Operational conditions:
Fixed | Measured | |
---|---|---|
Mass fraction of Ethanol (1) - Liquid | Solvent: Amount ratio of component to other component of binary solvent of ( S)-camphor (3) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.9500 | 0.1980 | -0.0173 |
0.9500 | 0.3960 | -0.0284 |
0.9500 | 0.5940 | -0.0351 |
0.9500 | 0.7920 | -0.0395 |
0.9500 | 0.9900 | -0.0421 |
0.9500 | 1.021 | -0.0434 |
0.9500 | 1.276 | -0.0411 |
0.9500 | 1.702 | -0.0369 |
0.9500 | 2.552 | -0.0304 |
0.9500 | 5.105 | -0.0187 |
0.9700 | 0.1950 | -0.0267 |
0.9700 | 0.3890 | -0.0448 |
0.9700 | 0.5840 | -0.0565 |
0.9700 | 0.7780 | -0.0643 |
0.9700 | 0.9730 | -0.0697 |
0.9700 | 1.026 | -0.0693 |
0.9700 | 1.283 | -0.0651 |
0.9700 | 1.71 | -0.0579 |
0.9700 | 2.565 | -0.0465 |
0.9700 | 5.131 | -0.0296 |
0.9900 | 0.1930 | -0.0712 |
0.9900 | 0.3860 | -0.1147 |
0.9900 | 0.5790 | -0.1372 |
0.9900 | 0.7720 | -0.1501 |
0.9900 | 0.9650 | -0.1572 |
0.9900 | 1.004 | -0.1571 |
0.9900 | 1.254 | -0.1508 |
0.9900 | 1.672 | -0.1371 |
0.9900 | 2.509 | -0.1153 |
0.9900 | 5.017 | -0.0707 |
0.9950 | 0.2010 | -0.1470 |
0.9950 | 0.4030 | -0.2502 |
0.9950 | 0.6040 | -0.3147 |
0.9950 | 0.8060 | -0.3517 |
0.9950 | 1.007 | -0.3733 |
0.9950 | 1.061 | -0.3735 |
0.9950 | 1.327 | -0.3516 |
0.9950 | 1.769 | -0.3089 |
0.9950 | 2.652 | -0.2466 |
0.9950 | 5.305 | -0.1508 |
Operational conditions:
Fixed | Measured | |
---|---|---|
Mass fraction of Ethanol (1) - Liquid | Solvent: Amount ratio of component to other component of binary solvent of ( S)-camphor (3) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.9500 | 0.1980 | -0.0173 |
0.9500 | 0.3960 | -0.0284 |
0.9500 | 0.5940 | -0.0351 |
0.9500 | 0.7920 | -0.0395 |
0.9500 | 0.9900 | -0.0421 |
0.9500 | 1.021 | -0.0434 |
0.9500 | 1.276 | -0.0411 |
0.9500 | 1.702 | -0.0369 |
0.9500 | 2.552 | -0.0304 |
0.9500 | 5.105 | -0.0187 |
0.9700 | 0.1950 | -0.0267 |
0.9700 | 0.3890 | -0.0448 |
0.9700 | 0.5840 | -0.0565 |
0.9700 | 0.7780 | -0.0643 |
0.9700 | 0.9730 | -0.0697 |
0.9700 | 1.026 | -0.0693 |
0.9700 | 1.283 | -0.0651 |
0.9700 | 1.71 | -0.0579 |
0.9700 | 2.565 | -0.0465 |
0.9700 | 5.131 | -0.0296 |
0.9900 | 0.1930 | -0.0712 |
0.9900 | 0.3860 | -0.1147 |
0.9900 | 0.5790 | -0.1372 |
0.9900 | 0.7720 | -0.1501 |
0.9900 | 0.9650 | -0.1572 |
0.9900 | 1.004 | -0.1571 |
0.9900 | 1.254 | -0.1508 |
0.9900 | 1.672 | -0.1371 |
0.9900 | 2.509 | -0.1153 |
0.9900 | 5.017 | -0.0707 |
0.9950 | 0.2010 | -0.1470 |
0.9950 | 0.4030 | -0.2502 |
0.9950 | 0.6040 | -0.3147 |
0.9950 | 0.8060 | -0.3517 |
0.9950 | 1.007 | -0.3733 |
0.9950 | 1.061 | -0.3735 |
0.9950 | 1.327 | -0.3516 |
0.9950 | 1.769 | -0.3089 |
0.9950 | 2.652 | -0.2466 |
0.9950 | 5.305 | -0.1508 |