Dortmund Data Bank
Density 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.
Density Data Set 31706
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
2 |
H2O |
18.015 |
7732-18-5 |
Water |
3 |
CH4O |
32.042 |
67-56-1 |
Methanol |
Search the DDB for all data of this mixture
Constant Value
Temperature |
298.150 |
K |
Pressure |
1.0132 |
bar |
Data Table
Density [g/cm3] |
x1 [mol/mol] |
x2 [mol/mol] |
0.9971 |
0.00000 |
1.00000 |
0.9900 |
0.00423846999183 |
0.97012 |
0.9900 |
0.008611 |
0.96653 |
0.9800 |
0.004359 |
0.93271 |
0.9800 |
0.00886 |
0.92840 |
0.9800 |
0.01349 |
0.92592 |
0.9800 |
0.018263 |
0.92336 |
0.9700 |
0.004487 |
0.89311 |
0.9700 |
0.00912 |
0.88869 |
0.9700 |
0.01390 |
0.88482 |
0.9700 |
0.018825 |
0.88153 |
0.9700 |
0.02392 |
0.87742 |
0.9600 |
0.004625 |
0.85041 |
0.9600 |
0.014318 |
0.84264 |
0.9600 |
0.024627 |
0.83588 |
0.9600 |
0.03003 |
0.83233 |
0.9500 |
0.004771 |
0.80501 |
0.9500 |
0.01478 |
0.79626 |
0.9500 |
0.02539 |
0.79100 |
0.9500 |
0.036635 |
0.78708 |
0.9500 |
0.04856 |
0.78378 |
0.9400 |
0.01258 |
0.75428 |
0.9400 |
0.026143 |
0.74670 |
0.9400 |
0.04076 |
0.74029 |
0.9400 |
0.05652 |
0.73524 |
0.9400 |
0.07349 |
0.73173 |
0.9300 |
0.01295 |
0.70932 |
0.9300 |
0.02691 |
0.70151 |
0.9300 |
0.041985 |
0.69403 |
0.9300 |
0.05824 |
0.68792 |
0.9300 |
0.07587 |
0.68129 |
0.9300 |
0.09499 |
0.67516 |
0.9300 |
0.11583 |
0.66849 |
0.9300 |
0.13855 |
0.66238 |
0.9200 |
0.01332 |
0.66440 |
0.9200 |
0.02771 |
0.65456 |
0.9200 |
0.05996 |
0.64078 |
0.9200 |
0.09811 |
0.62221 |
0.9200 |
0.14345 |
0.60510 |
0.9200 |
0.19847 |
0.58433 |
0.9100 |
0.013702 |
0.61783 |
0.9100 |
0.028505 |
0.60782 |
0.9100 |
0.06187 |
0.58853 |
0.9100 |
0.09473 |
0.67952 |
0.9100 |
0.14858 |
0.54500 |
0.9100 |
0.20600 |
0.51985 |
0.9100 |
0.27693 |
0.49209 |
0.9100 |
0.31920 |
0.47554 |
0.9000 |
0.01409 |
0.57058 |
0.9000 |
0.02931 |
0.56047 |
0.9000 |
0.06368 |
0.53882 |
0.9000 |
0.10448 |
0.51438 |
0.9000 |
0.15372 |
0.48490 |
0.9000 |
0.21373 |
0.45365 |
0.9000 |
0.28892 |
0.41449 |
0.9000 |
0.38544 |
0.36625 |
0.9000 |
0.51360 |
0.30457 |
0.9000 |
0.59463 |
0.26687 |
0.8900 |
0.014492 |
0.52166 |
0.8900 |
0.03016 |
0.51038 |
0.8900 |
0.06565 |
0.48484 |
0.8900 |
0.10794 |
0.45576 |
0.8900 |
0.15895 |
0.42366 |
0.8900 |
0.22206 |
0.38228 |
0.8900 |
0.30135 |
0.33406 |
0.8900 |
0.40352 |
0.27629 |
0.8900 |
0.54112 |
0.19849 |
0.8900 |
0.73517 |
0.09188 |
0.8800 |
0.01486 |
0.47679 |
0.8800 |
0.03094 |
0.46455 |
0.8800 |
0.06741 |
0.43680 |
0.8800 |
0.11102 |
0.40360 |
0.8800 |
0.16397 |
0.36487 |
0.8800 |
0.22948 |
0.31873 |
0.8800 |
0.31243 |
0.26231 |
0.8800 |
0.42120 |
0.18834 |
0.8800 |
0.56742 |
0.09713 |
0.8700 |
0.01526 |
0.42837 |
0.8700 |
0.031804 |
0.41375 |
0.8700 |
0.06946 |
0.38047 |
0.8700 |
0.11456 |
0.34363 |
0.8700 |
0.16947 |
0.30045 |
0.8700 |
0.23789 |
0.24665 |
0.8700 |
0.32512 |
0.18021 |
0.8700 |
0.44049 |
0.09233 |
0.8600 |
0.015658 |
0.37984 |
0.8600 |
0.032695 |
0.36137 |
0.8600 |
0.07148 |
0.32512 |
0.8600 |
0.11823 |
0.28141 |
0.8600 |
0.17536 |
0.23156 |
0.8600 |
0.24669 |
0.17132 |
0.8600 |
0.33847 |
0.09380 |
0.8500 |
0.01609 |
0.32735 |
0.8500 |
0.03359 |
0.30883 |
0.8500 |
0.07350 |
0.26962 |
0.8500 |
0.12172 |
0.22225 |
0.8500 |
0.18114 |
0.16389 |
0.8500 |
0.25616 |
0.09020 |
0.8400 |
0.016522 |
0.27474 |
0.8400 |
0.034506 |
0.25483 |
0.8400 |
0.07577 |
0.20752 |
0.8400 |
0.12565 |
0.15568 |
0.8400 |
0.18731 |
0.09161 |
0.8400 |
0.26517 |
0.01297 |
0.8300 |
0.016954 |
0.22222 |
0.8300 |
0.03545 |
0.19938 |
0.8300 |
0.07792 |
0.14862 |
0.8300 |
0.12949 |
0.09077 |
0.8300 |
0.19352 |
0.01893 |
0.8200 |
0.017422 |
0.16530 |
0.8200 |
0.036445 |
0.14081 |
0.8200 |
0.08026 |
0.08440 |
0.8200 |
0.13369 |
0.019615 |
0.8100 |
0.01789 |
0.10849 |
0.8100 |
0.03747 |
0.08063 |
0.8100 |
0.05899 |
0.05000 |
0.8100 |
0.08260 |
0.02020 |
0.8000 |
0.018368 |
0.05031 |
0.8000 |
0.03852 |
0.01884 |
0.7870 |
0.00000 |
0.00000 |
0.8945 |
1.00000 |
0.00000 |
Reference
Source |
Akita K.; Yoshida F.: Phase-Equilibria in Methanol-Ethyl Acetate-Water System. J.Chem.Eng.Data 8 (1963) 484-490 |
List of All References
Source |
Akita K.; Yoshida F.: Phase-Equilibria in Methanol-Ethyl Acetate-Water System. J.Chem.Eng.Data 8 (1963) 484-490 |
Density Data Overview
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