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Mixture of Diisopropyl ether + Ethanol + Water

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

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

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. Mole fraction (6)

Mole fraction [ref]

Operational conditions:

Fixed Measured
Mole fraction of Diisopropyl ether (1) - Liquid mixture 1 Mole fraction of Ethanol (2) - Liquid mixture 1 Mole fraction of Diisopropyl ether (1) - Liquid mixture 2 Mole fraction of Ethanol (2) - Liquid mixture 2
0.8451 0.0867 0.0029 0.0655
0.7507 0.1472 0.0040 0.1009
0.6453 0.2177 0.0054 0.1233
0.4801 0.2970 0.0095 0.1571
0.3610 0.3380 0.0154 0.1845
0.2542 0.3464 0.0263 0.2142
0.1486 0.3232 0.0564 0.2593

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Water (3) - Liquid Mole fraction of Diisopropyl ether (1) - Liquid Mole fraction of Water (3) - Gas Mole fraction of Diisopropyl ether (1) - Gas
339.99 0.5542 0.0586 0.2141 0.4830
340.64 0.5332 0.0538 0.2072 0.5056
342.13 0.5162 0.0464 0.2326 0.4195
342.40 0.4917 0.0486 0.2226 0.4046
343.80 0.4909 0.0380 0.2515 0.3384
344.26 0.4552 0.0388 0.2257 0.3342
345.23 0.4636 0.0341 0.2390 0.3003
345.43 0.4216 0.0347 0.2322 0.2815
346.16 0.4024 0.0362 0.2284 0.2628
346.24 0.4427 0.0301 0.2396 0.2623
346.83 0.3039 0.0343 0.3287 0.1842
347.08 0.3727 0.0288 0.2327 0.2215
347.35 0.2853 0.0321 0.3429 0.1656
348.07 0.2595 0.0252 0.2963 0.1432
348.84 0.2324 0.0221 0.4044 0.1049
349.24 0.2075 0.0205 0.2828 0.1094
349.50 0.0594 0.0202 0.2799 0.0936

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of Diisopropyl ether (1) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of Diisopropyl ether (1) - Liquid mixture 2 Mole fraction of Diisopropyl ether (1) - Gas Mole fraction of Water (3) - Gas
335.31 0.0476 0.9524 0.9991 0.0009 0.7814 0.2186
334.53 0.0605 0.8805 0.9636 0.0012 0.7049 0.2100
334.40 0.0644 0.8498 0.9510 0.0016 0.6945 0.2010
334.16 0.0877 0.7844 0.9231 0.0015 0.6670 0.1974
334.25 0.0997 0.7194 0.9161 0.0024 0.6631 0.1861
334.27 0.1051 0.7134 0.9221 0.0019 0.6597 0.1888
334.19 0.1168 0.6733 0.9128 0.0011 0.6219 0.1826
334.42 0.1232 0.6499 0.9004 0.0029 0.6447 0.1879
334.38 0.1451 0.6029 0.8845 0.0038 0.6391 0.1944
334.56 0.1520 0.5959 0.8852 0.0036 0.6299 0.1927
334.47 0.1635 0.5899 0.8852 0.0042 0.6188 0.1731
334.55 0.1738 0.5667 0.8798 0.0044 0.6306 0.1881
334.77 0.1951 0.5081 0.8644 0.0043 0.6196 0.1891
334.84 0.2599 0.4197 0.8530 0.0019 0.6195 0.1866
334.92 0.2629 0.4157 0.8365 0.0077 0.6147 0.1798
335.03 0.3408 0.3132 0.8201 0.0108 0.6081 0.1886
335.04 0.3473 0.2972 0.7858 0.0178 0.5982 0.1889
335.37 0.3813 0.2594 0.7761 0.0208 0.6034 0.1821
335.22 0.3941 0.2551 0.7590 0.0211 0.6081 0.1880
335.39 0.7927 0.0131 0.7954 0.0127 0.5840 0.1945
336.29 0.7644 0.0160 0.7674 0.0141 0.5770 0.2070

