Mixture of Diisopropyl ether + Acetone + Cyclohexane

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

Acetone

Name
Acetone
InChI
InChI=1S/C3H6O/c1-3(2)4/h1-2H3
InChI Key
CSCPPACGZOOCGX-UHFFFAOYSA-N
Formula
C3H6O
SMILES
CC(C)=O
Mol. Weight (g/mol)
58.08
CAS
67-64-1

Cyclohexane

Name
Cyclohexane
InChI
InChI=1S/C6H12/c1-2-4-6-5-3-1/h1-6H2
InChI Key
XDTMQSROBMDMFD-UHFFFAOYSA-N
Formula
C6H12
SMILES
C1CCCCC1
Mol. Weight (g/mol)
84.16
CAS
110-82-7
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Datasets

  1. Temperature, K x Mole fraction (2)
  2. γ - Surface tension liquid-gas, N/m (2)

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 94 (Gas)

Fixed Measured
Temperature, K - Gas Mole fraction of Acetone (2) - Liquid Mole fraction of Diisopropyl ether (1) - Liquid Mole fraction of Diisopropyl ether (1) - Gas Mole fraction of Acetone (2) - Gas
341.89 0.0350 0.0930 0.1130 0.2340
339.68 0.0420 0.2840 0.3030 0.2090
338.41 0.0430 0.4810 0.4840 0.1740
336.33 0.0430 0.8920 0.8260 0.1270
337.02 0.0440 0.6850 0.6510 0.1540
335.32 0.0760 0.4280 0.3890 0.2820
335.50 0.0770 0.3280 0.3030 0.3070
334.93 0.0770 0.6140 0.5480 0.2410
335.18 0.0770 0.5210 0.4690 0.2590
335.46 0.0800 0.2240 0.2100 0.3450
334.42 0.0810 0.7040 0.6160 0.2360
334.00 0.0840 0.8020 0.6950 0.2270
335.05 0.0850 0.1170 0.1110 0.3940
329.86 0.1790 0.1170 0.0890 0.5260
329.93 0.1830 0.2110 0.1590 0.4970
330.11 0.1850 0.3030 0.2290 0.4710
330.16 0.1860 0.3990 0.3020 0.4500
330.27 0.1900 0.4970 0.3770 0.4280
330.33 0.1930 0.5980 0.4580 0.4080
330.34 0.1960 0.6960 0.5360 0.3930
327.84 0.2840 0.2150 0.1500 0.5620
328.43 0.2850 0.6080 0.4520 0.4780
328.04 0.2870 0.3170 0.2240 0.5390
328.21 0.2870 0.4150 0.2990 0.5150
328.30 0.2870 0.5130 0.3740 0.4960
327.46 0.2910 0.1110 0.0770 0.5970
327.01 0.3840 0.5030 0.3690 0.5510
326.61 0.3900 0.3000 0.2110 0.5900
326.16 0.3910 0.1090 0.0750 0.6340
326.34 0.3930 0.2020 0.1390 0.6120
326.72 0.3960 0.3920 0.2830 0.5750
326.00 0.4830 0.4070 0.3080 0.6090
325.76 0.4830 0.3090 0.2280 0.6220
325.36 0.4870 0.1080 0.0770 0.6600
325.48 0.4870 0.2100 0.1510 0.6410
324.80 0.5910 0.1060 0.0810 0.6890
325.02 0.5930 0.2040 0.1590 0.6770
325.27 0.5950 0.3020 0.2450 0.6660
324.90 0.6930 0.2030 0.1800 0.7180
324.60 0.6950 0.1070 0.0920 0.7250
324.76 0.7990 0.1040 0.1050 0.7780
324.99 0.8000 0.1500 0.1570 0.7810
324.76 0.8280 0.0750 0.0800 0.7970

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 94 (Gas)

