Mixture of 1-Propanol + Diisopropyl ether + Water

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1-Propanol

Name
1-Propanol
InChI
InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3
InChI Key
BDERNNFJNOPAEC-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CCCO
Mol. Weight (g/mol)
60.09
CAS
71-23-8

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

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 (10)

Mole fraction [ref]

Operational conditions:

Fixed Measured
Mole fraction of Diisopropyl ether (2) - Liquid mixture 1 Mole fraction of 1-Propanol (1) - Liquid mixture 1 Mole fraction of Diisopropyl ether (2) - Liquid mixture 2 Mole fraction of 1-Propanol (1) - Liquid mixture 2
0.7998 0.1234 0.0018 0.0180
0.6029 0.2514 0.0019 0.0291
0.4651 0.3182 0.0020 0.0350
0.3509 0.3617 0.0021 0.0400
0.2598 0.3849 0.0021 0.0442
0.2069 0.3923 0.0021 0.0478
0.1396 0.3801 0.0024 0.0554
0.1004 0.3544 0.0029 0.0638

Temperature, K x Mole fraction x Mass fraction [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mole fraction of Water (3) - Liquid mixture 1 Mass fraction of 1-Propanol (1) - Liquid mixture 1 Mole fraction of 1-Propanol (1) - Liquid mixture 2 Mole fraction of Water (3) - Liquid mixture 2
298.20 0.9984 0.0000 0.0000 0.0016
298.20 0.9288 0.0640 0.0889 0.0050
298.20 0.8550 0.1280 0.1899 0.0110
298.20 0.8250 0.1521 0.2528 0.0175
298.20 0.7591 0.1992 0.3208 0.0480
298.20 0.6177 0.2887 0.3410 0.0750
298.20 0.5095 0.3405 0.3510 0.0936
308.20 0.9979 0.0000 0.0000 0.0278
308.20 0.9726 0.0250 0.1026 0.0580
308.20 0.9476 0.0495 0.2003 0.1106
308.20 0.9193 0.0778 0.2648 0.1591
308.20 0.8450 0.1521 0.3127 0.2187
308.20 0.7880 0.2060 0.3380 0.2640
308.20 0.7019 0.2710 0.3614 0.3318
313.20 0.9962 0.0000 0.0000 0.0338
313.20 0.9280 0.0677 0.0472 0.0464
313.20 0.8841 0.1075 0.1097 0.0708
313.20 0.8401 0.1450 0.1440 0.0880
313.20 0.7901 0.1872 0.2065 0.1252
313.20 0.7324 0.2288 0.2381 0.1465
313.20 0.6307 0.2987 0.2802 0.1790

Mole fraction [ref]

Operational conditions:

Fixed Measured
Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of 1-Propanol (1) - Liquid mixture 2 Mole fraction of 1-Propanol (1) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 1
0.9980 0.0000 0.0000 0.0289
0.9922 0.0078 0.0376 0.0359
0.9836 0.0142 0.0500 0.0571
0.9771 0.0212 0.0937 0.0691
0.9728 0.0252 0.1411 0.0827
0.9669 0.0313 0.2085 0.1072
0.9630 0.0351 0.2741 0.1685
0.9547 0.0439 0.3645 0.2928
0.9456 0.0527 0.4038 0.3716
0.9422 0.0564 0.3997 0.4368

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 (2) - Liquid Mole fraction of Water (3) - Gas Mole fraction of Diisopropyl ether (2) - Gas
349.36 0.5189 0.0472 0.3651 0.3560
351.06 0.4848 0.0523 0.3703 0.3157
351.51 0.4699 0.0422 0.3763 0.3015
353.12 0.4505 0.0448 0.3952 0.2650
353.30 0.4311 0.0389 0.3780 0.2690
354.22 0.4224 0.0287 0.4018 0.2209
354.36 0.4037 0.0340 0.4020 0.2199
355.17 0.3889 0.0272 0.4206 0.2003
355.58 0.3724 0.0317 0.4211 0.2440
356.16 0.3480 0.0252 0.4122 0.1685
357.43 0.3235 0.0256 0.3980 0.1555
357.60 0.2995 0.0222 0.3865 0.1417
358.33 0.2843 0.0226 0.3898 0.1287
359.47 0.2530 0.0165 0.3844 0.1036
360.78 0.2335 0.0130 0.3762 0.0841
361.13 0.2216 0.0135 0.3719 0.0688
361.51 0.2131 0.0143 0.3807 0.0664

