Mixture of Ethanol + Ethyl ether + 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

Ethyl ether

Name
Ethyl ether
InChI
InChI=1S/C4H10O/c1-3-5-4-2/h3-4H2,1-2H3
InChI Key
RTZKZFJDLAIYFH-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CCOCC
Mol. Weight (g/mol)
74.12
CAS
60-29-7

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. Vapor Liquid Equilibrium at Constant Pressure (3)

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 287.48 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Ethyl ether (2) - Liquid x2[mol/mol] of Ethanol (1) - Liquid y1[mol/mol] of Ethyl ether (2) - Vapour y2[mol/mol] of Ethanol (1) - Vapour
378.15 0.0050 0.5490 0.1100 0.5930
377.15 0.0100 0.4760 0.0540 0.5740
376.15 0.0080 0.2340 0.0740 0.5140
370.15 0.0170 0.4760 0.1160 0.5670
369.15 0.0170 0.8370 0.0770 0.8030
362.15 0.0090 0.2730 0.1530 0.3920
356.15 0.0600 0.6890 0.3450 0.4910
355.15 0.0480 0.5150 0.3060 0.4830
355.15 0.0690 0.7980 0.3380 0.4900
353.15 0.0740 0.6130 0.4240 0.4260
351.15 0.0310 0.4670 0.2840 0.4700
351.15 0.0390 0.5090 0.2160 0.4770
348.15 0.0410 0.7910 0.2820 0.5820
348.15 0.1030 0.5730 0.4790 0.3650
347.15 0.0090 0.1580 0.2960 0.3720
347.15 0.1180 0.5560 0.5040 0.2960
347.15 0.1210 0.4450 0.6030 0.2740
346.15 0.0230 0.2550 0.4560 0.3060
346.15 0.1390 0.4400 0.6140 0.2600
345.15 0.0050 0.1490 0.3030 0.3650
345.15 0.1730 0.4240 0.6640 0.2430
345.15 0.2310 0.4700 0.6790 0.2310
345.15 0.2420 0.3820 0.6940 0.2090
344.15 0.0160 0.0870 0.4680 0.3040
344.15 0.0230 0.1660 0.6720 0.3070
344.15 0.0300 0.4120 0.2700 0.4700
344.15 0.2700 0.4770 0.6930 0.2260
343.15 0.0130 0.1760 0.3800 0.3060
343.15 0.0230 0.3070 0.3880 0.3870
343.15 0.2230 0.4040 0.6720 0.2250
343.15 0.3680 0.4470 0.7330 0.2030
342.15 0.1120 0.3550 0.6440 0.2670
342.15 0.1850 0.4540 0.6760 0.2400
341.15 0.1670 0.5830 0.5710 0.3560
341.15 0.3200 0.5070 0.7020 0.2170
339.15 0.0060 0.0850 0.6440 0.2920
339.15 0.0080 0.0810 0.6430 0.3220
336.15 0.8570 0.1350 0.9410 0.0540
335.15 0.2270 0.1880 0.7720 0.1660

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 515.01 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Ethyl ether (2) - Liquid x2[mol/mol] of Ethanol (1) - Liquid y1[mol/mol] of Ethyl ether (2) - Vapour y2[mol/mol] of Ethanol (1) - Vapour
397.15 0.0090 0.4930 0.0230 0.5960
393.15 0.0040 0.1150 0.1110 0.3360
390.15 0.0280 0.5460 0.1240 0.5970
389.15 0.0270 0.8330 0.1220 0.7370
388.15 0.0400 0.8220 0.1780 0.6960
384.15 0.0840 0.7780 0.3370 0.5920
382.15 0.0620 0.5600 0.3110 0.4820
381.15 0.0630 0.6980 0.2450 0.5700
381.15 0.0740 0.7210 0.2720 0.5750
381.15 0.0870 0.6640 0.3060 0.4800
379.15 0.0090 0.5210 0.0320 0.6300
377.15 0.0100 0.4760 0.0540 0.5740
377.15 0.0690 0.5170 0.3380 0.4310
376.15 0.0140 0.2230 0.3390 0.3780
376.15 0.0470 0.4450 0.3100 0.4380
376.15 0.1300 0.6420 0.3860 0.4270
375.15 0.0150 0.5810 0.0630 0.6450
372.15 0.1140 0.4820 0.4360 0.3700
371.15 0.0510 0.3540 0.3760 0.3690
371.15 0.0710 0.4060 0.3930 0.4040
371.15 0.2380 0.5740 0.5190 0.3660
370.15 0.1130 0.4890 0.4630 0.3880
369.15 0.0040 0.1280 0.0710 0.4280
369.15 0.0070 0.0830 0.0850 0.2690
367.15 0.2500 0.4290 0.5460 0.2530
364.15 0.3090 0.4580 0.6100 0.2580
364.15 0.5740 0.3190 0.7370 0.1560
362.15 0.4460 0.2640 0.7180 0.1510
362.15 0.7090 0.2380 0.8280 0.1010
361.15 0.4930 0.2410 0.7240 0.1530
361.15 0.7210 0.2250 0.8440 0.1100
361.15 0.8570 0.0970 0.9360 0.0440
361.15 0.8630 0.1180 0.9410 0.0390

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 721.85 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Ethyl ether (2) - Liquid x2[mol/mol] of Ethanol (1) - Liquid y1[mol/mol] of Ethyl ether (2) - Vapour y2[mol/mol] of Ethanol (1) - Vapour
430.15 0.0030 0.0330 0.0050 0.2040
416.15 0.0070 0.5000 0.0230 0.5960
416.15 0.0740 0.8890 0.1360 0.8390
415.15 0.0100 0.5430 0.0420 0.6270
412.15 0.0070 0.2110 0.1560 0.4870
412.15 0.0210 0.5280 0.0860 0.5520
411.15 0.0130 0.8330 0.0370 0.8300
411.15 0.0580 0.6680 0.1660 0.5990
410.15 0.0130 0.8820 0.0250 0.8700
409.15 0.0280 0.7250 0.0670 0.7330
408.15 0.0360 0.7300 0.0930 0.6940
407.15 0.0200 0.6550 0.0540 0.6840
405.15 0.0120 0.7840 0.0130 0.8100
402.15 0.0200 0.2920 0.2170 0.5070
401.15 0.0060 0.1640 0.1160 0.4280
398.15 0.0480 0.5470 0.1860 0.5530
397.15 0.0680 0.8170 0.2080 0.6940
396.15 0.1300 0.7250 0.2860 0.5640
395.15 0.0400 0.3460 0.3980 0.4490
394.15 0.0030 0.0870 0.3080 0.3050
392.15 0.0330 0.4410 0.2550 0.4900
386.15 0.1870 0.5820 0.3850 0.4170
383.15 0.1130 0.2570 0.5590 0.3160
379.15 0.6690 0.2950 0.8000 0.1700
377.15 0.5190 0.2500 0.7230 0.1640
376.15 0.5320 0.4210 0.7420 0.2510
376.15 0.8920 0.0500 0.9150 0.0540
375.15 0.7660 0.0870 0.7990 0.0620

Sources