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 32203
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 3 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| Density [g/cm3] |
x1 [mol/mol] |
x2 [mol/mol] |
| 1.3630 |
0.02220 |
0.79640 |
| 1.3008 |
0.02900 |
0.70080 |
| 1.2380 |
0.03950 |
0.60200 |
| 1.1738 |
0.05190 |
0.49930 |
| 1.1136 |
0.05890 |
0.40130 |
| 1.0520 |
0.06950 |
0.29900 |
| 0.9932 |
0.07890 |
0.19970 |
| 0.9358 |
0.08800 |
0.10160 |
| 1.4321 |
0.02060 |
0.89950 |
| 1.3633 |
0.04010 |
0.79390 |
| 1.3031 |
0.06020 |
0.69950 |
| 1.2383 |
0.08090 |
0.59780 |
| 1.1762 |
0.10040 |
0.49930 |
| 1.1141 |
0.11970 |
0.39980 |
| 1.0518 |
0.13940 |
0.29880 |
| 0.9915 |
0.16100 |
0.20020 |
| 0.9308 |
0.17920 |
0.09980 |
| 1.4346 |
0.03910 |
0.89940 |
| 1.3733 |
0.07990 |
0.80090 |
| 1.3103 |
0.12010 |
0.70150 |
| 1.2451 |
0.16040 |
0.59880 |
| 1.1825 |
0.20060 |
0.50050 |
| 1.1182 |
0.23990 |
0.40060 |
| 1.0529 |
0.28030 |
0.29930 |
| 0.9883 |
0.32100 |
0.20040 |
| 0.9189 |
0.37990 |
0.09610 |
| 1.4357 |
0.05840 |
0.89680 |
| 1.3775 |
0.12160 |
0.79920 |
| 1.3152 |
0.17940 |
0.69880 |
| 1.2529 |
0.23980 |
0.59980 |
| 1.1887 |
0.29960 |
0.50030 |
| 1.1224 |
0.35970 |
0.40010 |
| 1.0572 |
0.41660 |
0.30440 |
| 0.9838 |
0.47840 |
0.19900 |
| 0.9141 |
0.53870 |
0.10120 |
| 1.4406 |
0.08070 |
0.89890 |
| 1.3832 |
0.15980 |
0.80010 |
| 1.3234 |
0.23830 |
0.70070 |
| 1.2585 |
0.32010 |
0.59650 |
| 1.1961 |
0.39960 |
0.50030 |
| 1.1246 |
0.47440 |
0.39640 |
| 1.0534 |
0.56500 |
0.29650 |
| 0.9808 |
0.63930 |
0.19970 |
| 0.9060 |
0.71660 |
0.10510 |
| 1.3860 |
0.17910 |
0.80050 |
| 1.3269 |
0.27000 |
0.70010 |
| 1.2668 |
0.35700 |
0.60260 |
| 1.1996 |
0.44970 |
0.49990 |
| 1.1307 |
0.53970 |
0.40020 |
| 1.0611 |
0.62270 |
0.30530 |
| 0.9785 |
0.71800 |
0.19930 |
| 0.8957 |
0.81030 |
0.09960 |
| 0.7937 |
1.00000 |
0.00000 |
| 1.4981 |
0.00000 |
1.00000 |
| 0.8842 |
0.00000 |
0.00000 |
Reference
| Source |
| Kijevcanin M.L.; Serbanovic S.P.; Radovic I.R.; Djordjevic B.D.; Tasic A.Z.: Experimental data, correlation and prediction by cubic EOS. Fluid Phase Equilib. 251 (2007) 78-92 |
Density Data Set 32204
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 3 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| Density [g/cm3] |
x1 [mol/mol] |
x2 [mol/mol] |
| 1.3546 |
0.02220 |
0.79640 |
| 1.2928 |
0.02900 |
0.70080 |
| 1.2304 |
0.03950 |
0.60200 |
| 1.1667 |
0.05190 |
0.49930 |
| 1.1069 |
0.05890 |
0.40130 |
| 1.0457 |
0.06950 |
0.29900 |
| 0.9872 |
0.07890 |
0.19970 |
| 0.9302 |
0.08800 |
0.10160 |
| 1.4231 |
0.02060 |
0.89950 |
| 1.3549 |
0.04010 |
0.79390 |
| 1.2950 |
0.06020 |
0.69950 |
| 1.2307 |
0.08090 |
0.59780 |
| 1.1690 |
0.10040 |
0.49930 |
| 1.1074 |
0.11970 |
0.39980 |
| 1.0455 |
0.13940 |
0.29880 |
| 0.9855 |
0.16100 |
0.20020 |
| 0.9252 |
0.17920 |
0.09980 |
| 1.4256 |
0.03910 |
0.89940 |
| 1.3647 |
0.07990 |
0.80090 |
| 1.3021 |
0.12010 |
0.70150 |
| 1.2374 |
0.16040 |
0.59880 |
| 1.1753 |
0.20060 |
0.50050 |
| 1.1114 |
0.23990 |
0.40060 |
| 1.0465 |
0.28030 |
0.29930 |
| 0.9824 |
0.32100 |
0.20040 |
| 0.9134 |
0.37990 |
0.09610 |
| 1.4266 |
0.05840 |
0.89680 |
| 1.3688 |
0.12160 |
0.79920 |
| 1.3070 |
0.17940 |
0.69880 |
| 1.2451 |
0.23980 |
0.59980 |
| 1.1814 |
0.29960 |
0.50030 |
| 1.1156 |
0.35970 |