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 (2) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of Diisopropyl ether (2) - Liquid mixture 2 Mole fraction of Diisopropyl ether (2) - Gas Mole fraction of Water (3) - Gas
335.31 0.0476 0.9524 0.9991 0.0009 0.7814 0.2186
335.71 0.0665 0.8649 0.9900 0.0009 0.7942 0.2042
335.89 0.0686 0.8380 0.9861 0.0010 0.7386 0.2214
336.97 0.1254 0.6704 0.9778 0.0011 0.6929 0.2341
337.34 0.1584 0.6048 0.9794 0.0008 0.6882 0.2339
337.60 0.1634 0.5912 0.9764 0.0009 0.6635 0.2399
337.90 0.1945 0.5083 0.9716 0.0014 0.6713 0.2375
338.30 0.2179 0.4859 0.9716 0.0011 0.6705 0.2362
340.63 0.3951 0.2465 0.9606 0.0013 0.6169 0.2584
340.90 0.3798 0.2603 0.9596 0.0015 0.6004 0.2783
341.05 0.3774 0.2609 0.9611 0.0016 0.6050 0.2583
341.65 0.4242 0.1920 0.9560 0.0015 0.6027 0.2629
342.42 0.4721 0.1640 0.9542 0.0021 0.5980 0.2731
342.62 0.4802 0.1510 0.9500 0.0017 0.5787 0.2860
343.03 0.5192 0.1163 0.9386 0.0022 0.5753 0.2925
343.82 0.5537 0.1009 0.9355 0.0026 0.5861 0.2722
344.25 0.5746 0.0810 0.9306 0.0059 0.5662 0.2958
345.76 0.6451 0.0588 0.8534 0.0151 0.4997 0.3111

Mole fraction [ref]

Operational conditions:

Fixed Measured
Mole fraction of Diisopropyl ether (2) - Liquid mixture 1 Mole fraction of 1-Propanol (1) - Liquid mixture 1 Mole fraction of Diisopropyl ether (2) - Liquid mixture 2 Mole fraction of 1-Propanol (1) - Liquid mixture 2
0.7998 0.1234 0.0018 0.0180
0.6029 0.2514 0.0019 0.0291
0.4651 0.3182 0.0020 0.0350
0.3509 0.3617 0.0021 0.0400
0.2598 0.3849 0.0021 0.0442
0.2069 0.3923 0.0021 0.0478
0.1396 0.3801 0.0024 0.0554
0.1004 0.3544 0.0029 0.0638

Temperature, K x Mole fraction x Mass fraction [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mole fraction of Water (3) - Liquid mixture 1 Mass fraction of 1-Propanol (1) - Liquid mixture 1 Mole fraction of 1-Propanol (1) - Liquid mixture 2 Mole fraction of Water (3) - Liquid mixture 2
298.20 0.9984 0.0000 0.0000 0.0016
298.20 0.9288 0.0640 0.0889 0.0050
298.20 0.8550 0.1280 0.1899 0.0110
298.20 0.8250 0.1521 0.2528 0.0175
298.20 0.7591 0.1992 0.3208 0.0480
298.20 0.6177 0.2887 0.3410 0.0750
298.20 0.5095 0.3405 0.3510 0.0936
308.20 0.9979 0.0000 0.0000 0.0278
308.20 0.9726 0.0250 0.1026 0.0580
308.20 0.9476 0.0495 0.2003 0.1106
308.20 0.9193 0.0778 0.2648 0.1591
308.20 0.8450 0.1521 0.3127 0.2187
308.20 0.7880 0.2060 0.3380 0.2640
308.20 0.7019 0.2710 0.3614 0.3318
313.20 0.9962 0.0000 0.0000 0.0338
313.20 0.9280 0.0677 0.0472 0.0464
313.20 0.8841 0.1075 0.1097 0.0708
313.20 0.8401 0.1450 0.1440 0.0880
313.20 0.7901 0.1872 0.2065 0.1252
313.20 0.7324 0.2288 0.2381 0.1465
313.20 0.6307 0.2987 0.2802 0.1790

