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
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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