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 4166
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 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| Excess Volume [cm3/mol] |
x1 [mol/mol] |
x2 [mol/mol] |
| -1.2365 |
0.14630 |
0.21110 |
| -1.3616 |
0.49400 |
0.07290 |
| -1.4048 |
0.28010 |
0.07610 |
| -1.3628 |
0.24330 |
0.09030 |
| -0.8674 |
0.07340 |
0.12820 |
| -1.3825 |
0.25010 |
0.15490 |
| -1.3322 |
0.43310 |
0.15790 |
| -1.3732 |
0.24430 |
0.16430 |
| -1.0493 |
0.09780 |
0.16870 |
| -1.4079 |
0.29980 |
0.17120 |
| -1.3838 |
0.26950 |
0.19160 |
| -1.2332 |
0.35410 |
0.29650 |
| -1.0438 |
0.05740 |
0.28300 |
| -1.0323 |
0.41610 |
0.33210 |
| -1.2333 |
0.28800 |
0.33850 |
| -1.2565 |
0.18370 |
0.35870 |
| -0.9033 |
0.45000 |
0.35270 |
| -1.1596 |
0.09390 |
0.41180 |
| -0.9064 |
0.30690 |
0.48390 |
| -1.1317 |
0.24430 |
0.44770 |
| -0.8395 |
0.32550 |
0.49660 |
| -1.0370 |
0.10620 |
0.55600 |
| -0.9653 |
0.10610 |
0.59340 |
| -0.6499 |
0.22000 |
0.64780 |
| -0.6697 |
0.18290 |
0.67430 |
| -1.4140 |
0.27090 |
0.09810 |
| -1.3990 |
0.34480 |
0.17220 |
| -1.2584 |
0.17010 |
0.16160 |
Reference
| Source |
| Noda K.; Ohashi M.; Ishida K.: Viscosities and Densities at 298.15 K for Mixtures of Methanol, Acetone, and Water. J.Chem.Eng.Data 27 (1982) 326-328 |
Excess Volume Data Set 9777
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 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| Excess Volume [cm3/mol] |
x1 [mol/mol] |
x2 [mol/mol] |
| -0.3080 |
0.01270 |
0.06690 |
| -0.5340 |
0.01390 |
0.13480 |
| -1.0070 |
0.01730 |
0.37020 |
| -1.0360 |
0.01860 |
0.47920 |
| -0.9670 |
0.02120 |
0.61400 |
| -0.4340 |
0.04760 |
0.02340 |
| -0.9870 |
0.05840 |
0.22570 |
| -1.1050 |
0.06360 |
0.31340 |
| -1.1430 |
0.06910 |
0.41450 |
| -1.0660 |
0.07740 |
0.54540 |
| -1.1580 |
0.10000 |
0.25100 |
| -1.2150 |
0.11150 |
0.35650 |
| -1.1350 |
0.12110 |
0.47820 |
| -0.8830 |
0.13780 |
0.63160 |
| -1.2430 |
0.14470 |
0.19070 |
| -1.2910 |
0.15750 |
0.28740 |
| -1.2250 |
0.17490 |
0.40850 |
| -0.9350 |
0.19960 |
0.57000 |
| -1.2850 |
0.19220 |
0.10500 |
| -1.3510 |
0.20990 |
0.21270 |
| -1.2970 |
0.23430 |
0.33380 |
| -1.0240 |
0.26340 |
0.48050 |
| -1.4140 |
0.26840 |
0.12230 |
| -1.3660 |
0.29610 |
0.24850 |
| -1.0870 |
0.34110 |
0.38880 |
| -1.1310 |
0.42250 |
0.29290 |
| -1.4450 |
0.45020 |
0.05820 |
| -1.1480 |
0.51590 |
0.18970 |
| -0.7470 |
0.75660 |
0.06050 |
| -0.6730 |
0.76930 |
0.07400 |
| -1.3190 |
0.48760 |
0.11270 |
| -0.7920 |
0.63340 |
0.19780 |
| -0.8170 |
0.50650 |
0.33200 |
| -0.7880 |
0.41030 |
0.44060 |
| -0.7390 |
0.32830 |
0.53620 |
| -0.6770 |
0.25050 |
0.62260 |
| -0.6510 |
0.17550 |
0.69200 |
| -0.5630 |
0.11300 |
0.76680 |
| -0.4670 |
0.05760 |
0.83210 |
| -0.6090 |
0.73810 |
0.14420 |
| -1.2840 |
0.40120 |
0.22390 |
| -1.1870 |
0.25400 |
0.40620 |
| -1.1010 |
0.18980 |
0.48500 |
| -1.0360 |
0.12900 |
0.55640 |
| -0.9470 |
0.08130 |
0.62130 |
| -0.5090 |
0.67390 |
0.25480 |
| -0.7930 |
0.68440 |
0.13850 |
| -0.9440 |
0.63710 |
0.13570 |
| -0.6080 |
0.50600 |
0.40850 |
| -0.9770 |
0.52210 |
0.25370 |
| -0.5330 |
0.27280 |
0.65420 |
| -0.4620 |
0.16930 |
0.76050 |
| -0.5760 |
0.59660 |
0.32260 |
| -0.8690 |
0.57020 |
0.24080 |
| -0.5260 |
0.43210 |
0.51220 |
| -1.1890 |
0.33190 |
0.34650 |
| -1.4470 |
0.31780 |
0.10770 |
| -1.1600 |
0.12110 |
0.18510 |
| -0.9350 |
0.05960 |
0.62780 |
| -0.8630 |
0.05630 |
0.67170 |
| -0.7300 |
0.04620 |
0.73770 |
| -1.0300 |
0.09310 |
0.16740 |
| -1.2300 |
0.17630 |
0.10280 |
| -1.2020 |
0.18500 |
0.05640 |
| -1.3330 |
0.20180 |
0.16300 |
| -1.4410 |
0.36710 |
0.10520 |
| -1.4670 |
0.35400 |
0.06160 |
| -1.3740 |
0.24870 |
0.07460 |
| -1.4070 |
0.28380 |
0.19460 |
| -1.3550 |
0.36690 |
0.20810 |
| -1.2530 |
0.42560 |
0.22670 |
| -1.1930 |
0.53370 |
0.13970 |
| -1.0960 |
0.62720 |
0.07380 |
| -0.5120 |
0.76500 |
0.14100 |
| -0.6970 |
0.28720 |
0.58550 |
| -0.7690 |
0.37310 |
0.48320 |
| -1.1230 |
0.35670 |
0.35930 |
| -0.8080 |
0.44360 |
0.40520 |
| -1.0830 |
0.41180 |
0.32170 |
Reference
| Source |
| Iglesias M.; Orge B.; Tojo J.: Refractive indices, densities and excess properties on mixing of the systems acetone + methanol + water and acetone + methanol + 1-butanol at 298.15 K. Fluid Phase Equilib. 126 (1996) 203-223 |
List of All References
| Source |
| Noda K.; Ohashi M.; Ishida K.: Viscosities and Densities at 298.15 K for Mixtures of Methanol, Acetone, and Water. J.Chem.Eng.Data 27 (1982) 326-328 |
| Iglesias M.; Orge B.; Tojo J.: Refractive indices, densities and excess properties on mixing of the systems acetone + methanol + water and acetone + methanol + 1-butanol at 298.15 K. Fluid Phase Equilib. 126 (1996) 203-223 |
Excess Volume Data Overview
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