Mole fraction [ref]

Operational conditions:

Fixed Measured
Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of 1-Propanol (1) - Liquid mixture 2 Mole fraction of 1-Propanol (1) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 1
0.9980 0.0000 0.0000 0.0289
0.9922 0.0078 0.0376 0.0359
0.9836 0.0142 0.0500 0.0571
0.9771 0.0212 0.0937 0.0691
0.9728 0.0252 0.1411 0.0827
0.9669 0.0313 0.2085 0.1072
0.9630 0.0351 0.2741 0.1685
0.9547 0.0439 0.3645 0.2928
0.9456 0.0527 0.4038 0.3716
0.9422 0.0564 0.3997 0.4368

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 (2) - Liquid Mole fraction of Water (3) - Gas Mole fraction of Diisopropyl ether (2) - Gas
349.36 0.5189 0.0472 0.3651 0.3560
351.06 0.4848 0.0523 0.3703 0.3157
351.51 0.4699 0.0422 0.3763 0.3015
353.12 0.4505 0.0448 0.3952 0.2650
353.30 0.4311 0.0389 0.3780 0.2690
354.22 0.4224 0.0287 0.4018 0.2209
354.36 0.4037 0.0340 0.4020 0.2199
355.17 0.3889 0.0272 0.4206 0.2003
355.58 0.3724 0.0317 0.4211 0.2440
356.16 0.3480 0.0252 0.4122 0.1685
357.43 0.3235 0.0256 0.3980 0.1555
357.60 0.2995 0.0222 0.3865 0.1417
358.33 0.2843 0.0226 0.3898 0.1287
359.47 0.2530 0.0165 0.3844 0.1036
360.78 0.2335 0.0130 0.3762 0.0841
361.13 0.2216 0.0135 0.3719 0.0688
361.51 0.2131 0.0143 0.3807 0.0664

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 (2) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of Diisopropyl ether (2) - Liquid mixture 2 Mole fraction of Diisopropyl ether (2) - Gas Mole fraction of Water (3) - Gas
335.31 0.0476 0.9524 0.9991 0.0009 0.7814 0.2186
335.71 0.0665 0.8649 0.9900 0.0009 0.7942 0.2042
335.89 0.0686 0.8380 0.9861 0.0010 0.7386 0.2214
336.97 0.1254 0.6704 0.9778 0.0011 0.6929 0.2341
337.34 0.1584 0.6048 0.9794 0.0008 0.6882 0.2339
337.60 0.1634 0.5912 0.9764 0.0009 0.6635 0.2399
337.90 0.1945 0.5083 0.9716 0.0014 0.6713 0.2375
338.30 0.2179 0.4859 0.9716 0.0011 0.6705 0.2362
340.63 0.3951 0.2465 0.9606 0.0013 0.6169 0.2584
340.90 0.3798 0.2603 0.9596 0.0015 0.6004 0.2783
341.05 0.3774 0.2609 0.9611 0.0016 0.6050 0.2583
341.65 0.4242 0.1920 0.9560 0.0015 0.6027 0.2629
342.42 0.4721 0.1640 0.9542 0.0021 0.5980 0.2731
342.62 0.4802 0.1510 0.9500 0.0017 0.5787 0.2860
343.03 0.5192 0.1163 0.9386 0.0022 0.5753 0.2925
343.82 0.5537 0.1009 0.9355 0.0026 0.5861 0.2722
344.25 0.5746 0.0810 0.9306 0.0059 0.5662 0.2958
345.76 0.6451 0.0588 0.8534 0.0151 0.4997 0.3111

Sources