0.40010 |
| 1.0509 |
0.41660 |
0.30440 |
| 0.9780 |
0.47840 |
0.19900 |
| 0.9086 |
0.53870 |
0.10120 |
| 1.4315 |
0.08070 |
0.89890 |
| 1.3745 |
0.15980 |
0.80010 |
| 1.3152 |
0.23830 |
0.70070 |
| 1.2507 |
0.32010 |
0.59650 |
| 1.1888 |
0.39960 |
0.50030 |
| 1.1178 |
0.47440 |
0.39640 |
| 1.0471 |
0.56500 |
0.29650 |
| 0.9751 |
0.63930 |
0.19970 |
| 0.9009 |
0.71660 |
0.10510 |
| 1.3772 |
0.17910 |
0.80050 |
| 1.3186 |
0.27000 |
0.70010 |
| 1.2589 |
0.35700 |
0.60260 |
| 1.1922 |
0.44970 |
0.49990 |
| 1.1239 |
0.53970 |
0.40020 |
| 1.0549 |
0.62270 |
0.30530 |
| 0.9729 |
0.71800 |
0.19930 |
| 0.8907 |
0.81030 |
0.09960 |
| 0.7895 |
1.00000 |
0.00000 |
| 1.4886 |
0.00000 |
1.00000 |
| 0.8789 |
0.00000 |
0.00000 |
Reference
| Source |
| Kijevcanin M.L.; Serbanovic S.P.; Radovic I.R.; Djordjevic B.D.; Tasic A.Z.: Experimental data, correlation and prediction by cubic EOS. Fluid Phase Equilib. 251 (2007) 78-92 |
Density Data Set 32205
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 3 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| Density [g/cm3] |
x1 [mol/mol] |
x2 [mol/mol] |
| 1.3461 |
0.02220 |
0.79640 |
| 1.2848 |
0.02900 |
0.70080 |
| 1.2228 |
0.03950 |
0.60200 |
| 1.1595 |
0.05190 |
0.49930 |
| 1.1001 |
0.05890 |
0.40130 |
| 1.0393 |
0.06950 |
0.29900 |
| 0.9811 |
0.07890 |
0.19970 |
| 0.9245 |
0.08800 |
0.10160 |
| 1.4141 |
0.02060 |
0.89950 |
| 1.3463 |
0.04010 |
0.79390 |
| 1.2869 |
0.06020 |
0.69950 |
| 1.2230 |
0.08090 |
0.59780 |
| 1.1618 |
0.10040 |
0.49930 |
| 1.1006 |
0.11970 |
0.39980 |
| 1.0391 |
0.13940 |
0.29880 |
| 0.9795 |
0.16100 |
0.20020 |
| 0.9195 |
0.17920 |
0.09980 |
| 1.4165 |
0.03910 |
0.89940 |
| 1.3560 |
0.07990 |
0.80090 |
| 1.2939 |
0.12010 |
0.70150 |
| 1.2297 |
0.16040 |
0.59880 |
| 1.1680 |
0.20060 |
0.50050 |
| 1.1046 |
0.23990 |
0.40060 |
| 1.0401 |
0.28030 |
0.29930 |
| 0.9764 |
0.32100 |
0.20040 |
| 0.9079 |
0.37990 |
0.09610 |
| 1.4175 |
0.05840 |
0.89680 |
| 1.3601 |
0.12160 |
0.79920 |
| 1.2987 |
0.17940 |
0.69880 |
| 1.2373 |
0.23980 |
0.59980 |
| 1.1740 |
0.29960 |
0.50030 |
| 1.1087 |
0.35970 |
0.40010 |
| 1.0445 |
0.41660 |
0.30440 |
| 0.9721 |
0.47840 |
0.19900 |
| 0.9031 |
0.53870 |
0.10120 |
| 1.4223 |
0.08070 |
0.89890 |
| 1.3657 |
0.15980 |
0.80010 |
| 1.3068 |
0.23830 |
0.70070 |
| 1.2428 |
0.32010 |
0.59650 |
| 1.1814 |
0.39960 |
0.50030 |
| 1.1110 |
0.47440 |
0.39640 |
| 1.0408 |
0.56500 |
0.29650 |
| 0.9694 |
0.63930 |
0.19970 |
| 0.8957 |
0.71660 |
0.10510 |
| 1.3684 |
0.17910 |
0.80050 |
| 1.3102 |
0.27000 |
0.70010 |
| 1.2510 |
0.35700 |
0.60260 |
| 1.1848 |
0.44970 |
0.49990 |
| 1.1170 |
0.53970 |
0.40020 |
| 1.0486 |
0.62270 |
0.30530 |
| 0.9672 |
0.71800 |
0.19930 |
| 0.8857 |
0.81030 |
0.09960 |
| 0.7852 |
1.00000 |
0.00000 |
| 1.4791 |
0.00000 |
1.00000 |
| 0.8736 |
0.00000 |
0.00000 |
Reference
| Source |
| Kijevcanin M.L.; Serbanovic S.P.; Radovic I.R.; Djordjevic B.D.; Tasic A.Z.: Experimental data, correlation and prediction by cubic EOS. Fluid Phase Equilib. 251 (2007) 78-92 |
List of All References
| Source |
| Kijevcanin M.L.; Serbanovic S.P.; Radovic I.R.; Djordjevic B.D.; Tasic A.Z.: Experimental data, correlation and prediction by cubic EOS. Fluid Phase Equilib. 251 (2007) 78-92 |
Density Data Overview
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