Mole fraction [ref]

Operational conditions:

Fixed Measured
Mole fraction of Diisopropyl ether (1) - Liquid mixture 1 Mole fraction of Ethanol (2) - Liquid mixture 1 Mole fraction of Diisopropyl ether (1) - Liquid mixture 2 Mole fraction of Ethanol (2) - Liquid mixture 2
0.8451 0.0867 0.0029 0.0655
0.7507 0.1472 0.0040 0.1009
0.6453 0.2177 0.0054 0.1233
0.4801 0.2970 0.0095 0.1571
0.3610 0.3380 0.0154 0.1845
0.2542 0.3464 0.0263 0.2142
0.1486 0.3232 0.0564 0.2593

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Water (3) - Liquid Mole fraction of Diisopropyl ether (1) - Liquid Mole fraction of Water (3) - Gas Mole fraction of Diisopropyl ether (1) - Gas
339.99 0.5542 0.0586 0.2141 0.4830
340.64 0.5332 0.0538 0.2072 0.5056
342.13 0.5162 0.0464 0.2326 0.4195
342.40 0.4917 0.0486 0.2226 0.4046
343.80 0.4909 0.0380 0.2515 0.3384
344.26 0.4552 0.0388 0.2257 0.3342
345.23 0.4636 0.0341 0.2390 0.3003
345.43 0.4216 0.0347 0.2322 0.2815
346.16 0.4024 0.0362 0.2284 0.2628
346.24 0.4427 0.0301 0.2396 0.2623
346.83 0.3039 0.0343 0.3287 0.1842
347.08 0.3727 0.0288 0.2327 0.2215
347.35 0.2853 0.0321 0.3429 0.1656
348.07 0.2595 0.0252 0.2963 0.1432
348.84 0.2324 0.0221 0.4044 0.1049
349.24 0.2075 0.0205 0.2828 0.1094
349.50 0.0594 0.0202 0.2799 0.0936

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of Diisopropyl ether (1) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of Diisopropyl ether (1) - Liquid mixture 2 Mole fraction of Diisopropyl ether (1) - Gas Mole fraction of Water (3) - Gas
335.31 0.0476 0.9524 0.9991 0.0009 0.7814 0.2186
334.53 0.0605 0.8805 0.9636 0.0012 0.7049 0.2100
334.40 0.0644 0.8498 0.9510 0.0016 0.6945 0.2010
334.16 0.0877 0.7844 0.9231 0.0015 0.6670 0.1974
334.25 0.0997 0.7194 0.9161 0.0024 0.6631 0.1861
334.27 0.1051 0.7134 0.9221 0.0019 0.6597 0.1888
334.19 0.1168 0.6733 0.9128 0.0011 0.6219 0.1826
334.42 0.1232 0.6499 0.9004 0.0029 0.6447 0.1879
334.38 0.1451 0.6029 0.8845 0.0038 0.6391 0.1944
334.56 0.1520 0.5959 0.8852 0.0036 0.6299 0.1927
334.47 0.1635 0.5899 0.8852 0.0042 0.6188 0.1731
334.55 0.1738 0.5667 0.8798 0.0044 0.6306 0.1881
334.77 0.1951 0.5081 0.8644 0.0043 0.6196 0.1891
334.84 0.2599 0.4197 0.8530 0.0019 0.6195 0.1866
334.92 0.2629 0.4157 0.8365 0.0077 0.6147 0.1798
335.03 0.3408 0.3132 0.8201 0.0108 0.6081 0.1886
335.04 0.3473 0.2972 0.7858 0.0178 0.5982 0.1889
335.37 0.3813 0.2594 0.7761 0.0208 0.6034 0.1821
335.22 0.3941 0.2551 0.7590 0.0211 0.6081 0.1880
335.39 0.7927 0.0131 0.7954 0.0127 0.5840 0.1945
336.29 0.7644 0.0160 0.7674 0.0141 0.5770 0.2070

Sources