Fixed Measured
Temperature, K - Gas Mole fraction of Acetone (2) - Liquid Mole fraction of Diisopropyl ether (1) - Liquid Mole fraction of Diisopropyl ether (1) - Gas Mole fraction of Acetone (2) - Gas
341.89 0.0350 0.0930 0.1130 0.2340
339.68 0.0420 0.2840 0.3030 0.2090
338.41 0.0430 0.4810 0.4840 0.1740
336.33 0.0430 0.8920 0.8260 0.1270
337.02 0.0440 0.6850 0.6510 0.1540
335.32 0.0760 0.4280 0.3890 0.2820
335.50 0.0770 0.3280 0.3030 0.3070
334.93 0.0770 0.6140 0.5480 0.2410
335.18 0.0770 0.5210 0.4690 0.2590
335.46 0.0800 0.2240 0.2100 0.3450
334.42 0.0810 0.7040 0.6160 0.2360
334.00 0.0840 0.8020 0.6950 0.2270
335.05 0.0850 0.1170 0.1110 0.3940
329.86 0.1790 0.1170 0.0890 0.5260
329.93 0.1830 0.2110 0.1590 0.4970
330.11 0.1850 0.3030 0.2290 0.4710
330.16 0.1860 0.3990 0.3020 0.4500
330.27 0.1900 0.4970 0.3770 0.4280
330.33 0.1930 0.5980 0.4580 0.4080
330.34 0.1960 0.6960 0.5360 0.3930
327.84 0.2840 0.2150 0.1500 0.5620
328.43 0.2850 0.6080 0.4520 0.4780
328.04 0.2870 0.3170 0.2240 0.5390
328.21 0.2870 0.4150 0.2990 0.5150
328.30 0.2870 0.5130 0.3740 0.4960
327.46 0.2910 0.1110 0.0770 0.5970
327.01 0.3840 0.5030 0.3690 0.5510
326.61 0.3900 0.3000 0.2110 0.5900
326.16 0.3910 0.1090 0.0750 0.6340
326.34 0.3930 0.2020 0.1390 0.6120
326.72 0.3960 0.3920 0.2830 0.5750
326.00 0.4830 0.4070 0.3080 0.6090
325.76 0.4830 0.3090 0.2280 0.6220
325.36 0.4870 0.1080 0.0770 0.6600
325.48 0.4870 0.2100 0.1510 0.6410
324.80 0.5910 0.1060 0.0810 0.6890
325.02 0.5930 0.2040 0.1590 0.6770
325.27 0.5950 0.3020 0.2450 0.6660
324.90 0.6930 0.2030 0.1800 0.7180
324.60 0.6950 0.1070 0.0920 0.7250
324.76 0.7990 0.1040 0.1050 0.7780
324.99 0.8000 0.1500 0.1570 0.7810
324.76 0.8280 0.0750 0.0800 0.7970

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 303.15 (Liquid)

Fixed Measured
Mole fraction of Acetone (2) - Liquid Mole fraction of Diisopropyl ether (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.0830 0.3000 0.0203
0.0840 0.3990 0.0196
0.0850 0.1930 0.0212
0.0860 0.5030 0.0190
0.0880 0.6050 0.0184
0.0900 0.0810 0.0223
0.0910 0.7060 0.0179
0.0960 0.8030 0.0174
0.1630 0.4540 0.0192
0.1730 0.5690 0.0185
0.1780 0.6770 0.0179
0.1810 0.3250 0.0200
0.1890 0.2040 0.0208
0.1890 0.7630 0.0175
0.1950 0.0830 0.0218
0.2920 0.1240 0.0212
0.2930 0.0340 0.0220
0.2950 0.2330 0.0204
0.3020 0.3550 0.0195
0.3070 0.4900 0.0187
0.3190 0.6240 0.0179
0.3560 0.3010 0.0197
0.3650 0.3150 0.0196
0.3670 0.2840 0.0198
0.3740 0.1310 0.0209
0.3760 0.4320 0.0189
0.4010 0.5780 0.0179
0.4100 0.3830 0.0191
0.4960 0.3010 0.0194
0.5010 0.4070 0.0186
0.5020 0.1000 0.0209
0.5040 0.1960 0.0202
0.5400 0.2150 0.0199
0.5750 0.3780 0.0187
0.6010 0.1010 0.0208
0.6020 0.2040 0.0199
0.6030 0.3070 0.0192
0.6230 0.2100 0.0199
0.7060 0.0930 0.0208
0.7100 0.1970 0.0199
0.7950 0.1280 0.0205
0.8100 0.0960 0.0208
0.8250 0.0780 0.0210

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 303.15 (Liquid)

Fixed Measured
Mole fraction of Acetone (2) - Liquid Mole fraction of Diisopropyl ether (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.0830 0.3000 0.0203
0.0840 0.3990 0.0196
0.0850 0.1930 0.0212
0.0860 0.5030 0.0190
0.0880 0.6050 0.0184
0.0900 0.0810 0.0223
0.0910 0.7060 0.0179
0.0960 0.8030 0.0174
0.1630 0.4540 0.0192
0.1730 0.5690 0.0185
0.1780 0.6770 0.0179
0.1810 0.3250 0.0200
0.1890 0.2040 0.0208
0.1890 0.7630 0.0175
0.1950 0.0830 0.0218
0.2920 0.1240 0.0212
0.2930 0.0340 0.0220
0.2950 0.2330 0.0204
0.3020 0.3550 0.0195
0.3070 0.4900 0.0187
0.3190 0.6240 0.0179
0.3560 0.3010 0.0197
0.3650 0.3150 0.0196
0.3670 0.2840 0.0198
0.3740 0.1310 0.0209
0.3760 0.4320 0.0189
0.4010 0.5780 0.0179
0.4100 0.3830 0.0191
0.4960 0.3010 0.0194
0.5010 0.4070 0.0186
0.5020 0.1000 0.0209
0.5040 0.1960 0.0202
0.5400 0.2150 0.0199
0.5750 0.3780 0.0187
0.6010 0.1010 0.0208
0.6020 0.2040 0.0199
0.6030 0.3070 0.0192
0.6230 0.2100 0.0199
0.7060 0.0930 0.0208
0.7100 0.1970 0.0199
0.7950 0.1280 0.0205
0.8100 0.0960 0.0208
0.8250 0.0780 0.0210

Sources