Mixture of Diisopropyl ether + Isopropyl Alcohol + 1-Butanol, 3-methyl-

Excel

Diisopropyl ether

Name
Diisopropyl ether
InChI
InChI=1S/C6H14O/c1-5(2)7-6(3)4/h5-6H,1-4H3
InChI Key
ZAFNJMIOTHYJRJ-UHFFFAOYSA-N
Formula
C6H14O
SMILES
CC(C)OC(C)C
Mol. Weight (g/mol)
102.17
CAS
108-20-3

Isopropyl Alcohol

Name
Isopropyl Alcohol
InChI
InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3
InChI Key
KFZMGEQAYNKOFK-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CC(C)O
Mol. Weight (g/mol)
60.09
CAS
67-63-0

1-Butanol, 3-methyl-

Name
1-Butanol, 3-methyl-
InChI
InChI=1S/C5H12O/c1-5(2)3-4-6/h5-6H,3-4H2,1-2H3
InChI Key
PHTQWCKDNZKARW-UHFFFAOYSA-N
Formula
C5H12O
SMILES
CC(C)CCO
Mol. Weight (g/mol)
88.15
CAS
123-51-3
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Datasets

  1. Temperature, K x Mole fraction (2)

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Fixed Measured
Temperature, K - Gas Mole fraction of Diisopropyl ether (1) - Liquid Mole fraction of Isopropyl Alcohol (2) - Liquid Mole fraction of Isopropyl Alcohol (2) - Gas Mole fraction of Diisopropyl ether (1) - Gas
340.30 0.7420 0.2210 0.2140 0.7830
341.43 0.5180 0.4430 0.3240 0.6740
341.45 0.8960 0.0570 0.0800 0.9140
342.14 0.5720 0.3340 0.2730 0.7200
342.36 0.7880 0.1110 0.1290 0.8600
342.67 0.6540 0.2200 0.2050 0.7820
343.72 0.3190 0.6460 0.4440 0.5530
344.25 0.3590 0.5480 0.3960 0.5970
345.30 0.6800 0.1090 0.1190 0.8570
345.54 0.4640 0.3280 0.2770 0.7050
345.83 0.3840 0.4340 0.3430 0.6420
347.21 0.5060 0.2120 0.2020 0.7680
348.46 0.2640 0.5360 0.4380 0.5450
348.47 0.5770 0.1030 0.1110 0.8520
348.54 0.1730 0.7330 0.5790 0.4130
348.92 0.6150 0.0600 0.0680 0.8920
349.66 0.3600 0.3210 0.2970 0.6710
350.46 0.2750 0.4340 0.3890 0.5830
350.46 0.1750 0.6490 0.5500 0.4340
351.25 0.3960 0.2120 0.2150 0.7410
352.41 0.4650 0.0990 0.1120 0.8330
352.53 0.0810 0.8250 0.7440 0.2460
353.40 0.0460 0.9090 0.8440 0.1510
353.90 0.1730 0.5220 0.5120 0.4560
355.04 0.2550 0.3130 0.3370 0.6120
356.73 0.1750 0.4220 0.4620 0.4860
356.94 0.2820 0.2090 0.2470 0.6810
357.30 0.3930 0.0570 0.0720 0.8440
357.45 0.0810 0.6380 0.6960 0.2670
357.58 0.3540 0.0960 0.1190 0.7990
359.03 0.0410 0.7080 0.8130 0.1510
362.80 0.1530 0.3000 0.4170 0.4920
363.47 0.2570 0.0980 0.1430 0.7360
364.16 0.1810 0.2060 0.3050 0.5800
364.79 0.0850 0.4090 0.5910 0.3120
365.32 0.0430 0.5170 0.7490 0.1630
370.92 0.1730 0.0950 0.1740 0.6340
371.27 0.1970 0.0520 0.0950 0.6980
374.69 0.0860 0.1950 0.4090 0.3780
374.96 0.0440 0.2900 0.6000 0.1960
380.08 0.0940 0.0970 0.2370 0.4550
393.35 0.0360 0.0460 0.1680 0.2250

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Fixed Measured
Temperature, K - Gas Mole fraction of Diisopropyl ether (1) - Liquid Mole fraction of Isopropyl Alcohol (2) - Liquid Mole fraction of Isopropyl Alcohol (2) - Gas Mole fraction of Diisopropyl ether (1) - Gas
340.30 0.7420 0.2210 0.2140 0.7830
341.43 0.5180 0.4430 0.3240 0.6740
341.45 0.8960 0.0570 0.0800 0.9140
342.14 0.5720 0.3340 0.2730 0.7200
342.36 0.7880 0.1110 0.1290 0.8600
342.67 0.6540 0.2200 0.2050 0.7820
343.72 0.3190 0.6460 0.4440 0.5530
344.25 0.3590 0.5480 0.3960 0.5970
345.30 0.6800 0.1090 0.1190 0.8570
345.54 0.4640 0.3280 0.2770 0.7050
345.83 0.3840 0.4340 0.3430 0.6420
347.21 0.5060 0.2120 0.2020 0.7680
348.46 0.2640 0.5360 0.4380 0.5450
348.47 0.5770 0.1030 0.1110 0.8520
348.54 0.1730 0.7330 0.5790 0.4130
348.92 0.6150 0.0600 0.0680 0.8920
349.66 0.3600 0.3210 0.2970 0.6710
350.46 0.2750 0.4340 0.3890 0.5830
350.46 0.1750 0.6490 0.5500 0.4340
351.25 0.3960 0.2120 0.2150 0.7410
352.41 0.4650 0.0990 0.1120 0.8330
352.53 0.0810 0.8250 0.7440 0.2460
353.40 0.0460 0.9090 0.8440 0.1510
353.90 0.1730 0.5220 0.5120 0.4560
355.04 0.2550 0.3130 0.3370 0.6120
356.73 0.1750 0.4220 0.4620 0.4860
356.94 0.2820 0.2090 0.2470 0.6810
357.30 0.3930 0.0570 0.0720 0.8440
357.45 0.0810 0.6380 0.6960 0.2670
357.58 0.3540 0.0960 0.1190 0.7990
359.03 0.0410 0.7080 0.8130 0.1510
362.80 0.1530 0.3000 0.4170 0.4920
363.47 0.2570 0.0980 0.1430 0.7360
364.16 0.1810 0.2060 0.3050 0.5800
364.79 0.0850 0.4090 0.5910 0.3120
365.32 0.0430 0.5170 0.7490 0.1630
370.92 0.1730 0.0950 0.1740 0.6340
371.27 0.1970 0.0520 0.0950 0.6980
374.69 0.0860 0.1950 0.4090 0.3780
374.96 0.0440 0.2900 0.6000 0.1960
380.08 0.0940 0.0970 0.2370 0.4550
393.35 0.0360 0.0460 0.1680 0.2250

Sources