Liquid x2[mol/mol] of Trichloromethane (2) - Liquid y1[mol/mol] of Ethanol (3) - Vapour y2[mol/mol] of Trichloromethane (2) - Vapour
42.636 0.1000 0.8010 0.1000 0.7740
42.557 0.2020 0.7000 0.1310 0.7270
43.623 0.0900 0.7020 0.1170 0.6650
42.01 0.3040 0.5990 0.1620 0.6750
43.343 0.2010 0.6010 0.1420 0.6140
43.85 0.0990 0.6010 0.1300 0.5800
41.183 0.4040 0.4980 0.1880 0.6200
43.01 0.3010 0.4990 0.1670 0.5560
43.65 0.2010 0.4990 0.1500 0.5200
43.69 0.0940 0.5010 0.1350 0.5000
40.237 0.5070 0.3940 0.2010 0.5620
42.197 0.4030 0.3990 0.1840 0.4900
43.156 0.3020 0.3990 0.1730 0.4510
43.423 0.2000 0.3990 0.1620 0.4310
43.396 0.0980 0.4000 0.1370 0.4220
38.237 0.6070 0.2960 0.2410 0.4710
41.397 0.5070 0.2960 0.2080 0.4020
42.157 0.4080 0.2980 0.2030 0.3700
42.916 0.3010 0.3000 0.1870 0.3450
42.557 0.2000 0.3000 0.1920 0.3310
42.33 0.0980 0.2960 0.1590 0.3370
35.77 0.7070 0.1940 0.2930 0.3530
39.437 0.6050 0.1990 0.2450 0.2970
41.077 0.5060 0.1980 0.2380 0.2580
41.917 0.4040 0.1990 0.2380 0.2410
42.117 0.3030 0.1990 0.2220 0.2370
42.197 0.1950 0.1990 0.1980 0.2350
41.943 0.0950 0.1990 0.1880 0.2350
31.931 0.8110 0.0960 0.3680 0.1950
37.557 0.7040 0.0990 0.2910 0.1490
39.783 0.6060 0.1000 0.2670 0.1310
40.397 0.5040 0.1000 0.2630 0.1220
40.97 0.4070 0.0990 0.2560 0.1180
41.117 0.3010 0.1000 0.2260 0.1190
41.117 0.1990 0.1000 0.2170 0.1200
40.703 0.0920 0.0990 0.2100 0.1240

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 318.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Ethanol (3) - Liquid x2[mol/mol] of Trichloromethane (2) - Liquid y1[mol/mol] of Ethanol (3) - Vapour y2[mol/mol] of Trichloromethane (2) - Vapour
63.155 0.1000 0.8000 0.1200 0.7580
63.261 0.2010 0.7000 0.1500 0.7100
64.568 0.1000 0.7010 0.1270 0.6560
62.755 0.3030 0.5990 0.1810 0.6590
64.395 0.2010 0.6000 0.1700 0.5950
64.995 0.0990 0.6010 0.1460 0.5700
61.662 0.4030 0.4980 0.2080 0.6050
64.128 0.3010 0.4990 0.1880 0.5410
64.688 0.2010 0.4990 0.1730 0.5060
64.915 0.0970 0.5000 0.1500 0.4930
60.382 0.5040 0.3960 0.2360 0.5400
63.195 0.4020 0.3990 0.2030 0.4790
64.741 0.3010 0.3990 0.1950 0.4400
64.981 0.2000 0.4000 0.1810 0.4190
64.621 0.0990 0.4000 0.1590 0.4110
57.849 0.6040 0.2970 0.2680 0.4570
63.248 0.5040 0.2970 0.2400 0.3850
63.835 0.4040 0.2990 0.2310 0.3520
64.475 0.3010 0.3000 0.2200 0.3300
63.728 0.2000 0.3000 0.2090 0.3240
63.328 0.0980 0.2980 0.1800 0.3260
54.822 0.7040 0.1970 0.3130 0.3440
59.875 0.6030 0.1990 0.2670 0.2880
62.035 0.5040 0.1980 0.2580 0.2500
62.928 0.4020 0.2000 0.2540 0.2360
63.528 0.3010 0.2000 0.2410 0.2290
63.568 0.1970 0.1990 0.2320 0.2260
62.755 0.0970 0.1990 0.2220 0.2260
50.356 0.8060 0.0980 0.3830 0.1830
57.435 0.7020 0.0990 0.3100 0.1440
60.328 0.6040 0.1000 0.2910 0.1280
61.395 0.5020 0.1000 0.2820 0.1190
62.075 0.4040 0.1000 0.2700 0.1160
62.368 0.3000 0.1000 0.2620 0.1140
62.195 0.1990 0.1000 0.2580 0.1140
61.595 0.0960 0.0990 0.2370 0.1200

Sources