Dortmund Data Bank

Excess Volume Data

The experimental data shown in these pages are freely available and have been published already in the DDB Explorer Edition. The data represent a small sub list of all available data in the Dortmund Data Bank. For more data or any further information please search the DDB or contact DDBST.


Excess Volume Data Set 5016

Components

No. Formula Molar Mass CAS Registry Number Name
1 C3H6O 58.080 67-64-1 Acetone
2 CH4O 32.042 67-56-1 Methanol
3 C2H6O 46.069 64-17-5 Ethanol
Search the DDB for all data of this mixture

Constant Value

Temperature 298.150 K

Data Table

Excess Volume [cm3/mol] x1 [mol/mol] x2 [mol/mol]
-0.21036 0.14636 0.65890
-0.17027 0.14797 0.50071
-0.1363 0.17481 0.26773
-0.22177 0.23198 0.46700
-0.23706 0.28360 0.42599
-0.19678 0.31075 0.31130
-0.2862 0.56037 0.25439
-0.2168 0.19767 0.53664
-0.18824 0.21160 0.40920
-0.18815 0.05544 0.81046
-0.1023 0.08222 0.18407
-0.36446 0.67274 0.18450

Reference

Source
Wei I.-C.; Rowley R.L.: Ternary Liquid Mixture Viscosities and Densities. J.Chem.Eng.Data 29 (1984) 336-340


Excess Volume Data Set 16443

Components

No. Formula Molar Mass CAS Registry Number Name
1 C3H6O 58.080 67-64-1 Acetone
2 CH4O 32.042 67-56-1 Methanol
3 C2H6O 46.069 64-17-5 Ethanol
Search the DDB for all data of this mixture

Constant Value

Temperature 298.150 K
Pressure 1.0132 bar

Data Table

Excess Volume [cm3/mol] x1 [mol/mol] x2 [mol/mol]
-0.0390 0.03120 0.08540
-0.0450 0.03190 0.23710
-0.0290 0.02280 0.38710
-0.0280 0.02410 0.51520
-0.0330 0.02300 0.63710
-0.0260 0.02200 0.74770
-0.0310 0.02300 0.85200
-0.0300 0.02110 0.94600
-0.0580 0.09060 0.08450
-0.0790 0.10690 0.23730
-0.0890 0.09840 0.38480
-0.0920 0.09410 0.51620
-0.1000 0.08980 0.63890
-0.1080 0.08540 0.75230
-0.1100 0.08200 0.85140
-0.0790 0.17110 0.08540
-0.1120 0.16440 0.24000
-0.1190 0.14820 0.39710
-0.1350 0.14640 0.52700
-0.1530 0.14010 0.65330
-0.1580 0.13230 0.76740
-0.1820 0.14490 0.81150
-0.1530 0.21320 0.39780
-0.1800 0.20420 0.53150
-0.2020 0.19420 0.66470
-0.2170 0.18450 0.77850
-0.1050 0.31190 0.09010
-0.1520 0.29050 0.25230
-0.1940 0.27920 0.40620
-0.2260 0.26730 0.54290
-0.2480 0.25520 0.66860
-0.2960 0.32720 0.63970
-0.2480 0.33860 0.50580
-0.2050 0.36310 0.35010
-0.1110 0.39160 0.08670
-0.1750 0.37160 0.25520
-0.1100 0.47100 0.08270
-0.1880 0.43880 0.26630
-0.2530 0.42450 0.41370
-0.3100 0.40480 0.55920
-0.1080 0.54890 0.08270
-0.2050 0.52180 0.26120
-0.2820 0.48810 0.42160
-0.1120 0.62830 0.09830
-0.2190 0.59190 0.26620
-0.2800 0.57640 0.37010
-0.1100 0.70890 0.09560
-0.2350 0.67950 0.27560
-0.0910 0.80350 0.08640
-0.0620 0.11130 0.05480
-0.0860 0.24220 0.06300
-0.0330 0.03340 0.14800
-0.0780 0.13370 0.13780
-0.1150 0.26510 0.16420
-0.1420 0.40710 0.17160
-0.1560 0.48400 0.18050
-0.1710 0.64560 0.18110
-0.0320 0.03350 0.23350
-0.0310 0.03370 0.30930
-0.0960 0.13620 0.29480
-0.1610 0.26120 0.32850
-0.2390 0.47060 0.35320

Reference

Source
Iglesias M.; Orge B.; Pineiro M.M.; de Cominges B.E.; Marino G.; Tojo J.: Thermodynamic Properties of the Ternary Mixture Acetone + Methanol + Ethanol at 298.15 K. J.Chem.Eng.Data 43 (1998) 776-780

List of All References

Source
Wei I.-C.; Rowley R.L.: Ternary Liquid Mixture Viscosities and Densities. J.Chem.Eng.Data 29 (1984) 336-340
Iglesias M.; Orge B.; Pineiro M.M.; de Cominges B.E.; Marino G.; Tojo J.: Thermodynamic Properties of the Ternary Mixture Acetone + Methanol + Ethanol at 298.15 K. J.Chem.Eng.Data 43 (1998) 776-780

Excess Volume Data Overview


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